#################################################################################
# WaterTAP Copyright (c) 2020-2024, 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/"
#################################################################################
"""
GUI configuration for the base BSM2 flowsheet.
"""
from pyomo.environ import units as pyunits, assert_optimal_termination
from pyomo.util.check_units import assert_units_consistent
from watertap.ui.fsapi import FlowsheetInterface
from watertap.core.util.initialization import assert_degrees_of_freedom
from watertap.examples.flowsheets.case_studies.full_water_resource_recovery_facility.BSM2 import (
build,
set_operating_conditions,
initialize_system,
solve,
)
[docs]def export_to_ui():
"""
Exports the variables, flowsheet build, and solver results to the GUI.
"""
return FlowsheetInterface(
name="BSM2",
do_export=export_variables,
do_build=build_flowsheet,
do_solve=solve_flowsheet,
)
[docs]def export_variables(flowsheet=None, exports=None, build_options=None, **kwargs):
"""
Exports the variables to the GUI.
"""
fs = flowsheet
# --- Input data ---
# Feed conditions
exports.add(
obj=fs.FeedWater.flow_vol[0],
name="Feed volumetric flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Inlet volumetric flow rate",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_I"],
name="Feed S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet soluble inert organic matter concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_S"],
name="Feed S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet readily biodegradable substrate concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_I"],
name="Feed X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet particulate inert organic matter concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_S"],
name="Feed X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet slowly biodegradable substrate concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_BH"],
name="Feed X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet active heterotrophic biomass concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_BA"],
name="Feed X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet active autotrophic biomass concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_P"],
name="Feed X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet particulate products arising from biomass decay concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_O"],
name="Feed S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet oxygen concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_NO"],
name="Feed S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet nitrate and nitrite nitrogen concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_NH"],
name="Feed S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet ammonium and ammonia nitrogen concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "S_ND"],
name="Feed S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet biodegradable organic nitrogen concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.conc_mass_comp[0, "X_ND"],
name="Feed X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=2,
description="Inlet particulate biodegradable organic nitrogen concentration",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
exports.add(
obj=fs.FeedWater.properties[0].alkalinity,
name="Feed S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=2,
description="Alkalinity",
is_input=True,
input_category="Feed",
is_output=True,
output_category="Feed",
)
# Unit model data, activated sludge process
exports.add(
obj=fs.R1.volume[0],
name="First anoxic reactor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="CSTR volume",
is_input=True,
input_category="Activated sludge process",
is_output=False,
)
exports.add(
obj=fs.R2.volume[0],
name="Second anoxic reactor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="CSTR volume",
is_input=True,
input_category="Activated sludge process",
is_output=False,
)
exports.add(
obj=fs.R3.volume[0],
name="First aerobic reactor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="CSTR volume",
is_input=True,
input_category="Activated sludge process",
is_output=False,
)
exports.add(
obj=fs.R4.volume[0],
name="Second aerobic reactor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="CSTR volume",
is_input=True,
input_category="Activated sludge process",
is_output=False,
)
exports.add(
obj=fs.R5.volume[0],
name="Third aerobic reactor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="CSTR volume",
is_input=True,
input_category="Activated sludge process",
is_output=False,
)
# Unit model data, anaerobic digester
exports.add(
obj=fs.RADM.volume_liquid[0],
name="Liquid volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="Liquid volume",
is_input=True,
input_category="Anaerobic digester",
is_output=False,
)
exports.add(
obj=fs.RADM.volume_vapor[0],
name="Vapor volume",
ui_units=pyunits.m**3,
display_units="m3",
rounding=1,
description="Vapor volume",
is_input=True,
input_category="Anaerobic digester",
is_output=False,
)
# Unit model data, secondary clarifier
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "H2O"],
name="H2O split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Water split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_I"],
name="S_I split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Soluble inert organic matter split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_S"],
name="S_S split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Readily biodegradable substrate split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_I"],
name="X_I split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate inert organic matter split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_S"],
name="X_S split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Slowly biodegradable substrate split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_BH"],
name="X_BH split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Active heterotrophic biomass split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_BA"],
name="X_BA split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Active autotrophic biomass split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_P"],
