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Computational Fluid Dynamic design of steam cracking reactors: extrusion method for simulation of dynamic coke layer growth

机译:蒸汽裂解反应器的计算流体动力学设计:动态焦炭层生长模拟挤出方法

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Computational fluid dynamics (CFD) gas been successfully applied for the evaluation of the start-of-run performance of three-dimensional (3D) coil geometries in steam cracking reactors. However, as the most attractive characteristic of these 3D coil geometries is the potential extension of the run length, determining the full economic potential of a coil involves tracking its performance throughout the run and not only at start-of-run. In the case of 3D tubular geometries, the growth of the coke layer will generally not be uniform. Because of this, the reactor geometry will change in time, which will in turn influence the fluid dynamics, product yields and successive coke formation. To take this into account, the coke layer growth needs to be incorporated in the CFD simulations. In this work an algorithm based on dynamic meshing will be discussed for simulating coke formation on the 3D reactor geometry and tracking the geometry deformation caused by the growing coke layer. As a proof-of-concept, a Millisecond propane cracker was simulated over the first days of its run length for a bare tube and a classically applied finned reactor design. Future work also includes comparison with other industrially relevant 3D reactor geometries.
机译:计算流体动力学(CFD)气体已成功应用于评估蒸汽裂化反应器中的三维(3D)线圈几何形状的运行开始性能。然而,由于这些3D线圈几何形状的最具吸引力的特征是运行长度的潜在延伸,确定线圈的完全经济潜力涉及在整个运行过程中跟踪其性能,而不仅在开始时。在3D管状几何形状的情况下,焦炭层的生长通常不均匀。因此,反应器几何形状将随时间变化,这将反过来影响流体动力学,产品产量和连续的焦炭形成。要考虑到这一点,需要在CFD模拟中纳入焦炭层生长。在这作用中,将讨论基于动态网格化的算法,用于在3D反应器几何形状上模拟焦炭形成,并跟踪由生长焦炭层引起的几何形状变形。作为概念验证,在其运行长度的第一天模拟毫秒丙烷饼干,用于裸管和经典施加的翅片反应器设计。未来的工作还包括与其他工业相关的3D反应器几何形状的比较。

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