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1D Membrane Model for CO2 Capture and Utilization #1378

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Add CCUS file structure
Morgan88888888 Mar 18, 2024
b0a336a
One-dimensional membrane model
Morgan88888888 Mar 18, 2024
775b27a
add the unit test file
Morgan88888888 Mar 18, 2024
dd437b7
reformatted by black
Morgan88888888 Mar 18, 2024
693fd68
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Morgan88888888 Mar 18, 2024
5505b1f
fixed the path issue in testing
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f91e825
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446951b
refined the workspace name
Morgan88888888 Mar 19, 2024
db77a65
formatting issue resolved for GitHub test
Morgan88888888 Mar 19, 2024
508f10c
fixed typo
Morgan88888888 Mar 19, 2024
d31a4cb
fixed the unit model importing issue
Morgan88888888 Mar 29, 2024
e228592
fixed linter warnings
Morgan88888888 Mar 29, 2024
feda25c
resolved the comments
Morgan88888888 Mar 29, 2024
054808f
fix linter issues
Morgan88888888 Mar 29, 2024
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formated
Morgan88888888 Mar 29, 2024
a6c9697
Merge branch 'IDAES:main' into co2_membrane
Morgan88888888 May 2, 2024
14d3856
remove the unit level property config
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Merge branch 'IDAES:main' into co2_membrane
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Merge branch 'IDAES:main' into co2_membrane
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Merge branch 'IDAES:main' into co2_membrane
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Merge branch 'co2_membrane' of https://github.com/Morgan88888888/idae…
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Merge branch 'IDAES:main' into co2_membrane
Morgan88888888 Nov 5, 2024
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Merge branch 'co2_membrane' of https://github.com/Morgan88888888/idae…
Morgan88888888 Nov 5, 2024
e721692
added test for different configs and added stream table display
Morgan88888888 Nov 5, 2024
2cd61a4
added more docs to explain the models and settings
Morgan88888888 Nov 5, 2024
3e3dda8
Addressed the comments to support different property packages
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093de8e
added material conservation test
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reformatted
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address comments
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added basic documentation
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c6d3677
fix pylint test
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83529cf
fix doc strings
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80befee
fix the doc string
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6f3f8a6
added what the inputs/degrees of freedom
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93038d4
fix pytest
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Merge branch 'main' into co2_membrane
ksbeattie Nov 14, 2024
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Merge branch 'main' into co2_membrane
ksbeattie Nov 21, 2024
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Merge branch 'main' into co2_membrane
lbianchi-lbl Nov 27, 2024
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This directory contains the unit models for Carbon Capture and Utilization
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#################################################################################
# The Institute for the Design of Advanced Energy Systems Integrated Platform
# Framework (IDAES IP) was produced under the DOE Institute for the
# Design of Advanced Energy Systems (IDAES).
#
# Copyright (c) 2018-2023 by the software owners: The Regents of the
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# University of California, through Lawrence Berkeley National Laboratory,
# National Technology & Engineering Solutions of Sandia, LLC, Carnegie Mellon
# University, West Virginia University Research Corporation, et al.
# All rights reserved. Please see the files COPYRIGHT.md and LICENSE.md
# for full copyright and license information.
#################################################################################
from .membrane_1d import Membrane1D, MembraneFlowPattern
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#################################################################################

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# The Institute for the Design of Advanced Energy Systems Integrated Platform
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# Framework (IDAES IP) was produced under the DOE Institute for the
# Design of Advanced Energy Systems (IDAES).
#
# Copyright (c) 2018-2023 by the software owners: The Regents of the
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# University of California, through Lawrence Berkeley National Laboratory,
# National Technology & Engineering Solutions of Sandia, LLC, Carnegie Mellon
# University, West Virginia University Research Corporation, et al.
# All rights reserved. Please see the files COPYRIGHT.md and LICENSE.md
# for full copyright and license information.
#################################################################################


from enum import Enum
from pyomo.common.config import Bool, ConfigDict, ConfigValue, In
from pyomo.environ import Constraint, Param, Var, units, Expression

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from pyomo.network import Port

from idaes.core import (
FlowDirection,
UnitModelBlockData,
declare_process_block_class,
useDefault,
MaterialFlowBasis,
)
from idaes.core.util.config import is_physical_parameter_block
from idaes.models.unit_models.mscontactor import MSContactor
from idaes.core.util.exceptions import ConfigurationError, InitializationError

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# TODO: add robust initialization
__author__ = "Maojian Wang"


class MembraneFlowPattern(Enum):
"""
Enum of supported flow patterns for membrane.
So far only support countercurrent and cocurrent flow
"""

countercurrent = 1
cocurrent = 2
crossflow = 3


@declare_process_block_class("Membrane1D")
class Membrane1DData(UnitModelBlockData):
"""Standard Membrane 1D Unit Model Class."""

