def setup_pipeline_network(self, fluid_list):
"""Setup a pipeline network."""
self.nw = Network(fluids=fluid_list)
self.nw.set_attr(p_unit='bar', T_unit='C', iterinfo=False)
# %% components
# main components
pu = Pump('pump')
pi = Pipe('pipeline')
es = HeatExchangerSimple('energy balance closing')
closer = CycleCloser('cycle closer')
pu_pi = Connection(pu, 'out1', pi, 'in1')
pi_es = Connection(pi, 'out1', es, 'in1')
es_closer = Connection(es, 'out1', closer, 'in1')
closer_pu = Connection(closer, 'out1', pu, 'in1')
self.nw.add_conns(pu_pi, pi_es, es_closer, closer_pu)
# %% parametrization of components
pu.set_attr(eta_s=0.7)
pi.set_attr(pr=0.95, L=100, ks=1e-5, D='var', Q=0)
es.set_attr(pr=1)
# %% parametrization of connections
pu_pi.set_attr(p=20, T=100, m=10, fluid={self.nw.fluids[0]: 1})
# %% solving
self.nw.solve('design')
def setup(self):
"""Set up clausis rankine cycle with turbine driven feed water pump."""
self.Tamb = 20
self.pamb = 1
fluids = ['water']
self.nw = Network(fluids=fluids)
self.nw.set_attr(p_unit='bar', T_unit='C', h_unit='kJ / kg')
# create components
splitter1 = Splitter('splitter 1')
merge1 = Merge('merge 1')
turb = Turbine('turbine')
fwp_turb = Turbine('feed water pump turbine')
condenser = HeatExchangerSimple('condenser')
fwp = Pump('pump')
steam_generator = HeatExchangerSimple('steam generator')
cycle_close = CycleCloser('cycle closer')
# create busses
# power output bus
self.power = Bus('power_output')
self.power.add_comps({'comp': turb, 'char': 1})
# turbine driven feed water pump internal bus
self.fwp_power = Bus('feed water pump power', P=0)
self.fwp_power.add_comps(
{'comp': fwp_turb, 'char': 1},
{'comp': fwp, 'char': 1, 'base': 'bus'})
# heat input bus
self.heat = Bus('heat_input')
self.heat.add_comps({'comp': steam_generator, 'base': 'bus'})
self.nw.add_busses(self.power, self.fwp_power, self.heat)
# create connections
fs_in = Connection(cycle_close, 'out1', splitter1, 'in1', label='fs')
fs_fwpt = Connection(splitter1, 'out1', fwp_turb, 'in1')
fs_t = Connection(splitter1, 'out2', turb, 'in1')
fwpt_ws = Connection(fwp_turb, 'out1', merge1, 'in1')
t_ws = Connection(turb, 'out1', merge1, 'in2')
ws = Connection(merge1, 'out1', condenser, 'in1')
cond = Connection(condenser, 'out1', fwp, 'in1', label='cond')
fw = Connection(fwp, 'out1', steam_generator, 'in1', label='fw')
fs_out = Connection(steam_generator, 'out1', cycle_close, 'in1')
self.nw.add_conns(fs_in, fs_fwpt, fs_t, fwpt_ws, t_ws, ws, cond, fw,
fs_out)
# component parameters
turb.set_attr(eta_s=1)
fwp_turb.set_attr(eta_s=1)
condenser.set_attr(pr=1)
fwp.set_attr(eta_s=1)
steam_generator.set_attr(pr=1)
# connection parameters
fs_in.set_attr(m=10, p=120, T=600, fluid={'water': 1})
cond.set_attr(T=self.Tamb, x=0)
# solve network
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
def setup_Network_individual_offdesign(self):
"""Set up network for individual offdesign tests."""
self.nw = Network(['H2O'], T_unit='C', p_unit='bar', v_unit='m3 / s')
so = Source('source')
sp = Splitter('splitter', num_out=2)
self.pump1 = Pump('pump 1')
self.sc1 = SolarCollector('collector field 1')
v1 = Valve('valve1')
self.pump2 = Pump('pump 2')
self.sc2 = SolarCollector('collector field 2')
v2 = Valve('valve2')
me = Merge('merge', num_in=2)
si = Sink('sink')
self.pump1.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'])
self.pump2.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'])
self.sc1.set_attr(pr=0.95,
lkf_lin=3.33,
lkf_quad=0.011,
A=1252,
E=700,
Tamb=20,
eta_opt=0.92,
design=['pr'],
offdesign=['zeta'])
self.sc2.set_attr(pr=0.95,
lkf_lin=3.5,
lkf_quad=0.011,
A=700,
E=800,
Tamb=20,
eta_opt=0.92,
design=['pr'],
offdesign=['zeta'])
fl = {'H2O': 1}
inlet = Connection(so, 'out1', sp, 'in1', T=50, p=3, fluid=fl)
outlet = Connection(me, 'out1', si, 'in1', p=3)
self.sp_p1 = Connection(sp, 'out1', self.pump1, 'in1')
self.p1_sc1 = Connection(self.pump1, 'out1', self.sc1, 'in1')
self.sc1_v1 = Connection(self.sc1, 'out1', v1, 'in1', p=3.1, T=90)
v1_me = Connection(v1, 'out1', me, 'in1')
self.sp_p2 = Connection(sp, 'out2', self.pump2, 'in1')
self.p2_sc2 = Connection(self.pump2, 'out1', self.sc2, 'in1')
self.sc2_v2 = Connection(self.sc2, 'out1', v2, 'in1', p=3.1, m=0.1)
v2_me = Connection(v2, 'out1', me, 'in2')
self.nw.add_conns(inlet, outlet, self.sp_p1, self.p1_sc1, self.sc1_v1,
v1_me, self.sp_p2, self.p2_sc2, self.sc2_v2, v2_me)
def setup_clausius_rankine(self, fluid_list):
"""Setup a Clausius-Rankine cycle."""
self.nw = Network(fluids=fluid_list)
self.nw.set_attr(p_unit='bar', T_unit='C', iterinfo=True)
# %% components
# main components
turb = Turbine('turbine')
con = Condenser('condenser')
pu = Pump('pump')
steam_generator = HeatExchangerSimple('steam generator')
closer = CycleCloser('cycle closer')
# cooling water
so_cw = Source('cooling water inlet')
si_cw = Sink('cooling water outlet')
# %% connections
# main cycle
fs_in = Connection(closer, 'out1', turb, 'in1', label='livesteam')
ws = Connection(turb, 'out1', con, 'in1', label='wastesteam')
cond = Connection(con, 'out1', pu, 'in1', label='condensate')
fw = Connection(pu, 'out1', steam_generator, 'in1', label='feedwater')
fs_out = Connection(steam_generator, 'out1', closer, 'in1')
self.nw.add_conns(fs_in, ws, cond, fw, fs_out)
# cooling water
cw_in = Connection(so_cw, 'out1', con, 'in2')
cw_out = Connection(con, 'out2', si_cw, 'in1')
self.nw.add_conns(cw_in, cw_out)
# %% parametrization of components
turb.set_attr(eta_s=0.9)
con.set_attr(pr1=1, pr2=0.99, ttd_u=5)
steam_generator.set_attr(pr=0.9)
# %% parametrization of connections
fs_in.set_attr(p=100, T=500, m=100, fluid={self.nw.fluids[0]: 1})
fw.set_attr(h=200e3)
cw_in.set_attr(T=20, p=5, fluid={self.nw.fluids[0]: 1})
cw_out.set_attr(T=30)
# %% solving
self.nw.solve('design')
pu.set_attr(eta_s=0.7)
fw.set_attr(h=None)
self.nw.solve('design')
def __init__(self):
self.nw = Network(fluids=['BICUBIC::water'],
p_unit='bar',
T_unit='C',
h_unit='kJ / kg',
iterinfo=False)
# components
# main cycle
eco = HeatExchangerSimple('economizer')
eva = HeatExchangerSimple('evaporator')
sup = HeatExchangerSimple('superheater')
cc = CycleCloser('cycle closer')
hpt = Turbine('high pressure turbine')
sp1 = Splitter('splitter 1', num_out=2)
mpt = Turbine('mid pressure turbine')
sp2 = Splitter('splitter 2', num_out=2)
lpt = Turbine('low pressure turbine')
con = Condenser('condenser')
pu1 = Pump('feed water pump')
fwh1 = Condenser('feed water preheater 1')
fwh2 = Condenser('feed water preheater 2')
dsh = Desuperheater('desuperheater')
me2 = Merge('merge2', num_in=2)
pu2 = Pump('feed water pump 2')
pu3 = Pump('feed water pump 3')
me = Merge('merge', num_in=2)
# cooling water
cwi = Source('cooling water source')
cwo = Sink('cooling water sink')
# connections
# main cycle
cc_hpt = Connection(cc, 'out1', hpt, 'in1', label='feed steam')
hpt_sp1 = Connection(hpt, 'out1', sp1, 'in1', label='extraction1')
sp1_mpt = Connection(sp1, 'out1', mpt, 'in1', state='g')
mpt_sp2 = Connection(mpt, 'out1', sp2, 'in1', label='extraction2')
