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ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

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ChE 553 Lecture 15 Catalytic Kinetics Continued 1
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Page 1: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

ChE 553 Lecture 15 Catalytic Kinetics Continued

1

Page 2: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Object

• Examine the effects of pairwise interactions on rates of surface reactions– Interactions change apparent order– Can fit to Langmuir, but with the wrong

mechanism

2

Page 3: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Started Catalytic Kinetics Last Time

• Catalytic reactions follow a catalytic cycle

reactants + S adsorbed reactants

Adsorbed reactants products + S• Different types of reactions

Langmuir Hinshelwood

Rideal-Eley

3

Page 4: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Key Predictions

Unimolecular reactions• Rate increases with pressure, levels off• Rate always increases with temperature• Very sensitive to poisons

Bimolecular reactions• Rate rises reaches a maximum at finite temp

and pressure, then drops• Sensitive to poisons

4

Page 5: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Qualitative Behavior For Unimolecular Reactions (AC)

P =25B

PA

0 10 20 30 40 500.0E+0

5.0E-9

1.0E-8

1.5E-8

2.0E-8

Rat

e, M

oles

/cm

/se

c 2

P =0B

5

0.01 0.1 1 10 1001E+16

1E+17

1E+18

1E+19

1E+20

770 K

1070 K

870 K

1270 K1670 K

Ammonia pressure, torr

Rat

e, M

olec

ules

/cm

-se

c2

rk3KA PAS0 k4KCPCS0

1 KA PA KBPB KCPC

Page 6: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Qualitative Behavior For Bimolecular Reactions (A+Bproducts)

PA

0 10 20 30 40 500.0E+0

5.0E+13

1.0E+14

1.5E+14

2.0E+14

2.5E+14

Rat

e, M

olec

ules

/cm

/se

c 2

6

Figure 12.32 A plot of the rate calculated from equation (12.161) with KBPB=10.

1012

1013

Rat

e, M

olec

ules

/cm

-se

c2

1011

10-6

CO pressure, torr10

-710

-8

390 K

410 K

450 K

440 K

Page 7: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Physical Interpretation Of Maximum Rate For A+BAB

• Catalysts have finite number of sites.

• Initially rates increase because surface concentration increases.

• Eventually A takes up so many sites that no B can adsorb.

• Further increases in A decrease rate.

7

Page 8: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Methods Do Not Always Work In Detail

• Pairwise interactions between adsorbed species– Leads to ordering, coverage dependent

kinetics– Can produce oscillations, steady states

that depend on how steady state is reached

8

Page 9: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Key Qualitative Effects

• Ordered Overlayers

• Island formation

• Fluctuations

9

Page 10: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

The Effect Of An Ordered C(2x2) Overlayer

• Notice that the environment of B is independent of the coverage of A provided θA > 0.5

• The rate is almost independent of the A concentration– Not exactly independent

because repulsions speed rate

10

Page 11: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Monte Carlo Calculation To Estimate Rate

Montecarlo to estimate coverage:• Randomly choose one of three steps

– Adsorption/desorption step– Reaction– Diffusion

• Use Metropolis algorithm to see whether step should be choosen

• Calculate rate via an ensemble average

11

Page 12: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Adsorption/desorption Similar To Previous Work

• Pick a random site• If empty adsorb A or B• If filled desorb molecule• If energy goes down

accept the step• If energy goes up accept

the step with probability exp(-βΔE)

• Repeat12

Page 13: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Diffusion Changes Algorithm Slightly

• Pick a random site• Pick an adjacent site • If adjacent site empty move

molecule• If adjacent site filled do nothing• If energy goes down accept the

step• If energy goes up accept the

step with probability exp(-βΔE)• Repeat

13

Page 14: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Reaction Requires Additional Changes

• Pick a random site• Pick an adjacent site • If A adsorbed on one of

the sites and B adsorbed on a different site Assume A and B react with a probability of p= koexp(-EA/kT)

• RepeatNote only 1 in 108 attempts

leads to reaction14

Page 15: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Next: Estimate The Rate

Rate = koexp(-EA/kT) * (number of adjacent pairs of molecules)

