主催: 一般社団法人 日本エネルギー学会 石炭科学部会, 一般社団法人 日本エネルギー学会 コークス工学研究部会
共催: 九州大学炭素資源国際教育研究センター, 化学工学会 エネルギー部会, 日本エネルギー学会 重質油部会, エネルギー学部会
会議名: 第50回石炭科学会議 第12回日中石炭・C1化学シンポジウム
回次: 50
開催地: 九州大学医学部 百年講堂
開催日: 2013/10/28 - 2013/10/31
p. 62-63
This study focuses on the syngas production by partial oxidation of coke oven gas (COG). The reforming of COG, which is a multi-component mixture, in a turbulent flow includes various complex processes. Previous studies were limited to the results using simulated gas with a laboratory scale small reactor and a laminar flow. In this study, we developed a model which considers both chemical reactions and fluid dynamics for simulating the reforming characteristics of the actual COG in a bench scale relatively large reactor. The detailed chemical kinetic model which consists of more than 2000 elementary reactions and 257 species was reduced to 410 reactions and 47 sepcies for realizing coupling a finite rate reaction model with the turbulence model. Numerical simulations could fairly reproduce the reformed gas compositions and temperature profiles in a reformer.
