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(iv) Molecules of C adsorb on type 1 sites and molecules of D adsorb on type 2 sites
Derive an LHHW type rate expression that is consistent with this mechanism.
9.14. The solid-catalyzed exothermic reaction
catalyst
2 D
is virtually irreversible at low temperatures and low product concentrations, and the
rate law is given by
A 2 þ
2 B
%
kC 1=2
A 2 C B
r ¼
p
K A 2 C A 2
2
ð
1
þ
þ K B C B Þ
(a) How many active sites are involved in the rate-limiting step?
C A p appearing in denominator of the rate law? How many species are
adsorbed on the catalyst surface?
(c) Suggest a rate law that is valid for a wide range of temperature and concentrations.
(d) Suggest a mechanism for the rate law you have suggested. Identify the rate-limiting
step.
(e) Show that your mechanism is consistent with the rate law.
9.15. Synthesis of ammonia from nitrogen and hydrogen over Ru/C catalyst is found to
follow the following steps:
(b) Why is
N 2 þ s %
N 2 $s
(1)
N 2 $s þ s %
2 N $s
(2)
H 2 þ
2s %
2 H $s
(3)
H $s þ
N $s %
NH $s þ s
(4)
H $s þ
NH $s %
NH 2 $s þ s
(5)
H $s þ
NH 2 $s %
NH 3 $s þ s
(6)
NH 3 $s %
NH 3 þ s
(7)
þÞ ¼
þ
3 H 2 %
2 NH 3
(8)
overall
N
The surface reaction step (4) is found to be the rate-limiting step. Derive a rate expres-
sion that is consistent with the mechanism based on nonideal surfaces with ExLan
isotherm.
9.16. The rate law for the hydrogenation (H) of ethylene (E) to form ethane (A) over a cobalt-
molybdenum catalyst is found to be
r 0 A ¼ kP E P H ln 1
K E
P E
þ
Suggest a mechanism and rate-limiting step consistent with the rate law. Describe the
feature of the catalysts surface.
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