ROLE OF PEROXY COMPOUNDS IN OXIDATION OF CROTONALDEHYDE
1001
Table 3. Characteristics of the oxidate after oxidation and storage (CAl content at the beginning of experiments 2.46 M, oxidation
time 180 min, storage for 7 h at 318 K)
0
0
0
c
c
c
CAc
xCAl
S CAc + PCAc
%
cCAl
cPCAc
M
cCAc
xCAl
SCAc
CAl
PCAc
p ,
atm
T,*
K
O
2
M
%
3
3
3
3
3
00
00
00
09
09
1
2
4
1
16
1.23
0.96
0.61
0.68
0.38
0.70
1.03
0.96
0.95
1.00
0.33
0.47
0.54
0.53
0.66
50.0
61.0
75.2
72.4
84.6
84.0
83.0
81.1
83.1
80.0
0.52
0.05
0.02
0.03
0.01
0.02
0.03
0.02
0.03
0.03
1.69
2.28
2.05
2.09
1.99
79.7
98.0
99.1
98.8
99.6
87.1
94.6
84.0
86.0
81.2
*
(
T) Oxidation temperature.
the concentrations of CAl and PCAc decrease to a
similar extent, with the total concentration of CAc
and PCAc growing simultaneously. For example, in
The results of these studies allowed development
of an efficient procedure for preparing CAc [8].
7
h, the PCAc concentration decreased by 0.61 M;
CONCLUSION
that of CAl, by 0.59 M; and that of the sum of CAc
and PCAc increased by 0.6 M. Within the same time,
To achieve the maximum yield of crotonic acid, it
is appropriate to perform oxidation of crotonaldehyde
with molecular oxygen at 300 310 K to 55 65% con-
version of crotonaldehyde, when the concentrations of
perctoronic acid and unchanged crotonaldehyde in the
oxidate become approximately equal. The unchanged
crotonaldehyde is subsequently oxidized with percro-
tonic acid at 315 320 K within 7.0 7.5 h.
9
.6 ml of CO and 2.4 ml of CO evolved from the
2
oxidate (30 ml). Hence, at 318 K only 1 2% of PCAc
is spent for side reactions (initiated radical decomposi-
tion), whereas 98 99% of PCAc reacts with CAl to
form CAc.
At 333 K (Fig. 1b), PCAc is consumed considera-
bly faster, and the process is complete within approx-
imately 4 h. However, the relative contribution of
PCAc decomposition grows. For example, 15 ml of
REFERENCES
CO and 5.4 ml of CO evolved from the reactor in
1. Fedevich, O.E., Levush, S.S., and Kit, Yu.V., Visn.
Derzh. Univ. L’vivs’ka Politekh., Khim., Tekhnol.
Rech. Ikh Zastosuv., 1998, no. 339, pp. 165 167.
2. Fedevich, O.E., Levush, S.S., and Kit, Yu.V., Teor.
Eksp. Khim., 1999, vol. 35, no. 5, pp. 332 337.
2
4
h. Percrotonic acid is consumed noticeably faster
than CAl: in 4 h, the PCAc concentration decreased
by 0.62 M, and that of CAl, by 0.56 M. The total
concentration of CAc and PCAc grew by only 0.54 M
(
87% of the consumed PCAc).
3. Fedevich, O.E., Levush, S.S., Fedevich, E.V., and
Kit, Yu.V., Zh. Prikl. Khim., 2002, vol. 75, no. 7,
pp. 1146 1150.
Apparently, to ensure the most efficient utilization
of PCAc and maximum yield of CAc, the oxidate
should be kept at relatively low temperatures. Table 3
illustrates the variation of the oxidate composition at
4
. Houben Weyl, Methoden der organischen Chemie,
vol. 2: Analytische Methoden, Stuttgart: Thieme, 1953.
5
. Fedevich, O.E., Levush, S.S., Fedevich, E.V., and
Kit, Yu.V., Zh. Org. Khim., 2003, vol. 39, no. 1,
pp. 41 43.
3
18 K in the course of 7 h. It is seen that oxidation of
CAl to CAc with PCAc occurs more selectively than
oxidation with molecular oxygen to CAc and PCAc.
Table 3 shows that the maximum efficiency is reached
when the concentrations of the accumulated PCAc and
unchanged CAl in the oxidate by the end of autooxi-
dation are approximately equal. This situation is at-
tained at 60% conversion of CAl. In the course of
storage, unchanged CAl is oxidized with PCAc, and
the total selectivity with respect to CAc reaches 94%.
6
7
. Boboleva, S.P., Bulygin, M.V., Valov, P.I., and Blyum-
berg, E.A., Neftekhimiya, 1990, vol. 30, no. 2,
pp. 239 243.
. Pikh, Z.G., Selective Oxidation of Unsaturated Com-
pounds with Bound Oxygen, Doctoral Dissertation,
Lviv, 1994.
8. Ukrainian Patent, Method for Preparing Crotonic Acid,
Promysl. Vlasp., 2002, no. 6.
RUSSIAN JOURNAL OF APPLIED CHEMISTRY Vol. 77 No. 6 2004