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Experimental investigations on lignite char gasification kinetics using a pressurized drop tube reactor

机译:加压滴管式反应器对褐煤焦气化动力学的实验研究

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摘要

A novel pressurized drop tube test facility, named KIVAN, for the investigation of heterogeneous gasification reactions under elevated pressures is presented. Facility configuration and possibilities of experimental test procedures are explained. The gasification behavior of a lignite char is investigated at a pressure of 21 bar. The effects of gasification temperature (1173-1323 K) and partial pressure of CO2 (5.25-15.75 bar) on the carbon conversion are determined. The measured temperature and concentration profiles inside the reactor, the settling velocity of the particles and the flow conditions along the reaction tube are used to determine kinetic parameters of the Boudouard reaction. Data on the char structural changes depending on the carbon conversion is provided and it is suitable for detailed numerical modeling of gasification processes. The determined kinetic parameters of the Boudouard reaction under these conditions are: activation energy 162 kJ.mol(-1), reaction order 0.36 and pre-exponential factor 3.26.10(5) s(-1) bar(-036).
机译:提出了一种新颖的加压滴管测试设备,称为KIVAN,用于研究高压下的非均质气化反应。解释了设备配置和实验测试程序的可能性。在21 bar的压力下研究褐煤焦的气化行为。确定了气化温度(1173-1323 K)和CO2分压(5.25-15.75 bar)对碳转化率的影响。测量的反应器内部温度和浓度分布,颗粒的沉降速度以及沿反应管的流动条件用于确定Boudouard反应的动力学参数。提供了取决于碳转化率的焦炭结构变化的数据,它适用于气化过程的详细数值模拟。在这些条件下确定的Boudouard反应动力学参数为:活化能162 kJ.mol(-1),反应级数0.36和预指数因子3.26.10(5)s(-1)bar(-036)。

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