name="X_P split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate products arising from biomass decay split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_O"],
name="S_O split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Oxygen split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_NO"],
name="S_NO split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Nitrate and nitrite nitrogen split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_NH"],
name="S_NH split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Ammonium and ammonia nitrogen split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_ND"],
name="S_ND split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Soluble biodegradable organic nitrogen split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "X_ND"],
name="X_ND split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate biodegradable organic nitrogen split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL1.split_fraction[0, "effluent", "S_ALK"],
name="S_ALK split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Alkalinity split fraction",
is_input=True,
input_category="Secondary clarifier",
is_output=False,
)
# Unit model data, primary clarifier
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "H2O"],
name="H2O split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Water split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_I"],
name="S_I split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Soluble inert organic matter split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_S"],
name="S_S split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Readily biodegradable substrate split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_I"],
name="X_I split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate inert organic matter split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_S"],
name="X_S split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Slowly biodegradable substrate split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_BH"],
name="X_BH split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Active heterotrophic biomass split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_BA"],
name="X_BA split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Active autotrophic biomass split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_P"],
name="X_P split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate products arising from biomass decay split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_O"],
name="S_O split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Oxygen split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_NO"],
name="S_NO split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Nitrate and nitrite nitrogen split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_NH"],
name="S_NH split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Ammonium and ammonia nitrogen split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_ND"],
name="S_ND split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Soluble biodegradable organic nitrogen split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "X_ND"],
name="X_ND split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Particulate biodegradable organic nitrogen split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
exports.add(
obj=fs.CL.split_fraction[0, "effluent", "S_ALK"],
name="S_ALK split fraction",
ui_units=pyunits.dimensionless,
display_units="fraction",
rounding=5,
description="Alkalinity split fraction",
is_input=True,
input_category="Primary clarifier",
is_output=False,
)
# TODO: uncomment and revise below once costing is merged
# System costing
# exports.add(
# obj=fs.costing.utilization_factor,
# name="Utilization factor",
# ui_units=pyunits.dimensionless,
# display_units="fraction",
# rounding=2,
# description="Utilization factor - [annual use hours/total hours in year]",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# exports.add(
# obj=fs.costing.TIC,
# name="Practical investment factor",
# ui_units=pyunits.dimensionless,
# display_units="fraction",
# rounding=1,
# description="Practical investment factor - [total investment cost/direct "
# "capital costs]",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# exports.add(
# obj=fs.costing.plant_lifetime,
# name="Plant lifetime",
# ui_units=pyunits.year,
# display_units="years",
# rounding=1,
# description="Plant lifetime",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# exports.add(
# obj=fs.costing.wacc,
# name="Discount rate",
# ui_units=pyunits.dimensionless,
# display_units="fraction",
# rounding=2,
# description="Discount rate used in calculating the capital annualization",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# exports.add(
# obj=fs.costing.maintenance_costs_percent_FCI,
# name="Fixed operating cost factor",
# ui_units=1 / pyunits.year,
# display_units="fraction/year",
# rounding=2,
# description="Fixed operating cost factor - [annual fixed operating cost/total "
# "investment cost]",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# exports.add(
# obj=fs.costing.electricity_cost,
# name="Electricity cost",
# ui_units=fs.costing.base_currency / pyunits.kWh,
# display_units="$/kWh",
# rounding=3,
# description="Electricity cost",
# is_input=True,
# input_category="System costing",
# is_output=False,
# )
# Outlets
exports.add(
obj=fs.Treated.properties[0].flow_vol,
name="Treated flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Outlet treated stream flow rate",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_I"],
name="Treated S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_S"],
name="Treated S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_I"],
name="Treated X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_S"],
name="Treated X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_BH"],
name="Treated X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_BA"],
name="Treated X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_P"],
name="Treated X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_O"],
name="Treated S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_NO"],
name="Treated S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_NH"],
