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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/* 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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/* >>>>>>>>>>>>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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}
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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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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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{
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/* panic step reduction */
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stepdn_();
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*press = 1.0e-10 - c[1];
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}
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if (*temp <= 1.0e-10)
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{
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/* panic step reduction */
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stepdn_();
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*temp = 1.0e-10;
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}
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/*** temperature & pressure variation ***/
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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);
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/* <<<<<<<<<<<<End of Calculation Executable Statements. */
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/* 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;
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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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*vol /= 1.00000000000000e-006;
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*mgas1 /= 1.00000000000000e-003;
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}
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@@ -0,0 +1,356 @@
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<?xml version="1.0" encoding="ISO-8859-1"?>
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<!DOCTYPE SPE>
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<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
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|
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<SUBMODEL>
|
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<SUB_TYPE>0</SUB_TYPE>
|
||||
<SUB_ID_MAX>33</SUB_ID_MAX>
|
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<DEFAULT_ICON>pn_c1</DEFAULT_ICON>
|
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<SUB_LABEL>variable volume pneumatic chamber with heat exchange (preferred)</SUB_LABEL>
|
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<SUB_UNIT>0</SUB_UNIT>
|
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<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
Binary file not shown.
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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 +0,0 @@
|
||||
{"provenance":"Frozen from the existing Python implementation before its removal on 2026-09-10. Expected values are not generated by the C implementation.","rtol":2e-08,"atol":2e-07,"cases":[{"components":[{"name":"amesim_pnch023_1","type":"amesim_pnch023","parameters":{"gi":1.0,"cvol":0.057,"kth":0.0,"sth":0.1,"extemp":293.15,"p0":15300000.0,"T0":293.15},"overrides":{},"medium":{"type":"AmesimHeliumPengRobinsonMedium","parameters":{"name":"AMESimHeliumPengRobinson","R_gas":2077.26439404998,"cp_ref":5193.1609851249505,"T_ref":293.15,"cp_slope":0.0,"viscosity_ref":1.96e-05,"viscosity_T_ref":293.15,"sutherland_constant":79.4}}},{"name":"amesim_pnvo001_1","type":"amesim_pnvo001","parameters":{"gi":1.0,"cq":0.45,"area0":7.85e-05,"Cv":0.5,"Kv":0.4,"flowset":1.0,"opening0":0.0},"overrides":{},"medium":{"type":"AmesimHeliumPengRobinsonMedium","parameters":{"name":"AMESimHeliumPengRobinson","R_gas":2077.26439404998,"cp_ref":5