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。
A kinetic coal gasification model combining chemical equilibrium was developed to evaluate and optimize gasifying parameters in entrained flow bed gasification.
采用未反应核收缩模型对试验数据进行处理，得到气化反应动力学参数。
The test data were processed with a reactionless core-shrinking model to obtain the kinetic parameters of the gasification reaction.
本文对低温等离子体净化汽车尾气化学动力学模型进行了研究。
In this paper, the model of chemical kinetics for the automobile exhaust control using non-thermal plasma is carried out.
利用DAEM(分布活化能模型)研究了显微组分半焦的气化动力学。
The pyrolysis kinetics was analysed by using Distribution Activation Energy Model (DAEM).
与随机孔模型对比，发现正态分布时间模型能较好地描述煤焦的气化动力学规律。
It was found that the reaction rate submitted normal distribution with reaction time and a normal distribution model was proposed to fit the kinetics data.
为了研究分级和气化炉结构对气化效果的影响，结合对分级气化炉内流动、燃烧和气化反应的分析，采用小室模型建立了分级气化炉的动力学模型，考虑了气化炉结构尺寸对气化过程和结果的影响。
The flow and heat transfer of high temperature syngas and slag layer in entrained-flow coal gasifier were analyzed, and a model for slag flow and heat transfer on the internal wall was proposed.
为了研究分级和气化炉结构对气化效果的影响，结合对分级气化炉内流动、燃烧和气化反应的分析，采用小室模型建立了分级气化炉的动力学模型，考虑了气化炉结构尺寸对气化过程和结果的影响。
The flow and heat transfer of high temperature syngas and slag layer in entrained-flow coal gasifier were analyzed, and a model for slag flow and heat transfer on the internal wall was proposed.
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