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Numerical simulation of flow and gasification characteristics with different swirl vane angles in a 2000 t/d GSP gasifier

机译:2000 T / D GSP气化器不同旋流叶片角度的流动和气化特性的数值模拟

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摘要

A 2000 t/d GSP entrained flow pulverized coal gasifier suffered problems of high temperature corrosion to burners and cooling screens. The simulation of the flow and gasification characteristics was conducted to find the cause. The cold-flow experiments in a 1:3.5 scale model gasifier and mimic simulation were carried out to verify the numerical methods. Then through the full-scale thermal simulation, the simulation results showed favorable agreement with the previous results in the literatures. The combustion reaction for pulverized coal occurred mainly in the jet region, while the coal gasification reaction was dominant in the gasification chamber. As the swirl vane angle increased from 0 degrees to 36 degrees, the expansion angle of the flame increased gradually, and the radial distance from the jet region to the wall decreased; the hot gas in the jet region was more concentrated and close to the burner. These aggravated the high temperature corrosion to the cooling screen and the burner. When the swirl vane angle was 26 degrees, the molar fraction of the syngas (CO + H-2) and carbon conversion rate reached the peak values of 96.2% and 98.1%, respectively.
机译:2000 T / D GSP夹带流粉碎煤气化煤气化器对燃烧器和冷却屏幕的高温腐蚀问题遭受了高温腐蚀。进行了流动和气化特性的模拟以找到原因。进行1:3.5规模模型气化器和模拟模拟中的冷流实验,以验证数值方法。然后通过满量程的热仿真,仿真结果表明,与先前的文献中的结果表现出有利一致。煤粉的燃烧反应主要发生在喷射区域,而煤气化反应在气化室中占主导地位。随着旋流叶片角度从0度增加到36度,火焰的膨胀角逐渐增加,并且从喷射区域到壁的径向距离减小;喷射区域中的热气体更浓缩并靠近燃烧器。这些加剧了冷却筛和燃烧器的高温腐蚀。当旋流叶片角度为26度时,合成气(CO + H-2)和碳转化率的摩尔分别分别达到96.2%和98.1%的峰值。

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