def build_model():
m = ConcreteModel()
m.BigM = Suffix(direction=Suffix.LOCAL)
m.periods_per_year = Param(initialize=4, doc="Quarters per year")
m.project_life = Param(initialize=15, doc="Years")
m.time = RangeSet(0,
m.periods_per_year * m.project_life - 1,
doc="Time periods")
m.discount_rate = Param(initialize=0.08, doc="8%")
m.learning_rate = Param(initialize=0.1,
doc="Fraction discount for doubling of quantity")
m.module_setup_time = Param(initialize=1,
doc="1 quarter for module transfer")
@m.Param(m.time)
def discount_factor(m, t):
return (1 + m.discount_rate / m.periods_per_year)**(-t /
m.periods_per_year)
xlsx_data = pd.read_excel(os.path.join(os.path.dirname(__file__),
"data.xlsx"),
sheet_name=None)
module_sheet = xlsx_data['modules'].set_index('Type')
m.module_types = Set(initialize=module_sheet.columns.tolist(), )
@m.Param(m.module_types)
def module_base_cost(m, mtype):
return float(module_sheet[mtype]['Capital Cost [MM$]'])
@m.Param(m.module_types,
doc="Natural gas consumption per module of this type [MMSCF/d]")
def unit_gas_consumption(m, mtype):
return float(module_sheet[mtype]['Nat Gas [MMSCF/d]'])
@m.Param(m.module_types,
doc="Gasoline production per module of this type [kBD]")
def gasoline_production(m, mtype):
return float(module_sheet[mtype]['Gasoline [kBD]'])
@m.Param(
m.module_types,
doc=
"Overall conversion of natural gas into gasoline per module of this type [kB/MMSCF]"
)
def module_conversion(m, mtype):
return float(module_sheet[mtype]['Conversion [kB/MMSCF]'])
site_sheet = xlsx_data['sites'].set_index('Potential site')
m.potential_sites = Set(initialize=site_sheet.index.tolist())
m.site_pairs = Set(doc="Pairs of potential sites",
initialize=m.potential_sites * m.potential_sites,
filter=lambda _, x, y: not x == y)
@m.Param(m.potential_sites)
def site_x(m, site):
return float(site_sheet['x'][site])
@m.Param(m.potential_sites)
def site_y(m, site):
return float(site_sheet['y'][site])
well_sheet = xlsx_data['wells'].set_index('Well')
m.well_clusters = Set(initialize=well_sheet.index.tolist())
@m.Param(m.well_clusters)
def well_x(m, well):
return float(well_sheet['x'][well])
@m.Param(m.well_clusters)
def well_y(m, well):
return float(well_sheet['y'][well])
sched_sheet = xlsx_data['well-schedule']
decay_curve = [1] + [
3.69 * exp(-1.31 * (t + 1)**0.292) for t in range(m.project_life * 12)
]
well_profiles = {
well: [0 for _ in decay_curve]
for well in m.well_clusters
}
for _, well_info in sched_sheet.iterrows():
start_time = int(well_info['Month'])
prod = [0] * start_time + decay_curve[:len(decay_curve) - start_time]
prod = [x * float(well_info['max prod [MMSCF/d]']) for x in prod]
current_profile = well_profiles[well_info['well-cluster']]
well_profiles[well_info['well-cluster']] = [
val + prod[i] for i, val in enumerate(current_profile)
]
@m.Param(m.well_clusters,
m.time,
doc="Supply of gas from well cluster [MMSCF/day]")
def gas_supply(m, well, t):
return sum(well_profiles[well][t * 3:t * 3 + 2]) / 3
mkt_sheet = xlsx_data['markets'].set_index('Market')
m.markets = Set(initialize=mkt_sheet.index.tolist())
@m.Param(m.markets)
def mkt_x(m, mkt):
return float(mkt_sheet['x'][mkt])
@m.Param(m.markets)
def mkt_y(m, mkt):
return float(mkt_sheet['y'][mkt])
@m.Param(m.markets, doc="Gasoline demand [kBD]")
def mkt_demand(m, mkt):
return float(mkt_sheet['demand [kBD]'][mkt])
m.sources = Set(initialize=m.well_clusters | m.potential_sites)
