Experimental investigation of the effects of various parameters on viscosity reduction of heavy crude by oil-water emulsion

被引:33
作者
Al-Wahaibi, Talal [1 ]
Al-Wahaibi, Yahya [1 ]
Al-Hashmi, Abdul-Aziz R. [1 ]
Mjalli, Farouq S. [1 ]
Al-Hatmi, Safiya [1 ]
机构
[1] Sultan Qaboos Univ, Petr & Chem Engn Dept, Coll Engn, Al Khoud 123, Oman
关键词
Viscosity reduction; Phase inversion; Non-newtonian fluid; Oil-in-water emulsions; Heavy crude oil; PIPELINE TRANSPORTATION; FLOW; EMULSIFICATION;
D O I
10.1007/s12182-014-0009-2
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The effects of water content, shear rate, temperature, and solid particle concentration on viscosity reduction (VR) caused by forming stable emulsions were investigated using Omani heavy crude oil. The viscosity of the crude oil was initially measured with respect to shear rates at different temperatures from 20 to 70 degrees C. The crude oil exhibited a shear thinning behavior at all the temperatures. The strongest shear thinning was observed at 20 degrees C. A non-ionic water soluble surfactant (Triton X-100) was used to form and stabilize crude oil emulsions. The emulsification process has significantly reduced the crude oil viscosity. The degree of VR was found to increase with an increase in water content and reach its maximum value at 50 % water content. The phase inversion from oil-in-water emulsion to water-in-oil emulsion occurred at 30 % water content. The results indicated that the VR was inversely proportional to temperature and concentration of silica nanoparticles. For water-in-oil emulsions, VR increased with shear rate and eventually reached a plateau at a shear rate of around 350 s(-1). This was attributed to the thinning behavior of the continuous phase. The VR of oil-in-water emulsions remained almost constant as the shear rate increased due to the Newtonian behavior of water, the continuous phase.
引用
收藏
页码:170 / 176
页数:7
相关论文
共 23 条
[1]   Pipeline transportation of viscous crudes as concentrated oil-in-water emulsions [J].
Abdurahman, N. H. ;
Rosli, Y. M. ;
Azhari, N. H. ;
Hayder, B. A. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2012, 90-91 :139-144
[2]   Experimental study on the transition between stratified and non-stratified horizontal oil-water flow [J].
Al-Wahaibi, T. ;
Yusuf, N. ;
Al-Wahaibi, Y. ;
Al-Ajmi, A. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2012, 38 (01) :126-135
[3]   Experimental study on interfacial waves in stratified horizontal oil-water flow [J].
Al-Wahaibi, Talal ;
Angeli, Panagiota .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2011, 37 (08) :930-940
[4]   Flow structure in horizontal oil-water flow [J].
Angeli, P ;
Hewitt, GF .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2000, 26 (07) :1117-1140
[5]   Emulsification of heavy crude oil in water for pipeline transportation [J].
Ashrafizadeh, S. N. ;
Kamran, M. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2010, 71 (3-4) :205-211
[6]   Flow enhancement of medium-viscosity crude oil [J].
Ghannam, Mamdouh T. ;
Esmail, Nabil .
PETROLEUM SCIENCE AND TECHNOLOGY, 2006, 24 (08) :985-999
[7]  
Gregoli A.A., 2006, US Patent, Patent No. [4,725,287, 4725287]
[8]   Heavy crude oil viscosity reduction and rheology for pipeline transportation [J].
Hasan, Shadi W. ;
Ghannam, Mamdouh T. ;
Esmail, Nabil .
FUEL, 2010, 89 (05) :1095-1100
[9]   Core-annular flows [J].
Joseph, DD ;
Bai, R ;
Chen, KP ;
Renardy, YY .
ANNUAL REVIEW OF FLUID MECHANICS, 1997, 29 :65-90
[10]   Crude oil emulsion properties and their application to heavy oil transportation [J].
Langevin, D ;
Poteau, S ;
Hénaut, I ;
Argillier, JF .
OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES, 2004, 59 (05) :511-521