C内核流量计算方法优化，前端文件名称读取优化
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"id": "test_mql_full_branches-historical-v1",
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"description": "Historical slow-region and 2.05 s production regression target with three locked-environment repeats and approved state goldens.",
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"source": {
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"path": "tests/data/test_mql-full-branches-01-04.xml",
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"path": "tests/baselines/simulation/test_mql_full_branches/sources/test_mql-full-branches-01-04.xml",
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"sha256": "2fb95e65f5de0c85a6a17802aef74ea004087323fd00fd8d01acf0184ff71d48",
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"bytes": 58860,
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"xmlIsAuthoritative": true,
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/* Submodel PNCH012 skeleton created by AME Submodel editing utility
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mar. oct. 9 14:41:15 2018 */
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#include <math.h>
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#include <stdio.h>
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#include <stdlib.h>
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#include "ameutils.h"
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/* *******************************************************************************
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TITLE : PNCH012
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--------------------------------------------------------------------------------
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DESCRIPTION :
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This submodel represents a pneumatic chamber with a variable volume
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and pressure dynamics.
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Each port receives a mass flow rate and an enthalpy flow rate as
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input and gives the pressure and the temperature of the chamber as
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output. Each port receives also the volume and volume variation as
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input. The total volume is calculated by summing the four volume
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inputs and a dead volume which is a parameter of PNCH012.
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The model takes into account heat exchange. It express the variation
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of internal energy U using the first law of thermodynamics applied to
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an open system. Therefore, this model should be preferred to the simple
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polytropic chamber PNCH011.
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The total volume of the chamber is limited to a lower value equal to
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the dead volume divided by 100.
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--------------------------------------------------------------------------------
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USAGE :
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Use this submodel to simulate a pneumatic chamber in a jack, spool
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valve or any pneumatic chamber in which the volume can vary.
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This submodel can be directly connected to any pneumatic PCD
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component or standard pneumatic component.
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The submodels PNGD001, PNGD002, PNGD003, PNGD004 or PNRGD00 should be
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included in your circuit to define the characteristics of the gas.
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--------------------------------------------------------------------------------
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PARAMETER SETTINGS:
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The dead volume is the volume of the pneumatic fluid when all the input
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volumes are zero. It is essential that this volume must be greater
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than zero.
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--------------------------------------------------------------------------------
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DATE OF CREATION / AUTHOR :
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2002 FS from PNCH12
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--------------------------------------------------------------------------------
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INDEX OF REVISIONS :
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2008 OBA - Real gas improvements : the mass and volume were considered as
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internal state variable, they are now coded as internal basic
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variable. The mass initialisation was removed as it was linked
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to the perfect gas formulation.
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--------------------------------------------------------------------------------
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LIST OF FUNCTIONS USED :
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pn2getatp : get atmospheric pressure
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firstc_ : checks if this is the first call to this submodel
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pn2vol_ : pneumatic chamber with heat exchange
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stepdn_ : reduce simulation step
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--------------------------------------------------------------------------------
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SOURCE :
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This material contains trade secrets or otherwise confidential
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information owned by Siemens Industry Software Inc. or its
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affiliates (collectively, "Siemens"), or its licensors. Access to
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and use of this information is strictly limited as set forth in the
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Customer's applicable agreements with Siemens.
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Unpublished work. Copyright 2023 Siemens
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******************************************************************************* */
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#define _SUBMODELNAME_ "PNCH012"
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/* >>>>>>>>>>>>Insert Private Code Here. */
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/* <<<<<<<<<<<<End of Private Code. */
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/* There are 4 real parameters:
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cvol0 dead volume [L -> m**3]
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kth thermal exchange coefficient [J/m**2/K/s -> W/m**2/K]
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sth thermal exchange area [m**2]
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extemp external temperature [K]
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*/
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/* There is 1 integer parameter:
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gi gas type index
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*/
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void pnch012in_(int *n, double rp[4], int ip[1], double c[2]
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, int ic[2], double *temp, double *press, double *dvol1
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, double *vol1, double *dvol2, double *vol2, double *dvol3
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, double *vol3, double *dvol4, double *vol4)
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{
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int loop, error;
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/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
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/* <<<<<<<<<<<<End of Extra Initialization declarations. */
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int gi;
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double cvol0, kth, sth, extemp;
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gi = ip[0];
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cvol0 = rp[0];
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kth = rp[1];
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sth = rp[2];
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extemp = rp[3];
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loop = 0;
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error = 0;
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/* Assign default values to input(s) with default. */
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*dvol1 = 0.00000000000000e+000;
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*vol1 = 0.00000000000000e+000;
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*dvol2 = 0.00000000000000e+000;
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*vol2 = 0.00000000000000e+000;
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*dvol3 = 0.00000000000000e+000;
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*vol3 = 0.00000000000000e+000;
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*dvol4 = 0.00000000000000e+000;
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*vol4 = 0.00000000000000e+000;
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/*
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If necessary, check values of the following:
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rp[0..3]
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*temp
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*press
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*/
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/* >>>>>>>>>>>>Initialization Function Check Statements. */
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pn2_valid_gas_(&gi, &error);
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if (cvol0 <= 0.0)
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{
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error = 2;
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amefprintf(stderr, "\nVolume chamber must be strictly positive.\n");
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}
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if (kth < 0.0)
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{
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error = 2;
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amefprintf(stderr, "\nthermal exchange coefficient must be positive.\n");
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}
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if (sth < 0.0)
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{
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error = 2;
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amefprintf(stderr, "\nthermal exchange area must be positive.\n");
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}
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if (extemp <= 0.0)
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{
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error = 2;
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amefprintf(stderr, "\nExternal temperature must be strictly positive.\n");
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}
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if (*temp <= 0.0)
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{
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error = 2;
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amefprintf(stderr, "\nInitial temperature must be strictly positive.\n");
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}
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/* <<<<<<<<<<<<End of Initialization Check Statements. */
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/* Integer parameter checking: */
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if (gi < 1 || gi > 99)
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{
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amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
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error = 2;
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}
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if(error == 1)
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{
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amefprintf(stderr, "\nWarning in %s instance %d.\n", _SUBMODELNAME_, *n);
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}
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else if(error == 2)
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{
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amefprintf(stderr, "\nFatal error in %s instance %d.\n", _SUBMODELNAME_, *n);
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amefprintf(stderr, "Terminating the program.\n");
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AmeExit(1);
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}
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/* Common -> SI units conversions. */
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rp[0] *= 1.00000000000000e-003;
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cvol0 = rp[0];
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/* >>>>>>>>>>>>Initialization Function Executable Statements. */
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c[0] = cvol0 / 100;
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/* Set initial value for the test of limited volume :
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ic[1] = 1 when the chamber volume is limited to cvol0 / 100 else ic[1] = 0*/
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ic[1] = 0;
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/* set atmospheric pressure */
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c[1] = pn2getatp_();
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/* <<<<<<<<<<<<End of Initialization Executable Statements. */
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}
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/* There are 4 ports.
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Port 1 has 6 variables:
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1 temp temperature [K] explicit state (derivative `dtemp')
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2 press pressure [Pa] explicit state (derivative `dpress')
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3 dh1 enthalpy flow rate at port 1 [J/s -> W] basic variable input
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4 dm1 mass flow rate at port 1 [g/s -> kg/s] basic variable input
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5 dvol1 derivative of volume at port 1 [L/min -> m**3/s] basic variable input with default 0.000000e+000
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6 vol1 volume at port 1 [cm**3 -> m**3] basic variable input with default 0.000000e+000
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Port 2 has 6 variables:
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1 temp2 duplicate of temp
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2 press2 duplicate of press
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3 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable input
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4 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable input
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5 dvol2 derivative of volume at port 2 [L/min -> m**3/s] basic variable input with default 0.000000e+000
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6 vol2 volume at port 2 [cm**3 -> m**3] basic variable input with default 0.000000e+000
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Port 3 has 6 variables:
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1 temp3 duplicate of temp
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2 press3 duplicate of press
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3 dh3 enthalpy flow rate at port 3 [J/s -> W] basic variable input
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4 dm3 mass flow rate at port 3 [g/s -> kg/s] basic variable input
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5 dvol3 derivative of volume at port 3 [L/min -> m**3/s] basic variable input with default 0.000000e+000
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6 vol3 volume at port 3 [cm**3 -> m**3] basic variable input with default 0.000000e+000
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Port 4 has 6 variables:
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1 temp4 duplicate of temp
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2 press4 duplicate of press
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3 dh4 enthalpy flow rate at port 4 [J/s -> W] basic variable input
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4 dm4 mass flow rate at port 4 [g/s -> kg/s] basic variable input
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5 dvol4 derivative of volume at port 4 [L/min -> m**3/s] basic variable input with default 0.000000e+000
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6 vol4 volume at port 4 [cm**3 -> m**3] basic variable input with default 0.000000e+000
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*/
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/* There are 2 internal variables.
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1 vol volume of pneumatic chamber [cm**3 -> m**3] basic variable
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2 mgas1 mass of gas in chamber [g -> kg] basic variable
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*/
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void pnch012_(int *n, double *temp, double *dtemp, double *press
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, double *dpress, double *dh1, double *dm1, double *dvol1
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, double *vol1, double *dh2, double *dm2, double *dvol2
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, double *vol2, double *dh3, double *dm3, double *dvol3
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, double *vol3, double *dh4, double *dm4, double *dvol4
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, double *vol4, double *vol, double *mgas1, double rp[4]
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, int ip[1], double c[2], int ic[2])
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{
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int loop;
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/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
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double dvol;
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double sdm, sdh;
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double dq;
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double pressa;
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/* <<<<<<<<<<<<End of Extra Calculation declarations. */
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int gi;
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double cvol0, kth, sth, extemp;
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gi = ip[0];
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cvol0 = rp[0];
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kth = rp[1];
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sth = rp[2];
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extemp = rp[3];
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loop = 0;
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/* Common -> SI units conversions. */
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*dm1 *= 1.00000000000000e-003;
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*dvol1 *= 1.66666666666667e-005;
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*vol1 *= 1.00000000000000e-006;
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*dm2 *= 1.00000000000000e-003;
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*dvol2 *= 1.66666666666667e-005;
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*vol2 *= 1.00000000000000e-006;
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*dm3 *= 1.00000000000000e-003;
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*dvol3 *= 1.66666666666667e-005;
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*vol3 *= 1.00000000000000e-006;
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*dm4 *= 1.00000000000000e-003;
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*dvol4 *= 1.66666666666667e-005;
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*vol4 *= 1.00000000000000e-006;
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/*
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Set all submodel outputs below:
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*dtemp = ??;
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*dpress = ??;
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*vol = ??;
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*mgas1 = ??;
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*/
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||||
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/* >>>>>>>>>>>>Calculation Function Executable Statements. */
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/* set absolute pressure */
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pressa = *press + c[1];
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/*** sum of the volume variation and volume ***/
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dvol = *dvol1 + *dvol2 + *dvol3 + *dvol4;
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/*** setup the initial mass of the gaz inside of the chamber ***/
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*vol = *vol1 + *vol2 + *vol3 + *vol4 + cvol0;
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/*** sum of the flows ***/
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sdm = *dm1 + *dm2 + *dm3 + *dm4; /* mass flow */
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sdh = *dh1 + *dh2 + *dh3 + *dh4; /* heat flow */
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/*** V, M, T and P can not be lower than zero ***/
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*vol = llimit_(vol, &c[0], &ic[0]);
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if (ic[0] == -1)
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{
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dvol = 0.;
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if (ic[1] == 0)
|
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{
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amefprintf(stderr, "\nWarning in %s instance %d chamber volume is limited by cvol0 / 100 = %g cm**3.\n", _SUBMODELNAME_, *n, c[0]*1E+6);
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ic[1] = 1;
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}
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||||
}
|
||||
|
||||
if (*vol < c[0]/10)
|
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{
|
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*vol = c[0]/10;
|
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}
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||||
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if ( (*mgas1 <= 1.0e-10) && (!firstc_()) )
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{
|
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/* panic step reduction */
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stepdn_();
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*mgas1 = 1.0e-10;
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}
|
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|
||||
if (pressa <= 1.0e-10)
|
||||
{
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||||
/* panic step reduction */
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||||
stepdn_();
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*press = 1.0e-10 - c[1];
|
||||
}
|
||||
|
||||
if (*temp <= 1.0e-10)
|
||||
{
|
||||
/* panic step reduction */
|
||||
stepdn_();
|
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*temp = 1.0e-10;
|
||||
}
|
||||
|
||||
/*** temperature & pressure variation ***/
|
||||
dq = kth*sth*(extemp-*temp);
|
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pn2vol_(dtemp, dpress, mgas1, temp, &pressa,
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&sdm, &sdh, vol, &dvol, &dq, &gi);
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
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*dm1 /= 1.00000000000000e-003;
|
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*dvol1 /= 1.66666666666667e-005;
|
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*vol1 /= 1.00000000000000e-006;
|
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*dm2 /= 1.00000000000000e-003;
|
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*dvol2 /= 1.66666666666667e-005;
|
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*vol2 /= 1.00000000000000e-006;
|
||||
*dm3 /= 1.00000000000000e-003;
|
||||
*dvol3 /= 1.66666666666667e-005;
|
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*vol3 /= 1.00000000000000e-006;
|
||||
*dm4 /= 1.00000000000000e-003;
|
||||
*dvol4 /= 1.66666666666667e-005;
|
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*vol4 /= 1.00000000000000e-006;
|
||||
*vol /= 1.00000000000000e-006;
|
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*mgas1 /= 1.00000000000000e-003;
|
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}
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|
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@@ -0,0 +1,356 @@
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<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>33</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>pn_c1</DEFAULT_ICON>
|
||||
<SUB_LABEL>variable volume pneumatic chamber with heat exchange (preferred)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>2</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>2</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>27</SUB_ID>
|
||||
<TITLE>dead volume</TITLE>
|
||||
<VARNAME>cvol0</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+005</MAX_VALUE>
|
||||
<UNITS>L</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>28</SUB_ID>
|
||||
<TITLE>thermal exchange coefficient</TITLE>
|
||||
<VARNAME>kth</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>0.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>J/m**2/K/s</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>29</SUB_ID>
|
||||
<TITLE>thermal exchange area</TITLE>
|
||||
<VARNAME>sth</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e-01</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e-01</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+002</MAX_VALUE>
|
||||
<UNITS>m**2</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>30</SUB_ID>
|
||||
<TITLE>external temperature</TITLE>
|
||||
<VARNAME>extemp</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>2.93150000000000e+02</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+02</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
|
||||
<UNITS>K</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>31</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>32</SUB_ID>
|
||||
<TITLE>volume of pneumatic chamber</TITLE>
|
||||
<VARNAME>vol</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>cm**3</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>33</SUB_ID>
|
||||
<TITLE>mass of gas in chamber</TITLE>
|
||||
<VARNAME>mgas1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>g</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>temperature</TITLE>
|
||||
<VARNAME>temp</VARNAME>
|
||||
<VARNAME2>dtemp</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>K</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
|
||||
<DEF_VALUE>2.93150000000000e+002</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+002</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>pressure</TITLE>
|
||||
<VARNAME>press</VARNAME>
|
||||
<VARNAME2>dpress</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
<MIN_VALUE>-1.01300000000000e+005</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+012</MAX_VALUE>
|
||||
<DEF_VALUE>0.00000000000000e+000</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+000</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 1</TITLE>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>mass flow rate at port 1</TITLE>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>derivative of volume at port 1</TITLE>
|
||||
<VARNAME>dvol1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>L/min</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<TITLE>volume at port 1</TITLE>
|
||||
<VARNAME>vol1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>cm**3</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<VARNAME>temp2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<VARNAME>press2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>11</SUB_ID>
|
||||
<TITLE>derivative of volume at port 2</TITLE>
|
||||
<VARNAME>dvol2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>L/min</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>volume at port 2</TITLE>
|
||||
<VARNAME>vol2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>cm**3</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<VARNAME>temp3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<VARNAME>press3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 3</TITLE>
|
||||
<VARNAME>dh3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>16</SUB_ID>
|
||||
<TITLE>mass flow rate at port 3</TITLE>
|
||||
<VARNAME>dm3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<TITLE>derivative of volume at port 3</TITLE>
|
||||
<VARNAME>dvol3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>L/min</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>volume at port 3</TITLE>
|
||||
<VARNAME>vol3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>cm**3</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>19</SUB_ID>
|
||||
<VARNAME>temp4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>20</SUB_ID>
|
||||
<VARNAME>press4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>0</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>21</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 4</TITLE>
|
||||
<VARNAME>dh4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>22</SUB_ID>
|
||||
<TITLE>mass flow rate at port 4</TITLE>
|
||||
<VARNAME>dm4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>23</SUB_ID>
|
||||
<TITLE>derivative of volume at port 4</TITLE>
|
||||
<VARNAME>dvol4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>L/min</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>24</SUB_ID>
|
||||
<TITLE>volume at port 4</TITLE>
|
||||
<VARNAME>vol4</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>3</IO>
|
||||
<UNITS>cm**3</UNITS>
|
||||
<DEF_VALUE>0</DEF_VALUE>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,348 @@
|
||||
/* Submodel PNL0001 skeleton created by AME Submodel editing utility
|
||||
mer. juin 20 14:20:39 2018 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNL0001 (C-R)
|
||||
------------------------------------------------------------------------------
|
||||
DESCRIPTION :
|
||||
PNL0001 is a submodel of a pneumatic pipe with only compressibility
|
||||
and friction effects taking into account heat exchange.
|
||||
|
||||
The compressibility of the gas is taken into account by using a
|
||||
simple polytropic model or a more complex one taking into account
|
||||
heat exchange.
|
||||
|
||||
The polytropic model is a simplified form of the general internal
|
||||
energy model based on the first law of thermodynamics. The polytropic
|
||||
approach is obtained by representing the thermal exchange phenomena
|
||||
by a polytropic constant k. In that case, the temperature and
|
||||
pressure are no more independent variables.
|
||||
|
||||
The reduction of the complexity of the model implies a lack of
|
||||
accuracy. For general studies, you'd better use the heat exchange
|
||||
approach.
|
||||
|
||||
Pipe friction is taken into account using a friction factor based on
|
||||
the Reynolds number and the relative roughness.
|
||||
|
||||
The temperature and pressure in the volume are state variables.
|
||||
------------------------------------------------------------------------------
|
||||
USAGE :
|
||||
Use this submodel to simulate a pneumatic pipe with compressibility
|
||||
and friction effects, when the Mach number is low, ie gas velocity
|
||||
< 0.3 * speed of sound .
|
||||
|
||||
The submodels PNGD001 or PNGD002 should be included in your circuit to
|
||||
define the characteristics of the gas.
|
||||
------------------------------------------------------------------------------
|
||||
PARAMETER SETTINGS :
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 FS from PNL01 SN.
|
||||
------------------------------------------------------------------------------
|
||||
REVISIONS :
|
||||
------------------------------------------------------------------------------
|
||||
LIST OF FUNCTIONS USED :
|
||||
pn2getatp_() : get atmospheric pressure
|
||||
pn2ri_() : get perfect gas constant
|
||||
pn2vol1_() : polytropic model for chambers
|
||||
pn2vol_() : heat exchange model for chambers
|
||||
pn2pipefr_() : frictional coeffitient in pneumatic pipes
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNL0001"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
#define TABFR 0 /* real store 0, 1 & 2 are used by pn2pipefr */
|
||||
#define PATM 3
|
||||
#define AREA 4
|
||||
#define VOL 5
|
||||
#define AREAEX 6
|
||||
|
||||
#define SPL_FR 0
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 6 real parameters:
|
||||
|
||||
diam diameter of pipe [mm -> m]
|
||||
le pipe length [m]
|
||||
rr relative roughness [null]
|
||||
k polytropic constant [null]
|
||||
kth thermal exchange coefficient [J/m**2/K/s -> W/m**2/K]
|
||||
extemp external temperature [K]
|
||||
*/
|
||||
|
||||
|
||||
/* There are 2 integer parameters:
|
||||
|
||||
gi gas type index
|
||||
mode model
|
||||
*/
|
||||
|
||||
void pnl0001in_(int *n, double rp[6], int ip[2], double c[7]
|
||||
, int ic[1], double *t2, double *p2)
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..5]
|
||||
*t2
|
||||
*p2
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (*p2 < -GPATMOS)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial pressure at port 2 should be > 0 [barA].\n");
|
||||
}
|
||||
|
||||
if (*t2 <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial temperature at port 2 should be > 0 [K].\n");
|
||||
}
|
||||
|
||||
if (diam <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nDiameter of pipe should be > 0 [mm].\n");
|
||||
}
|
||||
|
||||
if (le <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPipe length should be > 0 [m].\n");
|
||||
}
|
||||
|
||||
if (rr < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nRelative roughness should be >= 0.\n");
|
||||
}
|
||||
|
||||
if (mode == 1)
|
||||
{
|
||||
if (k <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPolytropic constant should be > 0.\n");
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
if (kth < 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nThermal exchange coefficient should be >= 0 [J/m**2/K/s].\n");
|
||||
}
|
||||
|
||||
if (extemp <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nExternal temperature should be > 0 [K].\n");
|
||||
}
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
if (mode < 1 || mode > 2)
|
||||
{
|
||||
amefprintf(stderr, "\nmodel must be in range [1..2].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[0] *= 1.00000000000000e-003;
|
||||
diam = rp[0];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
|
||||
/* get atmospheric pressure */
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
/* Compute the cross-sectional area of pipe. */
|
||||
c[AREA] = M_PI * (diam) * (diam) / 4.0;
|
||||
|
||||
/* Compute volume of pipe. */
|
||||
c[VOL] = c[AREA] * le;
|
||||
|
||||
/* Compute exchange area of pipe. */
|
||||
c[AREAEX] = M_PI * diam * le;
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 2 ports.
|
||||
|
||||
Port 1 has 4 variables:
|
||||
|
||||
1 dh1 enthalpy flow rate at port 1 [J/s -> W] basic variable output
|
||||
2 dm1 mass flow rate at port 1 [g/s -> kg/s] basic variable output
|
||||
3 t1 temperature at port 1 [K] basic variable input
|
||||
4 p1 pressure at port 1 [Pa] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 t2 temperature at port 2 [K] explicit state (derivative `dt2')
|
||||
2 p2 pressure at port 2 [Pa] explicit state (derivative `dp2')
|
||||
3 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable input
|
||||
4 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 5 internal variables.
|
||||
|
||||
1 mgas mass of gas in pipe [g -> kg] basic variable
|
||||
2 re Reynolds number [null] basic variable
|
||||
3 cm mass flow parameter (cm) [(kg*K/J)**(1/2)] basic variable
|
||||
4 v mean gas velocity [m/s] basic variable
|
||||
5 ff friction factor [null] basic variable
|
||||
*/
|
||||
|
||||
void pnl0001_(int *n, double *dh1, double *dm1, double *t1, double *p1
|
||||
, double *t2, double *dt2, double *p2, double *dp2, double *dh2
|
||||
, double *dm2, double *mgas, double *re, double *cm, double *v
|
||||
, double *ff, double rp[6], int ip[2], double c[7], int ic[1])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
static double zero = 0.0;
|
||||
double sdh;
|
||||
double dh2i, dm2i;
|
||||
double dq;
|
||||
double pa1, pa2, dmgas;
|
||||
double r;
|
||||
int dummyreg;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
*dm2 *= 1.00000000000000e-003;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dh1 = ??;
|
||||
*dm1 = ??;
|
||||
*dt2 = ??;
|
||||
*dp2 = ??;
|
||||
*mgas = ??;
|
||||
*re = ??;
|
||||
*cm = ??;
|
||||
*v = ??;
|
||||
*ff = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressures */
|
||||
pa1 = *p1 + c[PATM];
|
||||
pa2 = *p2 + c[PATM];
|
||||
|
||||
/* Compute flows through the pipe */
|
||||
pn2pipefr_(&pa1, t1, &pa2, t2, &diam, &rr, &le, &c[AREA], re, v,ff,
|
||||
dh1, dm1, &dh2i, &dm2i, cm, &c[TABFR], &gi, &ic[SPL_FR], &dummyreg);
|
||||
|
||||
/* Compute mass variation */
|
||||
dmgas = (*dm2) + dm2i;
|
||||
|
||||
/* sum of enthalpy flows */
|
||||
sdh = (*dh2) + dh2i;
|
||||
|
||||
/*** temperature & pressure variation ***/
|
||||
|
||||
if (mode == 1) /* Polytropic model. */
|
||||
{
|
||||
r = pn2ri_(&gi);
|
||||
/* Compute initial mass of gas inside the pipe */
|
||||
*mgas = (pa2) * c[VOL] / ((*t2) * r);
|
||||
|
||||
pn2vol1_(dt2, dp2, t2, &pa2,
|
||||
&dmgas, mgas, &zero, &c[VOL], &k, &gi);
|
||||
}
|
||||
else /* Heat exchange. */
|
||||
{
|
||||
dq = kth * c[AREAEX] * (extemp - *t2);
|
||||
|
||||
pn2vol_(dt2, dp2, mgas, t2, &pa2,
|
||||
&dmgas, &sdh, &c[VOL], &zero, &dq, &gi);
|
||||
}
|
||||
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm1 /= 1.00000000000000e-003;
|
||||
*dm2 /= 1.00000000000000e-003;
|
||||
*mgas /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,257 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>22</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>p2port</DEFAULT_ICON>
|
||||
<SUB_LABEL>Compressibility + friction submodel of pneumatic pipe (C-R)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>7</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>1</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>diameter of pipe</TITLE>
|
||||
<VARNAME>diam</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+01</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-003</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+007</MAX_VALUE>
|
||||
<UNITS>mm</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>pipe length</TITLE>
|
||||
<VARNAME>le</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-006</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<UNITS>m</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>16</SUB_ID>
|
||||
<TITLE>relative roughness</TITLE>
|
||||
<VARNAME>rr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e-05</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e-05</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e-001</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<TITLE>polytropic constant</TITLE>
|
||||
<VARNAME>k</VARNAME>
|
||||
<VISIBILITY>(mode == 1)</VISIBILITY>
|
||||
<DEF_VALUE>1.35000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.35000000000000e+00</VALUE>
|
||||
<MIN_VALUE>5.00000000000000e-001</MIN_VALUE>
|
||||
<MAX_VALUE>2.00000000000000e+000</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>thermal exchange coefficient</TITLE>
|
||||
<VARNAME>kth</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>0.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>J/m**2/K/s</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>19</SUB_ID>
|
||||
<TITLE>external temperature</TITLE>
|
||||
<VARNAME>extemp</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>2.93150000000000e+02</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+02</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
|
||||
<UNITS>K</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>20</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
<IPARAM>
|
||||
<SUB_ID>21</SUB_ID>
|
||||
<TITLE>model</TITLE>
|
||||
<VARNAME>mode</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>2</DEF_VALUE>
|
||||
<VALUE>2</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>2</MAX_VALUE>
|
||||
<ENUM_LIST>
|
||||
<ENUM>
|
||||
<ENUM_STRING>polytropic</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>with thermal exchange</ENUM_STRING>
|
||||
</ENUM>
|
||||
</ENUM_LIST>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>22</SUB_ID>
|
||||
<TITLE>mass of gas in pipe</TITLE>
|
||||
<VARNAME>mgas</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>g</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>Reynolds number</TITLE>
|
||||
<VARNAME>re</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>11</SUB_ID>
|
||||
<TITLE>mass flow parameter (cm)</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>mean gas velocity</TITLE>
|
||||
<VARNAME>v</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>friction factor</TITLE>
|
||||
<VARNAME>ff</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 1</TITLE>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>mass flow rate at port 1</TITLE>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>temperature at port 1</TITLE>
|
||||
<VARNAME>t1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>pressure at port 1</TITLE>
|
||||
<VARNAME>p1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>t2</VARNAME>
|
||||
<VARNAME2>dt2</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>K</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<DEF_VALUE>2.93150000000000e+002</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+002</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>p2</VARNAME>
|
||||
<VARNAME2>dp2</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
<MIN_VALUE>-1.01300000000000e+005</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+012</MAX_VALUE>
|
||||
<DEF_VALUE>0.00000000000000e+000</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+000</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,368 @@
|
||||
/* Submodel PNL0002 skeleton created by AME Submodel editing utility
|
||||
mer. juin 20 14:35:13 2018 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNL0002 (R-C-R)
|
||||
------------------------------------------------------------------------------
|
||||
DESCRIPTION :
|
||||
PNL0002 is a submodel of a pneumatic pipe with only compressibility
|
||||
and friction effects taking into account heat exchange.
