def calc_st2_o(self):
st2_o = Stream()
st2_o.fluid = self.st2_i.fluid
st2_o.flow_rate = self.st2_i.flow_rate
st2_o.pressure = self.st2_i.pressure - self.pressure_drop(
self.st2_i, self.st2_pip)
h = self.st2_i.h - (self.st1_i.h - self.st1_o.h) * self.st1_i.flow_rate[0] \
/ st2_o.flow_rate[0] / self.eta
h_l = PropsSI('H', 'P', st2_o.pressure, 'Q', 0, st2_o.fluid)
h_g = PropsSI('H', 'P', st2_o.pressure, 'Q', 1, st2_o.fluid)
if h_l <= h <= h_g:
st2_o.x = PropsSI('Q', 'P', st2_o.pressure, 'H', h, st2_o.fluid)
else:
st2_o.temperature = PropsSI('T', 'P', st2_o.pressure, 'H', h,
st2_o.fluid)
self.st2_o = st2_o
def calc_st2_i(self):
st2_i = Stream()
st2_i.fluid = self.st2_o.fluid
st2_i.flow_rate = self.st2_o.flow_rate
st2_i.pressure = self.st2_o.pressure + self.pressure_drop(
self.st2_o, self.st2_pip)
h = self.st2_o.h + (self.st1_i.h - self.st1_o.h) * self.st1_i.flow_rate[0] \
/ self.st2_o.flow_rate[0] * self.eta
h_l = PropsSI('H', 'P', st2_i.pressure, 'Q', 0, st2_i.fluid)
h_g = PropsSI('H', 'P', st2_i.pressure, 'Q', 1, st2_i.fluid)
if h_l <= h <= h_g:
st2_i.x = PropsSI('Q', 'P', st2_i.pressure, 'H', h, st2_i.fluid)
else:
st2_i.T = PropsSI('T', 'P', st2_i.pressure, 'H', h,
self.st2_i.fluid)
self.st2_i = st2_i
def get_st2(self, st1, pressure2):
st2 = Stream()
st2.fluid = st1.fluid
st2.flow_rate = st1.flow_rate
st2.pressure = pressure2
s_ideal = st1.s
h2_ideal = PropsSI('H', 'S', s_ideal, 'P', st2.pressure, st2.fluid)
eta = self.calculate_eta(st1.pressure, st2.pressure)
h2 = st1.h - eta * (st1.h - h2_ideal)
# Check whether it is saturated
h2_l = PropsSI('H', 'P', st2.pressure, 'Q', 0, st2.fluid)
h2_g = PropsSI('H', 'P', st2.pressure, 'Q', 1, st2.fluid)
if h2_l <= h2 <= h2_g:
st2.quality = PropsSI('Q', 'P', st2.pressure, 'H', h2, st2.fluid)
else:
st2.temperature = PropsSI('T', 'P', st2.pressure, 'H', h2,
st2.fluid)
return st2
st = Stream()
T0 = 100
T1 = 600
Delta_T = 50
s0 = 1e5
s1 = 1e8
s_num = 1000
S = np.linspace(s0, s1, s_num)
for T in range(T0, T1, Delta_T):
st.temperature_celcius = T
enthalpy = []
for i in range(s_num):
st.pressure = ps('P', 'S', S[i], 'T', st.temperature, 'water')
enthalpy.append(st.h)
plt.plot(S, enthalpy, label='$T$='+str(T)+'˚C')
h0 = []
h1 = []
num = 1000
S_s =
p = np.linspace(P0, P_s, num)
for i in range(num):
h0.append(ps('H','Q', 0, 'P', p[i], 'water'))
h1.append(ps('H','Q', 1, 'P', p[i], 'water'))
plt.plot(p, h0, '--', color = 'red')
plt.plot(p, h1, '--', color = 'red')
plt.legend(loc=1)
plt.xlabel("Pressure, Pa")
plt.ylabel("Enthalpy, J/kg")
from Stream import Stream
import numpy as np
from CoolProp.CoolProp import PropsSI as ps
import matplotlib.pyplot as plt
T_i = 500 # 初温，˚C
p_c = 4000 # 排气压力，Pa
mass_flow_rate = 61.3 # 主汽流量，kg/s
st_i = Stream()
st_i.temperature_celcius = T_i
st_i.flow_rate = mass_flow_rate
st_o = Stream()
st_o.pressure = p_c
st_c = Stream()
st_c.pressure = p_c
st_c.quality = 0
number = 40 # number组数据，压力从p0增加到p1
p0 = 10e6
p1 = 80e6
p = np.linspace(p0, p1, number)
T0 = 400
T1 = 850
Delta_T = 50
T = range(T0, T1, Delta_T)
for j in T:
st_i.temperature_celcius = j
efficiency_ideal = []
st = Stream()
T0 = 100
T1 = 600
Delta_T = 50
P0 = 1e5
P1 = 1e8
P_num = 1000
P = np.linspace(P0, P1, P_num)
for T in range(T0, T1, Delta_T):
st.temperature_celcius = T
enthalpy = []
for i in range(P_num):
st.pressure = P[i]
enthalpy.append(st.h)
plt.plot(enthalpy, P, label='$T$=' + str(T) + '˚C')
h0 = []
h1 = []
num = 1000
P_s = ps('P_CRITICAL', 'water')
p = np.linspace(P0, P_s, num)
for i in range(num):
h0.append(ps('H', 'Q', 0, 'P', p[i], 'water'))
h1.append(ps('H', 'Q', 1, 'P', p[i], 'water'))
plt.plot(h0, p, '--', color='red')
plt.plot(h1, p, '--', color='red')
plt.legend(loc=1)
plt.ylabel("Pressure, Pa")
plt.xlabel("Enthalpy, J/kg")
])
def get_A(self):
# Known inlet and outlet fluids to calculate the aperture area
self.st_o.fluid = self.st_i.fluid
self.st_o.flow_rate = self.st_i.flow_rate
# Assume no pressure loss
self.st_o.pressure = self.st_i.pressure
self.st_o.pressure = self.st_i.pressure
guess = np.array([500, 300, 19])
# options = optimset('Display','iter')
x = fsolve(self.CalcDishCollector3, guess)
self.A = x[2]
if __name__ == '__main__':
dc = DishCollector()
st_i = Stream()
st_i.fluid = Const.FLUID[2]
st_i.temperature = Const.convert_temperature(150, 'C', 'K')
st_i.pressure = 4e5
st_i.flow_rate[0] = 0.07
dc.st_i = st_i
st_o = Stream()
st_o.fluid = Const.FLUID[2]
# st_o.temperature = Const.convert_temperature(239.26, 'C', 'K')
st_o.pressure = 4e5
dc.st_o = st_o
dc.amb.irradiance = 700
dc.get_T_o()