CONFIG = UnitModelBlockData.CONFIG()

Stream_Config = ConfigDict()

Stream_Config.declare(
"property_package",
ConfigValue(
default=useDefault,
domain=is_physical_parameter_block,
description="Property package to use for given stream",
doc="""Property parameter object used to define property calculations for given stream,
**default** - useDefault.
**Valid values:** {
**useDefault** - use default package from parent model or flowsheet,
**PhysicalParameterObject** - a PhysicalParameterBlock object.}""",
),
)

Stream_Config.declare(
"property_package_args",
ConfigDict(
implicit=True,
description="Dict of arguments to use for constructing property package",
doc="""A ConfigDict with arguments to be passed to property block(s)
and used when constructing these,
**default** - None.
**Valid values:** {
see property package for documentation.}""",
),
)

Stream_Config.declare(
"flow_direction",
ConfigValue(
default=FlowDirection.forward,
domain=In(FlowDirection),
doc="Direction of flow for stream",
description="FlowDirection Enum indicating direction of "
"flow for given stream. Default=FlowDirection.forward.",
),
)

Stream_Config.declare(
"has_energy_balance",
ConfigValue(
default=True,
domain=Bool,
doc="Bool indicating whether to include energy balance for stream. Default=True.",
),
)

Stream_Config.declare(
"has_pressure_balance",
ConfigValue(
default=True,
domain=Bool,
doc="Bool indicating whether to include pressure balance for stream. Default=True.",
),
)

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Stream_Config.declare(
"has_feed",
ConfigValue(
default=True,
domain=Bool,
doc="Bool indicating whether stream has a feed.",
description="Bool indicating whether stream has a feed Port and inlet "
"state, or if all flow is provided via mass transfer. Default=True.",
),
)
CONFIG.declare(
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"sweep_flow",
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ConfigValue(
default=True,
domain=Bool,
doc="Bool indicating whether there is a sweep flow in the permeate side.",
description="Bool indicating whether stream has a feed Port and inlet "
"state, or if all flow is provided via mass transfer. Default=True.",
),
)

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CONFIG.declare(
"finite_elements",
ConfigValue(
default=5,
domain=int,
description="Number of finite elements in length domain",
doc="""Number of finite elements to use when discretizing length
domain (default=5)""",
),
)

CONFIG.declare(
"flow_type",
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ConfigValue(
default=MembraneFlowPattern.countercurrent,
domain=In(MembraneFlowPattern),
description="Flow configuration of membrane",
doc="""Flow configuration of membrane
- MembraneFlowPattern.cocurrent: feed and sweep flows from 0 to 1
- MembraneFlowPattern.countercurrent: feed side flows from 0 to 1
sweep side flows from 1 to 0 (default)""",
),
)

CONFIG.declare(
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"property_package",
ConfigValue(
default=None,
domain=is_physical_parameter_block,
description="Property package to use for control volume",
doc="""Property parameter object used to define property
calculations
(default = 'use_parent_value')
- 'use_parent_value' - get package from parent (default = None)
- a ParameterBlock object""",
),
)

CONFIG.declare(
"property_package_args",
ConfigValue(
default={},
description="Arguments for constructing property package",
doc="""A dict of arguments to be passed to the PropertyBlockData
and used when constructing these
(default = 'use_parent_value')
- 'use_parent_value' - get package from parent (default = None)
- a dict (see property package for documentation)""",
),
)

for side_name in ["feed", "sweep"]:
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CONFIG.declare(
side_name + "_side",
Stream_Config(),
)

def build(self):
super().build()

if self.config.sweep_flow == False:

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self.config.sweep_side.has_feed = False

# Set flow directions
if self.config.flow_type == MembraneFlowPattern.cocurrent:
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self.config.feed_side.flow_direction = FlowDirection.forward
self.config.sweep_side.flow_direction = FlowDirection.forward
elif self.config.flow_type == MembraneFlowPattern.countercurrent:
self.config.feed_side.flow_direction = FlowDirection.forward
self.config.sweep_side.flow_direction = FlowDirection.backward

else:
raise ConfigurationError(
"{} Membrane1D only supports cocurrent and "
"countercurrent flow patterns, but flow_type configuration"
" argument was set to {}.".format(self.name, self.config.flow_type)
)

if self.config.property_package != None:

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Comparison 'self.config.property_package != None' should be 'self.config.property_package is not None'
if self.config.feed_side.property_package == useDefault:
self.config.feed_side.property_package = self.config.property_package
if self.config.sweep_side.property_package == useDefault:
self.config.sweep_side.property_package = self.config.property_package

streams_dict = {
"feed_side": self.config.feed_side,
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"sweep_side": self.config.sweep_side,
}
self.mscontactor = MSContactor(
streams=streams_dict,
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number_of_finite_elements=self.config.finite_elements,
)

self.feed_side_inlet = Port(extends=self.mscontactor.feed_side_inlet)
self.feed_side_outlet = Port(extends=self.mscontactor.feed_side_outlet)
if self.config.sweep_flow == True:

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self.sweep_side_inlet = Port(extends=self.mscontactor.sweep_side_inlet)
self.sweep_side_outlet = Port(extends=self.mscontactor.sweep_side_outlet)

self._make_geometry()
self._make_performance()

def _make_geometry(self):
feed_side_units = (

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self.config.feed_side.property_package.get_metadata().derived_units
)

self.area = Var(initialize=100, units=units.cm**2, doc="The membrane area")
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self.length = Var(initialize=100, units=units.cm, doc="The membrane length")
self.cell_length = Expression(expr=self.length / self.config.finite_elements)

self.cell_area = Var(
initialize=100, units=units.cm**2, doc="The membrane area"
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)

@self.Constraint()
def area_per_cell(self):
return self.cell_area == self.area / self.config.finite_elements

def _make_performance(self):
feed_side_units = (
self.config.feed_side.property_package.get_metadata().derived_units
)

self.permeance = Var(
self.flowsheet().time,
self.mscontactor.elements,
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To check, does this need to be indexed by time and finite element? Whilst there are cases where you would want this degree of flexibility, is it something you want to support right now?

Also, I do not think this should be indexed by the feed side component list. Either you should have a single property package for the unit model, in which case you should use the uni level package, or it you want to support separate property packages you should use the intersection of the feed and sweep side component lists (i.e. only create a term for those species which appear in both property packages). Otherwise, you run the risk of trying to write constraints involving species which do not exist on the sweep side.

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In the simple assumption, it isn't necessary. However, retaining it isn't particularly harmful either.
The example you gave about indexing could occur in some membrane separations but isn't common in this application. I'll keep this idea in mind for future improvements if the need arises.

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It is better to fix these issues now rather than wait until later when you have forgotten how the model works.

You need to make the decision to either use a single property package for everything or not, and if you decide to allow for multiple property packages then you need to go the full way to supporting them.

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What happens here if the two property packages have different components? Should this instead use the intersection of the two component lists (which is easy to do)?

self.mscontactor.feed_side.component_list,
initialize=1,
doc="Values in Gas Permeance Unit(GPU)",
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Missing space "Unit (GPU)"

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fixed

units=units.dimensionless,
)

self.gpu_factor = Param(
default=10e-8 / 13333.2239,
units=units.m / units.s / units.Pa,
mutable=True,
)

self.selectivity = Var(
self.flowsheet().time,
self.mscontactor.elements,
self.mscontactor.feed_side.component_list,
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Do you need the full factorial combination of these? I suspect you do not need the combination where both components are the same, and that S[i, j] == 1/S[j, i]. Looking below, I think this is confirmed by the following constraint.

Thus, my question becomes how do you intend for a user to use these? If a user were to naively fix all the selectivity, then the problem would be over-specified.

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How are you handling the possible over-specification here?

self.mscontactor.feed_side.component_list,
initialize=1,
units=units.dimensionless,
)

@self.Constraint(
self.flowsheet().time,
self.mscontactor.elements,
self.mscontactor.feed_side.component_list,
self.mscontactor.feed_side.component_list,
doc="permeance calculation",
)
def permeance_calculation(self, t, e, a, b):
return (
self.permeance[t, e, a] * self.selectivity[t, e, a, b]
== self.permeance[t, e, b]
)
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This looks like it results in an over-specified problem. You write a constraint for a, b and b, a which are reflections of each other. If the user specifies all the selectivities they will have a degree of freedom issue.

I think you really need to only cover the unique pairs (and exclude a=b).


p_units = feed_side_units.PRESSURE

@self.Constraint(
self.flowsheet().time,
self.mscontactor.elements,
self.mscontactor.feed_side.component_list,
doc="permeability calculation",
)
def permeability_calculation(self, t, s, m):
feed_side_state = self.mscontactor.feed_side[t, s]
if feed_side_state.get_material_flow_basis() is MaterialFlowBasis.molar:
mb_units = feed_side_units.FLOW_MOLE
rho = self.mscontactor.feed_side[t, s].dens_mol
elif feed_side_state.get_material_flow_basis() is MaterialFlowBasis.mass:
mb_units = feed_side_units.FLOW_MASS
rho = self.mscontactor.feed_side[t, s].dens_mass
else:
raise TypeError("Undefined flow basis, please define the flow basis")
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return self.mscontactor.material_transfer_term[
t, s, "feed_side", "sweep_side", m
] == -units.convert(
(
rho
* self.gpu_factor
* self.permeance[t, s, m]
* self.cell_area
* (
self.mscontactor.feed_side[t, s].pressure
* self.mscontactor.feed_side[t, s].mole_frac_comp[m]
- units.convert(
self.mscontactor.sweep_side[t, s].pressure, to_units=p_units
)
* self.mscontactor.sweep_side[t, s].mole_frac_comp[m]
)
),
to_units=mb_units,
)

@self.Constraint(
self.flowsheet().time,
self.mscontactor.elements,
doc="Energy balance",
)
def energy_transfer(self, t, s):
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For clarity, I would call this an isothermal constraint. It is not an energy balance.

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fixed

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I would also suggest changing the name of the constraint (i.e. the name of the rule/function).

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changed

return (
self.mscontactor.feed_side[t, s].temperature
== self.mscontactor.sweep_side[t, s].temperature
)
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