Shape factor of the flake-like particle in thermal spallation and its effects on settling and transport behavior in drilling annulus

被引:27
作者
Hu, Xiaodong [1 ]
Song, Xianzhi [1 ]
Li, Gensheng [1 ]
Shen, Zhonghou [1 ]
Lyu, Zehao [1 ]
Shi, Yu [1 ]
机构
[1] China Univ Petr, Beijing, Peoples R China
基金
中国国家自然科学基金;
关键词
Multi-phase flow; Thermal spallation; Spalls; Settling velocity; Shape factor; NONSPHERICAL PARTICLES; DRAG COEFFICIENT; ASPECT RATIO; NEWTONIAN FLUIDS; GRANULAR FLOW; VELOCITY; MOTION; SEDIMENTATION; FALL;
D O I
10.1016/j.powtec.2018.05.014
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Thermal Spallation Drilling (TSD) is widely applied in the exploration and development of oil, gas, and geothermal resources. Flake-like spalls (or particles) are often created during the TSD process. Our study in this paper focused on shape factor of flake-like spall in thermal spallation and its effects on settling and transport behavior. First, we conducted thermal spallation experiment and collected spalls. The shape factor of spall was obtained. The spalls with the shape factor in the range of 0.6 to 0.7 occupy the largest percentage. Based on that, a settling velocity model of single spall was obtained. We verified the model by comparison with the settling experiment results. After that, we investigated the effects of fluid and spalls properties on settling velocity. Finally, the effects of shape factor on spalls transport in drilling annulus were clarified by numerical simulation. In vertical section, when the shape factor is smaller, spalls can transport for longer distance and the spall distribution is more uniform. In the horizontal section, with the decrease of shape factor, the spalls have a longer transport length and lower spalls bed. All these results can be used for the optimization of drilling fluid. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:211 / 221
页数:11
相关论文
共 41 条
[1]  
Augustine C. R., 2009, THESIS
[2]  
Chapman S., 1970, THERMAL CONDUCTION D
[3]   Drag on discs and square plates in pseudoplastic polymer solutions [J].
Chhabra, RP ;
McKay, A ;
Wong, P .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (24) :5353-5356
[4]   SETTLING VELOCITY OF IRREGULARLY SHAPED PARTICLES [J].
CHIEN, SF .
SPE DRILLING & COMPLETION, 1994, 9 (04) :281-289
[5]  
Clift R., 1978, BUBBLES DROPS PARTIC, P70
[6]   Performance evaluation of a complete Lagrangian KTGF approach for dilute granular flow modelling [J].
Cloete, Schalk ;
Johansen, Stein Tore ;
Amini, Shahriar .
POWDER TECHNOLOGY, 2012, 226 :43-52
[7]   The analysis of the influence of pumice shape on its terminal velocity [J].
Dellino, P ;
Mele, D ;
Bonasia, R ;
Braia, G ;
La Volpe, L ;
Sulpizio, R .
GEOPHYSICAL RESEARCH LETTERS, 2005, 32 (21) :1-4
[8]  
Dey TN, 1985, GRC T, V9, P103
[9]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[10]   A new shape dependent drag correlation formula for non-spherical rough particles. Experiments and results [J].
Dioguardi, Fabio ;
Mele, Daniela .
POWDER TECHNOLOGY, 2015, 277 :222-230