sp2_lpt = Connection(sp2, 'out1', lpt, 'in1')
lpt_con = Connection(lpt, 'out1', con, 'in1')
con_pu1 = Connection(con, 'out1', pu1, 'in1')
pu1_fwh1 = Connection(pu1, 'out1', fwh1, 'in2')
fwh1_me = Connection(fwh1, 'out2', me, 'in1', state='l')
me_fwh2 = Connection(me, 'out1', fwh2, 'in2', state='l')
fwh2_dsh = Connection(fwh2, 'out2', dsh, 'in2', state='l')
dsh_me2 = Connection(dsh, 'out2', me2, 'in1')
me2_eco = Connection(me2, 'out1', eco, 'in1', state='l')
eco_eva = Connection(eco, 'out1', eva, 'in1')
eva_sup = Connection(eva, 'out1', sup, 'in1')
sup_cc = Connection(sup, 'out1', cc, 'in1')
self.nw.add_conns(cc_hpt, hpt_sp1, sp1_mpt, mpt_sp2, sp2_lpt, lpt_con,
con_pu1, pu1_fwh1, fwh1_me, me_fwh2, fwh2_dsh,
dsh_me2, me2_eco, eco_eva, eva_sup, sup_cc)
# cooling water
cwi_con = Connection(cwi, 'out1', con, 'in2')
con_cwo = Connection(con, 'out2', cwo, 'in1')
self.nw.add_conns(cwi_con, con_cwo)
# preheating
sp1_dsh = Connection(sp1, 'out2', dsh, 'in1')
dsh_fwh2 = Connection(dsh, 'out1', fwh2, 'in1')
fwh2_pu2 = Connection(fwh2, 'out1', pu2, 'in1')
pu2_me2 = Connection(pu2, 'out1', me2, 'in2')
sp2_fwh1 = Connection(sp2, 'out2', fwh1, 'in1')
fwh1_pu3 = Connection(fwh1, 'out1', pu3, 'in1')
pu3_me = Connection(pu3, 'out1', me, 'in2')
self.nw.add_conns(sp1_dsh, dsh_fwh2, fwh2_pu2, pu2_me2, sp2_fwh1,
fwh1_pu3, pu3_me)
# busses
# power bus
self.power = Bus('power')
self.power.add_comps({
'comp': hpt,
'char': -1
}, {
'comp': mpt,
'char': -1
}, {
'comp': lpt,
'char': -1
}, {
'comp': pu1,
'char': -1
}, {
'comp': pu2,
'char': -1
}, {
'comp': pu3,
'char': -1
})
# heating bus
self.heat = Bus('heat')
self.heat.add_comps({
'comp': eco,
'char': 1
}, {
'comp': eva,
'char': 1
}, {
'comp': sup,
'char': 1
})
self.nw.add_busses(self.power, self.heat)
# parametrization
# components
hpt.set_attr(eta_s=0.9)
mpt.set_attr(eta_s=0.9)
lpt.set_attr(eta_s=0.9)
pu1.set_attr(eta_s=0.8)
pu2.set_attr(eta_s=0.8)
pu3.set_attr(eta_s=0.8)
eco.set_attr(pr=0.99)
eva.set_attr(pr=0.99)
sup.set_attr(pr=0.99)
con.set_attr(pr1=1, pr2=0.99, ttd_u=5)
fwh1.set_attr(pr1=1, pr2=0.99, ttd_u=5)
fwh2.set_attr(pr1=1, pr2=0.99, ttd_u=5)
dsh.set_attr(pr1=0.99, pr2=0.99)
# connections
eco_eva.set_attr(x=0)
eva_sup.set_attr(x=1)
cc_hpt.set_attr(m=200, T=650, p=100, fluid={'water': 1})
hpt_sp1.set_attr(p=20)
mpt_sp2.set_attr(p=3)
lpt_con.set_attr(p=0.05)
cwi_con.set_attr(T=20, p=10, fluid={'water': 1})
# test run
self.nw.solve('design')
document_model(self.nw)
sys_rf = Source('system return')
sys_ff = Sink('system feed')
sto_rf = Source('storage return')
sto_ff = Sink('storage feed')
# consumer system
cd = Condenser('condenser')
# evaporator system
valve = Valve('valve')
dr = Drum('drum')
ev = HeatExchanger('evaporator')
su = HeatExchanger('superheater')
pump_ev = Pump('evaporator reciculation pump')
# compressor-system
cp = Compressor('compressor 1')
# %% connections
# heating system interface
sys_IF = Connection(sys_rf, 'out1', cd, 'in2')
IF_sys = Connection(cd, 'out2', sys_ff, 'in1')
nw.add_conns(sys_IF, IF_sys)
# condenser, expansion valve
def setup(self):
# %% network setup
self.nw = Network(fluids=['water', 'NH3'],
T_unit='C',
p_unit='bar',
h_unit='kJ / kg',
m_unit='kg / s')
# %% components
# sources & sinks
cc_coolant = CycleCloser('coolant cycle closer')
cc_consumer = CycleCloser('consumer cycle closer')
amb_in = Source('source ambient')
amb_out = Sink('sink ambient')
ic_in = Source('source intercool')
ic_out = Sink('sink intercool')
# consumer system
cd = HeatExchanger('condenser')
rp = Pump('recirculation pump')
cons = HeatExchangerSimple('consumer')
# evaporator system
va = Valve('valve')
dr = Drum('drum')
ev = HeatExchanger('evaporator')
su = HeatExchanger('superheater')
pu = Pump('pump evaporator')
# compressor-system
cp1 = Compressor('compressor 1')
cp2 = Compressor('compressor 2')
he = HeatExchanger('intercooler')
# busses
self.power = Bus('total compressor power')
self.power.add_comps({
'comp': cp1,
'base': 'bus'
}, {
'comp': cp2,
'base': 'bus'
})
self.heat = Bus('total delivered heat')
self.heat.add_comps({'comp': cd, 'char': -1})
self.nw.add_busses(self.power, self.heat)
# %% connections
# consumer system
c_in_cd = Connection(cc_coolant, 'out1', cd, 'in1')
cb_rp = Connection(cc_consumer, 'out1', rp, 'in1')
rp_cd = Connection(rp, 'out1', cd, 'in2')
self.cd_cons = Connection(cd, 'out2', cons, 'in1')
cons_cf = Connection(cons, 'out1', cc_consumer, 'in1')
self.nw.add_conns(c_in_cd, cb_rp, rp_cd, self.cd_cons, cons_cf)
# connection condenser - evaporator system
cd_va = Connection(cd, 'out1', va, 'in1')
self.nw.add_conns(cd_va)
# evaporator system
va_dr = Connection(va, 'out1', dr, 'in1')
dr_pu = Connection(dr, 'out1', pu, 'in1')
pu_ev = Connection(pu, 'out1', ev, 'in2')
ev_dr = Connection(ev, 'out2', dr, 'in2')
dr_su = Connection(dr, 'out2', su, 'in2')
self.nw.add_conns(va_dr, dr_pu, pu_ev, ev_dr, dr_su)
self.amb_in_su = Connection(amb_in, 'out1', su, 'in1')
su_ev = Connection(su, 'out1', ev, 'in1')
ev_amb_out = Connection(ev, 'out1', amb_out, 'in1')
self.nw.add_conns(self.amb_in_su, su_ev, ev_amb_out)
# connection evaporator system - compressor system
su_cp1 = Connection(su, 'out2', cp1, 'in1')
self.nw.add_conns(su_cp1)
# compressor-system
cp1_he = Connection(cp1, 'out1', he, 'in1')
he_cp2 = Connection(he, 'out1', cp2, 'in1')
cp2_c_out = Connection(cp2, 'out1', cc_coolant, 'in1')
ic_in_he = Connection(ic_in, 'out1', he, 'in2')
he_ic_out = Connection(he, 'out2', ic_out, 'in1')
self.nw.add_conns(cp1_he, he_cp2, ic_in_he, he_ic_out, cp2_c_out)
# %% component parametrization
# condenser system
x = np.array([
0, 0.0625, 0.125, 0.1875, 0.25, 0.3125, 0.375, 0.4375, 0.5, 0.5625,
0.6375, 0.7125, 0.7875, 0.9, 0.9875, 1, 1.0625, 1.125, 1.175,
1.2125, 1.2375, 1.25
])
y = np.array([
0.0076, 0.1390, 0.2731, 0.4003, 0.5185, 0.6263, 0.7224, 0.8056,
0.8754, 0.9312, 0.9729, 1.0006, 1.0203, 1.0158, 1.0051, 1.0000,
0.9746, 0.9289, 0.8832, 0.8376, 0.7843, 0.7614
])
rp.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'],
eta_s_char={
'char_func': CharLine(x, y),
'param': 'm'
})
cons.set_attr(pr=1, design=['pr'], offdesign=['zeta'])
# evaporator system
x = np.linspace(0, 2.5, 26)
y = np.array([
0.000, 0.164, 0.283, 0.389, 0.488, 0.581, 0.670, 0.756, 0.840,
0.921, 1.000, 1.078, 1.154, 1.228, 1.302, 1.374, 1.446, 1.516,
1.585, 1.654, 1.722, 1.789, 1.855, 1.921, 1.986, 2.051
])
kA_char1 = {'char_func': CharLine(x, y), 'param': 'm'}
x = np.array([
0.0100, 0.0400, 0.0700, 0.1100, 0.1500, 0.2000, 0.2500, 0.3000,
0.3500, 0.4000, 0.4500, 0.5000, 0.5500, 0.6000, 0.6500, 0.7000,
0.7500, 0.8000, 0.8500, 0.9000, 0.9500, 1.0000, 1.5000, 2.0000
])
y = np.array([
0.0185, 0.0751, 0.1336, 0.2147, 0.2997, 0.4118, 0.5310, 0.6582,
0.7942, 0.9400, 0.9883, 0.9913, 0.9936, 0.9953, 0.9966, 0.9975,
0.9983, 0.9988, 0.9992, 0.9996, 0.9998, 1.0000, 1.0008, 1.0014
])
kA_char2 = {'char_func': CharLine(x, y), 'param': 'm'}
ev.set_attr(pr1=1,
pr2=.999,
ttd_l=5,
design=['ttd_l'],
offdesign=['kA_char'],
kA_char1=kA_char1,
kA_char2=kA_char2)
