Research progress on the BOG recovery technologies used at LNG stations


[1] KUMAR S,KWON H T,CHOI K H,et al. LNG:An ecofriendly cryogenic fuel for sustainable development[J]. AppliedEnergy,2011,88(12):4264-4273.

[2] 王震,薛庆. 充分发挥天然气在我国现代能源体系构建中的主 力作用——对《天然气发展“十三·五”规划》的解读[J]. 天然气 工业,2017,37(3):1-8.WANG Z,XUE Q. To fully exert the important role of naturalgas in building a modern energy security system in China:Anunderstanding of China’s National 13th Five-Year Plan for NaturalGas Development[J]. Natural Gas Industry,2017,37(3):1-8.
[3] LEE S,JEON J,LEE U,et al. A novel dynamic modelingmethodology for boil-off gas recondensers in liquefied naturalgas terminals[J]. Journal of Chemical Engineering of Japan, 2015,48(10):841-847.
[4] KURLE Y M,WANG S,XU Q. Dynamic simulation of LNGloading,BOG generation,and BOG recovery at LNG exportingterminals[J]. Computers & Chemical Engineering,2017,97:47-58.
[5] United Nations Framework Convention on Climate Change.Kyoto protocol to the united nations framework conventionon climate change[J]. Review of European Community &International Environmental Law,1998,7(2):214-217.
[6] JEONG H,SHIM W J. Calculation of boil-off gas(BOG) generation of KC-1 membrane LNG tank with high density rigidpolyurethane foam by numerical analysis[J]. Polish MaritimeResearch,2017,24(1):100-114.
[7] 孙宪航,陈保东,张莉莉,等. 液化天然气 BOG 的计算方法与处 理工艺[J]. 油气储运,2012,31(12):931-933.SUN X H,CHEN B D,ZHANG L L,et al. BOG calculationmethod and processing technique of liquefified natural gas[J]. Oil &Gas Storage and Transportation,2012,31(12):931-933.
[8] CHEN Q S,WEGRZVN J,PRASAD V. Analysis of temperatureand pressure changes in liquefied natural gas(LNG)cryogenictanks[J]. Cryogenics,2004,44(10):701-709.
[9] 陈雪,李明. LNG 储罐内 BOG 动态模拟研究[J]. 油气储运, 2008,27(11):36-40.CHEN X,LI M. Dynamic simulation research on BOG in LNGtank[J]. Oil & Gas Storage and Transportation,2008,27(11):36-40.
[10] 吕寻贞,张磊,李亚军,等. LNG 接收站 BOG 蒸发量及波动性 分析[J]. 低温工程,2014(2):70-76.LYU X Z,ZHANG L,LI Y J,et al. BOG production andflfluctuation in LNG receiving terminal[J]. Cryogenics,2014(2): 70-76.
[11] 王武昌,李玉星,孙法峰,等. 大型 LNG 储罐内压力及蒸发率 的影响因素分析[J]. 天然气工业,2010,30(7):87-92.WANG W C,LI Y X,SUN F F,et al. Controlling factors ofinternal pressure and evaporation rate in a huge LNG storagetank[J]. Natural Gas Industry,2010,30(7):87-92.
[12] 李玉星,王武昌,乔国发,等. 密闭 LNG 储罐内的压力和蒸发 率[J]. 化工学报,2010,61(5):1241-1246.LI Y X,WANG W C,QIAO G F,et al. Pressure andevaporation rate in a closed LNG tank[J]. CIESC Journal, 2010,61(5):1241-1246.
[13] EBENEZER A,ISLAM S Z,JI X. Modelling of boil-off gasin LNG tanks:A case study[J]. International Journal ofEngineering & Technology,2010,2(4):292-296.
[14] HASAN M M F,ZHENG A M,KARIMI I A. Minimizingboil-off losses in liquefied natural gas transportation[J].Industrial & Engineering Chemistry Research,2009,48(21): 9571-9580.
[15] 李亚军,夏岩. LNG 接收站 BOG 蒸发量的影响因素及稳定 性[J]. 低温工程,2012(4):38-43.LI Y J,XIA Y. Influencing factors and stability of BOGgeneration in LNG receiving terminal[J]. Cryogenics,2012(4): 38-43.
[16] GORLA R S R. Probabilistic analysis of a liquefified natural gasstorage tank[J]. Applied Thermal Engineering,2010,30(17/18): 2763-2769.
[17] GAN Z H,FAN B Y,WU Y Z,et al. A two-stage stirling-typepulse tube cryocooler with a cold inertance tube[J]. Cryogenics, 2010,50(6/7):426-431.
[18] SCHUNK L O,PFOTENHAUER J M,NELLIS G F,et al.Inertance tube optimization for kW-class pulse tubes[J]. AIPConference Proceedings,2004,710(1):1269-1276.