|
||||
|
||||
The compressibility of the gas is taken into account by using a
|
||||
simple polytropic model or a more complex one taking into account
|
||||
heat exchange.
|
||||
|
||||
The polytropic model is a simplified form of the general internal
|
||||
energy model based on the first law of thermodynamics. The polytropic
|
||||
approach is obtained by representing the thermal exchange phenomena
|
||||
by a polytropic constant k. In that case, the temperature and
|
||||
pressure are no more independent variables.
|
||||
|
||||
The reduction of the complexity of the model implies a lack of
|
||||
accuracy. For general studies, you'd better use the heat exchange
|
||||
approach.
|
||||
|
||||
Pipe friction is taken into account using a friction factor based on
|
||||
the Reynolds number and the relative roughness.
|
||||
|
||||
The temperature and pressure in the middle volume are state variables.
|
||||
------------------------------------------------------------------------------
|
||||
USAGE :
|
||||
Use this submodel to simulate a pneumatic pipe with compressibility
|
||||
and friction effects, when the Mach number is low, ie gas velocity
|
||||
< 0.3 * speed of sound .
|
||||
|
||||
PNL0002 is basically similar to PNL0001 and PNL0003 differing only in the
|
||||
input and output requirements.
|
||||
|
||||
The submodels PNGD01 or PNGD02 should be included in your circuit to
|
||||
define the characteristics of the gas.
|
||||
------------------------------------------------------------------------------
|
||||
PARAMETER SETTINGS :
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 FS from PNL02 SN.
|
||||
------------------------------------------------------------------------------
|
||||
REVISIONS :
|
||||
------------------------------------------------------------------------------
|
||||
LIST OF FUNCTIONS USED :
|
||||
pn2getatp_() : get atmospheric pressure
|
||||
pn2ri_() : get perfect gas constant
|
||||
pn2vol1_() : polytropic model for chambers
|
||||
pn2vol_() : heat exchange model for chambers
|
||||
pn2pipefr_() : frictional coeffitient in pneumatic pipes
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNL0002"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
#define TABFR 0 /* real store 0, 1 & 2 are used by pn2pipefr */
|
||||
#define PATM 3
|
||||
#define AREA 4
|
||||
#define VOL 5
|
||||
#define HALFLE 6
|
||||
#define AREAEX 7
|
||||
|
||||
|
||||
#define SPL_FR 0
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 6 real parameters:
|
||||
|
||||
diam diameter of pipe [mm -> m]
|
||||
le pipe length [m]
|
||||
rr relative roughness [null]
|
||||
k polytropic constant [null]
|
||||
kth thermal exchange coefficient [J/m**2/K/s -> W/m**2/K]
|
||||
extemp external temperature [K]
|
||||
*/
|
||||
|
||||
|
||||
/* There are 2 integer parameters:
|
||||
|
||||
gi gas type index
|
||||
mode model
|
||||
*/
|
||||
|
||||
void pnl0002in_(int *n, double rp[6], int ip[2], double c[8]
|
||||
, int ic[1], double *tctr, double *pctr)
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..5]
|
||||
*tctr
|
||||
*pctr
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (*pctr < -GPATMOS)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial pressure at center of pipe should be > 0 [barA].\n");
|
||||
}
|
||||
|
||||
if (*tctr <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial temperature at center of pipe should be > 0 [K].\n");
|
||||
}
|
||||
|
||||
if (diam <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nDiameter of pipe should be > 0 [mm].\n");
|
||||
}
|
||||
|
||||
if (le <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPipe length should be > 0 [m].\n");
|
||||
}
|
||||
|
||||
if (rr < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nRelative roughness should be >= 0.\n");
|
||||
}
|
||||
|
||||
if (mode == 1)
|
||||
{
|
||||
if (k <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPolytropic constant should be > 0.\n");
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
if (kth < 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nThermal exchange coefficient should be >= 0 [J/m**2/K/s].\n");
|
||||
}
|
||||
|
||||
if (extemp <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nExternal temperature should be > 0 [K].\n");
|
||||
}
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
if (mode < 1 || mode > 2)
|
||||
{
|
||||
amefprintf(stderr, "\nmodel must be in range [1..2].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[0] *= 1.00000000000000e-003;
|
||||
diam = rp[0];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
|
||||
/* get atmospheric pressure */
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
/* Compute the cross-sectional area of pipe. */
|
||||
c[AREA] = M_PI * (diam) * (diam) / 4.0;
|
||||
|
||||
/* Compute volume of pipe. */
|
||||
c[VOL] = c[AREA] * le;
|
||||
|
||||
/* Divide the restriction in 2 identical restrictions */
|
||||
c[HALFLE] = 0.5 * le;
|
||||
|
||||
/* Compute exchange area of pipe. */
|
||||
c[AREAEX] = M_PI * diam * le;
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 2 ports.
|
||||
|
||||
Port 1 has 4 variables:
|
||||
|
||||
1 dh1 enthalpy flow rate at port 1 [J/s -> W] basic variable output
|
||||
2 dm1 mass flow rate at port 1 [g/s -> kg/s] basic variable output
|
||||
3 t1 temperature at port 1 [K] basic variable input
|
||||
4 p1 pressure at port 1 [Pa] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable output
|
||||
2 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable output
|
||||
3 t2 temperature at port 2 [K] basic variable input
|
||||
4 p2 pressure at port 2 [Pa] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 7 internal variables.
|
||||
|
||||
1 tctr temperature at center of pipe [K] explicit state (derivative `dtctr')
|
||||
2 pctr pressure at center of pipe [Pa] explicit state (derivative `dpctr')
|
||||
3 mgas mass of gas in pipe [g -> kg] basic variable
|
||||
4 re mean Reynolds number [null] basic variable
|
||||
5 cm mean mass flow parameter [(kg*K/J)**(1/2)] basic variable
|
||||
6 v mean gas velocity [m/s] basic variable
|
||||
7 ff mean friction factor [null] basic variable
|
||||
*/
|
||||
|
||||
void pnl0002_(int *n, double *dh1, double *dm1, double *t1, double *p1
|
||||
, double *dh2, double *dm2, double *t2, double *p2, double *tctr
|
||||
, double *dtctr, double *pctr, double *dpctr, double *mgas
|
||||
, double *re, double *cm, double *v, double *ff, double rp[6]
|
||||
, int ip[2], double c[8], int ic[1])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
static double zero = 0.0;
|
||||
double sdh;
|
||||
double dh1i, dm1i;
|
||||
double dh2i, dm2i;
|
||||
double ff1, ff2, re1, re2, cm1, cm2;
|
||||
double dq;
|
||||
double pa1, pa2, pactr;
|
||||
double v1, v2;
|
||||
double dmgas;
|
||||
double r;
|
||||
int dummyreg;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dh1 = ??;
|
||||
*dm1 = ??;
|
||||
*dh2 = ??;
|
||||
*dm2 = ??;
|
||||
*dtctr = ??;
|
||||
*dpctr = ??;
|
||||
*mgas = ??;
|
||||
*re = ??;
|
||||
*cm = ??;
|
||||
*v = ??;
|
||||
*ff = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressure */
|
||||
pa1 = *p1 + c[PATM];
|
||||
pa2 = *p2 + c[PATM];
|
||||
pactr = *pctr + c[PATM];
|
||||
|
||||
/* Compute flows through the pipe */
|
||||
pn2pipefr_(&pa1, t1, &pactr, tctr, &diam, &rr, &c[HALFLE], &c[AREA], &re1, &v1, &ff1,
|
||||
dh1, dm1, &dh1i, &dm1i, &cm1, &c[TABFR], &gi, &ic[SPL_FR], &dummyreg);
|
||||
|
||||
pn2pipefr_(&pactr, tctr, &pa2, t2, &diam, &rr, &c[HALFLE], &c[AREA], &re2, &v2, &ff2,
|
||||
&dh2i, &dm2i, dh2, dm2, &cm2, &c[TABFR], &gi, &ic[SPL_FR], &dummyreg);
|
||||
|
||||
/* Mean variables */
|
||||
*ff = 0.5 * (ff1 + ff2);
|
||||
*re = 0.5 * (re1 + re2);
|
||||
*cm = 0.5 * (cm1 + cm2);
|
||||
*v = 0.5 * (fabs(v1) + fabs(v2));
|
||||
|
||||
/* Compute mass variation */
|
||||
dmgas = dm1i + dm2i;
|
||||
|
||||
/* sum of enthalpy flows */
|
||||
sdh = dh1i + dh2i;
|
||||
|
||||
/*** temperature & pressure variation ***/
|
||||
if (mode == 1) /* Polytropic model. */
|
||||
{
|
||||
r = pn2ri_(&gi);
|
||||
*mgas = (pactr) * c[VOL] / ((*tctr) * r);
|
||||
|
||||
pn2vol1_(dtctr, dpctr, tctr, &pactr,
|
||||
&dmgas, mgas, &zero, &c[VOL], &k, &gi);
|
||||
}
|
||||
else /* Heat exchange. */
|
||||
{
|
||||
dq = kth * c[AREAEX] * (extemp-*tctr);
|
||||
|
||||
pn2vol_(dtctr, dpctr, mgas, tctr, &pactr,
|
||||
&dmgas, &sdh, &c[VOL], &zero, &dq, &gi);
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm1 /= 1.00000000000000e-003;
|
||||
*dm2 /= 1.00000000000000e-003;
|
||||
*mgas /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,275 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>24</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>p2port</DEFAULT_ICON>
|
||||
<SUB_LABEL>Compressibility + friction submodel of pneumatic pipe (R-C-R)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>8</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>1</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>16</SUB_ID>
|
||||
<TITLE>diameter of pipe</TITLE>
|
||||
<VARNAME>diam</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+01</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-003</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+007</MAX_VALUE>
|
||||
<UNITS>mm</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<TITLE>pipe length</TITLE>
|
||||
<VARNAME>le</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-006</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<UNITS>m</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>relative roughness</TITLE>
|
||||
<VARNAME>rr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e-05</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e-05</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e-001</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>19</SUB_ID>
|
||||
<TITLE>polytropic constant</TITLE>
|
||||
<VARNAME>k</VARNAME>
|
||||
<VISIBILITY>(mode == 1)</VISIBILITY>
|
||||
<DEF_VALUE>1.35000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.35000000000000e+00</VALUE>
|
||||
<MIN_VALUE>5.00000000000000e-001</MIN_VALUE>
|
||||
<MAX_VALUE>2.00000000000000e+000</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>20</SUB_ID>
|
||||
<TITLE>thermal exchange coefficient</TITLE>
|
||||
<VARNAME>kth</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>0.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>J/m**2/K/s</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>21</SUB_ID>
|
||||
<TITLE>external temperature</TITLE>
|
||||
<VARNAME>extemp</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>2.93150000000000e+02</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+02</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
|
||||
<UNITS>K</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>22</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
<IPARAM>
|
||||
<SUB_ID>23</SUB_ID>
|
||||
<TITLE>model</TITLE>
|
||||
<VARNAME>mode</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>2</DEF_VALUE>
|
||||
<VALUE>2</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>2</MAX_VALUE>
|
||||
<ENUM_LIST>
|
||||
<ENUM>
|
||||
<ENUM_STRING>polytropic</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>with thermal exchange</ENUM_STRING>
|
||||
</ENUM>
|
||||
</ENUM_LIST>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>temperature at center of pipe</TITLE>
|
||||
<VARNAME>tctr</VARNAME>
|
||||
<VARNAME2>dtctr</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>K</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<DEF_VALUE>2.931500e+02</DEF_VALUE>
|
||||
<VALUE>2.931500e+02</VALUE>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>pressure at center of pipe</TITLE>
|
||||
<VARNAME>pctr</VARNAME>
|
||||
<VARNAME2>dpctr</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>Pa</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<DEF_VALUE>1.013000e+00</DEF_VALUE>
|
||||
<VALUE>1.013000e+00</VALUE>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>24</SUB_ID>
|
||||
<TITLE>mass of gas in pipe</TITLE>
|
||||
<VARNAME>mgas</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>g</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>mean Reynolds number</TITLE>
|
||||
<VARNAME>re</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>mean mass flow parameter</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>mean gas velocity</TITLE>
|
||||
<VARNAME>v</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>mean friction factor</TITLE>
|
||||
<VARNAME>ff</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 1</TITLE>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>mass flow rate at port 1</TITLE>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>temperature at port 1</TITLE>
|
||||
<VARNAME>t1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>pressure at port 1</TITLE>
|
||||
<VARNAME>p1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>t2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>p2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,399 @@
|
||||
/* Submodel PNL0003 skeleton created by AME Submodel editing utility
|
||||
mer. juin 20 14:17:28 2018 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNL0003 (C-R-C)
|
||||
------------------------------------------------------------------------------
|
||||
DESCRIPTION :
|
||||
PNL0003 is a submodel of a pneumatic pipe with only compressibility
|
||||
and friction effects taking into account heat exchange.
|
||||
|
||||
The compressibility of the gas is taken into account by using a
|
||||
simple polytropic model or a more complex one taking into account
|
||||
heat exchange.
|
||||
|
||||
The polytropic model is a simplified form of the general internal
|
||||
energy model based on the first law of thermodynamics. The polytropic
|
||||
approach is obtained by representing the thermal exchange phenomena
|
||||
by a polytropic constant k. In that case, the temperature and
|
||||
pressure are no more independent variables.
|
||||
|
||||
The reduction of the complexity of the model implies a lack of
|
||||
accuracy. For general studies, you'd better use the heat exchange
|
||||
approach.
|
||||
|
||||
Pipe friction is taken into account using a friction factor based on
|
||||
the Reynolds number and the relative roughness.
|
||||
|
||||
The temperature and pressure in each two volumes are state variables.
|
||||
------------------------------------------------------------------------------
|
||||
USAGE :
|
||||
Use this submodel to simulate a pneumatic pipe with compressibility
|
||||
and friction effects, when the Mach number is low, ie gas velocity
|
||||
< 0.3 * speed of sound .
|
||||
|
||||
PNL0003 is basically similar to PNL0001 and PNL0002 differing only in the
|
||||
input and output requirements.
|
||||
|
||||
The submodels PNGD01 or PNGD02 should be included in your circuit to
|
||||
define the characteristics of the gas.
|
||||
------------------------------------------------------------------------------
|
||||
PARAMETER SETTINGS :
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 FS from PNL03 SN.
|
||||
------------------------------------------------------------------------------
|
||||
REVISIONS :
|
||||
------------------------------------------------------------------------------
|
||||
LIST OF FUNCTIONS USED :
|
||||
pn2getatp_() : get atmospheric pressure
|
||||
pn2ri_() : get perfect gas constant
|
||||
pn2vol1_() : polytropic model for chambers
|
||||
pn2vol_() : heat exchange model for chambers
|
||||
pn2pipefr_() : frictional coefficient in pneumatic pipes
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNL0003"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
#define TABFR 0 /* real store 0, 1 & 2 are used by pn2pipefr */
|
||||
#define PATM 3
|
||||
#define AREA 4
|
||||
#define HALFVOL 5
|
||||
#define HALFAREAEX 6
|
||||
|
||||
|
||||
#define SPL_FR 0
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 6 real parameters:
|
||||
|
||||
diam diameter of pipe [mm -> m]
|
||||
le pipe length [m]
|
||||
rr relative roughness [null]
|
||||
k polytropic constant [null]
|
||||
kth thermal exchange coefficient [J/m**2/K/s -> W/m**2/K]
|
||||
extemp external temperature [K]
|
||||
*/
|
||||
|
||||
|
||||
/* There are 2 integer parameters:
|
||||
|
||||
gi gas type index
|
||||
mode model
|
||||
*/
|
||||
|
||||
void pnl0003in_(int *n, double rp[6], int ip[2], double c[7]
|
||||
, int ic[1], double *t1, double *p1, double *t2, double *p2)
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
double vol, areaex;
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..5]
|
||||
*t1
|
||||
*p1
|
||||
*t2
|
||||
*p2
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (*p1 < -GPATMOS)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial pressure at port 1 should be > 0 [barA].\n");
|
||||
}
|
||||
|
||||
if (*t1 <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial temperature at port 1 should be > 0 [K].\n");
|
||||
}
|
||||
|
||||
if (*p2 < -GPATMOS)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial pressure at port 2 should be > 0 [barA].\n");
|
||||
}
|
||||
|
||||
if (*t2 <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nInitial temperature at port 2 should be > 0 [K].\n");
|
||||
}
|
||||
|
||||
if (diam <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nDiameter of pipe should be > 0 [mm].\n");
|
||||
}
|
||||
|
||||
if (le <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPipe length should be > 0 [m].\n");
|
||||
}
|
||||
|
||||
if (rr < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nRelative roughness should be >= 0.\n");
|
||||
}
|
||||
|
||||
if (mode == 1)
|
||||
{
|
||||
if (k <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPolytropic constant should be > 0.\n");
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
if (kth < 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nThermal exchange coefficient should be >= 0 [J/m**2/K/s].\n");
|
||||
}
|
||||
|
||||
if (extemp <= 0.)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nExternal temperature should be > 0 [K].\n");
|
||||
}
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
if (mode < 1 || mode > 2)
|
||||
{
|
||||
amefprintf(stderr, "\nmodel must be in range [1..2].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[0] *= 1.00000000000000e-003;
|
||||
diam = rp[0];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
/* set atmospheric pressure */
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
/* Compute the cross-sectional area of pipe. */
|
||||
c[AREA] = M_PI * (diam) * (diam) / 4.0;
|
||||
|
||||
/* Compute volume of pipe. */
|
||||
vol = c[AREA] * le;
|
||||
|
||||
/* Divide the volume in 2 identical volumes */
|
||||
c[HALFVOL] = 0.5 * vol;
|
||||
|
||||
/* Compute exchange area of pipe. */
|
||||
areaex = M_PI * diam * le;
|
||||
|
||||
/* Divide the exchange area of pipe in 2 identical areas */
|
||||
c[HALFAREAEX] = 0.5 * areaex;
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 2 ports.
|
||||
|
||||
Port 1 has 4 variables:
|
||||
|
||||
1 t1 temperature at port 1 [K] explicit state (derivative `dt1')
|
||||
2 p1 pressure at port 1 [Pa] explicit state (derivative `dp1')
|
||||
3 dh1 enthalpy flow rate at port 1 [J/s -> W] basic variable input
|
||||
4 dm1 mass flow rate at port 1 [g/s -> kg/s] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 t2 temperature at port 2 [K] explicit state (derivative `dt2')
|
||||
2 p2 pressure at port 2 [Pa] explicit state (derivative `dp2')
|
||||
3 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable input
|
||||
4 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 7 internal variables.
|
||||
|
||||
1 dhctr enthalpy flow at center of pipe [J/s -> W] basic variable
|
||||
2 dmctr mass flow at center of pipe [g/s -> kg/s] basic variable
|
||||
3 mgas mass of gas in pipe [g -> kg] basic variable
|
||||
4 re Reynolds number [null] basic variable
|
||||
5 cm mass flow parameter (cm) [(kg*K/J)**(1/2)] basic variable
|
||||
6 v mean gas velocity [m/s] basic variable
|
||||
7 ff friction factor [null] basic variable
|
||||
*/
|
||||
|
||||
void pnl0003_(int *n, double *t1, double *dt1, double *p1, double *dp1
|
||||
, double *dh1, double *dm1, double *t2, double *dt2, double *p2
|
||||
, double *dp2, double *dh2, double *dm2, double *dhctr
|
||||
, double *dmctr, double *mgas, double *re, double *cm, double *v
|
||||
, double *ff, double rp[6], int ip[2], double c[7], int ic[1])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
static double zero = 0.0;
|
||||
double dh1i, dm1i;
|
||||
double dh2i, dm2i;
|
||||
double sdh1, sdm1;
|
||||
double sdh2, sdm2;
|
||||
double m1, m2;
|
||||
double dq1, dq2;
|
||||
double pa1, pa2;
|
||||
double dmgas;
|
||||
double r;
|
||||
int dummyreg;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi, mode;
|
||||
double diam, le, rr, k, kth, extemp;
|
||||
|
||||
gi = ip[0];
|
||||
mode = ip[1];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
k = rp[3];
|
||||
kth = rp[4];
|
||||
extemp = rp[5];
|
||||
loop = 0;
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
*dm1 *= 1.00000000000000e-003;
|
||||
*dm2 *= 1.00000000000000e-003;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dt1 = ??;
|
||||
*dp1 = ??;
|
||||
*dt2 = ??;
|
||||
*dp2 = ??;
|
||||
*dhctr = ??;
|
||||
*dmctr = ??;
|
||||
*mgas = ??;
|
||||
*re = ??;
|
||||
*cm = ??;
|
||||
*v = ??;
|
||||
*ff = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressures */
|
||||
pa1 = *p1 + c[PATM];
|
||||
pa2 = *p2 + c[PATM];
|
||||
|
||||
/* Compute flow through the pipe */
|
||||
pn2pipefr_(&pa1, t1, &pa2, t2, &diam, &rr, &le, &c[AREA], re, v, ff,
|
||||
&dh1i, &dm1i, &dh2i, &dm2i, cm, &c[TABFR], &gi, &ic[SPL_FR], &dummyreg);
|
||||
|
||||
/* Enthalpy flow and mass flow at center of pipe */
|
||||
*dhctr = dh1i; /* = -dh2i */
|
||||
*dmctr = dm1i; /* = -dm2i */
|
||||
|
||||
/* Compute the sum of the flows inside each volume */
|
||||
sdm1 = *dm1 + dm1i;
|
||||
sdh1 = *dh1 + dh1i;
|
||||
sdm2 = *dm2 + dm2i;
|
||||
sdh2 = *dh2 + dh2i;
|
||||
|
||||
dmgas = sdm1 + sdm2;
|
||||
|
||||
/*** temperature & pressure variation ***/
|
||||
if (mode == 1) /* Polytropic model. */
|
||||
{
|
||||
r = pn2ri_(&gi);
|
||||
|
||||
/* Current mass in each volume */
|
||||
m1 = pa1 * c[HALFVOL] / (*t1 * r);
|
||||
m2 = pa2 * c[HALFVOL] / (*t2 * r);
|
||||
|
||||
pn2vol1_(dt1, dp1, t1, &pa1,
|
||||
&sdm1, &m1, &zero, &c[HALFVOL], &k,&gi);
|
||||
|
||||
pn2vol1_(dt2, dp2, t2, &pa2,
|
||||
&sdm2, &m2, &zero, &c[HALFVOL], &k,&gi);
|
||||
}
|
||||
else /* Heat exchange. */
|
||||
{
|
||||
dq1 = kth * c[HALFAREAEX] * (extemp - *t1);
|
||||
|
||||
pn2vol_(dt1, dp1, &m1, t1, &pa1,
|
||||
&sdm1, &sdh1, &c[HALFVOL], &zero, &dq1, &gi);
|
||||
|
||||
dq2 = kth * c[HALFAREAEX] * (extemp - *t2);
|
||||
|
||||
pn2vol_(dt2, dp2, &m2, t2, &pa2,
|
||||
&sdm2, &sdh2, &c[HALFVOL], &zero, &dq2, &gi);
|
||||
}
|
||||
|
||||
*mgas = m1 + m2;
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm1 /= 1.00000000000000e-003;
|
||||
*dm2 /= 1.00000000000000e-003;
|
||||
*dmctr /= 1.00000000000000e-003;
|
||||
*mgas /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,285 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>24</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>p2port</DEFAULT_ICON>
|
||||
<SUB_LABEL>Compressibility + friction submodel of pneumatic pipe (C-R-C)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>7</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>1</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>16</SUB_ID>
|
||||
<TITLE>diameter of pipe</TITLE>
|
||||
<VARNAME>diam</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+01</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-003</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+007</MAX_VALUE>
|
||||
<UNITS>mm</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<TITLE>pipe length</TITLE>
|
||||
<VARNAME>le</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-006</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<UNITS>m</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>relative roughness</TITLE>
|
||||
<VARNAME>rr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e-05</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e-05</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e-001</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>19</SUB_ID>
|
||||
<TITLE>polytropic constant</TITLE>
|
||||
<VARNAME>k</VARNAME>
|
||||
<VISIBILITY>(mode == 1)</VISIBILITY>
|
||||
<DEF_VALUE>1.35000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.35000000000000e+00</VALUE>
|
||||
<MIN_VALUE>5.00000000000000e-001</MIN_VALUE>
|
||||
<MAX_VALUE>2.00000000000000e+000</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>20</SUB_ID>
|
||||
<TITLE>thermal exchange coefficient</TITLE>
|
||||
<VARNAME>kth</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>0.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>J/m**2/K/s</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>21</SUB_ID>
|
||||
<TITLE>external temperature</TITLE>
|
||||
<VARNAME>extemp</VARNAME>
|
||||
<VISIBILITY>(mode == 2)</VISIBILITY>
|
||||
<DEF_VALUE>2.93150000000000e+02</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+02</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
|
||||
<UNITS>K</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>22</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
<IPARAM>
|
||||
<SUB_ID>23</SUB_ID>
|
||||
<TITLE>model</TITLE>
|
||||
<VARNAME>mode</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>2</DEF_VALUE>
|
||||
<VALUE>2</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>2</MAX_VALUE>
|
||||
<ENUM_LIST>
|
||||
<ENUM>
|
||||
<ENUM_STRING>polytropic</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>with thermal exchange</ENUM_STRING>
|
||||
</ENUM>
|
||||
</ENUM_LIST>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>enthalpy flow at center of pipe</TITLE>
|
||||
<VARNAME>dhctr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>J/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>mass flow at center of pipe</TITLE>
|
||||
<VARNAME>dmctr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>g/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>24</SUB_ID>
|
||||
<TITLE>mass of gas in pipe</TITLE>
|
||||
<VARNAME>mgas</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>g</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>Reynolds number</TITLE>
|
||||
<VARNAME>re</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>mass flow parameter (cm)</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>mean gas velocity</TITLE>
|
||||
<VARNAME>v</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>friction factor</TITLE>
|
||||
<VARNAME>ff</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>temperature at port 1</TITLE>
|
||||
<VARNAME>t1</VARNAME>
|
||||
<VARNAME2>dt1</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>K</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<DEF_VALUE>2.93150000000000e+002</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+002</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>pressure at port 1</TITLE>
|
||||
<VARNAME>p1</VARNAME>
|
||||
<VARNAME2>dp1</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
<MIN_VALUE>-1.01300000000000e+005</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+012</MAX_VALUE>
|
||||
<DEF_VALUE>0.00000000000000e+000</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+000</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 1</TITLE>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>mass flow rate at port 1</TITLE>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>t2</VARNAME>
|
||||
<VARNAME2>dt2</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>K</UNITS>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<DEF_VALUE>2.93150000000000e+002</DEF_VALUE>
|
||||
<VALUE>2.93150000000000e+002</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>p2</VARNAME>
|
||||
<VARNAME2>dp2</VARNAME2>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>1</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
<MIN_VALUE>-1.01300000000000e+005</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+012</MAX_VALUE>
|
||||
<DEF_VALUE>0.00000000000000e+000</DEF_VALUE>
|
||||
<VALUE>0.00000000000000e+000</VALUE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,224 @@
|
||||
/* Submodel PNL00R skeleton created by AME Submodel editing utility
|
||||
ven. 5. août 14:34:41 2016 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNL00R
|
||||
------------------------------------------------------------------------------
|
||||
DESCRIPTION :
|
||||
PNL00R is a submodel of a pneumatic pipe with only friction effects.
