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- (125b) Hydrodeoxygenation of Biomass-Derived Compounds to Biofuels
Table 1: Catalytic performance for HDO of guaiacol.a
|
Catalysts |
10Cu/C |
10Fe/C |
2Pd10Fe/C |
5Pd/C |
5Pt/C |
5Ru/C |
|||||
|
Temperature/°C |
350 |
350 |
450 |
350 |
450 |
250 |
350 |
250 |
350 |
250 |
350 |
|
Conversion (%) |
69.5 |
96.0 |
96.4 |
99.1 |
100.0 |
50.4 |
98.8 |
87.7 |
97.1 |
95.5 |
100.0 |
|
Benzene (%)* |
0.2 |
3.6 |
36.4 |
21.7 |
75.9 |
0.5 |
2.4 |
0.9 |
28.7 |
5.0 |
0.0 |
|
Toluene/TMB (%)* |
0.6 |
2.8 |
6.8 |
4.2 |
7.3 |
0.2 |
0.3 |
0.1 |
0.6 |
0.1 |
0.0 |
|
Phenol (%)* |
54.6 |
72.3 |
38.5 |
57.5 |
0.0 |
30.6 |
78.8 |
50.0 |
28.3 |
61.6 |
0.0 |
|
O-Cresol (%)* |
2.1 |
4.5 |
2.1 |
2.6 |
0.0 |
0.2 |
0.5 |
0.4 |
0.6 |
0.3 |
0.0 |
|
Cyclohexanone* |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
8.6 |
0.0 |
12.3 |
0.0 |
9.7 |
0.0 |
|
Cyclohexanol* |
0.0 |
0.0 |
0.0 |
0.0 |
0.0 |
0.4 |
0.0 |
5.0 |
0.0 |
4.4 |
0.0 |
|
Catechol (%)* |
2.5 |
0.1 |
0.0 |
0.0 |
0.0 |
0.2 |
0.5 |
0.0 |
0.0 |
0.0 |
0.0 |
|
Gas phase (%)*b |
9.5 |
12.7 |
12.5 |
13.2 |
12.7 |
5.2 |
16.2 |
11.4 |
38.8 |
13.1 |
100.0 |
|
Others (%)*c |
0.0 |
0.0 |
0.0 |
0.0 |
4.1 |
4.6 |
0.0 |
7.6 |
0.0 |
1.2 |
0.0 |
*Represent products yield. a Reaction conditions: 100 mg, Pguaiacol=0.42 %; PH2=40%; W/F=0.15 s.g.mL-1; bGas phase products mainly include methanol, methane, CO, CO2 and small amounts of ethane. c others represent unidentified species which was quantified based on the catechol, for 2Pd10Fe/C, others refers to biphenyl; For 5Ru/C and 5Pt/C, others are mainly composed of other hydrogenated six-membered ring compounds (e.g., 2-methoxycyclohexanone, 2-methoxycyclohexanol) and traces amount of anisole, 1,2-dimethoxyphenol. Note: Theoretically, when gas phase selectivity is lower than 14.2% (corresponding to 1mol gas products per GUA via demethylation/demethoxylation), we assume there is negligible ring-opening reaction.