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Chemical Reaction Engineering Chemical Reaction Engineering

Chemical Reaction Engineering - PowerPoint Presentation

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Chemical Reaction Engineering - PPT Presentation

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 2 1 Todays lecture Review of Lecture 1 Solution to ID: 652082

reactors reactor mole conversion reactor reactors conversion mole pfr series balance rate cstr volume design batch stoichiometry lecture laws levenspiel reaction rule

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Slide1

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 2

1Slide2

Today’s lecture

Review of Lecture 1Solution to P1-6Definition of Conversion, X

Develop the Design Equations in Terms of X

Size CSTRs and PFRs given –

rA= f(X)Conversion for Reactors in SeriesReview the Fall of the Tower of CRE

2Slide3

Reactor Mole Balance Summary

Reactor

Differential

Algebraic

Integral

CSTR

Batch

N

A

t

PFR

F

A

V

3Slide4

Homework

Problem Solution

4

Liquid

phase

Given the following information, Find VSlide5

(1) Mole

Balance:

(2) Rate Law:

(3)

Stoichiometry

:

5Slide6

(4) Combine:

(5) Evaluate:

6Slide7

Consider the generic reaction

7Slide8

Batch

8Slide9

Batch

Integrating

The necessary

t

to achieve conversion X.

9Slide10

CSTR

Steady

State

10Slide11

Well

Mixed

CSTR

CSTR

volume

necessary

to

achieve conversion X. 11Slide12

Steady

State

PFR

12Slide13

This is the PFR volume necessary to achieve conversion X.

PFR

Integrating

13Slide14

Reactor Mole

Balances in terms of conversion

Reactor

Differential

Algebraic

Integral

CSTR

PFR

Batch

X

t

PBR

X

W

14Slide15

Levenspiel Plots

Reactor Sizing

Given –r

A

as a function of conversion, -rA= f(X), one can size any type of reactor. We do

this by

constructing

a

Levenspiel plot. Here we plot either (FA0/-rA) or (1/-rA) as a function of X. For (FA0/-rA) vs. X, the volume of a CSTR and the volume of a PFR can be represented as the shaded areas in the Levenspiel Plots shown as:15Slide16

Levenspiel Plots

16Slide17

Numerical Evaluations of Integrals

The integral to calculate the PFR volume can be evaluated using method as Simpson’s One-Third Rule: (See Appendix A.4)Other numerical methods are:

Trapezoidal Rule (uses two data points)

Simpson’s

Three-Eight’s Rule (uses

four

data points)

Five-Point Quadrature Formula17Slide18

Reactors in Series

Given: rA as a function of conversion, one can also design any sequence of reactors:

Only

valid

if

there

are no

side streams.Molecule Flow rate of species A at point i: 18Slide19

Reactors in Series

19Slide20

Reactors in Series

Reactor 1:

20

V

1Slide21

Reactors in Series

Reactor 2:

21

V

2Slide22

Reactors in Series

Reactor 3:

22

V

3Slide23

Reactors in Series

23Slide24

Reactors in Series

Space time τ is the time necessary to process 1 reactor volume of fluid at entrance conditions.

24Slide25

KEEPING UP

The tower of CRE, is it stable?

25Slide26

Reaction Engineering

These topics build upon one another

Mole Balance

Rate Laws

Stoichiometry

26Slide27

Mole Balance

Rate Laws

Stoichiometry

Isothermal Design

Heat Effects

27Slide28

Mole Balance

Rate Laws

28Slide29

Mole Balance

Rate Laws

Stoichiometry

Isothermal Design

Heat Effects

29Slide30

End of Lecture 2

30