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1-18 of 18
Keywords: liquid phase
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Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 25 (06): 865–874.
Paper Number: SPE-12708-PA
Published: 01 December 1985
... methods saturation liquid phase co 2 sandpack pvt measurement molecular weight oil pi displacement solid phase deposition oil flow oil recovery apparatus crude oil oil aromaticity petroleum engineer journal phase behavior Several reports suggest that oil aromaticity affects the CO...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 25 (02): 235–254.
Paper Number: SPE-10268-PA
Published: 01 April 1985
... is to find: (1) the vapor-liquid spinodal and critical point and then a succession of coexisting equilibrium vapor and liquid phase densities in each of the three single-component systems; (2) the vapor-liquid binodal and tie lines in each of the three binary systems, in each case starting at a pressure...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 24 (05): 485–497.
Paper Number: SPE-11125-PA
Published: 01 October 1984
.... Phase diagrams for CO 2 /crude-oil systems can be quite complex, however, since under some conditions such mixtures can form a liquid and a vapor, two liquid phases, or two liquids and a vapor in equilibrium. This paper examines P-X diagrams for two ternary systems, CO 2 /propane/hexadecane and CO 2...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 24 (01): 87–96.
Paper Number: SPE-11126-PA
Published: 01 February 1984
...Rasmus Risnes; Vilgeir Dalen Modeling of reservoir processes like gas miscible flooding may require consideration of phase equilibrium between multiple liquid phases. Under certain conditions two hydrocarbon liquid phases may form; one may also want to account for mass transfer between...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 23 (04): 595–601.
Paper Number: SPE-8812-PA
Published: 01 August 1983
... and 11 100 kPa ( Fig. 2 ). At pressures above this multiple-phase region, two liquid phases exist in equilibrium, and below the multiple-phase region, a liquid and vapor coexist. To obtain a direct comparison between static single-contact mixtures and dynamic multiple-contact mixtures. Oil A from...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 23 (02): 281–291.
Paper Number: SPE-10725-PA
Published: 01 April 1983
... 2 -rich liquid phase can contain as much as 30 wt% hydrocarbons and show that a CO 2 -rich vapor phase at the same conditions extracts hydrocarbons less efficiently. Pseudoternary phase diagrams are presented that summarize the results of the detailed phase composition measurements. Results of slim...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 23 (02): 339–348.
Paper Number: SPE-10273-PA
Published: 01 April 1983
... injection vapor phase slug displacement process reservoir model nitrogen gas injection method petroleum engineer journal liquid phase Previous researchers 1 – 9 have investigated, experimentally and theoretically, the problem of predicting the effects of dry-gas injection into a reservoir...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 22 (06): 805–815.
Paper Number: SPE-9785-PA
Published: 01 December 1982
... oil system. Displacements requiring the greatest length to develop miscibility were at pressures where single-contact mixtures of CO 2 and Levelland oil form two liquid phases. A companion paper 10 demonstrates the use of the analytical technique developed in this study to obtain process data from...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 21 (04): 480–492.
Paper Number: SPE-8813-PA
Published: 01 August 1981
... that L/L and L/L/V equilibria will occur for CO 2 /crude-oil mixtures at temperatures below about 120° F (49 °C) and that development of miscibility occurs by extraction of hydrocarbons from the oil into a CO 2 -rich liquid phase in such systems. 13 2 1980 26 5 1981 20 2 1981 1 8...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 19 (04): 203–210.
Paper Number: SPE-6722-PA
Published: 01 August 1979
... liquid phases and avapor phase) exist for some fluid mixtures (somemixtures of reservoir oil and CO2 or rich gas) overlimited ranges of pressure and temperature. These experimental results indicate that multiple phasesmay occur in the reservoir when enhancedoilrecovery methods are used. To predict...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 18 (01): 20–26.
Paper Number: SPE-6387-PA
Published: 01 February 1978
... of the gas and liquid phases were equal) properties of the gas and liquid phases were equal) is 2,570 psia and 60-mol percent CO2. OIL B Eight mixtures of CO2 and Reservoir Oil B also were prepared and studied in the visual cell at 255 degrees F. CO2 concentrations for these mixtures were 0, 20, 40, 55, 65...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 8 (03): 281–292.
Paper Number: SPE-2051-PA
Published: 01 September 1968
... Chappelear accuracy Retrograde Condensation shape factor PVT measurement methane calculation composition reference substance experimental data Upstream Oil & Gas liquid phase condensation correlation procedure reservoir fluid A Corresponding States Correlation for Calculating Gas...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 7 (02): 125–135.
Paper Number: SPE-1499-PA
Published: 01 June 1967
...C. Kenneth Eilerts; Eudora F. Sumner A partial differential equation was developed and programed to compute the cumulation and flow of the liquid phase of a gas-condensate fluid. It was found that such cumulation near the wellbore may attain saturations permitting liquid flow within periods...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 7 (02): 113–124.
Paper Number: SPE-1478-PA
Published: 01 June 1967
... of the rock near the wellbore with respect to non-Darcy flow of gas in the presence of a liquid phase. Laboratory techniques used to obtain them from special measurements on cores have been briefly ~escribed; 10 a detailed presentation of these techniques is given in the Appendix] 1 An examination...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 7 (01): 11–19.
Paper Number: SPE-1498-PA
Published: 01 March 1967
... core holder condensate 502 fog 0 berea 404 mobility-saturation relationship saturation permeability liquid phase diameter apparent velocity mobility liquid saturation Effect of Saturation on Mobility of Low Liquid-Vapor Ratio Fluids JERRY D. HAM JUNIOR MEMBER AIME C. KENNETH EILERTS...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 5 (01): 37–44.
Paper Number: SPE-962-PA
Published: 01 March 1965
... both the thermodynamical properties of the fluid and the mechanical properties of the reservoir. The fluid properties, reflecting the PVT relationship of the gaseous and liquid phases, are expressed by using the partial specific masses of the two main separator products in these phases. The flow...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 4 (02): 85–95.
Paper Number: SPE-680-PA
Published: 01 June 1964
... matrix itself, a gas phase and a "combined liquid phase" which is a combination of two immiscible liquid phases - namely, an oil phase and a water phase. The oil present in the reservoir is assumed to consist of three fractions, a noncondensable gas, a nondistillable residuum, and a vaporizable oil...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 1 (03): 137–141.
Paper Number: SPE-33-PA
Published: 01 September 1961
...Lowell Stroud; Will E. De Vaney; John E. Miller During a recent phase study of a natural gas, two stable equilibrium liquid phases were observed at temperatures below –200F and pressures above 200 psi. This paper reviews the published literature on the occurrence of multiple equilibrium liquid...