[19] 王坤,巨永林. LNG 储运装置的小型 BOG 回收再液化方法的 对比分析[J]. 低温与超导,2017,45(9):22-25.WANG K,JU Y L. Comparison analysis between the BOG reliquefified methods of LNG storage and transportation equipment[J].Cryogenics and Superconductivity,2017,45(9):22-25.
[20] 祝铁军,张华,巨永林,等. LNG 加气站用小型撬装式 BOG再液化装置的研制开发[J]. 化工学报,2015,66(增刊 2): 325-331.ZHU T J,ZHANG H,JU Y L,et al. Small scale BOG reliquefaction system in skid-mounted in LNG fifilling station[J].CIESC Journal,2015,66(S2):325-331.
[21] HU J Y,CHEN S,ZHU J,et al. An efficient pulse tubecryocooler for boil-off gas reliquefaction in liquid natural gastanks[J]. Applied Energy,2016,164:1012-1018.
[22] 肖荣鸽,戴政,曹沙沙,等. LNG 站 BOG 处理技术对比研究[J].天然气化工,2019,44(3):80-83,97.XIAO R G,DAI Z,CAO S S,et al. Comparative study on BOGprocessing technology in LNG station[J]. Natural Gas ChemicalIndustry,2019,44(3):80-83,97.
[23] 谭建宇,王莉,李素燕,等. 双级氮膨胀天然气液化制冷循环流 程优化[J]. 哈尔滨工业大学学报,2006,38(3):370-373.TAN J Y,WANG L,LI S Y,et al. Optimization of natural gasliquefaction in the nitrogen two-expanders cycle[J]. Journal ofHarbin Institute of Technology,2006,38(3):370-373.
[24] POZIVIL J. Apparatus for reliquefying compressed vapour: DE60123143[P]. 2007-09-06.
[25] SHARAFIAN A,TALEBIAN H,BLOMERUS P,et al. Areview of liquefied natural gas refueling station designs[J].Renewable and Sustainable Energy Reviews,2017,69:503-513.
[26] KASPERSKI J,GIL B. Performance estimation of ejector cyclesusing heavier hydrocarbon refrigerants[J]. Applied ThermalEngineering,2014,71(1):197-203.
[27] MIERCIEW K,GAGAN J,BUTRYMOWICZ D,et al.Experimental investigations of solar driven ejector airconditioning system[J]. Energy & Buildings,2014,80:260-267.
[28] 赵金睿,王同吉,余道丞,等. 喷射引流式 BOG 回收装置的研 究[J]. 化工自动化及仪表,2017,44(9):873-877.ZHAO J R,WANG T J,YU D C,et al. Research of jet-inducedflow BOG recovery device[J]. Control and Instruments inChemical Industry,2017,44(9):873-877.
[29] SHIRAZI M M H,MOWLA D. Energy optimization forliquefaction process of natural gas in peak shaving plant[J].Energy, 2010,35(7):2878-2885.
[30] LEE S. Multi-parameter optimization of cold energy recoveryin cascade Rankine cycle for LNG regasification using geneticalgorithm[J]. Energy,2017,118:776-782.
[31] MEHRPOOYA M,SHAEIFZADEH M M M. A novelintegration of oxy-fuel cycle,high temperature solar cycle andLNG cold recovery-energy and exergy analysis[J]. AppliedThermal Engineering,2017,114:1090-1104.
[32] 鹿晓斌. BOG 回收处理工艺比选[J]. 天然气化工,2017,42(1): 93-97.LU X B. Comparison and selection of BOG recoveryprocesses[J]. Natural Gas Chemical Industry,2017,42(1): 93-97.
[33] 薛倩,刘名瑞,肖文涛,等. LNG 接收站 BOG 处理工艺优化及 功耗分析[J]. 油气储运,2016,35(4):376-380.XUE Q,LIU M R,XIAO W T,et al. Optimization and energyconsumption analysis of BOG treatment processes in LNGterminal[J]. Oil & Gas Storage and Transportation,2016,35(4): 376-380.
[34] SHIN M W,SHIN D,CHOI S H,et al. Optimization of theoperation of boil-off gas compressors at a liquifified natural gasgasification plant[J]. Industrial & Engineering ChemistryResearch,2007,46(20):6540-6545.
[35] SHIN M W,SHIN D,CHOI S H,et al. Optimal operationof the boil-off gas compression process using a boil-off ratemodel for LNG storage tanks[J]. Korean Journal of ChemicalEngineering,2008,25(1):7-12.
[36] 廖晓梦,张昀,伍婷. LNG 加气站 BOG 用于站内生活用气的 可行性探讨[J]. 石油与天然气化工,2016,45(5):43-45.LIAO X M,ZHANG Y,WU T. Discussion on the feasibilityof using BOG for life in a LNG filling station[J]. ChemicalEngineering of Oil and Gas,2016,45(5):43-45.
[37] KURLE Y M,WANG S,XU Q. Simulation study on boiloff gas minimization and recovery strategies at LNG exportingterminals[J]. Applied Energy,2015,156:628-641.
