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

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y <br />

<br />

K K K K P <br />

<br />

c c<br />

y <br />

n<br />

C C<br />

0<br />

= (1)<br />

<br />

203 where a,b, and c are stoichiometric co efficients<br />

a b a b<br />

A <br />

B yA<br />

y <br />

B<br />

0.54 X<br />

<br />

(1.1)(0928) 1-X 1-X <br />

<br />

2<br />

<br />

2<br />

<br />

<br />

2 2<br />

-3<br />

and K <strong>is</strong> known already = 1.8029x10 = .(1)<br />

solving<br />

X = 0.0382<br />

then equilibrium Composion of C H <strong>is</strong> ( Max reversible reaction)<br />

2 2<br />

2 2<br />

moles C2H2reacted 0.0382<br />

= x 100 = 3.82%<br />

moles of C H in feed 1<br />

Calculate the K at 673K & 1.0 bar f<strong>or</strong> N2 (g) + 3 H2 (g) 2NH3 (g).<br />

Assume heat of reaction remains constant. Take standard heat of f<strong>or</strong>mation and<br />

standard free energy of f<strong>or</strong>mation of NH3 at 298 K to be - 46110 J / mol and – 16450 J<br />

/ mol respectively.<br />

G 2( 16450) 32900 J <br />

0<br />

298<br />

0<br />

298<br />

<br />

2 (-46110) = -92 220 J<br />

0<br />

G298 RT<br />

ln K298<br />

H <br />

G RT<br />

ln K<br />

0<br />

298 1<br />

- 32900 = - 8.314 (298) ln K<br />

K 564861.1<br />

0<br />

K2 H<br />

1 1 <br />

we have ln <br />

K1<br />

R T2 T1<br />

<br />

K2 92220 1 1 <br />

ln <br />

584861.1 8.314<br />

<br />

673 298<br />

<br />

<br />

K 5.75 10<br />

2<br />

4<br />

X <br />

Acetic acid <strong>is</strong> esterified in the liquid ph<strong>as</strong>e with ethanol at 373 K and 1.0 bar acc<strong>or</strong>ding<br />

to<br />

CH3COOH (L) + C2H5OH (L) CH3COOC2H5(L) + H2O (L)<br />

The feed cons<strong>is</strong>ts of 1.0 mol each of acetic acid & ethanol, estimate the mole fraction of<br />

ethyl acetate in the reacting mixture at equilibrium. The standard heat of f<strong>or</strong>mation<br />

and standard free energy of f<strong>or</strong>mation at 298 K are given below.<br />

Assume that the heat of reaction <strong>is</strong> independent of T and liquid mixture behaves <strong>as</strong><br />

ideal solution.<br />

1<br />

1

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