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首页> 外文期刊>Applied thermal engineering: Design, processes, equipment, economics >CFD simulation of reactor furnace of sulfur recovery units by considering kinetics of acid gas (H2S and CO2) destruction
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CFD simulation of reactor furnace of sulfur recovery units by considering kinetics of acid gas (H2S and CO2) destruction

机译:考虑酸性气体(H2S和CO2)破坏的动力学,CFD仿真硫恢复装置的仿真

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摘要

In the present study, a 3D model of the industrial thermal reactor furnace of sulfur recovery units (SRUs) was simulated using the commercial CFD code ANSYS-FLUENT. The RNG-k-epsilon turbulence model and the eddy-dissipation-concept for taking into account the interactions of chemical reactions and turbulent flow were used in the computational model. The radiative transport was analyzed using the discrete ordinates method. Detailed reaction mechanisms were introduced in the CFD model for providing accurate predictions of combustion and the resulting species concentrations. The furnace geometry that was identical to those used in the industry was simulated. The predicted species composition distribution, temperature distribution, and absolute pressure, were in close good agreement with the corresponding measured data. Relative errors between the CFD results and the industrial data in terms of H2S conversion and overall efficiency were, respectively, 0.081% and 0.56%. New aspects of influence of geometric parameters such as burner, choke ring, and checker wall on the hydrodynamics and thermal behavior of the reactor furnace were also discussed. (C) 2017 Elsevier Ltd. All rights reserved.
机译:在本研究中,使用商业CFD码ANSYS流畅的模拟硫回收单元(SRU)的工业热反应器炉的3D模型。用于考虑化学反应和湍流的相互作用的RNG-K-epsilon湍流模型和涡流耗散概念在计算模型中使用。使用离散坐标方法分析辐射传输。在CFD模型中引入了详细的反应机制,用于提供精确的燃烧预测和所得物种浓度。模拟了与该行业中使用的炉几何形状相同。预测物种组成分布,温度分布和绝对压力与相应的测量数据密切良好。 CFD结果与产业数据之间的相对误差分别为H2S转化和整体效率,0.081%和0.56%。还讨论了几何参数影响的新方面,例如燃烧器,扼流圈和检查器壁对反应器炉的流体动力学和热行为的影响。 (c)2017 Elsevier Ltd.保留所有权利。

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