Changes between Version 1 and Version 2 of Ticket #6199, comment 9


Ignore:
Timestamp:
2021-03-02T17:07:36Z (4 years ago)
Author:
Karim Adbdelhak

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  • Ticket #6199, comment 9

    v1 v2  
    4141
    4242---- involved set vars (28):
    43   (1):  pum.eff.hydDer[1]:VARIABLE(fixed = false protected = true final = true )  "Coefficients for polynomial of hydraulic efficiency vs. volume flow rate" type: Real [1]
    44   (2):  pum.eff.motDer[1]:VARIABLE(fixed = false protected = true final = true )  "Coefficients for polynomial of motor efficiency vs. volume flow rate" type: Real [1]
    45   (3):  pum.filter.r[2]:VARIABLE(fixed = false protected = true )  type: Real [2]
    46   (4):  pum.filter.r[1]:VARIABLE(fixed = false protected = true )  type: Real [2]
    47   (5):  pum.filter.cr[2]:VARIABLE(fixed = false protected = true )  type: Real [2]
    48   (6):  pum.filter.cr[1]:VARIABLE(fixed = false protected = true )  type: Real [2]
    49   (7):  pla.hea.eva.sta_start.T:VARIABLE(min = 1.0 max = 10000.0 start = 293.15 unit = "K" fixed = false nominal = 300.0 protected = true )  "Temperature of medium" type: Real
    50   (8):  pla.hea.eva.sta_start.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
    51   (9):  pla.hea.eva.h_outflow_start:VARIABLE(unit = "J/kg" protected = true )  = 1006.0 * (-273.15 + pla.hea.eva.sta_start.T) * (1.0 - pla.hea.eva.sta_start.X[1]) + (2501014.5 + 1860.0 * (-273.15 + pla.hea.eva.sta_start.T)) * pla.hea.eva.sta_start.X[1]  "Start value for outflowing enthalpy" type: Real
    52   (10): pla.hea.eva.sta_start.X[2]:VARIABLE(min = 0.0 max = 1.0 start = 0.99 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
    53   (11): pla.coo.con.sta_start.T:VARIABLE(min = 1.0 max = 10000.0 start = 293.15 unit = "K" fixed = false nominal = 300.0 protected = true )  "Temperature of medium" type: Real
    54   (12): pla.coo.con.sta_start.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
    55   (13): pla.coo.con.h_outflow_start:VARIABLE(unit = "J/kg" protected = true )  = 1006.0 * (-273.15 + pla.coo.con.sta_start.T) * (1.0 - pla.coo.con.sta_start.X[1]) + (2501014.5 + 1860.0 * (-273.15 + pla.coo.con.sta_start.T)) * pla.coo.con.sta_start.X[1]  "Start value for outflowing enthalpy" type: Real
    56   (14): pla.coo.con.sta_start.X[2]:VARIABLE(min = 0.0 max = 1.0 start = 0.99 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
    57   (37): pum.filter.y:VARIABLE(flow=false min = max(-min(100000.0, 100000.0), max(max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-9.999999999999999e+59, -9.999999999999999e+59)))))))))))))))))))))))))), max(max(-100000.0, max(-9.999999999999999e+59, -100000.0)), max(-9.999999999999999e+59, max(-9.999999999999999e+59, -9.999999999999999e+59))))) max = min(-max(-100000.0, -100000.0), min(min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(100000.0, min(9.999999999999999e+59, min(100000.0, 100000.0)))))))))))))))))))))))))), min(min(100000.0, min(100000.0, 100000.0)), min(100000.0, min(100000.0, 100000.0))))) start = 0.0 unit = "kg/s" nominal = pum.m_flow_nominal protected = true )  "Connector of Real output signal" type: Real
    58   (55): vol.dynBal.medium.T_degC:VARIABLE(unit = "degC" protected = true )  "Temperature of medium in [degC]" type: Real
    59   (56): vol.dynBal.medium.T:VARIABLE(min = max(1.0, 1.0) max = min(10000.0, 10000.0) start = 293.15 unit = "K" nominal = 300.0 protected = true )  "Temperature of medium" type: Real
    60   (58): vol.ports[1].h_outflow:VARIABLE(min = max(max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))), max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))))) max = min(min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))), min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))))) start = pum.h_outflow_start unit = "J/kg" nominal = 1000000.0 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [2]
    61   (106):        pla.hea.con.outCon.hSet:VARIABLE(unit = "J/kg" protected = true )  "Set point for enthalpy leaving port_b" type: Real
    62   (109):        pla.hea.con.preDro.dp:VARIABLE(start = 0.0 unit = "Pa" nominal = 30000.0 protected = true )  "Pressure difference between port_a and port_b" type: Real
