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"given" P[6]=7000[KPa] T[6]=500[C] P[7]=600[KPa] P[8]=10[KPa] m_dot=30[kg/s] m_frac=0.25 Fluid$ = 'Steam_IAPWS' "mass balance" m_dot[7]=m_frac*m_dot m_dot[3]=m_dot[7] m_dot[8]=(1-m_frac)*m_dot m_dot[1]=m_dot[8] m_dot[2]=m_dot[1] m_dot[4]=m_dot m_dot[5]=m_dot m_dot[6]=m_dot "pump I" P[1]=P[8] P[2]=P[7] w_p1_in = v[1] * (P[2]-P[1]) v[1]= volume(Fluid$, P=P[1], x=0) h[1]= enthalpy(Fluid$, P=P[1], x=0) h[2] =h[1] + w_p1_in "mixing chamber " P[3] = P[7] h[3] = enthalpy(Fluid$,P=P[3], x=0) m_dot[4] * h[4] = m_dot[2] * h[2] + m_dot[3] * h[3] "pump II" v[4] = volume(Fluid$, h=h[4], x=0) P[4]=P[7] P[5]=P[6] w_p2_in = v[4]*(P[5]-P[4]) h[5] = h[4] + w_p2_in "turbine" h[6] = enthalpy(Fluid$,P=P[6], T=T[6]) s[6] = entropy(Fluid$,P=P[6], T=T[6]) s[7]=s[6] h[7]=enthalpy ( Fluid$,P=P[7], s=s[7]) s[8]=s[6] h[8]=enthalpy ( Fluid$,P=P[8], s=s[8]) x[8]=quality(Fluid$,P=P[8],s=s[8]) "energy balance" Q_out_ph= m_dot[7] * (h[7] - h[3]) Q_in_b= m_dot[5] * (h[6] - h[5]) W_in_p= (m_dot[1] * w_p1_in) + (m_dot[4] * w_p2_in) W_out_t = m_dot[7]*(h[6]-h[7]) + m_dot[8]*(h[6]-h[8]) W_out_net = (W_out_t) - (W_in_p) epsilon_u = (W_out_net + Q_out_ph) / Q_in_b
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