|
||||
|
||||
Pipe friction is taken into account using a friction factor based on
|
||||
the Reynolds number and the relative roughness.
|
||||
------------------------------------------------------------------------------
|
||||
USAGE :
|
||||
Use this submodel to simulate a pneumatic pipe with friction effects,
|
||||
when the Mach number is low, ie gas velocity < 0.3 * speed of sound .
|
||||
|
||||
The submodels PNGD001 or PNGD002 should be included in your circuit to
|
||||
define the characteristics of the gas.
|
||||
------------------------------------------------------------------------------
|
||||
PARAMETER SETTINGS :
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 FS from PNL0R SN
|
||||
------------------------------------------------------------------------------
|
||||
REVISIONS :
|
||||
------------------------------------------------------------------------------
|
||||
LIST OF FUNCTIONS USED :
|
||||
pn2pipefr_() : frictional coefficient in pneumatic pipes
|
||||
pn2getatp_() : get atmospheric pressure
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNL00R"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
#define TABFR 0 /* real store 0, 1 & 2 are used by pn2pipefr */
|
||||
#define PATM 3
|
||||
#define AREA 4
|
||||
|
||||
|
||||
#define SPL_FR 0
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 3 real parameters:
|
||||
|
||||
diam diameter of pipe [mm -> m]
|
||||
le pipe length [m]
|
||||
rr relative roughness [null]
|
||||
*/
|
||||
|
||||
|
||||
/* There is 1 integer parameter:
|
||||
|
||||
gi gas type index
|
||||
*/
|
||||
|
||||
void pnl00rin_(int *n, double rp[3], int ip[1], double c[5], int ic[1])
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi;
|
||||
double diam, le, rr;
|
||||
|
||||
gi = ip[0];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..2]
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (diam <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nDiameter of pipe should be > 0 [mm].\n");
|
||||
}
|
||||
|
||||
if (le <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nPipe length should be > 0 [m].\n");
|
||||
}
|
||||
|
||||
if (rr < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nRelative roughness should be >= 0.\n");
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[0] *= 1.00000000000000e-003;
|
||||
diam = rp[0];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
/* Compute the cross-sectional area of pipe. */
|
||||
c[AREA] = M_PI * (diam) * (diam) / 4.0;
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 2 ports.
|
||||
|
||||
Port 1 has 4 variables:
|
||||
|
||||
1 dh1 duplicate of dh2 (sign reversed)
|
||||
2 dm1 duplicate of dm2 (sign reversed)
|
||||
3 t1 temperature at port 1 [K] basic variable input
|
||||
4 p1 pressure at port 1 [Pa] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable output
|
||||
2 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable output
|
||||
3 t2 temperature at port 2 [K] basic variable input
|
||||
4 p2 pressure at port 2 [Pa] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 4 internal variables.
|
||||
|
||||
1 re Reynolds number [null] basic variable
|
||||
2 cm mass flow parameter (cm) [(kg*K/J)**(1/2)] basic variable
|
||||
3 v mean gas velocity [m/s] basic variable
|
||||
4 ff friction factor [null] basic variable
|
||||
*/
|
||||
|
||||
void pnl00r_(int *n, double *t1, double *p1, double *dh2, double *dm2
|
||||
, double *t2, double *p2, double *re, double *cm, double *v
|
||||
, double *ff, double rp[3], int ip[1], double c[5], int ic[1])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
double pa1, pa2;
|
||||
double dh1loc, dm1loc;
|
||||
int dummyreg;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi;
|
||||
double diam, le, rr;
|
||||
|
||||
gi = ip[0];
|
||||
|
||||
diam = rp[0];
|
||||
le = rp[1];
|
||||
rr = rp[2];
|
||||
loop = 0;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dh2 = ??;
|
||||
*dm2 = ??;
|
||||
*re = ??;
|
||||
*cm = ??;
|
||||
*v = ??;
|
||||
*ff = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressure */
|
||||
pa1 = *p1 + c[PATM];
|
||||
pa2 = *p2 + c[PATM];
|
||||
|
||||
/* Compute flow through the pipe */
|
||||
|
||||
pn2pipefr_(&pa2, t2, &pa1, t1, &diam, &rr, &le, &c[AREA], re, v, ff,
|
||||
dh2, dm2, &dh1loc, &dm1loc, cm, &c[TABFR], &gi, &ic[SPL_FR], &dummyreg);
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm2 /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,185 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="14.0.0 - 42489-40361 2015">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>18</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>p2port</DEFAULT_ICON>
|
||||
<SUB_LABEL>Friction submodel of pneumatic pipe (R)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>5</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>1</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>diameter of pipe</TITLE>
|
||||
<VARNAME>diam</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+01</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-003</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+007</MAX_VALUE>
|
||||
<UNITS>mm</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>pipe length</TITLE>
|
||||
<VARNAME>le</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-006</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
|
||||
<UNITS>m</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>relative roughness</TITLE>
|
||||
<VARNAME>rr</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1.00000000000000e-05</DEF_VALUE>
|
||||
<VALUE>1.00000000000000e-05</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e-001</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>16</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>Reynolds number</TITLE>
|
||||
<VARNAME>re</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>mass flow parameter (cm)</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>11</SUB_ID>
|
||||
<TITLE>mean gas velocity</TITLE>
|
||||
<VARNAME>v</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>friction factor</TITLE>
|
||||
<VARNAME>ff</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>1</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>1</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>temperature at port 1</TITLE>
|
||||
<VARNAME>t1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>pressure at port 1</TITLE>
|
||||
<VARNAME>p1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>t2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>p2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,240 @@
|
||||
/* Submodel PNOR001 skeleton created by AME Submodel editing utility
|
||||
lun. 10. juil. 17:22:57 2017 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNOR001
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 : Created by FS from PNOR01
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNOR001"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
|
||||
/* real stores */
|
||||
#define PATM 0
|
||||
#define AREA 1
|
||||
#define CQ 2
|
||||
|
||||
/* integer stores */
|
||||
#define DISC_ORIF 0
|
||||
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 4 real parameters:
|
||||
|
||||
cq flow coefficient (Cq) [null]
|
||||
area orifice area [mm**2 -> m**2]
|
||||
Cv flow coefficient (Cv) [null]
|
||||
Kv flow coefficient (Kv) [null]
|
||||
*/
|
||||
|
||||
|
||||
/* There are 2 integer parameters:
|
||||
|
||||
gi gas type index
|
||||
flowset flow coefficient setting
|
||||
*/
|
||||
|
||||
void pnor001in_(int *n, double rp[4], int ip[2], double c[3]
|
||||
, int ic[1])
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi, flowset;
|
||||
double cq, area, Cv, Kv;
|
||||
|
||||
gi = ip[0];
|
||||
flowset = ip[1];
|
||||
|
||||
cq = rp[0];
|
||||
area = rp[1];
|
||||
Cv = rp[2];
|
||||
Kv = rp[3];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..3]
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (flowset == 1)
|
||||
{
|
||||
if (area < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nOrifice area should be positive.\n");
|
||||
}
|
||||
|
||||
if (cq <= 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nFlow coefficient should be strictly positive.\n");
|
||||
}
|
||||
}
|
||||
else if (flowset == 2)
|
||||
{
|
||||
if (Cv < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nFlow coefficient (Cv) should be positive (value is %g).\n", Cv);
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
if (Kv < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nFlow coefficient (Kv) should be positive (value is %g).\n", Kv);
|
||||
}
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
if (flowset < 1 || flowset > 3)
|
||||
{
|
||||
amefprintf(stderr, "\nflow coefficient setting must be in range [1..3].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[1] *= 1.00000000000000e-006;
|
||||
area = rp[1];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
|
||||
/* get atmospheric pressure */
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
if (flowset == 1)
|
||||
{
|
||||
c[CQ] = cq;
|
||||
c[AREA] = area;
|
||||
}
|
||||
else
|
||||
{
|
||||
/* calculation of equivalent area with Cv or Kv.
|
||||
Default value of cq; the same value will be used in pn2rcqfix. */
|
||||
c[CQ] = 0.72;
|
||||
|
||||
if (flowset == 2) /* Cv */
|
||||
orif_areafromcv_(&Cv, &c[CQ], &c[AREA]);
|
||||
else
|
||||
orif_areafromkv_(&Kv, &c[CQ], &c[AREA]);
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 2 ports.
|
||||
|
||||
Port 1 has 4 variables:
|
||||
|
||||
1 dh1 enthalpy flow rate at port 1 [J/s -> W] basic variable output
|
||||
2 dm1 mass flow rate at port 1 [g/s -> kg/s] basic variable output
|
||||
3 temp1 temperature at port 1 [K] basic variable input
|
||||
4 press1 pressure at port 1 [Pa] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 dh2 duplicate of dh1 (sign reversed)
|
||||
2 dm2 duplicate of dm1 (sign reversed)
|
||||
3 temp2 temperature at port 2 [K] basic variable input
|
||||
4 press2 pressure at port 2 [Pa] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 2 internal variables.
|
||||
|
||||
1 cm mass flow parameter (cm) [(kg*K/J)**(1/2)] basic variable
|
||||
2 gasvel vena contracta gas velocity [m/s] basic variable
|
||||
*/
|
||||
|
||||
void pnor001_(int *n, double *dh1, double *dm1, double *temp1
|
||||
, double *press1, double *temp2, double *press2, double *cm
|
||||
, double *gasvel, double rp[4], int ip[2], double c[3]
|
||||
, int ic[1])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
double pressa1, pressa2;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi, flowset;
|
||||
double cq, area, Cv, Kv;
|
||||
|
||||
gi = ip[0];
|
||||
flowset = ip[1];
|
||||
|
||||
cq = rp[0];
|
||||
area = rp[1];
|
||||
Cv = rp[2];
|
||||
Kv = rp[3];
|
||||
loop = 0;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dh1 = ??;
|
||||
*dm1 = ??;
|
||||
*cm = ??;
|
||||
*gasvel = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressures */
|
||||
pressa1 = *press1 + c[PATM];
|
||||
pressa2 = *press2 + c[PATM];
|
||||
|
||||
/* calculation of the flows */
|
||||
pn2rcqfix_( dh1, dm1, temp1, &pressa1, temp2, &pressa2, &c[AREA], &c[CQ], &gi,
|
||||
cm, gasvel, &ic[DISC_ORIF]);
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm1 /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,199 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="14.0.0 - 42489-40361 2015">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>18</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>pn_orifice</DEFAULT_ICON>
|
||||
<SUB_LABEL>pneumatic orifice (constant flow coefficient)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>3</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>1</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>flow coefficient (Cq)</TITLE>
|
||||
<VARNAME>cq</VARNAME>
|
||||
<VISIBILITY>flowset==1</VISIBILITY>
|
||||
<DEF_VALUE>7.20000000000000e-01</DEF_VALUE>
|
||||
<VALUE>7.20000000000000e-01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-010</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+000</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>11</SUB_ID>
|
||||
<TITLE>orifice area</TITLE>
|
||||
<VARNAME>area</VARNAME>
|
||||
<VISIBILITY>flowset==1</VISIBILITY>
|
||||
<DEF_VALUE>5.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>5.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>mm**2</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>17</SUB_ID>
|
||||
<TITLE>flow coefficient (Cv)</TITLE>
|
||||
<VARNAME>Cv</VARNAME>
|
||||
<VISIBILITY>flowset==2</VISIBILITY>
|
||||
<DEF_VALUE>5.00000000000000e-01</DEF_VALUE>
|
||||
<VALUE>5.00000000000000e-01</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+030</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>flow coefficient (Kv)</TITLE>
|
||||
<VARNAME>Kv</VARNAME>
|
||||
<VISIBILITY>flowset==3</VISIBILITY>
|
||||
<DEF_VALUE>4.00000000000000e-01</DEF_VALUE>
|
||||
<VALUE>4.00000000000000e-01</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+030</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
<IPARAM>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>flow coefficient setting</TITLE>
|
||||
<VARNAME>flowset</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>3</MAX_VALUE>
|
||||
<ENUM_LIST>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Cq</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Cv</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Kv</ENUM_STRING>
|
||||
</ENUM>
|
||||
</ENUM_LIST>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>mass flow parameter (cm)</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>vena contracta gas velocity</TITLE>
|
||||
<VARNAME>gasvel</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 1</TITLE>
|
||||
<VARNAME>dh1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>mass flow rate at port 1</TITLE>
|
||||
<VARNAME>dm1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>temperature at port 1</TITLE>
|
||||
<VARNAME>temp1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>pressure at port 1</TITLE>
|
||||
<VARNAME>press1</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>0</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>temp2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>press2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
@@ -0,0 +1,254 @@
|
||||
/* Submodel PNVO001 skeleton created by AME Submodel editing utility
|
||||
ven. 6. oct. 11:10:58 2017 */
|
||||
|
||||
|
||||
|
||||
#include <math.h>
|
||||
#include <stdio.h>
|
||||
#include <stdlib.h>
|
||||
#include "ameutils.h"
|
||||
/* *******************************************************************************
|
||||
TITLE : PNVO001
|
||||
------------------------------------------------------------------------------
|
||||
DATE OF CREATION / AUTHOR :
|
||||
2002 : Created by FS from PNVO01
|
||||
------------------------------------------------------------------------------
|
||||
SOURCE :
|
||||
|
||||
This material contains trade secrets or otherwise confidential
|
||||
information owned by Siemens Industry Software Inc. or its
|
||||
affiliates (collectively, "Siemens"), or its licensors. Access to
|
||||
and use of this information is strictly limited as set forth in the
|
||||
Customer's applicable agreements with Siemens.
|
||||
|
||||
Unpublished work. Copyright 2023 Siemens
|
||||
|
||||
******************************************************************************* */
|
||||
|
||||
#define _SUBMODELNAME_ "PNVO001"
|
||||
|
||||
/* >>>>>>>>>>>>Insert Private Code Here. */
|
||||
|
||||
/* real stores */
|
||||
#define PATM 0
|
||||
#define AREAMAX 1
|
||||
#define CQ 2
|
||||
|
||||
/* integer stores */
|
||||
#define DISC_LIMIT 0
|
||||
#define DISC_ORIF 1
|
||||
|
||||
/* <<<<<<<<<<<<End of Private Code. */
|
||||
|
||||
|
||||
/* There are 4 real parameters:
|
||||
|
||||
cq flow coefficient (Cq) [null]
|
||||
area0 orifice area at maximum opening [mm**2 -> m**2]
|
||||
Cv maximum flow coefficient (Cv) [null]
|
||||
Kv maximum flow coefficient (Kv) [null]
|
||||
*/
|
||||
|
||||
|
||||
/* There are 2 integer parameters:
|
||||
|
||||
gi gas type index
|
||||
flowset flow coefficient setting
|
||||
*/
|
||||
|
||||
void pnvo001in_(int *n, double rp[4], int ip[2], double c[3]
|
||||
, int ic[2])
|
||||
|
||||
{
|
||||
int loop, error;
|
||||
/* >>>>>>>>>>>>Extra Initialization Function Declarations Here. */
|
||||
/* <<<<<<<<<<<<End of Extra Initialization declarations. */
|
||||
int gi, flowset;
|
||||
double cq, area0, Cv, Kv;
|
||||
|
||||
gi = ip[0];
|
||||
flowset = ip[1];
|
||||
|
||||
cq = rp[0];
|
||||
area0 = rp[1];
|
||||
Cv = rp[2];
|
||||
Kv = rp[3];
|
||||
loop = 0;
|
||||
error = 0;
|
||||
|
||||
/*
|
||||
If necessary, check values of the following:
|
||||
|
||||
rp[0..3]
|
||||
*/
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Check Statements. */
|
||||
|
||||
pn2_valid_gas_(&gi, &error);
|
||||
|
||||
if (flowset == 1)
|
||||
{
|
||||
if (area0 < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nOrifice area at maximum opening should be positive.\n");
|
||||
}
|
||||
|
||||
if (cq <= 0.0 )
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nFlow coefficient should be strictly positive.\n");
|
||||
}
|
||||
}
|
||||
else if (flowset == 2)
|
||||
{
|
||||
if (Cv < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nMaximum flow coefficient (Cv) should be positive (value is %g).\n", Cv);
|
||||
}
|
||||
}
|
||||
else
|
||||
{
|
||||
if (Kv < 0.0)
|
||||
{
|
||||
error = 2;
|
||||
amefprintf(stderr, "\nMaximum flow coefficient (Kv) should be positive (value is %g).\n", Kv);
|
||||
}
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Check Statements. */
|
||||
|
||||
/* Integer parameter checking: */
|
||||
|
||||
if (gi < 1 || gi > 99)
|
||||
{
|
||||
amefprintf(stderr, "\ngas type index must be in range [1..99].\n");
|
||||
error = 2;
|
||||
}
|
||||
if (flowset < 1 || flowset > 3)
|
||||
{
|
||||
amefprintf(stderr, "\nflow coefficient setting must be in range [1..3].\n");
|
||||
error = 2;
|
||||
}
|
||||
|
||||
SUBMODEL_HANDLE_AND_RESET_ERROR(_SUBMODELNAME_, n, error)
|
||||
|
||||
/* Common -> SI units conversions. */
|
||||
|
||||
rp[1] *= 1.00000000000000e-006;
|
||||
area0 = rp[1];
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Initialization Function Executable Statements. */
|
||||
|
||||
/* get atmospheric pressure */
|
||||
c[PATM] = pn2getatp_();
|
||||
|
||||
if (flowset == 1)
|
||||
{
|
||||
c[CQ] = cq;
|
||||
c[AREAMAX] = area0;
|
||||
}
|
||||
else
|
||||
{
|
||||
/* calculation of equivalent maximal area with Cv or Kv.
|
||||
Default value of cq; the same value will be used in pn2rcqfix. */
|
||||
c[CQ] = 0.72;
|
||||
|
||||
if (flowset == 2) /* Cv */
|
||||
orif_areafromcv_(&Cv, &c[CQ], &c[AREAMAX]);
|
||||
else
|
||||
orif_areafromkv_(&Kv, &c[CQ], &c[AREAMAX]);
|
||||
}
|
||||
|
||||
/* <<<<<<<<<<<<End of Initialization Executable Statements. */
|
||||
}
|
||||
|
||||
/* There are 3 ports.
|
||||
|
||||
Port 1 has 1 variable:
|
||||
|
||||
1 res input signal [null] basic variable input
|
||||
|
||||
Port 2 has 4 variables:
|
||||
|
||||
1 dh2 enthalpy flow rate at port 2 [J/s -> W] basic variable output
|
||||
2 dm2 mass flow rate at port 2 [g/s -> kg/s] basic variable output
|
||||
3 temp2 temperature at port 2 [K] basic variable input
|
||||
4 press2 pressure at port 2 [Pa] basic variable input
|
||||
|
||||
Port 3 has 4 variables:
|
||||
|
||||
1 dh3 duplicate of dh2 (sign reversed)
|
||||
2 dm3 duplicate of dm2 (sign reversed)
|
||||
3 temp3 temperature at port 3 [K] basic variable input
|
||||
4 press3 pressure at port 3 [Pa] basic variable input
|
||||
*/
|
||||
|
||||
/* There are 3 internal variables.
|
||||
|
||||
1 xv fractional opening [null] basic variable
|
||||
2 cm mass flow parameter (cm) [(kg*K/J)**(1/2)] basic variable
|
||||
3 gasvel vena contracta gas velocity [m/s] basic variable
|
||||
*/
|
||||
|
||||
void pnvo001_(int *n, double *res, double *dh2, double *dm2
|
||||
, double *temp2, double *press2, double *temp3, double *press3
|
||||
, double *xv, double *cm, double *gasvel, double rp[4]
|
||||
, int ip[2], double c[3], int ic[2])
|
||||
|
||||
{
|
||||
int loop;
|
||||
/* >>>>>>>>>>>>Extra Calculation Function Declarations Here. */
|
||||
double marea; /* modulated area */
|
||||
double pressa2, pressa3;
|
||||
static double zero = 0.0, one = 1.0;
|
||||
/* <<<<<<<<<<<<End of Extra Calculation declarations. */
|
||||
int gi, flowset;
|
||||
double cq, area0, Cv, Kv;
|
||||
|
||||
gi = ip[0];
|
||||
flowset = ip[1];
|
||||
|
||||
cq = rp[0];
|
||||
area0 = rp[1];
|
||||
Cv = rp[2];
|
||||
Kv = rp[3];
|
||||
loop = 0;
|
||||
|
||||
/*
|
||||
Set all submodel outputs below:
|
||||
|
||||
*dh2 = ??;
|
||||
*dm2 = ??;
|
||||
*xv = ??;
|
||||
*cm = ??;
|
||||
*gasvel = ??;
|
||||
*/
|
||||
|
||||
|
||||
|
||||
/* >>>>>>>>>>>>Calculation Function Executable Statements. */
|
||||
|
||||
/* set absolute pressure */
|
||||
pressa2 = *press2 + c[PATM];
|
||||
pressa3 = *press3 + c[PATM];
|
||||
|
||||
*xv = dlimit_(res, &zero, &one, &ic[DISC_LIMIT]);
|
||||
|
||||
/* limitation of the modulated area */
|
||||
marea = *xv * c[AREAMAX];
|
||||
|
||||
/*** calculation of the flows ***/
|
||||
pn2rcqfix_( dh2, dm2, temp2, &pressa2, temp3, &pressa3, &marea, &c[CQ], &gi,
|
||||
cm, gasvel, &ic[DISC_ORIF] );
|
||||
|
||||
/* <<<<<<<<<<<<End of Calculation Executable Statements. */
|
||||
|
||||
/* SI -> Common units conversions. */
|
||||
|
||||
*dm2 /= 1.00000000000000e-003;
|
||||
}
|
||||
|
||||
@@ -0,0 +1,220 @@
|
||||
<?xml version="1.0" encoding="ISO-8859-1"?>
|
||||
<!DOCTYPE SPE>
|
||||
<SPE DOC_VERSION="2" AME_VERSION="14.0.0 - 42489-40361 2015">
|
||||
|
||||
<SUBMODEL>
|
||||
<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>20</SUB_ID_MAX>
|
||||
<DEFAULT_ICON>pn_morifice</DEFAULT_ICON>
|
||||
<SUB_LABEL>modulated pneumatic orifice (constant flow coefficient)</SUB_LABEL>
|
||||
<SUB_UNIT>0</SUB_UNIT>
|
||||
<R_STORES_NUMBER>3</R_STORES_NUMBER>
|
||||
<I_STORES_NUMBER>2</I_STORES_NUMBER>
|
||||
<OUTPUT_TYPE>1</OUTPUT_TYPE>
|
||||
<RPARAMS_LIST>
|
||||
<RPARAM>
|
||||
<SUB_ID>12</SUB_ID>
|
||||
<TITLE>flow coefficient (Cq)</TITLE>
|
||||
<VARNAME>cq</VARNAME>
|
||||
<VISIBILITY>flowset==1</VISIBILITY>
|
||||
<DEF_VALUE>7.20000000000000e-01</DEF_VALUE>
|
||||
<VALUE>7.20000000000000e-01</VALUE>
|
||||
<MIN_VALUE>1.00000000000000e-010</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+000</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>13</SUB_ID>
|
||||
<TITLE>orifice area at maximum opening</TITLE>
|
||||
<VARNAME>area0</VARNAME>
|
||||
<VISIBILITY>flowset==1</VISIBILITY>
|
||||
<DEF_VALUE>5.00000000000000e+00</DEF_VALUE>
|
||||
<VALUE>5.00000000000000e+00</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
|
||||
<UNITS>mm**2</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>18</SUB_ID>
|
||||
<TITLE>maximum flow coefficient (Cv)</TITLE>
|
||||
<VARNAME>Cv</VARNAME>
|
||||
<VISIBILITY>flowset==2</VISIBILITY>
|
||||
<DEF_VALUE>5.00000000000000e-01</DEF_VALUE>
|
||||
<VALUE>5.00000000000000e-01</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+030</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
<RPARAM>
|
||||
<SUB_ID>19</SUB_ID>
|
||||
<TITLE>maximum flow coefficient (Kv)</TITLE>
|
||||
<VARNAME>Kv</VARNAME>
|
||||
<VISIBILITY>flowset==3</VISIBILITY>
|
||||
<DEF_VALUE>4.00000000000000e-01</DEF_VALUE>
|
||||
<VALUE>4.00000000000000e-01</VALUE>
|
||||
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
|
||||
<MAX_VALUE>1.00000000000000e+030</MAX_VALUE>
|
||||
<UNITS>null</UNITS>
|
||||
</RPARAM>
|
||||
</RPARAMS_LIST>
|
||||
<IPARAMS_LIST>
|
||||
<IPARAM>
|
||||
<SUB_ID>14</SUB_ID>
|
||||
<TITLE>gas type index</TITLE>
|
||||
<VARNAME>gi</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>99</MAX_VALUE>
|
||||
</IPARAM>
|
||||
<IPARAM>
|
||||
<SUB_ID>15</SUB_ID>
|
||||
<TITLE>flow coefficient setting</TITLE>
|
||||
<VARNAME>flowset</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<DEF_VALUE>1</DEF_VALUE>
|
||||
<VALUE>1</VALUE>
|
||||
<MIN_VALUE>1</MIN_VALUE>
|
||||
<MAX_VALUE>3</MAX_VALUE>
|
||||
<ENUM_LIST>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Cq</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Cv</ENUM_STRING>
|
||||
</ENUM>
|
||||
<ENUM>
|
||||
<ENUM_STRING>Kv</ENUM_STRING>
|
||||
</ENUM>
|
||||
</ENUM_LIST>
|
||||
</IPARAM>
|
||||
</IPARAMS_LIST>
|
||||
<IVARS_LIST>
|
||||
<IVAR>
|
||||
<SUB_ID>20</SUB_ID>
|
||||
<TITLE>fractional opening</TITLE>
|
||||
<VARNAME>xv</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>null</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>10</SUB_ID>
|
||||
<TITLE>mass flow parameter (cm)</TITLE>
|
||||
<VARNAME>cm</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>(kg*K/J)**(1/2)</UNITS>
|
||||
</IVAR>
|
||||
<IVAR>
|
||||
<SUB_ID>11</SUB_ID>
|
||||
<TITLE>vena contracta gas velocity</TITLE>
|
||||
<VARNAME>gasvel</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<UNITS>m/s</UNITS>
|
||||
</IVAR>
|
||||
</IVARS_LIST>
|
||||
<EVARS_LIST>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>1</SUB_ID>
|
||||
<TITLE>input signal</TITLE>
|
||||
<VARNAME>res</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>null</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>2</SUB_ID>
|
||||
<TITLE>enthalpy flow rate at port 2</TITLE>
|
||||
<VARNAME>dh2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>J/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>3</SUB_ID>
|
||||
<TITLE>mass flow rate at port 2</TITLE>
|
||||
<VARNAME>dm2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>2</IO>
|
||||
<UNITS>g/s</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>4</SUB_ID>
|
||||
<TITLE>temperature at port 2</TITLE>
|
||||
<VARNAME>temp2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>5</SUB_ID>
|
||||
<TITLE>pressure at port 2</TITLE>
|
||||
<VARNAME>press2</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
<PORT>
|
||||
<EVAR>
|
||||
<SUB_ID>6</SUB_ID>
|
||||
<VARNAME>dh3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>1</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>0</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>7</SUB_ID>
|
||||
<VARNAME>dm3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>4</TYPE>
|
||||
<PRIMARY_PORT>1</PRIMARY_PORT>
|
||||
<PRIMARY_VAR>1</PRIMARY_VAR>
|
||||
<DUP_TYPE>1</DUP_TYPE>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>8</SUB_ID>
|
||||
<TITLE>temperature at port 3</TITLE>
|
||||
<VARNAME>temp3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>K</UNITS>
|
||||
</EVAR>
|
||||
<EVAR>
|
||||
<SUB_ID>9</SUB_ID>
|
||||
<TITLE>pressure at port 3</TITLE>
|
||||
<VARNAME>press3</VARNAME>
|
||||
<VISIBILITY>True</VISIBILITY>
|
||||
<TYPE>0</TYPE>
|
||||
<DIMENSION>1</DIMENSION>
|
||||
<IO>1</IO>
|
||||
<UNITS>Pa</UNITS>
|
||||
</EVAR>
|
||||
</PORT>
|
||||
</EVARS_LIST>
|
||||
<SUBIDS_RESET>0</SUBIDS_RESET>
|
||||
</SUBMODEL>
|
||||
</SPE>
|
||||
File diff suppressed because it is too large.
