6
LI ET AL.
alcohol. The total selectivity of benzaldehyde and benzyl
alcohol is 73.5% and the conversion of toluene is 9.7% at
210 min.
(380 m2 g−1). In the meantime, the catalyst remains highly
active under the optimized conditions. Particularly, the
conversion rate of toluene exceeds 9.0%, and the total
selectivity of benzaldehyde and benzyl alcohol remains
basically unchanged. Since industrial costs can be reduced
by continuing to increase the number of recycles, the catalyst
is potentially applicable in industry.
When [p‐ethynyl]4PMn is employed as catalyst (Figure 6
(b)), no benzoic acid is generated within 180 min. Even at
300 min, benzoic acid only accounts for 9.0% of the products,
and the total selectivity of benzaldehyde and benzyl alcohol
is as high as 75.5%, but the conversion rate of toluene is just
7.4%. The reaction was so slow that there was little benzalde-
hyde and benzyl alcohol generated before 30 min. Although
benzaldehyde increases rapidly and benzyl alcohol increases
slowly at later time, the total yields of benzaldehyde and
benzyl alcohol at 300 min (5.01%) are only similar to that
of MnE‐TPP as catalyst at 30 min (4.89%).
The total yields of benzaldehyde and benzyl alcohol,
when toluene oxidation was catalyzed by [p‐Br]4PMn,
increase rapidly to a plateau (5.24%) in about 30 min
(Figure 6(c)). With increasing time to 90 min, the yield of
benzoic acid exceeds those of benzaldehyde and benzyl
alcohol and keeps rising significantly thereafter. Although
the conversion rate of toluene is 12.0% at 300 min, the total
selectivity of benzaldehyde and benzyl alcohol is, however,
only 44.2%, which is much lower than that when MnE‐TPP
is used as catalyst (70%).
With MnE‐TPP (Table 1) as catalyst, the total selectivity
of benzaldehyde and benzyl alcohol is 70.0% at 10.2%
conversion of toluene, with a turnover number of about 13
653 mol at 160°C, 0.6 MPa and 1000 ml min−1 airflow rate.
Under the same conditions, the selectivity of total benzalde-
hyde and benzyl alcohol is 75.5% when [p‐ethynyl]4PMn is
used as the catalyst, but the conversion of toluene is only
7.4%. Although the conversion of toluene reaches 12.0% over
[p‐Br]4PMn, the total selectivity of benzaldehyde and benzyl
alcohol is only 44.2%. In comparison, Guo et al.[9] reported
that under catalysis of cobalt(II) tetraphenylporphyrin, the
highest conversion rate of toluene was only 8.9%, and the
maximum selectivity of total benzaldehyde and benzyl alco-
hol was just 60%. Hence, MnE‐TPP, which was synthesized
using [p‐ethynyl]4PMn and [p‐Br]4PMn, combines the
advantages of the two during toluene catalytic oxidation,
elevating the total selectivity of benzaldehyde and benzyl
alcohol, also the conversion rate of toluene.
4
| CONCLUSIONS
Single metal porphyrins are prone to loss of activity in
homogeneous catalytic oxidation due to gradual oxidization
and resulting in their single use. A metalloporphyrin
conjugated polymer with [p‐Br]4PMn and [p‐ethynyl]4PMn
as building blocks was synthesized in this work. With a
porous structure and large BET surface area, MnE‐TPP was
highly catalytically active in toluene oxidation and could be
reusable. Under MnE‐TPP catalysis, the total selectivity of
benzaldehyde and benzyl alcohol was 70.0% at 10.2%
conversion of toluene, with a turnover numbers of about 13
653 mol at 160°C, 0.6 MPa and 1000 ml min−1 airflow rate,
combining the advantages of the two during catalytic toluene
oxidation, elevating the conversion rate of toluene and the
total selectivity of benzaldehyde and benzyl alcohol. In addi-
tion, the porphyrin polymer had a recovery rate of over 90%,
thus meeting the requirements of modern green chemistry to
replace porphyrins for catalytic oxidation of hydrocarbons,
being potentially applicable to the industrial production of
benzaldehyde and benzyl alcohol.
ACKNOWLEDGMENTS
The financial support of the National Natural Science
Foundation of China (grant no. 21576074) is gratefully
acknowledged. We are also grateful for the financial support
of Hunan University.
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