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Impact of mixed refrigerant selection on energy and exergy performance of natural gas liquefaction processes

机译:混合制冷剂选择对天然气液化过程能量和漏洞性能的影响

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摘要

Selection of mixed refrigerant has a significant impact on the performance of the single mixed refrigerant process for natural gas liquefaction. However, current studies mainly focus on optimizing the fraction of the mixed refrigerant with pre-fixed components which cannot guarantee the optimal solution. To address this issue, a simulation-based optimization methodology was proposed for simultaneously determining the components and their respective fractions in a mixed refrigerant. The methodology selected the optimal mixed refrigerant components from a database of the potential refrigerants with different objective functions. Then, four case studies of mixed refrigerants with three, four, five, and six components were optimized to determine their optimal combination of components and the fraction of each component by minimizing the specific energy consumption. Subsequently, the energetic and exergetic analyses were conducted to reveal the relationships between the mixed refrigerant components and the process performance. The results showed that the minimum specific energy consumption for the mixed refrigerant comprising three, four, five and six components was 0.721 (A3), 0.403 (B10), 0.392 (C10) and 0.343 (D14) kWh/kg respectively. The specific energy consumption declined drastically by 44.11% in moving from three (A3) to four (B10) components, with a less pronounced decrease of 14.9% in moving from four (B10) to six (D14) components. Moreover, the exergy efficiency of A3, B10, C10, and D14 was 36.74, 55.39, 56.44, and 61.66%, respectively. The results indicated that the energetic and exergetic efficiencies were severely influenced by the selection of components for the mixed refrigerant. Therefore, the proposed methodology provides a viable method of simultaneously determining the refrigerant components and fractions for mixed refrigerant-based processes to achieve the minimum specific energy consumption and maximum exergy efficiency.
机译:混合制冷剂的选择对单一混合制冷剂工艺进行了显着影响,用于天然气液化。然而,目前的研究主要集中在优化混合制冷剂的分数与预固定组件,不能保证最佳溶液。为了解决这个问题,提出了一种用于同时确定混合制冷剂中的组分及其各自的级分的模拟的优化方法。该方法从具有不同目标功能的潜在制冷剂的数据库中选择了最佳混合制冷剂组件。然后,通过最小化特定能量消耗,优化了具有三个,四个,五个和六种组分的混合制冷剂的四个案例研究,以确定其组分的最佳组合和各组分的一部分。随后,进行了能量和前进分析,揭示了混合制冷剂组分与工艺性能之间的关系。结果表明,包含三个,四个,五个和六种组分的混合制冷剂的最小特定能耗分别为0.721(A3),0.403(B10),0.392(C10)和0.343(D14)KW / kg。从三(a3)至四个(b10)组分移动,从三(a3)到四个(b10)组分移动时,特定能耗急剧下降了44.11%,从四(b10)至六(d14)组分移动不太明显的降低14.9%。此外,A3,B10,C10和D14的出电效率分别为36.74,55.39,56.44和61.66%。结果表明,通过选择混合制冷剂的组件,精力充沛和举射效率严重影响。因此,所提出的方法提供了一种可行的方法,同时确定用于混合制冷剂的过程的制冷剂组分和馏分,以实现最小的特定能量消耗和最大的高度效率。

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  • 来源
    《Energy》 |2020年第may15期|117378.1-117378.17|共17页
  • 作者单位

    Department of Gas Engineering College of Pipeline and Civil Engineering China University of Petroleum (East China) Qingdao China;

    Department of Gas Engineering College of Pipeline and Civil Engineering China University of Petroleum (East China) Qingdao China;

    Department of Chemical and Biomolecular Engineering National University of Singapore 4 Engieering Drive 4 Singapore 118575 Singapore;

    School of Chemical Engineering Yeungnam University Gyeongsan 712-749 Republic of Korea;

    School of Chemical Engineering Yeungnam University Gyeongsan 712-749 Republic of Korea;

    Department of Chemical and Environmental Engineering University of New Brunswick 15 Dineen Drive E3B 5A3 Frederiction Canada;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    LNG; Mixed refrigerant selection; Single mixed refrigerant liquefaction process; Optimization; Energy consumption; Natural gas;

    机译:LNG;混合制冷剂选择;单混合制冷剂液化过程;优化;能源消耗;天然气;

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