#################################################################################
# WaterTAP Copyright (c) 2020-2023, The Regents of the University of California,
# through Lawrence Berkeley National Laboratory, Oak Ridge National Laboratory,
# National Renewable Energy Laboratory, and National Energy Technology
# Laboratory (subject to receipt of any required approvals from the U.S. Dept.
# of Energy). All rights reserved.
#
# Please see the files COPYRIGHT.md and LICENSE.md for full copyright and license
# information, respectively. These files are also available online at the URL
# "https://github.com/watertap-org/watertap/"
#################################################################################
"""
Tests for zero-order anaerobic MBR-MEC model
"""
import pytest

from pyomo.environ import (
    ConcreteModel,
    Constraint,
    value,
    Var,
    assert_optimal_termination,
    units as pyunits,
    Block,
    Param,
)
from pyomo.util.check_units import assert_units_consistent

from idaes.core import FlowsheetBlock
from idaes.core.solvers import get_solver
from idaes.core.util.model_statistics import degrees_of_freedom
from idaes.core.util.testing import initialization_tester
from idaes.core import UnitModelCostingBlock

from watertap.unit_models.zero_order import AnaerobicMBRMECZO
from watertap.core.wt_database import Database
from watertap.core.zero_order_properties import WaterParameterBlock
from watertap.core.zero_order_costing import ZeroOrderCosting

solver = get_solver()


class TestAnaerobicMBRMECZO:
    @pytest.fixture(scope="class")
    def model(self):
        m = ConcreteModel()
        m.db = Database()

        m.fs = FlowsheetBlock(dynamic=False)
        m.fs.params = WaterParameterBlock(
            solute_list=[
                "cod",
                "nonbiodegradable_cod",
                "ammonium_as_nitrogen",
                "phosphate_as_phosphorous",
            ]
        )

        m.fs.unit = AnaerobicMBRMECZO(property_package=m.fs.params, database=m.db)

        m.fs.unit.inlet.flow_mass_comp[0, "H2O"].fix(0.043642594)
        m.fs.unit.inlet.flow_mass_comp[0, "cod"].fix(1.00625e-4)
        m.fs.unit.inlet.flow_mass_comp[0, "nonbiodegradable_cod"].fix(1e-20)
        m.fs.unit.inlet.flow_mass_comp[0, "ammonium_as_nitrogen"].fix(4.59375e-06)
        m.fs.unit.inlet.flow_mass_comp[0, "phosphate_as_phosphorous"].fix(2.1875e-06)

        return m

    @pytest.mark.unit
    def test_build(self, model):
        assert model.fs.unit.config.database == model.db

        assert isinstance(model.fs.unit.lift_height, Param)
        assert isinstance(model.fs.unit.eta_pump, Param)
        assert isinstance(model.fs.unit.eta_motor, Param)
        assert isinstance(model.fs.unit.electricity, Var)
        assert isinstance(model.fs.unit.electricity_consumption, Constraint)

    @pytest.mark.component
    def test_load_parameters(self, model):
        data = model.db.get_unit_operation_parameters("anaerobic_mbr_mec")

        model.fs.unit.load_parameters_from_database(use_default_removal=True)

        assert model.fs.unit.recovery_frac_mass_H2O[0].fixed
        assert (
            model.fs.unit.recovery_frac_mass_H2O[0].value
            == data["recovery_frac_mass_H2O"]["value"]
        )

        for (t, j), v in model.fs.unit.removal_frac_mass_comp.items():
            assert v.fixed
            if j not in data["removal_frac_mass_comp"].keys():
                assert v.value == data["default_removal_frac_mass_comp"]["value"]
            else:
                assert v.value == data["removal_frac_mass_comp"][j]["value"]

    @pytest.mark.component
    def test_degrees_of_freedom(self, model):
        assert degrees_of_freedom(model.fs.unit) == 0

    @pytest.mark.component
    def test_unit_consistency(self, model):
        assert_units_consistent(model.fs.unit)

    @pytest.mark.component
    def test_initialize(self, model):
        initialization_tester(model)

    @pytest.mark.solver
    @pytest.mark.skipif(solver is None, reason="Solver not available")
    @pytest.mark.component
    def test_solve(self, model):
        results = solver.solve(model)

        # Check for optimal solution
        assert_optimal_termination(results)

    @pytest.mark.solver
    @pytest.mark.skipif(solver is None, reason="Solver not available")
    @pytest.mark.component
    def test_solution(self, model):
        assert pytest.approx(3780 / 3600 / 24 / 1000, rel=1e-5) == value(
            model.fs.unit.properties_in[0].flow_vol
        )
        assert pytest.approx(2.3, rel=1e-5) == value(
            model.fs.unit.properties_in[0].conc_mass_comp["cod"]
        )
        assert pytest.approx(0, rel=1e-5) == value(
            model.fs.unit.properties_in[0].conc_mass_comp["nonbiodegradable_cod"]
        )
        assert pytest.approx(0.105, rel=1e-5) == value(
            model.fs.unit.properties_in[0].conc_mass_comp["ammonium_as_nitrogen"]
        )
        assert pytest.approx(0.05, rel=1e-5) == value(
            model.fs.unit.properties_in[0].conc_mass_comp["phosphate_as_phosphorous"]
        )

        assert pytest.approx(1500 / 3600 / 24 / 1000, rel=1e-2) == value(
            model.fs.unit.properties_treated[0].flow_vol
        )
        assert pytest.approx(2.895771, rel=1e-5) == value(
            model.fs.unit.properties_treated[0].conc_mass_comp["cod"]
        )
        assert pytest.approx(1.5972836e-09, rel=1e-5) == value(
            model.fs.unit.properties_treated[0].conc_mass_comp["nonbiodegradable_cod"]
        )