m.destinations = Set(initialize=m.potential_sites | m.markets)
@m.Param(m.sources, m.destinations, doc="Distance [mi]")
def distance(m, src, dest):
if src in m.well_clusters:
src_x = m.well_x[src]
src_y = m.well_y[src]
else:
src_x = m.site_x[src]
src_y = m.site_y[src]
if dest in m.markets:
dest_x = m.mkt_x[dest]
dest_y = m.mkt_y[dest]
else:
dest_x = m.site_x[dest]
dest_y = m.site_y[dest]
return sqrt((src_x - dest_x)**2 + (src_y - dest_y)**2)
m.num_modules = Var(
m.module_types,
m.potential_sites,
m.time,
doc="Number of active modules of each type at a site in a period",
domain=Integers,
bounds=(0, 50),
initialize=1)
m.modules_transferred = Var(
m.module_types,
m.site_pairs,
m.time,
doc=
"Number of module transfers initiated from one site to another in a period.",
domain=Integers,
bounds=(0, 15),
initialize=0)
m.modules_purchased = Var(
m.module_types,
m.potential_sites,
m.time,
doc="Number of modules of each type purchased for a site in a period",
domain=Integers,
bounds=(0, 30),
initialize=1)
m.pipeline_unit_cost = Param(doc="MM$/mile", initialize=2)
@m.Param(m.time, doc="Module transport cost per mile [M$/100 miles]")
def module_transport_distance_cost(m, t):
return 50 * m.discount_factor[t]
@m.Param(m.time, doc="Module transport cost per unit [MM$/module]")
def module_transport_unit_cost(m, t):
return 3 * m.discount_factor[t]
@m.Param(m.time, doc="Stranded gas price [$/MSCF]")
def nat_gas_price(m, t):
return 5 * m.discount_factor[t]
@m.Param(m.time, doc="Gasoline price [$/gal]")
def gasoline_price(m, t):
return 2.5 * m.discount_factor[t]
@m.Param(m.time, doc="Gasoline transport cost [$/gal/100 miles]")
def gasoline_tranport_cost(m, t):
return 0.045 * m.discount_factor[t]
m.gal_per_bbl = Param(initialize=42, doc="Gallons per barrel")
m.days_per_period = Param(initialize=90, doc="Days in a production period")
m.learning_factor = Var(
m.module_types,
doc="Fraction of cost due to economies of mass production",
domain=NonNegativeReals,
bounds=(0, 1),
initialize=1)
@m.Disjunct(m.module_types)
def mtype_exists(disj, mtype):
disj.learning_factor_calc = Constraint(
expr=m.learning_factor[mtype] == (1 - m.learning_rate)**(
log(sum(m.modules_purchased[mtype, :, :])) / log(2)))
m.BigM[disj.learning_factor_calc] = 1
disj.require_module_purchases = Constraint(
expr=sum(m.modules_purchased[mtype, :, :]) >= 1)
@m.Disjunct(m.module_types)
def mtype_absent(disj, mtype):
disj.constant_learning_factor = Constraint(
expr=m.learning_factor[mtype] == 1)
@m.Disjunction(m.module_types)
def mtype_existence(m, mtype):
return [m.mtype_exists[mtype], m.mtype_absent[mtype]]
@m.Expression(m.module_types, m.time, doc="Module unit cost [MM$/module]")
def module_unit_cost(m, mtype, t):
return m.module_base_cost[mtype] * m.learning_factor[
mtype] * m.discount_factor[t]
m.production = Var(m.potential_sites,
m.time,
doc="Production of gasoline in a time period [kBD]",
domain=NonNegativeReals,
bounds=(0, 30),
initialize=10)
m.gas_consumption = Var(
m.potential_sites,
m.module_types,
m.time,
doc="Consumption of natural gas by each module type "
"at each site in a time period [MMSCF/d]",
domain=NonNegativeReals,
bounds=(0, 250),
initialize=50)
m.gas_flows = Var(
m.well_clusters,
m.potential_sites,
m.time,
doc="Flow of gas from a well cluster to a site [MMSCF/d]",
domain=NonNegativeReals,
bounds=(0, 200),
initialize=15)
