PDF下载
[1]张梦娴,李玉星,张建军.填料塔内液体分布对晃荡敏感性的研究进展[J].油气储运,2016,35(12):1267-1274.[doi:10.6047/j.issn.1000-8241.2016.12.003]
　ZHANG Mengxian,LI Yuxing,ZHANG Jianjun.Research progress of sensitivity of liquid distribution in packed tower to the sloshing[J].Oil & Gas Storage and Transportation,2016,35(12):1267-1274.[doi:10.6047/j.issn.1000-8241.2016.12.003]
点击复制

填料塔内液体分布对晃荡敏感性的研究进展

《油气储运》[ISSN:1000-8241/CN:13-1093/TE] 卷: 35 期数: 2016年第12期 页码: 1267-1274 栏目: 前瞻与综述 出版日期: 2016-12-25
Title:
Research progress of sensitivity of liquid distribution in packed tower to the sloshing
作者:
张梦娴1; 李玉星1; 张建军2
1. 中国石油大学（华东）储运与建筑工程学院；2. 大庆油田采油六厂
Author(s):
ZHANG Mengxian1;  LI Yuxing1;  ZHANG Jianjun2
1. College of Pipeline and Civil Engineering, China University of Petroleum (Huadong); 2. No.6 Oil Production Plant, PetroChina Daqing Oilfield Company
关键词:
海上油气; 填料塔; 晃荡; 倾斜; 液体分布; 数值模拟; 实验研究
Keywords:
offshore oil and gas;  packed tower;  sloshing;  tilt;  liquid distribution;  numerical simulation;  experimental study
分类号:
TE868
DOI:
10.6047/j.issn.1000-8241.2016.12.003
文献标志码:
A
摘要:
填料塔是海上浮式生产系统中天然气预处理的重要设备，在海上油气田特殊环境下，填料塔 内会存在较为严重的液体不均匀分布，降低填料塔的传质性能。通过调研国内外有关晃荡条件下填 料塔内气液流场和传质性能的研究现状，分别从实验研究、数值模拟研究、机理模型法3 个方面分析 了国内外的研究进展：实验研究方面主要集中于国外，研究内容主要为晃荡条件对填料塔整体性质 的影响，部分涉及流型的变化情况；数值模拟研究方面主要从宏观尺度研究晃荡条件对填料塔内气 液流场的影响；机理模型法进行改进后首次用于分析海上条件对规整填料塔内液体分布的影响，为 填料塔的研究提供了新的研究思路。结合工程实际，指出了晃荡条件下填料塔内运行性能研究方法 的不足和今后的研究重点，可为浮式环境中填料塔的优化设计提供一定参考。（参53）
Abstract:
Packed tower is the key equipment for natural gas pre-treatment on offshore floating production system. In the harsh environment of offshore oil and gas fields, however, the mass transfer behavior of packed tower is deteriorated for liquid maldistribution in the tower. In this paper, the worldwide research status of gas-liquid flow field and mass transfer behavior in packed towers under sloshing conditions was reviewed, and the research progress was analyzed from three aspects, including experimental study, numerical simulation and mechanism model. The experimental study is mainly carried out abroad, focusing on the effect of sloshing on the overall performance of packed tower and partially on the change of flow regime. The numerical simulation mainly surveys the effect of sloshing on the gas-liquid flow field at macro-scale. And the modified mechanistic model is, for the first time, used to analyze the effect of offshore conditions on liquid distribution in structured packed tower, and it provides a new research idea for studying packed towers. Based on actual engineering, it points out the deficiencies and future research focus of research methods on operation performance of packed tower under sloshing conditions, and provides the reference for optimization design of packed tower in floating environment. (53 References)

参考文献/References:

