#################################################################################
# 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/"
#################################################################################
# Import Pyomo libraries
from pyomo.environ import (
Var,
NonNegativeReals,
value,
)
from idaes.core import declare_process_block_class, FlowDirection
from idaes.core.util import scaling as iscale
from watertap.core import (
MembraneChannel0DBlock,
MassTransferCoefficient,
PressureChangeType,
)
from watertap.core.membrane_channel0d import CONFIG_Template
from watertap.unit_models.osmotically_assisted_reverse_osmosis_base import (
OsmoticallyAssistedReverseOsmosisBaseData,
_add_has_full_reporting,
)
__author__ = "Adam Atia, Chenyu Wang"
[docs]@declare_process_block_class("OsmoticallyAssistedReverseOsmosis0D")
class OsmoticallyAssistedReverseOsmosisData(OsmoticallyAssistedReverseOsmosisBaseData):
"""
Standard OARO Unit Model Class:
- zero dimensional model
- steady state only
- single liquid phase only
"""
CONFIG = CONFIG_Template()
_add_has_full_reporting(CONFIG)
def _add_membrane_channel_and_geometry(
self, side="feed_side", flow_direction=FlowDirection.forward
):
if not isinstance(side, str):
raise TypeError(
f"{side} is not a string. Please provide a string for the side argument."
)
# Build membrane channel control volume
setattr(
self,
side,
MembraneChannel0DBlock(
dynamic=False,
has_holdup=False,
property_package=self.config.property_package,
property_package_args=self.config.property_package_args,
),
)
mem_side = getattr(self, side)
if (self.config.pressure_change_type != PressureChangeType.fixed_per_stage) or (
self.config.mass_transfer_coefficient == MassTransferCoefficient.calculated
):
if not hasattr(self, "length") and not hasattr(self, "width"):
self._add_length_and_width()
mem_side.add_geometry(
length_var=self.length,
width_var=self.width,
flow_direction=flow_direction,
)
if not hasattr(self, "eq_area"):
add_eq_area = True
else:
add_eq_area = False
self._add_area(include_constraint=add_eq_area)
else:
mem_side.add_geometry(
length_var=None, width_var=None, flow_direction=flow_direction
)
self._add_area(include_constraint=False)
def _add_mass_transfer(self):
units_meta = self.config.property_package.get_metadata().get_derived_units
# mass transfer
def mass_transfer_phase_comp_initialize(b, t, p, j):
return value(
self.feed_side.properties_in[t].get_material_flow_terms("Liq", j)
* self.recovery_mass_phase_comp[t, "Liq", j]
)
self.mass_transfer_phase_comp = Var(
self.flowsheet().config.time,
self.config.property_package.phase_list,
self.config.property_package.component_list,
initialize=mass_transfer_phase_comp_initialize,
bounds=(0.0, 1e6),
domain=NonNegativeReals,
units=units_meta("mass") * units_meta("time") ** -1,
doc="Mass transfer to permeate",
)
@self.Constraint(
self.flowsheet().config.time,
self.config.property_package.phase_list,
self.config.property_package.component_list,
doc="Mass transfer term",
)
def eq_mass_transfer_term(self, t, p, j):
return (
self.mass_transfer_phase_comp[t, p, j]
== -self.feed_side.mass_transfer_term[t, p, j]
)
# Feed and permeate-side connection
@self.Constraint(
self.flowsheet().config.time,
self.config.property_package.phase_list,
self.config.property_package.component_list,
doc="Mass transfer from feed to permeate",
)
def eq_connect_mass_transfer(b, t, p, j):
return (
b.permeate_side.mass_transfer_term[t, p, j]
== -b.feed_side.mass_transfer_term[t, p, j]
)
@self.Constraint(
self.flowsheet().config.time,
self.config.property_package.phase_list,
self.config.property_package.component_list,
doc="Permeate production",
)
def eq_permeate_production(b, t, p, j):
return (
b.permeate_side.mass_transfer_term[t, p, j]
== b.area * b.flux_mass_phase_comp_avg[t, p, j]
)
def calculate_scaling_factors(self):
super().calculate_scaling_factors()
for (t, p, j), v in self.mass_transfer_phase_comp.items():
sf = iscale.get_scaling_factor(
self.feed_side.properties_in[t].get_material_flow_terms(p, j)
)
if iscale.get_scaling_factor(v) is None:
iscale.set_scaling_factor(v, sf)
v = self.feed_side.mass_transfer_term[t, p, j]
if iscale.get_scaling_factor(v) is None:
iscale.set_scaling_factor(v, sf)
v = self.permeate_side.mass_transfer_term[t, p, j]
if iscale.get_scaling_factor(v) is None:
iscale.set_scaling_factor(v, sf)
if hasattr(self, "length"):
if iscale.get_scaling_factor(self.length) is None:
iscale.set_scaling_factor(self.length, 1)
if hasattr(self, "width"):
if iscale.get_scaling_factor(self.width) is None:
iscale.set_scaling_factor(self.width, 1)