m.product_flows = Var(
m.potential_sites,
m.markets,
m.time,
doc="Product shipments from a site to a market in a period [kBD]",
domain=NonNegativeReals,
bounds=(0, 30),
initialize=10)
@m.Constraint(m.potential_sites, m.module_types, m.time)
def consumption_capacity(m, site, mtype, t):
return m.gas_consumption[site, mtype, t] <= (
m.num_modules[mtype, site, t] * m.unit_gas_consumption[mtype])
@m.Constraint(m.potential_sites, m.time)
def production_limit(m, site, t):
return m.production[site, t] <= sum(
m.gas_consumption[site, mtype, t] * m.module_conversion[mtype]
for mtype in m.module_types)
@m.Expression(m.potential_sites, m.time)
def capacity(m, site, t):
return sum(m.num_modules[mtype, site, t] *
m.unit_gas_consumption[mtype] * m.module_conversion[mtype]
for mtype in m.module_types)
@m.Constraint(m.potential_sites, m.time)
def gas_supply_meets_consumption(m, site, t):
return sum(m.gas_consumption[site, :, t]) == sum(m.gas_flows[:, site,
t])
@m.Constraint(m.well_clusters, m.time)
def gas_supply_limit(m, well, t):
return sum(m.gas_flows[well, site, t]
for site in m.potential_sites) <= m.gas_supply[well, t]
@m.Constraint(m.potential_sites, m.time)
def gasoline_production_requirement(m, site, t):
return sum(m.product_flows[site, mkt, t]
for mkt in m.markets) == m.production[site, t]
@m.Constraint(m.potential_sites, m.module_types, m.time)
def module_balance(m, site, mtype, t):
if t >= m.module_setup_time:
modules_added = m.modules_purchased[mtype, site,
t - m.module_setup_time]
modules_transferred_in = sum(
m.modules_transferred[mtype, from_site, to_site,
t - m.module_setup_time]
for from_site, to_site in m.site_pairs if to_site == site)
else:
modules_added = 0
modules_transferred_in = 0
if t >= 1:
existing_modules = m.num_modules[mtype, site, t - 1]
else:
existing_modules = 0
modules_transferred_out = sum(m.modules_transferred[mtype, from_site,
to_site, t]
for from_site, to_site in m.site_pairs
if from_site == site)
return m.num_modules[mtype, site,
t] == (existing_modules + modules_added +
modules_transferred_in -
modules_transferred_out)
@m.Disjunct(m.potential_sites)
def site_active(disj, site):
pass
@m.Disjunct(m.potential_sites)
def site_inactive(disj, site):
disj.no_production = Constraint(expr=sum(m.production[site, :]) == 0)
disj.no_gas_consumption = Constraint(
expr=sum(m.gas_consumption[site, :, :]) == 0)
disj.no_gas_flows = Constraint(expr=sum(m.gas_flows[:, site, :]) == 0)
disj.no_product_flows = Constraint(
expr=sum(m.product_flows[site, :, :]) == 0)
disj.no_modules = Constraint(expr=sum(m.num_modules[:, site, :]) == 0)
disj.no_modules_transferred = Constraint(expr=sum(
m.modules_transferred[mtypes, from_site, to_site, t]
for mtypes in m.module_types for from_site, to_site in m.site_pairs
for t in m.time if from_site == site or to_site == site) == 0)
disj.no_modules_purchased = Constraint(expr=sum(
m.modules_purchased[mtype, site, t] for mtype in m.module_types
for t in m.time) == 0)
@m.Disjunction(m.potential_sites)
def site_active_or_not(m, site):
return [m.site_active[site], m.site_inactive[site]]
@m.Disjunct(m.well_clusters, m.potential_sites)
def pipeline_exists(disj, well, site):
pass
@m.Disjunct(m.well_clusters, m.potential_sites)
def pipeline_absent(disj, well, site):
disj.no_natural_gas_flow = Constraint(expr=sum(m.gas_flows[well, site,
t]
for t in m.time) == 0)
@m.Disjunction(m.well_clusters, m.potential_sites)
