CFD simulation and experimental study of oil viscosity effect on multi-stage electrical submersible pump (ESP) performance

被引:61
作者
Zhu, Jianjun [1 ]
Banjar, Hattan [1 ]
Xia, Zhenyan [1 ]
Zhang, Hong-Quan [1 ]
机构
[1] Univ Tulsa, McDougall Sch Petr Engn, 800S Tucker Dr, Tulsa, OK 74104 USA
关键词
Artificial lift; Viscosity effect; Re-circulation flow; Electric submersible pump; Computational fluid dynamics; COMPREHENSIVE APPROACH; FLOW; VERIFICATION; VALIDATION;
D O I
10.1016/j.petrol.2016.07.033
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
In this study, the oil viscosity effect on ESP performance is investigated by experimental study and computational fluid dynamics (CFD) simulations. Oils with different viscosities are flowed through a DN1750ESP at varying flow rates and rotary speeds. The temperature is maintained at different levels with a heat exchanger circulated by cold water. The pressure increase over the 3rd stage as well as total 7 stages in ESP is measured with differential pressure transducers. The same geometries, fluid properties and flow characteristics are implemented into CFD simulations. The three-dimensional (3D), steady-state Reynolds-Averaged Navier-Stokes (RANS) equations with standard SST (shear stress transport) turbulence models are solved in ANSYS CFX by employing frozen-rotor technique. With high-quality structured hexahedral mesh, the simulated pressure increment is compared with corresponding experimental results. Flow structures inside ESP impeller and diffuser channels are analyzed. At pump best efficiency point (BEP), the boosting pressure decreases 30-40% when oil viscosity increases from 10 cp to 100 cp. ESP becomes ineffective when oil viscosity is higher than 200 cp. With oil viscosity increasing, pump H-Q performance curve becomes more linear. CFD simulation reveals that the recirculation flow at impeller blade trailing edge is more prominent at lower liquid flow rates. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:735 / 745
页数:11
相关论文
共 37 条
[11]  
Gulich J.F., 1999, WORLD PUMPS, V1999a, P30, DOI [10.1016/S0262-1762(00)87528-8, DOI 10.1016/S0262-1762(00)87528-8]
[12]  
Hydraulic Institute, 1948, TENT STAND HYDR I CH
[13]  
Ippen A.T., 1945, A4557 ASME FRITZ ENG
[14]  
Launder B. E., 1974, Computer Methods in Applied Mechanics and Engineering, V3, P269, DOI 10.1016/0045-7825(74)90029-2
[15]  
Li W.G., 2002, WORLD PUMPS, V425, P26, DOI [10.1115/1.1458581, DOI 10.1115/1.1458581]
[16]   Mechanism for Onset of Sudden-Rising Head Effect in Centrifugal Pump When Handling Viscous Oils [J].
Li, Wen-Guang .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2014, 136 (07)
[17]   2-EQUATION EDDY-VISCOSITY TURBULENCE MODELS FOR ENGINEERING APPLICATIONS [J].
MENTER, FR .
AIAA JOURNAL, 1994, 32 (08) :1598-1605
[18]   3-DIMENSIONAL CALCULATION OF AIR-WATER 2-PHASE FLOW IN CENTRIFUGAL PUMP IMPELLER BASED ON A BUBBLY FLOW MODEL [J].
MINEMURA, K ;
UCHIYAMA, T .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1993, 115 (04) :766-771
[19]   CALCULATION PROCEDURE FOR HEAT, MASS AND MOMENTUM-TRANSFER IN 3-DIMENSIONAL PARABOLIC FLOWS [J].
PATANKAR, SV ;
SPALDING, DB .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1972, 15 (10) :1787-&
[20]  
Qi X., 2012, GRC T, V2012, P543