Question 12.176E: A geothermal power plant on the Raft river uses isobutane as...

A geothermal power plant on the Raft river uses isobutane as the working fluid. The fluid enters the reversible adiabatic turbine at 320 F, 805 lbf / in. ^{2} and the condenser exit condition is saturated liquid at 91 F. Isobutane has the properties Tc = 734.65 R, Pc = 537 lbf / in. ^{2} , Cpo = 0.3974 Btu/lbm R and ratio of specific heats k = 1.094 with a molecular weight as 58.124. Find the specific turbine work and the specific pump work.

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R = 26.58 ft lbf/lbm R = 0.034 166 Btu/lbm R

Turbine inlet:      T _{ r1 }=779.7 / 734.7=1.061, \quad P _{ r1 }=805 / 537=1.499

Condenser exit:  T _{3}=91   F , x _{3}=0.0 ; \quad T _{ r 3}=550.7 / 734.7=0.75

From D.1 :      P _{ r 3}=0.165, Z _{3}=0.0275

P _{2}= P _{3}=0.165 \times 537=88.6   lbf / in .^{2}

From D.2 and D.3,

\begin{aligned}&\left( h _{1}^{*}- h _{1}\right)=0.034166 \times 734.7 \times 2.85=71.5   Btu / lbm \\&\left( s _{1}^{*}- s _{1}\right)=0.034166 \times 2.15=0.0735   Btu / lbm  R \\&\left( s _{2}^{*}- s _{1}^{*}\right)=0.3974 \ln \frac{550.7}{779.7}-0.034166 \ln \frac{88.6}{805}=-0.0628   Btu / lbm  R\end{aligned}

 

\begin{gathered}\left( s _{2}^{*}- s _{2}\right)=\left( s _{2}^{*}- s _{ F 2}\right)- x _{2} s _{ FG 2}=0.034166 \times 6.12- x _{2} \times 0.034166(6.12-0.29) \\=0.2090- x _{2} \times 0.1992\end{gathered}

 

\begin{aligned}&\left( s _{2}- s _{1}\right)=0=-0.2090+ x _{2} \times 0.1992-0.0628+0.0735 \Rightarrow x _{2}=0.9955 \\&\left( h _{2}^{*}- h _{1}^{*}\right)= C _{ P 0}\left( T _{2}- T _{1}\right)=0.3974(550.7-779.7)=-91.0   Btu / lbm\end{aligned}

 

From D.2,

\begin{gathered}\left( h _{2}^{*}- h _{2}\right)=\left( h _{2}^{*}- h _{ F 2}\right)- x _{2} h _{ FG 2}=0.034166 \times 734.7[4.69-0.9955(4.69-0.32)] \\=117.7-0.9955 \times 109.7=8.5   Btu / lbm\end{gathered}

Turbine:      w _{ T }=\left( h _{1}- h _{2}\right)=-71.5+91.0+8.5= 2 8 . 0   Btu / lbm

Pump          v _{ F 3}=\frac{ Z _{ F 3} RT _{3}}{ P _{3}}=\frac{0.0275 \times 26.58 \times 550.7}{88.6 \times 144}=0.03155   ft ^{3} / lbm

w _{ P }=-\int_{3}^{4} vdP \approx v _{ F 3}\left( P _{4}- P _{3}\right)=-0.03155(805-88.6) \times \frac{144}{778}=- 4 . 2   Btu / lbm

 

 

D.1
D.2
D.3

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