[1] 薄玉宝. 浮式液化天然气（FLNG）技术在中国海上开发应用探 讨[J]. 中国海洋平台，2013，28（3）：1-5. BO Y B. Floating liquefied natural gas（FLNG）technology in China offshore development application to discussion[J]. China Offshore Platform，2013，28（3）：1-5.
[2] WANG W，LI Y，ZANG L，et al. Offshore applicability analysis of the LNG-FPSO production process[C]. Beijing： The Twentieth International Offshore and Polar Engineering Conference，2010：466-469.
[3] WEEDMAN J A，DODGE B F. Rectification of liquid air in a packed column[J]. Industrial and Engineering Chemistry，1947， 39（6）：732-744. [4] HOERNER B K，WIESSNER F G，BERGER E A. Influence of irregular motion of a floating structure on absorption and distillation processes[C]. Houston：Offshore Technology Conference，1982：527-541.
[5] HOERNER B K，WIESSNER F G，BERGER E A. Effect of irregular motion on absorption/distillation processes[J]. Chemical Engineering Progress，1982，78（11）：47-52.
[6] SVENSSON H. Distillation problems on a floating plant[J]. Chemical Engineering Progress，1982，78（11）：43-46.
[7] BAKER S A，TANNER R K，WALDIE B. Comparison of packing types in a water deaeration column under vertical，tilt and motion conditions[J]. Chemical Engineering Research & Design， 1992，70（S5）：509-515.
[8] SCHUBERT M，HAMIDIPOUR M，DUCHESNE C，et al. Hydrodynamics of cocurrent two-phase flows in slanted porous media-Modulation of pulse flow via bed obliquity[J]. AIChE Journal，2010，56（12）：3189-3205.
[9] BOUTELDJA H，HAMIDIPOUR M，LARACHI F. Hydrodynamics of an inclined gas-liquid cocurrent upflow packed bed[J]. Chemical Engineering Science，2013，102（15）：397-404.
[10] WEISS C，HUGUET E，MAGNE-DRISCH J，et al. How waves can significantly impact performance of amine unit installed on a FLNG?[C]. Houston：Offshore Technology Conference，2014： OTC-25191-MS.
[11] ASSIMA G P，MOTAMED-DASHLIBORUN A，LARACHI F. Emulation of gas-liquid flow in packed beds for offshore floating applications using a swell simulation hexapod[J]. AIChE Journal，2015，61（5）：2354-2367.
[12] DASHLIBORUN A M，LARACHI F. Hydrodynamics of gasliquid cocurrent downflow in floating packed beds[J]. Chemical Engineering Science，2015，137：665-676.
[13] 唐建峰，杨帆，崔健，等. 晃动对FLNG 排管式液体分布器性能 的影响[J]. 天然气工业，2016，36（1）：123-128. TANG J F，YANG F，CUI J，et al. Effects of sloshing on the performance of FLNG calandria liquid distribution[J]. Natural Gas Industry，2016，36（1）：123-128.
[14] 张会书，袁希钢，KALBASSI M A. 规整填料内液体分布的实 验研究进展[J]. 化工进展，2015，34（8）：2932-2939. ZHANG H S，YUAN X G，KALBASSI M A. Reasearch process of liquid distribution in structured packing[J]. Chemical Industry and Engineering Progress，2015，34（8）：2932-2939.
[15] SIDI-BOUMEDINE R，RAYNAL L. Influence of the viscosity on the liquid hold-up in trickle-bed reactors with structured packings[J]. Catalysis Today，2005，105（3-4）：673-679.
[16] ALIX P，RAYNAL L. Liquid distribution and liquid hold-up in modern high capacity packings[J]. Chemical Engineering Research & Design，2008，86（6）：585-591.
[17] FOURATI M，ROIG V，RAYNAL L. Experimental study of liquid spreading in structured packings[J]. Chemical Engineering Science，2012，80（10）：1-15.
[18] AFERKA S，VIVA A，BRUNAZZI E，et al. Tomographic measurement of liquid hold up and effective interfacial area distributions in a column packed with high performance structured packings[J]. Chemical Engineering Science，2011， 66（14）：3413-3422.
[19] VIVA A，AFERKA S，BRUNAZZI E，et al. Processing of X-ray tomographic images：A procedure adapted for the analysis of phase distribution in MellapakPlus 752.Y and Katapak-SP packings[J]. Flow Measurement & Instrumentation，2011， 22（4）：279-290.
[20] JANZEN A，SCHUBERT M，BARTHEL F，e t a l . Investigation of dynamic liquid distribution and hold-up in structured packings using ultrafast electron beam X-ray tomography[J]. Chemical Engineering & Processing，2013， 66（4）：20-26.
[21] BASDEN M，ELDRIDGE R B，FARONE J，et al. Liquid holdup profiles in structured packing determined via neutron radiography[J]. Industrial & Engineering Chemistry Research， 2013，52（48）：17263-17269.
[22] 张会书，袁希钢，KALBASSI M A. 激光诱导荧光技术测量规 整填料内的液体分布[J]. 化工学报，2014（9）：3331-3339. ZHANG H S，YUAN X G，KALBASSI M A. Laser induced fluorescence technique for measuring liquid distribution in structured packing[J]. CIESC Journal，2014（9）：3331-3339.
[23] OLUJI? ? ，JANSEN H. Large-diameter experimental evidence on liquid （mal） distribution properties of structured packings[J]. Chemical Engineering Research and Design，2015， 99：2-13.
[24] 岳强，于开录，罗太刚，等. 倾斜状态下的填料塔液体分布性能 研究[J]. 化学工程师，2015（2）：43-46. YUE Q，YU K L，LUO T G，et al. Researching the performance of liquid distribution of packed column in the inclined state[J]. Chemical Engineer，2015（2）：43-46.
[25] WIDBOM G C，THORSSON C O. Offshore methanol production：Selection of carriers for different plant capacities[C]. Houston：Offshore Technology Conference，1984： 91-102.
[26] CULLINANE J T，YEH N，GRAVE E. Effects of tower motion on packing efficiency[C]. Macaé：Brasil Offshore Conference and Exhibition，2011：1-14.
[27] HAROUN Y，RAYNAL L，ALIX P. P a r t i t i o n e d distributor tray for offshore gas/liquid contact column： US20130277868[P]. 2013.
[28] DUSS M，ROZA M. Columns subject to motion：Maldistribution sensitivity and susceptibility[C]. Friedrichshafen： 10th International Conference on Distillation & Absorption， 2014：14-17.
[29] 张平，李雅侠，秦然，等. 倾斜塔板液相三维流场的数值模拟[J]. 高校化学工程学报，2014，28（6）：1217-1222. ZHANG P，LI Y X，QIN R，et al. Three-dimension numeric simulation of liquid flow on oblique sieve tray[J]. Journal of Chemical Engineering of Chinese Universities，2014，28（6）： 1217-1222.
[30] PHAM D A，LIM Y I，JEE H，et al. Effect of ship tilting on amine absorber with structured-packing for CO2 removal from natural gas[J]. Computer Aided Chemical Engineering，2014， 34：405-410.
[31] PHAM D A，LIM Y I，JEE H，et al. Effect of ship tilting and motion on amine absorber with structured-packing for CO2 removal from natural gas[J]. AIChE Journal，2015，61（12）： 4412-4425.
[32] LIU S，LONG J. Gas-liquid countercurrent flows through packed towers[J]. Journal of Porous Media，2000，3（2）：99-113.
[33] MEWES D，LOSER T，MILLIES M. Modelling of two-phase flow in packings and monoliths[J]. Chemical Engineering Science，1999，54（21）：4729-4747.
[34] LAPPALAINEN K，MANNINEN M，ALOPAEUS V，et al. An analytical model for capillary pressure–saturation relation for gas–liquid system in a packed-bed of spherical particles[J]. Transport in Porous Media，2009，77（1）：17-40.
[35] LAPPALAINEN K，GORSHKOVA E，MANNINEN M， et al. Characteristics of liquid and tracer dispersion in tricklebed reactors：Effect on CFD modeling and experimental analyses[J]. Computers & Chemical Engineering，2011，35（1）： 41-49.
[36] LAPPALAINEN K，MANNINEN M，ALOPAEUS V. CFD modelling of radial spreading of flow in trickle-bed reactors due to mechanical and capillary dispersion[J]. Chemical Engineering Science，2009，64（2）：207-218.
[37] EDWARDS D P，KRISHNAMURTHY K R，POTTHOFF R W. Development of an improved method to quantify maldistribution and its effect on structured packing columnperformance[J]. Chemical Engineering Research & Design， 1999，77（7）：656-662.
[38] FOURATI M，ROIG V，RAYNAL L. Liquid dispersion in packed columns： Experiments and numerical modeling[J]. Chemical Engineering Science，2013，100（2）：266-278.
[39] SOLOMENKO Z，HAROUN Y，FOURATI M，et al. Liquid spreading in trickle-bed reactors：Experiments and numerical simulations using Eulerian–Eulerian two-fluid approach[J]. Chemical Engineering Science， 2015，126：698-710.
[40] ILIUTA I，LARACHI F. Mechanistic model for structuredpacking- containing columns：Irrigated pressure drop，liquid holdup，and packing fractional wetted area[J]. Industrial & Engineering Chemistry Research，2001，40（23）：5140-5146.
[41] ILIUTA I，PETRE C F，LARACHI F. Hydrodynamic continuum model for two-phase flow structured-packingcontaining columns[J]. Chemical Engineering Science，2004， 59（4）：879-888.
[42] SHOJAEE S，HOSSEINI S H，RAFATI A，et al. Prediction of the effective area in structured packings by computational fluid dynamics[J]. Industrial & Engineering Chemistry Research， 2011，50（18）：10833-10842. [43] TSAI R E，FRANK S A，BRUCE E R，et al. A dimensionless model for predicting the mass-transfer area of structured packing[J]. AIChE Journal，2011，57（5）：1173-1184. [44] SEBASTIA-SAEZ D，GU S，RANGANATHAN P，et al. 3D modeling of hydrodynamics and physical mass transfer characteristics of liquid film flows in structured packing elements[J]. International Journal of Greenhouse Gas Control， 2013，19： 492-502. [45] SEBASTIA-SAEZ D， GU S， RANGANATHAN P， et al. Micro-scale CFD study about the influence of operative parameters on physical mass transfer within structured packing elements[J]. International Journal of Greenhouse Gas Control， 2014，28： 180-188. [46] SEBASTIA-SAEZ D，GU S，RANGANATHAN P，et al. Meso-scale CFD study of the pressure drop，liquid holdup， interfacial area and mass transfer in structured packing materials[J]. International Journal of Greenhouse Gas Control， 2015， 42：388-399. [47] PHAM D A，LIM Y I，JEE H，et al. Porous media eulerian computational fluid dynamics（ CFD） model of amine absorber with structured-packing for CO2 removal[J]. Chemical Engineering Science，2015，132：259-270. [48] HIKITA H，ASAI S，ISHIKAWA H，et al. The kinetics of reactions of carbon dioxide with monoethanolamine， diethanolamine and triethanolamine by a rapid mixing method[J]. Chemical Engineering Journal，1977，13（1）： 7-12. [49] PHAM D A，LIM Y I，JEE H，et al. Effect of ship motion on amine absorber with structured-packing for CO2 removal from natural gas：An approach based on porous medium CFD model[J]. Computer Aided Chemical Engineering，2015，37： 557-562. [50] NAWROCKI P A，XU Z P，CHUANG K T. Mass transfer in structured corrugated packing[J]. Canadian Journal of Chemical Engineering，1991，69（6）：1336-1343. [51] AROONWILAS A，TONTIWACHWUTHIKUL P. Mechanistic model for prediction of structured packing mass transfer performance in CO2，absorption with chemical reactions[J]. Chemical Engineering Science，2000，55（18）： 3651-3663. [52] QIU J H，CHEN G B，JI J B. Integrated liquid distribution model for the corrugated-sheet-structured packed columns[J]. Ind Eng Chem Res，2003，42（14）：3426-3433. [53] SON Y，MIN K，LEE K S. A liquid distribution model for a column with structured packing under offshore conditions[J]. Chemical Engineering Science，2016，153：199-211.

相似文献/References:

[1]唐建峰　金新明　周军逸　杨文刚　崔健　张豪杰.FLNG 填料塔内气体分布器适应性的实验研究[J].油气储运,2018,37(预出版):1.
　TANG Jianfeng,JIN Xinming,ZHOU Junyi,et al.Experimental study on the adaptability of gas distributor in the FLNG packed tower[J].Oil & Gas Storage and Transportation,2018,37(12):1.
[2]张梦娴　李玉星　张建军.填料塔内液体分布对晃荡敏感性的研究进展[J].油气储运,2016,35(预出版):1.
　ZHANG Mengxian,LI Yuxing,ZHANG Jianjun.Research progress of sensitivity of liquid distribution in packed tower to the sloshing[J].Oil & Gas Storage and Transportation,2016,35(12):1.
[3]李玉星,朱建鲁,王武昌.FLNG 液化工艺的关键技术[J].油气储运,2017,36(2):121.[doi:10.6047/j.issn.1000-8241.2017.02.001]
　LI Yuxing,ZHU Jianlu,WANG Wuchang.Key FLNG liquefaction technologies[J].Oil & Gas Storage and Transportation,2017,36(12):121.[doi:10.6047/j.issn.1000-8241.2017.02.001]
[4]唐建峰,金新明,周军逸,等.FLNG 填料塔内气体分布器适应性实验[J].油气储运,2018,37(7):822.[doi:10.6047/j.issn.1000-8241.2018.07.016]
　TANG Jianfeng,JIN Xinming,ZHOU Junyi,et al.Compatibility test of gas distributor in the FLNG packed tower[J].Oil & Gas Storage and Transportation,2018,37(12):822.[doi:10.6047/j.issn.1000-8241.2018.07.016]

备注/Memo

基金项目：国家科技重大专项“大型FLNG/FLPG、FDPSO 关键 技术”，2011ZX05026-006-07。 作者简介：张梦娴，女，在读硕士生，1991 年生，2014 年毕业于中 国石油大学（华东）油气储运工程专业，现主要从事FLNG 预处理 关键技术研究。地址：山东省青岛市黄岛区长江西路66 号，266580。 电话：18765922406，Email：zhangmx_125@163.com

更新日期/Last Update: 1900-01-01