def pipeline_existence(m, well, site):
return [m.pipeline_exists[well, site], m.pipeline_absent[well, site]]
# Objective Function Construnction
@m.Expression(m.potential_sites, doc="MM$")
def product_revenue(m, site):
return sum(m.product_flows[site, mkt, t] # kBD
* 1000 # bbl/kB
/ 1E6 # $ to MM$
* m.days_per_period * m.gasoline_price[t] * m.gal_per_bbl
for mkt in m.markets for t in m.time)
@m.Expression(m.potential_sites, doc="MM$")
def raw_material_cost(m, site):
return sum(m.gas_consumption[site, mtype, t] * m.days_per_period /
1E6 # $ to MM$
* m.nat_gas_price[t] * 1000 # MMSCF to MSCF
for mtype in m.module_types for t in m.time)
@m.Expression(
m.potential_sites,
m.markets,
doc="Aggregate cost to transport gasoline from a site to market [MM$]")
def product_transport_cost(m, site, mkt):
return sum(m.product_flows[site, mkt, t] * m.gal_per_bbl *
1000 # bbl/kB
/ 1E6 # $ to MM$
* m.distance[site, mkt] / 100 * m.gasoline_tranport_cost[t]
for t in m.time)
@m.Expression(m.well_clusters, m.potential_sites, doc="MM$")
def pipeline_construction_cost(m, well, site):
return (m.pipeline_unit_cost * m.distance[well, site] *
m.pipeline_exists[well, site].indicator_var)
# Module transport cost
@m.Expression(m.site_pairs, doc="MM$")
def module_relocation_cost(m, from_site, to_site):
return sum(m.modules_transferred[mtype, from_site, to_site, t] *
m.distance[from_site, to_site] / 100 *
m.module_transport_distance_cost[t] / 1E3 # M$ to MM$
+ m.modules_transferred[mtype, from_site, to_site, t] *
m.module_transport_unit_cost[t] for mtype in m.module_types
for t in m.time)
@m.Expression(m.potential_sites, doc="MM$")
def module_purchase_cost(m, site):
return sum(m.module_unit_cost[mtype, t] *
m.modules_purchased[mtype, site, t]
for mtype in m.module_types for t in m.time)
@m.Expression(doc="MM$")
def profit(m):
return (summation(m.product_revenue) - summation(m.raw_material_cost) -
summation(m.product_transport_cost) -
summation(m.pipeline_construction_cost) -
summation(m.module_relocation_cost) -
summation(m.module_purchase_cost))
m.neg_profit = Objective(expr=-m.profit)
# Tightening constraints
@m.Constraint(doc="Limit total module purchases over project span.")
def restrict_module_purchases(m):
return sum(m.modules_purchased[...]) <= 5
@m.Constraint(m.site_pairs, doc="Limit transfers between any two sites")
def restrict_module_transfers(m, from_site, to_site):
return sum(m.modules_transferred[:, from_site, to_site, :]) <= 5
return m
def build_model(use_cafaro_approximation, num_stages):
"""Build the model."""
m = ConcreteModel()
m.hot_process_streams = Set(initialize=['H1', 'H2'])
m.cold_process_streams = Set(initialize=['C1', 'C2'])
m.process_streams = m.hot_process_streams | m.cold_process_streams
m.hot_utility_streams = Set(initialize=['steam'])
m.cold_utility_streams = Set(initialize=['water'])
m.hot_streams = Set(
initialize=m.hot_process_streams | m.hot_utility_streams)
m.cold_streams = Set(
initialize=m.cold_process_streams | m.cold_utility_streams)
m.utility_streams = Set(
initialize=m.hot_utility_streams | m.cold_utility_streams)
m.streams = Set(
initialize=m.process_streams | m.utility_streams)
m.valid_matches = Set(
initialize=(m.hot_process_streams * m.cold_streams) |
(m.hot_utility_streams * m.cold_process_streams),
doc="Match all hot streams to cold streams, but exclude "
"matches between hot and cold utilities.")
