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Energy-use analysis and optimization for a continuous catalytic reforming unit

机译:连续催化重整装置的能耗分析与优化

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The continuous catalytic reforming unit consumes a large amount of energy in upgrading of naphtha to produce high-octane reformate,benzene-toluene-xylene and liquefied petroleum gas.To identify the potential of energy savings and then propose corresponding improvements to the process are crucial for better energy-use efficiency.In this paper,energy-use analysis and optimization to a domestic continuous catalytic reforming unit are performed by using three-link energy structural model as well as energy grade-heat load(ε-Q)diagram.The results show that poor design of the heat exchanger network(HEN)and inappropriate column operation are the bottlenecks of energy-use.Low-temperature cold streams are directly preheated by the high-temperature hot streams,and the large heat transfer temperature difference between them causes large exergy destruction.Moreover,repeated heating or cooling along the stream additionally introduces unreasonable exergy destruction.By using software PRO/II,the feeding temperature,fractionating columns pressure and the feed location are optimized for operation improvement.Overall,our optimized process decreases the energy requirement by about 7%as compared to that of the original unit,which suggests that the applied strategies are beneficial to the future design and operation of continuous catalytic reforming unites.
机译:连续催化重整装置在石脑油提质生产高辛烷值重整产品,苯-甲苯-二甲苯和液化石油气过程中会消耗大量能源。确定节能潜力并提出相应的工艺改进对本文通过三链能量结构模型以及能量等级-热负荷(ε-Q)图对家用连续催化重整装置进行了能耗分析和优化。结果表明,换热网络(HEN)的设计不良和柱操作不当是能源使用的瓶颈。低温冷流被高温热流直接预热,并且它们之间的较大的传热温差导致火用破坏很大。此外,沿流反复进行加热或冷却还会造成不合理的火用破坏。通过使用PRO / II软件,feedi优化了温度,分馏塔压力和进料位置,以改善操作。总体而言,与原始装置相比,我们优化的工艺使能源需求降低了约7%,这表明所采用的策略对将来的设计是有益的和连续催化重整装置的运行。

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