W. Deng et al. / Journal of Molecular Catalysis A: Chemical 372 (2013) 84–89
87
Table 3
Effect of the concentration of methanol on the toluene oxidation.
Table 5
Effect of the concentration of (T(p-Cl)PP)MnF on the toluene oxidation.
CH3OH (mmol)
Con. (mol%)
Selectivity (mol%)
(T(p-Cl)PP)MnF
ppm)
Conversion
(mol%)
TON (mol/mol)
Yield (mol%)
(
BA
BAL
BAC
BA
0.05
11.5
14.3
BAL
BAC
0.00
19.8
21.1
15.6
31.2
46.9
78.1
13.2
15.4
24.5
38.2
63.9
58.7
50.4
37.5
5.8
6.2
5.6
6.3
29.2
33.1
42.5
55.3
0
10
20
0.13
34.0
38.2
–
155,135
174,333
0.02
2.1
2.4
Reaction conditions: NHPI 5 mol%, CH3OH 78.1 mmol, HOAc 20 ml, O2 0.05 L/min,
◦
Reaction conditions: toluene 0.13 mol, NHPI 5 mol%, (T(p-Cl)PP)MnF 20 ppm, HOAc
0 ml, O2 0.05 L/min, temperature 100 C, reaction time 10 h.
temperature 100 C, reaction time 10 h.
◦
2
of toluene oxidation are obtained. In contrast, when some amount
of isopropanol or tert-butyl alcohol with larger steric hindrance
was added in the reaction solution, the oxidation of toluene was
slowed down considerably. It could be attributed to the larger steric
hindrance of branched-chain alcohols prohibiting molecular oxy-
gen from getting near the catalyst after the catalyst (T(p-Cl)PP)MnF
was coordinated with the added alcohol, consequently the ability of
3
.3. The effect of other reaction parameters on the toluene
oxidation
3.3.1. The effect of the amount of methanol
In order to further study the influence of alcohol on the toluene
oxidation catalyzed by (T(p-Cl)PP)MnF/NHPI, the changes of the
toluene conversion and the selectivity of benzaldehyde and ben-
zyl alcohol were investigated by varying the amount of methanol
added into the reaction solution. The results are listed in Table 3.
When the amount of methanol added was 15.6 mmol, the conver-
sion of toluene and the selectivities of benzaldehyde and benzyl
alcohol are 13.2%, 63.9%, 5.8% respectively. When the amount of
methanol added was further increased, the conversion and the
yield of benzaldehyde and benzyl alcohol increased rapidly. When
(T(p-Cl)PP)MnF activating dioxygen was decreased and the rate of
toluene oxidation was slowed down. Similar phenomenon was also
observed in the investigation of the aerobic oxidation of p-xylene
influenced with p-toluic alcohol by our research group [36].
3.3.3. The effect of the concentration of (T(p-Cl)PP)MnF
The catalyst concentration is a key factor influencing the conver-
sion and product selectivity in metalloporphyrin-catalyzed alkane
oxidations [10,17]. In order to understand the effect of the concen-
tration of (T(p-Cl)PP)MnF on the toluene oxidation, we investigated
the changes of the toluene conversion and the selectivity of
benzaldehyde and benzyl alcohol with different (T(p-Cl)PP)MnF
concentrations, and the results are shown in Table 5. With no cat-
alyst, the toluene conversion was about 0.13%. When 10 or 20 ppm
of (T(p-Cl)PP)MnF was used in the reaction, the toluene conver-
sion was increased to above 34% while the yield of benzaldehyde
was between 11 and 14%. In contrast the yield of benzyl alcohol was
only around 2%. It should be noted that the molar turnover numbers
were more than 150,000 in these reactions. These results illustrate
that the toluene conversion and benzaldehyde/benzyl alcohol yield
increased significantly when a small amount of (T(p-Cl)PP)MnF was
added, and the metalloporphyrin catalyst is a highly efficient cata-
lyst for the selective oxidation of toluene.