Load diff
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@@ -0,0 +1,140 @@
|
||||
# test_mql
|
||||
|
||||
本目录记录 AMESim 模型 `test_mql.ame` 向 `app.simulation` 迁移时使用的源模型信息、结果对齐约定和当前进度。
|
||||
|
||||
## 目标
|
||||
|
||||
迁移目标不是复制 AMESim `.results` 中的观测值，而是建立真实的 Python 仿真链路：
|
||||
|
||||
`组件方程 -> SimulationNetwork/系统装配 -> closure -> snapshot/端口写回 -> RHS -> solver -> reporting/comparison`
|
||||
|
||||
Python 输出只有通过 AMESim baseline 对比后才能作为数值一致性依据。duplicate、反号或派生观测可以用于验证端口方向，但不能替代组件方程和网络闭合。
|
||||
|
||||
## 模型与源数据
|
||||
|
||||
- AMESim 源模型：`AmesimModels/test_mql.ame`
|
||||
- Python 系统类：`app.simulation.examples.test_mql.system.TestMqlSystem`
|
||||
- 结构运行入口：`app.simulation.examples.test_mql.run`
|
||||
- 132 状态比较入口：`app.simulation.examples.test_mql.run_full_state_comparison`
|
||||
- AMESim 组件数：117
|
||||
- LINE 连接数：84
|
||||
- 连续状态数：132
|
||||
- 离散状态数：24
|
||||
- 全局参数：`D1=20`、`D2=20`、`D3=14`、`P0=153`、`Pdq=1`、`V=15`、`cf=0.45`
|
||||
|
||||
`.ame` 文件是 tar 包，迁移和校验主要使用其中的：
|
||||
|
||||
- `test_mql_.cir`：组件、连接、参数表达式和生成代码线索。
|
||||
- `test_mql_.param` / `test_mql_.data`：参数和结果配套数据。
|
||||
- `test_mql_.modelinfo` / `test_mql_.sim`：状态数和仿真设置。
|
||||
- `test_mql_.var` / `test_mql_.results`：AMESim `Data_Path` 目录和 baseline 时序。
|
||||
|
||||
当前结果解析器可读取 1002 个时间点和 1116 个保存变量，无需先转换成 CSV。
|
||||
|
||||
## 当前实现
|
||||
|
||||
当前已经完成：
|
||||
|
||||
- AMESim 组件、LINE 连接、直接组件接触、全局参数和变量目录解析。
|
||||
- 氦气 Peng-Robinson 物性；内部使用绝对压力，AMESim `press` 按相对 `101300 Pa` 的表压输出。
|
||||
- `PNCH023 / PNCH012 / PNOR001 / PNVO001` 气动组件。
|
||||
- `PNL0001 / PNL0002 / PNL0003 / PNL00R` 管路动态或阻性关系。
|
||||
- `PN3NODE2 / P4NODE2` 代数节点、真实邻接拓扑、canonical flow 和端口写回。
|
||||
- `PNRP17 / MECMAS21 / LSTP00A / LMECHN1 / UD00 / FORC` 当前工况可确认的机械行为。
|
||||
- 112 个气动状态和 20 个机械状态组成的 132 状态总闭包。
|
||||
- 活塞运动学、变容气室机械反馈、气动力、外力、端止动和质量约束耦合。
|
||||
- 关键 `Data_Path` 序列导出、schema validation、AMESim 插值 comparison、误差排序、端点诊断和变容气室 RHS 拆解。
|
||||
|
||||
主要实现位置：
|
||||
|
||||
- `app/simulation/examples/test_mql/system.py`
|
||||
- `app/simulation/examples/test_mql/closure.py`
|
||||
- `app/simulation/examples/test_mql/pneumatic.py`
|
||||
- `app/simulation/examples/test_mql/mechanical.py`
|
||||
- `app/simulation/examples/test_mql/lines.py`
|
||||
- `app/simulation/examples/test_mql/primitives/`
|
||||
- `app/simulation/examples/test_mql/structural_network.py`
|
||||
- `app/simulation/reporting/amesim_results.py`
|
||||
- `app/simulation/reporting/test_mql_comparison.py`
|
||||
- `app/simulation/examples/test_mql/run_full_state_comparison.py`
|
||||
|
||||
## 当前对比结果
|
||||
|
||||
默认 comparison 已从区间内插值的 `t=1e-5 s` 改为与 AMESim
|
||||
首个保存时刻精确对齐的 `t=0.01 s`，当前比较 13 个关键信号，并
|
||||
新增 `xv@pn_morifice_1`、`dm2@pn_morifice_1` 的结构化 PNVO 诊断。
|
||||
|
||||
事件前 `t=0.01 s` 对比：
|
||||
|
||||
- `press@pn_c1_8`：Python `-1286.601221 Pa`，AMESim
|
||||
`-1288.253185 Pa`，绝对误差约 `1.651964 Pa`。
|
||||
- `dm1@pneumatic_69`：Python `-0.002485112 g/s`，AMESim
|
||||
`-0.002054255 g/s`；换算后的 canonical 流量绝对误差约
|
||||
`4.30857e-7 kg/s`。
|
||||
- `xv@pn_morifice_1` 和 `dm2@pn_morifice_1` 在两侧均为 0，确认
|
||||
STEP0 事件前 PNVO 保持关闭。
|
||||
- `vol1@pn_brp2_8` 绝对误差约 `8.76e-5`，机械位移、速度和加速度
|
||||
仍保持较小误差；当前较明显的累计差异集中在 PNL0001 流量和
|
||||
PNCH012 压力/能量链路。
|
||||
|
||||
新增 `--pnvo-event-boundary` 诊断：先积分到 `0.04 s` 的左极限，
|
||||
再按 STEP0 的右连续语义在事件时刻读取开度和流量。结果为：
|
||||
|
||||
- `xv@pn_morifice_1`：Python/AMESim 均为 `1`。
|
||||
- `dm2@pn_morifice_1`：Python `502.945005 g/s`，AMESim
|
||||
`497.823823 g/s`，绝对误差约 `5.121182 g/s`，相对约 `1.03%`。
|
||||
- `press@pn_c1_8` 绝对误差约 `55.4815 Pa`；
|
||||
`dm1@pneumatic_69` 绝对误差约 `0.00281880 g/s`。
|
||||
|
||||
这说明 PNVO 开启瞬间的开度语义和主流量量级已经对齐，但事件前
|
||||
累积压力/支路流量仍有偏差。常规积分直接跨越事件到 `0.05 s` 时，
|
||||
当前进程会被系统终止，尚未形成可信的事件后结果；不能据此声明
|
||||
完整 `0.04 -> 0.05 s` 窗口已经可运行。
|
||||
|
||||
## 下一步
|
||||
|
||||
1. 优先定位 `0 -> 0.04 s` 累积的 `pneumatic_69` 流量与
|
||||
`pn_c1_8` 压力偏差，区分 PNL0001 阻力和 PNCH012 能量方程。
|
||||
2. 采用显式事件分段或针对事件后的局部数值策略，解决跨越
|
||||
`t=0.04 s` 后积分进程被终止的问题，再验证 `t=0.05 s` 保存点。
|
||||
3. 保留 `press@pn_c1_8`、`dm1@pneumatic_69`、PNVO `xv/dm2`
|
||||
和 chamber RHS breakdown 作为同一条诊断链。
|
||||
4. 在完整开启窗口稳定后，再判断是否需要校准 PNVO 流量系数。
|
||||
|
||||
`pn_c1_8` 的直接主线是 `pneumatic_69`；`pneumatic_96`
|
||||
属于另一条固定气室支路，不是该诊断对象。
|
||||
|
||||
## 运行与验证
|
||||
|
||||
运行默认短时域 comparison：
|
||||
|
||||
```bash
|
||||
python3 -m app.simulation.examples.test_mql.run_full_state_comparison
|
||||
```
|
||||
|
||||
运行 PNVO 事件边界诊断：
|
||||
|
||||
```bash
|
||||
python3 -m app.simulation.examples.test_mql.run_full_state_comparison --pnvo-event-boundary
|
||||
```
|
||||
|
||||
运行相关测试：
|
||||
|
||||
```bash
|
||||
python3 -m unittest tests.test_run_test_mql_full_state_comparison tests.test_test_mql_pnl0001_segment
|
||||
```
|
||||
|
||||
运行全量测试：
|
||||
|
||||
```bash
|
||||
python3 -m unittest discover -s tests -t .
|
||||
```
|
||||
|
||||
## 对齐约定
|
||||
|
||||
- 组件 alias 和输出名优先保持 AMESim 原名及 `Data_Path`。
|
||||
- `PortState.m_flow > 0` 表示流入当前组件。
|
||||
- closure 先定义 canonical flow，再按各组件端口方向写回 `m_flow`。
|
||||
- AMESim 管路质量流量通常以 `g/s` 保存，Python 内部统一使用 `kg/s`。
|
||||
- CSV 是人工检查和交换格式，不是读取 AMESim baseline 的前置条件。
|
||||
- 未完成真实 Python 输出对比前，不使用“与 AMESim 完全一致”之类结论。
|
||||
@@ -0,0 +1,24 @@
|
||||
# 浏览器四路、八路测试工程
|
||||
|
||||
本目录中的 JSON/XML 仅保留以下两个可由网页“导入工程 JSON”识别的工程文件。已逐项核对对应 AME 图纸的元件、公开物理参数及端口连接；AME 单位与工程 SI 单位之间的换算已纳入检查。
|
||||
|
||||
| 浏览器工程 | Amesim 原文件 | 元件 / 参数 / 连接 |
|
||||
|---|---|---|
|
||||
| [test-mql-4-corrected.json](test-mql-4-corrected.json) | [test_mql_4.ame](test_mql_4.ame) | 81 / 582 / 90 |
|
||||
| [test-mql-8-corrected.json](test-mql-8-corrected.json) | [test_mql.ame](test_mql.ame) | 157 / 1092 / 178 |
|
||||
|
||||
网页当前只支持导入工程 JSON；XML 可从网页下载，用作后端输入。网页使用原生 BDF 和当前默认 `rtol=1e-8`，与 AME 内部积分器及历史数值设置不能视为相同。这里的参数对齐指模型物理参数与初值，不声称不同仿真器所有数值输出完全一致。
|
||||
|
||||
2026-09-11 整理时，两份工程内容保持不变。其他 JSON/XML 已按用途移出本目录，移动前后字节数及 SHA256 相同：
|
||||
|
||||
| 原文件 | 当前路径 | 用途 |
|
||||
|---|---|---|
|
||||
| native-python-reference.json | [原生数值基准](../baselines/native/native-python-reference.json) | 50 网络冻结参考 |
|
||||
| test-mql-4-amesim-reference.json | [四路 Amesim 曲线基准](../baselines/simulation/test_mql_4/test-mql-4-amesim-reference.json) | 72 曲线、57 时刻 |
|
||||
| test-mql-4-corrected.xml | [四路执行 XML](../fixtures/amesim/test-mql-4-corrected.xml) | 与四路 JSON 同步的后端输入 |
|
||||
| test-mql-8.json / test-mql-8.xml | [旧 JSON](../fixtures/legacy/test-mql-8.json) / [旧 XML](../fixtures/legacy/test-mql-8.xml) | 修正前输入及布局来源 |
|
||||
| test_mql-full-branches-01-04.xml | [历史分支基准输入](../baselines/simulation/test_mql_full_branches/sources/test_mql-full-branches-01-04.xml) | 历史回归清单绑定的输入 |
|
||||
| native-skill-test.xml | [原生通用测试输入](../fixtures/native-skill-test.xml) | 原生编译、执行与 CI 检查 |
|
||||
| fixtures/high_stiffness_explicit_rk45.xml | [高刚度 RK45 输入](../fixtures/high_stiffness_explicit_rk45.xml) | 独立刚度回归用例 |
|
||||
|
||||
AME 原文件及本目录中其他类型的资料保持原位。历史运行记录保留当时路径；活动测试、审计脚本、CI 和当前交付说明已更新到新路径。
|
||||
@@ -1,325 +0,0 @@
|
||||
<?xml version="1.0" encoding="UTF-8"?>
|
||||
<System name="demo-system" schemaVersion="3" unitSystem="SI">
|
||||
<Simulation tStart="0" tStop="10" sampleStep="0.02" maxStep="0.02" method="RK45"/>
|
||||
<Components>
|
||||
<Component id="amesim_pnch023_1" type="amesim_pnch023" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol" value="0.057"/>
|
||||
<Parameter name="kth" value="0"/>
|
||||
<Parameter name="sth" value="0.1"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="15300000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnvo001_1" type="amesim_pnvo001" modelVersion="0.2.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cq" value="0.45"/>
|
||||
<Parameter name="area0" value="0.0000785"/>
|
||||
<Parameter name="Cv" value="0.5"/>
|
||||
<Parameter name="Kv" value="0.4"/>
|
||||
<Parameter name="flowset" value="1"/>
|
||||
<Parameter name="opening0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_step0_1" type="amesim_step0" modelVersion="0.1.0">
|
||||
<Parameter name="initial" value="0"/>
|
||||
<Parameter name="final" value="1"/>
|
||||
<Parameter name="time" value="0.04"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnch012_1" type="amesim_pnch012" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol0" value="0.015"/>
|
||||
<Parameter name="kth" value="1500"/>
|
||||
<Parameter name="sth" value="0.7"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="100000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
<Parameter name="vol1" value="0"/>
|
||||
<Parameter name="vol2" value="0"/>
|
||||
<Parameter name="vol3" value="0"/>
|
||||
<Parameter name="vol4" value="0"/>
|
||||
<Parameter name="dvol1" value="0"/>
|
||||
<Parameter name="dvol2" value="0"/>
|
||||
<Parameter name="dvol3" value="0"/>
|
||||
<Parameter name="dvol4" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnpl01_2" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_3" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_4" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_ud00_1" type="amesim_ud00" modelVersion="0.2.0">
|
||||
<Parameter name="tstart" value="0"/>
|
||||
<Parameter name="start1" value="100000000000000000"/>
|
||||
<Parameter name="end1" value="100000000000000000"/>
|
||||
<Parameter name="t1" value="0.8"/>
|
||||
<Parameter name="start2" value="49000"/>
|
||||
<Parameter name="end2" value="49000"/>
|
||||
<Parameter name="t2" value="10"/>
|
||||
<Parameter name="start3" value="1"/>
|
||||
<Parameter name="end3" value="1"/>
|
||||
<Parameter name="t3" value="0"/>
|
||||
<Parameter name="start4" value="1"/>
|
||||
<Parameter name="end4" value="1"/>
|
||||
<Parameter name="t4" value="0"/>
|
||||
<Parameter name="start5" value="1"/>
|
||||
<Parameter name="end5" value="1"/>
|
||||
<Parameter name="t5" value="0"/>
|
||||
<Parameter name="start6" value="1"/>
|
||||
<Parameter name="end6" value="1"/>
|
||||
<Parameter name="t6" value="0"/>
|
||||
<Parameter name="start7" value="1"/>
|
||||
<Parameter name="end7" value="1"/>
|
||||
<Parameter name="t7" value="0"/>
|
||||
<Parameter name="start8" value="1"/>
|
||||
<Parameter name="end8" value="1"/>
|
||||
<Parameter name="t8" value="0"/>
|
||||
<Parameter name="nstages" value="2"/>
|
||||
<Parameter name="iscyclic" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_forc_1" type="amesim_forc" modelVersion="0.2.0">
|
||||
<Parameter name="direction" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnrp17_1" type="amesim_pnrp17" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="dp" value="0.2"/>
|
||||
<Parameter name="dr" value="0.001"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_helium_medium_1" type="amesim_helium_medium" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="property_model" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnch012_2" type="amesim_pnch012" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol0" value="0.015"/>
|
||||
<Parameter name="kth" value="1500"/>
|
||||
<Parameter name="sth" value="0.7"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="100000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
<Parameter name="vol1" value="0"/>
|
||||
<Parameter name="vol2" value="0"/>
|
||||
<Parameter name="vol3" value="0"/>
|
||||
<Parameter name="vol4" value="0"/>
|
||||
<Parameter name="dvol1" value="0"/>
|
||||
<Parameter name="dvol2" value="0"/>
|
||||
<Parameter name="dvol3" value="0"/>
|
||||
<Parameter name="dvol4" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnpl01_6" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_7" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_8" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_9" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_mecmas21_2" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="50"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="-1"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0.8"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="4"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_f000_1" type="amesim_f000" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_f000_2" type="amesim_f000" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_lstp00a_1" type="amesim_lstp00a" modelVersion="0.2.0">
|
||||
<Parameter name="na" value="10"/>
|
||||
<Parameter name="gap0" value="0"/>
|
||||
<Parameter name="kcont" value="100000000000"/>
|
||||
<Parameter name="G" value="85700000000"/>
|
||||
<Parameter name="sdiam" value="0.02"/>
|
||||
<Parameter name="wdiam" value="0.002"/>
|
||||
<Parameter name="rcont" value="100000000000"/>
|
||||
<Parameter name="Pdis" value="1e-7"/>
|
||||
<Parameter name="stiffmode" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_forc_2" type="amesim_forc" modelVersion="0.2.0">
|
||||
<Parameter name="direction" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_ud00_2" type="amesim_ud00" modelVersion="0.2.0">
|
||||
<Parameter name="tstart" value="0"/>
|
||||
<Parameter name="start1" value="1000000000000"/>
|
||||
<Parameter name="end1" value="1000000000000"/>
|
||||
<Parameter name="t1" value="0.8"/>
|
||||
<Parameter name="start2" value="0"/>
|
||||
<Parameter name="end2" value="0"/>
|
||||
<Parameter name="t2" value="10"/>
|
||||
<Parameter name="start3" value="1"/>
|
||||
<Parameter name="end3" value="1"/>
|
||||
<Parameter name="t3" value="0"/>
|
||||
<Parameter name="start4" value="1"/>
|
||||
<Parameter name="end4" value="1"/>
|
||||
<Parameter name="t4" value="0"/>
|
||||
<Parameter name="start5" value="1"/>
|
||||
<Parameter name="end5" value="1"/>
|
||||
<Parameter name="t5" value="0"/>
|
||||
<Parameter name="start6" value="1"/>
|
||||
<Parameter name="end6" value="1"/>
|
||||
<Parameter name="t6" value="0"/>
|
||||
<Parameter name="start7" value="1"/>
|
||||
<Parameter name="end7" value="1"/>
|
||||
<Parameter name="t7" value="0"/>
|
||||
<Parameter name="start8" value="1"/>
|
||||
<Parameter name="end8" value="1"/>
|
||||
<Parameter name="t8" value="0"/>
|
||||
<Parameter name="nstages" value="2"/>
|
||||
<Parameter name="iscyclic" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_mecmas21_5" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="170000"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="0"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0.37"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_mecmas21_7" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="90000"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="-0.72"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
</Components>
|
||||
<Connections>
|
||||
<Connection id="edge-amesim_pnch023_1-port_2-amesim_pnvo001_1-port_2-1786524999267">
|
||||
<Endpoint component="amesim_pnch023_1" port="port_2"/>
|
||||
<Endpoint component="amesim_pnvo001_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_pnvo001_1-port_3-amesim_pnch012_1-port_1-1786525009973">
|
||||
<Endpoint component="amesim_pnvo001_1" port="port_3"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_2-port_1-amesim_pnch012_1-port_2-1786525035706-0">
|
||||
<Endpoint component="amesim_pnpl01_2" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_3-port_1-amesim_pnch012_1-port_3-1786525054054-0">
|
||||
<Endpoint component="amesim_pnpl01_3" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_4-port_1-amesim_pnch012_1-port_4-1786525061349-0">
|
||||
<Endpoint component="amesim_pnpl01_4" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_4"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_step0_1-out-amesim_pnvo001_1-res-1786525074494">
|
||||
<Endpoint component="amesim_step0_1" port="out"/>
|
||||
<Endpoint component="amesim_pnvo001_1" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_ud00_1-out-amesim_forc_1-res-1786525088412">
|
||||
<Endpoint component="amesim_ud00_1" port="out"/>
|
||||
<Endpoint component="amesim_forc_1" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_6-port_1-amesim_pnch023_1-port_1-1786525164428-0">
|
||||
<Endpoint component="amesim_pnpl01_6" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch023_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_7-port_1-amesim_pnch012_2-port_1-1786525181969-0">
|
||||
<Endpoint component="amesim_pnpl01_7" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_8-port_1-amesim_pnch012_2-port_4-1786525185493-0">
|
||||
<Endpoint component="amesim_pnpl01_8" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_4"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_9-port_1-amesim_pnch012_2-port_2-1786525188482-0">
|
||||
<Endpoint component="amesim_pnpl01_9" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_f000_1-port_1-amesim_mecmas21_2-port_2-1786525202665-0">
|
||||
<Endpoint component="amesim_f000_1" port="port_1"/>
|
||||
<Endpoint component="amesim_mecmas21_2" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_2-port_1-amesim_pnrp17_1-port_2-1786525203778">
|
||||
<Endpoint component="amesim_mecmas21_2" port="port_1"/>
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_pnrp17_1-port_5-amesim_lstp00a_1-port_1-1786525213548">
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_5"/>
|
||||
<Endpoint component="amesim_lstp00a_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_ud00_2-out-amesim_forc_2-res-1786525226761">
|
||||
<Endpoint component="amesim_ud00_2" port="out"/>
|
||||
<Endpoint component="amesim_forc_2" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnrp17_1-port_4-amesim_f000_2-port_1-1786525729832-0">
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_4"/>
|
||||
<Endpoint component="amesim_f000_2" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnrp17_1-port_1-amesim_pnch012_2-port_3-1786525729832-1">
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_forc_1-port_2-amesim_mecmas21_7-port_2-1786525915163">
|
||||
<Endpoint component="amesim_forc_1" port="port_2"/>
|
||||
<Endpoint component="amesim_mecmas21_7" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_7-port_1-amesim_pnrp17_1-port_3-1786525916652">
|
||||
<Endpoint component="amesim_mecmas21_7" port="port_1"/>
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_5-port_1-amesim_forc_2-port_2-1786525922010">
|
||||
<Endpoint component="amesim_mecmas21_5" port="port_1"/>
|
||||
<Endpoint component="amesim_forc_2" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_lstp00a_1-port_2-amesim_mecmas21_5-port_2-1786525924224">
|
||||
<Endpoint component="amesim_lstp00a_1" port="port_2"/>
|
||||
<Endpoint component="amesim_mecmas21_5" port="port_2"/>
|
||||
</Connection>
|
||||
</Connections>
|
||||
</System>
|
||||
@@ -1,325 +0,0 @@
|
||||
<?xml version="1.0" encoding="UTF-8"?>
|
||||
<System name="skill-test" schemaVersion="3" unitSystem="SI">
|
||||
<Simulation tStart="0" tStop="10" sampleStep="0.02" maxStep="0.001" method="RK45"/>
|
||||
<Components>
|
||||
<Component id="amesim_pnch023_1" type="amesim_pnch023" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol" value="0.057"/>
|
||||
<Parameter name="kth" value="0"/>
|
||||
<Parameter name="sth" value="0.1"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="15300000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnvo001_1" type="amesim_pnvo001" modelVersion="0.2.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cq" value="0.45"/>
|
||||
<Parameter name="area0" value="0.0000785"/>
|
||||
<Parameter name="Cv" value="0.5"/>
|
||||
<Parameter name="Kv" value="0.4"/>
|
||||
<Parameter name="flowset" value="1"/>
|
||||
<Parameter name="opening0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_step0_1" type="amesim_step0" modelVersion="0.1.0">
|
||||
<Parameter name="initial" value="0"/>
|
||||
<Parameter name="final" value="1"/>
|
||||
<Parameter name="time" value="0.04"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnch012_1" type="amesim_pnch012" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol0" value="0.015"/>
|
||||
<Parameter name="kth" value="1500"/>
|
||||
<Parameter name="sth" value="0.7"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="100000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
<Parameter name="vol1" value="0"/>
|
||||
<Parameter name="vol2" value="0"/>
|
||||
<Parameter name="vol3" value="0"/>
|
||||
<Parameter name="vol4" value="0"/>
|
||||
<Parameter name="dvol1" value="0"/>
|
||||
<Parameter name="dvol2" value="0"/>
|
||||
<Parameter name="dvol3" value="0"/>
|
||||
<Parameter name="dvol4" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnpl01_2" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_3" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_4" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_ud00_1" type="amesim_ud00" modelVersion="0.2.0">
|
||||
<Parameter name="tstart" value="0"/>
|
||||
<Parameter name="start1" value="100000000000000000"/>
|
||||
<Parameter name="end1" value="100000000000000000"/>
|
||||
<Parameter name="t1" value="0.8"/>
|
||||
<Parameter name="start2" value="49000"/>
|
||||
<Parameter name="end2" value="49000"/>
|
||||
<Parameter name="t2" value="10"/>
|
||||
<Parameter name="start3" value="1"/>
|
||||
<Parameter name="end3" value="1"/>
|
||||
<Parameter name="t3" value="0"/>
|
||||
<Parameter name="start4" value="1"/>
|
||||
<Parameter name="end4" value="1"/>
|
||||
<Parameter name="t4" value="0"/>
|
||||
<Parameter name="start5" value="1"/>
|
||||
<Parameter name="end5" value="1"/>
|
||||
<Parameter name="t5" value="0"/>
|
||||
<Parameter name="start6" value="1"/>
|
||||
<Parameter name="end6" value="1"/>
|
||||
<Parameter name="t6" value="0"/>
|
||||
<Parameter name="start7" value="1"/>
|
||||
<Parameter name="end7" value="1"/>
|
||||
<Parameter name="t7" value="0"/>
|
||||
<Parameter name="start8" value="1"/>
|
||||
<Parameter name="end8" value="1"/>
|
||||
<Parameter name="t8" value="0"/>
|
||||
<Parameter name="nstages" value="2"/>
|
||||
<Parameter name="iscyclic" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_forc_1" type="amesim_forc" modelVersion="0.2.0">
|
||||
<Parameter name="direction" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnrp17_1" type="amesim_pnrp17" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="dp" value="0.2"/>
|
||||
<Parameter name="dr" value="0.001"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_helium_medium_1" type="amesim_helium_medium" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="property_model" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnch012_2" type="amesim_pnch012" modelVersion="0.1.0">
|
||||
<Parameter name="gi" value="1"/>
|
||||
<Parameter name="cvol0" value="0.015"/>
|
||||
<Parameter name="kth" value="1500"/>
|
||||
<Parameter name="sth" value="0.7"/>
|
||||
<Parameter name="extemp" value="293.15"/>
|
||||
<Parameter name="p0" value="100000"/>
|
||||
<Parameter name="T0" value="293.15"/>
|
||||
<Parameter name="vol1" value="0"/>
|
||||
<Parameter name="vol2" value="0"/>
|
||||
<Parameter name="vol3" value="0"/>
|
||||
<Parameter name="vol4" value="0"/>
|
||||
<Parameter name="dvol1" value="0"/>
|
||||
<Parameter name="dvol2" value="0"/>
|
||||
<Parameter name="dvol3" value="0"/>
|
||||
<Parameter name="dvol4" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_pnpl01_6" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_7" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_8" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_pnpl01_9" type="amesim_pnpl01" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_mecmas21_2" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="50"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="-1"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0.8"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="4"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_f000_1" type="amesim_f000" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_f000_2" type="amesim_f000" modelVersion="0.1.0"/>
