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SystemSimulationApp/AmesimModels/help/source/PNCH012.spe
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2026-07-30 10:15:23 +00:00

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<?xml version="1.0" encoding="ISO-8859-1"?>
<!DOCTYPE SPE>
<SPE DOC_VERSION="2" AME_VERSION="16.0.0 - 68387-65635 2017">
<SUBMODEL>
<SUB_TYPE>0</SUB_TYPE>
<SUB_ID_MAX>33</SUB_ID_MAX>
<DEFAULT_ICON>pn_c1</DEFAULT_ICON>
<SUB_LABEL>variable volume pneumatic chamber with heat exchange (preferred)</SUB_LABEL>
<SUB_UNIT>0</SUB_UNIT>
<R_STORES_NUMBER>2</R_STORES_NUMBER>
<I_STORES_NUMBER>2</I_STORES_NUMBER>
<OUTPUT_TYPE>1</OUTPUT_TYPE>
<RPARAMS_LIST>
<RPARAM>
<SUB_ID>27</SUB_ID>
<TITLE>dead volume</TITLE>
<VARNAME>cvol0</VARNAME>
<VISIBILITY>True</VISIBILITY>
<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
<VALUE>1.00000000000000e+00</VALUE>
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+005</MAX_VALUE>
<UNITS>L</UNITS>
</RPARAM>
<RPARAM>
<SUB_ID>28</SUB_ID>
<TITLE>thermal exchange coefficient</TITLE>
<VARNAME>kth</VARNAME>
<VISIBILITY>True</VISIBILITY>
<DEF_VALUE>0.00000000000000e+00</DEF_VALUE>
<VALUE>0.00000000000000e+00</VALUE>
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+006</MAX_VALUE>
<UNITS>J/m**2/K/s</UNITS>
</RPARAM>
<RPARAM>
<SUB_ID>29</SUB_ID>
<TITLE>thermal exchange area</TITLE>
<VARNAME>sth</VARNAME>
<VISIBILITY>True</VISIBILITY>
<DEF_VALUE>1.00000000000000e-01</DEF_VALUE>
<VALUE>1.00000000000000e-01</VALUE>
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+002</MAX_VALUE>
<UNITS>m**2</UNITS>
</RPARAM>
<RPARAM>
<SUB_ID>30</SUB_ID>
<TITLE>external temperature</TITLE>
<VARNAME>extemp</VARNAME>
<VISIBILITY>True</VISIBILITY>
<DEF_VALUE>2.93150000000000e+02</DEF_VALUE>
<VALUE>2.93150000000000e+02</VALUE>
<MIN_VALUE>1.00000000000000e+000</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
<UNITS>K</UNITS>
</RPARAM>
</RPARAMS_LIST>
<IPARAMS_LIST>
<IPARAM>
<SUB_ID>31</SUB_ID>
<TITLE>gas type index</TITLE>
<VARNAME>gi</VARNAME>
<VISIBILITY>True</VISIBILITY>
<DEF_VALUE>1</DEF_VALUE>
<VALUE>1</VALUE>
<MIN_VALUE>1</MIN_VALUE>
<MAX_VALUE>99</MAX_VALUE>
</IPARAM>
</IPARAMS_LIST>
<IVARS_LIST>
<IVAR>
<SUB_ID>32</SUB_ID>
<TITLE>volume of pneumatic chamber</TITLE>
<VARNAME>vol</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<UNITS>cm**3</UNITS>
</IVAR>
<IVAR>
<SUB_ID>33</SUB_ID>
<TITLE>mass of gas in chamber</TITLE>
<VARNAME>mgas1</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<UNITS>g</UNITS>
</IVAR>
</IVARS_LIST>
<EVARS_LIST>
<PORT>
<EVAR>
<SUB_ID>1</SUB_ID>
<TITLE>temperature</TITLE>
<VARNAME>temp</VARNAME>
<VARNAME2>dtemp</VARNAME2>
<VISIBILITY>True</VISIBILITY>
<TYPE>1</TYPE>
<DIMENSION>1</DIMENSION>
<IO>2</IO>
<UNITS>K</UNITS>
<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+003</MAX_VALUE>
<DEF_VALUE>2.93150000000000e+002</DEF_VALUE>
<VALUE>2.93150000000000e+002</VALUE>
</EVAR>
<EVAR>
<SUB_ID>2</SUB_ID>
<TITLE>pressure</TITLE>
<VARNAME>press</VARNAME>
<VARNAME2>dpress</VARNAME2>
<VISIBILITY>True</VISIBILITY>
<TYPE>1</TYPE>
<DIMENSION>1</DIMENSION>
<IO>2</IO>
<UNITS>Pa</UNITS>
<MIN_VALUE>-1.01300000000000e+005</MIN_VALUE>
<MAX_VALUE>1.00000000000000e+012</MAX_VALUE>
<DEF_VALUE>0.00000000000000e+000</DEF_VALUE>
<VALUE>0.00000000000000e+000</VALUE>
</EVAR>
<EVAR>
<SUB_ID>3</SUB_ID>
<TITLE>enthalpy flow rate at port 1</TITLE>
<VARNAME>dh1</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>J/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>4</SUB_ID>
<TITLE>mass flow rate at port 1</TITLE>
<VARNAME>dm1</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>g/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>5</SUB_ID>
