True or false: The goal of fitting kinetic Reactive...

30
L6 L6 - - 1 1 ChE 400 - Reactive Process Engineering ChE ChE 400 400 - - Reactive Process Engineering Reactive Process Engineering Review of Fitting Kinetic Data True or false: The goal of fitting kinetic data is to find the true rate expression. What are the two general methods used to fit kinetic data?

Transcript of True or false: The goal of fitting kinetic Reactive...

Page 1: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--11

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Review of Fitting Kinetic Data

• True or false: The goal of fitting kinetic data is to find the true rate expression.

• What are the two general methods used to fit kinetic data?–

Page 2: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--22

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Advantages and Drawbacks

Page 3: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--33

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

CST Data as Obtained

0.0

5.0

10.0

15.0

20.0

25.0

30.0

0 50 100 150 200Time, min

Con

cent

ratio

n, m

g/L

Cin = 15 mg/LCin = 20 mg/LCin = 25 mg/L

Review of Fitting Kinetic Data

Page 4: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--44

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Transformed CST Data

-5.0

-4.0

-3.0

-2.0

-1.0

0.00 20 40 60 80 100 120 140 160 180 200

time, min

ln{(

Cin

-C)/(

Cin

-C0)

}

Cin = 15 mg/LCin = 20 mg/LCin = 25 mg/L

Transformed CST Data with Trendline (all data)

ln{(Cin-C)/(Cin-C0)} = -0.025 tR2 = 0.999

-5.0

-4.0

-3.0

-2.0

-1.0

0.00 20 40 60 80 100 120 140 160 180 200

time, min

ln{(

Cin

-C)/(

Cin

-C0)

}

Cin = 15 mg/LCin = 20 mg/LCin = 25 mg/L

Review of Fitting Kinetic Data

What is the order of the reaction?

Page 5: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--55

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Determining k0, EASo, now that we know k, how can we obtain k0 and EA??

Remember k?

ln k

1/T

ln k0

-E/R

Plotting ln k

What’s the slope?What’s the slope?What’s the slope?

What’s the intercept?What’s the intercept?What’s the intercept?

Page 6: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--66

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Kinetics of Many Processes in Nature Kinetics of Many Processes in Nature

follow Arrhenius Relationshipfollow Arrhenius RelationshipSome Examples• Cricket chirping• Ant walking• Tumor growth• Diffusion in solids [D = Do exp (-ED/RT)]

Page 7: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--77

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Ant walking: Does it follow Arrhenius’ Law?Ant walking: Does it follow Arrhenius’ Law?

M. I. M. I. MaselMasel, Chemical Kinetics and Catalysis, Chemical Kinetics and Catalysis

Page 8: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--88

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

The Ants are walking one by one…The Ants are walking one by one…

0

1

2

3

4

5

6

7

8

0 5 10 15 20 25 30 35 40 45

Temperature (C)

Run

ning

Spe

ed (c

m/s

)

Raw data Raw data (speed (speed vsvs temperature)temperature)

-1.0

-0.5

0.0

0.5

1.0

1.5

2.0

2.5

3.15 3.20 3.25 3.30 3.35 3.40 3.45 3.50 3.55 3.60

1000/T (K-1)

ln (w

laki

ng s

peed

)

LinearizedLinearized datadata((lnln u u vsvs 1/T)1/T)

Page 9: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--99

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Summary: Determining Rate Coefficients

1.1. set upset up

2.2. measuremeasure

3.3. setset--up up

4.4. linearizelinearize

5.5. use use

6.6. do this do this

7.7. linearizelinearize, ,

8.8. use linear use linear -- slopeslope-- interceptintercept

Page 10: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1010

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Example: determining k

t (s) [NO2] (mol/l)

0 0.01

50 0.00787

100 0.00649

200 0.00481

300 0.0038

Nitrogen dioxide is introduced into an isothermal batch reactor at a temperature of 300°C. Its decomposition to nitrogen oxide and oxygen is followed over time and the data below is obtained. Is the reaction first order or second order? Determine the reaction rate coefficient.

2 NO2 <=> 2 NO + O2

order integrated rate law linear plot for

1

2

…so, let’s do it!……so, let’s do it!so, let’s do it!

Page 11: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1111

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Example: 1st order kinetics

1st order fit

y = -0.0032x - 4.6679R2 = 0.9824

-6

-5.8

-5.6

-5.4

-5.2

-5

-4.8

-4.6

-4.4

-4.2

-4

0 50 100 150 200 250 300 350

t [s]

ln {[

NO

2 / (

mol

/l)}

Page 12: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1212

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Example: 2nd order kinetics

2nd order fit

y = 0.5431x + 99.833R2 = 1

100

120

140

160

180

200

220

240

260

0 50 100 150 200 250 300 350

t [s]

1/[N

O2]

/ (m

ol/l)

perfect fit indicates

Page 13: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1313

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Determining Reaction OrderGreat, so if I know the reaction order n, I can determine k. What if I do not know n?

