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Coupled Simulation of the Flue Gas and Process Gas Side of a Steam Cracker Convection Section

机译:蒸汽裂化器对流段烟气和工艺气侧的耦合模拟

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A coupled simulation of the flue gas and process gas side of the convection section of a steam cracker is performed, making use of the CFD software package Fluent. A detailed overview of the operating mode of the different heat exchangers suspended in the convection section is obtained. The asymmetric inlet flow field of the flue gas in the convection section, and the radiation from the convection section walls leads to large differences in outlet temperatures of the tubes located in the same row. The flow fields and temperature fields in the tubes of a single heat exchanger differ significantly with e.g., outlet temperatures of the hydrocarbon-steam mixture ranging from 820 K to 852 K. Moreover, the simulations reveal the presence of hot spots on the lowest tube row, possibly causing fouling.
机译:利用CFD软件包Fluent,对蒸汽裂化器对流段的烟气和工艺气体侧进行了耦合模拟。获得了对流部分中悬挂的不同热交换器的运行模式的详细概述。对流段中烟气的入口流场不对称,对流段壁的辐射导致位于同一排中的管道出口温度差异很大。单个热交换器的管中的流场和温度场明显不同,例如碳氢化合物-蒸汽混合物的出口温度范围为820 K至852K。此外,模拟显示最低的管排上存在热点,可能导致结垢。

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