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Numerical simulation of coal gasification in OMB coal gasifier

机译:OMB煤气化炉煤气化的数值模拟。

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A comprehensive model was used to simulate the multiphase reaction flow in entrained flow gasifier in this paper.The model of computation was based on gas-phase Eulerian balance equations and the realizable k-ε turbulence modelwas applied to close the Reynolds-averaged Navier-Stokes equation.The particle phase was described by Lagrangianequation of motion. The eddy-dissipation-concept model and unreacted-core shrinking model were used to simulate thehomogeneous and heterogeneous reactions. The P1 radiation model was adopt to model the radioactive heat transfer ingasifier. The results show that the simulated carbon conversion, outlet gas concentration and temperature were agreedwith the industrial performance data. The two phases flow field, temperature and species concentration distributions ingasifier were illustrated. The influences of gasifier pressure and O_2/Coal ratio on gasification performance werediscussed.
机译:本文采用综合模型模拟了气流床气化炉中的多相反应流。 计算模型基于气相欧拉平衡方程和可实现的k-ε湍流模型 用雷诺兹平均Navier-Stokes方程关闭。粒子相由拉格朗日描述 运动方程。利用涡耗散概念模型和未反应堆芯收缩模型对模型进行了模拟。 均相和异质反应。采用P1辐射模型模拟了大气中的放射性传热。 气化炉。结果表明,模拟的碳转化率,出口气体浓度和温度是一致的 与工业性能数据。两相流场,温度和物种浓度分布。 图示了气化炉。气化炉压力和O_2 /煤比对气化性能的影响为 讨论过。

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