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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<?xml version="1.0" encoding="ISO-8859-1"?>
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<!DOCTYPE SPE>
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<SPE DOC_VERSION="2" AME_VERSION="14.0.0 - 42489-40361 2015">
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<SUBMODEL>
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<SUB_TYPE>0</SUB_TYPE>
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<SUB_ID_MAX>18</SUB_ID_MAX>
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<DEFAULT_ICON>p2port</DEFAULT_ICON>
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<SUB_LABEL>Friction submodel of pneumatic pipe (R)</SUB_LABEL>
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<SUB_UNIT>0</SUB_UNIT>
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<R_STORES_NUMBER>5</R_STORES_NUMBER>
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<I_STORES_NUMBER>1</I_STORES_NUMBER>
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<OUTPUT_TYPE>1</OUTPUT_TYPE>
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<RPARAMS_LIST>
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<RPARAM>
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<SUB_ID>13</SUB_ID>
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<TITLE>diameter of pipe</TITLE>
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<VARNAME>diam</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<DEF_VALUE>1.00000000000000e+01</DEF_VALUE>
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<VALUE>1.00000000000000e+01</VALUE>
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<MIN_VALUE>1.00000000000000e-003</MIN_VALUE>
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<MAX_VALUE>1.00000000000000e+007</MAX_VALUE>
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<UNITS>mm</UNITS>
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</RPARAM>
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<RPARAM>
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<SUB_ID>14</SUB_ID>
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<TITLE>pipe length</TITLE>
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<VARNAME>le</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<DEF_VALUE>1.00000000000000e+00</DEF_VALUE>
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<VALUE>1.00000000000000e+00</VALUE>
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<MIN_VALUE>1.00000000000000e-006</MIN_VALUE>
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<MAX_VALUE>1.00000000000000e+004</MAX_VALUE>
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<UNITS>m</UNITS>
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</RPARAM>
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<RPARAM>
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<SUB_ID>15</SUB_ID>
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<TITLE>relative roughness</TITLE>
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<VARNAME>rr</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<DEF_VALUE>1.00000000000000e-05</DEF_VALUE>
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<VALUE>1.00000000000000e-05</VALUE>
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<MIN_VALUE>0.00000000000000e+000</MIN_VALUE>
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<MAX_VALUE>1.00000000000000e-001</MAX_VALUE>
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<UNITS>null</UNITS>
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</RPARAM>
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</RPARAMS_LIST>
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<IPARAMS_LIST>
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<IPARAM>
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<SUB_ID>16</SUB_ID>
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<TITLE>gas type index</TITLE>
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<VARNAME>gi</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<DEF_VALUE>1</DEF_VALUE>
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<VALUE>1</VALUE>
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<MIN_VALUE>1</MIN_VALUE>
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<MAX_VALUE>99</MAX_VALUE>
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</IPARAM>
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</IPARAMS_LIST>
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<IVARS_LIST>
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<IVAR>
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<SUB_ID>9</SUB_ID>
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<TITLE>Reynolds number</TITLE>
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<VARNAME>re</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<UNITS>null</UNITS>
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</IVAR>
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<IVAR>
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<SUB_ID>10</SUB_ID>
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<TITLE>mass flow parameter (cm)</TITLE>
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<VARNAME>cm</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<UNITS>(kg*K/J)**(1/2)</UNITS>
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</IVAR>
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<IVAR>
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<SUB_ID>11</SUB_ID>
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<TITLE>mean gas velocity</TITLE>
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<VARNAME>v</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<UNITS>m/s</UNITS>
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</IVAR>
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<IVAR>
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<SUB_ID>12</SUB_ID>
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<TITLE>friction factor</TITLE>
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<VARNAME>ff</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<UNITS>null</UNITS>
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</IVAR>
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</IVARS_LIST>
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<EVARS_LIST>
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<PORT>
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<EVAR>
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<SUB_ID>17</SUB_ID>
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<VARNAME>dh1</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>4</TYPE>
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<PRIMARY_PORT>1</PRIMARY_PORT>
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<PRIMARY_VAR>0</PRIMARY_VAR>
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<DUP_TYPE>1</DUP_TYPE>
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</EVAR>
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<EVAR>
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<SUB_ID>18</SUB_ID>
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<VARNAME>dm1</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>4</TYPE>
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<PRIMARY_PORT>1</PRIMARY_PORT>
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<PRIMARY_VAR>1</PRIMARY_VAR>
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<DUP_TYPE>1</DUP_TYPE>
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</EVAR>
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<EVAR>
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<SUB_ID>3</SUB_ID>
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<TITLE>temperature at port 1</TITLE>
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<VARNAME>t1</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>1</IO>
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<UNITS>K</UNITS>
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</EVAR>
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<EVAR>
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<SUB_ID>4</SUB_ID>
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<TITLE>pressure at port 1</TITLE>
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<VARNAME>p1</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>1</IO>
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<UNITS>Pa</UNITS>
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</EVAR>
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</PORT>
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<PORT>
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<EVAR>
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<SUB_ID>5</SUB_ID>
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<TITLE>enthalpy flow rate at port 2</TITLE>
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<VARNAME>dh2</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>2</IO>
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<UNITS>J/s</UNITS>
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</EVAR>
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<EVAR>
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<SUB_ID>6</SUB_ID>
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<TITLE>mass flow rate at port 2</TITLE>
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<VARNAME>dm2</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>2</IO>
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<UNITS>g/s</UNITS>
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</EVAR>
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<EVAR>
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<SUB_ID>7</SUB_ID>
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<TITLE>temperature at port 2</TITLE>
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<VARNAME>t2</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>1</IO>
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<UNITS>K</UNITS>
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</EVAR>
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<EVAR>
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<SUB_ID>8</SUB_ID>
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<TITLE>pressure at port 2</TITLE>
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<VARNAME>p2</VARNAME>
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<VISIBILITY>True</VISIBILITY>
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<TYPE>0</TYPE>
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<DIMENSION>1</DIMENSION>
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<IO>1</IO>
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<UNITS>Pa</UNITS>
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</EVAR>
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</PORT>
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</EVARS_LIST>
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<SUBIDS_RESET>0</SUBIDS_RESET>
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</SUBMODEL>
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</SPE>
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