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NUMERICAL SIMULATION OF COAL GASIFICATION IN A 1 T/H TWO-STAGE ENTRAINED FLOW GASIFIER

机译:1 T / H两级气流床气化炉中煤气化过程的数值模拟

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Coal gasification has received increasing attention in the past two decades due to the growing demand for clean gaseous fuels. Numerical simulations of the coal gasification process inside a two-stage dry feed entrained flow gasifier were carried out using the commercial CFD solver FLUENT. The predicted main product gas components and carbon conversion were in well agreement with the measured data, which verified the validity of the model. A series of calculations were carried out to investigate the effects of operating parameters on the performance of gasifier, including the coal particle size, coal type and coal feeding ratio between the first and the second stages. The flow field, coal particle deposition on the wall, gas temperature and mole fraction inside of the gasifier were analyzed. And the simulation results indicated that the performance of gasifier is improved with decreasing particle size. The low volatile component fraction or high ash content in coal is not propitious to the gasification performance. And the performance of gasifier of the case with coal distribution with 75% (first stage) vs. 25% (second stage) is better than the case with 50% (first stage) vs. 50% (second stage) and the case with 100% for the first stage. The calculation is helpful for designing the operating conditions of the gasifier.
机译:在过去的二十年中,由于对清洁气态燃料的需求不断增长,煤气化受到了越来越多的关注。使用商用CFD求解器FLUENT对两级干式进料气流床气化炉内的煤气化过程进行了数值模拟。预测的主要产品气体成分和碳转化率与实测数据吻合良好,验证了该模型的有效性。进行了一系列计算以研究操作参数对气化炉性能的影响,包括第一阶段和第二阶段之间的煤粒度,煤类型和给煤比。分析了流场,煤颗粒在壁上的沉积,气体温度和气化炉内部的摩尔分数。仿真结果表明,气化炉的性能随着粒径的减小而提高。煤中的挥发性组分含量低或灰分含量高不利于气化性能。配煤率分别为75%(第一阶段)与25%(第二阶段)的情况下的气化器性能优于50%(第一阶段)与50%(第二阶段)的情况下的气化炉性能。第一阶段为100%。该计算有助于设计气化炉的运行条件。

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