name="Treated S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["S_ND"],
name="Treated S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].conc_mass_comp["X_ND"],
name="Treated X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.Treated.properties[0].alkalinity,
name="Treated S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.flow_vol[0],
name="Primary clarifier effluent flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Outlet primary clarifier flow rate",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_I"],
name="Primary clarifier effluent S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_S"],
name="Primary clarifier effluent S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_I"],
name="Primary clarifier effluent X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_S"],
name="Primary clarifier effluent X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_BH"],
name="Primary clarifier effluent X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_BA"],
name="Primary clarifier effluent X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_P"],
name="Primary clarifier effluent X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_O"],
name="Primary clarifier effluent S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_NO"],
name="Primary clarifier effluent S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_NH"],
name="Primary clarifier effluent S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "S_ND"],
name="Primary clarifier effluent S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.conc_mass_comp[0, "X_ND"],
name="Primary clarifier effluent X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.effluent.alkalinity[0],
name="Primary clarifier effluent S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Effluent",
)
exports.add(
obj=fs.CL.underflow.flow_vol[0],
name="Primary clarifier underflow flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Outlet primary clarifier flow rate",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_I"],
name="Primary clarifier underflow S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_S"],
name="Primary clarifier underflow S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_I"],
name="8Primary clarifier underflow X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_S"],
name="Primary clarifier underflow X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_BH"],
name="Primary clarifier underflow X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_BA"],
name="Primary clarifier underflow X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_P"],
name="Primary clarifier underflow X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_O"],
name="Primary clarifier underflow S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_NO"],
name="Primary clarifier underflow S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_NH"],
name="Primary clarifier underflow S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "S_ND"],
name="Primary clarifier underflow S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.conc_mass_comp[0, "X_ND"],
name="Primary clarifier underflow X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.CL.underflow.alkalinity[0],
name="Primary clarifier underflow S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Primary Clarifier Underflow",
)
exports.add(
obj=fs.SP6.recycle.flow_vol[0],
name="ASP recycle inlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="ASP recycle flow rate",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_I"],
name="ASP recycle inlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_S"],
name="ASP recycle inlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_I"],
name="ASP recycle inlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_S"],
name="ASP recycle inlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_BH"],
name="ASP recycle inlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_BA"],
name="ASP recycle inlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_P"],
name="ASP recycle inlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_O"],
name="ASP recycle inlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet oxygen concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_NO"],
name="ASP recycle inlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_NH"],
name="ASP recycle inlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "S_ND"],
name="ASP recycle inlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.conc_mass_comp[0, "X_ND"],
name="ASP recycle inlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP6.recycle.alkalinity[0],
name="ASP recycle inlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Inlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="ASP Recycle Inlet",
)
exports.add(
obj=fs.SP5.overflow.flow_vol[0],
name="Secondary clarifier inlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Secondary clarifier inlet flow rate",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_I"],
name="Secondary clarifier inlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_S"],
name="Secondary clarifier inlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_I"],
name="Secondary clarifier inlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_S"],
name="Secondary clarifier inlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_BH"],
name="Secondary clarifier inlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_BA"],
name="Secondary clarifier inlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_P"],
name="Secondary clarifier inlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_O"],
name="Secondary clarifier inlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_NO"],
name="Secondary clarifier inlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_NH"],
name="Secondary clarifier inlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "S_ND"],
name="Secondary clarifier inlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.conc_mass_comp[0, "X_ND"],
name="Secondary clarifier inlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.SP5.overflow.alkalinity[0],
name="Secondary clarifier inlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Inlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Secondary Clarifier Inlet",
)
exports.add(