# no kA modification for hot side!
x = np.array([0, 1])
y = np.array([1, 1])
kA_char1 = {'char_func': CharLine(x, y), 'param': 'm'}
# characteristic line for superheater kA
x = np.array(
[0, 0.045, 0.136, 0.244, 0.43, 0.6, 0.7, 0.8, 0.9, 1, 1.1, 1.2])
y = np.array(
[0, 0.037, 0.112, 0.207, 0.5, 0.8, 0.85, 0.9, 0.95, 1, 1.04, 1.07])
kA_char2 = {'char_func': CharLine(x, y), 'param': 'm'}
su.set_attr(kA_char1=kA_char1,
kA_char2=kA_char2,
offdesign=['zeta1', 'zeta2', 'kA_char'])
x = np.array([
0, 0.0625, 0.125, 0.1875, 0.25, 0.3125, 0.375, 0.4375, 0.5, 0.5625,
0.6375, 0.7125, 0.7875, 0.9, 0.9875, 1, 1.0625, 1.125, 1.175,
1.2125, 1.2375, 1.25
])
y = np.array([
0.0076, 0.1390, 0.2731, 0.4003, 0.5185, 0.6263, 0.7224, 0.8056,
0.8754, 0.9312, 0.9729, 1.0006, 1.0203, 1.0158, 1.0051, 1.0000,
0.9746, 0.9289, 0.8832, 0.8376, 0.7843, 0.7614
])
pu.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'],
eta_s_char={
'char_func': CharLine(x, y),
'param': 'm'
})
# compressor system
x = np.array([0, 0.4, 1, 1.2])
y = np.array([0.5, 0.9, 1, 1.1])
cp1.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'],
eta_s_char={
'char_func': CharLine(x, y),
'param': 'm'
})
cp2.set_attr(eta_s=0.8,
design=['eta_s'],
offdesign=['eta_s_char'],
eta_s_char={
'char_func': CharLine(x, y),
'param': 'm'
})
# characteristic line for intercooler kA
x = np.linspace(0, 2.5, 26)
y = np.array([
0.0000, 0.2455, 0.3747, 0.4798, 0.5718, 0.6552, 0.7323, 0.8045,
0.8727, 0.9378, 1.0000, 1.0599, 1.1176, 1.1736, 1.2278, 1.2806,
1.3320, 1.3822, 1.4313, 1.4792, 1.5263, 1.5724, 1.6176, 1.6621,
1.7058, 1.7488
])
kA_char1 = {'char_func': CharLine(x, y), 'param': 'm'}
x = np.linspace(0, 2.5, 26)
y = np.array([
0.000, 0.164, 0.283, 0.389, 0.488, 0.581, 0.670, 0.756, 0.840,
0.921, 1.000, 1.078, 1.154, 1.228, 1.302, 1.374, 1.446, 1.516,
1.585, 1.654, 1.722, 1.789, 1.855, 1.921, 1.986, 2.051
])
kA_char2 = {'char_func': CharLine(x, y), 'param': 'm'}
he.set_attr(kA_char1=kA_char1,
kA_char2=kA_char2,
offdesign=['zeta1', 'zeta2', 'kA_char'])
# characteristic line for condenser kA
x = np.linspace(0, 2.5, 26)
y = np.array([
0.0000, 0.2455, 0.3747, 0.4798, 0.5718, 0.6552, 0.7323, 0.8045,
0.8727, 0.9378, 1.0000, 1.0599, 1.1176, 1.1736, 1.2278, 1.2806,
1.3320, 1.3822, 1.4313, 1.4792, 1.5263, 1.5724, 1.6176, 1.6621,
1.7058, 1.7488
])
kA_char1 = {'char_func': CharLine(x, y), 'param': 'm'}
x = np.linspace(0, 2.5, 26)
y = np.array([
0.000, 0.164, 0.283, 0.389, 0.488, 0.581, 0.670, 0.756, 0.840,
0.921, 1.000, 1.078, 1.154, 1.228, 1.302, 1.374, 1.446, 1.516,
1.585, 1.654, 1.722, 1.789, 1.855, 1.921, 1.986, 2.051
])
kA_char2 = {'char_func': CharLine(x, y), 'param': 'm'}
cd.set_attr(kA_char1=kA_char1,
kA_char2=kA_char2,
pr2=0.9998,
design=['pr2'],
offdesign=['zeta2', 'kA_char'])
# %% connection parametrization
# condenser system
c_in_cd.set_attr(fluid={'water': 0, 'NH3': 1}, p=60)
rp_cd.set_attr(T=60, fluid={'water': 1, 'NH3': 0}, p=10)
self.cd_cons.set_attr(T=105)
cd_va.set_attr(p=Ref(c_in_cd, 1, -0.01), Td_bp=-5, design=['Td_bp'])
# evaporator system cold side
pu_ev.set_attr(m=Ref(va_dr, 10, 0), p0=5)
dr_su.set_attr(p0=5, T=5)
su_cp1.set_attr(p=Ref(dr_su, 1, -0.05), Td_bp=5, design=['Td_bp', 'p'])
# evaporator system hot side
self.amb_in_su.set_attr(m=20, T=12, p=1, fluid={'water': 1, 'NH3': 0})
su_ev.set_attr(p=Ref(self.amb_in_su, 1, -0.001), design=['p'])
ev_amb_out.set_attr()
# compressor-system
cp1_he.set_attr(p=15)
he_cp2.set_attr(T=40, p=Ref(cp1_he, 1, -0.01), design=['T', 'p'])
ic_in_he.set_attr(p=1, T=20, m=5, fluid={'water': 1, 'NH3': 0})
he_ic_out.set_attr(p=Ref(ic_in_he, 1, -0.002), design=['p'])
def __init__(self, working_fluid):
"""Set up model."""
