Highly effective gasoline synthesis from carbon dioxide

被引:10
作者
Inui, T
Hara, H
Takeguchi, T
Ichino, K
Kim, JB
Iwamoto, S
Pu, SB
机构
关键词
gasoline synthesis; CO2-rich syngas; methanol synthesis; syngas synthesis; methane reforming; CO2-reforming; on-site heat supply; serially connected reactor; one-pass operation; metallosilicate;
D O I
10.1016/S0196-8904(96)00299-3
中图分类号
O414.1 [热力学];
学科分类号
摘要
Effective catalytic conversion of CO2 into gasoline was investigated by one-pass operation using a serially connected flow-type reactor. Rapid CO2-reforming of methane into syngas was conducted by a newly developed Rh-modified Ni-Ce2O3-Pt catalyst at a low furnace-temperature around 400-500 degrees C. A high methane conversion was achieved by an in-situ heat supply due to catalytic combustion of added ethane or propane which is more combustible with higher combustion heat than methane. Thus obtained syngas or a CO2-enriched syngas was then converted into methanol on a novel highly active methanol synthesis catalyst, composed of Pd-modified Cu-Zn-Cr-Ga-Al mixed oxides, and the methanol produced was introduced to the successive reactor packed with a metallosilicate catalyst having MFI structure, and totally converted into gasoline with a high space-time yield and selectivity. (C) 1997 Elsevier Science Ltd.
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收藏
页码:S385 / S390
页数:6
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