obj=fs.TU.inlet.flow_vol[0],
name="Thickener inlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Thickener inlet flow rate",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_I"],
name="Thickener inlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_S"],
name="Thickener inlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_I"],
name="Thickener inlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_S"],
name="Thickener inlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_BH"],
name="Thickener inlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_BA"],
name="Thickener inlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_P"],
name="Thickener inlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_O"],
name="Thickener inlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_NO"],
name="Thickener inlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_NH"],
name="Thickener inlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "S_ND"],
name="Thickener inlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.conc_mass_comp[0, "X_ND"],
name="Thickener inlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.TU.inlet.alkalinity[0],
name="Thickener inlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Inlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Thickener Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.flow_vol[0],
name="ASM1/ADM1 inlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="ASM1/ADM1 interface inlet flow rate",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_I"],
name="ASM1/ADM1 inlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_S"],
name="ASM1/ADM1 inlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_I"],
name="ASM1/ADM1 inlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_S"],
name="ASM1/ADM1 inlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_BH"],
name="ASM1/ADM1 inlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_BA"],
name="ASM1/ADM1 inlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_P"],
name="ASM1/ADM1 inlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_O"],
name="ASM1/ADM1 inlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet oxygen concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_NO"],
name="ASM1/ADM1 inlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_NH"],
name="ASM1/ADM1 inlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "S_ND"],
name="ASM1/ADM1 inlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.conc_mass_comp[0, "X_ND"],
name="ASM1/ADM1 inlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.inlet.alkalinity[0],
name="ASM1/ADM1 inlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Inlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="ASM1/ADM1 Interface Inlet",
)
exports.add(
obj=fs.asm_adm.outlet.flow_vol[0],
name="Anaerobic digester inlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Anaerobic digester inlet flow rate",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_su"],
name="Anaerobic digester inlet S_su concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Monosaccharides concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_aa"],
name="Anaerobic digester inlet S_aa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Amino acids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_fa"],
name="Anaerobic digester inlet S_fa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Long chain fatty acids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_va"],
name="Anaerobic digester inlet S_va concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total valerate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_bu"],
name="Anaerobic digester inlet S_bu concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total butyrate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_pro"],
name="Anaerobic digester inlet S_pro concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total propionate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_ac"],
name="Anaerobic digester inlet S_ac concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total acetate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_h2"],
name="Anaerobic digester inlet S_h2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Hydrogen gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_ch4"],
name="Anaerobic digester inlet S_ch4 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Methane gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_IC"],
name="Anaerobic digester inlet S_IC concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inorganic carbon concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_IN"],
name="Anaerobic digester inlet S_IN concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inorganic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "S_I"],
name="Anaerobic digester inlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Soluble inerts concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_c"],
name="Anaerobic digester inlet X_c concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Composites concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_ch"],
name="Anaerobic digester inlet X_ch concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Carbohydrates concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_pr"],
name="Anaerobic digester inlet X_pr concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Proteins concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_li"],
name="Anaerobic digester inlet X_li concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Lipids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_su"],
name="Anaerobic digester inlet X_su concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Sugar degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_aa"],
name="Anaerobic digester inlet X_aa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Amino acid degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_fa"],
name="Anaerobic digester inlet X_fa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Long chain fatty acid (LCFA) degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_c4"],
name="Anaerobic digester inlet X_c4 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Valerate and butyrate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_pro"],