|
||||
<Component id="amesim_lstp00a_1" type="amesim_lstp00a" modelVersion="0.2.0">
|
||||
<Parameter name="na" value="10"/>
|
||||
<Parameter name="gap0" value="0"/>
|
||||
<Parameter name="kcont" value="100000000000"/>
|
||||
<Parameter name="G" value="85700000000"/>
|
||||
<Parameter name="sdiam" value="0.02"/>
|
||||
<Parameter name="wdiam" value="0.002"/>
|
||||
<Parameter name="rcont" value="100000000000"/>
|
||||
<Parameter name="Pdis" value="1e-7"/>
|
||||
<Parameter name="stiffmode" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_forc_2" type="amesim_forc" modelVersion="0.2.0">
|
||||
<Parameter name="direction" value="1"/>
|
||||
</Component>
|
||||
<Component id="amesim_ud00_2" type="amesim_ud00" modelVersion="0.2.0">
|
||||
<Parameter name="tstart" value="0"/>
|
||||
<Parameter name="start1" value="1000000000000"/>
|
||||
<Parameter name="end1" value="1000000000000"/>
|
||||
<Parameter name="t1" value="0.8"/>
|
||||
<Parameter name="start2" value="0"/>
|
||||
<Parameter name="end2" value="0"/>
|
||||
<Parameter name="t2" value="10"/>
|
||||
<Parameter name="start3" value="1"/>
|
||||
<Parameter name="end3" value="1"/>
|
||||
<Parameter name="t3" value="0"/>
|
||||
<Parameter name="start4" value="1"/>
|
||||
<Parameter name="end4" value="1"/>
|
||||
<Parameter name="t4" value="0"/>
|
||||
<Parameter name="start5" value="1"/>
|
||||
<Parameter name="end5" value="1"/>
|
||||
<Parameter name="t5" value="0"/>
|
||||
<Parameter name="start6" value="1"/>
|
||||
<Parameter name="end6" value="1"/>
|
||||
<Parameter name="t6" value="0"/>
|
||||
<Parameter name="start7" value="1"/>
|
||||
<Parameter name="end7" value="1"/>
|
||||
<Parameter name="t7" value="0"/>
|
||||
<Parameter name="start8" value="1"/>
|
||||
<Parameter name="end8" value="1"/>
|
||||
<Parameter name="t8" value="0"/>
|
||||
<Parameter name="nstages" value="2"/>
|
||||
<Parameter name="iscyclic" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_mecmas21_5" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="170000"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="0"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0.37"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
<Component id="amesim_mecmas21_7" type="amesim_mecmas21" modelVersion="0.2.0">
|
||||
<Parameter name="mass" value="90000"/>
|
||||
<Parameter name="fstick" value="0"/>
|
||||
<Parameter name="fcoul" value="0"/>
|
||||
<Parameter name="rvisc" value="0"/>
|
||||
<Parameter name="wind" value="0"/>
|
||||
<Parameter name="dvel" value="0.000001"/>
|
||||
<Parameter name="restdvel" value="0.000001"/>
|
||||
<Parameter name="restcoeff" value="0.65"/>
|
||||
<Parameter name="astrib" value="0.001"/>
|
||||
<Parameter name="xmin" value="-0.72"/>
|
||||
<Parameter name="Kbmin" value="1000000000"/>
|
||||
<Parameter name="Dbmin" value="10000"/>
|
||||
<Parameter name="Pdmin" value="0.0001"/>
|
||||
<Parameter name="xmax" value="0"/>
|
||||
<Parameter name="Kbmax" value="1000000000"/>
|
||||
<Parameter name="Dbmax" value="10000"/>
|
||||
<Parameter name="Pdmax" value="0.0001"/>
|
||||
<Parameter name="theta" value="0"/>
|
||||
<Parameter name="useFriction" value="1"/>
|
||||
<Parameter name="stoptype" value="1"/>
|
||||
<Parameter name="discContactOption" value="1"/>
|
||||
<Parameter name="strib" value="1"/>
|
||||
<Parameter name="frictionType" value="1"/>
|
||||
<Parameter name="v0" value="0"/>
|
||||
<Parameter name="x0" value="0"/>
|
||||
</Component>
|
||||
</Components>
|
||||
<Connections>
|
||||
<Connection id="edge-amesim_pnch023_1-port_2-amesim_pnvo001_1-port_2-1786524999267">
|
||||
<Endpoint component="amesim_pnch023_1" port="port_2"/>
|
||||
<Endpoint component="amesim_pnvo001_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_pnvo001_1-port_3-amesim_pnch012_1-port_1-1786525009973">
|
||||
<Endpoint component="amesim_pnvo001_1" port="port_3"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_2-port_1-amesim_pnch012_1-port_2-1786525035706-0">
|
||||
<Endpoint component="amesim_pnpl01_2" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_3-port_1-amesim_pnch012_1-port_3-1786525054054-0">
|
||||
<Endpoint component="amesim_pnpl01_3" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_4-port_1-amesim_pnch012_1-port_4-1786525061349-0">
|
||||
<Endpoint component="amesim_pnpl01_4" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_1" port="port_4"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_step0_1-out-amesim_pnvo001_1-res-1786525074494">
|
||||
<Endpoint component="amesim_step0_1" port="out"/>
|
||||
<Endpoint component="amesim_pnvo001_1" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_ud00_1-out-amesim_forc_1-res-1786525088412">
|
||||
<Endpoint component="amesim_ud00_1" port="out"/>
|
||||
<Endpoint component="amesim_forc_1" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_6-port_1-amesim_pnch023_1-port_1-1786525164428-0">
|
||||
<Endpoint component="amesim_pnpl01_6" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch023_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_7-port_1-amesim_pnch012_2-port_1-1786525181969-0">
|
||||
<Endpoint component="amesim_pnpl01_7" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_8-port_1-amesim_pnch012_2-port_4-1786525185493-0">
|
||||
<Endpoint component="amesim_pnpl01_8" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_4"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnpl01_9-port_1-amesim_pnch012_2-port_2-1786525188482-0">
|
||||
<Endpoint component="amesim_pnpl01_9" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_2-port_1-amesim_pnrp17_1-port_2-1786525203778">
|
||||
<Endpoint component="amesim_mecmas21_2" port="port_1"/>
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_pnrp17_1-port_5-amesim_lstp00a_1-port_1-1786525213548">
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_5"/>
|
||||
<Endpoint component="amesim_lstp00a_1" port="port_1"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_ud00_2-out-amesim_forc_2-res-1786525226761">
|
||||
<Endpoint component="amesim_ud00_2" port="out"/>
|
||||
<Endpoint component="amesim_forc_2" port="res"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_pnrp17_1-port_1-amesim_pnch012_2-port_3-1786525729832-1">
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_1"/>
|
||||
<Endpoint component="amesim_pnch012_2" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_forc_1-port_2-amesim_mecmas21_7-port_2-1786525915163">
|
||||
<Endpoint component="amesim_forc_1" port="port_2"/>
|
||||
<Endpoint component="amesim_mecmas21_7" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_7-port_1-amesim_pnrp17_1-port_3-1786525916652">
|
||||
<Endpoint component="amesim_mecmas21_7" port="port_1"/>
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_3"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_mecmas21_5-port_1-amesim_forc_2-port_2-1786525922010">
|
||||
<Endpoint component="amesim_mecmas21_5" port="port_1"/>
|
||||
<Endpoint component="amesim_forc_2" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-amesim_lstp00a_1-port_2-amesim_mecmas21_5-port_2-1786525924224">
|
||||
<Endpoint component="amesim_lstp00a_1" port="port_2"/>
|
||||
<Endpoint component="amesim_mecmas21_5" port="port_2"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_f000_2-port_1-amesim_pnrp17_1-port_4-1788429018340-0">
|
||||
<Endpoint component="amesim_f000_2" port="port_1"/>
|
||||
<Endpoint component="amesim_pnrp17_1" port="port_4"/>
|
||||
</Connection>
|
||||
<Connection id="edge-contact-amesim_f000_1-port_1-amesim_mecmas21_2-port_2-1788429022851-0">
|
||||
<Endpoint component="amesim_f000_1" port="port_1"/>
|
||||
<Endpoint component="amesim_mecmas21_2" port="port_2"/>
|
||||
</Connection>
|
||||
</Connections>
|
||||
</System>
|
||||
File diff suppressed because it is too large.
Load diff
File diff suppressed because it is too large.
Load diff
@@ -1,6 +1,6 @@
|
||||
{
|
||||
"projectSchemaVersion": 1,
|
||||
"name": "test-mql-8",
|
||||
"name": "test-mql-8-corrected",
|
||||
"nodes": [
|
||||
{
|
||||
"id": "pn_gas_data",
|
||||
@@ -2679,7 +2679,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2732,7 +2732,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2785,7 +2785,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2838,7 +2838,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2891,7 +2891,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2944,7 +2944,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -2997,7 +2997,7 @@
|
||||
"parameters": {},
|
||||
"parameterUnits": {},
|
||||
"parameterScientificNotation": {},
|
||||
"rotation": 0,
|
||||
"rotation": 180,
|
||||
"mirrored": false
|
||||
}
|
||||
},
|
||||
@@ -7368,7 +7368,7 @@
|
||||
}
|
||||
],
|
||||
"parameters": {
|
||||
"mass": 90000,
|
||||
"mass": 100.0,
|
||||
"fstick": 0,
|
||||
"fcoul": 0,
|
||||
"rvisc": 0,
|
||||
@@ -7377,17 +7377,17 @@
|
||||
"restdvel": 1e-06,
|
||||
"restcoeff": 0.65,
|
||||
"astrib": 0.001,
|
||||
"xmin": -0.72,
|
||||
"xmin": -1.0,
|
||||
"Kbmin": 1000000000,
|
||||
"Dbmin": 10000,
|
||||
"Pdmin": 0.0001,
|
||||
"xmax": 0,
|
||||
"xmax": 1.0,
|
||||
"Kbmax": 1000000000,
|
||||
"Dbmax": 10000,
|
||||
"Pdmax": 0.0001,
|
||||
"theta": 0,
|
||||
"useFriction": 1,
|
||||
"stoptype": 1,
|
||||
"stoptype": 4.0,
|
||||
"discContactOption": 1,
|
||||
"strib": 1,
|
||||
"frictionType": 1,
|
||||
@@ -8768,7 +8768,7 @@
|
||||
"source": "amesim_pnvo001_1",
|
||||
"target": "amesim_p4node2_1",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8778,7 +8778,7 @@
|
||||
"source": "amesim_pnvo001_2",
|
||||
"target": "amesim_p4node2_2",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8788,7 +8788,7 @@
|
||||
"source": "amesim_pnvo001_3",
|
||||
"target": "amesim_p4node2_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8798,7 +8798,7 @@
|
||||
"source": "amesim_pnvo001_4",
|
||||
"target": "amesim_p4node2_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8807,7 +8807,7 @@
|
||||
"id": "edge-amesim_p4node2_2-port_4-amesim_pnl0002_2-port_1-1786949195556",
|
||||
"source": "amesim_p4node2_2",
|
||||
"target": "amesim_pnl0002_2",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8818,7 +8818,7 @@
|
||||
"source": "amesim_pnl0002_2",
|
||||
"target": "amesim_p4node2_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8828,26 +8828,26 @@
|
||||
"source": "amesim_pnl0002_3",
|
||||
"target": "amesim_p4node2_3",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_4",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-contact-amesim_p4node2_4-port_1-amesim_pnl0002_3-port_2-1786949205596-0",
|
||||
"source": "amesim_p4node2_4",
|
||||
"target": "amesim_pnl0002_3",
|
||||
"sourceHandle": "port_1",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-amesim_p4node2_4-port_4-amesim_pnl0002_4-port_1-1786949231675",
|
||||
"source": "amesim_p4node2_4",
|
||||
"target": "amesim_pnl0002_4",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8858,7 +8858,7 @@
|
||||
"source": "amesim_pnl0002_4",
|
||||
"target": "amesim_p4node2_5",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8867,20 +8867,20 @@
|
||||
"id": "edge-contact-amesim_p4node2_5-port_4-amesim_pnl0002_5-port_1-1786949246412-0",
|
||||
"source": "amesim_p4node2_5",
|
||||
"target": "amesim_pnl0002_5",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-contact-amesim_p4node2_6-port_1-amesim_pnl0002_5-port_2-1786949247647-0",
|
||||
"source": "amesim_p4node2_6",
|
||||
"target": "amesim_pnl0002_5",
|
||||
"sourceHandle": "port_1",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -8888,7 +8888,7 @@
|
||||
"source": "amesim_pnl0002_6",
|
||||
"target": "amesim_p4node2_6",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_4",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8898,7 +8898,7 @@
|
||||
"source": "amesim_pnl0002_6",
|
||||
"target": "amesim_p4node2_7",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -8908,26 +8908,26 @@
|
||||
"source": "amesim_pnl0002_7",
|
||||
"target": "amesim_p4node2_7",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_4",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-contact-amesim_p4node2_8-port_1-amesim_pnl0002_7-port_2-1786949266454-0",
|
||||
"source": "amesim_p4node2_8",
|
||||
"target": "amesim_pnl0002_7",
|
||||
"sourceHandle": "port_1",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-amesim_p4node2_2-port_3-amesim_pnl0001_14-port_2-1786949362056",
|
||||
"source": "amesim_p4node2_2",
|
||||
"target": "amesim_pnl0001_14",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8937,7 +8937,7 @@
|
||||
"id": "edge-amesim_p4node2_3-port_3-amesim_pnl0001_15-port_2-1786949364233",
|
||||
"source": "amesim_p4node2_3",
|
||||
"target": "amesim_pnl0001_15",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8947,7 +8947,7 @@
|
||||
"id": "edge-amesim_p4node2_4-port_3-amesim_pnl0001_16-port_2-1786949365198",
|
||||
"source": "amesim_p4node2_4",
|
||||
"target": "amesim_pnl0001_16",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8957,7 +8957,7 @@
|
||||
"id": "edge-amesim_p4node2_5-port_3-amesim_pnl0001_17-port_2-1786949374542",
|
||||
"source": "amesim_p4node2_5",
|
||||
"target": "amesim_pnl0001_17",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8967,7 +8967,7 @@
|
||||
"id": "edge-amesim_p4node2_6-port_3-amesim_pnl0001_18-port_2-1786949377180",
|
||||
"source": "amesim_p4node2_6",
|
||||
"target": "amesim_pnl0001_18",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8977,7 +8977,7 @@
|
||||
"id": "edge-amesim_p4node2_7-port_3-amesim_pnl0001_19-port_2-1786949380063",
|
||||
"source": "amesim_p4node2_7",
|
||||
"target": "amesim_pnl0001_19",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -8987,7 +8987,7 @@
|
||||
"id": "edge-amesim_p4node2_8-port_3-amesim_pnl0001_20-port_2-1786949381164",
|
||||
"source": "amesim_p4node2_8",
|
||||
"target": "amesim_pnl0001_20",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9018,9 +9018,9 @@
|
||||
"source": "amesim_pnpl01_2",
|
||||
"target": "amesim_pnch012_8",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9038,9 +9038,9 @@
|
||||
"source": "amesim_pnpl01_4",
|
||||
"target": "amesim_pnch012_9",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9068,9 +9068,9 @@
|
||||
"source": "amesim_pnpl01_6",
|
||||
"target": "amesim_pnch012_10",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9098,9 +9098,9 @@
|
||||
"source": "amesim_pnpl01_8",
|
||||
"target": "amesim_pnch012_11",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9128,9 +9128,9 @@
|
||||
"source": "amesim_pnpl01_10",
|
||||
"target": "amesim_pnch012_12",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9158,9 +9158,9 @@
|
||||
"source": "amesim_pnpl01_12",
|
||||
"target": "amesim_pnch012_13",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9188,9 +9188,9 @@
|
||||
"source": "amesim_pnpl01_14",
|
||||
"target": "amesim_pnch012_14",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9218,9 +9218,9 @@
|
||||
"source": "amesim_pnpl01_16",
|
||||
"target": "amesim_pnch012_15",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9237,7 +9237,7 @@
|
||||
"id": "edge-amesim_pnch012_15-port_2-amesim_pnrp17_1-port_1-1786949561970",
|
||||
"source": "amesim_pnch012_15",
|
||||
"target": "amesim_pnrp17_1",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9247,7 +9247,7 @@
|
||||
"id": "edge-amesim_pnch012_14-port_2-amesim_pnrp17_2-port_1-1786949570722",
|
||||
"source": "amesim_pnch012_14",
|
||||
"target": "amesim_pnrp17_2",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9257,7 +9257,7 @@
|
||||
"id": "edge-amesim_pnch012_13-port_2-amesim_pnrp17_3-port_1-1786949575918",
|
||||
"source": "amesim_pnch012_13",
|
||||
"target": "amesim_pnrp17_3",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9267,7 +9267,7 @@
|
||||
"id": "edge-amesim_pnch012_12-port_2-amesim_pnrp17_4-port_1-1786949579000",
|
||||
"source": "amesim_pnch012_12",
|
||||
"target": "amesim_pnrp17_4",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9277,7 +9277,7 @@
|
||||
"id": "edge-amesim_pnch012_11-port_2-amesim_pnrp17_5-port_1-1786949583304",
|
||||
"source": "amesim_pnch012_11",
|
||||
"target": "amesim_pnrp17_5",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9287,7 +9287,7 @@
|
||||
"id": "edge-amesim_pnch012_10-port_2-amesim_pnrp17_6-port_1-1786949586596",
|
||||
"source": "amesim_pnch012_10",
|
||||
"target": "amesim_pnrp17_6",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9297,7 +9297,7 @@
|
||||
"id": "edge-amesim_pnch012_9-port_2-amesim_pnrp17_7-port_1-1786949589317",
|
||||
"source": "amesim_pnch012_9",
|
||||
"target": "amesim_pnrp17_7",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9307,7 +9307,7 @@
|
||||
"id": "edge-amesim_pnch012_8-port_2-amesim_pnrp17_8-port_1-1786949590677",
|
||||
"source": "amesim_pnch012_8",
|
||||
"target": "amesim_pnrp17_8",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9667,7 +9667,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_1-amesim_pnrp17_1-port_3-1786949849269",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_1",
|
||||
"sourceHandle": "port_1",
|
||||
"sourceHandle": "port_8",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9677,7 +9677,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_2-amesim_pnrp17_2-port_3-1786949850839",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_2",
|
||||
"sourceHandle": "port_2",
|
||||
"sourceHandle": "port_7",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9687,7 +9687,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_3-amesim_pnrp17_3-port_3-1786949852383",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_3",
|
||||
"sourceHandle": "port_3",
|
||||
"sourceHandle": "port_6",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9697,7 +9697,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_4-amesim_pnrp17_4-port_3-1786949854874",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_4",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_5",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9707,7 +9707,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_5-amesim_pnrp17_5-port_3-1786949858405",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_5",
|
||||
"sourceHandle": "port_5",
|
||||
"sourceHandle": "port_4",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9717,7 +9717,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_6-amesim_pnrp17_6-port_3-1786949862365",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_6",
|
||||
"sourceHandle": "port_6",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9727,7 +9727,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_7-amesim_pnrp17_7-port_3-1786949896879",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_7",
|
||||
"sourceHandle": "port_7",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9737,7 +9737,7 @@
|
||||
"id": "edge-amesim_lmechn1_3-port_8-amesim_pnrp17_8-port_3-1786949898922",
|
||||
"source": "amesim_lmechn1_3",
|
||||
"target": "amesim_pnrp17_8",
|
||||
"sourceHandle": "port_8",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
@@ -9778,7 +9778,7 @@
|
||||
"source": "amesim_lstp00a_1",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_8",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9788,7 +9788,7 @@
|
||||
"source": "amesim_lstp00a_2",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_7",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9798,7 +9798,7 @@
|
||||
"source": "amesim_lstp00a_3",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_6",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9808,7 +9808,7 @@
|
||||
"source": "amesim_lstp00a_4",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_5",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9818,7 +9818,7 @@
|
||||
"source": "amesim_lstp00a_5",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"targetHandle": "port_5",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9828,7 +9828,7 @@
|
||||
"source": "amesim_lstp00a_6",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_3",
|
||||
"targetHandle": "port_6",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9838,7 +9838,7 @@
|
||||
"source": "amesim_lstp00a_7",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_7",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9848,7 +9848,7 @@
|
||||
"source": "amesim_lstp00a_8",
|
||||
"target": "amesim_lmechn1_4",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_1",
|
||||
"targetHandle": "port_8",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -9978,9 +9978,9 @@
|
||||
"source": "amesim_pnl0002_1",
|
||||
"target": "amesim_p4node2_2",
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_1",
|
||||
"targetHandle": "port_3",
|
||||
"data": {
|
||||
"isContactEdge": true
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -9997,20 +9997,10 @@
|
||||
"id": "edge-amesim_p4node2_1-port_4-amesim_pnl0002_8-port_2-1786972824427",
|
||||
"source": "amesim_p4node2_1",
|
||||
"target": "amesim_pnl0002_8",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_3",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": 19.87945415380198,
|
||||
"y": 52.17994257325029
|
||||
},
|
||||
{
|
||||
"x": 199.87521088533356,
|
||||
"y": 52.17994257325029
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -10020,37 +10010,17 @@
|
||||
"sourceHandle": "port_2",
|
||||
"targetHandle": "port_2",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": 80.32926682952949,
|
||||
"y": 139.08364630171945
|
||||
},
|
||||
{
|
||||
"x": 80.32926682952949,
|
||||
"y": 181.8752425865067
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
"id": "edge-amesim_p4node2_8-port_4-amesim_pnl0002_8-port_1-1786972860850",
|
||||
"source": "amesim_p4node2_8",
|
||||
"target": "amesim_pnl0002_8",
|
||||
"sourceHandle": "port_4",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_1",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": 21.87942245262885,
|
||||
"y": 1602.5991575147043
|
||||
},
|
||||
{
|
||||
"x": 199.87521088533356,
|
||||
"y": 1602.5991575147043
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -10058,7 +10028,7 @@
|
||||
"source": "amesim_pnl0001_21",
|
||||
"target": "amesim_p4node2_5",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false
|
||||
}
|
||||
@@ -10098,19 +10068,9 @@
|
||||
"source": "amesim_pnl0001_27",
|
||||
"target": "amesim_p4node2_8",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": -8.800000000000004,
|
||||
"y": 1512
|
||||
},
|
||||
{
|
||||
"x": -8.800000000000004,
|
||||
"y": 1449.5999999999997
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -10138,19 +10098,9 @@
|
||||
"source": "amesim_pnl0001_26",
|
||||
"target": "amesim_p4node2_7",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": -8.800000000000004,
|
||||
"y": 1350
|
||||
},
|
||||
{
|
||||
"x": -8.800000000000004,
|
||||
"y": 1344
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
},
|
||||
{
|
||||
@@ -10178,27 +10128,17 @@
|
||||
"source": "amesim_pnl0001_25",
|
||||
"target": "amesim_p4node2_6",
|
||||
"sourceHandle": "port_1",
|
||||
"targetHandle": "port_2",
|
||||
"targetHandle": "port_4",
|
||||
"data": {
|
||||
"isContactEdge": false,
|
||||
"routePoints": [
|
||||
{
|
||||
"x": -9.800000000000004,
|
||||
"y": 1116
|
||||
},
|
||||
{
|
||||
"x": -9.800000000000004,
|
||||
"y": 1054.8
|
||||
}
|
||||
]
|
||||
"isContactEdge": false
|
||||
}
|
||||
}
|
||||
],
|
||||
"simulation": {
|
||||
"t_start": 0,
|
||||
"t_stop": 10,
|
||||
"t_start": 0.0,
|
||||
"t_stop": 10.0,
|
||||
"step": 0.01,
|
||||
"max_step": 0.02,
|
||||
"max_step": 1e+30,
|
||||
"method": "BDF"
|
||||
}
|
||||
}
|
||||
File diff suppressed because it is too large.
