Exemplo n.º 1
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                 T_range=[110, 1500],
                 h_range=[500, 4000])

# %% components
# gas turbine part
comp = cmp.compressor('compressor')
c_c = cmp.combustion_chamber('combustion')
g_turb = cmp.turbine('gas turbine')

CH4 = cmp.source('fuel source')
air = cmp.source('ambient air')

# waste heat recovery
suph = cmp.heat_exchanger('superheater')
evap = cmp.heat_exchanger('evaporator')
drum = cmp.drum('drum')
eco = cmp.heat_exchanger('economizer')
dh_whr = cmp.heat_exchanger('waste heat recovery')
ch = cmp.sink('chimney')

# steam turbine part
turb = cmp.turbine('steam turbine')
cond = cmp.condenser('condenser')
pump = cmp.pump('feed water pump')
ls_out = cmp.sink('ls sink')
ls_in = cmp.source('ls source')

# district heating
dh_in = cmp.source('district heating backflow')
dh_out = cmp.sink('district heating feedflow')
Exemplo n.º 2
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cf = cmp.sink('consumer feed flow')
amb_in = cmp.source('source ambient')
amb_out = cmp.sink('sink ambient')

cp1 = cmp.sink('compressor 1')

# consumer system

cd = cmp.condenser('condenser')
rp = cmp.pump('recirculation pump')
cons = cmp.heat_exchanger_simple('consumer')

# evaporator system

ves = cmp.vessel('vessel')
dr = cmp.drum('drum')
ev = cmp.heat_exchanger('evaporator')
su = cmp.heat_exchanger('superheater')
pu = cmp.pump('pump evaporator')

# %% connections

# consumer system

c_in_cd = con.connection(c_in, 'out1', cd, 'in1')

cb_rp = con.connection(cb, 'out1', rp, 'in1')
rp_cd = con.connection(rp, 'out1', cd, 'in2')
cd_cons = con.connection(cd, 'out2', cons, 'in1')
cons_cf = con.connection(cons, 'out1', cf, 'in1')
Exemplo n.º 3
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    def setup(self):
        # %% network

        self.nw = nwk.network(fluids=['water', 'NH3'],
                              T_unit='C',
                              p_unit='bar',
                              h_unit='kJ / kg',
                              m_unit='kg / s')

        # %% components

        # sources & sinks

        c_in = cmp.source('coolant in')
        cb = cmp.source('consumer back flow')
        cf = cmp.sink('consumer feed flow')
        amb_in = cmp.source('source ambient')
        amb_out = cmp.sink('sink ambient')
        ic_in = cmp.source('source intercool')
        ic_out = cmp.sink('sink intercool')

        c_out = cmp.sink('coolant out')

        # consumer system

        cd = cmp.heat_exchanger('condenser')
        rp = cmp.pump('recirculation pump')
        cons = cmp.heat_exchanger_simple('consumer')

        # evaporator system

        va = cmp.valve('valve')
        dr = cmp.drum('drum')
        ev = cmp.heat_exchanger('evaporator')
        su = cmp.heat_exchanger('superheater')
        pu = cmp.pump('pump evaporator')

        # compressor-system

        cp1 = cmp.compressor('compressor 1')
        cp2 = cmp.compressor('compressor 2')
        he = cmp.heat_exchanger('intercooler')

        # busses

        x = np.array([0, 0.7, 1, 1.3])
        y = 1 / np.array([0.8, 0.95, 1, 0.98]) / 0.9583794
        motor = cmp_char.characteristics(x=x, y=y)

        self.power = con.bus('total compressor power')
        self.power.add_comps({
            'c': cp1,
            'char': motor
        }, {
            'c': cp2,
            'char': motor
        })
        self.heat = con.bus('total delivered heat')
        self.heat.add_comps({'c': cd, 'char': -1})
        self.nw.add_busses(self.power, self.heat)

        # %% connections

        # consumer system

        c_in_cd = con.connection(c_in, 'out1', cd, 'in1')

        cb_rp = con.connection(cb, 'out1', rp, 'in1')
        rp_cd = con.connection(rp, 'out1', cd, 'in2')
        self.cd_cons = con.connection(cd, 'out2', cons, 'in1')
        cons_cf = con.connection(cons, 'out1', cf, 'in1')

        self.nw.add_conns(c_in_cd, cb_rp, rp_cd, self.cd_cons, cons_cf)

