The gas phase reaction, 2A B C, is carried out in a PFR. The feed is equal molar in A and B and the entering temperature is 650K and the entering pressure is 21 atm. If the exit conversion is X, then the exit concentration of B (in mol/dm3 ) is:
Initial Pressure P0 = 21 atm
Initial temperature T0 = 650K
Initial concentration of A CA0 = P/RT
CA0 = 21 atm/(0.0821 L-atm/mol-K x 650 K)
CA0 = 0.39 mol/L = 0.4 mol/L
Feed is equimolar
CB0 = 0.4 mol/L
We can write the equation
A + 0.5 B = 0.5 C
Exit concentration CB = [CB0 - (b/a) CA0*X]/[1+AX]
A = (0.4 - 0.8)/0.4 = - 1
CB = [0.4 - 0.5*0.4*X] / [1 - X]
CB = 0.4 (1 - 0.5X)/(1-X)
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