Load diff
@@ -0,0 +1,91 @@
|
||||
"""Compare identical native models with the old fixed-point, previous and current pipe solvers.
|
||||
|
||||
Run with Python 3.12 from the repository; generated programs/results stay in --output-dir.
|
||||
The baseline ref is an explicit Git revision, never a frozen numerical result substituted for execution.
|
||||
"""
|
||||
from __future__ import annotations
|
||||
import argparse
|
||||
from hashlib import sha256
|
||||
import json
|
||||
from pathlib import Path
|
||||
import statistics
|
||||
import subprocess
|
||||
import sys
|
||||
|
||||
ROOT = Path(__file__).resolve().parents[2]
|
||||
sys.path.insert(0, str(ROOT))
|
||||
from app.main import compile_system_xml_network
|
||||
from app.simulation.backends import simulation_config
|
||||
from app.simulation.native_codegen import build as builder
|
||||
from app.simulation.native_codegen.compiler import compile_native_program
|
||||
from app.simulation.native_codegen.input import load_input
|
||||
from app.simulation.native_codegen.runner import execute_native
|
||||
|
||||
OLD_ITERATION = '''double rough_limit=pipe_rough_limit(rr);
|
||||
double base=area*p*cm/sqrt(T),q=sqrt(d/(length*.02))*base;
|
||||
for(int i=0;i<(kind==0?64:16);i++) {
|
||||
double next=sqrt(d/(length*pipe_friction_prepared(4*fabs(q)/den,rr,rough_limit)))*base;
|
||||
if(fabs(next-q)<=fmax(1e-12,fabs(q)*1e-9)) return sign*next;
|
||||
q=.5*(q+next);
|
||||
}
|
||||
return sign*q;'''
|
||||
NEW_CALL = '''double base=area*p*cm/sqrt(T),K=pow(4*base/den,2)*d/length;
|
||||
return sign*native_pipe_resistance(K,rr,den/4,NULL)*den/4;'''
|
||||
|
||||
|
||||
def main():
|
||||
parser=argparse.ArgumentParser(description=__doc__)
|
||||
parser.add_argument('input',type=Path)
|
||||
parser.add_argument('--output-dir',type=Path,required=True)
|
||||
parser.add_argument('--baseline-ref',default='5d5a2e1')
|
||||
parser.add_argument('--runs',type=int,default=3)
|
||||
args=parser.parse_args()
|
||||
if args.runs<1:parser.error('--runs must be positive')
|
||||
out=args.output_dir.resolve();out.mkdir(parents=True,exist_ok=True)
|
||||
if (out/'summary.json').exists():parser.error('Choose a fresh output directory')
|
||||
revision=subprocess.check_output(['git','rev-parse',args.baseline_ref],cwd=ROOT,text=True).strip()
|
||||
xml,doc=load_input(args.input)
|
||||
program=compile_native_program(compile_system_xml_network(doc))
|
||||
config=simulation_config(doc.simulation)
|
||||
(out/'input.xml').write_bytes(xml)
|
||||
(out/('input'+args.input.suffix)).write_bytes(args.input.read_bytes())
|
||||
paths=subprocess.check_output(['git','ls-tree','-r','--name-only',revision,'native'],cwd=ROOT,text=True).splitlines()
|
||||
variants={}
|
||||
original_native=builder.NATIVE
|
||||
try:
|
||||
for variant in ('fixed-point','previous-newton','guarded-newton'):
|
||||
directory=out/variant
|
||||
for name in paths:
|
||||
if variant=='guarded-newton':data=(ROOT/name).read_bytes()
|
||||
else:data=subprocess.check_output(['git','show',f'{revision}:{name}'],cwd=ROOT)
|
||||
target=directory/name;target.parent.mkdir(parents=True,exist_ok=True);target.write_bytes(data)
|
||||
if variant=='fixed-point':
|
||||
target=directory/'native/components/kernels.c';source=target.read_text()
|
||||
if source.count(NEW_CALL)!=1:raise ValueError('Baseline pipe flow layout does not match the audited fixed-point substitution')
|
||||
target.write_text(source.replace(NEW_CALL,OLD_ITERATION))
|
||||
builder.NATIVE=directory/'native'
|
||||
variants[variant]=builder.build_native(program,cache_dir=out/'cache')
|
||||
finally:builder.NATIVE=original_native
|
||||
rows=[]
|
||||
for index in range(args.runs+1):
|
||||
order=list(variants)
|
||||
if index%2:order.reverse()
|
||||
for variant in order:
|
||||
data=execute_native(variants[variant],config,doc.simulation.sample_step,
|
||||
run_dir=out/variant/('warmup' if index==0 else f'run-{index}'),timeout=120)
|
||||
row={key:value for key,value in data.items() if key not in ('series','final','finalState')}
|
||||
row.update(variant=variant,run=index)
|
||||
rows.append(row);print(json.dumps(row,ensure_ascii=False),flush=True)
|
||||
if not data['success']:raise RuntimeError(f'{variant} did not complete: {data["message"]}')
|
||||
summary={'baselineRef':revision,'input':str(args.input.resolve()),
|
||||
'inputSha256':sha256(args.input.read_bytes()).hexdigest(),'xmlSha256':sha256(xml).hexdigest(),
|
||||
'settings':vars(config),'sampleStep':doc.simulation.sample_step,'rows':rows,
|
||||
'variants':{name:{'sourceSha256':sha256((out/name/'native/components/kernels.c').read_bytes()).hexdigest(),
|
||||
'buildKey':build.manifest['buildKey'],
|
||||
'medianSolveSeconds':statistics.median(row['solveSeconds'] for row in rows if row['variant']==name and row['run']>0),
|
||||
'medianProcessSeconds':statistics.median(row['processWallSeconds'] for row in rows if row['variant']==name and row['run']>0)}
|
||||
for name,build in variants.items()}}
|
||||
(out/'summary.json').write_text(json.dumps(summary,ensure_ascii=False,indent=2)+'\n')
|
||||
print(json.dumps(summary['variants'],ensure_ascii=False,indent=2))
|
||||
|
||||
if __name__=='__main__':main()
|
||||
@@ -0,0 +1,89 @@
|
||||
// Real browser/HTTP/native execution. No API routes or result data are mocked.
|
||||
import { chromium } from '../../frontend/node_modules/playwright/index.mjs';
|
||||
import fs from 'node:fs/promises';
|
||||
import path from 'node:path';
|
||||
import { performance } from 'node:perf_hooks';
|
||||
import assert from 'node:assert/strict';
|
||||
import { createHash } from 'node:crypto';
|
||||
const [input, output, baseURL = 'http://127.0.0.1:8011', runCount = '3'] = process.argv.slice(2);
|
||||
if (!input || !output) throw new Error('Usage: node browser_native_simulation.mjs MODEL.json OUTPUT_DIR [URL] [RUNS]');
|
||||
await fs.mkdir(output, { recursive: true });
|
||||
const inputText = await fs.readFile(input, 'utf8');
|
||||
const project = JSON.parse(inputText);
|
||||
const curveNodeId = project.nodes.find(node => node.id === 'amesim_pnl0002_10')?.id
|
||||
?? project.nodes.find(node => node.data.modelType === 'amesim_pnl0002')?.id;
|
||||
if (!curveNodeId) throw new Error('Curve verification requires a PNL0002 component.');
|
||||
await fs.writeFile(path.join(output, 'input.json'), inputText);
|
||||
const browser = await chromium.launch({ headless: true });
|
||||
const context = await browser.newContext({ viewport: { width: 1600, height: 1000 }, acceptDownloads: true });
|
||||
const page = await context.newPage();
|
||||
page.setDefaultTimeout(30000);
|
||||
const errors = [];
|
||||
page.on('pageerror', error => errors.push(String(error)));
|
||||
const rows = [];
|
||||
try {
|
||||
await page.goto(baseURL);
|
||||
await page.locator('input[type="file"][accept*=".json"]').setInputFiles(path.resolve(input));
|
||||
await page.getByRole('textbox', { name: '工程', exact: true }).waitFor();
|
||||
await page.waitForFunction(name => document.querySelector('input[aria-label="工程"]')?.value === name || [...document.querySelectorAll('input')].some(input => input.value === name), path.basename(input, path.extname(input)));
|
||||
await page.screenshot({ path: path.join(output, 'model.png'), fullPage: true });
|
||||
for (let i = 0; i <= Number(runCount); i++) {
|
||||
const oldMarker = await page.evaluate(() => sessionStorage.getItem('system-simulation-flow:latest-result'));
|
||||
const responsePromise = page.waitForResponse(response => response.url().endsWith('/api/system-xml/simulate-stream'), { timeout: 180000 });
|
||||
const started = performance.now();
|
||||
await page.getByRole('button', { name: '运行仿真', exact: true }).click();
|
||||
const response = await responsePromise;
|
||||
await response.finished();
|
||||
if (!response.ok()) throw new Error(`Simulation HTTP ${response.status()}`);
|
||||
const receivedMs = performance.now() - started;
|
||||
await page.waitForFunction(old => {
|
||||
const marker = sessionStorage.getItem('system-simulation-flow:latest-result');
|
||||
return marker && marker !== old && JSON.parse(marker).storage === 'indexeddb';
|
||||
}, oldMarker, { timeout: 180000 });
|
||||
await page.getByRole('button', { name: '运行仿真', exact: true }).waitFor({ state: 'visible' });
|
||||
await page.waitForFunction(() => !document.querySelector('button[aria-label="运行仿真"]')?.disabled);
|
||||
await page.getByRole('tab', { name: /^结果/ }).click();
|
||||
await page.getByRole('button', { name: '下载结果文件', exact: true }).waitFor();
|
||||
const readyMs = performance.now() - started;
|
||||
await page.waitForFunction(old => {
|
||||
const marker = sessionStorage.getItem('system-simulation-flow:latest-result');
|
||||
return marker && marker !== old && JSON.parse(marker).storage === 'indexeddb';
|
||||
}, oldMarker);
|
||||
const downloadPromise = page.waitForEvent('download');
|
||||
await page.getByRole('button', { name: '下载结果文件', exact: true }).click();
|
||||
await (await downloadPromise).saveAs(path.join(output, `run-${i}.simresult`));
|
||||
const exported = JSON.parse(await fs.readFile(path.join(output, `run-${i}.simresult`), 'utf8'));
|
||||
const result = exported.snapshot.result;
|
||||
if (!result.success) throw new Error(result.message);
|
||||
assert.equal(result.diagnostics.integration.rtol, 1e-8);
|
||||
assert.equal(result.simulatedUntil, project.simulation.t_stop);
|
||||
const row = { run: i, receivedMs, readyMs, sampleCount: result.series.time.length,
|
||||
...result.diagnostics.native };
|
||||
rows.push(row);
|
||||
console.log(JSON.stringify(row));
|
||||
if (i < Number(runCount)) await page.getByRole('tab', { name: '建模', exact: true }).click();
|
||||
}
|
||||
await page.getByRole('button', { name: '适应系统图窗口', exact: true }).click();
|
||||
await page.locator(`.results-system-panel .react-flow__node[data-id=${JSON.stringify(curveNodeId)}]`).click();
|
||||
await page.locator('.results-variable-list button').filter({ has: page.locator('small', { hasText: /^K$/ }) }).first().click();
|
||||
await page.locator('.results-chart-panel .result-chart-window svg').first().waitFor();
|
||||
const csvDownload = page.waitForEvent('download');
|
||||
await page.getByRole('button', { name: '下载结果 CSV', exact: true }).click();
|
||||
await (await csvDownload).saveAs(path.join(output, 'result.csv'));
|
||||
await page.screenshot({ path: path.join(output, 'result.png'), fullPage: true });
|
||||
await page.reload();
|
||||
await page.getByRole('tab', { name: /^结果/ }).click();
|
||||
await page.getByRole('button', { name: '下载结果文件', exact: true }).waitFor();
|
||||
const restored = page.waitForEvent('download');
|
||||
await page.getByRole('button', { name: '下载结果文件', exact: true }).click();
|
||||
await (await restored).saveAs(path.join(output, 'restored.simresult'));
|
||||
const restoredData = JSON.parse(await fs.readFile(path.join(output, 'restored.simresult'), 'utf8'));
|
||||
const lastData = JSON.parse(await fs.readFile(path.join(output, `run-${runCount}.simresult`), 'utf8'));
|
||||
assert.deepEqual(restoredData.snapshot.result, lastData.snapshot.result);
|
||||
await fs.writeFile(path.join(output, 'summary.json'), JSON.stringify({ input: path.resolve(input), inputSha256: createHash('sha256').update(inputText).digest('hex'), baseURL, browser: browser.version(), rows, errors, restored: true, restoredResultIdentical: true, csvExported: true }, null, 2));
|
||||
if (errors.length) throw new Error(`Browser errors: ${errors.join('\n')}`);
|
||||
} catch (error) {
|
||||
await page.screenshot({ path: path.join(output, 'failure.png'), fullPage: true });
|
||||
await fs.writeFile(path.join(output, 'failure.txt'), `${error.stack}\nPage errors: ${JSON.stringify(errors)}\n${await page.locator('body').innerText()}`);
|
||||
throw error;
|
||||
} finally { await context.close(); await browser.close(); }
|
||||
@@ -0,0 +1,92 @@
|
||||
"""Compare real native/browser results to the frozen 72-curve Amesim reference.
|
||||
|
||||
Run with Python + NumPy. --plot additionally requires Matplotlib, available in
|
||||
this workstation's system Python. Outputs stay in the requested artifact folder.
|
||||
"""
|
||||
from __future__ import annotations
|
||||
import argparse
|
||||
import csv
|
||||
import hashlib
|
||||
import json
|
||||
from pathlib import Path
|
||||
import numpy as np
|
||||
|
||||
ROOT = Path(__file__).resolve().parents[2]
|
||||
LIMITS = {'pressure': 250., 'temperature': .015, 'displacement': 2e-6,
|
||||
'velocity': 1e-5, 'mass_flow': 3e-5}
|
||||
UNITS = {'pressure': 'Pa', 'temperature': 'K', 'displacement': 'm',
|
||||
'velocity': 'm/s', 'mass_flow': 'kg/s'}
|
||||
|
||||
|
||||
def main():
|
||||
parser = argparse.ArgumentParser(description=__doc__)
|
||||
parser.add_argument('result', type=Path)
|
||||
parser.add_argument('--reference', type=Path, default=ROOT/'tests/baselines/simulation/test_mql_4/test-mql-4-amesim-reference.json')
|
||||
parser.add_argument('--output-dir', type=Path, required=True)
|
||||
parser.add_argument('--plot', action='store_true')
|
||||
args = parser.parse_args()
|
||||
ref = json.loads(args.reference.read_text())
|
||||
data = json.loads(args.result.read_text())
|
||||
if 'snapshot' in data:
|
||||
data = data['snapshot']['result']
|
||||
series = data['series']; times = np.array(series['time']); ref_times = np.array(ref['times'])
|
||||
if not data['success'] or times[-1] < ref_times[-1] or times[0] > ref_times[0]:
|
||||
raise ValueError('A completed result covering all reference times is required.')
|
||||
if np.any(np.diff(times) < 0):
|
||||
raise ValueError('Native sample times are not ordered.')
|
||||
finite = all(np.all(np.isfinite(values)) for values in series.values())
|
||||
rows = []; grouped = {}
|
||||
for key, curve in ref['series'].items():
|
||||
actual = np.interp(ref_times, times, series[key]); error = actual - curve['values']
|
||||
worst = int(np.argmax(abs(error))); quantity = curve['quantity']
|
||||
row = {'key': key, 'quantity': quantity, 'unit': UNITS[quantity],
|
||||
'maxAbsoluteError': float(abs(error[worst])), 'rmsError': float(np.sqrt(np.mean(error**2))),
|
||||
'worstTime': float(ref_times[worst]), 'limit': LIMITS[quantity],
|
||||
'passed': bool(np.max(abs(error)) <= LIMITS[quantity])}
|
||||
rows.append(row)
|
||||
if quantity not in grouped or row['maxAbsoluteError'] > grouped[quantity]['maxAbsoluteError']:
|
||||
grouped[quantity] = row
|
||||
masses = np.array([v for k, v in series.items() if k.rsplit('.', 1)[-1] in ('m', 'm1', 'm2')])
|
||||
total = np.sum(masses, axis=0)
|
||||
mass_drift = float(np.max(abs(total-total[0])))
|
||||
force_peaks = sorted(({'key': k, 'peakAbsolute': max(map(abs, v))} for k, v in series.items()
|
||||
if k.startswith('amesim_lstp00a_') and k.endswith('.f')),
|
||||
key=lambda row: row['peakAbsolute'], reverse=True)
|
||||
summary = {'resultPath': str(args.result.resolve()),
|
||||
'resultSha256': hashlib.sha256(args.result.read_bytes()).hexdigest(),
|
||||
'referencePath': str(args.reference.resolve()),
|
||||
'referenceSha256': hashlib.sha256(args.reference.read_bytes()).hexdigest(),
|
||||
'referenceSource': ref['source'], 'freshAmesimRun': False,
|
||||
'referenceCurveCount': len(rows), 'referenceTimeCount': len(ref_times),
|
||||
'nativeSampleCount': len(times), 'allSamplesFinite': bool(finite),
|
||||
'massStateCount': len(masses), 'maxTotalMassDriftKg': mass_drift,
|
||||
'groupedWorstErrors': grouped, 'curves': rows, 'contactForcePeaksOutsideReferenceScope': force_peaks,
|
||||
'passed': bool(finite and mass_drift <= 1e-10 and all(row['passed'] for row in rows))}
|
||||
args.output_dir.mkdir(parents=True, exist_ok=True)
|
||||
(args.output_dir/'comparison.json').write_text(json.dumps(summary, ensure_ascii=False, indent=2)+'\n')
|
||||
with (args.output_dir/'curve-errors.csv').open('w', newline='') as output:
|
||||
writer = csv.DictWriter(output, fieldnames=list(rows[0])); writer.writeheader(); writer.writerows(rows)
|
||||
if args.plot:
|
||||
import matplotlib
|
||||
matplotlib.use('Agg')
|
||||
import matplotlib.pyplot as plt
|
||||
fig, axes = plt.subplots(5, 2, figsize=(13, 15), constrained_layout=True)
|
||||
for (quantity, row), (left, right) in zip(grouped.items(), axes):
|
||||
key = row['key']; values = ref['series'][key]['values']
|
||||
actual = np.interp(ref_times, times, series[key])
|
||||
left.plot(times, series[key], linewidth=1, label='Native, rtol=1e-8')
|
||||
left.plot(ref_times, values, '.', markersize=3, label='Saved Amesim reference')
|
||||
left.set_title(key, fontsize=9); left.set_ylabel(UNITS[quantity]); left.legend(fontsize=7)
|
||||
right.plot(ref_times, actual-values, '.-', linewidth=.8, markersize=3)
|
||||
right.axhline(row['limit'], color='gray', linestyle='--', linewidth=.6)
|
||||
right.axhline(-row['limit'], color='gray', linestyle='--', linewidth=.6)
|
||||
right.set_title(f'{quantity}: sampled difference and acceptance limits', fontsize=9)
|
||||
right.set_ylabel(UNITS[quantity])
|
||||
for ax in (left, right): ax.grid(alpha=.2); ax.set_xlabel('Time [s]')
|
||||
fig.suptitle('Four-branch model: 72 curves checked at 57 stored Amesim times\nWorst curve per quantity; contact force is outside this reference', fontsize=12)
|
||||
fig.savefig(args.output_dir/'comparison.svg'); fig.savefig(args.output_dir/'comparison.png', dpi=140)
|
||||
print(json.dumps({k: summary[k] for k in ('passed', 'nativeSampleCount', 'maxTotalMassDriftKg', 'groupedWorstErrors')}, indent=2))
|
||||
if not summary['passed']: raise SystemExit(1)
|
||||
|
||||
|
||||
if __name__ == '__main__': main()
|
||||
@@ -0,0 +1,403 @@
|
||||
"""Audit the AME diagram against the corrected XML; emit an aligned browser project.
|
||||
|
||||
Run from the repository root with .venv/bin/python. Does not run Amesim or use
|
||||
the stale eight-branch compiled/result cache inside the four-branch archive.
|
||||
"""
|
||||
from __future__ import annotations
|
||||
|
||||
import argparse
|
||||
from collections import Counter, defaultdict
|
||||
from copy import deepcopy
|
||||
import hashlib
|
||||
import json
|
||||
from pathlib import Path
|
||||
import re
|
||||
import sys
|
||||
if '--check' in sys.argv:
|
||||
sys.dont_write_bytecode = True
|
||||
import struct
|
||||
import tarfile
|
||||
import xml.etree.ElementTree as ET
|
||||
|
||||
ROOT = Path(__file__).resolve().parents[2]
|
||||
sys.path.insert(0, str(ROOT))
|
||||
from app.simulation.registry import get_component_model_spec
|
||||
from tests.test_test_mql_ame_contract import (
|
||||
_blocks, _required_element_text, _element_text, _resolve_globals,
|
||||
_public_model_type, _expected_parameters, _value_fields,
|
||||
)
|
||||
|
||||
OUT = ROOT / 'test/solver-newton-20260911/mql4'
|
||||
AME = ROOT / 'tests/data/test_mql_4.ame'
|
||||
XML = ROOT / 'tests/fixtures/amesim/test-mql-4-corrected.xml'
|
||||
REFERENCE = ROOT / 'tests/baselines/simulation/test_mql_4/test-mql-4-amesim-reference.json'
|
||||
PROJECT = ROOT / 'tests/data/test-mql-4-corrected.json'
|
||||
|
||||
|
||||
def sha(path):
|
||||
return hashlib.sha256(path.read_bytes()).hexdigest()
|
||||
|
||||
|
||||
def public_port(model, index):
|
||||
if index == 0 and model in {'amesim_pnvo001', 'amesim_forc'}:
|
||||
return 'res'
|
||||
if index == 0 and model in {'amesim_step0', 'amesim_ud00'}:
|
||||
return 'out'
|
||||
return f'port_{index + 1}'
|
||||
|
||||
|
||||
def parameter_key(values):
|
||||
return tuple(sorted((key, format(float(value), '.12g')) for key, value in values.items()))
|
||||
|
||||
|
||||
def audit_source():
|
||||
with tarfile.open(AME) as archive:
|
||||
def read(suffix):
|
||||
names = [name for name in archive.getnames() if name.endswith(suffix)]
|
||||
if len(names) != 1:
|
||||
raise ValueError((suffix, names))
|
||||
return archive.extractfile(names[0]).read().decode('latin1')
|
||||
cir = read('.cir')
|
||||
sim = read('.sim')
|
||||
modelinfo = read('.modelinfo')
|
||||
variables = read('.var')
|
||||
perf = read('.ameperf')
|
||||
result_name = next(name for name in archive.getnames() if name.endswith('.results'))
|
||||
result_data = archive.extractfile(result_name).read()
|
||||
result_points, result_columns = struct.unpack('<2i', result_data[:8])
|
||||
member_hashes = {}
|
||||
for suffix in ['.cir', '.sim', '.modelinfo', '.var', '.results']:
|
||||
name = next(name for name in archive.getnames() if name.endswith(suffix))
|
||||
data = archive.extractfile(name).read()
|
||||
member_hashes[name] = {'bytes': len(data), 'sha256': hashlib.sha256(data).hexdigest()}
|
||||
globals_ = _resolve_globals(cir)
|
||||
components = _blocks(cir, 'COMP')
|
||||
lines = _blocks(cir, 'LINE')
|
||||
nodes = {}
|
||||
for kind, entities in [('component', components), ('line', lines)]:
|
||||
for index, body in enumerate(entities):
|
||||
submodel = _required_element_text(body, 'SUB_NAME')
|
||||
if submodel == 'DIRECT':
|
||||
continue
|
||||
model = _public_model_type(submodel)
|
||||
nodes[f'{kind}:{index}'] = {
|
||||
'modelType': model,
|
||||
'alias': _required_element_text(body, 'ALIAS'),
|
||||
'parameters': _expected_parameters(body, model, globals_),
|
||||
'sourceValues': {name: {'expression': value.expression, 'unit': value.unit}
|
||||
for name, value in _value_fields(body).items()},
|
||||
'position': _element_text(body, 'COMP_POS') or _element_text(body, 'LINE_POINTS'),
|
||||
'geometry': _element_text(body, 'COMP_GEOMETRY'),
|
||||
'outputType': _element_text(body, 'OUTPUT_TYPE'),
|
||||
}
|
||||
edges = set()
|
||||
contacts = set()
|
||||
for index, body in enumerate(components):
|
||||
for port_index, port_body in enumerate(_blocks(body, 'COMP_PORT')):
|
||||
if _required_element_text(port_body, 'PORT_CONNECT') != '1':
|
||||
continue
|
||||
for connection in _blocks(port_body, 'CONNECT'):
|
||||
other = int(_required_element_text(connection, 'CONNECT_ENTITY_NUM'))
|
||||
other_port = int(_required_element_text(connection, 'CONNECT_ENTITY_PORT'))
|
||||
contacts.add(((index, port_index), (other, other_port)))
|
||||
assert all((b, a) in contacts for a, b in contacts)
|
||||
def endpoint(index, port):
|
||||
key = f'component:{index}'
|
||||
return key, public_port(nodes[key]['modelType'], port)
|
||||
for a, b in contacts:
|
||||
edges.add(tuple(sorted((endpoint(*a), endpoint(*b)))))
|
||||
for index, body in enumerate(lines):
|
||||
assert _required_element_text(body, 'LINE_START_TYPE') == '0'
|
||||
assert _required_element_text(body, 'LINE_END_TYPE') == '0'
|
||||
start = endpoint(int(_required_element_text(body, 'LINE_START_ENTITY')),
|
||||
int(_required_element_text(body, 'LINE_START_PORT')))
|
||||
end = endpoint(int(_required_element_text(body, 'LINE_END_ENTITY')),
|
||||
int(_required_element_text(body, 'LINE_END_PORT')))
|
||||
if _required_element_text(body, 'SUB_NAME') == 'DIRECT':
|
||||
edges.add(tuple(sorted((start, end))))
|
||||
else:
|
||||
key = f'line:{index}'
|
||||
output_type = _required_element_text(body, 'OUTPUT_TYPE')
|
||||
assert output_type in {'1', '2'}
|
||||
first, second = ('port_1', 'port_2') if output_type == '1' else ('port_2', 'port_1')
|
||||
edges.add(tuple(sorted((start, (key, first)))))
|
||||
edges.add(tuple(sorted((end, (key, second)))))
|
||||
count = Counter(node['modelType'] for node in nodes.values())
|
||||
states = sum(count[model] * size for model, size in {
|
||||
'amesim_pnch012': 2, 'amesim_pnch023': 2, 'amesim_pnl0001': 2,
|
||||
'amesim_pnl0002': 2, 'amesim_pnl0003': 4, 'amesim_mecmas21': 2,
|
||||
}.items())
|
||||
return nodes, sorted(edges), {
|
||||
'archiveSha256': sha(AME), 'archiveBytes': AME.stat().st_size,
|
||||
'members': member_hashes, 'globals': globals_,
|
||||
'componentCount': len(components), 'modeledLineCount': len(nodes) - len(components),
|
||||
'directLineCount': len(lines) - (len(nodes) - len(components)),
|
||||
'contactCount': len(contacts) // 2, 'publicNodeCount': len(nodes),
|
||||
'publicParameterCount': sum(len(node['parameters']) for node in nodes.values()),
|
||||
'connectionCount': len(edges), 'typeCounts': dict(count),
|
||||
'diagramDynamicStateCount': states,
|
||||
'simulationFileRaw': sim, 'savedSimulationNumericRows': [[float(x) for x in row.split()] for row in sim.splitlines()],
|
||||
'cachedModelInfo': modelinfo,
|
||||
'cachedResultsSuitableForFourBranchComparison': False,
|
||||
'cacheRejectionReason': 'Diagram has 64 states / four pistons; cached modelinfo has 132 states, .ameperf contains eight LSTP00A instances, and .results declares 1116 saved variables while the current .var has only 640 rows.',
|
||||
'cachedResultHeader': {'pointCount': result_points, 'savedVariableCount': abs(result_columns)},
|
||||
'variableRowCount': len(variables.splitlines()),
|
||||
'cachedPerformanceContactInstances': sorted(set(re.findall(r'LSTP00A-([0-9]+)', perf))),
|
||||
'cachedPistonAliases': sorted(set(re.findall(r'Data_Path=\S+@(pn_brp2[^\s]*)', variables))),
|
||||
}
|
||||
|
||||
|
||||
def xml_model(root=None):
|
||||
if root is None:
|
||||
root = ET.parse(XML).getroot()
|
||||
nodes = {item.attrib['id']: {
|
||||
'modelType': item.attrib['type'],
|
||||
'modelVersion': item.attrib['modelVersion'],
|
||||
'parameters': {p.attrib['name']: float(p.attrib['value']) for p in item.findall('Parameter')},
|
||||
} for item in root.findall('./Components/Component')}
|
||||
edges = [tuple(sorted((ep.attrib['component'], ep.attrib['port']) for ep in item.findall('Endpoint')))
|
||||
for item in root.findall('./Connections/Connection')]
|
||||
return nodes, edges, root
|
||||
|
||||
|
||||
def find_mapping(first, first_edges, second, second_edges, *, ports=False, parameters=True):
|
||||
"""Find an actual graph bijection, preserving node types and all parameters."""
