Determination of gas dispersion in vapor extraction of heavy oil and bitumen

被引:24
|
作者
Kapadia, Ronak A.
Upreti, Simant R. [1 ]
Lohi, Ali
Chatzis, Ioannis
机构
[1] Ryerson Univ, Dept Chem Engn, Toronto, ON M5B 2K3, Canada
[2] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
gas dispersion; vapor extraction; heavy oil and bitumen; modeling vapex front; enhanced oil recovery;
D O I
10.1016/j.petrol.2006.01.001
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 work, a mathematical model is developed and simulated to determine gas dispersion along with solubility during the vapor extraction (Vapex) of live oil from a laboratory scale physical model. The physical model is a rectangular block of homogenous porous medium saturated with heavy oil and bitumen. At a given temperature and pressure, the block is initially exposed on its side to a solvent gas, which diffuses into the medium and gets absorbed. The absorption of gas reduces the viscosity of heavy oil and bitumen causing it to drain under gravity. The low-viscosity "live oil" is produced at the bottom of the porous block. The production of live oil with time is accompanied by the shrinkage of oil in the block as well as its increased exposure to gas from top. These phenomena of Vapex are described by the mathematical model, which is used to calculate live oil production with various values of gas solubility and dispersion. Their optimal values are determined for the vapor extraction of Cold Lake bitumen with butane by matching calculated live oil production with its experimental values published earlier. (C) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:214 / 222
页数:9
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