Angewandte
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Chemie
Table 1: Biomass hydrolysis by W-Te-AC350 under different conditions.[a]
Entry Biomass t [h] T [8C] Conversion [%]
Yield based on carbon [%]
glucose mannose formic acid levulinic acid HMF
Total yield of organics [%]
1
2
3
4
5
6
7
cellobiose
sucrose
starch
4
4
4
2
2
2
2
130
130
130
175
175
175
175
93.1
99
–
–
–
90.5
43.9
78.4
8.8
19.0
25.8
0
0
0.1
3.3
0.5
0.5
0.7
3.0
0
0.1
15.1
1.0
1.1
2.5
8.5
0
0.7
7.8
1.2
0.7
1.2
2.0
0
91.4
72.0
81.3
14.0
30.6
47.1
0
1.9
0.2
2.9
7.2
7.8
0
microcrystalline cellulose[b]
ball-milled cellulose
ball-milled cellulose[c]
microcrystalline cellulose[d]
–
–
[a] Reaction conditions: biomass: 0.308 mmol based on glucose unit, W-Te-AC350: 0.05 g, water 0.5 mL. [b] Carbon balance was 86.7% (see details in
the Supporting Information). [c] cellulose: 0.185 mmol. [d] Without catalyst.
saccharides (Supporting Information, Tables S4 and S5).
Cellulose is more difficult to convert and was hydrolyzed at
1758C for 2 h. Hexoses (glucose and mannose) were the
primary products. Some other products were detected, such as
5-hydroxymethylfurfural (HMF), levulinic acid, and formic
acid. Ball-milling can decrease the crystallinity of cellulose
(Supporting Information, Figure S18) and activate the cellu-
lose.[14] The activity of the reaction increased using the ball-
milled cellulose (Table 1, entries 5,6). In the absence of the
catalyst, no products were detected (Table 1, entry 7).
The catalytic activities of different materials were inves-
tigated for comparison with W-Te-AC350. As shown in the
Supporting Information, Table S6, under the same conditions,
W-Te-AC350 was more active for microcrystalline cellulose
conversion than other solid acids based on the amount of acid.
Moreover, the activity of W-Te-AC350 was comparable to
homogeneous catalysts (Supporting Information, Table S6).
The calcination temperature affected the catalytic activity
of W-Te-AC350. As shown in the Supporting Information,
Figure S19, the as-synthesized material exhibited low activity,
and an increase in the calcination temperature enhanced the
activity. When the calcination was conducted at 3508C, the
highest activity was obtained. This result demonstrated that
acid sites were generated by calcination. However, a further
increase in the calcination temperature (4008C) deactivated
the catalyst, which was most likely due to structural decom-
position of the material at a high temperature. Therefore,
maintaining the nanowire structure is a key factor for high
catalytic activity.
The catalyst concentration was investigated. As the
catalyst concentration increased, the total detected products
increased, and hexoses tended to be further converted into
other products, such as levulinic acid and formic acid. A
decrease in the catalyst concentration effectively increased
the selectivity to hydrolysis products (Supporting Informa-
tion, Figure S20). Prolonging the reaction time yielded more
organic acids and HMF, although the total yield of detected
products increased (Supporting Information, Figure S21). A
decrease in the reaction temperature decreased the activity
and effectively suppressed the conversion of the generated
hexoses. The selectivity to hexose increased at a low reaction
temperature (Supporting Information, Figure S22).
low (Supporting Information, Figure S23). TEM (Supporting
Information, Figure S10i,j) and the size distribution (Sup-
porting Information, Figure S16) indicated that some nano-
wires were still in the solution. When a high-speed centrifu-
gation condition (48000 G, 24 h) was used, a higher activity of
the recovered catalyst was achieved.
The high catalytic activity of W-Te-AC350 was primarily
due to two factors: ultrafine nanosized catalyst particles after
dispersal and the strong interactions between the catalyst and
the biomass. W-Te-AC350 could be well dispersed in water
under hydrothermal conditions (1758C, 2 h). After the
hydrothermal treatment, the photographic images indicated
that the solution containing the material became transparent
and exhibited laser scattering, which indicated that the
material dispersed and formed ultrafine nanowires in water
(Supporting Information, Figure S24a,b). For a sample with
a low concentration, the laser scattering phenomenon still
existed after the hydrothermal treatment (Figure S24c,d),
indicating that the material was not dissolved in water but
dispersed. Before and after the hydrothermal treatment,
dynamic light scattering (DLS) was conducted for W-Te-
AC350, and the results revealed that after the hydrothermal
treatment, the particle size of the material decreased (Sup-
porting Information, Figure S25). The SEM and TEM images
(Figure S10e,f) revealed that W-Te-AC350 remained a nano-
wire. After the hydrothermal treatment, W-Te-AC350 was
dried at ꢁ308C under high vacuum. The surface area of the
dispersed W-Te-AC350 (15 m2 gꢁ1) was higher than that of the
as-synthesized W-Te oxide (Supporting Information, Fig-
ure S9). The adsorption under low pressure demonstrated the
existence of micropores that may be due to the gap formed by
isolated molecular wires. The calcined crystalline-W-Te oxide
(Supporting Information, Figure S26) exhibited a lower activ-
ity than that of W-Te-AC350, which indicated that the
nanosized material exhibited improved activity for the
reaction (Supporting Information, Table S6, entry 2). All of
the results demonstrated that the hydrothermal treatment
promoted dispersal of the material in water and increase in
the surface area.
Four oxygen sites are present in W-Te-AC350, including
corner-sharing oxygen (O1), edge-sharing oxygen (O2), layer-
sharing oxygen (O3), and terminal oxygen (O4), for proto-
nation without considering the interactions between protons
The catalyst can be reused. Elemental analysis indicated
that 47% of the catalyst was recovered by a low-speed
centrifugation (9800 G, 1 h). The activity of the catalyst was
+
with NH4 (Supporting Information, Figure S27). When O2
was protonated, the system energy was the lowest among all
4
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2016, 55, 1 – 6
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