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为优化LNG 接收站BOG 处理工艺,降低整个接收站的功耗,以外输量为200 t/h、储罐BOG蒸发量为3.04 t/h 的某LNG 接收站为例,对再冷凝工艺和直接压缩工艺两种典型的BOG 处理工艺进行了功耗分析,得出BOG 压缩机和LNG 高压泵的功耗为整个工艺的主要功耗。运用ASPENHYSYS模拟软件对现有工艺流程进行了优化:在现有BOG 处理工艺的基础上,通过对LNG 进一步加压至高于外输压力,靠气化后膨胀高压外输天然气做功来实现BOG 的压缩和对LNG 的加压。优化结果表明:BOG 直接压缩工艺和再冷凝工艺分别节约功耗1 616.27 kW、1 270.64 kW。
To further optimize the BOG treatment process in LNG terminals and reduce energy consumption of the entire LNG terminal, a LNG terminals with LNG output capacity of 200 t/h and BOG evaporation of 3.04 t/h is taken as an example to analyze power consumptions of two classical BOG treatment processes, namely re-condensation process and direct compression process. The results show that BOG compressors and high-pressure LNG pumps contribute dominant proportions in energy consumption. ASPEN-HYSYS simulation software is used to optimize existing processes. Specifically, LNG is further pressurized to a level higher than outlet pressure, and the gasification and expansion of the high-pressure outlet natural gas are used to compress BOG and pressurize LNG. The improved BOG direct compression process and recondensation process can reduce energy consumption by 1 616.27 kW and 1 270.64 kW, respectively.
[1] 朱建鲁,李玉星,王武昌,等. LNG 接收站终端工艺流程动态仿 真[J]. 化工学报,2013,64(3):1000-1007. ZHU J L,LI Y X,WANG W C,et al. Dynamic simulation of LNG import terminal process[J]. CIESC Journal,2013,64(3): 1000-1007.
[2] 李兆慈,王敏,亢永博. LNG 接收站BOG 的再冷凝工艺[J]. 化 工进展,2011,30(增刊1):521-524. LI Z C,WANG M,KANG Y B. Recondensation process of the LNG terminal[J]. Chemical Industry and Engineering Progress, 2011,30(S1):521-524.
[3] 陈利琼,韩晓瑜,黄坤,等. LNG 储备库蒸发气回收工艺研 究[J]. 石油与天然气化工,2015,44(1):39-44. CHEN L Q,HAN X Y,HUANG K,et al. Study of boil off gas recovery process in LNG repository[J]. Chemical Engineering of Oil & Gas,2015,44(1):39-44.
[4] 张奕,吴斌,艾绍平. 液化天然气接收站的工艺流程[J]. 重庆科 技学院学报(自然科学版),2012,14(1):104-105,114. ZHANG Y,WU B,AI S P. The process of liquid natural gas terminal[J]. Journal of Chongqing University of Science and Technology(Natural Sciences Edition),2012,14(1):104-105,114.
[5] 李亚军,陈行水. 液化天然气接收站蒸发气体再冷凝工艺控制 系统优化[J]. 低温工程,2011(3):44-49. LI Y J,CHEN X S. Optimization of control system to BOG recondensation process at LNG receiving terminal[J]. Cryogenics,2011(3):44-49.
[6] 况岱坪,董事尔,杨冲伟,等. LNG 卫星站冷能制冰工艺优化及 模拟分析[J]. 石油与天然气化工,2014,43(2):140-145. KUANG D P,DONG S E,YANG C W,et al. Process optimization and simulation of ice-making utilizing cold energy from LNG satellite station[J]. Chemical Engineering of Oil & Gas,2014,43(2):140-145.
[7] ROMERO G M, FERREIRO G R, GARBIA G J, et al. High efficiency power plant with liquefied natural gas cold energy utilization[J]. Journal of the Energy Institute,2014,87(1):59-68.
[8] PARK C,SONG K,LEE S,et al. Retrofit design of a boil-off gas handing process in liquefied natural gas receiving terminals[J]. Energy,2012(44):69-78.
[9] 姜国良,侯志强,刘骁,等. 山东LNG 接收站再冷凝器工艺及控 制系统[J]. 油气储运,2015,34(1):42-45. JIANG G L, HOU Z Q, LIU X,et al. Recondenser process and control system of Shandong LNG Terminal[J]. Oil & Gas Storage and Transportation,2015,34(1):42-45.