1. “Try” different reaction orders (i.e. search for the best fit of the data to the integrated rate laws)Works only for reasonably simple reaction orders (n = -1, 0, 1, 2)

t (min) CA (mol/L)0 2.005 1.609 1.3515 1.1022 0.8730 0.7040 0.5360 0.35

0.0

0.5

1.0

1.5

2.0

0 10 20 30 40 50 60

time (min)

CA

(mol

/L)

Example: The following is measured data from some reaction A -> P

Page 14: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1414

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Reaction Order: Example cont’d

0.0

0.2

0.4

0.6

0.8

1.0

0 10 20 30 40 50 60

time (min)

ln(C

A/C

A,0) (

dim

ensi

onle

ss)

(1) Assume 1st order, linearize, and replot

Page 15: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1515

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Reaction Order: Example cont’d(1) Assume 2nd order, linearize, and replot

0.0

0.5

1.0

1.5

2.0

2.5

0 10 20 30 40 50 60

time (min)

[1/C

A - 1

/CA

,0] (

L/m

ol)

ktCC AA

=−0,

11

Page 16: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1616

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

1/CA0.5 - 1/CA,0

0.5 = 0.0165tR2 = 0.9998

0.0

0.2

0.4

0.6

0.8

1.0

1.2

0 10 20 30 40 50 60

time (min)

1/C

A0.5 -

1/C

A,0

0.5

Reaction Order: Example cont’d(1) Assume order 1.5, linearize, and replot

r = k CA1.5 into BR design equation:

with constant volume assumption:

…and integration yields:

What is k??

Page 17: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1717

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Determining Reaction OrderObviously, trial-and-error fits will not help us except for very simple cases. Hence we need a generally applicable way…

2. Initial Rates (differential) Method:Measure reaction rate at several different initial concentrations.

From r = k [A]n => ln r = n ln[A] + ln kHence, the logarithmic plot of initial reaction rate r0 vs [A]0 yields the reaction order n as the slope.

•••

ln [A]0

ln r0

Page 18: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1818

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Reaction Order, cont’dIn practice, one rarely deals with simple reactions with only one reactantA -> products. Therefore, the reaction order needs to be determined foreach reactant separately. This is done by the…

Isolation Method:Isolation Method:The concentrations of all but one reactant are kept constant during an experiment, thus isolating the effect of this reactant on the reaction rate.

Page 19: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--1919

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Summary: Determining Reaction Orders

•• Integral + Trial and ErrorIntegral + Trial and Error:

•• Differential MethodDifferential Method

•• Isolation MethodIsolation Method

Page 20: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2020

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Designing a Kinetic Experiment

1. Select

2. set up

3. measure

4. determine

5. measure

6. determine

That’s it! You now know how to design That’s it! You now know how to design an experiment to determine all relevant an experiment to determine all relevant kinetic data for any reaction system:kinetic data for any reaction system:

Page 21: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2121

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

A Glimpse of Theory…

As we saw above, kinetic experiments are difficult and lengthy

procedures (and hence also expensive…), so one would really LOVE

to replace experiments by theoretical calculationsreplace experiments by theoretical calculations.

While we are still far away from being able to do this reliably,

theoretical chemistry has made great progress in past decades

and is becoming an increasingly important tool in chemical kinetics

(even in industrial application!).

The following will give just a very brief glimpse of some of the

very basics of those calculations.

Page 22: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2222

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

A (very brief) Theory of Reaction Rates

All chemical reactions occur by collisions between moleculescollisions between molecules (or by collision of molecules with surfaces – that’s catalysis, and we’ll talk about that a bit later…).One very simple theory of reactions builds on this observation, and is hence called

‘collision theory’‘collision theory’.

Consider the simple bimolecular reaction:

In the framework of the collision theory, the rate of this reaction is described by:r = r =

You can’t react if you don’t collide!You can’t react if you don’t collide!

Page 23: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2323

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Probability of Successful Collision

Boltzmann-Distributionp(E) = exp{-E/RT}p(Ep(E) = exp{) = exp{--E/RT}E/RT}

fraction of successful collisions(= probability distribution)

The probability of a ‘successful’ collisionprobability of a ‘successful’ collision can be estimated based on the fact that a bond needs to be broken during a reactive event. This requires a certain amount of energy, E. Since the energy distribution (for thermal energy) is governed by a BoltzmannBoltzmanndistributiondistribution, the probability that a molecule at temperature T has acquired the

necessary energy is p(Ep(E) = exp{) = exp{--E/RT}E/RT}.

