Supercritical fluid extraction for the determination of optimum oil recovery conditions

被引:40
|
作者
Al-Marzouqi, Ali H. [1 ]
Zekri, Abdulrazag Y. [1 ]
Jobe, Baboucarr [1 ]
Dowaidar, Ali [1 ]
机构
[1] United Arab Emirates Univ, Dept Chem & Petr Engn, Al Ain, U Arab Emirates
关键词
hydrocarbons; supercritical fluid extraction; extraction efficiency; compositional analysis of extracts and residues;
D O I
10.1016/j.petrol.2006.04.011
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
CO2 under supercritical (SC) conditions is a powerful solvent capable of extracting hydrocarbons from crude oil. The extraction capacity of CO2 is a function of pressure, temperature and composition of the crude oil. This paper presents the results of a laboratory study investigating the capacity of CO2 to extract hydrocarbons from an oil-saturated soil under a wide range of pressures and temperatures (80-120 bar for temperatures ranging from 40 to 60 degrees C and 200-300 bar for temperatures varying from 100 to 140 degrees C). The soil samples were collected from Sahel oil filed, which is near Bit Hasa oil field (Abu Dhabi, UAE) Where the crude oil was obtained from. The extracted oil from the SC CO2 process and the residual oil remaining in the soil sample were analyzed by gas chromatography to shed more light on the extraction phenomenon. Extraction efficiency of CO2 increased with pressure and decreased with temperature. Moreover, the amount of extracted heavy fractions increased with pressure for all temperatures. On the other hand, the amount of extracted heavy hydrocarbons decreased with temperature for the low pressure range (80-120 bar) and remained the same for the pressure range of 250-300 bar. The maximum extraction efficiency of CO2 was 72.4%, which was obtained at the highest pressure (300 bar) and a temperature of 100 degrees C. (c) 2006 Elsevier B.V All rights reserved.
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页码:37 / 47
页数:11
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