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not deactivated in the process. In an additional experiment to
assess fl-BN catalytic stability, a 10 times-larger amount of
phenol (1000 mgLꢁ1), close to the saturation limit at the reac-
tion pH, was used alongside a 4 times-lower catalyst amount
(50 mgLꢁ1), which effected complete phenol disappearance
even under these conditions. Furthermore, H2O2 was not com-
pletely consumed (only 80%), maintaining the same 8 equiva-
lent consumption as in the other experiments, indicating that
there is not deactivation even under these conditions.
To support the generation of free OH radicals, we carried
out a test of phenol degradation in the presence of dimethyl
·
sulfoxide (DMSO). DMSO is a known quencher of OH radi-
cals.[36–38] DMSO acting as an OH quencher completely stops
·
·
phenol degradation (Figure 6D). We also performed OH radical
trapping using phenyl tert-butyl nitrone (PBNO) as quencher,
monitoring the process by conventional EPR spectroscopy (Fig-
ure 6D, inset). As anticipated, the characteristic EPR spectra
·
corresponding to the OH/PBNO adduct was recorded, provid-
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Most of the precedents in the catalytic Fenton degradation
of phenol use a very large H2O2 excess, frequently above
1000 times.[31–34] In contrast, herein only 11 equivalents of H2O2
were employed but only 8 equivalents were consumed. This
efficiency in the utilization of H2O2 is remarkable and close to
the theoretical limit. Thus, oxidation of phenol to benzoqui-
none, via dihydroxybenzene intermediate, requires 3 equiva-
lents of H2O2 [Eq. (2)], plus an additional 3 equivalents for site
regeneration. Therefore, a total of 6 equivalents of H2O2 are
necessary to catalytically convert phenol to benzoquinone,
close to the 8 equivalents of H2O2 consumed in these experi-
ments (Figure 6A and B). This is orders of magnitude more effi-
cient that common Fenton catalysts reported. Therefore, the
negligible H2O2 decomposition by fl-BN is very minor com-
pared to previously reported catalysts.[31]
ing firm evidence of the generation of free OH radicals by BN.
With respect to the nature of the active sites that reduce
·
H2O2 to OH radicals, we propose that they could be N atoms
at the periphery, probably bound to oxygen. To support this
proposal, the catalytic activity of pyridine-N-oxide was
checked. It was observed that this molecule was able to pro-
mote degradation of phenol, providing experimental evidence
for the nature of the fl-BN active sites. Accordingly, the very
low activity as a Fenton catalyst measured for commercial h-
BN (Figure 6A and B, closed circles) compared to fl-BN should
be due to the poor dispersibility in water of h-BN and the
smaller population of active sites, rather than to structural dif-
ferences between the two materials.
Conclusion
Herein, we have presented an innovative procedure based on
the use of biomass waste to template the synthesis of fl-BN on
arbitrary substrates or for fl-BN platelets in suspension. The
success of the film formation derives from the known property
of chitosan to form defect-free nanometric films with subnano-
metric roughness and its capability to embed ammonium
borate, templating its pyrolysis. The pyrolysis of the (NH4)3BO3–
chitosan material led to the spontaneous segregation of BN
and subsequent combustion of the carbon afforded fl-BN. The
process can also be carried out with particles that, after easy
exfoliation, formed fl-BN platelets suspended in water and
other solvents. The quality of the BN materials was determined
by electron microscopy and also by the characteristic deep UV
photoluminescence. The BN platelets could be suspended in
water, which allowed this material’s activity as a Fenton cata-
lyst to be tested, demonstrating an extremely high efficiency
for the generation of free hydroxyl radicals without significant
H2O2 decomposition.
Analysis of the product distribution shows the formation of
hydroquinone, catechol, and benzoquinone. The temporal evo-
lution of these products (Figure 6C) shows that they are pri-
mary degradation products appearing since the initial reaction
time, but that they undergo degradation over the course of
the reaction, reaching concentration maxima and, then, their
concentration diminishes at longer times. The high efficiency
in the use of H2O2 and the low excess required for the com-
plete disappearance of phenol using BN as catalyst can be un-
derstood considering that, once formed in the redox site, hy-
droxyl radicals will not have affinity for the surface of BN due
to its chemical inertness and, therefore, they will become free
·OH radicals in solution. In most of the Fenton catalysts report-
Experimental Section
Synthesis of h-BN films
Prior to coating, the quartz supports were treated to increase their
surface hydrophilicity. For this purpose, quartz plates (1ꢃ1 cm2,
1 mm thick) were immersed overnight in a 1m HCl aqueous solu-
tion and then washed exhaustively with Milli Q water, acetone, and
isopropanol by sonication for 15 min in each solvent. After clean-
ing, the quartz plates were submitted to ozonization during
30 min to decompose any residual organic matter. Afterwards, an
aqueous solution of chitosan (1.12 g, high quality chitosan of
MW 60,000–120,000 from Aldrich, ref. 740063, dissolved in a 25 mL
of 0.3m acetic acid aqueous solution) and (NH4)3BO3 (0.45 g) was
·
ed to date, OH radicals become attached to the metal and do
·
not really form free OH radicals.[31] Only in a few cases, using
·
extremely robust diamond nanoparticles, have OH radicals
generated catalytically been claimed as free radicals in solu-
tion,[35] and the present case would be similar, considering that
the surface of BN is even more inert.
Chem. Eur. J. 2014, 20, 1 – 8
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