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CFD modelling of CO_2 enhanced gasification of coal in a pressurized circulating fluidized bed reactor

机译:加压循环流化床反应器中CO_2强化煤气化的CFD模型

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Two CFD models of CO2-enhanced coal gasification in pressurized circulating fluidized bed reactor were developed and applied to simulate the process and predict syngas composition at the reactor outlet. The models were developed using commercial codes ANSYS Fluent and CPFD Barracuda. The models allowed to predict the outlet syngas composition and give insight into the processes occurring in the reactor. Results of the analyses were compared with experimental data obtained from a small scale test facility. The predicted syngas compositions agreed well with the experimental data, however the local gas composition in some instances were different. The predicted temperature distribution in Fluent agreed well with the experimental data. The examined cases confirmed that addition of CO2 to the gasifying agent in a pressurized reactor can increase the CO yield per unit of feedstock and reduce the oxygen demand. (C) 2018 Elsevier Ltd. All rights reserved.
机译:建立了两个在加压循环流化床反应器中CO2强化煤气化的CFD模型,并将其用于模拟过程并预测反应器出口处的合成气组成。这些模型是使用商业代码ANSYS Fluent和CPFD Barracuda开发的。该模型可以预测出口合成气的组成,并深入了解反应器中发生的过程。将分析结果与从小型测试机构获得的实验数据进行比较。预测的合成气成分与实验数据非常吻合,但是在某些情况下局部气体成分不同。 Fluent中的预测温度分布与实验数据非常吻合。检查的情况证实,在加压反应器中向气化剂中添加CO2可以提高每单位原料的CO收率并减少氧气需求。 (C)2018 Elsevier Ltd.保留所有权利。

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