# m.EMAT = Param(doc="Exchanger minimum approach temperature [K]",
# initialize=1)
# Unused right now, but could be used for variable bound tightening
# in the LMTD calculation.
m.stages = RangeSet(num_stages)
m.T_in = Param(
m.streams, doc="Inlet temperature of stream [K]",
initialize={'H1': 443,
'H2': 423,
'C1': 293,
'C2': 353,
'steam': 450,
'water': 293})
m.T_out = Param(
m.streams, doc="Outlet temperature of stream [K]",
initialize={'H1': 333,
'H2': 303,
'C1': 408,
'C2': 413,
'steam': 450,
'water': 313})
m.heat_exchanged = Var(
m.valid_matches, m.stages,
domain=NonNegativeReals,
doc="Heat exchanged from hot stream to cold stream in stage [kW]",
initialize=1, bounds=(0, 5000))
m.overall_FCp = Param(
m.process_streams,
doc="Flow times heat capacity of stream [kW / K]",
initialize={'H1': 30,
'H2': 15,
'C1': 20,
'C2': 40})
m.utility_usage = Var(
m.utility_streams,
doc="Hot or cold utility used [kW]",
domain=NonNegativeReals, initialize=1, bounds=(0, 5000))
m.stage_entry_T = Var(
m.streams, m.stages,
doc="Temperature of stream at stage entry.",
initialize=350,
bounds=(293, 450) # TODO set to be equal to min and max temps
)
m.stage_exit_T = Var(
m.streams, m.stages,
doc="Temperature of stream at stage exit.",
initialize=350,
bounds=(293, 450) # TODO set to be equal to min and max temps
)
# Improve bounds on stage entry and exit temperatures
for strm, stg in m.process_streams * m.stages:
m.stage_entry_T[strm, stg].setlb(
min(value(m.T_in[strm]), value(m.T_out[strm])))
m.stage_exit_T[strm, stg].setlb(
min(value(m.T_in[strm]), value(m.T_out[strm])))
m.stage_entry_T[strm, stg].setub(
max(value(m.T_in[strm]), value(m.T_out[strm])))
m.stage_exit_T[strm, stg].setub(
max(value(m.T_in[strm]), value(m.T_out[strm])))
for strm, stg in m.utility_streams * m.stages:
_fix_and_bound(m.stage_entry_T[strm, stg], m.T_in[strm])
_fix_and_bound(m.stage_exit_T[strm, stg], m.T_out[strm])
for strm in m.hot_process_streams:
_fix_and_bound(m.stage_entry_T[strm, 1], m.T_in[strm])
_fix_and_bound(m.stage_exit_T[strm, num_stages], m.T_out[strm])
for strm in m.cold_process_streams:
_fix_and_bound(m.stage_exit_T[strm, 1], m.T_out[strm])
_fix_and_bound(m.stage_entry_T[strm, num_stages], m.T_in[strm])
m.BigM = Suffix(direction=Suffix.LOCAL)
m.utility_unit_cost = Param(
m.utility_streams,
doc="Annual unit cost of utilities [$/kW]",
initialize={'steam': 80, 'water': 20})
m.module_sizes = Set(initialize=[10, 50, 100])
m.max_num_modules = Param(m.module_sizes, initialize={
# 5: 100,
10: 50,
50: 10,
100: 5,
# 250: 2
}, doc="maximum number of each module size available.")
m.exchanger_fixed_unit_cost = Param(
m.valid_matches, default=2000)
m.exchanger_area_cost_factor = Param(
m.valid_matches, default=1000,
initialize={
('steam', cold): 1200
for cold in m.cold_process_streams},
doc="1200 for heaters. 1000 for all other exchangers.")