self.working_fluid = working_fluid
fluids = ['water', self.working_fluid, 'air']
self.nw = Network(fluids=fluids)
self.nw.set_attr(p_unit='bar', T_unit='C', h_unit='kJ / kg')
# geo parameters
self.geo_mass_flow = 200
geo_steam_share = 0.1
self.T_brine_in = 140
# ambient parameters
self.T_amb = 5
self.p_amb = 0.6
# main components
geo_steam = Source('geosteam source')
geo_brine = Source('geobrine source')
geo_reinjection = Sink('re-injection')
air_in = Source('air source')
air_out = Sink('air sink')
air_fan = Compressor('air fan')
air_cond = Condenser('condenser')
orc_cc = CycleCloser('orc cycle closer')
evap_splitter = Splitter('splitter evaporation')
evap_merge = Merge('merge evaporation')
evap_steam = Condenser('geosteam evaporator')
evap_brine = HeatExchanger('geobrine evaporator')
dr = Drum('drum')
geo_merge = Merge('merge brine')
pre = HeatExchanger('preheater')
feed_working_fluid_pump = Pump('feed pump')
tur = Turbine('turbine')
ihe = HeatExchanger('internal heat exchanger')
# busses
net_power = Bus('net power output')
net_power.add_comps(
{'comp': tur, 'char': 0.97},
{'comp': feed_working_fluid_pump, 'char': 0.97, 'base': 'bus'},
{'comp': air_fan, 'char': 0.97, 'base': 'bus'}
)
ORC_power_bus = Bus('cycle gross power output')
ORC_power_bus.add_comps(
{'comp': tur}, {'comp': feed_working_fluid_pump}
)
geothermal_bus = Bus('thermal input')
geothermal_bus.add_comps(
{'comp': pre, 'char': -1}, {'comp': evap_brine, 'char': -1},
{'comp': evap_steam, 'char': -1}
)
self.nw.add_busses(net_power, ORC_power_bus, geothermal_bus)
# turbine to condenser
c1 = Connection(orc_cc, 'out1', tur, 'in1', label='1')
c2 = Connection(tur, 'out1', ihe, 'in1', label='2')
c3 = Connection(ihe, 'out1', air_cond, 'in1', label='3')
self.nw.add_conns(c1, c2, c3)
# condenser to steam generator
c4 = Connection(air_cond, 'out1', feed_working_fluid_pump, 'in1', label='4')
c5 = Connection(feed_working_fluid_pump, 'out1', ihe, 'in2', label='5')
self.nw.add_conns(c4, c5)
# steam generator
c6 = Connection(ihe, 'out2', pre, 'in2', label='6')
c7 = Connection(pre, 'out2', dr, 'in1', label='7')
c8 = Connection(dr, 'out1', evap_splitter, 'in1', label='8')
c9 = Connection(evap_splitter, 'out2', evap_steam, 'in2', label='9')
c10 = Connection(evap_steam, 'out2', evap_merge, 'in2', label='10')
c11 = Connection(evap_splitter, 'out1', evap_brine, 'in2', label='11')
c12 = Connection(evap_brine, 'out2', evap_merge, 'in1', label='12')
c13 = Connection(evap_merge, 'out1', dr, 'in2', label='13')
c0 = Connection(dr, 'out2', orc_cc, 'in1', label='0')
self.nw.add_conns(c6, c7, c8, c11, c9, c12, c10, c13, c0)
# condenser cold side
c20 = Connection(air_in, 'out1', air_fan, 'in1', label='20')
c21 = Connection(air_fan, 'out1', air_cond, 'in2', label='21')
c22 = Connection(air_cond, 'out2', air_out, 'in1', label='22')
self.nw.add_conns(c20, c21, c22)
# geo source
c30 = Connection(geo_steam, 'out1', evap_steam, 'in1', label='30')
c31 = Connection(evap_steam, 'out1', geo_merge, 'in1', label='31')
c32 = Connection(geo_brine, 'out1', geo_merge, 'in2', label='32')
c33 = Connection(geo_merge, 'out1', evap_brine, 'in1', label='33')
self.nw.add_conns(c30, c31, c32, c33)
c34 = Connection(evap_brine, 'out1', pre, 'in1', label='34')
c35 = Connection(pre, 'out1', geo_reinjection, 'in1', label='35')
self.nw.add_conns(c34, c35)
# generate a set of stable starting values of every working fluid
# fluid settings
c6.set_attr(fluid={self.working_fluid: 1.0, 'air': 0.0, 'water': 0.0})
c20.set_attr(fluid={self.working_fluid: 0.0, 'air': 1.0, 'water': 0.0})
c30.set_attr(fluid={self.working_fluid: 0.0, 'air': 0.0, 'water': 1.0})
c32.set_attr(fluid={self.working_fluid: 0.0, 'air': 0.0, 'water': 1.0})
# connection parameters
p0 = PSI('P', 'T', self.T_brine_in + 273.15, 'Q', 1, self.working_fluid)
c1.set_attr(p0=p0 / 1e5)
ws_stable_h0 = (
PSI('H', 'T', self.T_amb + 273.15, 'Q', 1, self.working_fluid) +
0.5 * (
PSI('H', 'T', self.T_brine_in + 273.15, 'Q', 1, self.working_fluid) -
PSI('H', 'T', self.T_amb + 273.15, 'Q', 1, self.working_fluid)
)
) / 1e3
c2.set_attr(h=ws_stable_h0)
p0 = PSI('P', 'T', self.T_amb + 273.15, 'Q', 1, self.working_fluid)
c3.set_attr(Td_bp=5, design=['Td_bp'], p0=p0 / 1e5)
c5.set_attr(h=Ref(c4, 1, 1))
# steam generator
c30.set_attr(
m=self.geo_mass_flow * geo_steam_share,
T=self.T_brine_in, x=1, p0=5)
c32.set_attr(
m=self.geo_mass_flow * (1 - geo_steam_share),
T=self.T_brine_in, x=0)
c13.set_attr()
c12.set_attr(x=0.5)
c10.set_attr(x=0.5, design=['x'])
c34.set_attr(h=Ref(c33, 1, -50))
c7.set_attr(Td_bp=-2)
# main condenser
c20.set_attr(p=self.p_amb, T=self.T_amb)
c22.set_attr(T=self.T_amb + 15, p=self.p_amb)
# component parameters
# condensing
ihe.set_attr(pr1=0.98, pr2=0.98)
air_cond.set_attr(pr1=1, pr2=0.995, ttd_u=10)
air_fan.set_attr(eta_s=0.6)
# steam generator
evap_brine.set_attr(pr1=0.98, ttd_l=8)
pre.set_attr(pr1=0.98, pr2=0.98)
self.nw.set_attr(iterinfo=False)
self.nw.solve('design')
self.nw.save('stable_' + self.working_fluid)
# specify actual parameters
tur.set_attr(eta_s=0.9)
feed_working_fluid_pump.set_attr(eta_s=0.75)
c2.set_attr(h=None)
c5.set_attr(h=None)
c34.set_attr(h=None, T=Ref(c33, 1, -10))
self.nw.solve('design')
c22.set_attr(T=None)
c3.set_attr(Td_bp=None)
self.ude_IHE_size = UserDefinedEquation(
label='ihe deshuperheat ratio',
func=desuperheat, deriv=desuperheat_deriv,
latex={
'equation':
r'0 = h_3 - h_2 - x_\mathrm{IHE} \cdot \left(h_3 -'
r'h\left(p_2, T_5 + \Delta T_\mathrm{t,u,min} \right)'
r'\right)'},
conns=[
self.nw.get_conn('2'),
self.nw.get_conn('3'),
self.nw.get_conn('5')],
params={'distance': 0.0, 'ttd_min': 2}
)
if self.nw.lin_dep or self.nw.res[-1] > 1e-3:
msg = 'No stable solution found.'
raise TESPyNetworkError(msg)
print(
'Generated stable starting values for working fluid ' +
self.working_fluid + '.')
nw = Network(fluids=fluid_list,
p_unit='bar',
T_unit='C',
p_range=[0.1, 10],
T_range=[50, 1200])
# %% components
# sinks & sources
amb = Source('ambient')
sf = Source('fuel')
chbp = Sink('chimney bypass')
ch = Sink('chimney')
cw = Source('cooling water')
pump = Pump('cooling water pump')
cw_split = Splitter('cooling water splitter')
cw_merge = Merge('cooling water merge')
fg_split = Splitter('flue gas splitter')
fgc = HeatExchanger('flue gas cooler')
cons = HeatExchangerSimple('consumer')
cw_out = Sink('cooling water sink')
# combustion engine
ice = CombustionEngine(label='internal combustion engine')
# %% connections
# sources & sinks
cc = CycleCloser('coolant cycle closer')
cc_cons = CycleCloser('consumer cycle closer')
amb = Source('ambient air')
amb_out1 = Sink('sink ambient 1')
amb_out2 = Sink('sink ambient 2')
# ambient air system
sp = Splitter('splitter')
fan = Compressor('fan')
# consumer system
cd = Condenser('condenser')
dhp = Pump('district heating pump')
cons = HeatExchangerSimple('consumer')
# evaporator system
ves = Valve('valve')
dr = Drum('drum')
ev = HeatExchanger('evaporator')
su = HeatExchanger('superheater')
erp = Pump('evaporator reciculation pump')
# compressor-system
cp1 = Compressor('compressor 1')
cp2 = Compressor('compressor 2')
ic = HeatExchanger('intercooler')
# %% network
fluids = ['water']
nw = Network(fluids=fluids)
nw.set_attr(
p_unit='bar', T_unit='C', h_unit='kJ / kg',
p_range=[0.01, 150], h_range=[10, 5000])
# %% components
# main components
turb = Turbine('turbine')
con = Condenser('condenser')
pu = Pump('pump')
steam_generator = HeatExchangerSimple('steam generator')
closer = CycleCloser('cycle closer')
# cooling water
so_cw = Source('cooling water inlet')
si_cw = Sink('cooling water outlet')
# %% connections
# main cycle
fs_in = Connection(closer, 'out1', turb, 'in1')
ws = Connection(turb, 'out1', con, 'in1')
cond = Connection(con, 'out1', pu, 'in1')
fw = Connection(pu, 'out1', steam_generator, 'in1')
fs_out = Connection(steam_generator, 'out1', closer, 'in1')
class TestNetworkIndividualOffdesign:
def setup_Network_individual_offdesign(self):
"""Set up network for individual offdesign tests."""