15

Page 16: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8

Rat

e

A

h = -0.5AB

h = +0.5AB

Result Of Simulation Using Montecarlo

16

βhAA = -3

Fit

Langmuir

Page 17: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Implications

• Can fit rate data to Langmuir kinetics even where coverage does not follow Langmuir isotherm– Langmuir kinetics calculated for the wrong

mechanism (aqua line) fit the data– However, Langmuir kinetics calculated for the

correct mechanism (orange line) do not fit the data

• Cannot use kinetics to infer mechanism

17

Page 18: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Dynamic Islanding

If diffusion is slow see dynamic islanding

• A molecules next to B molecules react

• A molecules next to A unreactive

• B molecules next to B unreactive

Leads to islands of A and B

18

Page 19: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Rate Oscillations Observed Experimentally Under Such Conditions

19

Page 20: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Interactions Between Molecules Seen In Transient Measurements

Temperature programmed desorption (TPD)

• Adsorb gas on cold surface

• Heat at a constant 1-100K/sec

• Measure gas evolution as a function of time

20

Pumps

Heat

Temperature

Rat

e

Page 21: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Typical TPD Spectrum

21

100 200 300 400 500 600 700 800 900 1000

Temperature (K)

Des

orpt

ion

Rat

e5

4

3

2

1

0

2 AMU (Hydrogen)

30 AMU (Ethane)

27 AMU (Ethylene)

x10 16 AMU (Methane)

TPD of ethylene

Page 22: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Why Peaks In TPD?

22

340 360 380 400 420 4400

0.2

0.4

0.6

0.8

1

CoverageRate

Constant

(TPD Spectrum)

Temperature, K

1/sec

Fractional

Rate

Page 23: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Qualitative Effects In TPD

23

350 400 450 500

Des

orpt

ion

Rat

e

Temperature, K350 400 450 500

n =1 n =2

Temperature, K

Page 24: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Qualitative Effects On TPD

24

0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1

(Thousands)

6

5

4

3

2

1

0

Ea =10 kcal/mole

20

3040

50

Page 25: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Qualitative Effects On TPD

25

300 350 400 450 500 550250 300 350 400 450 500

Temperature Temperature

Des

orpt

ion

Rat

e

First Order Second Order

1011

1015

1011

1015

Page 26: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

TPD To Estimate Ea

26

0 10 20 30 40 50

800

700

600

500

400

300

200

100

TPD

Pea

k T

empe

ratu

re, K

E A ,Kcal/mole

k 0

= 10

14/K

k 0

= 10

10/K

H

H

Ea = (0.06 kcal/mole-K) Tp

Page 27: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Can Use Methods To Get Approximate Activation Energies

27

100 200 300 400 500 600 700 800 900 1000

Temperature (K)

Des

orpt

ion

Rat

e5

4

3

2

1

0

2 AMU (Hydrogen)

30 AMU (Ethane)

27 AMU (Ethylene)

x10 16 AMU (Methane)

TPD of ethylene

Page 28: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Method Assumes No Interactions Between Molecules

28

200 220 240 260 280 300 320 340 360 380 400 420 440 460

Temperature, K

Mas

s Sp

ec S

igna

l

300 320 340 360 380 400 420 440 460 480 500

Temperature, KD

esor

ptio

n R

ate

k dConstant

k dVaries WithNumber OfNeighbors

x3

x3

x3

x3

x3

Attractive InteractionsRepulsive Interactions

Page 29: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Repulsive Interactions

29

= 0.44 = 0.73Adsorption Site Adsorbed Molecule

200 220 240 260 280 300 320 340 360 380 400 420 440 460

Temperature, K

Mas

s S

pec

Sig

nal

Page 30: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Attractive Interactions

30

300 320 340 360 380 400 420 440 460 480 500

Temperature, KD

esor

ptio

n R

ate

k dConstant

k dVaries WithNumber OfNeighbors

x3

x3

x3

x3

x3

Page 31: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Ea Varies Non-linearly With Coverage

31

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1

32

30

28

26

24

22

20

18

16

EaP

, Kca

l/M

ole

d

h = -2 kcal/mole

h = 2 kcal/mole

h = 0

Page 32: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Summary

• Pairwise interactions change kinetics in unexpected ways– Data fits Langmuir-Hinshellwood rate

expression – but for the wrong mechanism

– Ea varies non-linearly with coverage even though interactions linear with number of nearest neighbors

– Multiple peaks in TPD

32

Page 33: ChE 553 Lecture 15 Catalytic Kinetics Continued 1.

Key Implication

• Extreme care needed in using kinetics to infer mechanisms etc– Can easily get the wrong mechanisms with

the wrong analysis to fit data.

33


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