N. Kashyap, S. Das and R. Borah
Polyhedron 196 (2021) 114993
ied yields of oxidized product which were observed to proceed
through either homogeneous or heterogeneous catalytic phases
in reaction media. The catalyst was seen to be soluble in MeOH,
CH3CN as polar solvents (Table 2, entries 2, 3) except water making
the reaction as homogenous catalysis and the percentage yield of
products were raised to higher levels. At the same time, the insol-
ubility of catalyst in H2O, CH2Cl2 and n-hexane converts the reac-
tion as heterogenous catalysis and pulling down the percentage
yields (Table 2, entries 1, 4, 5). In case of ethyl acetate solvent,
the catalyst was found to be sparingly soluble in the reaction med-
ium making the reaction system non homogenous in nature that
may be accounted for moderate yield of the product (Table 2, entry
7). The self-precipitation of the [DEDSA]3[PW12O40] catalyst from
the reaction mixture was done by pouring CH2Cl2 solvent in the
crude product mixture of oxidation obtained Fig. 11(a) after evap-
oration of the homogeneous solution of reaction in acetonitrile
under reduced pressure. The catalyst was recovered and reused
after filtration of the dichloromethane solution of oxidation pro-
duct by keeping in vacuum oven for 5 h at 80 °C. The other polyox-
ometalate catalyst [DEDSA]3[PMo12O40] also displayed similar
solubility behavior with these solvents which was represented in
Fig. 11(b) for the model reaction in acetonitrile. The solvent depen-
dence behavior of the IL-POM hybrid towards polar and non-polar
solvent can be considered as a combined outcome of secondary
interactions including H-bonding, ion–dipole interactions etc. for
each ionic component of the POM with the solvent molecules.
The inability of water to solubilize the catalyst can be expected
for insufficient H-bonding interaction with the water molecules
in presence of two hydrophobic ethyl groups tethered to the
ammonium cation of hybrid salt. This factor may become a prefer-
ential condition for self-aggregation of the POM hybrid in water
through intermolecular H-bonding interactions involving the
POM anion and -SO3H groups of the ammonium cation of the
hybrid material. The non-polar solvents like dichloromethane, hex-
ane etc. are favorable for self-aggregation of the POM hybrid. In
MeOH and CH3CN, each of the ionic component of POM hybrid
can make sufficient intermolecular H-bonding as well as ion–
dipole interactions with the solvent molecules in presence of slight
amount of miscible water which may increase the solubility of the
catalyst.
alyst in case of p-methoxy benzyl alcohol and p-hydroxy benzyl
alcohol (Table 3, entries 4,8) because of strong mesomeric effect
as compared to p-chloro benzyl alcohol (Table 3, entry 6). The elec-
tron donating substituents in benzyl alcohol expressed excellent
yields (Table 3, entry 3) while the substrates with electron with-
drawing group showed relatively low reactivity (Table 3, entries
5, 6) as observed from GC analysis. The % yield of oxidised product
of p-chloro benzyl alcohol was increased to some extent after
increasing the catalyst amount up to 4 mol% (Table 3, entry 7)
within 6.5 h reaction at 65 °C in CH3CN. Surprisingly, the optimized
amount of catalyst did not work with cyclohexanol even after
increasing the catalyst amount upto 4 mol % (Table 3, entry 9) at
the temperature of 65 °C. Acyclic 2° alcohols like 1-phenylethanol
and p-chloro-1 phenylethanol proceded efficiently for 2–3 h reac-
tion with varied amount of the catalyst (Table 3, entries 1, 11). In
case of oxidation of 4-phenyl-1-buten-4-ol, a rearranged
a, b
unsaturated keto compound was formed after shifting of double
bond position without oxidation (Table 3, entry 10). No carbonyl
products were obtained under the optimized condition for oxida-
tion of primary alcohol other than benzylic alcohol (Table 3, entry
12).
3.10.4. Plausible reaction mechanism
The mechanism (Scheme 3) demonstrates that the Keggin
polyanion in the IL-POM hybrids gets degraded in presence of
H2O2 to an active metal peroxo intermediate {PO4[MO(O2)2]4},3-
which is found to be responsible for the oxidation reaction
[7,58,59]. This was further evidenced from respective IR spectrum
of peroxo intermediate isolated after treatment of the [DEDSA]3-
PW12O40 with H2O2 solution at room temperature (Fig. S5). The spec-
trum displayed peaks at 857 cmꢃ1 for (OAO) vibration, 555 cmꢃ1
t
for symmetric metal–oxygen (W–O2) stretching frequency and
677 cmꢃ1 for asymmetric (W–O2) stretching frequency which also
proved the involvement of peroxophosphometalate intermediate in
the oxidation reaction [60,61].
3.10.5. Recyclability of catalyst
The catalytic recyclability was studied by taking 3 mmol of 1-
phenylethanol as model substrate with the optimized amount of
[DEDSA]3PW12O40 catalyst for 2 h reaction in CH3CN at 65 °C. The
catalyst was precipitated out from the homogeneous solution of
acetonitrile through addition of dry CH2Cl2 which is insoluble in
CH2Cl2. The POM catalyst was then washed with hexane and then
reactivated in vacuum oven at 80 °C for 5 h for next catalytic run.
Fig. 12 displays reusability profile of the spent catalyst for seven
consecutive cycles. Similar catalytic activity with each cycle was
observed till third run with modest decrease in yield after the
3.10.3. Substrate scope study
The substrate scope study of oxidation reaction was investi-
gated in acetonitrile solution for different substituted benzyl alco-
hol or cyclic/acyclic secondary alcohol under the optimized
condition using [DEDSA]3[PW12O40] as catalyst (Table 3). The rate
of oxidation was found to be relatively high with 3 mol% of the cat-
Fig. 11. Photograph of (a) [DEDSA]3[PW12O40] and (b) [DEDSA]3[PMo12O40] switching from homogenous reaction medium in left testube to heterogenous one by self-
precipitating in testube kept in right after evaporation of acetonitrile solvent and pouring dry CH2Cl2 afterwards.
10