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超短接触反应器气固快分装置的数值模拟
  • 期刊名称:化工学报
  • 时间:0
  • 页码:623-628
  • 分类:TQ015[化学工程]
  • 作者机构:[1]清华大学化学工程系,北京市绿色反应工程与工艺重点实验室,北京100084
  • 相关基金:国家自然科学基金项目(20976091)
  • 相关项目:毫秒级超高温煤裂解制乙炔过程研究
中文摘要:

引言作为一种极端条件下操作的超短接触反应过程,等离子体裂解煤制乙炔过程是利用等离子体的高温高焓条件,实现煤中挥发分(甚至固定碳)向乙炔的转化,是一种极具发展前景的绿色煤化工技术。美国AVCO公司1980年完成了1MW级工业装置的实验;

英文摘要:

A gas-solids fast separator was studied for its potential application in the process of coal pyrolysis to acetylene in plasma.The CFD method was employed to simulate the flow behavior in the gas-solids fast separator based on the realizable k-ε turbulence model and the discrete particle model(DPM).The separation efficiency and residence time of gas phase in the gas-solids fast separator could be calculated.The numerical simulations were validated by the experimental results at a low velocity of the inlet gas(e.g.,4 m·s-1).With the increase of gas velocity at the inlet,the separation efficiency was increased,and the residence time of gas phase was reduced accordingly.The separation efficiency approached 100% when particle diameter was larger than 20 μm.When inlet velocity was 100 m·s-1,the mean residence time of gas phase was about 35 ms.To be noted,the performance of the gas-solids fast separator could be improved,for example by shortening the length of the separator,with a reduced residence time of gas phase at ~20 ms.It is expected that the gas-solids fast separator can meet the stringent demand of the coal pyrolysis to acetylene process for the milliseconds reaction,quench and separation.

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