CHAP. 9: CHEMICAL KINETICS [CONTENTS] 322
Example
A first-order reaction A
k
→ P, wherek = 0.1 hour−^1 , proceeds in a batch reactor. The
initial concentration of the reactant iscA0= 2.6 mol dm−^3. The reaction terminates when the
concentration of the substanceAfalls tocA= 0. 1 mol dm−^3. A total ofnP= 250 moles of the
product is to be produced. What must be the reactor volume and how long will the reaction
proceed?
Solution
cP=cA0−cA= 2. 5 mol dm−^3 =⇒ V =nP/cP= 250/ 2 .5 = 100dm^3.
The reaction time will be calculated from equation (9.24)
τ=
1
k
ln
cA0
cA
=
1
0. 1
ln
2. 6
0. 1
= 32. 58 hours.
9.7.3 Flow reactor.
If the reacting mixture flows through the reactor at a constant flow (volume rate), we have
dV
dτ
=F , (9.166)
whereF is the feed, i.e. the volume of reactants entering the reactor per unit time. By
integrating this relation we obtain
τr=
Vr
F
, (9.167)
whereτris theresidence time, i.e. the time in which the reacting mixture passes through the
reactor, andVris the reactor volume.
Note:Relation (9.167) and the relations ensuing from it do not apply if the total amount
of substance changes in the course of the reaction.