self.nw = Network(['H2O'], T_unit='C', p_unit='bar', v_unit='m3 / s')
so = Source('source')
sp = Splitter('splitter', num_out=2)
self.pump1 = Pump('pump 1')
self.sc1 = SolarCollector('collector field 1')
v1 = Valve('valve1')
self.pump2 = Pump('pump 2')
self.sc2 = SolarCollector('collector field 2')
v2 = Valve('valve2')
me = Merge('merge', num_in=2)
si = Sink('sink')
self.pump1.set_attr(eta_s=0.8, design=['eta_s'],
offdesign=['eta_s_char'])
self.pump2.set_attr(eta_s=0.8, design=['eta_s'],
offdesign=['eta_s_char'])
self.sc1.set_attr(pr=0.95, lkf_lin=3.33, lkf_quad=0.011, A=1252, E=700,
Tamb=20, eta_opt=0.92, design=['pr'],
offdesign=['zeta'])
self.sc2.set_attr(pr=0.95, lkf_lin=3.5, lkf_quad=0.011, A=700, E=800,
Tamb=20, eta_opt=0.92, design=['pr'],
offdesign=['zeta'])
fl = {'H2O': 1}
inlet = Connection(so, 'out1', sp, 'in1', T=50, p=3, fluid=fl)
outlet = Connection(me, 'out1', si, 'in1', p=3)
self.sp_p1 = Connection(sp, 'out1', self.pump1, 'in1')
self.p1_sc1 = Connection(self.pump1, 'out1', self.sc1, 'in1')
self.sc1_v1 = Connection(self.sc1, 'out1', v1, 'in1', p=3.1, T=90)
v1_me = Connection(v1, 'out1', me, 'in1')
self.sp_p2 = Connection(sp, 'out2', self.pump2, 'in1')
self.p2_sc2 = Connection(self.pump2, 'out1', self.sc2, 'in1')
self.sc2_v2 = Connection(self.sc2, 'out1', v2, 'in1', p=3.1, m=0.1)
v2_me = Connection(v2, 'out1', me, 'in2')
self.nw.add_conns(inlet, outlet, self.sp_p1, self.p1_sc1, self.sc1_v1,
v1_me, self.sp_p2, self.p2_sc2, self.sc2_v2, v2_me)
def test_individual_design_path_on_connections_and_components(self):
"""Test individual design path specification."""
self.setup_Network_individual_offdesign()
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.sc2_v2.set_attr(m=0)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('design1')
v1_design = self.sc1_v1.v.val_SI
zeta_sc1_design = self.sc1.zeta.val
self.sc2_v2.set_attr(T=95, state='l', m=None)
self.sc1_v1.set_attr(m=0.001, T=None)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('design2')
v2_design = self.sc2_v2.v.val_SI
zeta_sc2_design = self.sc2.zeta.val
self.sc1_v1.set_attr(m=np.nan)
self.sc1_v1.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc2_v2.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc2.set_attr(design_path='design2')
self.pump2.set_attr(design_path='design2')
self.sp_p2.set_attr(design_path='design2')
self.p2_sc2.set_attr(design_path='design2')
self.sc2_v2.set_attr(design_path='design2')
self.nw.solve('offdesign', design_path='design1')
convergence_check(self.nw.lin_dep)
self.sc1.set_attr(E=500)
self.sc2.set_attr(E=950)
self.nw.solve('offdesign', design_path='design1')
convergence_check(self.nw.lin_dep)
self.sc2_v2.set_attr(design_path=np.nan)
# volumetric flow comparison
msg = ('Design path was set to None, is ' +
str(self.sc2_v2.design_path) + '.')
assert self.sc2_v2.design_path is None, msg
# volumetric flow comparison
msg = ('Value of volumetric flow must be ' + str(v1_design) + ', is ' +
str(self.sc1_v1.v.val_SI) + '.')
assert round(v1_design, 5) == round(self.sc1_v1.v.val_SI, 5), msg
msg = ('Value of volumetric flow must be ' + str(v2_design) + ', is ' +
str(self.sc2_v2.v.val_SI) + '.')
assert round(v2_design, 5) == round(self.sc2_v2.v.val_SI, 5), msg
# zeta value of solar collector comparison
msg = ('Value of zeta must be ' + str(zeta_sc1_design) + ', is ' +
str(self.sc1.zeta.val) + '.')
assert round(zeta_sc1_design, 0) == round(self.sc1.zeta.val, 0), msg
msg = ('Value of zeta must be ' + str(zeta_sc2_design) + ', is ' +
str(self.sc2.zeta.val) + '.')
assert round(zeta_sc2_design, 0) == round(self.sc2.zeta.val, 0), msg
shutil.rmtree('./design1', ignore_errors=True)
shutil.rmtree('./design2', ignore_errors=True)
def test_local_offdesign_on_connections_and_components(self):
"""Test local offdesign feature."""
self.setup_Network_individual_offdesign()
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.sc2_v2.set_attr(m=0)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('design1')
self.sc1_v1.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc2_v2.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc1.set_attr(local_offdesign=True, design_path='design1')
self.pump1.set_attr(local_offdesign=True, design_path='design1')
self.sp_p1.set_attr(local_offdesign=True, design_path='design1')
self.p1_sc1.set_attr(local_offdesign=True, design_path='design1')
self.sc1_v1.set_attr(local_offdesign=True, design_path='design1')
self.sc1.set_attr(E=500)
self.sc2_v2.set_attr(T=95, m=np.nan)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('design2')
# connections and components on side 1 must have switched to offdesign
msg = ('Solar collector outlet temperature must be different from ' +
'design value ' + str(round(self.sc1_v1.T.design - 273.15, 1)) +
', is ' + str(round(self.sc1_v1.T.val, 1)) + '.')
assert self.sc1_v1.T.design > self.sc1_v1.T.val, msg
msg = ('Parameter eta_s_char must be set for pump one.')
assert self.pump1.eta_s_char.is_set, msg
msg = ('Parameter v must be set for connection from solar collector1 '
'to pump1.')
assert self.sc1_v1.v.val_set, msg
shutil.rmtree('./design1', ignore_errors=True)
shutil.rmtree('./design2', ignore_errors=True)
def test_missing_design_path_local_offdesign_on_connections(self):
"""Test missing design path on connections in local offdesign mode."""
