A set of transparent cold model was designed for studying the movements of biomass particulate in horizontal entrained bed of the plasma heated biomass fast pyrolysis liquefaction prototype.
为了研究生物质颗粒在等离子体快速热解液化设备水平携带床热解管中的运动，设计制造了水平携带床冷态模拟装置。
The mean velocity and time passing the horizontal entrained bed of the particles and Argon gas were obtained and the difference between the granules and the gas movement in mean velocity was analyzed.
计算出了颗粒和氩气的平均速度以及流经水平携带床的时间，对颗粒与氩气的跟随性进行了分析。
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。
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。
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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