m.area_cost_exponent = Param(default=0.6)
if use_cafaro_approximation:
k, b = calculate_cafaro_coefficients(10, 500, m.area_cost_exponent)
m.cafaro_k = Param(default=k)
m.cafaro_b = Param(default=b)
@m.Param(m.valid_matches, m.module_sizes,
doc="Area cost factor for modular exchangers.")
def module_area_cost_factor(m, hot, cold, area):
if hot == 'steam':
return 1300
else:
return 1100
m.module_fixed_unit_cost = Param(default=0)
m.module_area_cost_exponent = Param(default=0.6)
@m.Param(m.valid_matches, m.module_sizes,
doc="Cost of a module with a particular area.")
def module_area_cost(m, hot, cold, area):
return (m.module_area_cost_factor[hot, cold, area]
* area ** m.module_area_cost_exponent)
m.U = Param(
m.valid_matches,
default=0.8,
initialize={
('steam', cold): 1.2
for cold in m.cold_process_streams},
doc="Overall heat transfer coefficient."
"1.2 for heaters. 0.8 for everything else.")
m.exchanger_hot_side_approach_T = Var(
m.valid_matches, m.stages,
doc="Temperature difference between the hot stream inlet and cold "
"stream outlet of the exchanger.",
bounds=(0.1, 500), initialize=10
)
m.exchanger_cold_side_approach_T = Var(
m.valid_matches, m.stages,
doc="Temperature difference between the hot stream outlet and cold "
"stream inlet of the exchanger.",
bounds=(0.1, 500), initialize=10
)
m.LMTD = Var(
m.valid_matches, m.stages,
doc="Log mean temperature difference across the exchanger.",
bounds=(1, 500), initialize=10
)
# Improve LMTD bounds based on T values
for hot, cold, stg in m.valid_matches * m.stages:
hot_side_dT_LB = max(0, value(
m.stage_entry_T[hot, stg].lb - m.stage_exit_T[cold, stg].ub))
hot_side_dT_UB = max(0, value(
m.stage_entry_T[hot, stg].ub - m.stage_exit_T[cold, stg].lb))
cold_side_dT_LB = max(0, value(
m.stage_exit_T[hot, stg].lb - m.stage_entry_T[cold, stg].ub))
cold_side_dT_UB = max(0, value(
m.stage_exit_T[hot, stg].ub - m.stage_entry_T[cold, stg].lb))
m.LMTD[hot, cold, stg].setlb((
hot_side_dT_LB * cold_side_dT_LB * (
hot_side_dT_LB + cold_side_dT_LB) / 2) ** (1 / 3)
)
m.LMTD[hot, cold, stg].setub((
hot_side_dT_UB * cold_side_dT_UB * (
hot_side_dT_UB + cold_side_dT_UB) / 2) ** (1 / 3)
)
m.exchanger_fixed_cost = Var(
m.stages, m.valid_matches,
doc="Fixed cost for an exchanger between a hot and cold stream.",
domain=NonNegativeReals, bounds=(0, 1E5), initialize=0)
m.exchanger_area = Var(
m.stages, m.valid_matches,
doc="Area for an exchanger between a hot and cold stream.",
domain=NonNegativeReals, bounds=(0, 500), initialize=5)
m.exchanger_area_cost = Var(
m.stages, m.valid_matches,
doc="Capital cost contribution from exchanger area.",
domain=NonNegativeReals, bounds=(0, 1E5), initialize=1000)
@m.Constraint(m.hot_process_streams)
def overall_hot_stream_heat_balance(m, strm):
return (m.T_in[strm] - m.T_out[strm]) * m.overall_FCp[strm] == (
sum(m.heat_exchanged[strm, cold, stg]
for cold in m.cold_streams for stg in m.stages))
@m.Constraint(m.cold_process_streams)
def overall_cold_stream_heat_balance(m, strm):
return (m.T_out[strm] - m.T_in[strm]) * m.overall_FCp[strm] == (
sum(m.heat_exchanged[hot, strm, stg]
for hot in m.hot_streams for stg in m.stages))
@m.Constraint(m.utility_streams)
def overall_utility_stream_usage(m, strm):
return m.utility_usage[strm] == (
sum(m.heat_exchanged[hot, strm, stg]
for hot in m.hot_process_streams
for stg in m.stages
) if strm in m.cold_utility_streams else 0 +
sum(m.heat_exchanged[strm, cold, stg]
for cold in m.cold_process_streams
for stg in m.stages
) if strm in m.hot_utility_streams else 0
)
@m.Constraint(m.stages, m.hot_process_streams,
doc="Hot side overall heat balance for a stage.")
