Novel propane-free mixed refrigerant integrated with nitrogen expansion natural gas liquefaction process for offshore units

被引:21
作者
Jin, Chunhe [1 ,2 ]
Yuan, Yilong [1 ,2 ]
Son, Heechang [3 ]
Lim, Youngsub [3 ]
机构
[1] Jilin Univ, Key Lab Groundwater Resources & Environm, Minist Educ, Changchun 130021, Peoples R China
[2] Jilin Univ, Jilin Prov Key Lab Water Resources & Environm, Changchun 130021, Peoples R China
[3] Seoul Natl Univ, Coll Engn, Dept Naval Architecture & Ocean Engn, 1 Gwanak Ro, Seoul 08826, South Korea
关键词
Liquefaction process; Mixed refrigerant; Nitrogen expander; Energy consumption; Exergy analysis; ENERGY-EFFICIENT; DUAL EXPANDER; LNG PROCESSES; OPTIMIZATION; SINGLE; CYCLE; ENHANCEMENT; EXERGY; DESIGN; PERFORMANCE;
D O I
10.1016/j.energy.2021.121765
中图分类号
O414.1 [热力学];
学科分类号
摘要
The presence of propane inventory in offshore liquefaction processes increases the concerns for platform safety. To address this, we propose a novel liquefaction process that integrates propane-free mixed refrigerant and nitrogen expander cycles (MR-N-2). The proposed design adopts the advantages of both nitrogen expander and single mixed refrigerant (SMR) processes. The process was rigorously simulated using Aspen HYSYS, and the specific energy consumption was optimized as an objective function using the genetic algorithm technique. Additionally, the MR-N-2 process was investigated using exergy and sensitivity analyses to compare the obtained results with those of the previous studies. The results verify that both liquefaction and exergy efficiencies are improved by 27.15% and 14.92%, respectively, in comparison with those of the base case. Moreover, the MR-N-2 process exhibits enhanced energy efficiency compared to that of the various existing nitrogen expander-based processes. The energy savings of the proposed method varies between 3.2% and 61.7%, and the cycle capacity is 22.43% better than that of the SMR process. (C) 2021 Elsevier Ltd. All rights reserved.
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页数:12
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