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Energy and Exergy Optimization of Hydrocarbon Recovery (HCR) Plant Considering Potential Environmental Impact and Economics

机译:考虑潜在环境影响和经济学的烃恢复(HCR)植物能量和漏洞优化

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Process energy integration and continuous improvement of process technology are one of the increasing issues to ensure profitability of chemical productions. The energy conservation, process economics and environmental aspects are integrated at the early stage of the process development, the easier and less expensive to improve the process design. In this work different distillation process design alternatives have been considered with respect to evaluations of process economics and potential environmental impacts. The concept of exergy distribution has also been used as a tool to identify exergy loss profiles in each distillation unit. A multi-criteria decision making technique such as (Analytic Hierarchy Process) AHP is applied for ranking the alternatives. This method reveals that the heat pump distillation unit which has the highest score of 52% is the best alternative when compare with the base case. In terms of the effluent streams, the base case has a less potential environmental impact (PEI) compared to heat pump. The lower total PEI/kg (7.45E-01) of the base case illustrates that the material utilization efficiency of the base case is better than that of the heat pump which PEI/kg is 8.14E-01.
机译:工艺能量集成和持续改进过程技术是确保化学产品盈利能力的越来越多的问题之一。节能,工艺经济学和环境方面集成在过程开发的早期阶段,更容易,更便宜,以改善工艺设计。在这项工作中,已经考虑了不同蒸馏过程的设计替代方案,用于评估过程经济学和潜在的环境影响。漏洞分配的概念也被用作识别每个蒸馏装置中的漏洞损失型材的工具。应用诸如(分析层次处理)AHP的多标准决策技术,用于排名替代方案。该方法显示,当与基本情况相比,热泵蒸馏装置最高得分为52%是最佳替代方案。就流出物流而言,与热泵相比,基本情况具有较小的环境影响(PEI)。基础壳体的下总PEI / kg(7.45e-01)说明了基础壳体的材料利用效率优于PEI / kg为8.14e-01的热泵的利用效率。

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