Slug length for high viscosity oil-gas flow in horizontal pipes: Experiments and prediction

被引:35
作者
Baba, Yahaya D. [1 ,3 ]
Aliyu, Aliyu M. [2 ]
Archibong, Archibong E. [1 ,4 ]
Abdulkadir, Mukhtar [5 ]
Lao, Liyun [1 ]
Yeung, Hoi [1 ]
机构
[1] Cranfield Univ, Oil & Gas Engn Ctr, Cranfield MK43 0AL, Beds, England
[2] Pusan Natl Univ, Sch Mech Engn, Busan 609735, South Korea
[3] Afe Babalola Univ, Chem & Petr Engn Dept, PMB 5454, Ado Ekiti, Ekiti, Nigeria
[4] Cross River Univ Technol, Dept Mech Engn, Ekpo Abasi St, Calabar, Nigeria
[5] Fed Univ Technol, Dept Chem Engn, PMB 65, Minna, Nigeria
关键词
High viscosity oil; Gamma densitometer; Slug length; Translational velocity; Two phase flow; LIQUID SLUG; INTERMITTENT FLOW; MODEL; HOLDUP; TRANSITIONS; FREQUENCY; EVOLUTION; DIAMETER; TUBES;
D O I
10.1016/j.petrol.2018.02.003
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
An experimental investigation was carried out on the effects of high liquid viscosities on slug length in a 0.0762-m ID horizontal pipe using air-water and air-oil systems with nominal viscosities ranging from 1.0 to 5.5 Pa s. The measurements of slug length were carried out using two fast sampling gamma densitometers with a sampling frequency of 250 Hz. The results obtained show that liquid viscosity has a significant effect on slug length. An assessment of existing prediction models and correlations in the literature was carried out and statistical analysis against the present data revealed some discrepancies, which can be attributed to fluid properties in particular, low viscous oil data used in their derivation Hence, a new high viscous oil data presented here from which we derive a new slug length correlation was derived using dimensional analysis. The proposed correlation will improve prediction of slug length as well as provide a closure relationship for use in flow simulations involving heavy oil. This is important since most current fields produce highly viscous oil with some reaching 10 Pa s.
引用
收藏
页码:397 / 411
页数:15
相关论文
共 66 条
[1]   Liquid slug holdup in horizontal and slightly inclined two-phase slug flow [J].
Abdul-Majeed, GH .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2000, 27 (1-2) :27-32
[2]   Experimental study of the hydrodynamic behaviour of slug flow in a horizontal pipe [J].
Abdulkadir, M. ;
Hernandez-Perez, V. ;
Lowndes, I. S. ;
Azzopardi, B. J. ;
Sam-Mbomah, E. .
CHEMICAL ENGINEERING SCIENCE, 2016, 156 :147-161
[3]   Liquid holdup in horizontal two-phase gas-liquid flow [J].
AbdulMajeed, GH .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 1996, 15 (2-4) :271-280
[4]  
Al-Safran E., 2012, 8 N AM C MULT TECHN
[5]  
Al-Safran E., 2015, J PETROL SCI ENG
[6]  
Al-safran E., 2011, 15 INT C MULT PROD T, P257
[7]   Investigation and Prediction of High-Viscosity Liquid Effect on Two-Phase Slug Length in Horizontal Pipelines [J].
Al-Safran, E. M. ;
Gokcal, B. ;
Sarica, C. .
SPE PRODUCTION & OPERATIONS, 2013, 28 (03) :296-305
[8]   Investigation and prediction of slug frequency in gas/liquid horizontal pipe flow [J].
Al-Safran, Eissa .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2009, 69 (1-2) :143-155
[9]   Prediction of Slug Liquid Holdup in Horizontal Pipes [J].
Al-Safran, Eissa .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2009, 131 (02) :0230011-0230018
[10]   EFFECT OF LIQUID VISCOSITY ON THE STRATIFIED SLUG TRANSITION IN HORIZONTAL PIPE-FLOW [J].
ANDRITSOS, N ;
WILLIAMS, L ;
HANRATTY, TJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (06) :877-892