Synthesis of methanol and isobutanol from syngas over ZrO2-based catalysts

被引:16
作者
Cai, YN [1 ]
Niu, YQ [1 ]
Chen, ZG [1 ]
机构
[1] CHINESE ACAD SCI,INST COAL CHEM,TAIYUAN SHAXI 030001,PEOPLES R CHINA
关键词
methanol; isobutanol; syngas; ZrO2-based catalysts;
D O I
10.1016/S0378-3820(96)01060-0
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The effects of reaction conditions on the synthesis of isobutanol and methanol from syngas over Zr-K and Zr-Mn-K catalysts have been investigated, with the reactions carried out at pressures between 8 and 16 MPa, temperatures between 380 and 440 degrees C, and gas hourly space velocity (GHSV) between 3000 and 8000 h(-1). It was Found that the Zr-K catalyst exhibited the highest activity and selectivity at 420 degrees C, 10.0 MPa, and 5000 h(-1), and that the Mn-promoted catalyst increased the yield of isobutanol with the corresponding optimum temperature being 400 degrees C. Moreover, the higher pressure and GHSV favored isobutanol synthesis. At 16, 0 MPa, 400 OC, 5000 h(-1), the space time yield of isobutanol was about 21.5 mi per mi cat. h(-1), and selectivity reached 98% over the Zr-Mn-K catalyst. (C) 1997 Elsevier Science B.V.
引用
收藏
页码:163 / 170
页数:8
相关论文
共 9 条
[1]  
Cai Y, 1996, J FUEL CHEM TECHNOL, V24, P11
[2]  
CAI YN, 1995, J NATURAL GAS CHEM, V20, P18
[3]  
FEELEY OC, 1992, AM CHEM SOC DIV FUEL, V37, P1817
[5]  
KEN WO, 1993, OIL GAS J, V1, P11
[6]   SELECTIVE FORMATION OF ISO-BUTENE FROM CARBON-MONOXIDE AND HYDROGEN OVER ZIRCONIUM-OXIDE CATALYST [J].
MAEHASHI, T ;
MARUYA, K ;
DOMEN, K ;
AIKA, K ;
ONISHI, T .
CHEMISTRY LETTERS, 1984, (05) :747-748
[7]  
NIU YZ, 1988, J FUEL CHEM TECHNOL, V16, P82
[8]  
ROPER M, 1987, 208102 EP
[9]   PRODUCTION OF BRANCHED-CHAIN HYDROCARBONS VIA ISOSYNTHESIS [J].
SOFIANOS, A .
CATALYSIS TODAY, 1992, 15 (01) :149-175