放热反应
煤
煤气化
木材气体发生器
甲烷
废物管理
吸热过程
一氧化碳
工艺工程
催化作用
环境科学
过程(计算)
化学
工程类
吸附
计算机科学
有机化学
操作系统
作者
Robert L. Hirsch,John Gallagher,Richard R. Lessard,Robert D. Wesslhoft
出处
期刊:Science
[American Association for the Advancement of Science (AAAS)]
日期:1982-01-08
卷期号:215 (4529): 121-127
被引量:99
标识
DOI:10.1126/science.215.4529.121
摘要
Catalytic coal gasification is being developed as a more efficient and less costly approach to producing methane from coal. With a potassium catalyst all the reactions can take place at one temperature, so that endothermic and exothermic reactions can be integrated in a single reactor. A key aspect of the concept involves continuous recycling of product carbon monoxide and hydrogen to the gasifier following separation of methane. Development of the process has advanced steadily since the basic concept was proposed in 1971. A 23-day demonstration run was recently completed in a process development unit with a coal feed rate of 1 ton per day. The next major step in the program will be to design and construct a large pilot plant to bring the technology to commercial readiness in the late 1980's.
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