        assert pytest.approx(2280 / 3600 / 24 / 1000, rel=1e-2) == value(
            model.fs.unit.properties_byproduct[0].flow_vol
        )
        assert pytest.approx(1.0521862e-09, rel=1e-5) == value(
            model.fs.unit.properties_byproduct[0].conc_mass_comp["cod"]
        )
        assert pytest.approx(1.907545, rel=1e-5) == value(
            model.fs.unit.properties_byproduct[0].conc_mass_comp["nonbiodegradable_cod"]
        )
        assert pytest.approx(4.347, rel=1e-3) == value(
            pyunits.convert(
                model.fs.unit.properties_byproduct[0].flow_mass_comp[
                    "nonbiodegradable_cod"
                ],
                to_units=pyunits.kg / pyunits.day,
            )
        )
        assert pytest.approx(0.0161213, rel=1e-5) == value(model.fs.unit.electricity[0])

    @pytest.mark.solver
    @pytest.mark.skipif(solver is None, reason="Solver not available")
    @pytest.mark.component
    def test_conservation(self, model):
        for j in model.fs.params.component_list:
            assert 1e-6 >= abs(
                value(
                    model.fs.unit.inlet.flow_mass_comp[0, j]
                    + sum(
                        model.fs.unit.generation_rxn_comp[0, r, j]
                        for r in model.fs.unit.reaction_set
                    )
                    - model.fs.unit.treated.flow_mass_comp[0, j]
                    - model.fs.unit.byproduct.flow_mass_comp[0, j]
                )
            )

    @pytest.mark.component
    def test_report(self, model):
        model.fs.unit.report()


db = Database()
params = db._get_technology("anaerobic_mbr_mec")


class Test_AnMBRMEC_ZO_subtype:
    @pytest.fixture(scope="class")
    def model(self):
        m = ConcreteModel()

        m.fs = FlowsheetBlock(dynamic=False)
        m.fs.params = WaterParameterBlock(solute_list=["cod", "nonbiodegradable_cod"])

        m.fs.unit = AnaerobicMBRMECZO(property_package=m.fs.params, database=db)

        return m

    @pytest.mark.parametrize("subtype", [params.keys()])
    @pytest.mark.component
    def test_load_parameters(self, model, subtype):
        model.fs.unit.config.process_subtype = subtype
        data = db.get_unit_operation_parameters("anaerobic_mbr_mec", subtype=subtype)

        model.fs.unit.load_parameters_from_database()

        for (t, j), v in model.fs.unit.removal_frac_mass_comp.items():
            assert v.fixed
            assert v.value == data["removal_frac_mass_comp"][j]["value"]


@pytest.mark.unit
def test_ffCOD_not_in_solute_list():
    model = ConcreteModel()
    model.db = Database()

    model.fs = FlowsheetBlock(dynamic=False)
    model.fs.params = WaterParameterBlock(solute_list=["cod"])
    with pytest.raises(
        ValueError,
        match="nonbiodegradable_cod must be included in the solute list since"
        " this unit model converts cod to nonbiodegradable_cod.",
    ):
        model.fs.unit = AnaerobicMBRMECZO(
            property_package=model.fs.params, database=model.db
        )


@pytest.mark.unit
def test_COD_not_in_solute_list():
    model = ConcreteModel()
    model.db = Database()

    model.fs = FlowsheetBlock(dynamic=False)
    model.fs.params = WaterParameterBlock(solute_list=["nonbiodegradable_cod"])
    with pytest.raises(
        ValueError,
        match="fs.unit - key_reactant cod for reaction cod_to_nonbiodegradable_cod "
        "is not in the component list used by the assigned property package.",
    ):
        model.fs.unit = AnaerobicMBRMECZO(
            property_package=model.fs.params, database=model.db
        )


def test_costing():
    m = ConcreteModel()
    m.db = Database()

    m.fs = FlowsheetBlock(dynamic=False)

    m.fs.params = WaterParameterBlock(
        solute_list=[
            "cod",
            "nonbiodegradable_cod",
            "ammonium_as_nitrogen",
            "phosphate_as_phosphorous",
        ]
    )

    m.fs.costing = ZeroOrderCosting()

    m.fs.unit1 = AnaerobicMBRMECZO(property_package=m.fs.params, database=m.db)

    m.fs.unit1.inlet.flow_mass_comp[0, "H2O"].fix(0.043642594)
    m.fs.unit1.inlet.flow_mass_comp[0, "cod"].fix(1.00625e-4)
    m.fs.unit1.inlet.flow_mass_comp[0, "nonbiodegradable_cod"].fix(1e-20)
    m.fs.unit1.inlet.flow_mass_comp[0, "ammonium_as_nitrogen"].fix(4.59375e-06)
    m.fs.unit1.inlet.flow_mass_comp[0, "phosphate_as_phosphorous"].fix(2.1875e-06)

    m.fs.unit1.load_parameters_from_database(use_default_removal=True)
    assert degrees_of_freedom(m.fs.unit1) == 0

    m.fs.unit1.costing = UnitModelCostingBlock(flowsheet_costing_block=m.fs.costing)

    assert isinstance(m.fs.costing.anaerobic_mbr_mec, Block)
    assert isinstance(m.fs.costing.anaerobic_mbr_mec.unit_capex, Var)
    assert isinstance(m.fs.costing.anaerobic_mbr_mec.unit_opex, Var)
    assert isinstance(m.fs.unit1.costing.capital_cost, Var)
    assert isinstance(m.fs.unit1.costing.capital_cost_constraint, Constraint)

    assert_units_consistent(m.fs)
    assert degrees_of_freedom(m.fs.unit1) == 0

    assert m.fs.unit1.electricity[0] in m.fs.costing._registered_flows["electricity"]