[10] 王红,白改玲,李艳辉,等. LNG 接收站流程模拟计算[J]. 天然 气工业,2007,27(11):108-109. WANG H,BAI G L, LI Y H,et al. The simulated calculation on LNG receiving terminal process[J]. Natural Gas Industry, 2007,27(11):108-109.
[1]贾保印 白改玲.大气压变化对蒸发气压缩机处理能力的影响[J].油气储运,2016,35(预出版):1.
JIA Baoyin,BAI Gailing.Impacts of changes in atmospheric pressure to processing capacity of BOG compressor[J].Oil & Gas Storage and Transportation,2016,35(4):1.
[2]彭延建,张超,肖立.LNG卸料管道穿堤布置方案的设计[J].油气储运,2016,35(4):412.[doi:10.6047/j.issn.1000-8241.2016.04.012]
PENG Yanjian,ZHANG Chao,XIAO Li.Design on the arrangement program of LNG unloading pipeline crossing seawall[J].Oil & Gas Storage and Transportation,2016,35(4):412.[doi:10.6047/j.issn.1000-8241.2016.04.012]
[3]彭延建 张超 肖立.LNG 卸料管道穿堤布置方案的设计[J].油气储运,2016,35(预出版):1.
PENG Yanjian,ZHANG Chao,XIAO Li.Design on the arrangement program of LNG unloading pipeline crossing seawall[J].Oil & Gas Storage and Transportation,2016,35(4):1.
[4]王赟,贺三,战永辉,等.移动式小型BOG增压再液化装置功耗的模拟计算[J].油气储运,2015,34(6):662.[doi:10.6047/j.issn.1000-8241.2015.06.021]
WANG Yun,HE San,ZHAN Yonghui,et al.Simulated calculation of power consumption of the mobile small-scale BOG compression and reliquefaction plant[J].Oil & Gas Storage and Transportation,2015,34(4):662.[doi:10.6047/j.issn.1000-8241.2015.06.021]
[5]薛倩 刘名瑞 肖文涛 王晓霖 张久久.LNG 接收站 BOG 处理工艺优化及能耗分析[J].油气储运,2016,35(预出版):1.
XUE Qian,LIU Mingrui,XIAO Wentao,et al.Optimization and energy consumption analysis of BOG treatment processes in LNG terminal[J].Oil & Gas Storage and Transportation,2016,35(4):1.
[6]周怀发 申永亮 张兴 刘铭刚.基于层次分析与集对分析法的LNG 槽车区风险评价[J].油气储运,2019,38(预出版):1.
ZHOU Huaifa,SHEN Yongliang,ZHANG Xing,et al.Risk assessment on LNG tanker loading region based on analytical hierarchy process and set pair analysis theory[J].Oil & Gas Storage and Transportation,2019,38(4):1.
[7]徐波 段林杰 戴梦 李妍 闫锋 胡森.LNG 全运输系统运行可靠度计算方法[J].油气储运,2020,39(01):48.[doi:10.6047/j.issn.1000-8241.2020.01.007]
XU Bo,DUAN Linjie,DAI Meng,et al.A calculation method for the operation reliability of LNG whole transportation system[J].Oil & Gas Storage and Transportation,2020,39(4):48.[doi:10.6047/j.issn.1000-8241.2020.01.007]
[8]远双杰 孟凡鹏 安云朋 董平省 孙立刚 崔亚梅 张效铭.LNG 接收站工程中外输首站的设计探讨及优化[J].油气储运,2020,39(10):1.[doi:10.6047/j.issn.1000-8241.2020.10.014]
YUAN Shuangjie,MENG Fanpeng,AN Yunpeng,et al.Discussion and optimization of the design of the initial transportationstation in LNG receiving terminal project[J].Oil & Gas Storage and Transportation,2020,39(4):1.[doi:10.6047/j.issn.1000-8241.2020.10.014]
收稿日期:2015-6-16;改回日期:2016-3-13。
作者简介:薛倩,女,工程师,1986年生,2012年硕士毕业于大连理工大学化学工程专业,现主要从事LNG接收站工艺优化研究工作。地址:辽宁省抚顺市望花区丹东路东段31号,113001。电话:024-85639300,Email:xueqian.fshy@sinopec.com