[38] DELAHUNTY T. System for reliquefying boil-off vapor fromliquefified gas:US3733838[P]. 1973-05-22.
[39] NEWTON C L. Apparatus and method for recovering liquefifiednatural gas vapor boiloff by reliquefying during startup orturndown:US4675037[P]. 1987-06-23.
[40] 李立婉,万宇飞. LNG 接收站 BOG 再冷凝工艺模拟及分析[J].现代化工,2014,34(6):129-132.LI L W,WAN Y F. Simulation and analysis on BOGrecondensation process of LNG receiving station[J]. ModernChemical Industry,2014,34(6):129-132.
[41] 杨志国,李亚军. 液化天然气接收站蒸发气体再冷凝工艺的优 化[J]. 化工学报,2009,60(11):2876-2881.YANG Z G,LI Y J. Optimization of boil-off gas recondensationprocess in LNG receiving terminal[J]. Journal of ChemicalIndustry and Engineering(China),2009,60(11):2876-2881.
[42] PARK C,SONG K,LEE S,et al. Retrofit design of a boiloff gas handling process in liquefied natural gas receivingterminals[J]. Energy,2012,44(1):69-78.
[43] LEE S. Operating information system for LNG facilities[J].2001,34(27):363-368.
[44] YAMASHITA Y,HIRATA Y,IWATA Y,et al. Performanceand heat transfer characteristics of a latent heat storage unitwith fifinned tubes:Experimental study on liquefaction of LNGboil-off gas by melting n-pentane as a phase-change material[J].Kagaku Kogaku Ronbunshu,2004,30(4):399-406.
[45] 薛鹏,张引弟,杨建平,等. 基于变压吸附制氮系统的 BOG 再 冷凝工艺[J]. 天然气工业, 2017, 37(12): 92-98.XUE P,ZHANG Y D,YANG J P,et al. A BOG recondensationprocess based on a PSA nitrogen system[J]. Natural GasIndustry,2017,37(12):92-98.
[46] 向丽君,全日,邱奎,等. LNG 接收站 BOG 气体回收工艺改进 与能耗分析[J]. 天然气化工,2012,37(3):48-50.XIANG L J,QUAN R,QIU K,et al. LNG terminal BOGrecovery process improvement and energy saving analysis[J].Natural Gas Chemical Industry,2012,37(3):48-50.
[47] 杨志国,李亚军. 液化天然气接收站蒸发气体再冷凝工艺的优 化[J]. 化工学报,2009,60(11):2876-2881.YANG Z G,LI Y J. Optimization of boil-off gas recondensationprocess in LNG receiving terminal[J]. Journal of ChemicalIndustry and Engineering(China),2009,60(11):2876-2881.
[48] CUI M,YUAN Z,SONG R,et al. Performance improvement ofa boil-off gas re-condensation process with pre-cooling at LNGterminals[J]. International Journal of Thermodynamics,2015, 18(2):74-80.
[49] 张弛,潘振,商丽艳,等. LNG 接收站 BOG 处理工艺优化及能 耗分析[J]. 油气储运,2017,36(4):421-425.ZHANG C,PAN Z,SHANG L Y,et al. Optimizationand energy consumption analysis on the BOG treatmenttechnology in LNG receiving station[J]. Oil & Gas Storage andTransportation,2017,36(4):421-425.
[50] QUEROL E,GONZALEZ-REGUERAL B,GARCIATORRENT J,et al. Boil off gas(BOG)management in Spanishliquid natural gas(LNG)terminals[J]. Applied Energy,2010, 87(11):3384-3392.
[51] 杨志国,李亚军. 液化天然气接收站再冷凝工艺优化研究[J].现代化工,2009,29(11):74-77.YANG Z G,LI Y J. Inflfluence of operational parameters on boiloff gas recondensation process[J]. Modern Chemical Industry, 2009, 29(11):74-77.
[52] 李亚军,陈蒙. LNG 接收站 BOG 多阶压缩再液化工艺优化分 析[J]. 化工学报,2013,64(3):986-992.LI Y J,CHEN M. Simulation-based optimization and analysisof BOG multi-stage compression and recondensation process atLNG receiving terminal[J]. Journal of Chemical Industry andEngineering(China),2013,64(3):986-992.
[53] 严涛,刘玉丰,刘丰. 液化天然气(LNG)接收站节能再冷凝器 的研究与设计[J]. 化工进展,2015,34(增刊 1):51-54.YAN T,LIU Y F,LIU F. Research and design of the LNGterminal station energy-saving recondenser[J]. ChemicalIndustry and Engineering Progress,2015,34(S1):51-54.
[54] 王同吉,陈文杰,赵金睿,等. LNG 接收终端气化器冬季运行模 式优化[J]. 油气储运,2018,37(11):1272-1279.WANG T J,CHEN W J,ZHAO J R,et al. Optimization of theoperation mode of vaporizers at LNG terminals in winter[J].Oil & Gas Storage and Transportation,2018,37(11):1272-1279.



Last Update: 2019-12-25