Lecture 11

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Lecture 11. Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Today’s lecture. Determining the Rate Law from Experimental Data Integral Method Differential (Graphical) Method - PowerPoint PPT Presentation

Transcript of Lecture 11

Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of

chemical reactions and the design of the reactors in which they take place.

Lecture 11

Today’s lectureDetermining the Rate Law from

Experimental DataIntegral MethodDifferential (Graphical) MethodNonlinear Least Regression

Multiple ReactionsThe Four TypesWhat’s New to Our AlgorithmReactions in Series

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Integral MethodConsider the following reaction that occurs in a constant volume Batch Reactor: (We will withdraw samples and record the concentration of A as a function of time.)A Products

dNAdt

rAVMole Balance:

rA kCARate Law:

V V0Stochiometry:

dCAdt

kCACombine:

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Finally we should also use the formula to plot reaction rate data in terms of conversion vs. time for 0, 1st and 2nd order reactions.

Derivation Equations used to Plot 0, 1st and 2nd order reactions.These types of plots are usually used to determine the values k for runs at various temperatures and then used to determine the activation energy.Zero order First Order Second

Order

dCAdt

rA k

at t 0, CA CA 0

CA CA 0 kt

dCAdt

rA kCA

at t 0, CA CA 0

lnCA 0

CA

kt

dCAdt

rA kCA2

at t 0, CA CA 0

1CA

1CA 0

kt4

Guess and check for α = 0, 1, 2 and check against experimental plot

ktCC

ktCCktCr

AAA

AAA

0

00

11 ln

2 1 0

t

CA

t

ln(CA0/CA)

t

1/CA

Finding the Rate law (Integral Method)

Differential Method

AA Clnkln

dtdCln

AA kC

dtdCTaking the natural log of

dCAdt

vs CAThe reaction order can be found from a ln-ln plot of:

dtdCA

ACAPC

P

A

dtdC

Slope = α

ln

ln

Ap

p

A

C

dtdC

k

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Methods for finding the slope of log-log and semi-log graph papers may be found at

http://www.physics.uoguelph.ca/tutorials/GLP/.

However, we are usually given concentration as a function of time from batch reactor experiments:time (s) 0 t1 t2 t3

concentration (moles/dm3)

CA0 CA1 CA2 CA3

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Three Ways to determine (-dCA/dt) from Concentration-Time Data Graphical differentiationNumerical differentiation formulasDifferentiation of a polynomial fit to the data1. Graphical

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CAt

t

The method accentuates measurement error!

1t

A

dtdC

CAt

0

A

dtdC

2t

A

dtdC

0 1t 2t t

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Example - Finding Rate Lawt(min) 0 1 2 3

CA(mol/L) 1 0.7 0.5 0.35

0.3 0.2 0.15tCA

tCA

.1.2.3

t1 2 3

Areas equal for both sides of the histogram

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Example - Finding Rate LawFind the f(t) of using equal area differentiation t

CA

CA 1 0.7 0.5 0.35-dCA/dt 0.35 0.25 0.175 0.12Plot –dCA/dt as a function of CA

Ap

p

A

C

dtdC

k

ln

CA

Slope = α

dCA/dt

ln11

Non-Linear Least-Square Analysis

2 rmi rci 2

N Ki1

n

That is we want to be a minimum.

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We want to find the parameter values (α, k, E) for which the sum of the squares of the differences, the measured rate (rm), and the calculated rate (rc) is a minimum.

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Non-Linear Least-Square AnalysisFor concentration-time data, we can integrate the mole balance equation for to obtain

rA kCA

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dCAdt

kCA

t 0

CA CA 0

CA CA 01 1 kt 1

Non-Linear Least-Square Analysis

s2 CAmi CAci 2

i1

N

CAmi CA 01 1 kti 1 1 2

i1

N

We find the values of alpha and k which minimize s2

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Cmeas 1 0.7 0.5 0.35CCalc 1 0.5 0.3

30.25

(Cc-Cm) 0 -0.2 -0.17

-0.10

(Cc-Cm)2 0 0.04

0.029

0.01 0.07for α= 2, k = 1 → S2 = 0.07for α = 2, k = 2 → S2 = 0.27etc. until S2 is a minimum15

Regression MethodGuess values forα and k and solve for measured data points then sum squared differences:

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Residuals

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End of Lecture 11

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