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Dimensionless groups for three-phase gravity drainage flow in porous media

Journal of petroleum science & engineering, 2001, Vol.29 (1), p.53-65

2001

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Formula for the conductivity of a two-component material based on the reciprocity theorem

Solid state communications, 1998-04, Vol.106 (4), p.183-186

1998

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Averaging methods for numerical simulations of flows through heterogeneous porous media

Transport in porous media, 1987-01, Vol.2 (3), p.241-267

1987

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Surfactant based mobility control. Progress in miscible flood enhanced oil recovery

Journal of colloid and interface science, 1989-06, Vol.130 (1), p.297-298

Dawe, R.A

1989

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Flow of Oil and Water Through Elastic Polymer Gels

Oil & gas science and technology, 2001-03, Vol.56 (2), p.145-152

2001

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Lower critical solution coexistence curve and physical properties (density, viscosity, surface tension, and interfacial tension) of 2,6-lutidine + water

Journal of chemical and engineering data, 1993-10, Vol.38 (4), p.516-519

1993

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Experimental enthalpy of C2H4(g) in the range 0.1 to 6.0 MPa and 273.15 to 373.15 K

The Journal of chemical thermodynamics, 1974-08, Vol.6 (8), p.743-749

1974

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Anisotropy in pore structure of porous media

Powder technology, 1995, Vol.85 (2), p.143-151

1995

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On the simulatneous determination of dispersion and nonlinear adsorption parameters from displacement tests by using numerical models and optimisation techniques

Advances in water resources, 1993, Vol.16 (2), p.127-135

1993

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Liquid—liquid equilibrium and extraction, a literature source book Parts A and B (physical sciences data 7)

The Chemical engineering journal, 1982-01, Vol.25 (2), p.234-235

Dawe, R.A.

1982

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Critical behavior of phase separating mixtures in porous media

Journal of colloid and interface science, 1987, Vol.117 (1), p.81-86

1987

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Viscous effects for miscible displacements in regular heterogeneous porous media

Chemical engineering research & design, 1987, Vol.65 (1), p.52-62

1987

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Surfactant based mobility control. Progress in miscible flood enhanced oil recovery: Edited by Duane H. Smith. Amer. Chem. Soc., Washington, DC, 1988. 449 pp. $94.95

Journal of Colloid And Interface Science, 1989, Vol.130 (1), p.297-298

Dawe, R.A

1989

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Liquid—liquid equilibrium and extraction, a literature source book Parts A and B (physical sciences data 7) : by J. Wisniak and A Tamir Published by Elsevier, Amsterdam: Part A: 1980. xxii + 1252 pp., price U.S.$ 160, ISBN 0-444-41909-8; Part B: 1981, xxii + 1438 pp., price U.S.$ 191, ISBN 0-444-42023-1

The Chemical Engineering Journal, 1982, Vol.25 (2), p.234-235

Dawe, R.A.

1982

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Experimental high-pressure enthalpies of N 2(g), CO 2(g), and C 2H 4(g). Correction of errors in previous papers

The Journal of chemical thermodynamics, 1975, Vol.7 (6), p.607-607

1975

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Experimental enthalpy of C 2H 4(g) in the range 0.1 to 6.0 MPa and 273.15 to 373.15 K

The Journal of chemical thermodynamics, 1974, Vol.6 (8), p.743-749

1974

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Experimental high pressure enthalpies of N 2(g) and CO 2(g) in the range 273.15 to 373.15 K

The Journal of chemical thermodynamics, 1974, Vol.6 (3), p.293-301

1974

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Effects of a vertical discontinuity in a porous medium on a plane convection plume at high Rayleigh numbers

International journal of heat and mass transfer, 1985-01, Vol.28 (4), p.789-794

1985

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Experimental high pressure enthalpies of N2(g) and CO2(g) in the range 273.15 to 373.15 K

The Journal of chemical thermodynamics, 1974-03, Vol.6 (3), p.293-301

1974

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Experimental high-pressure enthalpies of N2(g), CO2(g), and C2H4(g). Correction of errors in previous papers

The Journal of chemical thermodynamics, 1975-06, Vol.7 (6), p.607

1975

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Spontaneous emulsification aspect of enhanced oil recovery

Journal of chemical technology and biotechnology (1979), 1985-04, Vol.35A, p.132-144

1985

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A Joule-Thomson apparatus for the determination of the enthalpies of gases

The Journal of chemical thermodynamics, 1974, Vol.6 (1), p.65-74

1974

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Experimental enthalpies for gaseous hydrogen in the range 1 to 100 bar and 367.00 to 222.15 K

Physica, 1974-06, Vol.74 (2), p.435-440

1974

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Experimental enthalpies for gaseous air in the range 1 to 100 bar and 222.00 to 366.45 K

Physica, 1974-08, Vol.76 (1), p.167-171

1974

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Heavy component and fraction properties at low reduced temperatures for petroleum mixtures

The Chemical engineering journal, 1988, Vol.38 (3), p.195-204

1988

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Dimensionless groups for three-phase gravity drainage flow in porous media

Formula for the conductivity of a two-component material based on the reciprocity theorem

Averaging methods for numerical simulations of flows through heterogeneous porous media

Surfactant based mobility control. Progress in miscible flood enhanced oil recovery

Flow of Oil and Water Through Elastic Polymer Gels

Lower critical solution coexistence curve and physical properties (density, viscosity, surface tension, and interfacial tension) of 2,6-lutidine + water

Experimental enthalpy of C2H4(g) in the range 0.1 to 6.0 MPa and 273.15 to 373.15 K

Anisotropy in pore structure of porous media

On the simulatneous determination of dispersion and nonlinear adsorption parameters from displacement tests by using numerical models and optimisation techniques

Liquid—liquid equilibrium and extraction, a literature source book Parts A and B (physical sciences data 7)

Critical behavior of phase separating mixtures in porous media

Viscous effects for miscible displacements in regular heterogeneous porous media

Surfactant based mobility control. Progress in miscible flood enhanced oil recovery: Edited by Duane H. Smith. Amer. Chem. Soc., Washington, DC, 1988. 449 pp. $94.95

Experimental high-pressure enthalpies of N 2(g), CO 2(g), and C 2H 4(g). Correction of errors in previous papers

Experimental enthalpy of C 2H 4(g) in the range 0.1 to 6.0 MPa and 273.15 to 373.15 K

Experimental high pressure enthalpies of N 2(g) and CO 2(g) in the range 273.15 to 373.15 K

Effects of a vertical discontinuity in a porous medium on a plane convection plume at high Rayleigh numbers

Experimental high pressure enthalpies of N2(g) and CO2(g) in the range 273.15 to 373.15 K

Experimental high-pressure enthalpies of N2(g), CO2(g), and C2H4(g). Correction of errors in previous papers

Spontaneous emulsification aspect of enhanced oil recovery

A Joule-Thomson apparatus for the determination of the enthalpies of gases

Experimental enthalpies for gaseous hydrogen in the range 1 to 100 bar and 367.00 to 222.15 K

Experimental enthalpies for gaseous air in the range 1 to 100 bar and 222.00 to 366.45 K

Heavy component and fraction properties at low reduced temperatures for petroleum mixtures

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