姜洪涛; 李会泉; 张懿
Source Publication化学进展
AbstractTri-reforming of methane is a novel process of methane reforming by carbon dioxide, steam, and oxygen simultaneously in one reactor. Tri-reforming of methane can not only produce synthesis gas with H-2/CO ratio of 1.5-2.0 but also mitigate or eliminate coke deposition of catalyst. It is fit for producing synthesis gas which can be used for production of chemicals (such as methanol and dimethyl ether), and ultra-clean fuels (such as liquid hydrocarbons) at lower cost than current process of steam reforming of methane. In this paper, the progress in tri-reforming of methane to synthesis gas is reviewed, including thermodynamics, catalyst development, reactor and kinetic behavior. We also point out the favorable foreground of tri-reforming on synthetical utilization of flue gas, coal-bed methane and natural gas. In order to make the process of tri-reforming of methane to synthesis gas economically feasible, what still should be done are developing high-active and coke-resistant catalyst, improving reactor, and probing mechanism of reaction and kinetic behavior.
Document Type期刊论文
First Author Affilication中国科学院过程工程研究所
Recommended Citation
GB/T 7714
姜洪涛,李会泉,张懿. 甲烷三重整制合成气[J]. 化学进展,2006,18(10):1270.
APA 姜洪涛,李会泉,&张懿.(2006).甲烷三重整制合成气.化学进展,18(10),1270.
MLA 姜洪涛,et al."甲烷三重整制合成气".化学进展 18.10(2006):1270.
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