7
8.1 mmol of methanol was added, the conversion went up to 38.2%
and the selectivity of benzaldehyde dropped to 37.5%, in other
words, the total yield of benzaldehyde and benzyl alcohol was
1
6.2%. This is understandable since at higher conversion, more alde-
hyde and alcohol were converted to benzoic acids, thus lowering
the selectivities. However, the yield increase can be rationalized
by better coordination of methanol with (T(p-Cl)PP)MnF at higher
concentrations. When the methanol concentration was lower, only
some of the (T(p-Cl)PP)MnF catalysts were coordinated axially
with methanol. When the methanol concentration was higher,
most of the (T(p-Cl)PP)MnF catalysts were converted to the sta-
+
IV
+•
ble [(T(p-Cl)PP)Mn(CH OH) ] or [(T(p-Cl)PP)Mn (O)(CH OH)]
3
2
3
in the process of toluene oxidation. Some literatures [30,34] have
also reported that the increase of alcohol concentration could
change the reductive potentials of metalloporphyrins, thus influ-
encing their catalytic ability in chemical reactions.
3
.3.4. The effect of reaction time on the toluene oxidation
The changes of toluene conversion and the selectivity of benz-
3
.3.2. The effect of aliphatic alcohol structure
In order to gain further insight into the effect of aliphatic alco-
aldehyde and benzyl alcohol of the toluene oxidation with reaction
time are shown in Fig. 4. The plot shows that the conversion of
toluene increased and the selectivity to benzaldehyde and benzyl
alcohol decreased with reaction time. When the reaction time was
hol on the catalytic ability of manganese porphyrin, the changes of
toluene conversion and yields of benzaldehyde and benzyl alcohol
were investigated by adding different aliphatic alcohols. The results
are shown in Table 4. The influences of different aliphatic alcohols
on the toluene oxidation over (T(p-Cl)PP)MnF/NHPI are significant
different. Straight-chain alcohols, such as methanol, ethanol, and
propanol which have smaller steric hindrance, can promote the
catalytic ability of manganese porphyrin and higher conversions
1
0 h, the maximum conversion of toluene was up to 12.8%, and
the selectivities of benzaldehyde and benzyl alcohol was 37.5% and
.3%, respectively, in the absence of any alcohol. When methanol or
6
ethanol was added into the reaction solution, the maximum con-
version of toluene was increased significantly to 38.2% or 32.1%
respectively, and the selectivities of benzaldehyde and benzyl alco-
hol were maintained between 37.5 and 42.4% and 6.3 and 7.1%,
respectively.
Table 4
Effect of different aliphatic alcohols on the toluene oxidation.
Alcohols
Conversion (mol%)
Selectivity (mol%)
3
.3.5. The effect of reaction temperature on the toluene oxidation
Normally temperature is very important on the metallopor-
BA
BAL
BAC
–
12.8
38.2
32.1
17.5
8.4
39.6
37.5
42.4
56.2
75.0
69.0
4.7
6.3
7.1
7.8
9.4
8.3
54.3
55.3
49.2
34.5
14.1
20.8
phyrin catalyzed reactions. Increasing reaction temperature can
shorten the induction period and accelerate the reaction rate of
metalloporphyrin catalyzed reactions [37,18]. In this paper, the
influence of reaction temperature on the toluene oxidation cat-
alyzed by (T(p-Cl)PP)MnF/NHPI with methanol at the temperature
CH3OH
CH3CH2OH
CH3CH2CH2OH
(
(
CH3)2CHOH
CH3)3COH
7.5
◦
Reaction conditions: toluene 0.13 mol, NHPI 5 mol%, (T(p-Cl)PP)MnF 20 ppm, alcohol
8.1 mmol, HOAc 20 ml, O2 0.05 L/min, temperature 100 C, reaction time 10 h.
range of 70–100 C was investigated. As illustrated in Table 6,
the conversion of toluene was influenced significantly by the
◦
7