    63   (110):        pla.hea.con.preDro.port_b.h_outflow:VARIABLE(min = -10000000000.0 max = 10000000000.0 start = 83680.0 unit = "J/kg" nominal = 83680.0 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
    64   (159):        pla.coo.con.vol.dynBal.medium.T_degC:VARIABLE(start = 20.0 unit = "degC" protected = true final = true )  "Temperature of medium in [degC]" type: Real
    65   (163):        pla.coo.con.vol.dynBal.medium.T:VARIABLE(min = max(1.0, 1.0) max = min(10000.0, 10000.0) start = 293.15 unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of medium" type: Real
    66   (166):        pla.coo.con.vol.dynBal.medium.p:DUMMY_STATE(flow=false min = 0.0 start = pla.coo.con.vol.dynBal.p_start unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.never protected = true )  "Absolute pressure of medium" type: Real
    67   (185):        pla.coo.sta_a1.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
    68   (189):        $START.pla.coo.port_b1.h_outflow:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))) unit = "J/kg" fixed = false nominal = 45300.945 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
    69   (190):        pla.coo.port_b1.h_outflow:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))) start = pla.coo.con.h_outflow_start unit = "J/kg" nominal = 45300.945 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
    70   (198):        pla.sta_b.p:VARIABLE(min = max(max(0.0, 0.0), max(max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))), max(max(0.0, 0.0), max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))))))))))) max = min(min(100000000.0, 100000000.0), min(min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))), min(min(100000000.0, 100000000.0), min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))))))))))) start = 300000.0 unit = "Pa" nominal = 100000.0 )  "Absolute pressure of medium" type: Real
     43  1:    pum.eff.hydDer[1]:VARIABLE(fixed = false protected = true final = true )  "Coefficients for polynomial of hydraulic efficiency vs. volume flow rate" type: Real [1]
     44  2:    pum.eff.motDer[1]:VARIABLE(fixed = false protected = true final = true )  "Coefficients for polynomial of motor efficiency vs. volume flow rate" type: Real [1]
     45  3:    pum.filter.r[2]:VARIABLE(fixed = false protected = true )  type: Real [2]
     46  4:    pum.filter.r[1]:VARIABLE(fixed = false protected = true )  type: Real [2]
     47  5:    pum.filter.cr[2]:VARIABLE(fixed = false protected = true )  type: Real [2]
     48  6:    pum.filter.cr[1]:VARIABLE(fixed = false protected = true )  type: Real [2]
     49  7:    pla.hea.eva.sta_start.T:VARIABLE(min = 1.0 max = 10000.0 start = 293.15 unit = "K" fixed = false nominal = 300.0 protected = true )  "Temperature of medium" type: Real
     50  8:    pla.hea.eva.sta_start.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
     51  9:    pla.hea.eva.h_outflow_start:VARIABLE(unit = "J/kg" protected = true )  = 1006.0 * (-273.15 + pla.hea.eva.sta_start.T) * (1.0 - pla.hea.eva.sta_start.X[1]) + (2501014.5 + 1860.0 * (-273.15 + pla.hea.eva.sta_start.T)) * pla.hea.eva.sta_start.X[1]  "Start value for outflowing enthalpy" type: Real
     52  10:   pla.hea.eva.sta_start.X[2]:VARIABLE(min = 0.0 max = 1.0 start = 0.99 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
     53  11:   pla.coo.con.sta_start.T:VARIABLE(min = 1.0 max = 10000.0 start = 293.15 unit = "K" fixed = false nominal = 300.0 protected = true )  "Temperature of medium" type: Real
     54  12:   pla.coo.con.sta_start.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
     55  13:   pla.coo.con.h_outflow_start:VARIABLE(unit = "J/kg" protected = true )  = 1006.0 * (-273.15 + pla.coo.con.sta_start.T) * (1.0 - pla.coo.con.sta_start.X[1]) + (2501014.5 + 1860.0 * (-273.15 + pla.coo.con.sta_start.T)) * pla.coo.con.sta_start.X[1]  "Start value for outflowing enthalpy" type: Real
     56  14:   pla.coo.con.sta_start.X[2]:VARIABLE(min = 0.0 max = 1.0 start = 0.99 unit = "kg/kg" fixed = false nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
