A numerical investigation on LNG flow and heat transfer characteristic in heat exchanger

被引:21
作者
Afrianto, Handry [1 ]
Tanshen, Md Riyad [1 ]
Munkhbayar, B. [1 ,2 ]
Suryo, U. Tony [3 ]
Chung, Hanshik [1 ]
Jeong, Hyomin [1 ]
机构
[1] Gyeongsang Natl Univ, Dept Energy & Mech Engn, Tongyeong 650160, Gyeongnam, South Korea
[2] Univ Adelaide, Sch Chem Engn, Adelaide, SA 5005, Australia
[3] Diponegoro Univ, Dept Mech Engn, Semarang, Indonesia
关键词
CFD; LNG heat transfer; 1-2 Shell and tube exchanger; Buoyancy effect;
D O I
10.1016/j.ijheatmasstransfer.2013.09.036
中图分类号
O414.1 [热力学];
学科分类号
摘要
The current article reports a numerical study on liquid natural gas (LNG) flow and heat transfer characteristic in heat exchanger at 0.6 MPa pressure condition. The computational fluid dynamics (CFD) code FLUENT was used to simulate the fluids flow and heat transfer characteristic in heat exchanger. The three-dimensional model of 1-2 heat exchangers was used to perform the numerical simulation. The numerical simulation of the current study was validated and compared with a reference data, indicating effectiveness-NTU and LMTD method. Therefore, the properties of LNG were calculated from NIST standard database 4 (SUPERTRAPP) versions 3.2. The variation effects of mass flow rate and heat transfer characteristic of the fluids were investigated. The numerical results show that the heat transfer coefficient increases with increasing the mass flow rate. Furthermore, the optimization of mass flow rate of fluids for vaporization process was reported in this study. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:110 / 118
页数:9
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