Source code for watertap.examples.flowsheets.full_treatment_train.flowsheet_components.translator_block

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# WaterTAP Copyright (c) 2021, 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/"
#
###############################################################################

"""Translator blocks for supported property packages"""

from pyomo.environ import Constraint
from idaes.models.unit_models.translator import Translator
from idaes.core.util.scaling import (
    calculate_scaling_factors,
    constraint_scaling_transform,
    get_scaling_factor,
)
from watertap.examples.flowsheets.full_treatment_train.model_components import (
    property_models,
)


[docs]def build_tb(m, base_inlet="ion", base_outlet="TDS", name_str=None): """ Build a translator block to convert for the specified base from inlet to outlet. """ if name_str is None: name_str = "tb_" + base_inlet + "_to_" + base_outlet if base_inlet not in ["ion", "salt"]: raise ValueError( "Unexpected property base inlet {base_inlet} for build_tb" "".format(base_inlet=base_inlet) ) prop_inlet = property_models.get_prop(m, base=base_inlet) if base_outlet not in ["TDS"]: raise ValueError( "Unexpected property base outlet {base_outlet} for build_tb" "".format(base_outlet=base_outlet) ) prop_outlet = property_models.get_prop(m, base=base_outlet) # build translator block setattr( m.fs, name_str, Translator( inlet_property_package=prop_inlet, outlet_property_package=prop_outlet ), ) blk = getattr(m.fs, name_str) # scale translator block to get scaling factors calculate_scaling_factors(blk) # add translator block constraints blk.eq_equal_temperature = Constraint( expr=blk.inlet.temperature[0] == blk.outlet.temperature[0] ) constraint_scaling_transform( blk.eq_equal_temperature, get_scaling_factor(blk.properties_in[0].temperature) ) blk.eq_equal_pressure = Constraint( expr=blk.inlet.pressure[0] == blk.outlet.pressure[0] ) constraint_scaling_transform( blk.eq_equal_pressure, get_scaling_factor(blk.properties_in[0].pressure) ) if base_inlet == "ion" and base_outlet == "TDS": blk.eq_H2O_balance = Constraint( expr=blk.inlet.flow_mass_phase_comp[0, "Liq", "H2O"] == blk.outlet.flow_mass_phase_comp[0, "Liq", "H2O"] ) constraint_scaling_transform( blk.eq_H2O_balance, get_scaling_factor( blk.properties_out[0].flow_mass_phase_comp["Liq", "H2O"] ), ) blk.eq_TDS_balance = Constraint( expr=sum( blk.inlet.flow_mass_phase_comp[0, "Liq", j] for j in ["Na", "Ca", "Mg", "SO4", "Cl"] ) == blk.outlet.flow_mass_phase_comp[0, "Liq", "TDS"] ) constraint_scaling_transform( blk.eq_TDS_balance, get_scaling_factor( blk.properties_out[0].flow_mass_phase_comp["Liq", "TDS"] ), ) elif base_inlet == "salt" and base_outlet == "TDS": blk.eq_H2O_balance = Constraint( expr=blk.inlet.flow_mass_phase_comp[0, "Liq", "H2O"] == blk.outlet.flow_mass_phase_comp[0, "Liq", "H2O"] ) constraint_scaling_transform( blk.eq_H2O_balance, get_scaling_factor( blk.properties_out[0].flow_mass_phase_comp["Liq", "H2O"] ), ) blk.eq_TDS_balance = Constraint( expr=sum( blk.inlet.flow_mass_phase_comp[0, "Liq", j] for j in ["NaCl", "CaSO4", "MgSO4", "MgCl2"] ) == blk.outlet.flow_mass_phase_comp[0, "Liq", "TDS"] ) constraint_scaling_transform( blk.eq_TDS_balance, get_scaling_factor( blk.properties_out[0].flow_mass_phase_comp["Liq", "TDS"] ), ) else: raise ValueError("Unexpected property base combination for build_tb") blk.properties_in[0].mass_frac_phase_comp # touch for initialization blk.properties_out[0].mass_frac_phase_comp