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Consider the gas phase reversible reaction 2A ↔ B that occurs at atmospheric pressure. a) If...

Consider the gas phase reversible reaction 2A ↔ B that occurs at atmospheric pressure.

a) If the equilibrium constant Ka = 0.1, what are the equilibrium mole fractions of A and B?

b) Assuming the reaction is elementary, write the rate law using kA and k-A as the forward and reverse rate constants, respectively. What is the equilibrium constant Kc in terms of kA and k-A? Assuming an ideal gas system, write an expression for Ka in terms of kA and k-A. If the temperature is 25oC, what is the value of KC?

c) Assuming the reaction is elementary, and that the forward reaction rate constant kA is 2.4 L/(mol·min), determine the time for the reaction to reach 80% of equilibrium in a constant volume batch reactor. Use the value for KC you obtained in part d to solve the problem.

Solutions

Expert Solution

Solution:

(a) equalibrium constant Ka = aB / aA2 Where aB and aA are activity of B and A, respectively.

aB = For ideal gas and pressure = 1 atm = mole fraction * Partial pressure/ total pressure = mole fraction

0.1 = aB / aA2

if mole fraction of XA = x so XB = 1-x

For atmospheric pressure P=1;

So equation becomes: 1-x = 0.1 x2

0.1 x2+x-1 = 0

Solving above quardratic equation will give:

Mole fraction of A = 0.92

Mole fraction of B = 1-0.92 = 0.08

(b) Rate of forward reaction (rforw ) = KA [A]2

Rate of backward reaction (rback ) = KA-A[B]

At equalibrium:

Rate of forward = Rate of backward

KA [A]2 = KA-A[B]

equalibrium constant (Kc) = KA/KA-A = [B]/[A]2

thermodynamic equalibrium (Ka) = aB / aA2 = (PB/PB0)/(PA / PA0)2 =KA/KA-A

We know that: P = CRT; standard state pressure = PA0 = PB0 = 1 atm

So, (PB/PB0)/(PA / PA0)2 = [B]RT/[A]2(RT)2 = ([B]/[A]2 ) RT-1

So Ka = ((Kc) or KA/KA-A)RT-1

Kc = Ka (RT) = 0.1* 0.082 * 298 = 2.4436

Kc = 2.4436

(C) Given:

KA = 2.4 L/mol.min

Kc = 2.4436 (calculated in above part)

Conversion (x) = 0.8

Constant volume batch reactor:

Kc = KA / KA-A

So KA-A = KA/Kc = 0.982

CB0 = 0 and let CA0 = P/RT = 1/(0.082*298) = 0.041 mol/l

                2A <-> B

initial             0.041    0

After t time 0.041-x      x/2

t = 0.388 min. or 23.28 sec


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