self.setup_Network_individual_offdesign()
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.sc2_v2.set_attr(m=0)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('design1')
self.sc1_v1.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc2_v2.set_attr(design=['T'], offdesign=['v'], state='l')
self.sc1.set_attr(local_offdesign=True, design_path='design1')
self.pump1.set_attr(local_offdesign=True, design_path='design1')
self.sp_p1.set_attr(local_offdesign=True, design_path='design1')
self.p1_sc1.set_attr(local_offdesign=True, design_path='design1')
self.sc1_v1.set_attr(local_offdesign=True)
self.sc1.set_attr(E=500)
self.sc2_v2.set_attr(T=95, m=np.nan)
try:
self.nw.solve('design', init_only=True)
except TESPyNetworkError:
pass
shutil.rmtree('./design1', ignore_errors=True)
# waste heat recovery
suph = HeatExchanger('superheater')
evap = HeatExchanger('evaporator')
drum = Drum('drum')
eco = HeatExchanger('economizer')
ch = Sink('chimney')
# steam turbine part
turb_hp = Turbine('steam turbine high pressure')
cond_dh = Condenser('district heating condenser')
mp_split = Splitter('mp split')
turb_lp = Turbine('steam turbine low pressure')
cond = Condenser('condenser')
merge = Merge('merge')
pump1 = Pump('feed water pump 1')
pump2 = Pump('feed water pump 2')
ls_out = Sink('ls sink')
ls_in = Source('ls source')
mp_valve = Valve('mp valve')
# district heating
dh_in = Source('district heating backflow')
dh_out = Sink('district heating feedflow')
# cooling water
cw_in = Source('cooling water backflow')
cw_out = Sink('cooling water feedflow')
# %% connections
# gas turbine part
m_unit='kg / s')
# %% components
# sources & sinks
c_in = Source('coolant in')
cons_closer = CycleCloser('consumer cycle closer')
amb_in = Source('source ambient')
amb_out = Sink('sink ambient')
# consumer system
cd = Condenser('condenser')
rp = Pump('recirculation pump')
cons = HeatExchangerSimple('consumer')
# evaporator system
va = Valve('valve')
dr = Drum('drum')
ev = HeatExchanger('evaporator')
su = HeatExchanger('superheater')
pu = Pump('pump evaporator')
cp1 = Sink('compressor 1')
# %% connections
# consumer system
m_unit='kg / s')
# %% components
cc = CycleCloser('cycle closer')
# heat pump system
cd = Condenser('condenser')
va = Valve('valve')
ev = HeatExchanger('evaporator')
cp = Compressor('compressor')
# geothermal heat collector
gh_in = Source('ground heat feed flow')
gh_out = Sink('ground heat return flow')
ghp = Pump('ground heat loop pump')
# heating system
hs_feed = Sink('heating system feed flow')
hs_ret = Source('heating system return flow')
hsp = Pump('heating system pump')
# %% connections
# heat pump system
cc_cd = Connection(cc, 'out1', cd, 'in1')
cd_va = Connection(cd, 'out1', va, 'in1')
va_ev = Connection(va, 'out1', ev, 'in2')
ev_cp = Connection(ev, 'out2', cp, 'in1')
cp_cc = Connection(cp, 'out1', cc, 'in1')
nw.add_conns(cc_cd, cd_va, va_ev, ev_cp, cp_cc)
def setup(self):
"""
Full model validation of SEGS model in TESPy vs. EBSILON.
Find original models at https://github.com/fwitte/SEGS_exergy.
"""
# specification of ambient state
self.pamb = 1.013
self.Tamb = 25
# setting up network
self.nw = Network(fluids=['water', 'INCOMP::TVP1', 'air'])
self.nw.set_attr(T_unit='C',
p_unit='bar',
h_unit='kJ / kg',
m_unit='kg / s',
s_unit="kJ / kgK")
# components definition
air_in = Source('Ambient air source', fkt_group='CW')
air_out = Sink('Ambient air sink', fkt_group='CW')
closer_pt = CycleCloser('Cycle closer pt', fkt_group='SF')
pt = ParabolicTrough('Parabolic trough', fkt_group='SF')
ptpump = Pump('HTF pump', fkt_group='SF')
closer = CycleCloser('Cycle closer power cycle', fkt_group='SG')
eco = HeatExchanger('Economizer', fkt_group='SG')
eva = HeatExchanger('Evaporator', fkt_group='SG')
sup = HeatExchanger('Superheater', fkt_group='SG')
drum = Drum('Drum', fkt_group='SG')
reh = HeatExchanger('Reheater', fkt_group='RH')
hpt1 = Turbine('HP turbine 1', fkt_group='HPT')
hpt2 = Turbine('HP turbine 2', fkt_group='HPT')
lpt1 = Turbine('LP turbine 1', fkt_group='LPT')
lpt2 = Turbine('LP turbine 2', fkt_group='LPT')
lpt3 = Turbine('LP turbine 3', fkt_group='LPT')
lpt4 = Turbine('LP turbine 4', fkt_group='LPT')
lpt5 = Turbine('LP turbine 5', fkt_group='LPT')
cond = Condenser('Condenser', fkt_group='CW')
condpump = Pump('Condenser pump', fkt_group='CW')
fwt = Merge('Feedwater tank', num_in=3, fkt_group='LPP')
fwp = Pump('Feedwater pump', fkt_group='FWP')
cwp = Pump('Cooling water pump', fkt_group='CW')
closer_cw = CycleCloser('Cycle closer cw', fkt_group='CW')
ct = HeatExchanger('Cooling tower', fkt_group='CW')
fan = Compressor('Cooling tower fan', fkt_group='CW')
sp1 = Splitter('Splitter 1', fkt_group='HPT')
sp2 = Splitter('Splitter 2', fkt_group='HPT')
sp3 = Splitter('Splitter 3', fkt_group='LPT')
sp4 = Splitter('Splitter 4', fkt_group='LPT')
sp5 = Splitter('Splitter 5', fkt_group='LPT')
sp6 = Splitter('Splitter 6', fkt_group='LPT')
sp7 = Splitter('Splitter 7', fkt_group='SF')
m1 = Merge('Merge 1', fkt_group='CW')
m2 = Merge('Merge 2', fkt_group='HPP')
m3 = Merge('Merge 3', fkt_group='LPP')
m4 = Merge('Merge 4', fkt_group='LPP')
m5 = Merge('Merge 5', fkt_group='SF')
v1 = Valve('Valve 1', fkt_group='HPP')
v2 = Valve('Valve 2', fkt_group='HPP')
v3 = Valve('Valve 3', fkt_group='LPP')
v4 = Valve('Valve 4', fkt_group='LPP')
v5 = Valve('Valve 5', fkt_group='LPP')
hppre1 = Condenser('High pressure preheater 1', fkt_group='HPP')
hppre2 = Condenser('High pressure preheater 2', fkt_group='HPP')
hppre1_sub = HeatExchanger('High pressure preheater 1 subcooling',
fkt_group='HPP')
hppre2_sub = HeatExchanger('High pressure preheater 2 subcooling',
fkt_group='HPP')
lppre1 = Condenser('Low pressure preheater 1', fkt_group='LPP')
lppre2 = Condenser('Low pressure preheater 2', fkt_group='LPP')
lppre3 = Condenser('Low pressure preheater 3', fkt_group='LPP')
lppre1_sub = HeatExchanger('Low pressure preheater 1 subcooling',
fkt_group='LPP')
lppre2_sub = HeatExchanger('Low pressure preheater 2 subcooling',
fkt_group='LPP')
lppre3_sub = HeatExchanger('Low pressure preheater 3 subcooling',
fkt_group='LPP')
# connections definition
# power cycle
c1 = Connection(sup, 'out2', closer, 'in1', label='1')
c2 = Connection(closer, 'out1', hpt1, 'in1', label='2')
c3 = Connection(hpt1, 'out1', sp1, 'in1', label='3')
c4 = Connection(sp1, 'out1', hpt2, 'in1', label='4')
c5 = Connection(hpt2, 'out1', sp2, 'in1', label='5')
c6 = Connection(sp2, 'out1', reh, 'in2', label='6')
c7 = Connection(reh, 'out2', lpt1, 'in1', label='7')
c8 = Connection(lpt1, 'out1', sp3, 'in1', label='8')
c9 = Connection(sp3, 'out1', lpt2, 'in1', label='9')
c10 = Connection(lpt2, 'out1', sp4, 'in1', label='10')
c11 = Connection(sp4, 'out1', lpt3, 'in1', label='11')
c12 = Connection(lpt3, 'out1', sp5, 'in1', label='12')
c13 = Connection(sp5, 'out1', lpt4, 'in1', label='13')