def hot_stage_overall_heat_balance(m, stg, strm):
return ((m.stage_entry_T[strm, stg] - m.stage_exit_T[strm, stg])
* m.overall_FCp[strm]) == sum(
m.heat_exchanged[strm, cold, stg]
for cold in m.cold_streams)
@m.Constraint(m.stages, m.cold_process_streams,
doc="Cold side overall heat balance for a stage.")
def cold_stage_overall_heat_balance(m, stg, strm):
return ((m.stage_exit_T[strm, stg] - m.stage_entry_T[strm, stg])
* m.overall_FCp[strm]) == sum(
m.heat_exchanged[hot, strm, stg]
for hot in m.hot_streams)
@m.Constraint(m.stages, m.hot_process_streams)
def hot_stream_monotonic_T_decrease(m, stg, strm):
return m.stage_exit_T[strm, stg] <= m.stage_entry_T[strm, stg]
@m.Constraint(m.stages, m.cold_process_streams)
def cold_stream_monotonic_T_increase(m, stg, strm):
return m.stage_exit_T[strm, stg] >= m.stage_entry_T[strm, stg]
@m.Constraint(m.stages, m.hot_process_streams)
def hot_stream_stage_T_link(m, stg, strm):
return (
m.stage_exit_T[strm, stg] == m.stage_entry_T[strm, stg + 1]
) if stg < num_stages else Constraint.NoConstraint
@m.Constraint(m.stages, m.cold_process_streams)
def cold_stream_stage_T_link(m, stg, strm):
return (
m.stage_entry_T[strm, stg] == m.stage_exit_T[strm, stg + 1]
) if stg < num_stages else Constraint.NoConstraint
@m.Expression(m.valid_matches, m.stages)
def exchanger_capacity(m, hot, cold, stg):
return m.exchanger_area[stg, hot, cold] * (
m.U[hot, cold] * (
m.exchanger_hot_side_approach_T[hot, cold, stg] *
m.exchanger_cold_side_approach_T[hot, cold, stg] *
(m.exchanger_hot_side_approach_T[hot, cold, stg] +
m.exchanger_cold_side_approach_T[hot, cold, stg]) / 2
) ** (1 / 3))
def _exchanger_exists(disj, hot, cold, stg):
disj.indicator_var.value = 1
# Log mean temperature difference calculation
disj.LMTD_calc = Constraint(
doc="Log mean temperature difference",
expr=m.LMTD[hot, cold, stg] == (
m.exchanger_hot_side_approach_T[hot, cold, stg] *
m.exchanger_cold_side_approach_T[hot, cold, stg] *
(m.exchanger_hot_side_approach_T[hot, cold, stg] +
m.exchanger_cold_side_approach_T[hot, cold, stg]) / 2
) ** (1 / 3)
)
m.BigM[disj.LMTD_calc] = 160
# disj.MTD_calc = Constraint(
# doc="Mean temperature difference",
# expr=m.LMTD[hot, cold, stg] <= (
# m.exchanger_hot_side_approach_T[hot, cold, stg] +
# m.exchanger_cold_side_approach_T[hot, cold, stg]) / 2
# )
# Calculation of the approach temperatures
if hot in m.hot_utility_streams:
disj.stage_hot_approach_temperature = Constraint(
expr=m.exchanger_hot_side_approach_T[hot, cold, stg] <=
m.T_in[hot] - m.stage_exit_T[cold, stg])
disj.stage_cold_approach_temperature = Constraint(
expr=m.exchanger_cold_side_approach_T[hot, cold, stg] <=
m.T_out[hot] - m.stage_entry_T[cold, stg])
elif cold in m.cold_utility_streams:
disj.stage_hot_approach_temperature = Constraint(
expr=m.exchanger_hot_side_approach_T[hot, cold, stg] <=
