#################################################################################
# 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/"
#################################################################################
"""
This module contains a zero-order representation of a centrifuge unit.
"""
import pyomo.environ as pyo
from pyomo.environ import units as pyunits, Var
from idaes.core import declare_process_block_class
from watertap.core import build_sido, constant_intensity, ZeroOrderBaseData
# Some more information about this module
__author__ = "Marcus Holly"
[docs]@declare_process_block_class("CentrifugeZO")
class CentrifugeZOData(ZeroOrderBaseData):
"""
Zero-Order model for a centrifuge reactor unit.
"""
CONFIG = ZeroOrderBaseData.CONFIG()
[docs] def build(self):
super().build()
self._tech_type = "centrifuge"
build_sido(self)
constant_intensity(self)
self.polymer_dose = Var(
self.flowsheet().time,
units=pyunits.mg / pyunits.L,
bounds=(0, None),
doc="Dosing rate of polymer",
)
self._fixed_perf_vars.append(self.polymer_dose)
self._perf_var_dict["Dosage of polymer per sludge"] = self.polymer_dose
self.polymer_demand = Var(
self.flowsheet().time,
units=pyunits.kg / pyunits.hr,
bounds=(0, None),
doc="Consumption rate of polymer",
)
self._perf_var_dict["Polymer Demand"] = self.polymer_demand
@self.Constraint(self.flowsheet().time, doc="Polymer demand constraint")
def polymer_demand_equation(b, t):
return b.polymer_demand[t] == pyunits.convert(
b.polymer_dose[t] * b.properties_in[t].flow_vol,
to_units=pyunits.kg / pyunits.hr,
)
@property
def default_costing_method(self):
return self.cost_centrifuge
[docs] @staticmethod
def cost_centrifuge(blk):
"""
Method for costing centrifuge unit.
"""
t0 = blk.flowsheet().time.first()
# Get parameter dict from database
parameter_dict = blk.unit_model.config.database.get_unit_operation_parameters(
blk.unit_model._tech_type, subtype=blk.unit_model.config.process_subtype
)
# Get costing parameter sub-block for this technology
HRT, size_cost = blk.unit_model._get_tech_parameters(
blk,
parameter_dict,
blk.unit_model.config.process_subtype,
["HRT", "sizing_cost"],
)
# Add cost variable and constraint
blk.capital_cost = pyo.Var(
initialize=1,
units=blk.config.flowsheet_costing_block.base_currency,
bounds=(0, None),
doc="Capital cost of unit operation",
)
expr = pyo.units.convert(
blk.unit_model.properties_in[t0].flow_vol * HRT * size_cost,
to_units=blk.config.flowsheet_costing_block.base_currency,
)
# Determine if a costing factor is required
blk.costing_package.add_cost_factor(
blk, parameter_dict["capital_cost"]["cost_factor"]
)
blk.capital_cost_constraint = pyo.Constraint(
expr=blk.capital_cost == blk.cost_factor * expr
)
# Register flows
blk.config.flowsheet_costing_block.cost_flow(
blk.unit_model.electricity[t0], "electricity"
)
blk.config.flowsheet_costing_block.cost_flow(
blk.unit_model.polymer_demand[t0], "polymer"
)