通过热交换器网络改造和可再生能源提高炼油厂的环境可持续性

Behrouz Raei, A. Ghannadzadeh
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引用次数: 2

摘要

本文介绍了一个基于火用诊断方法提高石油炼制过程中环境可持续性的案例研究。生命周期评估(LCA)指出原油生产和发电系统是环境不可持续性的主要来源。该工艺的现有热效用需求为78.4 MW,温差为40℃,其中现有设计的面积效率为0.7254。目标阶段将最低接近温度设定为18.96°C,从而确定了潜在节能的范围。建议的设计方案总能源需求为109,048 kW,与现有方案相同,但比目标高72,699 kW,需要38个交换器的17,873 m2面积。值得注意的是,这需要减少2914平方米的表面积,这表明该项目的实用性,只需对现有的交换装置进行有限的修改,如重新铺设管道。此外,为了进一步提高石油炼制过程的可持续性,通过各种场景评估了可再生能源等可能的解决方案;因此,根据ReCiPe,将环境影响从2.34E-06降低到2.27E-06,从而为可持续的石油炼制过程铺平了道路。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Environmental sustainability enhancement of a petroleum refinery through heat exchanger network retrofitting and renewable energy
This paper presents a case study on the enhancement of environmental sustainability in a petroleum refining process based on an exergetic diagnostic approach. The Life Cycle Assessment (LCA) pinpointed crude oil production and electricity generating systems as the main sources of environmental unsustainability. The existing hot utility demand of the process is 78.4 MW with a temperature difference of 40°C, where the area efficiency of the existing design is 0.7254. The targeting stage sets the minimum approach temperature at 18.96 °C, thereby establishing the scope for potential energy savings. The suggested design option with a total energy demand of 109,048 kW, the same as the existing one but 72,699 kW higher than the target, needs a 17,873 m2 area in 38 exchangers. Notably, this requires 2,914 m2 less surface area, suggesting the practicality of the project with a limited number of modifications such as the repiping of the existing exchanger units. Moreover, to enhance further the sustainability of the petroleum refining process, the possible solutions such as the renewables were evaluated through various scenarios; thus, resulting in a reduction in the environmental impacts from 2.34E-06 to 2.27E-06 according to ReCiPe, and thus paving the way towards a sustainable petroleum refining process.
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