SONG Zhi-chun,BAO Wei-ren,CHANG Li-ping,LI Fan (Key Laboratory of Coal Science and Technology,Taiyuan University of Technology, Ministry of Education and Shanxi Province,Taiyuan 030024,China)Based on the process simulator-Aspen Plus software,the entrained-flow pulverized coal gasification process was simulated by Gibbs free energy minimization method,the flow arithmetic was improved also.The effects of oxygen-coal ratio,steam-coal ratio,pressure and pulverized coal particle size on the crude syngas composition, gasification temperature,cold gas efficiency,carbon conversion efficiency and productivity of CO+H_2 were studied.The results show that the simulation and the experiment results fit well.Oxygen-coal ratio is one of the most important conditions for gasification process,which is more significant than the other conditions,and the best oxygen-coal ratio is 0.70~0.80 kg/kg for simulated coal.The best parameters corresponding gasification process are CO+H_2 volume fraction of 96.48%(dry base),cold gas efficiency of 83.56% and CO+H_2 yield of 1.74 m~3/kg coal.The gasification temperature is elevated about 40℃ when the oxygen-coal ratio is increased by 0.1kg/ kg and reduced about 8℃ when the stream-coal ratio is increased by 0.1 kg/kg.
2010 03 v.16;No.67 [Abstract][OnlineView][Download 748K]