CHE594 - Lesson Plan - July 2010

8/10/2019 CHE594 - Lesson Plan - July 2010

1/5

LESSON PLAN

CHE594

CHEMICAL REACTION

ENGINEERING

FACULTY OF CHEMICAL ENGINEERING

UNIVERSITI TEKNOLOGI MARA

PAGE

1.0 COURSE INFORMATION

COURSE NAME : CHEMICAL REACTION ENGINEERING

COURSE CODE : CHE594

PROGRAM : EH220

SEMESTER : 4

CREDIT HOURS : 4

CONTACT HOURS : 4

COURSE STATUS : CORE

PRE-REQUISITE : NIL

2.0 SYNOPSIS

The course deals with the engineering activities concerned with the exploitation of chemical

reactions on a commercial scale. Its goal is the successful design and operation of chemical

reactors which set the chemical engineering apart as a distinct branch of engineering

profession. Thus, in designing and operating chemical reactors, important topics including

strong fundamentals in chemical kinetics, types of reactors and simple design approach to

more complex design are also discussed.

.0 O!"ECTIVES

Upon completion of this course, students should be able to:

1. pply principles related to chemical reactions to determine rate kinetics.

!. "erform basic design and predict the operating performance of different types of reactors

e.g. batch, continuous stirred tank and tubular flow reactors for single#multiple reactions

under isothermal and non$isothermal conditions.

%. pply the principles of catalytic reactions and design simple heterogeneous reactors.

&. pply the knowledge of this sub'ect in carrying out chemical engineering pro'ects.

4.0 METHODS OF INSTRUCTION

(ectures and tutorials

(ectures : % hours#week

Tutorials : 1 hour#week

1#)


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LESSON PLAN

CHE594

CHEMICAL REACTION

ENGINEERING



PAGE

#K DURATION TOPIC$CONTENT ACTIVITIES

1 1

T%&'( 1

I)*+%,(*'%) *% C/'( R/(*'%)

E)3')//+')3 ), R/(*'%) K')/*'(

$ *lassification of reactions

$ +efinition of reaction rate

lementary and non$elementary

reactions

-olecularity and order of reactions

inetic models for non$elementary

reactions

$ Temperature dependent term of a rate

e/uation

0ead C&*/+ 1

L/6/)&'/7

verview of

*hemical 0eaction

ngineering

0eadC&*/+ 2

L/6/)&'/7,

inetics of2omogeneous

0eactions

!$% !

T%&'( 2

D/*/+')*'%) %8 R*/ L

$ *onstant$volume of batch reactor

Integral method of analysis of data

+ifferential method of analysis of data

-ethod of Initial 0ates

-ethod of 2alf$(ives

$ 3arying$volume batch reactor

0ead C&*/+ 5

F%3/+74 *ollection

and nalysis of 0ate

+ata5

0ead C&*/+ L/6/)&'/7

Interpretation of

6atch 0eactor +ata

& 1

T%&'(

S*%'('%/*+'( T/ ), M*/+' !)(/

$ 7toichiometric Table

$ -aterial 6alance

$ 0elationship between *and 8

*ase 1: *onstant density and flow

systems

*ase !: 6atch and flow systems of

gases of changing density but with T

and 9 constant.

0ead C&*/+

F%3/+74 0ate (aws

and 7toichiometry

0ead C&*/+ 4

L/6/)&'/7

Introduction to0eactor +esign

!#)


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LESSON PLAN

CHE594

CHEMICAL REACTION

ENGINEERING



PAGE

) 1

T%&'( 4

D/'3) %8 I,/ R/(*%+ 8%+ S')3/ R/(*'%)

$ Ideal batch reactor 605

$ 7pace$time and space$velocity

$ 7teady state mixed flow reactor -;05

$ 7teady state plug flow reactor ";05

$ 2olding time and space time for flow reactor

$ 7i

A)@' %8 N%)-'%*/+ R/(*%+

$ 2eat of reaction

$ /uilibrium constants from thermodynamics

/uilibrium conversion

ffect of temperature on e/uilibrium

conversion at constant pressure

$ nergy balance in an -;0

$ nergy balance in a ";0

$ 2eat removal or addition to maintain a

reactor isothermal

$ diabatic -;0 B ";0

0ead C&*/+ ?=

F%3/+$ 7teady 7tate

Don$isothermal

0eactor +esign5

0ead C&*/+ 9

L/6/)&'/7

Temperature and

"ressure ffects

%#)


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LESSON PLAN

CHE594

CHEMICAL REACTION

ENGINEERING



PAGE

1! 1

T%&'( ?

N%)-',/ R/(*%+

$ 0esidence time distribution

$ 7tate of aggregation of the flowing stream

$ arliness of mixing

0ead C&*/+ 11

L/6/)&'/7

6asics of Don$Ideal

;low

0ead C&*/+ 1

F%3/+7+istribution

of 0esidence Times

for *hemical 0eactors

1% 1

T%&'( 9S%', C*@/, R/(*'%)

$ Introduction

$ +esign of catalytic reactor

$ 0eactors for determination of rate laws

TEST 2 %) T%&'( 5 *% ?

0ead C&*/+ 1>

L/6/)&'/7

2eterogeneous

0eactions

Introduction

0eadC&*/+ 1?

L/6/)&'/7

7olid *ataly


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LESSON PLAN

CHE594

CHEMICAL REACTION

ENGINEERING



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?.0 ADDITIONAL INFORMATION

"lease make appointments for any consultancy.

ttendance is compulsory.

Do make up test will be given unless for medical excuses with legal documents presented.

Do cheating in any aspect. Don$compliance will be met with the severest conse/uences.

PREPARED !Y: APPROVED !Y:

SIGNATURE:

NAME:

15 D0 ;J2 6IDTI I+0U7

!5 7ITI 0;I+2 6IDTI 6 072I+

%5 D027FI-I 6IDTI 02-T

&5 "- +0 -U0T2F 3"7 3(U0I

POSITION: (*TU00

DATE:

SIGNATURE:

NAME: +0. GUDI+2 GI

POSITION: *hairman,*hemical ngineering 7tudies

DATE:

)#)

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CHE594 - Lesson Plan - July 2010