Page 24: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2424

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

(Simple) Collision Theory

The collision cross section (assuming hard spheres) is

The collision rate can be calculated from the The collision rate can be calculated from the kinetic theory of gaseskinetic theory of gases::

The frequency of collisions of a molecule of A with B is given by:

ZZABAB ==

Therein, the average thermal velocity u is given by <u> =

The ‘reduced molecular mass’ is given by: μ =

The The collision cross sectioncollision cross section for two for two molecules can be regarded asmolecules can be regarded as

σAB =

Page 25: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2525

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

ZAB =

(Simple) Collision Theory

Or, with concentrations:

We can hence write for the reaction rate:

k0 = kk00 = =

Compare this to the usual rate law for bimolecular (elementary) reactions:r = k0 exp{-EA/RT} CA CB

We can therefore calculate the pre-exponential factor for a 2nd order reaction from:

ZAB =

Putting this all together, we obtain for the collision ratecollision rate:

r =

ZAB =

Page 26: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2626

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

kk00 = {8 RT/(= {8 RT/(π μπ μ)})}1/2 1/2 ππ ddABAB22

(Simple) Collision Theory, cont’d

This value gives in effect the maximal possible rate coefficientmaximal possible rate coefficient for bimolecular reactions. In reality, the rate coefficients are typically significantly lower than this, due to steric as well as energetic considerations.

ExampleExample: .OH + H. -> .O. + H2

Page 27: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2727

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Example 2:

This value gives in effect the maximal possible rate coefficientmaximal possible rate coefficient

kk00 = {8 RT/(= {8 RT/(π μπ μ)})}1/2 1/2 ππ ddABAB22

(Simple) Collision Theory, cont’d

for bimolecular reactions. In reality, the rate coefficients are typically significantly lower than this, due to steric as well as energetic considerations.

Steric and energetic factors can reduce the rate coefficient by many orders of magnitude. Collision theory can hence only give an upper limit to k!(Comparison with “similar” reactions with known steric factors occasionally allows us to estimate the steric factor and hence to calculate k0 from collision theory.

=> rcorrected = P Z exp{-E/RT} )

Page 28: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2828

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

ExampleEstimate the rate coefficient for bimolecular gas phase reactions. Assume room temperature.

k0 = {8 RT/(π μ)}1/2 π dAB2kk00 = {8 RT/= {8 RT/(π μ(π μ)})}1/2 1/2 ππ ddABAB22

μ =dAB ≈

kk00 ==

Dimensions:

[k0] =

-> to obtain the usual dimensions for a 2nd order rate constant, we need to multiplywith Avogadro’s number NA= 6.02 * 1023 (atoms)/mol

R = 8.3 J/mol K, T = 300 KValues:

Let’s assume simple molecules: NLet’s assume simple molecules: N2 2 and Oand O22

Compare with experimental valuesCompare with experimental values::K + BrK + Br2 2 --> > KBrKBr + Br+ Br kk0,exp0,exp≈≈CHCH33 + CH+ CH3 3 --> C> C22HH66 kk0,exp0,exp≈≈HH22 + C+ C22HH4 4 --> C> C22HH66 kk0,exp0,exp≈≈ kk00 = k= k0,theo 0,theo × P ; × P ; P ≈P ≈

Page 29: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--2929

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Collision Theory: “Summary”

frequencyof

collision

frequencyof

collision

fraction ofmolecules

facing each other correctly

fraction ofmolecules

facing each other correctly

fraction ofmolecules

with sufficientkinetic energyto break bonds

fraction ofmolecules

with sufficientkinetic energyto break bonds

k = x x

Which of these terms does Collision Theory capture (more or less)correctly, and which does it not?

Page 30: True or false: The goal of fitting kinetic Reactive ...puccini.che.pitt.edu/~karlj/Classes/CHE400/lecture06-web.pdf · - Reactive Process Engineering ChE 400-Reactive Process Engineering

L6L6--3030

ChE

400

-Re

activ

e Pr

oces

s En

gine

erin

gCh

ECh

E40

040

0--

Reac

tive

Proc

ess

Engi

neer

ing

Reac

tive

Proc

ess

Engi

neer

ing

Collision Theory: Unimolecular RctnsCollision theory does offer interesting insights into unimolecular reactions: It is experimentally observed that unimolecular reactions show a surprising decrease in the measured reaction coefficient towards very low pressures (so-called “fall-off” regime). How can that be explained?

In reality, unimolecular reactions require intermolecular collisions!

A -> B , r = k CA

is in reality the sum reaction for a reaction sequence!A + A <=> A* + A , r1 =

A* -> B , r2=

Since A* is a highly reactive intermediate, let’s assume it’s concentration is essentially constant:

dCA*/dt =

CA* =

Hence: rB = r2 =

High pressure limit:High pressure limit:

Low pressure limit:Low pressure limit: