[1]孙广宇,张劲军.含蜡原油乳状液凝胶结构裂降行为模型[J].油气储运,2017,36(1):49-58.[doi:10.6047/j.issn.1000-8241.2017.01.007]
 SUN Guangyu,ZHANG Jinjun.A model used to describe the structural breakdown behavior of waxy crude oil emulsion gel[J].Oil & Gas Storage and Transportation,2017,36(1):49-58.[doi:10.6047/j.issn.1000-8241.2017.01.007]
点击复制

含蜡原油乳状液凝胶结构裂降行为模型

参考文献/References:

[1] CHANG C,NGUYEN Q D,RØNNINGSEN H P. Isothermal start-up of pipeline transporting waxy crude oil[J]. Journal of Non-Newtonian Fluid Mechanics,1999, 87(2):127-154.
[2] CHILINGARIAN G V,ROBERTSON J O,KUMAR S. Surface operations in petroleum production[M]. New York:Elsevier Science Publication Co. Inc.,1987: 2-3.
[3] GHOSH S,PRADHAN M,PATEL T,et al. Long-term stability of crystal-stabilized water-in-oil emulsions[J]. Journal of Colloid and Interface Science,2015,460:247-257.
[4] VISINTIN R F G,LOCKHART T P,LAPASIN R,et al. Structure of waxy crude oil emulsion gels[J]. Journal of NonNewtonian Fluid Mechanics,2008,149(1):34-39.
[5] SUN G Y,ZHANG J J,LI H Y. Structural behaviors of waxy crude oil emulsion gels[J]. Energy & Fuels,2014,28(6):    3718-3729.
[6] 孙广宇,张劲军. W/O 型原油乳状液及其凝胶流变特性研究进 展[J]. 油气储运,2016, 35(3):229-240.
SUN G Y,ZHANG J J. Progress in rheological studies of W/O emulsion and its gel[J]. Oil & Gas Storage and Transportation, 2016, 35(3):229-240.
[7] HAJ-SHAFIEI S,GHOSH S,ROUSSEAU D. Kinetic stability and rheology of wax-stabilized water-in-oil emulsions at different water cuts[J]. Journal of Colloid and Interface Science,2013,410: 11-20.
[8] 黄启玉,王蕾. 微观液滴分布对含蜡原油乳状液流变性的影    响[J]. 石油学报,2013, 34(4):765-774.
HUANG Q Y,WANG L. Effect of droplet distribution on rheological properties of water-in-oil emulsion in waxy crude oils[J]. Acta Petrolei Sinica,2013, 34(4):765-774.
[9] 王玮,宫敬,李晓平. 非牛顿稠油包水乳状液的剪切稀释性[J]. 石油学报,2010, 31(6):1024-1026.
WANG W,GONG J,LI X P. Shear thinning behaviors of nonNewtonian water-in-heavy-oil emulsions[J]. Acta Petrolei Sinica, 2010, 31(6):1024-1026.
[10] SUN G Y,ZHANG J J. Structural breakdown and recovery of waxy crude oil emulsion gels[J]. Rheologica Acta,2015,          54(9-10):817-829.
[11] GUO L P,ZHANG J J,SUN G Y,et al. Thixotropy and its estimation of water-in-waxy crude emulsion gels[J]. Journal of Petroleum Science and Engineering,2015,131: 86-95.
[12] 国丽萍,张劲军. 含蜡原油乳状液触变性研究[J]. 工程热物理 学报,2009, 30(2):246-248.
GUO L P,ZHANG J J. Study on thixotropy of waxy crude oil emulsion[J]. Journal of Engineering Thermophysics,2009,       30(2):246-248.
[13] YAN D F,LUO Z M. Rheological properties of Daqing crude oil and their application in pipeline transportation[J]. SPE Production Engineering,1987, 2 (4):267-276.
[14] KANÉ M,DJABOUROV M,VOLLE J L. Rheology and structure of waxy crude oils in quiescent and under shearing conditions[J]. Fuel,2004, 83(11):1591-1605.
[15] NGUYEN Q D,BOGER D V. Thixotropic behaviour of concentrated bauxite residue suspensions[J]. Rheologica Acta, 1985, 24(4):427-437.
[16] DEKRETSER R G,BOGER D V. A structural model for the time-dependent recovery of mineral suspensions[J]. Rheologica Acta,2001, 40(6):582-590.
[17] MEWIS J,WAGNER N J. Thixotropy[J]. Advances in Colloid and Interface Science,2009,147-148:214-227.
[18] ROUSSEL N. A thixotropy model for fresh fluid concretes: Theory,validation and applications[J]. Cement and Concrete Research,2006, 36(10):1797-1806.
[19] VINAY G,WACHS A,AGASSANT J F. Numerical simulation of non-isothermal viscoplastic waxy crude oil flows[J]. Journal of Non-Newtonian Fluid Mechanics,2005, 128(2):144-162.
[20] DAVIDSON M R,NGUYEN Q D,RØNNINGSEN H P. Restart model for a multi-plug gelled waxy oil pipeline[J]. Journal of Petroleum Science and Engineering,2007, 59(1):1-16.
[21] VINAY G,WACHS A,FRIGAARD I. Start-up transients and efficient computation of isothermal waxy crude oil flows[J]. Journal of Non-Newtonian Fluid Mechanics,2007,143(2): 141-156.
[22] 滕厚兴,张劲军. 含蜡原油触变模型研究现状[J]. 油气储运, 2013, 32(9):923-938.
TENG H X,ZHANG J J. Review of the thixotropic models for waxy crude[J]. Oil & Gas Storage and Transportation,2013,   32(9):923-938.
[23] BURGOS G R,ALEXANDROU A N,ENTOV V. Thixotropic rheology of semisolid metal suspensions[J]. Journal of Materials Processing Technology,2001,110(2):   164-176.
[24] CAWKWELL M G,CHARLES M E. Characterization of Canadian arctic thixotropic gelled crude oils utilizing an eightparameter model[J]. Journal of Pipelines,1989, 7:251-264.
[25] CROSS M M. Rheology of non-Newtonian fluids:A new flow equation for pseudoplastic systems[J]. Journal of Colloid Science,1965, 20(5):417-437.
26] GUO L P,ZHANG J J,HAN S P,et al. Evaluation of thixotropic models for waxy crudes based on stepwise shearing measurements[J]. Petroleum Science and Technology,2013,    31(9):895-901.
[27] HOUSKA M. Engineering aspects of the rheology of thixotropic liquids[D]. Prague:Czech Techincal University of Prague,1981: 47-83.
[28] MOORE F. The rheology of ceramic slips and bodies[J]. Transactions of the British Ceramic Society,1959, 58:470-494.
[29] WORRALL W,ETULIANI S. Viscosity changes during the ageing of clay-water suspensions[J]. Transactions of the British Ceramic Society,1964, 63:167-185.
[30] 贾邦龙,张劲军. 六参数含蜡原油触变模型[J]. 石油学报, 2012, 33(6):1080-1085.
JIA B L,ZHANG J J. A six-parameter thixotropic model for waxy crude oil[J]. Acta Petrolei Sinica,2012,33(6):1080-1085.
[31] WACHS A,VINAY G,FRIGAARD I. A 1.5D numerical model for the start up of weakly compressible flow of a viscoplastic and thixotropic fluid in pipelines[J]. Journal of Non-Newtonian Fluid Mechanics,2009,159(1):81-94.
[32] AHMADPOUR A,SADEGHY K,MADDAH-SADATIEH S R. The effect of a variable plastic viscosity on the restart problem of pipelines filled with gelled waxy crude oils[J]. Journal of Non-Newtonian Fluid Mechanics,2014,205: 16-27.
[33] ZHANG J J,GUO L P,TENG H X. Evaluation of thixotropic models for waxy crude oils based on shear stress decay at constant shear rates[J]. Applied Rheology,2010,20(5):  53944-53950.
[34] TENG H X,ZHANG J J. A new thixotropic model for waxy crude[J]. Rheologica Act,2013, 52(10-12):903-911.
[35] 赵晓东. 改性原油输送管道启动过程非稳态水力、热力计算方 法研究[D]. 北京:中国石油大学(北京),1999: 42-61.
ZHAO X D. Study on the unsteady hydraulic and thermalcomputation of the restart process of the PPDbeneficiated crude oil pipeline[D]. Beijing:China University of Petroleum(Beijing),1999: 42-61.
[36] PAULO D S. Modeling the thixotropic behavior of structured fluids[J]. Journal of Non-Newtonian Fluid Mechanics,2009, 164(1):66-75.
[37] PAULO D E S M. Thixotropic elasto-viscoplastic model for structured fluids[J]. Soft Matter,2011, 7 (6):2471-2483.
[38] PAULO D E S M,THOMPSON R L. A critical overview of elasto-viscoplastic thixotropic modeling[J]. Journal of NonNewtonian Fluid Mechanics,2012,187-188: 8-15.
[39] PAULO D E S M,THOMPSON R L. A unified approach to model elasto-viscoplastic thixotropic yield-stress materials and apparent yield-stress fluids[J]. Rheologica Acta,2013,52(7): 673-694.
[40] DORAISWAMY D,MUJUMDAR A N,TSAO I,et al. The Cox-Merz rule extended:A rheological model for concentrated suspensions and other materials with a yield stress[J]. Journal of Rheology,1991, 35(4):647-685.
[41] DULLAERT K,MEWIS J. A structural kinetics model for thixotropy[J]. Journal of Non-Newtonian Fluid Mechanics, 2006,139(1):21-30.
[42] FANG B,JIANG T Q. A novel constitutive equation for viscoelastic-thixotropic fluids and its application in the characterization of blood hysteresis loop[J]. Chinese Journal of Chemical Engineering,1998, 6 (3):264-270.
[43] HUANG S,LU C. The characterization of the time-dependent nonlinear viscoelastic of an LDPE melt using a simple thixotropy model[J]. Acta Mechanica Sinica,2005,21(4):  330-335.
[44] LABANDA J,MARCO P,LLORENS J. Rheological model to predict the thixotropic behaviour of colloidal dispersions[J]. Colloids and Surfaces A:Physicochemical and Engineering Aspects,2004,249(1):123-126.
[45] LABANDA J,LLORENS J. A structural model for thixotropy of colloidal dispersions[J]. Rheologica Acta,2006,45(3):   305-314.
[46] MUJUMDAR A,BERIS A N,METZNER A B. Transient phenomena in thixotropic systems[J]. Journal of NonNewtonian Fluid Mechanics,2002,102(2):157-178.
[47] TENG H,ZHANG J J. Modeling the viscoelasto-plastic behavior of waxy crude[J]. Petroleum Science,2013,10(3): 395-401.
[48] TENG H X,ZHANG J J. Modeling the thixotropic behavior of waxy crude[J]. Industrial & Engineering Chemistry Research, 2013, 52(23):8079-8089.
[49] ZHU C,SMAY J E. Thixotropic rheology of concentrated alumina colloidal gels for solid freeform fabrication[J]. Journal of Rheology,2011, 55(3):655-672.

相似文献/References:

[1]张其敏,孟江,李顺勇,等.易凝高粘原油乳状悬浮液分散体系研究[J].油气储运,2010,29(2):118.[doi:10.6047/j.issn.1000-8241.2010.02.010]
 Zhang Qimin,Meng Jiang,Li Shunyong.Research on Dispersion System of Emulsion-suspending Liquid of Waxy and High Viscosity Crude Oil[J].Oil & Gas Storage and Transportation,2010,29(1):118.[doi:10.6047/j.issn.1000-8241.2010.02.010]
[2]黄启玉,张帆,张劲军,等.原油水乳状液制备条件研究[J].油气储运,2007,26(6):49.[doi:DOI:10.6047/j.issn.1000-8241.2007.06.014]
 HUANG Qiyu,ZHANG Fan.Research on Preparation Condition of Water Emulsion for Crnde Oil[J].Oil & Gas Storage and Transportation,2007,26(1):49.[doi:DOI:10.6047/j.issn.1000-8241.2007.06.014]
[3]孟江 任连城 魏小林 张燕.环道试验条件下稠油O/W 乳状液的性质[J].油气储运,2012,31(3):167.[doi:10.6047/j.issn.1000-8241.2012.03.003]
 Meng Jiang,Ren Liancheng,Wei Xiaolin,et al.Heavy oil O/W emulsion properties under the test loop conditions[J].Oil & Gas Storage and Transportation,2012,31(1):167.[doi:10.6047/j.issn.1000-8241.2012.03.003]
[4]孟江,郑猛.高凝稠油乳化降凝降粘试验与研究[J].油气储运,2006,25(9):48.[doi:10.6047/j.issn.1000-8241.2006.09.013]
 MENG Jiang,ZHENG Meng.Study on Reducing Freezing Point and Viscosity of High Freezing Point Heavy Oil by Emulsion[J].Oil & Gas Storage and Transportation,2006,25(1):48.[doi:10.6047/j.issn.1000-8241.2006.09.013]
[5]敬加强,孟江,秦文婷,等.KD18稠油W/O型乳状液特性及其降粘方法[J].油气储运,2003,22(6):23.[doi:10.6047/j.issn.1000-8241.2003.06.004]
 JING Jiaqiang,MENG Jiang.The Properties of Water-in-Oil Emulsion of KD18 Viscous Oils in Xintan Oilfield and its Viscosity Reduction Method[J].Oil & Gas Storage and Transportation,2003,22(1):23.[doi:10.6047/j.issn.1000-8241.2003.06.004]
[6]江延明,李传宪.W/O乳状液的流变性研究[J].油气储运,2000,19(1):10.[doi:DOI:10.6047/j.issn.1000-8241.2000.01.004]
 Jiang Yanming,Li Chuanxian.Research on Rheological Properties of W/O Emulsion[J].Oil & Gas Storage and Transportation,2000,19(1):10.[doi:DOI:10.6047/j.issn.1000-8241.2000.01.004]
[7]段林林,敬加强,牛洪彬,等.BZ28-2S混合稠油及其乳状液的特性[J].油气储运,2010,29(5):331.[doi:10.6047/j.issn.1000-8241.2010.05.005]
 Duan Linlin,Jing Jiaqiang,Niu Hongbin.BZ28-2S Mixed Heavy Crude Oil and Characteristics of its Emulsion[J].Oil & Gas Storage and Transportation,2010,29(1):331.[doi:10.6047/j.issn.1000-8241.2010.05.005]
[8]聂向荣,杨胜来,丁景辰,等.微观蜡晶特征在流变曲线上的宏观体现[J].油气储运,2014,33(3):255.[doi:10.6047/j.issn.1000-8241.2014.03.007]
 NIE Xiangrong,YANG Shenglai,DING Jingchen,et al.Macroscopic manifestation of microscopic wax crystal characteristics on rheological curve[J].Oil & Gas Storage and Transportation,2014,33(1):255.[doi:10.6047/j.issn.1000-8241.2014.03.007]
[9]张静楠,兰浩,崔博,等.含蜡原油管道停输再启动压力计算新方法[J].油气储运,2016,35(预出版):1.
 ZHANG Jingnan,LAN Hao,CUI Bo,et al.A new calculation method of shutdown and restart pressure of waxy crude oil pipeline[J].Oil & Gas Storage and Transportation,2016,35(1):1.
[10]李鸿英,毛荣,李慧.含蜡原油蜡晶颗粒分布特征的定量分析[J].油气储运,2015,34(10):1047.[doi:10.6047/j.issn.1000-8241.2015.10.005]
 LI Hongying,MAO Rong,LI Hui.Quantitative analysis on distribution characteristics of wax crystal particles in waxy crude oil[J].Oil & Gas Storage and Transportation,2015,34(1):1047.[doi:10.6047/j.issn.1000-8241.2015.10.005]
[11]孙广宇 张劲军.W/O 型原油乳状液及其凝胶流变特性研究进展[J].油气储运,2016,35(预出版):1.
 SUN Guangyu,ZHANG Jinjun.Progress in rheological studies of W/O emulsion and its gel[J].Oil & Gas Storage and Transportation,2016,35(1):1.
[12]孙广宇,张劲军.W/O型原油乳状液及其凝胶流变特性研究进展[J].油气储运,2016,35(3):229.[doi:10.6047/j.issn.1000-8241.2016.03.001]
 SUN Guangyu,ZHANG Jinjun.Progress in rheological studies of W/O emulsion and its gel[J].Oil & Gas Storage and Transportation,2016,35(1):229.[doi:10.6047/j.issn.1000-8241.2016.03.001]
[13]孙广宇 张劲军.含蜡原油乳状液凝胶结构裂降行为模型[J].油气储运,2016,35(预出版):1.
 SUN Guangyu,ZHANG Jinjun.A model used to describe the structural breakdown behavior of waxy crude oil emulsion gel[J].Oil & Gas Storage and Transportation,2016,35(1):1.
[14]国丽萍 李文博 王宇 李文竹.W/O 型含蜡原油乳状液触变特性[J].油气储运,2018,37(预出版):1.
 GUO Liping,LI Wenbo,WANG Yu,et al.The thixotropic behavior of W/O waxy crude oil emulsion[J].Oil & Gas Storage and Transportation,2018,37(1):1.

备注/Memo

收稿日期:2016-10-10;修回日期:2016-11-25;编辑:刘朝阳

基金项目:国家自然科学基金重点项目“深水环境下易凝高黏原 油-天然气输送系统流动保障基础问题研究”,51134006;国家自然科学基金重点项目“含蜡原油常温输送机理及流动改性方法研究”,51534007。

作者简介:孙广宇,男,1987 年生,博士后,2015 年博士毕业于中国石油大学(北京)油气储运工程专业,现主要从事易凝高黏原油流变性及输送技术的研究工作。地址:山东省青岛市黄岛区长江西路66 号,266580。电话:15610509026,Email:sunguangyu@upc.edu.cn

通讯作者:张劲军,男,1962 年生,教授,1998 年博士毕业于中国石油大学(北京)油气储运工程专业,现主要从事易凝高黏原油流变性及输送技术的研究工作。地址:北京市昌平区府学路 18 号,102249。 电话:010-89734627,Email:zhangjj@cup.edu.cn
 

更新日期/Last Update: 2017-02-06