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p_b=150 [bar]

T_max= 500 [C]

"p_reheat = 10 [Bar]"

T_reheat= 500 [c]

p_c = 0.1 [bar]

eta_turbine=0.85

eta_pump=0.95

{point 1}

p[1]=p_c

x[1]=0

h[1]=enthalpy(water,p=p[1],x=x[1])

s[1]=entropy(water,p=p[1],x=x[1])

{point 2}

p[2]=p_b

{isentropic}

s_s[2]=s[1]

h_s[2]=enthalpy(water,p=p[2],s=s_s[2])

{Actual}

eta_pump*(h[1]-h[2])=(h[1]-h_s[2])

{point 3}

p[3]=p_b

T[3]=T_max

h[3]=enthalpy(water,p=p[3],T=T[3])

S[3]=entropy(water,p=p[3],T=T[3])

{point 4}

p[4]=p_reheat

{isentropic}

s_s[4]=s[3]

h_s[4]=enthalpy(water,p=p[4],s=s_s[4])

{Actual}

eta_turbine*(h_s[4]-h[3])=(h[4]-h[3])

{point 5}

p[5]=p_reheat

T[5]=T_reheat

h[5]=enthalpy(water,p=p[5],T=T[5])

s[5]=entropy(water,p=p[5],T=T[5])

{point 6}

p[6] =p_c

{isentropic}

s_s[6]=s[5]

h_s[6]=enthalpy(water,p=p[6],s=s_s[6])

{Actual}

eta_turbine*(h_s[6]-h[5])=(h[6]-h[5])

{Work net}

w_net=((h[3]-h[4])+(h[5]-h[6]))-(h[2]-h[1])

{efficiency}

eta_th=w_net / q_in

q_in =(h[3]-h[2])+(h[5]-h[4])