Use of Carbon Dioxide in Enhanced Oil Recovery
- 11 May 1984
- journal article
- research article
- Published by American Association for the Advancement of Science (AAAS) in Science
- Vol. 224 (4649) , 563-569
- https://doi.org/10.1126/science.224.4649.563
Abstract
Large volumes of oil will remain in U.S. oil reservoirs when standard recovery methods have been completed. Supercritical carbon dioxide can be used to recover part of that remaining oil. If carbon dioxide is dense enough, it extracts hydrocarbons from the oil to make a mixture miscible with crude oil. Such a mixture can recover 95 percent of the oil in controlled laboratory flow settings. Heterogeneity of reservoir rocks and the low viscosity of carbon dioxide reduce the fraction of oil recovered in projects to lower but still significant levels. With the construction of three pipelines to carry naturally occurring carbon dioxide from Colorado and New Mexico to Permian basin oil fields, large-scale implementation of enhanced oil recovery by carbon dioxide flooding is now beginning.Keywords
This publication has 20 references indexed in Scilit:
- Interpretation of Pressure-Composition Phase Diagrams for CO2/Crude-Oil SystemsSociety of Petroleum Engineers Journal, 1984
- Supercritical Fluid ChromatographyScience, 1983
- Effects of Mobile Water on Multiple-Contact Miscible Gas DisplacementsSociety of Petroleum Engineers Journal, 1983
- Equilibrium Phase Compositions of CO2/Crude Oil Mixtures—Part 2: Comparison of Continuous Multiple-Contact and Slim-Tube Displacement TestsSociety of Petroleum Engineers Journal, 1983
- Effect of Oil Composition on Miscible-Type Displacement by Carbon DioxideSociety of Petroleum Engineers Journal, 1982
- Phase Behavior of CO2 and Crude Oil in Low-Temperature ReservoirsSociety of Petroleum Engineers Journal, 1981
- Extraction with supercritical gasesChemical Engineering Science, 1981
- Phase equilibria and critical phenomena in fluid mixtures of carbon dioxide + 2,6,10,15,19,23-hexamethyltetracosane up to 423 K and 100 MPaThe Journal of Chemical Thermodynamics, 1975
- Phasengleichgewichte und kritische Erscheinungen in binären Mischsystemen bis 1500 bar, CO2mit n‐Octan, n‐Undecan, n‐Tridecan und n‐HexadecanChemie Ingenieur Technik - CIT, 1967
- Phase relations of miscible displacement in oil recoveryAIChE Journal, 1961