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Modification of Preheating Heat Exchanger Network in Crude Distillation Unit of Arak Refinery Based on Pinch Technology

机译:基于PINCH技术的ARAK炼油厂原油蒸馏装置预热热交换器网络的改变

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In this work, the Hint software that is based on methods of pinch technology was applied for design, optimizing and improving the integrated heat exchanger network of crude oil preheating Process in distillation unit in Arak refinery with the aim of heat load reduction in the furnace. In the first step, the data gathering of hot and cold streams in preheating section of distillation unit has been done and then by using Hint software, integrated heat exchanger network was designed with assumption of ΔT = 30k. Improving the existing heat - exchanger network has been done with respect to operating conditions and hydraulic limitation by considering the aim of least changes in the existing arrangement of exchangers, which is led to increasing of furnace inlet temperature up to 10.5°k and deceasing of heat duty of the distillation furnace about 9855 kw. The most important results in this project are: Decreasing of heat duty of distillation furnace to 9855 kw that leads to saving about 820000 US$ per year. Increasing the inlet temperature of the furnace up to 10.5°k. Decreasing the temperature of furnace tubes skin to 300°k. Decreasing the temperature of furnace flue gas to 290°k. Decreasing the greenhouse emission to 20000 tones per year.
机译:在这项工作中,应用了基于PINCH技术方法的提示软件,用于设计,优化和改进ARAK炼油厂蒸馏装置中原油预热过程的集成热交换器网络,其目的是炉子的热负荷减少。在第一步中,已经完成了在蒸馏单元的预热部分中的热和冷流的数据收集,然后通过使用提示软件,设计了集成的热交换器网络,其中设计了ΔT= 30k的假设。通过考虑现有的交换机排列的最小变化的目的,改善了现有的热交换器网络,这导致了炉内温度的增加,从而增加了10.5°K和热量的死亡蒸馏炉占9855 kW。该项目中最重要的结果是:将蒸馏炉的热义减少到9855千瓦,导致每年节省约820000美元。增加炉子的入口温度高达10.5°K。将炉子管皮肤的温度降低至300°K.将炉子烟气的温度降低至290°K。每年将温室排放减少到20000强调。

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