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Journal of the American Chemical Society
The transformation of toluene and its derivatives to the
electrode cell configuration consisting of (i) glassy carꢀ
bon working electrode, (ii) a Pt wire counter electrode,
and (iii) a calomel a reference electrode. experiments
were performed at room temperature. The scan rate was
50 mV sec–1. Electrolysis in a one cell configuration was
carried out using (i) Platinum gauze (working electrode),
(ii) a Pt wire (counter electrode), and (iii) Pt (a reference
electrode). The experiments were performed at 25ꢀ80
°C. Electrolysis in a two half cell configuaration was
carried out in presence of Pt gauze as working electrode,
and Pt wire as counter and reference electrode at differꢀ
ent potentials from 1.3 to 1.5 V between the anode and
cathode. The higher the potential the faster is the reoxiꢀ
dation reaction. The two half cells were separated by a
Nafion 212 membrane washed before use with 5% wt
H2O2 and 8% H2SO4 consecutively.
1
corresponding benzaldehyde compounds as presented in
Scheme 1, shows both the ETꢀOT oxidation of the subꢀ
strate and the formation of H2 in a second step to form a
cyclic repeatable process, for the high yield formation of
products with a 100% theoretical atom economy, conꢀ
sidering that H2 has value. The oxidation potential of
H5PV2Mo10O40 in this media, 1.1 V SCE (1.34 V NHE),
is higher than the potential for aerobic formation of waꢀ
ter (1.23 V NHE), equation 1. This prevents the thermal
reꢀoxidation of the reduced polyoxometalate and preꢀ
cludes an aerobic reaction requiring an electrochemical
oxidation of the reduced polyoxometalate. The generalꢀ
ly very high reaction yield lends an important practical
aspect to such a reaction with potential to replace comꢀ
mon nonꢀbenign procedures. Notably, the use of aqueous
H2SO4 as solvent leads to an aqueous biphasic reaction
medium,38 and therefore a simple cascade of operations
– (i) thermal substrate oxygenation, (ii) phase separation
of the organic and catalyst phase and (iii) catalyst recyꢀ
cle and recovery by electrolysis, can be implemented.
However, oneꢀstage electrocatalytic reactions are also
viable. The stability of the Nafion membrane in a two
halfꢀcell configuration at elevated temperatures someꢀ
times needed is a remaining technical issue to be solved.
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Computational method. All computations were done
using the same methodology previously described by us
for calculations involving H5PV2Mo10O40.32 Bulk solꢀ
vent effects of the sulfuric acid medium have been calꢀ
culated at the M06/PC1 level using the continuum solvaꢀ
tion model COSMO with a static dielectric constant, ε =
100.41
ASSOCIATED CONTENT
Supporting Information. Additional experimental inꢀ
formation and data. This material is available free of
In summary, the use of strong mineral acids as solvents
that allows significantly improved reactivity due to the
higher redox potential of H5PV2Mo10O40. There are also
advantages in catalyst recovery that are intrinsic to biꢀ
phasic media. Together with the unique ETꢀOT oxygenaꢀ
tion reactions that H5PV2Mo10O40 catalyzes, this reꢀ
search opens up new prospects for selective oxidative
transformations, demonstrated here by the selective
oxygenation of methylarenes.
AUTHOR INFORMATION
Corresponding Author
Email: Ronny.Neumann@weizmann.ac.il
ACKNOWLEDGMENT
This research was supported by the Israel Science Foundation
grants # 1073/10 and 763/14, the Bernice and Peter Cohn Catalyꢀ
sis Research Fund and the Helen and Martin Kimmel Center for
Molecular Design. R.N. is the Rebecca and Israel Sieff Professor
of Chemistry.
Experimental Section
Materials. Alkylarenes were of analytical grade. Deuꢀ
terated compounds were purchased from Cambridge
Isotope Laboratories. H5PV2Mo10O40•32H2O was preꢀ
pared by a known procedure.40
REFERENCES
Reactions. Typically the oxidation reactions of ArCH3
were carried out in 50 mL pressure tubes under N2 under
the conditions given in the tables and figures. The prodꢀ
ucts were decanted and diluted by dichloromethane for
analysis by gas chromatography. GCꢀFID (HP 6890) and
GCꢀMSD (HP 5973) instruments were used equipped
with a 5% phenyl methylsilicone 0.32 mm ID, 0.25 mm
coating, 30 m column (Restek 5MS) using helium as
carrier gas. H2 was volumetrically quantified by calibraꢀ
tion by GCꢀTCD using a 20' x 1/8" stainless steel colꢀ
umn packed with molecular Sieve 5Å in series with a 4'
x 1/8" stainless steel column packed with HayeSep T.
The carrier gas was Ar, column T = 90 °C.
1. Que Jr, L.; Tolman, W. B. Nature, 2008, 455, 333ꢀ340.
2. Bordeaux, M.; Galarneau, A.; Drone, J. Angew. Chem. Int.
Ed. 2012, 51, 10712–10723.
3. Poulos, T. L. Chem. Rev. 2014, 114, 3919ꢀ3962.
4. Nam, W.; Lee, Y.ꢀM; Fukuzumi, S. Acc. Chem. Res. 2014,
47, 1146ꢀ1154.
5. Partenheimer, W. Catal. Today 1995, 23, 69ꢀ158.
6. Crounse, N. N. Org. React. 1949, 5, 290–300.
7. Truce, W. E. Org. React. 1957, 9, 37–72.
8. Jones, G.; Stanforth, S. P. Org. React. 2004, 49, 1–330.
9. Wynberg, H.; Meijer, E. W. Org. React. 2005, 28, 1–36.
10. Rieche, A.; Gross, H.; Höft, E. Chem. Ber. 1960, 93, 88–94.
11. Olah, G. A.; Kuhn, S. J. J. Am. Chem. Soc. 1960, 82, 2380–
2382.
Electrolysis and cyclic voltammetry experiments. Cyꢀ
clic voltammetry experiments were performed using a
potentiostat (CHI660A) connected to a personal comꢀ
puter. The measurements were performed in a threeꢀ
12. K. Ditrich, Sci. Synth. 2007, 25, 575ꢀ584.
13. Klaus, S.; Neumann, H.; Zapf, A.; Strübing, D.; Hübner, S.;
Almena, J.; Riermeier, T.; Gross, P.; Sarich, M.; Krahnert, W.ꢀR.;
Rossen, K.; Beller, M. Angew. Chem. Int. Ed. 2006, 45, 154–158.
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