514 11 The Rates of Chemical Reactions
We have
d[F]
dt
k 1 [A]k 1 [A] 0 e−(k^1 +k^2 )t (11.6-5)
The right-hand side of this equation does not contain [F], so we can multiply bydtand
integrate to obtain
[F]t′−[F] 0 [F]t′
−k 1 [A] 0
k 1 +k 2
(e−(k^1 +k^2 )t
′
−1) (11.6-6)
where we assume that[F] 0 0. A similar treatment for[G]gives the same result except
thatk 1 is replaced byk 2 in the numerator:
[G]t′−[G] 0 [G]t′
−k 2 [A] 0
k 1 +k 2
(e−(k^1 +k^2 )t
′
−1) (11.6-7)
where we also assume that[G] 0 0 .The ratio[F]/[G]has the same value at any time:
[F]
[G]
k 1
k 2
(reverse reactions negligible) (11.6-8)
Exercise 11.22
For the reactions shown in Eq. (11.6-1) assume that[A] 0 0 .500 mol L−^1 , thatk 1 0 .100 s−^1
and thatk 2 0 .0100 s−^1. Construct a graph showing [A], [F], and [G] fortranging from
0to20s.
If the reverse reactions cannot be neglected, the situation can be different. If the
system comes to equilibrium,
[F]eq
[A]eq
k 1
k′ 1
K 1 (11.6-9a)
[G]eq
[A]eq
k 2
k′ 2
K 2 (11.6-9b)
so that
[F]eq
[G]eq
k 1
k 1 ′
k′ 2
k 2
k 1
k 2
k′ 2
k′ 1
K 1
K 2
(at equilibrium) (11.6-10)
Depending on the values of the four rate constants, this ratio might differ significantly
from the ratio in Eq. (11.6-8). If F is a desired product and G is an undesired product,
the ratio of[F]to[G]might be optimized by allowing the system to come to equi-
librium (usingthermodynamic control) or by stopping the reaction before it comes to
equilibrium (usingkinetic control).