TY - GEN
T1 - Catalytic conversion of formic acid into methanol in subcritical hydrothermal conditions
AU - Hu, Mingbo
AU - Jin, Fangming
AU - Ma, Cuixian
AU - Chen, Hongjuan
PY - 2010/12/1
Y1 - 2010/12/1
N2 - Efforts were made to explore the potentiality that formic acid gives a conversion into methanol by applying metallic catalysts in subcritical hydrothermal conditions. The subcritical hydrothermal conversion of formic acid into methanol was carried out by using Zn as a reductant and Ni as a catalyst. The effect of various experimental parameters, e.g., the amount of Zn (Ni), Zn/Ni ratio, temperature, pressure, reaction time and filling rate etc. was investigated. The conclusion showed that the highest methanol yield of 11.95% was achieved under proper conditions which was certified in the experiment that Zn/Ni ratio of 1:1.3, temperature of 180, reaction time of 12 hours, filling rate of 35%. Nickel, as one of transition metals, was effective catalyst in the hydrothermal conversion of formic acid into methanol. The reaction time was extended unavoidably with relatively low temperature. It can be expected that reaction time could have farther reduction with the increase of temperature. Additionally, the hydrothermal reaction can also occur without the addition of reductant and catalysts. According to the analysis of GC-TCD(thermal conductivity detector), H2 and CO2 were detected. It was supposed that formic acid gave a quick decomposition into H2 and CO2 initially and then the reaction of methanol synthesis occurred and the reaction of H2 and CO2 was proved existing through the observation of changes of H2 and CO2 amount. However, methanol can also be obtained through reducing formic acid with H2 as reductant. Based on present experimental analysis, it can be determined that the former reaction path has its priority. It is not sure that whether formic acid was directly reduced into methanol by H2.
AB - Efforts were made to explore the potentiality that formic acid gives a conversion into methanol by applying metallic catalysts in subcritical hydrothermal conditions. The subcritical hydrothermal conversion of formic acid into methanol was carried out by using Zn as a reductant and Ni as a catalyst. The effect of various experimental parameters, e.g., the amount of Zn (Ni), Zn/Ni ratio, temperature, pressure, reaction time and filling rate etc. was investigated. The conclusion showed that the highest methanol yield of 11.95% was achieved under proper conditions which was certified in the experiment that Zn/Ni ratio of 1:1.3, temperature of 180, reaction time of 12 hours, filling rate of 35%. Nickel, as one of transition metals, was effective catalyst in the hydrothermal conversion of formic acid into methanol. The reaction time was extended unavoidably with relatively low temperature. It can be expected that reaction time could have farther reduction with the increase of temperature. Additionally, the hydrothermal reaction can also occur without the addition of reductant and catalysts. According to the analysis of GC-TCD(thermal conductivity detector), H2 and CO2 were detected. It was supposed that formic acid gave a quick decomposition into H2 and CO2 initially and then the reaction of methanol synthesis occurred and the reaction of H2 and CO2 was proved existing through the observation of changes of H2 and CO2 amount. However, methanol can also be obtained through reducing formic acid with H2 as reductant. Based on present experimental analysis, it can be determined that the former reaction path has its priority. It is not sure that whether formic acid was directly reduced into methanol by H2.
KW - Hydrothermal conversion
KW - Metal catalyst
KW - Methanol
KW - Reaction path
KW - Reductant
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U2 - 10.1063/1.3456323
DO - 10.1063/1.3456323
M3 - Conference contribution
AN - SCOPUS:78650894359
SN - 9780735407985
T3 - AIP Conference Proceedings
SP - 238
EP - 241
BT - 2nd International Symposium on Aqua Science, Water Resource and Low Carbon Energy
T2 - 2nd International Symposium on Aqua Science, Water Resource and Low Carbon Energy
Y2 - 7 December 2009 through 10 December 2009
ER -