CHEN3010 Lecture Notes - Lecture 2: Hung Pham, Prentice Hall, Reaction Rate
Chemical Reaction Engineering
Unit CHEN3010/5040
Semester 1 / 2018
Week 2
Lecture 1
Conversion and Reactor Sizing
(Fogler Chapter 2)
Based on the prescribed textbook: H. Scott Fogler; Elements of Chemical Reaction Engineering; Fifth Edition 2016; Prentice Hall
Gia Hung Pham
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Objectives
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Conversion
We have the following chemical reaction
aA+bBcC+dD
a,b,c,d : stoichiometric coefficient
A,B,C,D : chemical species
Taking species A as our basic of calculation, we divide the
reaction expression through by the stoichiometric
coefficient of A.
D
a
d
C
a
c
B
a
b
A
Limiting reactant
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Document Summary
Based on the prescribed textbook: h. scott fogler; elements of chemical reaction engineering; fifth edition 2016; prentice hall. We have the following chemical reaction aa bb cc dd a,b,c,d : stoichiometric coefficient. Taking species a as our basic of calculation, we divide the reaction expression through by the stoichiometric coefficient of a. Now we can put every quantity on a per mol of a" basic. The conversion xa is the number of moles of a that have reacted per mole of a fed to the system. At the time t=0 min : number of moles of a = na0. At the time t=t min : number of moles of a reacted = na0 xa. Number of moles of a that remains in the reactor after a time t. Moles of a in reactor at time t=t min. This is the mole balance for batch reactor (br) We use the rate of disappearance of a; -ra for the mol balance. dn.