Buoyancy driven slump flows of non-Newtonian fluids in pipes

被引:16
|
作者
Malekmohammadi, S. [2 ]
Naccache, M. F. [3 ]
Frigaard, I. A. [2 ,4 ]
Martinez, D. M. [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, Vancouver, BC V6T 1Z4, Canada
[2] Univ British Columbia, Dept Mech Engn, Vancouver, BC V6T 1Z4, Canada
[3] Pontificia Univ Catolica Rio de Janeiro, Dept Mech Engn, BR-22453 Rio De Janeiro, Brazil
[4] Univ British Columbia, Dept Math, Vancouver, BC V6T 1Z2, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
slump flows; visco-plastic fluids; yield stress; exchange flows; 2 BINGHAM FLUIDS; UNIAXIAL EXCHANGE FLOWS; VISCOPLASTIC MATERIAL;
D O I
10.1016/j.petrol.2010.03.024
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
We present results of a comparative experimental-numerical study of the buoyancy-driven slumping flow of two non-Newtonian fluids in a horizontal closed pipe. This type of flow occurs during the abandonment of horizontal oil and gas wells, when sealing the well through the setting of cement plugs. In our study, both of the fluids exhibit shear-thinning behaviour and one of the fluids has a yield stress. The yield stress is necessary in order for the flow to have a static equilibrium. We have studied the effects of changes in density difference and of small deviations from perfectly horizontal. The effects of these parameters on the interface shape and on the slump length versus time were analyzed. Comparison of numerical and experimental results shows broadly similar trends, but with some qualitative differences also observed, possibly due to interfacial effects at the interface. We also compare the slump length and shape against existing analytical results that predict the maximal static slump length. Crown Copyright (C) 2010 Published by Elsevier B.V. All rights reserved.
引用
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页码:236 / 243
页数:8
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