主催: 社団法人 日本エネルギー学会
共催: 化学工学会 エネルギー部会, 群馬大学工学部
後援: 桐生市, 群馬大学科学技術振興会
会議名: 第41回石炭科学会議
回次: 41
開催地: 桐生市市民文化会館 4Fスカイホール
開催日: 2004/11/25 - 2004/11/26
p. 75-76
Coal gasification in entrained bed type of gasifier is performed under high temperature (〜1400℃), high pressure (〜3MPa), and high heating rate of coal particles (〜10,000K/s). Then little is known on the pyrolysis and gasification behavior of coal in the entrained bed type of gasifier due to experimental difficulty. In this paper coal pyrolysis was performed using a pressurized drop tube furnace (PDTF) which can simulate the entrained bed gasifier very well. The pyrolysis behavior was examined in detail, and detailed characterization of the solid product was also performed. These examinations clarified that the pyrolysis behavior of coal in the entrained bed gasifier is significantly different from that under ambient pressure and slow heating rate.