A dynamic model for FLNG spiral wound heat exchanger with multiple phase-change streams based on moving boundary method

被引:26
作者
Duan, Zhongdi [1 ]
Ren, Tao [1 ]
Ding, Guoliang [1 ]
Chen, Jie [2 ]
Pu, Hui [2 ]
机构
[1] Shanghai Jiao Tong Univ, Inst Refrigerat & Cryogen, Shanghai 200240, Peoples R China
[2] CNOOC Gas & Power Grp, R&D Ctr, Beijing 100007, Peoples R China
基金
国家高技术研究发展计划(863计划); 中国国家自然科学基金;
关键词
Dynamic model; Floating liquefied natural gas; Moving boundary; Multiple streams; Spiral wound heat exchanger; LOW-FREQUENCY OSCILLATIONS; LIQUEFIED NATURAL-GAS; PRESSURE-DROP; FRICTION FACTORS; LAMINAR-FLOW; PIPE-FLOW; SIMULATION; SYSTEM; LIQUEFACTION; PERFORMANCE;
D O I
10.1016/j.jngse.2016.07.036
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
For predicting the dynamic performance of spiral wound heat exchangers (SWHEs) applied in floating liquefied natural gas (FLNG) offshore platforms, a dynamic model reflecting the heat transfer among multiple phase-change streams in SWHEs is presented. In the dynamic model, a two-dimensional partitioned matrix is proposed to describe the heat transfer relations among phase-change streams in a general form; a group of generic equations based on the partitioned matrix is developed to calculate the heat capacities of phase-change streams, suitable for all types of phase zones (i.e. vapor, two-phase and liquid zones). An implicit iterative algorithm is proposed to solve the equations. The reliability and capability of the model has been partly validated by comparing the calculated steady-state performance with experimental data, and the dynamic performance under sloshing conditions are investigated, indicating that the sloshing-induced reduction of SWHE overall performance is within 5% for most cases. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:657 / 669
页数:13
相关论文
共 35 条
[1]  
Abidin M.Z.Z., 2011, 2011 NAT POSTGR C IE, P1, DOI [10.1109/NatPC.2011.6136278., DOI 10.1109/NATPC.2011.6136278]
[2]  
Bukowski J, 2011, INNOVATIONS NATURAL
[3]  
Bybee K, 2010, J PET TECHNOL, V62, P64, DOI DOI 10.2118/0710-0064-JPT
[4]  
Çarpinlioglu MÖ, 2001, FLOW MEAS INSTRUM, V12, P163, DOI 10.1016/S0955-5986(01)00020-6
[5]   Effect of multi-stream heat exchanger on performance of natural gas liquefaction with mixed refrigerant [J].
Chang, Ho-Myung ;
Lim, Hye Su ;
Choe, Kum Hyung .
CRYOGENICS, 2012, 52 (12) :642-647
[6]   Turbulent heat transfer in a tube fitted with serrated twist tape under rolling and pitching environments with applications to shipping machineries [J].
Chang, Shyy Woei ;
Liou, Tong-Miin ;
Liou, Jin Shuen ;
Chen, Kun-Tse .
OCEAN ENGINEERING, 2008, 35 (16) :1569-1577
[7]   Development of a dynamic model for a DX VAV air conditioning system [J].
Chen, Wu ;
Deng, Shiming .
ENERGY CONVERSION AND MANAGEMENT, 2006, 47 (18-19) :2900-2924
[8]   NUMERICAL-SOLUTIONS OF PULSATING FLOW AND HEAT-TRANSFER CHARACTERISTICS IN A PIPE [J].
CHO, HW ;
HYUN, JM .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 1990, 11 (04) :321-330
[9]   Review of natural gas hydrates as an energy resource: Prospects and challenges [J].
Chong, Zheng Rong ;
Yang, She Hern Bryan ;
Babu, Ponnivalavan ;
Linga, Praveen ;
Li, Xiao-Sen .
APPLIED ENERGY, 2016, 162 :1633-1652
[10]   Recent developments in simulation techniques for vapour-compression refrigeration systems [J].
Ding, Guo-liang .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 2007, 30 (07) :1119-1133