首页> 外文会议>ASME joint US-European Fluids Engineering Division summer meeting >REACTING TURBULENT FLOW SIMULATION TO IMPROVE THE MIXING PROCESS IN AN OIL REFINERY INCINERATOR
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REACTING TURBULENT FLOW SIMULATION TO IMPROVE THE MIXING PROCESS IN AN OIL REFINERY INCINERATOR

机译:进行湍流模拟以改善炼油厂焚烧炉的混合过程

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Combustion emission is one of the most important issues in the design of industries. Todays' strict environmental standards have limited the productions of CO, NO_x, SO_x, and other hazardous pollutants from the related industries. In this work, we study a typical oil refinery incinerator, which is used to burn waste gases residue produced during bitumen production process. The waste gas mainly includes a mixture including N_2, H_2O-vapor, and O_2 species. Additionally, there are significant amounts of CO species and C_xH_y droplets in the waste gas composition. The measurements show that the CO emission becomes so crucial in high flow rate of feeding waste gas to the incinerator. Here, we numerically simulate the combustion process in this incinerator by solving the full turbulent reacting flow equations. In this regard, we use the finite-volume method to solve the RANS equations. For turbulence modeling purposes, we use the two-equation k-ε model along with standard wall functions. The non-premixed combustion is simulated by solving the mixture fraction equations for both fuel and waste gas streams. The interaction between turbulence and combustion is properly considered in the current modeling. We use the P_1 method to solve the radiation transfer equation in emitting and absorbing medium of combustion gasses. The WSGG model is used to consider the absorption coefficient variation. The set of governing equations are solved using a SMPLE-based algorithm. The current solutions provide good knowledge about the mixing pattern of flue gas and air-fuel streams in the incinerator. The improper mixing in the incinerator suggests we present a new design to re-design the waste gas inlet to the incinerator. Our simulation shows that the new design would result in substantial improvement in mixing process of these two streams. We find that this new design would effectively reduce the CO ppm at the exit of incinerator's stack.
机译:燃烧排放是工业设计中最重要的问题之一。当今严格的环境标准限制了相关行业的CO,NO_x,SO_x和其他有害污染物的生产。在这项工作中,我们研究了典型的炼油厂焚化炉,该焚化炉用于燃烧沥青生产过程中产生的废气残留物。废气主要包括由N_2,H_2O蒸气和O_2组成的混合物。另外,在废气成分中存在大量的CO物种和C_xH_y液滴。测量结果表明,CO排放对于将废气送入焚烧炉的高流量至关重要。在这里,我们通过求解完整的湍流反应流方程来数值模拟该焚烧炉中的燃烧过程。在这方面,我们使用有限体积法求解RANS方程。为了进行湍流建模,我们使用了两方程式k-ε模型以及标准壁函数。通过求解燃料和废气流的混合比方程,可以模拟非预混合燃烧。在当前模型中已适当考虑了湍流与燃烧之间的相互作用。我们使用P_1方法来求解燃烧气体的发射和吸收介质中的辐射传递方程。 WSGG模型用于考虑吸收系数的变化。使用基于SMPLE的算法求解控制方程组。当前的解决方案提供了有关焚烧炉中烟气和空气-燃料流混合模式的丰富知识。焚化炉中混合不当表明我们提出了一种重新设计焚化炉废气入口的新设计。我们的模拟表明,新设计将大大改善这两股物流的混合过程。我们发现,这种新设计将有效降低焚化炉烟囱出口处的CO ppm。

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