def test_initialize(self, RO_frame):
     initialization_tester(RO_frame)
    def test_CP_calculation_with_kf_fixed(self):
        """ Testing 0D-RO with ConcentrationPolarizationType.calculated option enabled.
        This option makes use of an alternative constraint for the feed-side, membrane-interface concentration.
        Additionally, two more variables are created when this option is enabled: Kf_io - feed-channel
        mass transfer coefficients at the channel inlet and outlet.
        """
        m = ConcreteModel()
        m.fs = FlowsheetBlock(default={"dynamic": False})

        m.fs.properties = props.NaClParameterBlock()

        m.fs.unit = ReverseOsmosis0D(
            default={
                "property_package": m.fs.properties,
                "has_pressure_change": True,
                "concentration_polarization_type":
                ConcentrationPolarizationType.calculated,
                "mass_transfer_coefficient": MassTransferCoefficient.fixed
            })

        # fully specify system
        feed_flow_mass = 1
        feed_mass_frac_NaCl = 0.035
        feed_pressure = 50e5
        feed_temperature = 273.15 + 25
        membrane_pressure_drop = 3e5
        membrane_area = 50
        A = 4.2e-12
        B = 3.5e-8
        pressure_atmospheric = 101325
        kf = 2e-5

        feed_mass_frac_H2O = 1 - feed_mass_frac_NaCl
        m.fs.unit.inlet.flow_mass_phase_comp[0, 'Liq', 'NaCl'].fix(
            feed_flow_mass * feed_mass_frac_NaCl)
        m.fs.unit.inlet.flow_mass_phase_comp[0, 'Liq', 'H2O'].fix(
            feed_flow_mass * feed_mass_frac_H2O)
        m.fs.unit.inlet.pressure[0].fix(feed_pressure)
        m.fs.unit.inlet.temperature[0].fix(feed_temperature)
        m.fs.unit.deltaP.fix(-membrane_pressure_drop)
        m.fs.unit.area.fix(membrane_area)
        m.fs.unit.A_comp.fix(A)
        m.fs.unit.B_comp.fix(B)
        m.fs.unit.permeate.pressure[0].fix(pressure_atmospheric)
        m.fs.unit.Kf_io[0, 'in', 'NaCl'].fix(kf)
        m.fs.unit.Kf_io[0, 'out', 'NaCl'].fix(kf)

        # test statistics
        assert number_variables(m) == 94
        assert number_total_constraints(m) == 65
        assert number_unused_variables(
            m) == 7  # vars from property package parameters

        # test degrees of freedom
        assert degrees_of_freedom(m) == 0

        # test scaling
        m.fs.properties.set_default_scaling('flow_mass_phase_comp',
                                            1,
                                            index=('Liq', 'H2O'))
        m.fs.properties.set_default_scaling('flow_mass_phase_comp',
                                            1e2,
                                            index=('Liq', 'NaCl'))
        calculate_scaling_factors(m)

        # check that all variables have scaling factors.
        # TODO: Setting the "include_fixed" arg as True reveals
        #  unscaled vars that weren't being accounted for previously. However, calling the whole block (i.e.,
        #  m) shows that several NaCl property parameters are unscaled. For now, we are just interested in ensuring
        #  unit variables are scaled (hence, calling m.fs.unit) but might need to revisit scaling and associated
        #  testing for property models.

        unscaled_var_list = list(
            unscaled_variables_generator(m.fs.unit, include_fixed=True))
        assert len(unscaled_var_list) == 0

        # check that all constraints have been scaled
        unscaled_constraint_list = list(unscaled_constraints_generator(m))
        assert len(unscaled_constraint_list) == 0

        # test initialization
        initialization_tester(m)

        # test variable scaling
        badly_scaled_var_lst = list(badly_scaled_var_generator(m))
        assert badly_scaled_var_lst == []

        # test solve
        solver.options = {'nlp_scaling_method': 'user-scaling'}
        results = solver.solve(m)

        # Check for optimal solution
        assert results.solver.termination_condition == \
               TerminationCondition.optimal
        assert results.solver.status == SolverStatus.ok

        # test solution
        assert (pytest.approx(3.807e-3, rel=1e-3) == value(
            m.fs.unit.flux_mass_phase_comp_avg[0, 'Liq', 'H2O']))
        assert (pytest.approx(1.668e-6, rel=1e-3) == value(
            m.fs.unit.flux_mass_phase_comp_avg[0, 'Liq', 'NaCl']))
        assert (pytest.approx(0.1904, rel=1e-3) == value(
            m.fs.unit.properties_permeate[0].flow_mass_phase_comp['Liq',
                                                                  'H2O']))
        assert (pytest.approx(8.342e-5, rel=1e-3) == value(
            m.fs.unit.properties_permeate[0].flow_mass_phase_comp['Liq',
                                                                  'NaCl']))
        assert (pytest.approx(35.751, rel=1e-3) == value(
            m.fs.unit.feed_side.properties_in[0].conc_mass_phase_comp['Liq',
                                                                      'NaCl']))
        assert (pytest.approx(46.123, rel=1e-3) == value(
            m.fs.unit.feed_side.properties_interface_in[0].
            conc_mass_phase_comp['Liq', 'NaCl']))
        assert (pytest.approx(44.321, rel=1e-3) == value(
            m.fs.unit.feed_side.properties_out[0].conc_mass_phase_comp['Liq',
                                                                       'NaCl'])
                )
        assert (pytest.approx(50.081, rel=1e-3) == value(
            m.fs.unit.feed_side.properties_interface_out[0].
            conc_mass_phase_comp['Liq', 'NaCl']))
 def test_initialize(self, model):
     initialization_tester(model)
Example #4
0
 def test_initialize(self, iapws):
     initialization_tester(iapws)
Example #5
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 def test_initialize(self, btx):
     initialization_tester(btx)
Example #6
0
 def test_initialize(self, sapon):
     initialization_tester(sapon)
def test_initialize(solid_prop):
    initialization_tester(
            solid_prop)