Source code for watertap.costing.unit_models.heat_exchanger

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# 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
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import pyomo.environ as pyo
from ..util import register_costing_parameter_block, make_capital_cost_var


def build_heat_exchanger_cost_param_block(blk):

    blk.unit_cost = pyo.Var(
        initialize=300,
        doc="Estimated from multiple sources",
        units=pyo.units.USD_2020,
    )

    blk.material_factor_cost = pyo.Var(
        initialize=1,
        doc="Material factor",
        units=pyo.units.dimensionless,
    )

    blk.steam_cost = pyo.Var(
        initialize=0.008,
        units=pyo.units.USD_2018 / (pyo.units.kg),
        doc="steam cost per kg",
    )

    blk.parent_block().register_flow_type("steam", blk.steam_cost)


[docs]@register_costing_parameter_block( build_rule=build_heat_exchanger_cost_param_block, parameter_block_name="heat_exchanger", ) def cost_heat_exchanger(blk, cost_steam_flow=False): """ Heat Exchanger Costing Method TODO: describe equations """ make_capital_cost_var(blk) blk.costing_package.add_cost_factor(blk, "TIC") blk.capital_cost_constraint = pyo.Constraint( expr=blk.capital_cost == blk.cost_factor * pyo.units.convert( blk.costing_package.heat_exchanger.unit_cost * blk.costing_package.heat_exchanger.material_factor_cost * ( pyo.units.convert(blk.unit_model.area, to_units=(pyo.units.m**2)) / pyo.units.m**2 ), to_units=blk.costing_package.base_currency, ) ) if cost_steam_flow: blk.costing_package.cost_flow( pyo.units.convert( (blk.unit_model.hot_side_inlet.flow_mass_phase_comp[0, "Vap", "H2O"]), to_units=pyo.units.kg / pyo.units.s, ), "steam", )