TY - JOUR
T1 - Direct synthesis of ethanol from dimethyl ether and syngas over combined H-Mordenite and Cu/ZnO catalysts
AU - Li, Xingang
AU - San, Xiaoguang
AU - Zhang, Yi
AU - Ichii, Takashi
AU - Meng, Ming
AU - Tan, Yisheng
AU - Tsubaki, Noritatsu
PY - 2010/10
Y1 - 2010/10
N2 - Ethanol was directly synthesized from dimethyl ether (DME) and syngas with the combined H-Mordenite and Cu/ZnO catalysts that were separately loaded in a dual-catalyst bed reactor. Methyl acetate (MA) was formed by DME carbonylation over the H-Mordenite catalyst. Thereafter, ethanol and methanol were produced by MA hydrogenation over the Cu/ZnO catalyst. With the reactant gas containing 1.0 % DME, the optimized temperature for the reaction was at 493 K to reach 100 % conversion. In the products, the yield of methanol and ethanol could reach 46.3 % and 42.2 %, respectively, with a small amount of MA, ethyl acetate, and CO2. This process is environmentally friendly as the main byproduct methanol can be recycled to DME by a dehydration reaction. In contrast, for the physically mixed catalysts, the low conversion of DME and high selectivity of methanol were observed.Do or dual not: A dual-catalyst bed reactor loaded separately with the Cu/ZnO and H-Mordenite catalyst is employed to directly synthesize ethanol from dimethyl ether (DME) and syngas. The yield of ethanol and the main byproduct methanol are 42.2 % and 46.3 %, respectively. The latter can be further recycled to DME realizing an environmentally friendly process.
AB - Ethanol was directly synthesized from dimethyl ether (DME) and syngas with the combined H-Mordenite and Cu/ZnO catalysts that were separately loaded in a dual-catalyst bed reactor. Methyl acetate (MA) was formed by DME carbonylation over the H-Mordenite catalyst. Thereafter, ethanol and methanol were produced by MA hydrogenation over the Cu/ZnO catalyst. With the reactant gas containing 1.0 % DME, the optimized temperature for the reaction was at 493 K to reach 100 % conversion. In the products, the yield of methanol and ethanol could reach 46.3 % and 42.2 %, respectively, with a small amount of MA, ethyl acetate, and CO2. This process is environmentally friendly as the main byproduct methanol can be recycled to DME by a dehydration reaction. In contrast, for the physically mixed catalysts, the low conversion of DME and high selectivity of methanol were observed.Do or dual not: A dual-catalyst bed reactor loaded separately with the Cu/ZnO and H-Mordenite catalyst is employed to directly synthesize ethanol from dimethyl ether (DME) and syngas. The yield of ethanol and the main byproduct methanol are 42.2 % and 46.3 %, respectively. The latter can be further recycled to DME realizing an environmentally friendly process.
KW - Alcohols
KW - Carbonylation
KW - Ethers
KW - Heterogeneous catalysis
KW - Hydrogenation
UR - http://www.scopus.com/inward/record.url?scp=77958575677&partnerID=8YFLogxK
U2 - 10.1002/cssc.201000109
DO - 10.1002/cssc.201000109
M3 - 学術論文
C2 - 20715046
AN - SCOPUS:77958575677
SN - 1864-5631
VL - 3
SP - 1192
EP - 1199
JO - ChemSusChem
JF - ChemSusChem
IS - 10
ER -