|
||||
def edge_label(node, port):
|
||||
if not ports:
|
||||
return ''
|
||||
return port
|
||||
def graph(nodes, edges):
|
||||
adjacency = {key: defaultdict(Counter) for key in nodes}
|
||||
for (a, ap), (b, bp) in edges:
|
||||
adjacency[a][b][(edge_label(a, ap), edge_label(b, bp))] += 1
|
||||
adjacency[b][a][(edge_label(b, bp), edge_label(a, ap))] += 1
|
||||
return adjacency
|
||||
a, b = graph(first, first_edges), graph(second, second_edges)
|
||||
def signature(nodes, adj, key):
|
||||
return (nodes[key]['modelType'], parameter_key(nodes[key]['parameters']) if parameters else (),
|
||||
sum(sum(labels.values()) for labels in adj[key].values()))
|
||||
candidates = {key: [other for other in second if signature(first, a, key) == signature(second, b, other)]
|
||||
for key in first}
|
||||
if any(not options for options in candidates.values()):
|
||||
return None
|
||||
mapping = {}
|
||||
used = set()
|
||||
def search():
|
||||
if len(mapping) == len(first):
|
||||
return dict(mapping)
|
||||
key = min((key for key in first if key not in mapping),
|
||||
key=lambda key: (-sum(neighbor in mapping for neighbor in a[key]),
|
||||
len([other for other in candidates[key] if other not in used]), -len(a[key])))
|
||||
for other in candidates[key]:
|
||||
if other in used:
|
||||
continue
|
||||
if any(a[key].get(existing, Counter()) != b[other].get(target, Counter())
|
||||
for existing, target in mapping.items()):
|
||||
continue
|
||||
mapping[key] = other
|
||||
used.add(other)
|
||||
result = search()
|
||||
if result is not None:
|
||||
return result
|
||||
used.remove(other)
|
||||
del mapping[key]
|
||||
return None
|
||||
return search()
|
||||
|
||||
|
||||
def check_project_contract(project, xml_root):
|
||||
"""Check generated port metadata and exact JSON/XML execution data, without writes.
|
||||
|
||||
This covers the observed nullable optional-field failure and shared physical
|
||||
data, not a replacement for the complete frontend project parser.
|
||||
"""
|
||||
xml_nodes, xml_edges, _ = xml_model(xml_root)
|
||||
json_nodes = {node['id']: node['data'] for node in project['nodes']}
|
||||
if len(json_nodes) != len(project['nodes']) or json_nodes.keys() != xml_nodes.keys():
|
||||
raise ValueError('JSON/XML component IDs differ or JSON contains duplicate IDs.')
|
||||
for node_id, data in json_nodes.items():
|
||||
expected = xml_nodes[node_id]
|
||||
if (data['componentType'] != expected['modelType'] or
|
||||
data['modelType'] != expected['modelType'] or
|
||||
data['modelVersion'] != expected['modelVersion']):
|
||||
raise ValueError(f'{node_id}: JSON/XML model type or version differs.')
|
||||
if data['parameters'] != expected['parameters']:
|
||||
raise ValueError(f'{node_id}: JSON/XML parameters differ.')
|
||||
for port in data['ports']:
|
||||
# frontend/src/App.tsx:isProjectPortDefinitionValue accepts omission,
|
||||
# or the literal intoComponent. An explicit null rejects the import.
|
||||
if ('positiveFlowDirection' in port and
|
||||
port['positiveFlowDirection'] != 'intoComponent'):
|
||||
raise ValueError(f"{node_id}.{port['name']}: omit undefined positiveFlowDirection instead of null.")
|
||||
json_edges = []
|
||||
for edge in project['edges']:
|
||||
endpoints = []
|
||||
for side in ['source', 'target']:
|
||||
component, port = edge[side], edge[side + 'Handle']
|
||||
if component not in json_nodes:
|
||||
raise ValueError(f'Unknown connection component {component}.')
|
||||
data = json_nodes[component]
|
||||
active_ports = get_component_model_spec(data['modelType']).active_ports(data['parameters'])
|
||||
if port not in {item.name for item in active_ports}:
|
||||
raise ValueError(f'{component}.{port}: connection port is inactive or unknown.')
|
||||
endpoints.append((component, port))
|
||||
json_edges.append(tuple(sorted(endpoints)))
|
||||
if Counter(json_edges) != Counter(xml_edges):
|
||||
raise ValueError('JSON/XML connection endpoints differ.')
|
||||
simulation = xml_root.find('Simulation').attrib
|
||||
for key, xml_key in [('t_start', 'tStart'), ('t_stop', 'tStop'),
|
||||
('step', 'sampleStep'), ('max_step', 'maxStep')]:
|
||||
if project['simulation'][key] != float(simulation[xml_key]):
|
||||
raise ValueError(f'JSON/XML simulation {key} differs.')
|
||||
if project['simulation']['method'] != simulation['method']:
|
||||
raise ValueError('JSON/XML integration methods differ.')
|
||||
return {'valid': True, 'componentCount': len(json_nodes), 'connectionCount': len(json_edges),
|
||||
'parameterCount': sum(len(data['parameters']) for data in json_nodes.values()),
|
||||
'optionalPortFieldsValid': True, 'jsonXmlExecutionDataEqual': True}
|
||||
|
||||
|
||||
def generate_project(source, source_edges, target, target_edges, xml_root, mapping):
|
||||
layout_source = ROOT / 'tests/fixtures/legacy/test-mql-8.json'
|
||||
layout = json.loads(layout_source.read_text())
|
||||
layout_nodes = {node['id']: node for node in layout['nodes']}
|
||||
reverse_mapping = {value: key for key, value in mapping.items()}
|
||||
nodes = []
|
||||
for node_id, model in target.items():
|
||||
source_node = source[reverse_mapping[node_id]]
|
||||
template = layout_nodes.get(node_id)
|
||||
if template is None:
|
||||
template = next(node for node in layout['nodes'] if node['data']['modelType'] == model['modelType'])
|
||||
node = deepcopy(template)
|
||||
node['id'] = node_id
|
||||
node['selected'] = False
|
||||
node['data']['label'] = source_node['alias']
|
||||
node['data']['parameters'] = source_node['parameters']
|
||||
node['data']['modelVersion'] = model['modelVersion']
|
||||
node['data']['ports'] = get_component_model_spec(model['modelType']).as_catalog_dict()['ports']
|
||||
for port in node['data']['ports']:
|
||||
if port.get('positiveFlowDirection') is None:
|
||||
port.pop('positiveFlowDirection', None)
|
||||
if model['modelType'] == 'amesim_p4node2':
|
||||
node['data']['rotation'] = 180
|
||||
node['data']['mirrored'] = False
|
||||
if node_id not in layout_nodes:
|
||||
# The extra closing pipe sits below the four retained branches.
|
||||
node['position'] = {'x': 80.0, 'y': 900.0}
|
||||
node['data']['rotation'] = 0
|
||||
nodes.append(node)
|
||||
original_by_pair = {}
|
||||
for edge in layout['edges']:
|
||||
pair = tuple(sorted((edge['source'], edge['target'])))
|
||||
original_by_pair[pair] = edge
|
||||
xml_by_pair = {}
|
||||
for connection in xml_root.findall('./Connections/Connection'):
|
||||
pair = tuple(sorted(ep.attrib['component'] for ep in connection.findall('Endpoint')))
|
||||
xml_by_pair[pair] = connection
|
||||
edges = []
|
||||
changed_connections = []
|
||||
for ((a, ap), (b, bp)) in source_edges:
|
||||
a, b = mapping[a], mapping[b]
|
||||
pair = tuple(sorted((a, b)))
|
||||
existing = original_by_pair.get(pair)
|
||||
edge = deepcopy(existing) if existing else {'id': 'ame-' + a + '-' + ap + '-' + b + '-' + bp}
|
||||
if existing and existing['source'] == b:
|
||||
a, ap, b, bp = b, bp, a, ap
|
||||
old_connection = xml_by_pair[pair]
|
||||
old_endpoints = {ep.attrib['component']: ep.attrib['port'] for ep in old_connection.findall('Endpoint')}
|
||||
changed = old_endpoints != {a: ap, b: bp}
|
||||
if changed:
|
||||
changed_connections.append({'components': pair, 'before': old_endpoints, 'after': {a: ap, b: bp}})
|
||||
edge.update({'source': a, 'target': b, 'sourceHandle': ap, 'targetHandle': bp})
|
||||
edge.pop('selected', None)
|
||||
if any(target[node_id]['modelType'] == 'amesim_p4node2' for node_id in [a, b]):
|
||||
edge.setdefault('data', {}).pop('routePoints', None)
|
||||
if changed or existing is None:
|
||||
edge['data'] = {'isContactEdge': False}
|
||||
edges.append(edge)
|
||||
for endpoint in old_connection.findall('Endpoint'):
|
||||
endpoint.attrib['port'] = {a: ap, b: bp}[endpoint.attrib['component']]
|
||||
parameter_changes = []
|
||||
for component in xml_root.findall('./Components/Component'):
|
||||
node_id = component.attrib['id']
|
||||
parameters = source[reverse_mapping[node_id]]['parameters']
|
||||
for parameter in component.findall('Parameter'):
|
||||
key = parameter.attrib['name']
|
||||
before = float(parameter.attrib['value'])
|
||||
after = parameters[key]
|
||||
if abs(before - after) > max(1e-18, abs(after) * 1e-12):
|
||||
parameter_changes.append({'component': node_id, 'parameter': key, 'before': before, 'after': after})
|
||||
parameter.attrib['value'] = repr(after)
|
||||
simulation = {'t_start': 0.0, 't_stop': 10.0, 'step': 0.01, 'max_step': 1e30, 'method': 'BDF'}
|
||||
project = {'projectSchemaVersion': 1, 'name': 'test-mql-4-AME-aligned', 'nodes': nodes,
|
||||
'edges': edges, 'simulation': simulation}
|
||||
check_project_contract(project, xml_root)
|
||||
PROJECT.write_text(json.dumps(project, indent=2, ensure_ascii=False) + '\n')
|
||||
generated_xml = OUT / 'aligned-input.xml'
|
||||
xml_root.attrib['name'] = project['name']
|
||||
ET.indent(xml_root)
|
||||
ET.ElementTree(xml_root).write(generated_xml, encoding='utf-8', xml_declaration=True)
|
||||
XML.write_bytes(generated_xml.read_bytes())
|
||||
# Check the delivered JSON itself, including every exact endpoint and number.
|
||||
json_nodes = {node['id']: node['data'] for node in json.loads(PROJECT.read_text())['nodes']}
|
||||
for source_id, project_id in mapping.items():
|
||||
assert json_nodes[project_id]['parameters'] == source[source_id]['parameters']
|
||||
expected_edges = {tuple(sorted(((mapping[a], ap), (mapping[b], bp)))) for ((a, ap), (b, bp)) in source_edges}
|
||||
actual_edges = {tuple(sorted(((edge['source'], edge['sourceHandle']), (edge['target'], edge['targetHandle'])))) for edge in edges}
|
||||
assert expected_edges == actual_edges
|
||||
for edge in edges:
|
||||
for side in ['source', 'target']:
|
||||
data = json_nodes[edge[side]]
|
||||
active_ports = get_component_model_spec(data['modelType']).active_ports(data['parameters'])
|
||||
assert edge[side + 'Handle'] in {port.name for port in active_ports}
|
||||
return {'path': str(PROJECT.relative_to(ROOT)), 'sha256': sha(PROJECT),
|
||||
'xmlPath': str(generated_xml.relative_to(ROOT)), 'xmlSha256': sha(generated_xml),
|
||||
'nodeCount': len(nodes), 'edgeCount': len(edges), 'parameterCount': sum(len(n['data']['parameters']) for n in nodes),
|
||||
'allMappedParametersExactlyMatchAme': True, 'allMappedConnectionPortsExactlyMatchAme': True,
|
||||
'parameterChangesFromLegacyXml': parameter_changes, 'connectionPortChangesFromLegacyXml': changed_connections,
|
||||
'layoutMetadataSource': {'path': str(layout_source.relative_to(ROOT)), 'sha256': sha(layout_source)},
|
||||
'simulation': simulation,
|
||||
'simulationSettingsNote': 'AME archive stores historical fixed-step settings. This JSON uses native BDF; rtol is supplied by the backend and is not stored in the project. Initial validation used 1e-7; the backend default was subsequently changed to 1e-8. The earlier official Standard variable-step reference remains tolerance 1e-7. Inspect actual run diagnostics; solver algorithms are not identical.'}
|
||||
|
||||
|
||||
def main():
|
||||
parser = argparse.ArgumentParser(description=__doc__)
|
||||
parser.add_argument('--check', action='store_true', help='Validate delivered JSON/XML only; do not generate or write files.')
|
||||
arguments = parser.parse_args()
|
||||
if arguments.check:
|
||||
print(json.dumps(check_project_contract(json.loads(PROJECT.read_text()), ET.parse(XML).getroot()), indent=2))
|
||||
return
|
||||
OUT.mkdir(parents=True, exist_ok=True)
|
||||
source, source_edges, audit = audit_source()
|
||||
legacy_xml = OUT / 'legacy-corrected-input.xml'
|
||||
if not legacy_xml.exists():
|
||||
legacy_xml.write_bytes(XML.read_bytes())
|
||||
target, target_edges, xml_root = xml_model()
|
||||
mapping = find_mapping(source, source_edges, target, target_edges)
|
||||
audit['correctedXml'] = {'path': str(XML.relative_to(ROOT)), 'sha256': sha(XML),
|
||||
'parameterAndComponentTopologyIsomorphic': mapping is not None}
|
||||
ref = json.loads(REFERENCE.read_text())
|
||||
audit['reference'] = {'path': str(REFERENCE.relative_to(ROOT)), 'sha256': sha(REFERENCE),
|
||||
'source': ref['source'], 'timeCount': len(ref['times']), 'seriesCount': len(ref['series']),
|
||||
'ameHashMatches': ref['originalAmeSha256'] == sha(AME),
|
||||
'xmlHashMatches': ref['xmlSha256'] == sha(XML),
|
||||
'newAmesimRunPerformed': False}
|
||||
(OUT / 'source-model.json').write_text(json.dumps({'nodes': source, 'edges': source_edges}, indent=2, ensure_ascii=False) + '\n')
|
||||
if not mapping:
|
||||
mapping = find_mapping(source, source_edges, target, target_edges, parameters=False)
|
||||
if mapping:
|
||||
audit['componentMapping'] = {key: {'alias': source[key]['alias'], 'projectId': value} for key, value in mapping.items()}
|
||||
transformed = {tuple(sorted(((mapping[a], ap), (mapping[b], bp)))) for ((a, ap), (b, bp)) in source_edges}
|
||||
target_set = set(target_edges)
|
||||
audit['correctedXml']['exactPortDifferencesForTopologyMapping'] = {
|
||||
'ameOnly': sorted(transformed - target_set), 'xmlOnly': sorted(target_set - transformed)}
|
||||
if mapping:
|
||||
audit['generatedProject'] = generate_project(source, source_edges, target, target_edges, xml_root, mapping)
|
||||
audit['correctedXml']['scope'] = 'Input XML snapshot before this generation; generatedProject describes the delivered corrected files.'
|
||||
audit_text = json.dumps(audit, indent=2, ensure_ascii=False) + '\n'
|
||||
(OUT / 'model-audit.json').write_text(audit_text)
|
||||
(ROOT / 'tests/model_audit/test-mql-4-audit.json').write_text(audit_text)
|
||||
print(json.dumps({key: value for key, value in audit.items() if key not in {'componentMapping', 'members', 'globals'}}, indent=2))
|
||||
|
||||
|
||||
if __name__ == '__main__':
|
||||
main()
|
||||
@@ -0,0 +1,101 @@
|
||||
"""Independent read of AME XML fields; no shared expected-parameter helper."""
|
||||
from pathlib import Path
|
||||
import ast, collections, hashlib, json, math, operator, re, sys, tarfile
|
||||
import xml.etree.ElementTree as ET
|
||||
ROOT=Path(__file__).resolve().parents[2]
|
||||
sys.path.insert(0,str(ROOT))
|
||||
from app.simulation.registry import get_component_model_spec
|
||||
OUT=ROOT/'test/solver-newton-20260911/mql4/visual-recheck'
|
||||
OUT.mkdir(parents=True,exist_ok=True)
|
||||
with tarfile.open(ROOT/'tests/data/test_mql_4.ame') as archive:
|
||||
cir=archive.extractfile('test_mql_4_.cir').read().decode('latin1')
|
||||
# AME stores unescaped C-style && in visibility metadata, outside parameter values.
|
||||
xml_text=re.sub(r'<VISIBILITY>.*?</VISIBILITY>', '<VISIBILITY/>', cir, flags=re.S)
|
||||
xml_text=re.sub(r'&(?!amp;|lt;|gt;|quot;|apos;|#)', '&', xml_text)
|
||||
root=ET.fromstring(xml_text)
|
||||
BINARY={ast.Add:operator.add,ast.Sub:operator.sub,ast.Mult:operator.mul,ast.Div:operator.truediv,ast.Pow:operator.pow}
|
||||
UNARY={ast.UAdd:operator.pos,ast.USub:operator.neg}
|
||||
def evaluate(text,names):
|
||||
def visit(node):
|
||||
if isinstance(node,ast.Constant) and isinstance(node.value,(int,float)):return float(node.value)
|
||||
if isinstance(node,ast.Name):return names[node.id]
|
||||
if isinstance(node,ast.BinOp) and type(node.op) in BINARY:return BINARY[type(node.op)](visit(node.left),visit(node.right))
|
||||
if isinstance(node,ast.UnaryOp) and type(node.op) in UNARY:return UNARY[type(node.op)](visit(node.operand))
|
||||
raise ValueError(ast.dump(node))
|
||||
return visit(ast.parse(text.strip().replace('^','**'),mode='eval').body)
|
||||
variables={};pending={g.findtext('GLOB_PARAM_NAME').strip():g.findtext('VALUE').strip() for g in root.findall('.//GLOBALPARAM')}
|
||||
while pending:
|
||||
count=len(pending)
|
||||
for key,value in list(pending.items()):
|
||||
try:variables[key]=evaluate(value,variables)
|
||||
except KeyError:continue
|
||||
del pending[key]
|
||||
assert len(pending)<count,pending
|
||||
entities={}
|
||||
for kind in ['COMP','LINE']:
|
||||
for index,item in enumerate(root.findall('.//'+kind)):
|
||||
model=item.findtext('./SUBMODEL/SUB_NAME')
|
||||
if not model or model=='DIRECT':continue
|
||||
fields={}
|
||||
for tag in ['RPARAM','IPARAM','IVAR','EVAR']:
|
||||
for field in item.findall('.//'+tag):
|
||||
name=field.findtext('VARNAME');value=field.findtext('VALUE')
|
||||
if name and value:
|
||||
assert name not in fields,(item.findtext('ALIAS'),name)
|
||||
fields[name.strip()]={'value':value.strip(),'unit':(field.findtext('UNITS') or '').strip()}
|
||||
alias=item.findtext('ALIAS').strip()
|
||||
assert alias not in entities
|
||||
entities[alias]={'element':item,'fields':fields,'model':model,'source':kind+':'+str(index)}
