and hydrogen peroxide through the formation of 1-hydroxy-1-hydroperoxycyclohex-
ane (11) (path 1). Treatment of the resulting reaction mixture with an appropriate
catalyst would produce e-caprolactone (12) (path 2). A KA oil consisting of a 1 : 1
mixture of 3 and 2 was employed as a model starting material. If the aerobic oxidation
of the KA oil in the presence of NHPI is completed, 2 equiv. of 3 and 1 equiv. of H
2
O
2
are expected to be formed. Treatment of a 1 : 1 mixture of 3 (6 mmol) and 2 (6 mmol)
by catalytic amounts of NHPI (0.6 mmol) and 2,2
0
-azobisisobutyronitrile (AIBN)
(0.3 mmol) under an O
2
atmosphere in CH
3
CN at 75
C for 15 h, followed by InCl
3
(0.45 mmol) at 25
C for 6 h affords 12 in 57% selectivity based on the KA oil reacted,
and 77% of KA oil was recovered (Eq. (6.21)). Water-stable Lewis acids such as
Sc(OTf)
3
and Gd(OTf)
3
afford e -caprolactone in somewhat lower yields [125].
ð6:21Þ
6.2.7
Preparation of e-Caprolactam Precursor from KA Oil
e-Caprolactam (CL) is a very important monomer for the production of nylon-6, and
about 4.2 million tons of CL were manufactured worldwide in 1998 [126]. Most
current methods of CL production involve the conversion of cyclohexanone with
hydroxylamine sulfate into cyclohexanone oxime followed by Beckmann rearrange-
ment by the action of oleum and then treatment with ammonia, giving CL. A serious
drawback of this process is the co-production of a large amount of ammonium sulfate
waste [126, 127]. Raja and Thomas reported a method for one-step production of
cyclohexanone oxime and CL by the reaction of cyclohexanone with ammonia under
high-pressure air (34.5 atm) in the presence of a bifunctional molecular sieve
catalyst [128]. Hydrogen peroxide oxidation of cyclohexanone in the presence of
NH
3
catalyzed by titanium silicate is reported to produce CL [129]. In patent work, on
the other hand, the transformation of 1,1
0
-peroxydicyclohexylamine (PDHA) to a 1 : 1
mixture of CL and cyclohexanone by LiBr has been reported [130].
It is interesting to develop a novel route to the CL precursor, PDHA, which was
hitherto prepared by hydrogen peroxide oxidation of cyclohexanone (3) followed by
treatment with ammonia [126, 130]. Because of the ease of transformation of PDHA
to a 1 : 1 mixture of CL and 3 under the influence of an appropriate catalyst such as
lithium halides, the CL production via PDHA is considered to be a superior candidate
for a next-generation waste-free process for CL. The NHPI-catalyzed aerobic oxida-
tion of KA oil was applied to the synthesis of PDHA without formation of
any ammonium sulfate waste. The strategy is outlined in Scheme 6.10. The
NHPI-catalyzed oxidation of KA oil (a mixture of 3 and 2) with O
2
produces 1,1
0
-
dihydroxydicyclohexyl peroxide, which seems to exist in equilibrium with cyclohex-
anone and H
2
O
2
(path 1). Subsequent treatment of the resulting reaction mixture
210
j
6 Aerobic Oxidations and Related Reactions Catalyzed by N-Hydroxyphthalimide