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Page 1: 6.Multiple_reactions.ppt

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Page 2: 6.Multiple_reactions.ppt

Scope:

• Limited to Qualitative treatment

• Design aspects – not included

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Page 3: 6.Multiple_reactions.ppt

What is a multiple reaction ?

• Require rate w.r.t. more than one species

• Require more than one stoichiometric equation and equilibrium expression

Classification: • Series (consecutive) reactions

A R S• Parallel (competing) reactions

A R A S

• Series – Parallel reactions 3

Page 4: 6.Multiple_reactions.ppt

Criteria for selecting the reactor:• Good product distribution • Size of the reactor

Good product distribution could be the dominant criteria in many cases.

The above two criteria are contradictory to each other. Good design w.r.t one requirement may be poor w.r.t. the other.

An economic analysis will give the best compromise.

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Page 5: 6.Multiple_reactions.ppt

Selectivity: A R (desired reaction)A S (undesired reaction)

Selectivity = rdesired/rundesired

The selectivity should be maximum for the chosen reactor.

Yield = rdesired /-rA

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Page 6: 6.Multiple_reactions.ppt

Parallel reactions

Series reactions

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Page 7: 6.Multiple_reactions.ppt

Series-Parallel reactions

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Page 8: 6.Multiple_reactions.ppt

Parallel reactions

A R (desired reaction)A S (undesired reaction)

A

RR Ck

dt

dCr 1

AS

S Ckdt

dCr 2

k1, k2, , are all constant for a specific system at a given temperature.

How to maximize S ??

AS

R Ck

k

dC

dCS

2

1

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Page 9: 6.Multiple_reactions.ppt

AS

R Ck

k

dC

dCS

2

1

How to decide the concentration level??

Case – 1: > , ndesired > nundesired

High concentration is desirable as it maximizes the selectivity.

Case – 2: < , ndesired < nundesired

Low concentration is desirable as it maximizes the selectivity.

Case – 3: = , ndesired = nundesired

Concentration level does not affect the selectivity.

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Page 10: 6.Multiple_reactions.ppt

Concentration can be maintained low:• Using a CSTR• Designing for high conversions• Increasing inerts in the feed• Decreasing pressure in gas phase

reactions

Concentration can be maintained high:• Using a PFR• Designing for low conversions• Decreasing inerts in the feed• Increasing pressure in gas phase reactions

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Page 11: 6.Multiple_reactions.ppt

How to decide the temperature level??

Case – 1: ED > EU

High temperature is desirable as it maximizes the selectivity.

Case – 2: ED < EU

Low temperature is desirable as it maximizes the selectivity.

Case – 3: ED = EU

Temperature level does not affect the selectivity.

S is maximized at higher k1/k2

AS

R Ck

k

dC

dCS

2

1

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Page 12: 6.Multiple_reactions.ppt

Example: A + B R (desired reaction)A + B S (undesired reaction)

2211

2

1 BAS

R CCk

k

dC

dCS

Case – 1: 1 > 1 and 2 > 2 Maintain both CA and CB high.

Case – 2: 1 < 1 and 2 < 2 Maintain both CA and CB low.

Case – 3: 1 = 1 and 2 = 2 CA and CB levels will not affect S.

Temperature levels can be decided based on the activation energies 12

Page 13: 6.Multiple_reactions.ppt

Contacting patterns for batch operation:

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Page 14: 6.Multiple_reactions.ppt

Contacting patterns for continuous operation:

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Page 15: 6.Multiple_reactions.ppt

•For parallel reactions, the concentration level of the reactants is the key to control product distribution.

•High reactant concentration favors the higher order reaction

•Low reactant concentration favors the lower order reaction

•Similarly high temperature favors the reaction with high activation energy

•Low temperature favors the reaction with low activation energy

Conclusions:

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Page 16: 6.Multiple_reactions.ppt

Series reactions:A R S (I order at constant density)

meanopt kkk

kkt

log

12

12 /1)/ln( )(

2

1

0

max,12

2kk

k

A

R

k

k

C

C

Batch Reactor:

meanopt kkk

kk

log

12

12 /1)/ln(

)(

2

1

0

max,12

2kk

k

A

R

k

k

C

C

Plug Flow Reactor:

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Page 17: 6.Multiple_reactions.ppt

CSTR:

A

AA

A

AA

Ck

CC

r

CC

1

00

10

1 kC

C

A

A

Material balance for species R: vCR0 = vCR + (-rR)V

0 = vCR + (-k1CA+ k2CR)V 0 = CR + (-k1CA + k2CR) CR(1 + k2) = k1CA

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Page 18: 6.Multiple_reactions.ppt

)1)(1(1 21

01

2

1

kk

Ck

k

CkC AAR

For maximum concentration of R: dCR/d = 0

2120

max,

1/

1

kkC

C

A

R

21

1

kkopt

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Page 19: 6.Multiple_reactions.ppt

Consecutive I-order reactionsCB exhibits a maximum at opt

PFR

CSTR

CB,max (PFR) > CB,max (CSTR)19

Page 20: 6.Multiple_reactions.ppt

•For series reactions, the time of reaction / space time is the key for obtaining the maximum concentration of the desired product.

•For higher order reactions and series-parallel reactions, such analytical derivations for optimum space time would be tedious.

•In such cases, optimization methods can be used to find the optimum space time and the corresponding maximum concentration of the desired product.

Conclusions:

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Page 21: 6.Multiple_reactions.ppt

Assignment:1. Find expressions for optimum space time

and maximum concentration of R for the following series reaction, if k1 = k2 in both CSTR and PFRA R S (I order at constant density)

2. Find expressions for optimum space time and maximum concentration of R for the following series reaction, if k1 = 2k2 in both CSTR and PFRA R S (I order at constant density)

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Page 22: 6.Multiple_reactions.ppt

ANY CLARIFICATIONS ?

Berrill, N.J.A great teacher is not simply one who imparts knowledge to his

students but is one who awakens their interest in the subject and makes them eager to pursue it for themselves. An outstanding

teacher is a spark plug, not a fuel line.

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