     57  37:   pum.filter.y:VARIABLE(flow=false min = max(-min(100000.0, 100000.0), max(max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-100000.0, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-9.999999999999999e+59, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-100000.0, max(-9.999999999999999e+59, -9.999999999999999e+59)))))))))))))))))))))))))), max(max(-100000.0, max(-9.999999999999999e+59, -100000.0)), max(-9.999999999999999e+59, max(-9.999999999999999e+59, -9.999999999999999e+59))))) max = min(-max(-100000.0, -100000.0), min(min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(100000.0, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(9.999999999999999e+59, min(100000.0, min(9.999999999999999e+59, min(100000.0, 100000.0)))))))))))))))))))))))))), min(min(100000.0, min(100000.0, 100000.0)), min(100000.0, min(100000.0, 100000.0))))) start = 0.0 unit = "kg/s" nominal = pum.m_flow_nominal protected = true )  "Connector of Real output signal" type: Real
     58  55:   vol.dynBal.medium.T_degC:VARIABLE(unit = "degC" protected = true )  "Temperature of medium in [degC]" type: Real
     59  56:   vol.dynBal.medium.T:VARIABLE(min = max(1.0, 1.0) max = min(10000.0, 10000.0) start = 293.15 unit = "K" nominal = 300.0 protected = true )  "Temperature of medium" type: Real
     60  58:   vol.ports[1].h_outflow:VARIABLE(min = max(max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))), max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0)))))) max = min(min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))), min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0)))))) start = pum.h_outflow_start unit = "J/kg" nominal = 1000000.0 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [2]
     61  106:  pla.hea.con.outCon.hSet:VARIABLE(unit = "J/kg" protected = true )  "Set point for enthalpy leaving port_b" type: Real
     62  109:  pla.hea.con.preDro.dp:VARIABLE(start = 0.0 unit = "Pa" nominal = 30000.0 protected = true )  "Pressure difference between port_a and port_b" type: Real
     63  110:  pla.hea.con.preDro.port_b.h_outflow:VARIABLE(min = -10000000000.0 max = 10000000000.0 start = 83680.0 unit = "J/kg" nominal = 83680.0 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
     64  159:  pla.coo.con.vol.dynBal.medium.T_degC:VARIABLE(start = 20.0 unit = "degC" protected = true final = true )  "Temperature of medium in [degC]" type: Real
     65  163:  pla.coo.con.vol.dynBal.medium.T:VARIABLE(min = max(1.0, 1.0) max = min(10000.0, 10000.0) start = 293.15 unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of medium" type: Real
     66  166:  pla.coo.con.vol.dynBal.medium.p:DUMMY_STATE(flow=false min = 0.0 start = pla.coo.con.vol.dynBal.p_start unit = "Pa" nominal = 100000.0 stateSelect=StateSelect.never protected = true )  "Absolute pressure of medium" type: Real
     67  185:  pla.coo.sta_a1.X[1]:VARIABLE(min = 0.0 max = 1.0 start = 0.01 unit = "kg/kg" nominal = 0.1 protected = true )  "Mass fractions (= (component mass)/total mass  m_i/m)" type: Real [2]
     68  189:  $START.pla.coo.port_b1.h_outflow:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))) unit = "J/kg" fixed = false nominal = 45300.945 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
     69  190:  pla.coo.port_b1.h_outflow:VARIABLE(min = max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, max(-10000000000.0, -10000000000.0))))) max = min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, min(10000000000.0, 10000000000.0))))) start = pla.coo.con.h_outflow_start unit = "J/kg" nominal = 45300.945 protected = true )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real
     70  198:  pla.sta_b.p:VARIABLE(min = max(max(0.0, 0.0), max(max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))), max(max(0.0, 0.0), max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, max(0.0, 0.0))))))))))))))))))) max = min(min(100000000.0, 100000000.0), min(min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))), min(min(100000000.0, 100000000.0), min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, min(100000000.0, 100000000.0))))))))))))))))))) start = 300000.0 unit = "Pa" nominal = 100000.0 )  "Absolute pressure of medium" type: Real
    7171--------------------------------------------------
    7272}}}