HYDROGEN PRODUCTION BY A STEAM REFORMING REACTOR FOR HEAVY HYDROCARBONS

被引:0
|
作者
Fujimoto, Yasutaka [1 ]
Shinoki, Toshio [2 ]
Tanigawa, Hirochika [3 ]
Funaki, Jiro [1 ]
Hirata, Katsuya [1 ]
机构
[1] Doshisha Univ, Dept Mech Engn, Kyoto 602, Japan
[2] Mitsubishi Elect Corp Amagasaki, Amagasaki, Japan
[3] Maizuru Natl Coll Technol Maizuru, Maizuru, Japan
关键词
KEROSENE; CATALYST;
D O I
暂无
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The authors develop a small and simple steam-reforming reactor in a home-use size for n-dodecane as a heavy-hydrocarbons fuel. Under the thermal condition controlled by electric heaters and a gas burner with a thermal diffuser, the authors measure the inside-temperature profile and the hydrogen-molecule ratio (concentration) R-H2, together with the molecule ratios R-CH4, R-CO and R-CO2 of other main gas components such as CH4, CO and CO2, respectively. Besides, the authors conduct numerical simulations based on a thermal-equilibrium theory, in addition to experiments. As a result, the authors successfully achieve suitable inside-temperature profiles. And, the effects of the liquid-hourly-space velocity LHSV upon R-H2, R-CH4, R-CO and R-CO2 are shown, experimentally. For LHSV <= 1, the experimental results agree well with the thermal equilibrium theory. This is in consistent with high conversion ratio X-C12H26 -greater than or similar to 80 %. Furthermore, the authors reveal the effects of the temperature T inside the reactor upon the molecule ratios, comparing with the thermal-equilibrium theory.
引用
收藏
页码:161 / +
页数:3
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