<TITLE>derivative of volume at port 1</TITLE>
<VARNAME>dvol1</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>L/min</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
<EVAR>
<SUB_ID>6</SUB_ID>
<TITLE>volume at port 1</TITLE>
<VARNAME>vol1</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>cm**3</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
</PORT>
<PORT>
<EVAR>
<SUB_ID>7</SUB_ID>
<VARNAME>temp2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>0</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>8</SUB_ID>
<VARNAME>press2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>1</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>9</SUB_ID>
<TITLE>enthalpy flow rate at port 2</TITLE>
<VARNAME>dh2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>J/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>10</SUB_ID>
<TITLE>mass flow rate at port 2</TITLE>
<VARNAME>dm2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>g/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>11</SUB_ID>
<TITLE>derivative of volume at port 2</TITLE>
<VARNAME>dvol2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>L/min</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
<EVAR>
<SUB_ID>12</SUB_ID>
<TITLE>volume at port 2</TITLE>
<VARNAME>vol2</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>cm**3</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
</PORT>
<PORT>
<EVAR>
<SUB_ID>13</SUB_ID>
<VARNAME>temp3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>0</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>14</SUB_ID>
<VARNAME>press3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>1</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>15</SUB_ID>
<TITLE>enthalpy flow rate at port 3</TITLE>
<VARNAME>dh3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>J/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>16</SUB_ID>
<TITLE>mass flow rate at port 3</TITLE>
<VARNAME>dm3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>g/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>17</SUB_ID>
<TITLE>derivative of volume at port 3</TITLE>
<VARNAME>dvol3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>L/min</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
<EVAR>
<SUB_ID>18</SUB_ID>
<TITLE>volume at port 3</TITLE>
<VARNAME>vol3</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>cm**3</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
</PORT>
<PORT>
<EVAR>
<SUB_ID>19</SUB_ID>
<VARNAME>temp4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>0</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>20</SUB_ID>
<VARNAME>press4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>4</TYPE>
<PRIMARY_PORT>0</PRIMARY_PORT>
<PRIMARY_VAR>1</PRIMARY_VAR>
<DUP_TYPE>0</DUP_TYPE>
</EVAR>
<EVAR>
<SUB_ID>21</SUB_ID>
<TITLE>enthalpy flow rate at port 4</TITLE>
<VARNAME>dh4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>J/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>22</SUB_ID>
<TITLE>mass flow rate at port 4</TITLE>
<VARNAME>dm4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>1</IO>
<UNITS>g/s</UNITS>
</EVAR>
<EVAR>
<SUB_ID>23</SUB_ID>
<TITLE>derivative of volume at port 4</TITLE>
<VARNAME>dvol4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>L/min</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
<EVAR>
<SUB_ID>24</SUB_ID>
<TITLE>volume at port 4</TITLE>
<VARNAME>vol4</VARNAME>
<VISIBILITY>True</VISIBILITY>
<TYPE>0</TYPE>
<DIMENSION>1</DIMENSION>
<IO>3</IO>
<UNITS>cm**3</UNITS>
<DEF_VALUE>0</DEF_VALUE>
</EVAR>
</PORT>
</EVARS_LIST>
<SUBIDS_RESET>0</SUBIDS_RESET>
</SUBMODEL>
</SPE>