def run_simple_heat_pump_model():
nw = Network(['NH3'], T_unit='C', p_unit='bar', h_unit='kJ / kg')
nw.set_attr(iterinfo=False)
cp = Compressor('compressor')
cc = CycleCloser('cycle_closer')
cd = HeatExchangerSimple('condenser')
va = Valve('expansion valve')
ev = HeatExchangerSimple('evaporator')
cc_cd = Connection(cc, 'out1', cd, 'in1')
cd_va = Connection(cd, 'out1', va, 'in1')
va_ev = Connection(va, 'out1', ev, 'in1')
ev_cp = Connection(ev, 'out1', cp, 'in1')
cp_cc = Connection(cp, 'out1', cc, 'in1')
nw.add_conns(cc_cd, cd_va, va_ev, ev_cp, cp_cc)
cd.set_attr(pr=0.95, Q=-1e6)
ev.set_attr(pr=0.9)
cp.set_attr(eta_s=0.9)
cc_cd.set_attr(fluid={'NH3': 1})
cd_va.set_attr(Td_bp=-5, T=85)
ev_cp.set_attr(Td_bp=5, T=15)
nw.solve('design')
result_dict = {}
result_dict.update({
cp.label: cp.get_plotting_data()[1]
for cp in nw.comps.index if cp.get_plotting_data() is not None
})
return result_dict
# %% design calculation
path = 'R410A'
nw.solve('design')
# alternatively use:
# nw.solve('design', init_path=path)
print("\n##### DESIGN CALCULATION #####\n")
nw.print_results()
nw.save(path)
# %% plot h_log(p) diagram
# generate plotting data
result_dict = {}
result_dict.update({ev.label: ev.get_plotting_data()[2]})
result_dict.update({cp.label: cp.get_plotting_data()[1]})
result_dict.update({cd.label: cd.get_plotting_data()[1]})
result_dict.update({va.label: va.get_plotting_data()[1]})
# create plot
diagram = FluidPropertyDiagram('R410A')
diagram.set_unit_system(T='°C', p='bar', h='kJ/kg')
for key, data in result_dict.items():
result_dict[key]['datapoints'] = diagram.calc_individual_isoline(**data)
diagram.set_limits(x_min=200, x_max=500, y_min=0.8e1, y_max=0.8e2)
diagram.calc_isolines()
diagram.draw_isolines('logph')
for key in result_dict.keys():