|
||||
# Explicit initial-state translations; all other public names are read verbatim.
|
||||
state_names={
|
||||
'MECMAS21':{'v0':'v1','x0':'x1'},'PNCH012':{'p0':'press','T0':'temp'},'PNCH023':{'p0':'press','T0':'temp'},
|
||||
'PNL0001':{'p0':'p2','T0':'t2'},'PNL0002':{'p0':'pctr','T0':'tctr'},
|
||||
'PNL0003':{'p1_0':'p1','T1_0':'t1','p2_0':'p2','T2_0':'t2'},
|
||||
'STEP0':{'initial':'out0','final':'out1','time':'t0'},
|
||||
}
|
||||
unit_scale={('mm','m'):1e-3,('mm**2','m2'):1e-6,('L','m3'):1e-3,('N/mm','N/m'):1e3,('N/(mm/s)','N/(m/s)'):1e3}
|
||||
unit_aliases={('null',''),('degree',''),('J/m**2/K/s','W/(m2*K)'),('N/m**2','Pa'),('m**2','m2'),('N/(m/s)**2','N/(m/s)^2')}
|
||||
project=json.loads((ROOT/'tests/data/test-mql-4-corrected.json').read_text())
|
||||
rows=[];issues=[];unit_counts=collections.Counter();extras=[]
|
||||
for node in project['nodes']:
|
||||
d=node['data'];entry=entities[d['label']];model=entry['model'];fields=entry['fields']
|
||||
specs=get_component_model_spec(d['modelType']).parameter_by_name
|
||||
for key,actual in d['parameters'].items():
|
||||
source=state_names.get(model,{}).get(key,key)
|
||||
rule='raw field'
|
||||
if source in fields:
|
||||
f=fields[source];raw=evaluate(f['value'],variables);source_unit=f['unit'];target_unit=specs[key].unit
|
||||
if source in {'press','p1','p2','pctr'}:
|
||||
assert (source_unit,target_unit)==('Pa','Pa')
|
||||
expected=raw+101300.;rule='gauge Pa + 101300 Pa atmospheric pressure'
|
||||
elif (source_unit,target_unit) in unit_scale:
|
||||
expected=raw*unit_scale[source_unit,target_unit];rule='multiply by '+str(unit_scale[source_unit,target_unit])
|
||||
elif source_unit==target_unit or (source_unit,target_unit) in unit_aliases:
|
||||
expected=raw
|
||||
else:raise AssertionError((source,source_unit,target_unit))
|
||||
unit_counts[(source_unit,target_unit,rule)]+=1
|
||||
row={'jsonId':node['id'],'ameAlias':d['label'],'sourceEntity':entry['source'],'parameter':key,'sourceField':source,
|
||||
'rawExpression':f['value'],'rawValue':raw,'sourceUnit':source_unit,'targetUnit':target_unit,'conversion':rule,
|
||||
'expected':expected,'actual':actual}
|
||||
else:
|
||||
if model=='PNCH012' and key in {'vol1','vol2','vol3','vol4','dvol1','dvol2','dvol3','dvol4'}:expected=0.;rule='public extra port-volume inputs default zero'
|
||||
elif model=='PNVO001' and key=='opening0':expected=1.;rule='public fallback opening parameter; model signal port supplies actual command'
|
||||
elif model=='FORC' and key=='direction':
|
||||
geometry=entry['element'].findtext('COMP_GEOMETRY');assert geometry in {'2','8'}
|
||||
expected=1. if geometry=='2' else -1.;rule='force direction from AME geometry '+geometry
|
||||
elif model=='PNGD00' and key=='property_model':
|
||||
codes={name:evaluate(fields[name]['value'],variables) for name in ['fluidType','eosType','gasSetting']}
|
||||
assert codes=={'fluidType':12.,'eosType':6.,'gasSetting':1.},codes
|
||||
expected=0.;rule='public helium model selection mapped from explicit AME fluid/eos/gas codes'
|
||||
else:raise AssertionError((model,key))
|
||||
row={'jsonId':node['id'],'ameAlias':d['label'],'sourceEntity':entry['source'],'parameter':key,'conversion':rule,'expected':expected,'actual':actual}
|
||||
extras.append(row)
|
||||
row['matches']=math.isclose(actual,expected,rel_tol=1e-12,abs_tol=1e-15)
|
||||
if not row['matches']:issues.append(row)
|
||||
rows.append(row)
|
||||
result={'method':'Independent xml.etree XML parsing and arithmetic AST evaluation; does not import or call _expected_parameters or its source-field helpers.',
|
||||
'nodeCount':len(project['nodes']),'parameterCount':len(rows),'directSourceFieldCount':len(rows)-len(extras),'publicExtraOrGeometryMappedCount':len(extras),
|
||||
'unitConversionCounts':[{'source':a,'target':b,'rule':c,'count':n} for (a,b,c),n in unit_counts.items()],
|
||||
'extraParameters':extras,'differences':issues,'parameters':rows}
|
||||
(OUT/'independent-parameters.json').write_text(json.dumps(result,indent=2,ensure_ascii=False)+'\n')
|
||||
print(json.dumps({k:v for k,v in result.items() if k not in ['parameters','extraParameters']},indent=2))
|
||||
@@ -0,0 +1,98 @@
|
||||
{
|
||||
"source": "tests/data/test_mql_4.ame:test_mql_4_.cir COMP_PORT/PORT_POS (zero-based component indices)",
|
||||
"archiveSha256": "99a071896671d634d651a7b21f487662dd7c122af8fd3d60ead404a5afa53ed4",
|
||||
"components": [
|
||||
{
|
||||
"componentIndex": 47,
|
||||
"alias": "pnnode4_16",
|
||||
"geometry": 1,
|
||||
"ports": {
|
||||
"port_1": {
|
||||
"x": 10.0,
|
||||
"y": 19.0
|
||||
},
|
||||
"port_2": {
|
||||
"x": 19.0,
|
||||
"y": 10.0
|
||||
},
|
||||
"port_3": {
|
||||
"x": 10.0,
|
||||
"y": 1.0
|
||||
},
|
||||
"port_4": {
|
||||
"x": 1.0,
|
||||
"y": 10.0
|
||||
}
|
||||
}
|
||||
},
|
||||
{
|
||||
"componentIndex": 48,
|
||||
"alias": "pnnode4_17",
|
||||
"geometry": 1,
|
||||
"ports": {
|
||||
"port_1": {
|
||||
"x": 10.0,
|
||||
"y": 19.0
|
||||
},
|
||||
"port_2": {
|
||||
"x": 19.0,
|
||||
"y": 10.0
|
||||
},
|
||||
"port_3": {
|
||||
"x": 10.0,
|
||||
"y": 1.0
|
||||
},
|
||||
"port_4": {
|
||||
"x": 1.0,
|
||||
"y": 10.0
|
||||
}
|
||||
}
|
||||
},
|
||||
{
|
||||
"componentIndex": 49,
|
||||
"alias": "pnnode4_18",
|
||||
"geometry": 1,
|
||||
"ports": {
|
||||
"port_1": {
|
||||
"x": 10.0,
|
||||
"y": 19.0
|
||||
},
|
||||
"port_2": {
|
||||
"x": 19.0,
|
||||
"y": 10.0
|
||||
},
|
||||
"port_3": {
|
||||
"x": 10.0,
|
||||
"y": 1.0
|
||||
},
|
||||
"port_4": {
|
||||
"x": 1.0,
|
||||
"y": 10.0
|
||||
}
|
||||
}
|
||||
},
|
||||
{
|
||||
"componentIndex": 50,
|
||||
"alias": "pnnode4_19",
|
||||
"geometry": 1,
|
||||
"ports": {
|
||||
"port_1": {
|
||||
"x": 10.0,
|
||||
"y": 19.0
|
||||
},
|
||||
"port_2": {
|
||||
"x": 19.0,
|
||||
"y": 10.0
|
||||
},
|
||||
"port_3": {
|
||||
"x": 10.0,
|
||||
"y": 1.0
|
||||
},
|
||||
"port_4": {
|
||||
"x": 1.0,
|
||||
"y": 10.0
|
||||
}
|
||||
}
|
||||
}
|
||||
]
|
||||
}
|
||||
File diff suppressed because it is too large.
Load diff
@@ -9,7 +9,7 @@ from app.simulation.systems.network import SimulationNetwork
|
||||
|
||||
|
||||
def reference_data():
|
||||
return json.loads((Path(__file__).parent / 'data/native-python-reference.json').read_text(encoding='utf-8'))
|
||||
return json.loads((Path(__file__).parent / 'baselines/native/native-python-reference.json').read_text(encoding='utf-8'))
|
||||
|
||||
|
||||
def reference_network(case):
|
||||
|
||||
@@ -10,7 +10,6 @@ from app.main import run_system_xml_simulation
|
||||
|
||||
FIXTURE_PATH = (
|
||||
Path(__file__).resolve().parent
|
||||
/ "data"
|
||||
/ "fixtures"
|
||||
/ "high_stiffness_explicit_rk45.xml"
|
||||
)
|
||||
|
||||
@@ -22,7 +22,7 @@ from app.simulation.config import SolverActivityTracker
|
||||
from app.system_xml import validate_system_xml_document
|
||||
|
||||
ROOT = Path(__file__).resolve().parents[1]
|
||||
FIXTURE = ROOT / "tests/data/native-skill-test.xml"
|
||||
FIXTURE = ROOT / "tests/fixtures/native-skill-test.xml"
|
||||
|
||||
|
||||
def network(xml=None):
|
||||
@@ -76,7 +76,8 @@ class NativeExecutionTests(unittest.TestCase):
|
||||
def test_cache_and_standalone_executable_without_python_path(self):
|
||||
cached = build_native(self.program)
|
||||
self.assertTrue(cached.cache_hit)
|
||||
env = {**os.environ, "PATH": str(Path(os.environ["SystemRoot"]) / "System32")}
|
||||
isolated_path = str(Path(os.environ["SystemRoot"]) / "System32") if os.name == "nt" else str(self.root / "no-path")
|
||||
env = {**os.environ, "PATH": isolated_path}
|
||||
r = subprocess.run([str(cached.executable), "--init"], env=env, cwd=self.root,
|
||||
capture_output=True, text=True, check=True)
|
||||
self.assertEqual(len(json.loads(r.stdout)), 12)
|
||||
|
||||
@@ -29,7 +29,7 @@ sys.meta_path.insert(0, NoNumericalPython())
|
||||
from app.main import compile_system_xml_network
|
||||
from app.simulation.native_codegen.compiler import compile_native_program
|
||||
from app.system_xml import validate_system_xml_document
|
||||
doc = validate_system_xml_document(Path('tests/data/native-skill-test.xml').read_bytes()).document
|
||||
doc = validate_system_xml_document(Path('tests/fixtures/native-skill-test.xml').read_bytes()).document
|
||||
program = compile_native_program(compile_system_xml_network(doc))
|
||||
assert len(program.state_keys) == 12
|
||||
assert len(program.variables) == 175
|
||||
|
||||
@@ -152,8 +152,8 @@ int main(void) {
|
||||
self.assertLess(abs(sum(rates)),1e-10+sum(map(abs,rates))*1e-12)
|
||||
|
||||
def test_web_stream_completes_mql4_and_matches_amesim_reference(self):
|
||||
reference=json.loads((ROOT/'tests/data/test-mql-4-amesim-reference.json').read_text())
|
||||
xml=(ROOT/'tests/data/test-mql-4-corrected.xml').read_bytes()
|
||||
reference=json.loads((ROOT/'tests/baselines/simulation/test_mql_4/test-mql-4-amesim-reference.json').read_text())
|
||||
xml=(ROOT/'tests/fixtures/amesim/test-mql-4-corrected.xml').read_bytes()
|
||||
events=[json.loads(line) for line in simulation_event_stream(xml)]
|
||||
self.assertFalse([e for e in events if e['event']=='error'])
|
||||
self.assertTrue(any(e['event']=='progress' for e in events))
|
||||
@@ -161,7 +161,7 @@ int main(void) {
|
||||
self.assertTrue(result['success'],result['message'])
|
||||
self.assertEqual(result['simulatedUntil'],10)
|
||||
self.assertEqual(result['diagnostics']['backend'],'native-c')
|
||||
self.assertEqual(result['diagnostics']['integration']['rtol'],1e-7)
|
||||
self.assertEqual(result['diagnostics']['integration']['rtol'],1e-8)
|
||||
self.assertEqual(result['diagnostics']['integration']['method'],'BDF')
|
||||
self.assertEqual(result['diagnostics']['stateCount'],64)
|
||||
# Bound the formerly stalled tiny-step failure by work, not machine time.
|
||||
|
||||
@@ -0,0 +1,237 @@
|
||||
"""Standalone pipe-root checks; only a C compiler and Python stdlib are needed."""
|
||||
import ctypes
|
||||
import math
|
||||
import os
|
||||
from pathlib import Path
|
||||
import shlex
|
||||
import shutil
|
||||
import subprocess
|
||||
import tempfile
|
||||
import unittest
|
||||
|
||||
|
||||
ROOT = Path(__file__).resolve().parents[1]
|
||||
LAMINAR_END = 89.96829989
|
||||
|
||||
|
||||
def reference_friction(reynolds, roughness):
|
||||
"""Independent evaluation of the retained Darcy blend, without its slope."""
|
||||
laminar = 64 / reynolds
|
||||
if reynolds <= LAMINAR_END:
|
||||
return laminar
|
||||
smooth = (-1.8 * math.log10(6.9 / reynolds)) ** -2
|
||||
turbulent = smooth
|
||||
if roughness:
|
||||
fully_rough = (-2 * math.log10(roughness / 3.7)) ** -2
|
||||
weight = 1 / (1 + (180 / (reynolds * roughness)) ** 2)
|
||||
turbulent = (1 - weight) * smooth + weight * fully_rough
|
||||
transition = ((reynolds - LAMINAR_END) / 2741.96700831) ** 8.37293695
|
||||
return (laminar + transition * turbulent) / (1 + transition)
|
||||
|
||||
|
||||
def reference_root(constant, roughness):
|
||||
if constant == 0:
|
||||
return 0.0
|
||||
low, high = 0.0, 1.0
|
||||
while high * high * reference_friction(high, roughness) < constant:
|
||||
high *= 2
|
||||
for _ in range(120):
|
||||
middle = low + (high - low) / 2
|
||||
if middle == low or middle == high:
|
||||
break
|
||||
if middle * middle * reference_friction(middle, roughness) < constant:
|
||||
low = middle
|
||||
else:
|
||||
high = middle
|
||||
return low + (high - low) / 2
|
||||
|
||||
|
||||
class PipeStatus(ctypes.Structure):
|
||||
_fields_ = [
|
||||
('converged', ctypes.c_int),
|
||||
('iterations', ctypes.c_int),
|
||||
('bisections', ctypes.c_int),
|
||||
('relative_residual', ctypes.c_double),
|
||||
]
|
||||
|
||||
|
||||
class NativePipeSolverTests(unittest.TestCase):
|
||||
@classmethod
|
||||
def setUpClass(cls):
|
||||
command = shlex.split(os.environ.get('CC', ''))
|
||||
if not command:
|
||||
compiler = shutil.which('gcc') or shutil.which('clang')
|
||||
if not compiler:
|
||||
raise unittest.SkipTest('A native C compiler is required')
|
||||
command = [compiler]
|
||||
cls.directory = tempfile.TemporaryDirectory(prefix='native-pipe-solver-')
|
||||
cls.addClassCleanup(cls.directory.cleanup)
|
||||
cls.compiler = command
|
||||
source = (ROOT / 'native/components/kernels.c').read_text()
|
||||
cls.library = cls.build_library(source, 'ordinary')
|
||||
|
||||
# Fault injection only in the temporary test translation unit. The
|
||||
# resistance equation and public production ABI have no test switches.
|
||||
prepared = 'static double pipe_friction_prepared('
|
||||
derivative = 'static double pipe_friction_derivative('
|
||||
assert source.count(prepared) == source.count(derivative) == 1
|
||||
injected = 'int test_pipe_fault_mode=0;\n' + source.replace(
|
||||
prepared, 'static double pipe_friction_prepared_original(', 1)
|
||||
injected = injected.replace('static double pipe_friction(double', r'''
|
||||
static double pipe_friction_prepared(double re,double rr,double rough) {
|
||||
if(test_pipe_fault_mode==5)return 0; /* No upper sign change. */
|
||||
if(test_pipe_fault_mode==6)return re<2000 ? .01 : 100;
|
||||
return pipe_friction_prepared_original(re,rr,rough);
|
||||
}
|
||||
static double pipe_friction(double''', 1)
|
||||
injected = injected.replace(
|
||||
derivative, 'static double pipe_friction_derivative_original(', 1)
|
||||
injected = injected.replace('static double pipe_checked_solution(', r'''
|
||||
static double pipe_friction_derivative(double re,double rr,double rough,double *df) {
|
||||
double f=pipe_friction_derivative_original(re,rr,rough,df);
|
||||
double slope=2*re*f+re*re*(*df);
|
||||
if(test_pipe_fault_mode==1)*df=(1e6*slope-2*re*f)/(re*re);
|
||||
if(test_pipe_fault_mode==2)*df=NAN;
|
||||
if(test_pipe_fault_mode==3)*df=(-slope-2*re*f)/(re*re);
|
||||
if(test_pipe_fault_mode==4)return NAN;
|
||||
if(test_pipe_fault_mode==6){*df=0;return re<2000 ? .01 : 100;}
|
||||
return f;
|
||||
}
|
||||
static double pipe_checked_solution(''', 1)
|
||||
cls.fault_library = cls.build_library(injected, 'faults')
|
||||
cls.fault_mode = ctypes.c_int.in_dll(cls.fault_library, 'test_pipe_fault_mode')
|
||||
|
||||
@classmethod
|
||||
def build_library(cls, source, name):
|
||||
directory = Path(cls.directory.name)
|
||||
source_path = directory / (name + '.c')
|
||||
library_path = directory / (name + ('.dll' if os.name == 'nt' else '.so'))
|
||||
source_path.write_text(source)
|
||||
command = cls.compiler + [
|
||||
'-std=c11', '-O3', '-Wall', '-Wextra', '-Werror',
|
||||
'-ffp-contract=off', '-fno-fast-math', '-shared',
|
||||
]
|
||||
if os.name != 'nt':
|
||||
command.append('-fPIC')
|
||||
command += ['-I', str(ROOT / 'native/include'), str(source_path),
|
||||
'-lm', '-o', str(library_path)]
|
||||
run = subprocess.run(command, capture_output=True, text=True, timeout=60)
|
||||
if run.returncode:
|
||||
raise AssertionError(run.stderr)
|
||||
library = ctypes.CDLL(str(library_path))
|
||||
if os.name == 'nt':
|
||||
import _ctypes
|
||||
cls.addClassCleanup(_ctypes.FreeLibrary, library._handle)
|
||||
library.native_pipe_resistance.argtypes = [
|
||||
ctypes.c_double, ctypes.c_double, ctypes.c_double,
|
||||
ctypes.POINTER(PipeStatus),
|
||||
]
|
||||
library.native_pipe_resistance.restype = ctypes.c_double
|
||||
return library
|
||||
|
||||
def solve(self, constant, roughness=0, flow_scale=1, library=None):
|
||||
# Nonzero sentinel fields ensure every call resets a reused status.
|
||||
status = PipeStatus(1, 999, 999, -1)
|
||||
result = (library or self.library).native_pipe_resistance(
|
||||
constant, roughness, flow_scale, ctypes.byref(status))
|
||||
return result, status
|
||||
|
||||
def assert_root(self, constant, roughness, result, status):
|
||||
self.assertTrue(status.converged)
|
||||
self.assertTrue(math.isfinite(result))
|
||||
self.assertLessEqual(status.relative_residual, 1e-9)
|
||||
expected = reference_root(constant, roughness)
|
||||
self.assertLessEqual(abs(result - expected), 1e-12 + expected * 1e-9)
|
||||
residual = abs(result * result * reference_friction(result, roughness) / constant - 1)
|
||||
self.assertLessEqual(residual, 1e-9)
|
||||
|
||||
def test_independent_bisection_across_reynolds_roughness_and_flow_scales(self):
|
||||
fallbacks = 0
|
||||
maximum_iterations = 0
|
||||
for exponent in range(151):
|
||||
reynolds = 10 ** (-6 + exponent * .1)
|
||||
for roughness in (0, 1e-5, 1e-4, 1e-3, 1e-2, .1):
|
||||
constant = reynolds ** 2 * reference_friction(reynolds, roughness)
|
||||
for scale in (1e-12, 1e-6, 1):
|
||||
with self.subTest(reynolds=reynolds, roughness=roughness, scale=scale):
|
||||
result, status = self.solve(constant, roughness, scale)
|
||||
self.assert_root(constant, roughness, result, status)
|
||||
self.assertLess(status.iterations, 20)
|
||||
fallbacks += status.bisections
|
||||
maximum_iterations = max(maximum_iterations, status.iterations)
|
||||
self.assertGreater(fallbacks, 0)
|
||||
self.assertGreater(maximum_iterations, 0)
|
||||
|
||||
def test_laminar_transition_neighbors_and_extreme_flow_scales(self):
|
||||
for center in (LAMINAR_END, 1000, 2300, LAMINAR_END + 2741.96700831, 4000):
|
||||
for reynolds in (math.nextafter(center, 0), center, math.nextafter(center, math.inf)):
|
||||
for roughness in (0, 1e-5, .1):
|
||||
constant = reynolds ** 2 * reference_friction(reynolds, roughness)
|
||||
for scale in (1e-300, 1e-12, 1, 1e300):
|
||||
with self.subTest(reynolds=reynolds, roughness=roughness, scale=scale):
|
||||
result, status = self.solve(constant, roughness, scale)
|
||||
self.assert_root(constant, roughness, result, status)
|
||||
|
||||
def test_zero_invalid_inputs_and_unrepresentable_values_fail_explicitly(self):
|
||||
result, status = self.solve(0)
|
||||
self.assertEqual(result, 0)
|
||||
self.assertTrue(status.converged)
|
||||
self.assertEqual(status.relative_residual, 0)
|
||||
result, status = self.solve(64, 0, 1.7e308)
|
||||
self.assertEqual(result, 1)
|
||||
self.assertTrue(status.converged)
|
||||
for constant, roughness, scale in (
|
||||
(-1, 0, 1), (math.nan, 0, 1), (math.inf, 0, 1),
|
||||
(1, -1, 1), (1, math.nan, 1), (1, math.inf, 1),
|
||||
(1, 0, 0), (1, 0, -1), (1, 0, math.nan), (1, 0, math.inf),
|
||||
(math.ulp(0.0), 0, 1), # A positive root rounds to zero.
|
||||
(1e8, 3.7, 1), # Non-finite roughness limit.
|
||||
(1e100, 0, 1), # Non-finite friction in bracket expansion.
|
||||
(1e308, 0, 1), # Non-finite starting bound.
|
||||
(128, 0, 1.7e308), (1e8, 0, 1.7e308),
|
||||
):
|
||||
with self.subTest(constant=constant, roughness=roughness, scale=scale):
|
||||
result, status = self.solve(constant, roughness, scale)
|
||||
self.assertTrue(math.isnan(result))
|
||||
self.assertFalse(status.converged)
|
||||
self.assertLessEqual(status.iterations, 128)
|
||||
self.assertNotEqual(status.relative_residual, -1)
|
||||
|
||||
def test_inaccurate_or_unusable_newton_slopes_trigger_convergent_bisection(self):
|
||||
try:
|
||||
for mode in (1, 2, 3):
|
||||
self.fault_mode.value = mode
|
||||
for reynolds in (1000, 2800, 1e5, 1e9):
|
||||
for roughness in (0, .1):
|
||||
constant = reynolds ** 2 * reference_friction(reynolds, roughness)
|
||||
with self.subTest(mode=mode, reynolds=reynolds, roughness=roughness):
|
||||
result, status = self.solve(constant, roughness, library=self.fault_library)
|
||||
self.assert_root(constant, roughness, result, status)
|
||||
self.assertGreater(status.bisections, 0)
|
||||
self.assertLess(status.iterations, 128)
|
||||
finally:
|
||||
self.fault_mode.value = 0
|
||||
|
||||
def test_nonfinite_equation_missing_bracket_and_float_stagnation_fail(self):
|
||||
try:
|
||||
for mode in (4, 5, 6):
|
||||
self.fault_mode.value = mode
|
||||
with self.subTest(mode=mode):
|
||||
result, status = self.solve(1e6, library=self.fault_library)
|
||||
self.assertTrue(math.isnan(result))
|
||||
self.assertFalse(status.converged)
|
||||
if mode == 4:
|
||||
self.assertEqual(status.iterations, 1)
|
||||
elif mode == 5:
|
||||
self.assertEqual(status.iterations, 0)
|
||||
else:
|
||||
# A discontinuous equation has no valid root even when
|
||||
# the bracket narrows to adjacent representable values.
|
||||
self.assertGreater(status.bisections, 0)
|
||||
self.assertLess(status.iterations, 128)
|
||||
finally:
|
||||
self.fault_mode.value = 0
|
||||
|
||||
|
||||
if __name__ == '__main__':
|
||||
unittest.main()
|
||||
@@ -0,0 +1,84 @@
|
||||
from __future__ import annotations
|
||||
|
||||
from copy import deepcopy
|
||||
import subprocess
|
||||
import unittest
|
||||
from xml.etree import ElementTree as ET
|
||||
|
||||
from app.main import run_system_xml_simulation
|
||||
from app.simulation.native_codegen.build import toolchain
|
||||
from app.simulation.native_codegen.input import project_xml
|
||||
from app.system_xml import validate_system_xml_document
|
||||
from tests.test_amesim_pnch012_xml import amesim_pnch012_project
|
||||
|
||||
|
||||
def pressure_project(value: float | str, unit: str = "bar") -> dict:
|
||||
project = amesim_pnch012_project().model_dump(mode="json")
|
||||
chamber = project["nodes"][0]["data"]
|
||||
chamber["parameters"]["p0"] = value
|
||||
chamber["parameterUnits"]["p0"] = unit
|
||||
return project
|
||||
|
||||
|
||||
class PressureUnitInputTests(unittest.TestCase):
|
||||
def test_absolute_bar_expression_exports_si_without_atmospheric_offset(self) -> None:
|
||||
project = pressure_project("= 0.25 + 0.75")
|
||||
original = deepcopy(project)
|
||||
xml = project_xml(project)
|
||||
root = ET.fromstring(xml)
|
||||
self.assertEqual(root.attrib["unitSystem"], "SI")
|
||||
parameter = root.find(
|
||||
"./Components/Component[@id='chamber_1']/Parameter[@name='p0']"
|
||||
)
|
||||
self.assertIsNotNone(parameter)
|
||||
self.assertEqual(float(parameter.attrib["value"]), 100000.0)
|
||||
self.assertNotIn("unit", parameter.attrib)
|
||||
report = validate_system_xml_document(xml)
|
||||
self.assertTrue(report.valid, report.as_dict())
|
||||
self.assertEqual(project, original)
|
||||
|
||||
def test_saved_numeric_values_are_already_si_with_absolute_bar_display(self) -> None:
|
||||
for value in (250000.0, "250000"):
|
||||
with self.subTest(value=value):
|
||||
self.assertEqual(
|
||||
project_xml(pressure_project(value)),
|
||||
project_xml(pressure_project(250000.0, "Pa")),
|
||||
)
|
||||
|
||||
def test_absolute_bar_and_existing_pressure_expression_units_are_equivalent(self) -> None:
|
||||
expected = project_xml(pressure_project(250000.0, "Pa"))
|
||||
for unit, expression in (
|
||||
("bar", "2 + 0.5"),
|
||||
("kPa", "200 + 50"),
|
||||
("MPa", "0.2 + 0.05"),
|
||||
("Pa", "200000 + 50000"),
|
||||
):
|
||||
with self.subTest(unit=unit):
|
||||
self.assertEqual(project_xml(pressure_project(expression, unit)), expected)
|
||||
|
||||
def test_absolute_bar_and_pa_simulations_return_identical_si_pressure(self) -> None:
|
||||
try:
|
||||
toolchain()
|
||||
except (OSError, RuntimeError, subprocess.SubprocessError) as exc:
|
||||
self.skipTest(f"Native toolchain unavailable: {exc}")
|
||||
absolute_bar = run_system_xml_simulation(
|
||||
project_xml(pressure_project("2 + 0.5", "bar"))
|
||||
)
|
||||
pascals = run_system_xml_simulation(
|
||||
project_xml(pressure_project(250000.0, "Pa"))
|
||||
)
|
||||
self.assertTrue(absolute_bar["success"], absolute_bar["message"])
|
||||
self.assertTrue(pascals["success"], pascals["message"])
|
||||
self.assertEqual(absolute_bar["series"], pascals["series"])
|
||||
self.assertEqual(absolute_bar["series"]["time"], [0.0, 0.001, 0.002])
|
||||
for pressure in absolute_bar["series"]["chamber_1.p"]:
|
||||
self.assertAlmostEqual(pressure, 250000.0, places=6)
|
||||
pressure_metadata = next(
|
||||
variable for variable in absolute_bar["variables"]
|
||||
if variable["key"] == "chamber_1.p"
|
||||
)
|
||||
self.assertEqual(pressure_metadata["unit"], "Pa")
|
||||
|
||||
|
||||
if __name__ == "__main__":
|
||||
unittest.main()
|
||||
@@ -11,9 +11,9 @@ BASELINE_ROOT = REPOSITORY_ROOT / "tests" / "baselines" / "simulation"
|
||||
GIT_ATTRIBUTES_PATH = REPOSITORY_ROOT / ".gitattributes"
|
||||
|
||||
EXPECTED_ATTRIBUTE_RULES = {
|
||||
("tests/data/test-mql-8.xml", "text", "eol=lf"),
|
||||
("tests/data/test-mql-8.json", "text", "eol=lf"),
|
||||
("tests/data/test_mql-full-branches-01-04.xml", "text", "eol=lf"),
|
||||
("tests/fixtures/legacy/test-mql-8.xml", "text", "eol=lf"),
|
||||
("tests/fixtures/legacy/test-mql-8.json", "text", "eol=lf"),
|
||||
("tests/baselines/simulation/test_mql_full_branches/sources/test_mql-full-branches-01-04.xml", "text", "eol=lf"),
|
||||
("tests/baselines/simulation/**/*.json", "text", "eol=lf"),
|
||||
}
|
||||
|
||||
|
||||
Reference in new issue
Block a user