A kinetic coal gasification model combining chemical equilibrium was developed to evaluate and optimize gasifying parameters in entrained flow bed gasification.
为评价和优化气流床煤气化中的气化方案和气化参数，从化学动力学角度并结合化学平衡，依据气流床特性建立了气化动力学模型。
Entrained-flow gasification of coal water slurry is the key technology of clean utilization of coal.
气流床水煤浆气化是煤高效、洁净利用的一项关键技术。
The advantages and disadvantages of fluidized bed, entrained flow bed and moving bed coal gasification technology and their current trends were analyzed.
分析了流化床、气流床和移动床煤气化工艺优缺点和煤气化工艺的发展趋势。
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