Low-temperature thermal performance of propane condenser for recovering LNG cryogenic energy

被引:1
作者
Xu, Huijin [1 ]
Luo, Xuan [1 ]
Huang, Shanbo [1 ]
Gong, Liang [1 ]
机构
[1] College of Pipeline and Civil Engineering in China University of Petroleum, Qingdao
来源
Zhongguo Shiyou Daxue Xuebao (Ziran Kexue Ban)/Journal of China University of Petroleum (Edition of Natural Science) | 2015年 / 39卷 / 04期
关键词
Gasification; Heat transfer; Natural gas; Optimization design; Supercritical fluid;
D O I
10.3969/j.issn.1673-5005.2015.04.019
中图分类号
学科分类号
摘要
Using propane to recover LNG cold energy is an effective way to avoid the problem of heat transfer with large temperature difference. The heat transfer between supercritical LNG and propane in the condenser was theoretically investigated, which is significant for the utilization of LNG cold energy. According to the propane state, LNG-propane heat transfer area can be divided into overheating region, two-phase region and sub-cooling liquid region. By means of parameter analysis method, the effects of some main parameters (propane inlet temperature, condenser size, propane flow rate) on the overall heat transfer performance of condenser were discussed. The results show that properly increasing LNG mass flow rate and decreasing channel width are beneficial to the recovery of LNG cold energy, while the effect of inlet temperature of propane gas on the recovery of LNG cold energy turns out to be little. The approaches that can improve the condenser effectiveness include determining the optimal propane inlet temperature, properly decreasing the propane mass flow rate and decreasing the width of propane-side channel. ©, 2015, Zhongguo Shiyou Daxue Xuebao (Ziran Kexue Ban)/Journal of China University of Petroleum (Edition of Natural Science). All right reserved.
引用
收藏
页码:140 / 146
页数:6
相关论文
共 25 条
[1]  
Rocca V.L., Cold recovery during regasification of LNG part one: cold utilization far from the regasification facility, Energy, 35, pp. 2049-2058, (2010)
[2]  
Rocca V.L., Cold recovery during regasification of LNG part two: applications in an agro food industry and a hypermarket, Energy, 36, pp. 4897-4908, (2011)
[3]  
Tsatsaronis G., Morosuk T., Advanced exergetic analysis of a novel system for generating electricity and vaporizing liquefied natural gas, Energy, 35, pp. 820-829, (2010)
[4]  
Liu Y.N., Guo K.H., Efficiency of power generation by LNG cold energy, Power and Energy Engineering Conference, (2010)
[5]  
Disenza C., Disenza G., Rocca V.L., Et al., Exergy recovery during LNG regasification: electric energy production-part one, Applied Thermal Engineering, 29, pp. 380-387, (2009)
[6]  
Liu Y.N., Guo K.H., A novel cryogenic power cycle for LNG cold energy recovery, Energy, 36, pp. 2828-2833, (2011)
[7]  
Miyazaki T., Kang Y.T., Akisawa A., Et al., A combined power cycle using refuse incineration and LNG cold energy, Energy, 25, pp. 639-655, (2000)
[8]  
Zhang N., Lior N., A novel near-zero CO<sub>2</sub> emission thermal cycle with LNG cryogenic exergy utilization, Energy, 31, pp. 1666-1679, (2006)
[9]  
Zhang N., Lior N., Liu M., Et al., COOLCEP (cool clean efficient power): A novel CO<sub>2</sub>-capturing oxy-fuel power system with LNG (liquefied natural gas) coldness energy utilization, Energy, 35, pp. 1200-1210, (2010)
[10]  
Shen Q.Q., Lin W.S., Gu A.Z., Et al., A simplified model of direct-contact heat transfer in desalination system utilizing LNG cold energy, Energy, 10, pp. 1-7, (2011)