c14 = Connection(lpt4, 'out1', sp6, 'in1', label='14')
c15 = Connection(sp6, 'out1', lpt5, 'in1', label='15')
c16 = Connection(lpt5, 'out1', m1, 'in1', label='16')
c17 = Connection(m1, 'out1', cond, 'in1', label='17')
c18 = Connection(cond, 'out1', condpump, 'in1', label='18')
c19 = Connection(condpump, 'out1', lppre1, 'in2', label='19')
# c19 = Connection(condpump, 'out1', lppre1_sub, 'in2', label='19')
# c20 = Connection(lppre1_sub, 'out2', lppre1, 'in2', label='20')
c21 = Connection(lppre1, 'out2', lppre2, 'in2', label='21')
# c21 = Connection(lppre1, 'out2', lppre2_sub, 'in2', label='21')
# c22 = Connection(lppre2_sub, 'out2', lppre2, 'in2', label='22')
c23 = Connection(lppre2, 'out2', lppre3, 'in2', label='23')
# c23 = Connection(lppre2, 'out2', lppre3_sub, 'in2', label='23')
# c24 = Connection(lppre3_sub, 'out2', lppre3, 'in2', label='24')
c25 = Connection(lppre3, 'out2', fwt, 'in1', label='25')
c26 = Connection(fwt, 'out1', fwp, 'in1', label='26')
c27 = Connection(fwp, 'out1', hppre1, 'in2', label='27')
c29 = Connection(hppre1, 'out2', hppre2, 'in2', label='29')
c31 = Connection(hppre2, 'out2', eco, 'in2', label='31')
c36 = Connection(sp1, 'out2', hppre2, 'in1', label='36')
c37 = Connection(hppre2, 'out1', v1, 'in1', label='37')
c39 = Connection(v1, 'out1', m2, 'in2', label='39')
c40 = Connection(sp2, 'out2', m2, 'in1', label='40')
c41 = Connection(m2, 'out1', hppre1, 'in1', label='41')
c42 = Connection(hppre1, 'out1', v2, 'in1', label='42')
c44 = Connection(v2, 'out1', fwt, 'in2', label='44')
c45 = Connection(sp3, 'out2', fwt, 'in3', label='45')
c46 = Connection(sp4, 'out2', lppre3, 'in1', label='46')
c47 = Connection(lppre3, 'out1', v3, 'in1', label='47')
# c47 = Connection(lppre3, 'out1', lppre3_sub, 'in1', label='47')
# c48 = Connection(lppre3_sub, 'out1', v3, 'in1', label='48')
c49 = Connection(v3, 'out1', m3, 'in1', label='49')
c50 = Connection(sp5, 'out2', m3, 'in2', label='50')
c51 = Connection(m3, 'out1', lppre2, 'in1', label='51')
c52 = Connection(lppre2, 'out1', v4, 'in1', label='52')
# c52 = Connection(lppre2, 'out1', lppre2_sub, 'in1', label='52')
# c53 = Connection(lppre2_sub, 'out1', v4, 'in1', label='53')
c54 = Connection(v4, 'out1', m4, 'in2', label='54')
c55 = Connection(sp6, 'out2', m4, 'in1', label='55')
c56 = Connection(m4, 'out1', lppre1, 'in1', label='56')
c57 = Connection(lppre1, 'out1', v5, 'in1', label='57')
# c57 = Connection(lppre1, 'out1', lppre1_sub, 'in1', label='57')
# c58 = Connection(lppre1_sub, 'out1', v5, 'in1', label='58')
c59 = Connection(v5, 'out1', m1, 'in2', label='59')
# components from subsystem
c32 = Connection(eco, 'out2', drum, 'in1', label='32')
c33 = Connection(drum, 'out1', eva, 'in2', label='33')
c34 = Connection(eva, 'out2', drum, 'in2', label='34')
c35 = Connection(drum, 'out2', sup, 'in2', label='35')
c73 = Connection(sup, 'out1', eva, 'in1', label='73')
c74 = Connection(eva, 'out1', eco, 'in1', label='74')
# cooling water
c60 = Connection(cond, 'out2', closer_cw, 'in1', label='60')
c61 = Connection(closer_cw, 'out1', ct, 'in1', label='61')
c62 = Connection(ct, 'out1', cwp, 'in1', label='62')
c63 = Connection(cwp, 'out1', cond, 'in2', label='63')
# cooling tower
c64 = Connection(air_in, 'out1', fan, 'in1', label='64')
c65 = Connection(fan, 'out1', ct, 'in2', label='65')
c66 = Connection(ct, 'out2', air_out, 'in1', label='66')
# parabolic trough cycle
c70 = Connection(pt, 'out1', closer_pt, 'in1', label='67')
c71 = Connection(closer_pt, 'out1', sp7, 'in1', label='71')
c72 = Connection(sp7, 'out1', sup, 'in1', label='72')
c75 = Connection(eco, 'out1', m5, 'in1', label='75')
c76 = Connection(sp7, 'out2', reh, 'in1', label='76')
c77 = Connection(reh, 'out1', m5, 'in2', label='77')
c78 = Connection(m5, 'out1', ptpump, 'in1', label='78')
c79 = Connection(ptpump, 'out1', pt, 'in1', label='79')
# add connections to network
self.nw.add_conns(c1, c2, c3, c4, c5, c6, c7, c8, c9, c10, c11, c12,
c13, c14, c15, c16, c17, c18, c19, c21, c23, c25,
c26, c27, c29, c31, c32, c33, c34, c35, c36, c37,
c39, c40, c41, c42, c44, c45, c46, c47, c49, c50,
c51, c52, c54, c55, c56, c57, c59, c60, c61, c62,
c63, c64, c65, c66, c70, c71, c72, c73, c74, c75,
c76, c77, c78, c79)
# power bus
power = Bus('total output power')
power.add_comps({
'comp': hpt1,
'char': 0.97,
'base': 'component'
}, {
'comp': hpt2,
'char': 0.97,
'base': 'component'
}, {
'comp': lpt1,
'char': 0.97,
'base': 'component'
}, {
'comp': lpt2,
'char': 0.97,
'base': 'component'
}, {
'comp': lpt3,
'char': 0.97,
'base': 'component'
}, {
'comp': lpt4,
'char': 0.97,
'base': 'component'
}, {
'comp': lpt5,
'char': 0.97,
'base': 'component'
}, {
'comp': fwp,
'char': 0.95,
'base': 'bus'
}, {
'comp': condpump,
'char': 0.95,
'base': 'bus'
}, {
'comp': ptpump,
'char': 0.95,
'base': 'bus'
}, {
'comp': cwp,
'char': 0.95,
'base': 'bus'
}, {
'comp': fan,
'char': 0.95,
'base': 'bus'
})
heat_input_bus = Bus('heat input')
heat_input_bus.add_comps({'comp': pt, 'base': 'bus'})
exergy_loss_bus = Bus('exergy loss')
exergy_loss_bus.add_comps({
'comp': air_in,
'base': 'bus'
}, {'comp': air_out})
self.nw.add_busses(power, heat_input_bus, exergy_loss_bus)
# component parameters
pt.set_attr(doc=0.95,
aoi=0,
Tamb=25,
A='var',
eta_opt=0.73,
c_1=0.00496,
c_2=0.000691,
E=1000,
iam_1=1,
iam_2=1)
ptpump.set_attr(eta_s=0.6)
eco.set_attr()
eva.set_attr(ttd_l=5)
sup.set_attr()
hpt1.set_attr(eta_s=0.8376)
hpt2.set_attr(eta_s=0.8463)
lpt1.set_attr(eta_s=0.8623)
lpt2.set_attr(eta_s=0.917)
lpt3.set_attr(eta_s=0.9352)
lpt4.set_attr(eta_s=0.88)
lpt5.set_attr(eta_s=0.6445)
cond.set_attr(pr1=1, pr2=0.9, ttd_u=5)
condpump.set_attr(eta_s=0.7)
fwp.set_attr(eta_s=0.7)
cwp.set_attr(eta_s=0.7)
ct.set_attr(pr1=0.95)
fan.set_attr(eta_s=0.6)
lppre1.set_attr(pr1=1, ttd_u=5)
lppre2.set_attr(pr1=1, ttd_u=5)
lppre3.set_attr(pr1=1, ttd_u=5)
hppre1.set_attr(pr1=1, ttd_u=5)
hppre2.set_attr(pr1=1, ttd_u=5)
lppre1_sub.set_attr(pr1=1, pr2=1, ttd_l=10)
lppre2_sub.set_attr(pr1=1, pr2=1, ttd_l=10)
lppre3_sub.set_attr(pr1=1, pr2=1, ttd_l=10)
hppre1_sub.set_attr(pr1=1, pr2=1, ttd_l=10)
hppre2_sub.set_attr(pr1=1, pr2=1, ttd_l=10)
# connection parameters
# parabolic trough cycle
c70.set_attr(fluid={'TVP1': 1, 'water': 0, 'air': 0}, T=390, p=23.304)
c76.set_attr(m=Ref(c70, 0.1284, 0))
c73.set_attr(p=22.753)
c74.set_attr(p=21.167)
c78.set_attr(p=20.34)
c79.set_attr(p=41.024)
# cooling water
c62.set_attr(fluid={
'TVP1': 0,
'water': 1,
'air': 0
},
T=30,
p=self.pamb)
# cooling tower
c64.set_attr(fluid={
'water': 0,
'TVP1': 0,
'air': 1
},
p=self.pamb,
T=self.Tamb)
c65.set_attr(p=self.pamb + 0.0005)
c66.set_attr(p=self.pamb, T=30)
# power cycle
c32.set_attr(Td_bp=-2)
c34.set_attr(x=0.5)
c1.set_attr(fluid={'water': 1, 'TVP1': 0, 'air': 0}, p=100, T=371)
# steam generator pressure values
c31.set_attr(p=103.56)
c35.set_attr(p=103.42)
# turbine pressure values
c3.set_attr(p=33.61, m=38.969)
c5.set_attr(p=18.58)
