Novel design of LNG (liquefied natural gas) reliquefaction process

被引:20
|
作者
Baek, S. [1 ]
Hwang, G. [1 ]
Lee, C. [1 ]
Jeong, S. [1 ]
Choi, D. [1 ,2 ]
机构
[1] Korea Adv Inst Sci & Technol, Dept Mech Engn, Cryogen Engn Lab, Taejon 305701, South Korea
[2] Daewoo Shipbldg & Marine Engn Co Ltd, Ship Plant Syst R&D Team, Koje 656714, Kyungnam, South Korea
关键词
LNG; Regasification; Reliquefaction; Heavy Hydrocarbon Removal process; ELECTRIC ENERGY-PRODUCTION; EXERGY RECOVERY; HEAT;
D O I
10.1016/j.enconman.2011.02.015
中图分类号
O414.1 [热力学];
学科分类号
摘要
This paper presents an investigation of novel LNG reliquefaction process where the cold exergy of subcooled LNG is utilized to recondense the vaporized light component of LNG after it is separated from the heavier component in a phase separator. The regeneration of cold exergy is especially effective as well as important in thermodynamic sense when a cryogenic process is involved. To verify the proposed idea, we performed an experimental study by facilitating liquid nitrogen apparatus to mock up the LNG reliquefaction process. Subcooled liquid nitrogen is produced for a commercial transportation container with a house-made atmospheric liquid nitrogen heat exchanger and then, having subooled degree of up to 19 K, it simulates the behavior of subcooled LNG in the lab-scale reliquefaction experiment Recondensation of the vaporized gas is possible by using the cold exergy of subcooled liquid in a properly fabricated heat exchanger. Effect of heat exchanger performance factor and degree of subcooling on recondensation portion has been discussed in this paper. It is concluded that utilizing pressurized subcooled liquid that is obtained by liquid pump can surely reduce the pumping power of the vaporized natural gas and save the overall energy expenditure in LNG reliquefaction process. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2807 / 2814
页数:8
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