Full Papers
recyclability, up to five consecutive catalytic runs, for the cata-
lyst in the studied catalytic transformation.
furans, catalysts are generally active at higher temperatures
[Pd/C (1208C), Au/Nb2O5 (1408C), Pd/Al2O3 (1408C), Ni–Al2O3
(1808C)].[14,15b,28,29] Catalytic transformations with homogene-
ous catalysts show narrow product distributions and greater
selectivity towards the open-ring products, for instance, with
Cp*–Ir catalysts and arene–RuII catalysts.[16,17] Moreover, ruthe-
nium-based homogeneous catalysts were found to be highly
active and recyclable even in aqueous media.[17] In the present
study, arene–Ru complexes containing ethylenedia-
mine ligands were also found to be highly active and
stable even at 1008C in water and open atmospheric
conditions, and can be recycled in up to five consec-
utive catalytic cycles without any significant loss in
the catalytic activity. Moreover, the studied arene–Ru
catalyst [Ru]-1 has shown potential to convert fruc-
tose to LA and diketones (1-HHD, 3-HHD, 2,5-HD) in
water under moderate reaction conditions.
Catalytic transformation of fructose to LA and diketones
Next, we explored the catalytic transformation of fructose to
LA and diketones in the presence of 5 mol% [Ru]-1 catalyst
(Scheme 3).
Scheme 3. Catalytic transformation of fructose to LA and diketones.
After heating fructose at 1008C for 8 h in the presence of
12 equivalents of formic acid, conversion of fructose to 1-HHD
and LA as the major products were achieved with 27 and 51%
selectivity, respectively, along with 5-HMF (5%), diketone (4%),
and 3-HHD (13%) as minor products. The reaction products
obtained from fructose transformation were found to be analo-
gous to the products obtained with 5-HMF, suggesting that,
presumably, the reaction proceeds through the initial forma-
tion of 5-HMF.[3] Moreover, by increasing the reaction time to
16 h or doubling the formic acid amount (24 equiv.), the selec-
tivity for 1-HHD increased and 87% selectivity was observed
when the reaction was performed at 1008C for 16 h in the
presence of 12 equivalents of formic acid. Unfortunately, at-
tempts to use glucose in place to fructose failed, possibly be-
cause the [Ru]-1 catalyst cannot catalyze the isomerization of
glucose to fructose. Despite the low fructose transformation
observed for the catalytic reaction, it is worth noting that the
direct catalytic transformation of fructose to open-ring compo-
nents such as LA and diketones can also be achieved with
ruthenium-based homogenous catalysts.
Conclusions
Highly active water-soluble homogenous catalysts based on
arene–ruthenium(II) complexes containing simple and readily
available ethylenediamine (or its derivatives) ligands, were suc-
cessfully employed for the catalytic transformation of bio-
derived furans into open-ring value-added ketoacid (LA) and
diketones (1-HHD, 3-HHD, and 2,5-HD) in the presence of
formic acid. Depending upon the furan used, formic acid con-
centration, reaction temperature, and the catalyst, catalytic
conversion, selectivity, and the product distribution can be
fine-tuned. The NÀH bonds present in the ruthenium catalyst
were shown to exert a significant on the catalytic transforma-
tion, where the most active catalyst has the highest number of
NÀH bonds. Moreover, direct catalytic transformation of fruc-
tose to 1-HHD and LA was also achieved with limited conver-
1
sion. Mechanistic studies involving H NMR spectroscopy and
experiments with variable formic acid concentrations revealed
a tandem mode of catalytic transformation of furfural to LA via
the hydrogenated intermediate, furfuryl alcohol. Furthermore,
high aqueous solubility and stability of the ruthenium catalyst
offers the potential for easy recovery and reusability in at least
five consecutive catalytic runs without any significant loss of
the catalytic activity. Through our study, we have demonstrat-
ed a significant cooperation between the ruthenium catalyst
and formic acid to achieve high catalytic turnover for the trans-
formation of furans. We believe that this work will encourage
extensive research on the design and development of simple
yet active catalysts for this or several other important catalytic
transformations in the fine chemical industry and biofuel-
based energy sector.
Most of the studies on the transformation of furans have
been performed in autoclaves by using mineral acids or H2 gas
with high pressure and temperature.[15,16,25–28] Among these,
there are many reports on the catalytic transformation of 5-
HMF to ketoacids and diketones, particularly by using hetero-
geneous catalysts, whereas studies with homogeneous catalyst
are relatively few.[14,15b,16,17,25–30] Li et al. employed Amberlyst 70
for furfural transformation in water, as well as methanol, and
observed that furfural converted to a polymer in both reaction
media.[15a] Even by using Pd/Al2O3 with Amberlyst 70 and
70 bar H2 at 1658C in methanol, only low yields (23.1 and
2.4%) of methyl-levulinate and levulinic acid were achieved,
whereas Pd/Al2O3 on its own was found to be inactive.[26]
Riisager et al. explored Ru(OH)x/Al2O3 catalysts for the aerobic
oxidation of 5-HMF at 1408C, where LA was observed as a side
product along with the oxygenated products 2,5-furandi-
carboxylic acid and so on.[30] Also, LA was observed as a by-
product during the catalytic hydrogenation of furfural and 5-
HMF over a Pd–Ir/SiO2 catalyst.[27] In the transformation of
Experimental Section
Materials and methods
All reactions were performed without inert gas protection, using
chemicals of high purity purchased from Aldrich or Alfa Aesar. Di-
chloro-bridged arene–RuII precursors [{(h6-C6H6)RuCl2}2] and [{(h6-
ChemCatChem 2015, 7, 4050 – 4058
4056
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