c7.set_attr(p=17.1, T=371)
c8.set_attr(p=7.98)
c10.set_attr(p=2.73)
c12.set_attr(p=0.96)
c14.set_attr(p=0.29)
# preheater pressure values
c19.set_attr(p=14.755, state='l')
c21.set_attr(p=9.9975, state='l')
c23.set_attr(p=8.7012, state='l')
c25.set_attr(state='l')
c27.set_attr(p=125)
c29.set_attr(p=112)
# condensation
c16.set_attr(p=0.08)
# feedwater tank
c26.set_attr(x=0)
# a stable solution is generated for parts of the network
self.nw.solve(mode='design')
self.nw.del_conns(c19, c21, c23, c27, c29, c37, c42, c47, c52, c57)
c19 = Connection(condpump, 'out1', lppre1_sub, 'in2', label='19')
c20 = Connection(lppre1_sub, 'out2', lppre1, 'in2', label='20')
c21 = Connection(lppre1, 'out2', lppre2_sub, 'in2', label='21')
c22 = Connection(lppre2_sub, 'out2', lppre2, 'in2', label='22')
c23 = Connection(lppre2, 'out2', lppre3_sub, 'in2', label='23')
c24 = Connection(lppre3_sub, 'out2', lppre3, 'in2', label='24')
c27 = Connection(fwp, 'out1', hppre1_sub, 'in2', label='27')
c28 = Connection(hppre1_sub, 'out2', hppre1, 'in2', label='28')
c29 = Connection(hppre1, 'out2', hppre2_sub, 'in2', label='29')
c30 = Connection(hppre2_sub, 'out2', hppre2, 'in2', label='30')
c37 = Connection(hppre2, 'out1', hppre2_sub, 'in1', label='37')
c38 = Connection(hppre2_sub, 'out1', v1, 'in1', label='38')
c42 = Connection(hppre1, 'out1', hppre1_sub, 'in1', label='42')
c43 = Connection(hppre1_sub, 'out1', v2, 'in1', label='43')
c47 = Connection(lppre3, 'out1', lppre3_sub, 'in1', label='47')
c48 = Connection(lppre3_sub, 'out1', v3, 'in1', label='48')
c52 = Connection(lppre2, 'out1', lppre2_sub, 'in1', label='52')
c53 = Connection(lppre2_sub, 'out1', v4, 'in1', label='53')
c57 = Connection(lppre1, 'out1', lppre1_sub, 'in1', label='57')
c58 = Connection(lppre1_sub, 'out1', v5, 'in1', label='58')
self.nw.add_conns(c19, c20, c21, c22, c23, c24, c27, c28, c29, c30,
c37, c38, c42, c43, c47, c48, c52, c53, c57, c58)
# specification of missing parameters
c19.set_attr(p=14.755)
c21.set_attr(p=9.9975, state='l')
c23.set_attr(p=8.7012, state='l')
c27.set_attr(p=125)
c29.set_attr(p=112)
# solve final state
self.nw.solve(mode='design')
def test_Pump(self):
"""Test component properties of pumps."""
instance = Pump('pump')
self.setup_network(instance)
fl = {'N2': 0, 'O2': 0, 'Ar': 0, 'DowQ': 1, 'NH3': 0}
self.c1.set_attr(fluid=fl, v=1, p=5, T=50)
self.c2.set_attr(p=7)
instance.set_attr(eta_s=1)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
# test calculated value for efficiency
eta_s = ((isentropic(self.c1.get_flow(), self.c2.get_flow()) -
self.c1.h.val_SI) / (self.c2.h.val_SI - self.c1.h.val_SI))
msg = ('Value of isentropic efficiency must be ' + str(eta_s) +
', is ' + str(instance.eta_s.val) + '.')
assert eta_s == instance.eta_s.val, msg
# isentropic efficiency of 1 means inlet and outlet entropy are
# identical
s1 = round(s_mix_ph(self.c1.get_flow()), 4)
s2 = round(s_mix_ph(self.c2.get_flow()), 4)
msg = ('Value of entropy must be identical for inlet (' + str(s1) +
') and outlet (' + str(s2) +
') at 100 % isentropic efficiency.')
assert s1 == s2, msg
# specify realistic value for efficiency, outlet pressure from flow
# char
eta_s_d = 0.8
instance.set_attr(eta_s=eta_s_d)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
self.nw.save('tmp')
self.c2.set_attr(p=np.nan)
# flow char (pressure rise vs. volumetric flow)
x = [0, 0.2, 0.4, 0.6, 0.8, 1, 1.2, 1.4]
y = np.array([14, 13.5, 12.5, 11, 9, 6.5, 3.5, 0]) * 1e5
char = {'char_func': CharLine(x, y), 'is_set': True}
# apply flow char and eta_s char
instance.set_attr(flow_char=char,
eta_s=np.nan,
eta_s_char={
'char_func':
ldc('pump', 'eta_s_char', 'DEFAULT', CharLine),
'is_set':
True
})
self.nw.solve('offdesign', design_path='tmp')
convergence_check(self.nw.lin_dep)
# value for difference pressure
dp = 650000.0
msg = ('Value of pressure rise must be ' + str(dp) + ', is ' +
str(self.c2.p.val_SI - self.c1.p.val_SI) + '.')
assert round(self.c2.p.val_SI - self.c1.p.val_SI, 0) == dp, msg
# test ohter volumetric flow on flow char
self.c1.set_attr(v=0.9)
self.nw.solve('offdesign', design_path='tmp')
convergence_check(self.nw.lin_dep)
dp = 775000.0
msg = ('Value of pressure rise must be ' + str(dp) + ', is ' +
str(round(self.c2.p.val_SI - self.c1.p.val_SI, 0)) + '.')
assert round(self.c2.p.val_SI - self.c1.p.val_SI, 0) == dp, msg
# test value of isentropic efficiency
eta_s = round(
eta_s_d * instance.eta_s_char.char_func.evaluate(
self.c1.v.val_SI / self.c1.v.design), 3)
msg = ('Value of isentropic efficiency must be ' + str(eta_s) +
', is ' + str(instance.eta_s.val) + '.')
assert eta_s == round(instance.eta_s.val, 3), msg
instance.eta_s_char.is_set = False
# test boundaries of characteristic line:
# lower boundary
instance.set_attr(eta_s=0.8)
self.c1.set_attr(m=0, v=None)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
msg = ('Value of power must be ' + str(14e5) + ', is ' +
str(round(self.c2.p.val_SI - self.c1.p.val_SI, 0)) + '.')
assert round(self.c2.p.val_SI - self.c1.p.val_SI, 0) == 14e5, msg
# upper boundary
self.c1.set_attr(v=1.5, m=None)
self.nw.solve('design')
convergence_check(self.nw.lin_dep)
msg = ('Value of power must be 0, is ' +
str(round(self.c2.p.val_SI - self.c1.p.val_SI, 0)) + '.')
assert round(self.c2.p.val_SI - self.c1.p.val_SI, 0) == 0, msg
shutil.rmtree('./tmp', ignore_errors=True)
CH4 = Source('fuel source')
air = Source('ambient air')
# waste heat recovery
suph = HeatExchanger('superheater')
evap = HeatExchanger('evaporator')
dr = Drum('drum')
eco = HeatExchanger('economizer')
dh_whr = HeatExchanger('waste heat recovery')
ch = Sink('chimney')
# steam turbine part
turb = Turbine('steam turbine')
cond = Condenser('condenser')
pu = Pump('feed water pump')
cc = CycleCloser('ls cycle closer')
# district heating
dh_in = Source('district heating backflow')
dh_out = Sink('district heating feedflow')
# %% connections
# gas turbine part
c_in = Connection(air, 'out1', comp, 'in1')
c_out = Connection(comp, 'out1', c_c, 'in1')
fuel = Connection(CH4, 'out1', c_c, 'in2')
gt_in = Connection(c_c, 'out1', g_turb, 'in1')
gt_out = Connection(g_turb, 'out1', suph, 'in1')
nw.add_conns(c_in, c_out, fuel, gt_in, gt_out)
nw = Network(fluids=['water', 'NH3'], T_unit='C', p_unit='bar',
h_unit='kJ / kg', m_unit='kg / s')
# %% components
# sources & sinks
c_in = Source('coolant in')
cons_closer = CycleCloser('consumer cycle closer')
va = Sink('valve')
# consumer system
cd = Condenser('condenser')
rp = Pump('recirculation pump')
cons = HeatExchangerSimple('consumer')
# %% connections
# consumer system
c_in_cd = Connection(c_in, 'out1', cd, 'in1')
close_rp = Connection(cons_closer, 'out1', rp, 'in1')
rp_cd = Connection(rp, 'out1', cd, 'in2')
cd_cons = Connection(cd, 'out2', cons, 'in1')
cons_close = Connection(cons, 'out1', cons_closer, 'in1')
nw.add_conns(c_in_cd, close_rp, rp_cd, cd_cons, cons_close)