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Received January 15, 2014
Accepted August 24, 2014
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Asphaltene laboratory assessment of a heavy onshore reservoir during pressure, temperature and composition variations to predict asphaltene onset pressure
Department of Oil and Gas Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran 1Petroleum University of Technology, Tehran, Iran 2Memorial University of Newfoundland, Canada
Korean Journal of Chemical Engineering, February 2015, 32(2), 316-322(7), 10.1007/s11814-014-0245-6
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Abstract
An Iranian heavy oil reservoir recently encountered challenges in oil production rate, and further investigation has proven that asphaltene precipitation was the root cause of this problem. In addition, CO2 gas injection could be an appropriate remedy to enhance the production of heavy crudes. In this study, high pressure-high temperature asphaltene precipitation experiments were performed at different temperatures and pressures to investigate the asphaltene phase behavior during the natural depletion process and CO2 gas injection. Compositional modeling of experimental data predicted onset points at different temperatures which determine the zone of maximum probability of asphaltene precipitation for the studied heavy oil reservoir. Also, the effect of CO2 gas injection was investigated as a function of CO2 concentration and pressure. It was found that a CO2-oil ratio of 40% is the optimum for limiting precipitation to have the least formation damage and surface instrument contamination.
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Emadi A, Sohrabi M, Jamiolahmady M, Ireland S, Robertson G, Chem. Eng. Res. Des., 89(9A), 1783 (2011)
Holt T, Lindeberg E, Wessel-Berg D, Energy Procedia, 1, 4159 (2009)
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Soave G, Chem. Eng. Sci., 27, 1197 (1972)
Kawanaka S, Park SJ, Mansoori GA, SPE Res. Eng., 6, 185 (1991)
Cimino R, Correra S, Sacomani PA, Carniani C, SPE International Symposium on Oilfield Chemistry, San Antonio, Texas, USA, SPE 28993 (1995)
Thomas FB, Bennion DB, Bennion DW, Hunter BE, JCPT, 31, 22 (1992)
Nghiem LX, Hassam MS, Nutakki R, George AED, SPE Annual Technical Conference and Exhibition, Houston, Texas, USA, SPE 26642 (1993)
Nghiem LX, Coombe DA, SPE J., 2, 170 (1997)
Nghiem LX, Coombe DA, Farouq Ali SM, SPE Annual Technical Conference and Exhibition, New Orleans, USA, SPE 48996 (1998)
Leontaritis KJ, Mansoori GA, SPE International Symposium on Oilfield Chemistry, San Antonio, Texas, USA, SPE 16258 (1987)
Du JL, Zhang D, JPST, 22, 1023 (2004)
de Boer RB, Leerlooyer K, Eigner MRP, Van Bergen ARD, SPE Prod. Facilities J., 10, 55 (1995)
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Stankiewicz AB, Flannery MD, Fuex NA, Broze G, Couch JL, Dubey ST, Iyer SD, Ratulowski J, Westerich JT, AIChE Spring National Meeting, New Orleans, 47, 410 (2002)
Jamaluddin AKM, Creek J, Kabir CS, SPE Asia Pacific Improved Oil Recovery Conference, Kuala Lumpur, Malaysia, SPE 72154 (2001)
Standard Test Method for Determination of Asphaltenes (Heptane Insolubles) in Crude Petroleum and Petroleum Products, ASTM D6560-00, 143.1 (2000)
Peramanu S, Clarke PF, Pruden B, JPSE, 23, 133 (1999)