主催: 社団法人 日本エネルギー学会 石炭科学部会, 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: 化学工学会 エネルギー部会, 日本学術振興会 石炭・炭素資源利用技術第148委員会, 日本エネルギー学会 重質油部会
会議名: 第46回石炭科学会議
回次: 46
開催地: 鹿児島東急ホテル
開催日: 2009/11/26 - 2009/11/27
p. 88-89
In the air blown IGCC demonstration plant, a small scale air separation unit (ASU) is set up. Nitrogen from ASU is used for the transportation of coal and the char etc., and oxygen is mixed with air as a gasifying agent. From the viewpoint of a highly effective and stable operation of the gasifier, and improvement of plant efficiency in a commercial plant, in order to optimize the oxygen concentration of the gasifying agent, it is necessary to clarify the influence of the oxygen concentration in the gasifying agent on the gasification performance quantitatively. In this study, the influence of the oxygen concentration in the gasifying agent on the gasifier per pass performance was clarified by using a 3t/d bench scale coal gasifier. In addition, the gasification performance in the state of char-balance was estimated from the heat and mass balance of the gasifier. As a result, the influence of the oxygen concentration in the gasifying agent on the gasification performance (cold gas efficiency, char product rate, gas temperature in combustor, etc.) was able to be evaluated quantitatively.