Experimental investigation of different simulated formation water salinity in three-phase waxy crude oil-water-gas flow in horizontal pipes

被引:9
作者
Husein, Norhafizuddin [1 ]
Ismail, Issham [1 ]
Boyou, Natalie Vanessa [2 ]
Mani, Sanjihuen V. Selva [1 ]
Wong, Zhu Ker [1 ]
Sulaiman, Wan Rosli Wan [1 ]
机构
[1] Univ Teknol Malaysia, Sch Chem & Energy Engn, Dept Petr Engn, Skudai 81310, Johor, Malaysia
[2] Kings Coll, Sch Engn, Dept Petr Engn, Aberdeen AB24 3FX, Scotland
关键词
Waxy crude oil; Oil-water-gas three-phase flow; Flow pattern; Pressure gradient; Liquid holdup; 2-PHASE FLOW; PRESSURE-DROP; MULTIPHASE FLOW; PREDICTING FLOW; VOID FRACTION; EMULSIONS; PATTERNS; VISCOSITY; DIAMETER; TRANSITIONS;
D O I
10.1016/j.petrol.2021.109160
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
Three-phase oil-water-gas flow experiments have been conducted in a horizontally configured rig made of carbon steel pipe with an ID of 0.041 m and a total length of 24.3 m. The test fluids were Malaysian waxy crude oil from Malay basin and three concentrations of simulated formation water salinity, namely 0 ppm, 15 000 ppm, and 30 000 ppm. The waxy crude oil and simulated formation water are varied at six different superficial liquid velocities ranging from 0.5 to 3.0 m/s while the gas phase is varied at 10 different superficial velocities ranging from 0.01 to 0.61 m/s. Eight flow patterns are observed using observational method; one of which is a newly discovered flow pattern identified as Slug with Oil Film-Oil Continuous (SLOF-OC). Salinity does not give significant effect on oil-gas interface but significantly affects the oil-water interface as lower formation water salinity is dispersed easily in crude oil compared to higher formation water salinity. The highest pressure gradient recorded was 2506.84 Pa/m at the highest superficial gas velocity while the lowest pressure gradient recorded was 89.53 Pa/m at the lowest superficial gas velocity. It is imperative to note that the experimental investigation of Malaysian waxy crude oil with different formation salinity in the three-phase flow study is in an unchartered area, therefore it provides a new platform for furthering more complex research works such as fourphase flow (gas, oil, water, and wax particles) below Wax-Appearing Temperature (WAT).
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页数:15
相关论文
共 97 条
[1]   AN EXPERIMENTAL-STUDY OF 3-PHASE FLOW REGIMES [J].
ACIKGOZ, M ;
FRANCA, F ;
LAHEY, RT .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1992, 18 (03) :327-336
[2]   Experimental Study on the Flow Regimes and Pressure Gradients of Air-Oil-Water Three-Phase Flow in Horizontal Pipes [J].
Al-Hadhrami, Luai M. ;
Shaahid, S. M. ;
Tunde, Lukman O. ;
Al-Sarkhi, A. .
SCIENTIFIC WORLD JOURNAL, 2014,
[3]   Effect of drag-reducing polymers on horizontal oil-water flows [J].
Al-Wahaibi, Talal ;
Smith, Mujeeb ;
Angeli, Panagiota .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2007, 57 (3-4) :334-346
[4]   The role of asphaltenes, resins and other solids in the stabilization of water in oil emulsions and its effects on oil production in Saudi oil fields [J].
Ali, MF ;
Alqam, MH .
FUEL, 2000, 79 (11) :1309-1316
[5]  
Anumbe N.C., 2018, THESIS U S CAROLINA
[6]   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
[7]  
Baker O., 1953, FALL M PETROLEUM BRA, DOI DOI 10.2118/323-G
[8]   Experimental investigation on liquid-liquid-gas flow: Flow patterns and pressure-gradient [J].
Bannwart, A. C. ;
Rodriguez, O. M. H. ;
Trevisan, F. E. ;
Vieira, F. F. ;
de Carvalho, C. H. M. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2009, 65 (1-2) :1-13
[9]   A UNIFIED MODEL FOR PREDICTING FLOW-PATTERN TRANSITIONS FOR THE WHOLE RANGE OF PIPE INCLINATIONS [J].
BARNEA, D .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1987, 13 (01) :1-12
[10]   STUDY OF 2-PHASE FLOW IN INCLINED PIPES [J].
BEGGS, HD ;
BRILL, JP .
JOURNAL OF PETROLEUM TECHNOLOGY, 1973, 25 (MAY) :607-617