The rate of the heterogenous catalytic reaction A(g) + B(g) ? C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction isA. absorption of A.

Chemical Reaction Engineering
The rate of the heterogenous catalytic reaction A(g) + B(g) ? C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction isA. absorption of A.

Surface reaction between absorbed A and absorbed B

Surface reaction between absorbed A and B in the gas phase

Surface reaction between A in the gas phase and absorbed B

Absorption of A

Surface reaction between absorbed A and absorbed B

Surface reaction between absorbed A and B in the gas phase

Surface reaction between A in the gas phase and absorbed B

Absorption of A

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Chemical Reaction Engineering
A space velocity of 5 hr⁻¹ means that

After every 5 hours, reactor is being filled with the feed

Cent per cent conversion can be achieved in at least 5 hours

Five reactor volumes of feed (at specified conditions) are being fed into the reactor per hour

A fixed conversion of a given batch of feed takes 5 hours

After every 5 hours, reactor is being filled with the feed

Cent per cent conversion can be achieved in at least 5 hours

Five reactor volumes of feed (at specified conditions) are being fed into the reactor per hour

A fixed conversion of a given batch of feed takes 5 hours

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Chemical Reaction Engineering
The eddy diffusivity for a liquid in plug flow must be

1

0

Between 0 and 1

∞

1

0

Between 0 and 1

∞

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Chemical Reaction Engineering
Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is

43833

43835

43834

43832

43833

43835

43834

43832

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Chemical Reaction Engineering
The temperature dependence of reaction rate constant (K) by Arhenius law is given by

K α √T . e-E/RT

K α e-E/RT

K α eE/RT

K α T . e-E/RT

K α √T . e-E/RT

K α e-E/RT

K α eE/RT

K α T . e-E/RT

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Chemical Reaction Engineering
For the reaction, A + B → 2B + C,

rA = rB

rA = -rB

rA = 2rB

rA = rB/2

rA = rB

rA = -rB

rA = 2rB

rA = rB/2

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Chemical Reaction Engineering

Chemical Reaction Engineering The rate of the heterogenous catalytic reaction A(g) + B(g) ? C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction isA. absorption of A.

Chemical Reaction Engineering A space velocity of 5 hr⁻¹ means that

Chemical Reaction Engineering The eddy diffusivity for a liquid in plug flow must be

Chemical Reaction Engineering Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is

Chemical Reaction Engineering The temperature dependence of reaction rate constant (K) by Arhenius law is given by

Chemical Reaction Engineering For the reaction, A + B → 2B + C,

Chemical Reaction Engineering
The rate of the heterogenous catalytic reaction A(g) + B(g) ? C(g) is given by -rA = k.KA.pA.PB/(1 + KA.PA + Kc.pc), where KA and Kc are the adsorption equilibrium constants. The rate controlling step for this reaction isA. absorption of A.

Chemical Reaction Engineering
A space velocity of 5 hr⁻¹ means that

Chemical Reaction Engineering
The eddy diffusivity for a liquid in plug flow must be

Chemical Reaction Engineering
Pure A in gas phase enters a reactor 50% of this A is converted to B through the reaction, A 3B. Mole fraction of A in the exit stream is

Chemical Reaction Engineering
The temperature dependence of reaction rate constant (K) by Arhenius law is given by

Chemical Reaction Engineering
For the reaction, A + B → 2B + C,