name="Anaerobic digester inlet X_pro concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Propionate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_ac"],
name="Anaerobic digester inlet X_ac concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Acetate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_h2"],
name="Anaerobic digester inlet X_h2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Hydrogen degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.asm_adm.outlet.conc_mass_comp[0, "X_I"],
name="Anaerobic digester inlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Particulate inerts concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Inlet (post-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.flow_vol[0],
name="Anaerobic digester liquid outlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Anaerobic digester liquid outlet flow rate",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_su"],
name="Anaerobic digester liquid outlet S_su concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Monosaccharides concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_aa"],
name="Anaerobic digester liquid outlet S_aa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Amino acids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_fa"],
name="Anaerobic digester liquid outlet S_fa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Long chain fatty acids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_va"],
name="Anaerobic digester liquid outlet S_va concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total valerate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_bu"],
name="Anaerobic digester liquid outlet S_bu concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total butyrate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_pro"],
name="Anaerobic digester liquid outlet S_pro concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total propionate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_ac"],
name="Anaerobic digester liquid outlet S_ac concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Total acetate concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_h2"],
name="Anaerobic digester liquid outlet S_h2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Hydrogen gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_ch4"],
name="Anaerobic digester liquid outlet S_ch4 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Methane gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_IC"],
name="Anaerobic digester liquid outlet S_IC concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inorganic carbon concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_IN"],
name="Anaerobic digester liquid outlet S_IN concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Inorganic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "S_I"],
name="Anaerobic digester liquid outlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Soluble inerts concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_c"],
name="Anaerobic digester liquid outlet X_c concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Composites concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_ch"],
name="Anaerobic digester liquid outlet X_ch concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Carbohydrates concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_pr"],
name="Anaerobic digester liquid outlet X_pr concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Proteins concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_li"],
name="Anaerobic digester liquid outlet X_li concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Lipids concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_su"],
name="Anaerobic digester liquid outlet X_su concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Sugar degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_aa"],
name="Anaerobic digester liquid outlet X_aa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Amino acid degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_fa"],
name="Anaerobic digester liquid outlet X_fa concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Long chain fatty acid (LCFA) degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_c4"],
name="Anaerobic digester liquid outlet X_c4 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Valerate and butyrate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_pro"],
name="Anaerobic digester liquid outlet X_pro concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Propionate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_ac"],
name="Anaerobic digester liquid outlet X_ac concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Acetate degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_h2"],
name="Anaerobic digester liquid outlet X_h2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Hydrogen degraders concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.inlet.conc_mass_comp[0, "X_I"],
name="Anaerobic digester liquid outlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Particulate inerts concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Liquid Outlet (pre-interface)",
)
exports.add(
obj=fs.adm_asm.outlet.flow_vol[0],
name="ADM1/ASM1 outlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="ADM1/ASM1 interface outlet flow rate",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_I"],
name="ADM1/ASM1 outlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_S"],
name="ADM1/ASM1 outlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_I"],
name="ADM1/ASM1 outlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_S"],
name="ADM1/ASM1 outlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_BH"],
name="ADM1/ASM1 outlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_BA"],
name="ADM1/ASM1 outlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_P"],
name="ADM1/ASM1 outlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_O"],
name="ADM1/ASM1 outlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_NO"],
name="ADM1/ASM1 outlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_NH"],
name="ADM1/ASM1 outlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "S_ND"],
name="ADM1/ASM1 outlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.conc_mass_comp[0, "X_ND"],