193.1609851249505,"T_ref":293.15,"cp_slope":0.0,"viscosity_ref":1.96e-05,"viscosity_T_ref":293.15,"sutherland_constant":79.4}}},{"name":"amesim_step0_1","type":"amesim_step0","parameters":{"initial":0.0,"final":1.0,"time":0.04},"overrides":{},"medium":null},{"name":"amesim_pnch012_1","type":"amesim_pnch012","parameters":{"gi":1.0,"cvol0":0.015,"kth":1500.0,"sth":0.7,"extemp":293.15,"p0":100000.0,"T0":293.15,"vol1":0.0,"vol2":0.0,"vol3":0.0,"vol4":0.0,"dvol1":0.0,"dvol2":0.0,"dvol3":0.0,"dvol4":0.0},"overrides":{"external_volumes":{"port_1":0.0,"port_2":0.0,"port_3":0.0,"port_4":0.0},"external_volume_rates":{"port_1":0.0,"port_2":0.0,"port_3":0.0,"port_4":0.0}},"medium":{"type":"AmesimHeliumPengRobinsonMedium","parameters":{"name":"AMESimHeliumPengRobinson","R_gas":2077.26439404998,"cp_ref":5193.1609851249505,"T_ref":293.15,"cp_slope":0.0,"viscosity_ref":1.96e-05,"viscosity_T_ref":293.15,"sutherland_constant":79.4}}},{"name":"amesim_pnpl01_2","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_pnpl01_3","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_pnpl01_4","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_ud00_1","type":"amesim_ud00","parameters":{"tstart":0.0,"start1":1e+17,"end1":1e+17,"t1":0.8,"start2":49000.0,"end2":49000.0,"t2":10.0,"start3":1.0,"end3":1.0,"t3":0.0,"start4":1.0,"end4":1.0,"t4":0.0,"start5":1.0,"end5":1.0,"t5":0.0,"start6":1.0,"end6":1.0,"t6":0.0,"start7":1.0,"end7":1.0,"t7":0.0,"start8":1.0,"end8":1.0,"t8":0.0,"nstages":2.0,"iscyclic":0.0},"overrides":{"iscyclic":true,"starts":[1e+17,49000.0,1.0,1.0,1.0,1.0,1.0,1.0],"ends":[1e+17,49000.0,1.0,1.0,1.0,1.0,1.0,1.0],"durations":[0.8,10.0,0.0,0.0,0.0,0.0,0.0,0.0],"nstages":2},"medium":null},{"name":"amesim_forc_1","type":"amesim_forc","parameters":{"direction":1.0},"overrides":{},"medium":null},{"name":"amesim_pnrp17_1","type":"amesim_pnrp17","parameters":{"gi":1.0,"dp":0.2,"dr":0.001,"x0":0.0},"overrides":{},"medium":{"type":"AmesimHeliumPengRobinsonMedium","parameters":{"name":"AMESimHeliumPengRobinson","R_gas":2077.26439404998,"cp_ref":5193.1609851249505,"T_ref":293.15,"cp_slope":0.0,"viscosity_ref":1.96e-05,"viscosity_T_ref":293.15,"sutherland_constant":79.4}}},{"name":"amesim_pnch012_2","type":"amesim_pnch012","parameters":{"gi":1.0,"cvol0":0.015,"kth":1500.0,"sth":0.7,"extemp":293.15,"p0":100000.0,"T0":293.15,"vol1":0.0,"vol2":0.0,"vol3":0.0,"vol4":0.0,"dvol1":0.0,"dvol2":0.0,"dvol3":0.0,"dvol4":0.0},"overrides":{"external_volumes":{"port_1":0.0,"port_2":0.0,"port_3":0.0,"port_4":0.0},"external_volume_rates":{"port_1":0.0,"port_2":0.0,"port_3":0.0,"port_4":0.0}},"medium":{"type":"AmesimHeliumPengRobinsonMedium","parameters":{"name":"AMESimHeliumPengRobinson","R_gas":2077.26439404998,"cp_ref":5193.1609851249505,"T_ref":293.15,"cp_slope":0.0,"viscosity_ref":1.96e-05,"viscosity_T_ref":293.15,"sutherland_constant":79.4}}},{"name":"amesim_pnpl01_6","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_pnpl01_7","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_pnpl01_8","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_pnpl01_9","type":"amesim_pnpl01","parameters":{},"overrides":{},"medium":null},{"name":"amesim_mecmas21_2","type":"amesim_mecmas21","parameters":{"mass":50.0,"fstick":0.0,"fcoul":0.0,"rvisc":0.0,"wind":0.0,"dvel":1e-06,"restdvel":1e-06,"restcoeff":0.65,"astrib":0.001,"xmin":-1.0,"Kbmin":1000000000.0,"Dbmin":10000.0,"Pdmin":0.0001,"xmax":0.8,"Kbmax":1000000000.0,"Dbmax":10000.0,"Pdmax":0.0001,"theta":0.0,"useFriction":1.0,"stoptype":4.0,"discContactOption":1.0,"strib":1.0,"frictionType":1.0,"v0":0.0,"x0":0.0},"overrides":{},"medium":null},{"name":"amesim_f000_1","type":"amesim_f000","parameters":{},"overrides":{},"medium":null},{"name":"amesim_f000_2","type":"amesim_f000","parameters":{},"overrides":{},"medium":null},{"name":"amesim_lstp00a_1","type":"amesim_lstp00a","parameters":{"na":10.0,"gap0":0.0,"kconLine truncated
|
||||
@@ -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
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
File diff suppressed because it is too large.
Load diff
Reference in new issue
Block a user