m.stage_entry_T[hot, stg] - m.T_out[cold])
disj.stage_cold_approach_temperature = Constraint(
expr=m.exchanger_cold_side_approach_T[hot, cold, stg] <=
m.stage_exit_T[hot, stg] - m.T_in[cold])
else:
disj.stage_hot_approach_temperature = Constraint(
expr=m.exchanger_hot_side_approach_T[hot, cold, stg] <=
m.stage_entry_T[hot, stg]
- m.stage_exit_T[cold, stg])
disj.stage_cold_approach_temperature = Constraint(
expr=m.exchanger_cold_side_approach_T[hot, cold, stg] <=
m.stage_exit_T[hot, stg]
- m.stage_entry_T[cold, stg])
def _exchanger_absent(disj, hot, cold, stg):
disj.indicator_var.value = 0
disj.no_match_exchanger_cost = Constraint(
expr=m.exchanger_area_cost[stg, hot, cold] == 0)
disj.no_match_exchanger_area = Constraint(
expr=m.exchanger_area[stg, hot, cold] == 0)
disj.no_match_exchanger_fixed_cost = Constraint(
expr=m.exchanger_fixed_cost[stg, hot, cold] == 0)
disj.no_heat_exchange = Constraint(
expr=m.heat_exchanged[hot, cold, stg] == 0)
m.exchanger_exists = Disjunct(
m.valid_matches, m.stages,
doc="Disjunct for the presence of an exchanger between a "
"hot stream and a cold stream at a stage.", rule=_exchanger_exists)
m.exchanger_absent = Disjunct(
m.valid_matches, m.stages,
doc="Disjunct for the absence of an exchanger between a "
"hot stream and a cold stream at a stage.", rule=_exchanger_absent)
def _exchanger_exists_or_absent(m, hot, cold, stg):
return [m.exchanger_exists[hot, cold, stg],
m.exchanger_absent[hot, cold, stg]]
m.exchanger_exists_or_absent = Disjunction(
m.valid_matches, m.stages,
doc="Disjunction between presence or absence of an exchanger between "
"a hot stream and a cold stream at a stage.",
rule=_exchanger_exists_or_absent, xor=True)
# Only hot utility matches in first stage and cold utility matches in last
# stage
for hot, cold in m.valid_matches:
if hot not in m.utility_streams:
m.exchanger_exists[hot, cold, 1].deactivate()
m.exchanger_absent[hot, cold, 1].indicator_var.fix(1)
if cold not in m.utility_streams:
m.exchanger_exists[hot, cold, num_stages].deactivate()
m.exchanger_absent[hot, cold, num_stages].indicator_var.fix(1)
# Exclude utility-stream matches in middle stages
for hot, cold, stg in m.valid_matches * (m.stages - [1, num_stages]):
if hot in m.utility_streams or cold in m.utility_streams:
m.exchanger_exists[hot, cold, stg].deactivate()
m.exchanger_absent[hot, cold, stg].indicator_var.fix(1)
@m.Expression(m.utility_streams)
def utility_cost(m, strm):
return m.utility_unit_cost[strm] * m.utility_usage[strm]
m.total_cost = Objective(
expr=sum(m.utility_cost[strm] for strm in m.utility_streams)
+ sum(m.exchanger_fixed_cost[stg, hot, cold]
for stg in m.stages
for hot, cold in m.valid_matches)
+ sum(m.exchanger_area_cost[stg, hot, cold]
for stg in m.stages
for hot, cold in m.valid_matches),
sense=minimize
)
return m