期刊
FUEL PROCESSING TECHNOLOGY
卷 91, 期 8, 页码 951-957出版社
ELSEVIER SCIENCE BV
DOI: 10.1016/j.fuproc.2009.10.014
关键词
Ruthenium catalyst; Steam reforming; Polypropylene; Two-stage gasification
资金
- JSPS
- KOSEF under the Japan-Korea Basic Scientific Cooperation
- [19360435]
We studied fuel gas production by means of pyrolysis and steam reforming of waste plastics for applications in solid oxide fuel cells. More specifically, we evaluated the effects of pyrolytic gasification temperature, catalyst content, steam reforming temperature, and weight hourly space velocity for a Ru catalyst used in a 60 g h(-1)-scale continuous experimental apparatus, which consisted of a tank reactor for pyrolysis and a packed-bed catalytic reactor for steam reforming. Polypropylene (PP) pellets were used as a model waste plastic. Ru/gamma-Al2O3 catalysts with two different Ru contents were investigated. To suppress residue formation, the optimum operating temperature of the pyrolyzer was 673 K. To ensure suppressed coke formation, sufficient carbon conversion to gaseous products, and minimized heat loss from the reactor, the optimum operating conditions for the reformer were determined to be 903 K and 0.11 g-sample g-catalyst(-1) h(-1) with a 5 wt.% Ru/gamma-Al2O3 catalyst. The composition of the gas produced with the 5 wt.% catalyst was almost the same as that predicted by chemical equilibrium laws, and it was applicable for a direct hydrocarbon fuel cell. (C) 2009 Elsevier B.V. All rights reserved.
作者
我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。
推荐
暂无数据