name="ADM1/ASM1 outlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.adm_asm.outlet.alkalinity[0],
name="ADM1/ASM1 outlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="ADM1/ASM1 Interface Outlet",
)
exports.add(
obj=fs.RADM.vapor_outlet.flow_vol[0],
name="Anaerobic digester vapor flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Anaerobic digester vapor outlet flow rate",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Vapor Outlet",
)
exports.add(
obj=fs.RADM.vapor_outlet.conc_mass_comp[0, "S_h2"],
name="Anaerobic digester vapor S_h2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Hydrogen gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Vapor Outlet",
)
exports.add(
obj=fs.RADM.vapor_outlet.conc_mass_comp[0, "S_ch4"],
name="Anaerobic digester vapor S_ch4 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Methane gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Vapor Outlet",
)
exports.add(
obj=fs.RADM.vapor_outlet.conc_mass_comp[0, "S_co2"],
name="Anaerobic digester vapor S_co2 concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Carbon dioxide gas concentration",
is_input=False,
is_output=True,
output_category="Anaerobic Digester Vapor Outlet",
)
exports.add(
obj=fs.DU.underflow.flow_vol[0],
name="Dewatered sludge flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Outlet sludge disposal flow rate",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_I"],
name="Dewatered sludge S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_S"],
name="Dewatered sludge S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_I"],
name="Dewatered sludge X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_S"],
name="Dewatered sludge X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_BH"],
name="Dewatered sludge X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_BA"],
name="Dewatered sludge X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_P"],
name="Dewatered sludge X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_O"],
name="Dewatered sludge S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_NO"],
name="Dewatered sludge S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_NH"],
name="Dewatered sludge S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "S_ND"],
name="Dewatered sludge S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.conc_mass_comp[0, "X_ND"],
name="Dewatered sludge X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.underflow.alkalinity[0],
name="Dewatered sludge S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Dewatered Sludge",
)
exports.add(
obj=fs.DU.overflow.flow_vol[0],
name="Dewatering unit liquid outlet flow rate",
ui_units=pyunits.m**3 / pyunits.day,
display_units="m3/day",
rounding=2,
description="Dewatering unit overflow flow rate",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_I"],
name="Dewatering unit liquid outlet S_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_S"],
name="Dewatering unit liquid outlet S_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet readily biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_I"],
name="Dewatering unit liquid outlet X_I concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate inert organic matter concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_S"],
name="Dewatering unit liquid outlet X_S concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet slowly biodegradable substrate concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_BH"],
name="Dewatering unit liquid outlet X_BH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active heterotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_BA"],
name="Dewatering unit liquid outlet X_BA concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet active autotrophic biomass concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_P"],
name="Dewatering unit liquid outlet X_P concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate products arising from biomass decay concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_O"],
name="Dewatering unit liquid outlet S_O concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet oxygen concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_NO"],
name="Dewatering unit liquid outlet S_NO concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet nitrate and nitrite nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_NH"],
name="Dewatering unit liquid outlet S_NH concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet ammonium and ammonia nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "S_ND"],
name="Dewatering unit liquid outlet S_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet soluble biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.conc_mass_comp[0, "X_ND"],
name="Dewatering unit liquid outlet X_ND concentration",
ui_units=pyunits.g / pyunits.m**3,
display_units="g/m3",
rounding=5,
description="Outlet particulate biodegradable organic nitrogen concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
exports.add(
obj=fs.DU.overflow.alkalinity[0],
name="Dewatering unit liquid outlet S_ALK concentration",
ui_units=pyunits.mol / pyunits.m**3,
display_units="mol/m3",
rounding=5,
description="Outlet alkalinity concentration",
is_input=False,
is_output=True,
output_category="Dewatering Unit Liquid Outlet",
)
# performance metrics
recovery_vol = (
fs.Treated.properties[0].flow_vol / fs.FeedWater.properties[0].flow_vol
)
exports.add(
obj=recovery_vol,
name="Volumetric recovery",
ui_units=pyunits.dimensionless,
display_units="m3 of product/m3 of feed",
rounding=5,
description="Normalized volumetric recovery",
is_input=False,
is_output=True,
output_category="Normalized performance metrics",
)
[docs]def build_flowsheet(build_options=None, **kwargs):
"""
Builds the initial flowsheet.
"""
m = build()
set_operating_conditions(m)
assert_degrees_of_freedom(m, 0)
assert_units_consistent(m)
initialize_system(m)
results = solve(m)
assert_optimal_termination(results)
# TODO: incorporate costing when merged
# add_costing(m)
# assert_degrees_of_freedom(m, 0)
# m.fs.costing.initialize()
#
# results = solve(m)
# assert_optimal_termination(results)
return m
[docs]def solve_flowsheet(flowsheet=None):
"""
Solves the initial flowsheet.
"""
fs = flowsheet
results = solve(fs)
return results