        # connection condenser - evaporator system

        cd_va = con.connection(cd, 'out1', va, 'in1')

        self.nw.add_conns(cd_va)

        # evaporator system

        va_dr = con.connection(va, 'out1', dr, 'in1')
        dr_pu = con.connection(dr, 'out1', pu, 'in1')
        pu_ev = con.connection(pu, 'out1', ev, 'in2')
        ev_dr = con.connection(ev, 'out2', dr, 'in2')
        dr_su = con.connection(dr, 'out2', su, 'in2')

        self.nw.add_conns(va_dr, dr_pu, pu_ev, ev_dr, dr_su)

        self.amb_in_su = con.connection(amb_in, 'out1', su, 'in1')
        su_ev = con.connection(su, 'out1', ev, 'in1')
        ev_amb_out = con.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 = con.connection(su, 'out2', cp1, 'in1')

        self.nw.add_conns(su_cp1)

        # compressor-system

        cp1_he = con.connection(cp1, 'out1', he, 'in1')
        he_cp2 = con.connection(he, 'out1', cp2, 'in1')
        cp2_c_out = con.connection(cp2, 'out1', c_out, 'in1')

        ic_in_he = con.connection(ic_in, 'out1', he, 'in2')
        he_ic_out = con.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

        rp.set_attr(eta_s=0.8, design=['eta_s'], offdesign=['eta_s_char'])
        cons.set_attr(pr=1, design=['pr'], offdesign=['zeta'])

        # evaporator system

        ev.set_attr(pr1=1,
                    pr2=.999,
                    ttd_l=5,
                    design=['ttd_l'],
                    offdesign=['kA'],
                    kA_char1='EVA_HOT',
                    kA_char2='EVA_COLD')

        # 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])
        su_char = hlp.dc_cc(x=x, y=y, param='m')
        su.set_attr(kA_char1='default',
                    kA_char2=su_char,
                    offdesign=['zeta1', 'zeta2', 'kA'])
        pu.set_attr(eta_s=0.8, design=['eta_s'], offdesign=['eta_s_char'])

        # compressor system

        cp1.set_attr(eta_s=0.8, design=['eta_s'], offdesign=['eta_s_char'])
        cp2.set_attr(eta_s=0.8, design=['eta_s'], offdesign=['eta_s_char'])

        # characteristic line for intercooler kA
        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
        ])
        he_char_cold = hlp.dc_cc(x=x, y=y, param='m')

        he.set_attr(kA_char1='default',
                    kA_char2=he_char_cold,
                    offdesign=['zeta1', 'zeta2', 'kA'])
        cd.set_attr(pr2=0.998, design=['pr2'], offdesign=['zeta2', 'kA'])

        # %% connection parametrization

        # condenser system

        c_in_cd.set_attr(fluid={'water': 0, 'NH3': 1}, p=60)
        cb_rp.set_attr(T=60, p=10, fluid={'water': 1, 'NH3': 0})
        self.cd_cons.set_attr(T=105)
        cons_cf.set_attr(h=con.ref(cb_rp, 1, 0), p=con.ref(cb_rp, 1, 0))
        cd_va.set_attr(p=con.ref(c_in_cd, 1, -1000),
                       Td_bp=-5,
                       h0=500,
                       design=['Td_bp'])

        # evaporator system cold side

        pu_ev.set_attr(m=con.ref(va_dr, 10, 0), p0=5)
        dr_su.set_attr(p0=5, T=5)
        su_cp1.set_attr(p=con.ref(dr_su, 1, -5000),
                        Td_bp=5,
                        h0=1700,
                        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=con.ref(self.amb_in_su, 1, -100), design=['p'])
        ev_amb_out.set_attr()

        # compressor-system

        cp1_he.set_attr(p=15)
        he_cp2.set_attr(T=40, p=con.ref(cp1_he, 1, -1000), 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=con.ref(ic_in_he, 1, -200), design=['p'])
        cp2_c_out.set_attr(p=con.ref(c_in_cd, 1, 0), h=con.ref(c_in_cd, 1, 0))