예제 #1
0
def test_build():
    m = ConcreteModel()
    m.fs = FlowsheetBlock(default={"dynamic": False})

    m.fs.properties = SaponificationParameterBlock()
    m.fs.reactions = SaponificationReactionParameterBlock(
        default={"property_package": m.fs.properties})

    m.fs.pfr = PFR(
        default={
            "property_package": m.fs.properties,
            "reaction_package": m.fs.reactions,
            "has_equilibrium_reactions": False,
            "has_heat_transfer": True,
            "has_pressure_change": True
        })

    assert hasattr(m.fs.pfr, "inlet")
    assert len(m.fs.pfr.inlet.vars) == 4
    assert hasattr(m.fs.pfr.inlet, "flow_vol")
    assert hasattr(m.fs.pfr.inlet, "conc_mol_comp")
    assert hasattr(m.fs.pfr.inlet, "temperature")
    assert hasattr(m.fs.pfr.inlet, "pressure")

    assert hasattr(m.fs.pfr, "outlet")
    assert len(m.fs.pfr.outlet.vars) == 4
    assert hasattr(m.fs.pfr.outlet, "flow_vol")
    assert hasattr(m.fs.pfr.outlet, "conc_mol_comp")
    assert hasattr(m.fs.pfr.outlet, "temperature")
    assert hasattr(m.fs.pfr.outlet, "pressure")

    assert hasattr(m.fs.pfr, "performance_eqn")
    assert hasattr(m.fs.pfr.control_volume, "heat")
    assert hasattr(m.fs.pfr, "heat_duty")
    assert hasattr(m.fs.pfr, "deltaP")
예제 #2
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def test_config():
    m = ConcreteModel()
    m.fs = FlowsheetBlock(default={"dynamic": False})

    m.fs.properties = PhysicalParameterTestBlock()
    m.fs.reactions = ReactionParameterTestBlock(
        default={"property_package": m.fs.properties})

    m.fs.unit = PFR(default={
        "property_package": m.fs.properties,
        "reaction_package": m.fs.reactions
    })

    # Check unit config arguments
    assert len(m.fs.unit.config) == 19

    assert m.fs.unit.config.material_balance_type == \
        MaterialBalanceType.componentPhase
    assert m.fs.unit.config.energy_balance_type == \
        EnergyBalanceType.enthalpyTotal
    assert m.fs.unit.config.momentum_balance_type == \
        MomentumBalanceType.pressureTotal
    assert not m.fs.unit.config.has_heat_transfer
    assert not m.fs.unit.config.has_pressure_change
    assert not m.fs.unit.config.has_equilibrium_reactions
    assert not m.fs.unit.config.has_phase_equilibrium
    assert not m.fs.unit.config.has_heat_of_reaction
    assert m.fs.unit.config.property_package is m.fs.properties
    assert m.fs.unit.config.reaction_package is m.fs.reactions

    assert m.fs.unit.config.length_domain_set == [0.0, 1.0]
    assert m.fs.unit.config.transformation_method == "dae.finite_difference"
    assert m.fs.unit.config.transformation_scheme == "BACKWARD"
    assert m.fs.unit.config.finite_elements == 20
    assert m.fs.unit.config.collocation_points == 3
예제 #3
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    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 = PFR(default={"property_package": m.fs.properties,
                                 "reaction_package": m.fs.reactions,
                                 "has_equilibrium_reactions": False,
                                 "has_heat_transfer": True,
                                 "has_heat_of_reaction": True,
                                 "has_pressure_change": True})

        return m
예제 #4
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def test_report():
    m = ConcreteModel()
    m.fs = FlowsheetBlock(default={"dynamic": False})

    m.fs.properties = SaponificationParameterBlock()
    m.fs.reactions = SaponificationReactionParameterBlock(
        default={"property_package": m.fs.properties})

    m.fs.pfr = PFR(
        default={
            "property_package": m.fs.properties,
            "reaction_package": m.fs.reactions,
            "has_equilibrium_reactions": False,
            "has_heat_transfer": False,
            "has_pressure_change": False
        })

    m.fs.pfr.report()
예제 #5
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def test_initialize():
    m = ConcreteModel()
    m.fs = FlowsheetBlock(default={"dynamic": False})

    m.fs.properties = SaponificationParameterBlock()
    m.fs.reactions = SaponificationReactionParameterBlock(
        default={"property_package": m.fs.properties})

    m.fs.pfr = PFR(
        default={
            "property_package": m.fs.properties,
            "reaction_package": m.fs.reactions,
            "has_equilibrium_reactions": False,
            "has_heat_transfer": False,
            "has_pressure_change": False
        })

    m.fs.pfr.inlet.flow_vol.fix(1.0)
    m.fs.pfr.inlet.conc_mol_comp[0, "H2O"].fix(55388.0)
    m.fs.pfr.inlet.conc_mol_comp[0, "NaOH"].fix(100.0)
    m.fs.pfr.inlet.conc_mol_comp[0, "EthylAcetate"].fix(100.0)
    m.fs.pfr.inlet.conc_mol_comp[0, "SodiumAcetate"].fix(0.0)
    m.fs.pfr.inlet.conc_mol_comp[0, "Ethanol"].fix(0.0)

    m.fs.pfr.inlet.temperature.fix(303.15)
    m.fs.pfr.inlet.pressure.fix(101325.0)

    m.fs.pfr.control_volume.length.fix(0.5)
    m.fs.pfr.control_volume.area.fix(0.1)

    assert degrees_of_freedom(m) == 0

    m.fs.pfr.initialize(outlvl=5, optarg={'tol': 1e-6})

    assert (pytest.approx(101325.0,
                          abs=1e-2) == m.fs.pfr.outlet.pressure[0].value)
    assert (pytest.approx(303.15,
                          abs=1e-2) == m.fs.pfr.outlet.temperature[0].value)