Question 16.CSGP.105: A coal gasifier produces a mixture of 1 CO and 2H2 that is t......

A coal gasifier produces a mixture of 1 CO and 2H_2 that is then fed to a catalytic converter to produce methane. A chemical-equilibrium gas mixture containing CH _4, CO , H _2 \text {, and } H _2 O exits the reactor at 600 K, 600 kPa. Determine the mole fraction of methane in the mixture.

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\begin{array}{lllcc}& CO & +3 H _2 & \leftrightarrow CH _4 & + H _2 O \\\text { Initial } & \quad 1 & 2 & 0 & 0 \\\text { Change } & \quad – x & -3 x & x & x \\\text { Equil. } & \quad 1- x & 2-3 x & x & x\end{array}

Total: n = (1 – x) + (2 – 3x) + x + x = 3 – 2x

K =\frac{ y _{ CH 4} y _{ H 2 O }}{ y _{ CO } y _{ H 2}^3}\left\lgroup \frac{ P }{ P _{ o }} \right\rgroup^{(1+1-1-3)=-2}=\frac{ x ^2}{(1- x )(2-3 x )^3}\left\lgroup \frac{ P }{ P _{ o }} \right\rgroup^{-2}

\begin{aligned}& \ln K =-\Delta G ^{ O } / \overline{ R } ; \quad \Delta G ^{ O }=\Delta H ^{ O }- T \Delta S ^{ O } \\& \begin{aligned}H _{ P } & = n _{ CH 4}\left[\overline{ h }_{ f }^{ o }+\overline{ C }_{ P }\left( T – T _{ o }\right)\right]+ n _{ H 2 O }\left(\overline{ h }_{ f }^{ o }+\Delta \overline{ h }\right) \\& =[-74873+2.254 \times 16.04(600-298.15)]+(-241826+10499)=-295290 \\H _{ R } & = n _{ CO }\left(\overline{ h }_{ f }^{ o }+\Delta \overline{ h }\right)+ n _{ H 2}\left(\overline{ h }_{ f }^{ o }+\Delta \overline{ h }\right)=1(-110527+8942)+3(0+8799) \\& =-75188 \,kJ\end{aligned}\end{aligned}

\begin{aligned}& \Delta H _{600}^{ o }= H _{ P }- H _{ R }=-295290-(-75188)=-220102 \,kJ \\& \left(\overline{ s }_{ T }^{ o }\right)_{ CH 4}=\overline{ s }_{ To }^{ o }+\overline{ C }_{ P } \ln \left( T / T _{ o }\right)=186.251+2.254 \times 16.04 \ln (600 / 298.2)=211.549 \\& \left(\overline{ s }_{ T }^{ o }\right)_{ H 2 O }=213.051 \,kJ / kmol – K ; \quad S _{ P }=424.6 \,kJ / K \\& \left(\overline{ s }_{ T }^{ o }\right)_{ CO }=218.321 \,kJ / kmol – K , \quad\left(\overline{ s }_{ T }^{ o }\right)_{ H 2}=151.078 \,kJ / kmol – K\end{aligned}

\begin{aligned}& \Delta S _{600}^{ o }= S _{ P }- S _{ R }=\left( n \overline{ s }_{ T }^{ o }\right)_{ CH 4}+\left( n \overline{ s }_{ T }^{ o }\right)_{ H 2 O }-\left( n \overline{ s }_{ T }^{ o }\right)_{ CO }-\left( n \overline{ s }_{ T }^{ o }\right)_{ H 2} \\& =(211.549+213.051)-(218.321+3 \times 151.078)=-246.955 \,kJ / K \\& \Delta G ^{ O }=\Delta H ^{ O }- T \Delta S ^{ O }=-220102-600(-246.955)=-71929 \,kJ \text {, } \\& \ln K =-(-71915) /(8.31451 \times 600)=14.418 \quad \Rightarrow K =1.827 \times 10^6 \\& \text { Solve for } x.  x =0.6667, n _{\text {tot }}=1.6667, \quad y _{ C H 4}= 0 . 4 \end{aligned}

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