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Ethylene Furnace Modeling: an integrated approach

机译:乙烯炉建模:一种集成方法

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摘要

After more than fifty years of development the thermal cracking or pyrolysis of hydrocarbons has matured into the single most important process to produce ethylene. It is carried out inside tubular coils that are installed vertically in large fired heaters where the heat for the endothermic cracking reaction is supplied by a large number of hearth burners and/or wall burners. High heat fluxes are required to supply the heat for the endothermic reaction. Furthermore, the coils need to be operated at very high temperature to obtain reasonable conversions. Expensive Cr-Ni alloys have been developed that allow for metal temperatures over 1100℃. Historically, heaters have been designed using detailed process yield models with uniform temperature firebox models or simplified zonal firebox models. It was assumed that the burners themselves did not have a major impact upon the performance calculations and simply provided the heat.
机译:经过五十多年的发展,碳氢化合物的热裂解或热解已经发展成为生产乙烯的最重要的单一过程。它是在垂直安装在大型燃烧加热器中的管状盘管内进行的,在该加热器中,吸热裂化反应的热量由大量的炉膛燃烧器和/或壁式燃烧器提供。需要高热通量来为吸热反应提供热量。此外,线圈需要在非常高的温度下运行以获得合理的转换。已经开发出允许金属温度超过1100℃的昂贵Cr-Ni合金。从历史上看,加热器是使用详细的工艺产量模型,均匀温度燃烧室模型或简化的分区燃烧室模型进行设计的。假定燃烧器本身对性能计算没有重大影响,只是提供热量。

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