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Fugacity: It is derived from Latin, expressed as fleetness or escaping ...

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The standard free energy change f<strong>or</strong> the reaction C4H8 (g) C4H6 (g) + H2 (g)<br />

<strong>is</strong> given by ΔGT 0 =1.03665 X 10 5 – 20.9759T ln T 12.9372 T, where range of ΔGT 0 in J<br />

/ mol and T in K<br />

a) Over what range of T, <strong>is</strong> the reaction prom<strong>is</strong>ing <strong>from</strong> thermodynamic view<br />

point?<br />

b) F<strong>or</strong> a reaction of pure butene at 800K, calculate equilibrium conversion at 1.0<br />

bar & 5.0 bar<br />

c) Repeat part (b) f<strong>or</strong> the feed with the 50 mol% butene and the rest inerts<br />

a. F<strong>or</strong> the reaction at ΔG = 0, T ≈ 812.4 K, above th<strong>is</strong> temperature ΔG <<br />

0, reaction <strong>is</strong> prom<strong>is</strong>ing below 550 K, ΔG > 0, reaction <strong>is</strong> unfav<strong>or</strong>able,<br />

b. At 800K, ΔG 0 = 1842.16 J / mol<br />

ΔG 0 = - RT ln K, <strong>or</strong> 1842.16 = - 8.314 ( 800 ) ln K <strong>or</strong><br />

K = 1.3191<br />

K = ky P Δn = ky P ( 2- 1 ) = ky P<br />

Theref<strong>or</strong>e at 1.0 bar K = kyP 1.3191 = ky ( 1 )<br />

ky = 1.31910At 5 bar, 1.3191 = ky ( 5 )<br />

ky = 0.26382<br />

Moles in<br />

feed<br />

C4H8 1 1 - X<br />

Moles in product stream yi<br />

(1 – X ) / (1 +<br />

C4H6 X X / (1 + X)<br />

H2 X X / (1 + X)<br />

1 + X<br />

X)

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