首页> 外文会议>International conference on coal science;ICCS '97 >Dynamic pore analysis of shock tube, grid reactor and entrained flow reactor experiments on char combustion and gasification
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Dynamic pore analysis of shock tube, grid reactor and entrained flow reactor experiments on char combustion and gasification

机译:焦炭燃烧和气化的激波管,格栅反应器和气流床反应器的动态孔分析

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Combustion and gasification reactivity measurements of a char of bituminous coal in a broad range of particle temperatures (1500-3000K.) are performed using a shock tube and a grid reactor facility. The partial pressure of a reactant was varied between 0-10 bar for the shock tube and 0-25 bar for the grid reactor. Oxygen, carbon dioxide and water vapour are used as reactants in the reactions of combustion and gasification. A computational model is developed to describe the reactions on and the dynamic growth of the internal and the external surface. The model was used to gain understanding of the interaction of chemical and leactant transport processes. Furthermore it is used to correlate the data acquired in the shock tube experiments with experimental data acquired with the entrained flow reactor of the International Flame Research Foundation (IFRF). The computational model succeeds to explain the change of the char reactivity as a function of time and the burnout without the use of non-physical fit parameters.
机译:使用激波管和格栅反应器设备,在很宽的颗粒温度范围内(1500-3000K。)对烟煤焦炭的燃烧和气化反应性进行了测量。对于激波管,反应物的分压在0-10 bar之间变化,而对于栅极反应器,在0-25 bar之间变化。氧气,二氧化碳和水蒸气在燃烧和气化反应中用作反应物。开发了一个计算模型来描述内部和外部表面的反应以及动态增长。该模型用于了解化学物质和主链运输过程之间的相互作用。此外,它还用于将在冲击管实验中获得的数据与在国际火焰研究基金会(IFRF)的夹带流动反应器中获得的实验数据相关联。该计算模型成功地解释了炭反应性随时间的变化和燃尽,而无需使用非物理拟合参数。

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