def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.reactions = SaponificationReactionParameterBlock(
default={"property_package": m.fs.properties})
m.fs.unit = StoichiometricReactor(
default={
"property_package": m.fs.properties,
"reaction_package": m.fs.reactions,
"has_heat_transfer": True,
"has_heat_of_reaction": True,
"has_pressure_change": True
})
m.fs.unit.inlet.flow_vol.fix(1)
m.fs.unit.inlet.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.inlet.temperature.fix(303.15)
m.fs.unit.inlet.pressure.fix(101325.0)
m.fs.unit.rate_reaction_extent[0, 'R1'].fix(90)
m.fs.unit.heat_duty.fix(0)
m.fs.unit.deltaP.fix(0)
return m
def model(self):
model = ConcreteModel()
model.pparams = SaponificationParameterBlock()
model.rparams = SaponificationReactionParameterBlock(
default={"property_package": model.pparams})
return model
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = PressureChanger(
default={
"property_package": m.fs.properties,
"thermodynamic_assumption": ThermodynamicAssumption.pump,
"compressor": False
})
m.fs.unit.inlet.flow_vol[0].fix(1e-3)
m.fs.unit.inlet.temperature[0].fix(320)
m.fs.unit.inlet.pressure[0].fix(101325)
m.fs.unit.inlet.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.deltaP.fix(-20000)
m.fs.unit.efficiency_pump.fix(0.9)
iscale.calculate_scaling_factors(m)
return m
def model(self):
model = ConcreteModel()
model.params = SaponificationParameterBlock()
model.props = model.params.state_block_class(
[1], default={"parameters": model.params})
return model
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = Feed(default={"property_package": m.fs.properties})
return m
def model(self):
model = ConcreteModel()
model.pparams = SaponificationParameterBlock()
model.rparams = SaponificationReactionParameterBlock(
default={"property_package": model.pparams})
model.props = model.pparams.build_state_block([1])
model.rxns = model.rparams.build_reaction_block(
[1], default={"state_block": model.props})
return model
def trans(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties1 = SaponificationParameterBlock()
m.fs.properties2 = BTXParameterBlock()
m.fs.unit = Translator(
default={"inlet_property_package": m.fs.properties1,
"outlet_property_package": m.fs.properties2})
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = PressureChanger(
default={
"property_package": m.fs.properties,
"thermodynamic_assumption": ThermodynamicAssumption.pump,
"compressor": False
})
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.reactions = SaponificationReactionParameterBlock(default={
"property_package": m.fs.properties})
m.fs.unit = StoichiometricReactor(default={
"property_package": m.fs.properties,
"reaction_package": m.fs.reactions,
"has_heat_transfer": True,
"has_heat_of_reaction": True,
"has_pressure_change": True})
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = HeatExchanger(
default={
"shell": {
"property_package": m.fs.properties
},
"tube": {
"property_package": m.fs.properties
},
"flow_pattern": HeatExchangerFlowPattern.crossflow
})
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = Product(default={"property_package": m.fs.properties})
m.fs.unit.flow_vol.fix(1.0e-03)
m.fs.unit.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.temperature.fix(303.15)
m.fs.unit.pressure.fix(101325.0)
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = Heater(default={"property_package": m.fs.properties})
m.fs.unit.inlet.flow_vol[0].fix(1e-3)
m.fs.unit.inlet.temperature[0].fix(320)
m.fs.unit.inlet.pressure[0].fix(101325)
m.fs.unit.inlet.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.heat_duty.fix(1000)
return m
def trans(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties1 = SaponificationParameterBlock()
m.fs.properties2 = BTXParameterBlock()
m.fs.unit = Translator(
default={
"inlet_property_package": m.fs.properties1,
"outlet_property_package": m.fs.properties2
})
m.fs.unit.inlet.flow_vol.fix(1.0e-03)
m.fs.unit.inlet.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet.conc_mol_comp[0, "Ethanol"].fix(0.0)
return m
def sapon(self):
m = ConcreteModel()
m.fs = FlowsheetBlock(default={"dynamic": False})
m.fs.properties = SaponificationParameterBlock()
m.fs.unit = HeatExchanger(
default={
"shell": {
"property_package": m.fs.properties
},
"tube": {
"property_package": m.fs.properties
},
"flow_pattern": HeatExchangerFlowPattern.crossflow
})
m.fs.unit.inlet_1.flow_vol[0].fix(1e-3)
m.fs.unit.inlet_1.temperature[0].fix(320)
m.fs.unit.inlet_1.pressure[0].fix(101325)
m.fs.unit.inlet_1.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet_1.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet_1.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet_1.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet_1.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.inlet_2.flow_vol[0].fix(1e-3)
m.fs.unit.inlet_2.temperature[0].fix(300)
m.fs.unit.inlet_2.pressure[0].fix(101325)
m.fs.unit.inlet_2.conc_mol_comp[0, "H2O"].fix(55388.0)
m.fs.unit.inlet_2.conc_mol_comp[0, "NaOH"].fix(100.0)
m.fs.unit.inlet_2.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
m.fs.unit.inlet_2.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
m.fs.unit.inlet_2.conc_mol_comp[0, "Ethanol"].fix(0.0)
m.fs.unit.area.fix(1000)
m.fs.unit.overall_heat_transfer_coefficient.fix(100)
m.fs.unit.crossflow_factor.fix(0.6)
return m
def test_build_defined_state(self):
model = ConcreteModel()
model.params = SaponificationParameterBlock()
model.props = model.params.build_state_block(
[1], default={"defined_state": True})
assert isinstance(model.props[1].flow_vol, Var)
assert value(model.props[1].flow_vol) == 1
assert isinstance(model.props[1].pressure, Var)
assert value(model.props[1].pressure) == 101325
assert isinstance(model.props[1].temperature, Var)
assert value(model.props[1].temperature) == 298.15
assert isinstance(model.props[1].conc_mol_comp, Var)
assert len(model.props[1].conc_mol_comp) == 5
for i in model.props[1].conc_mol_comp:
assert value(model.props[1].conc_mol_comp[i]) == 100
assert not hasattr(model.props[1], "conc_water_eqn")
def model(self):
model = ConcreteModel()
model.params = SaponificationParameterBlock()
return model