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The Viscosity of Carbon Dioxide

Journal of physical and chemical reference data, 1998-01, Vol.27 (1), p.31-44

1998

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Densities and bubble points of binary mixtures of carbon dioxide and n-heptane and ternary mixtures of n-butane, n-heptane and n-hexadecane

Fluid phase equilibria, 2001-07, Vol.185 (1), p.349-358

2001

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Densities and bubble points of ternary mixtures of methane, n-butane and n-hexadecane and quaternary mixtures of methane, n-butane, n-heptane and n-hexadecane

Fluid phase equilibria, 2001-06, Vol.182 (1), p.111-119

2001

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Phase behaviour and density of (methane+ n-butane)

Fluid phase equilibria, 1999-09, Vol.163 (1), p.139-156

1999

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Densities of (water + carbon dioxide) in the temperature range 415 K to 700 K and pressures up to 35 MPa

The Journal of chemical thermodynamics, 1996-04, Vol.28 (4), p.433-446

1996

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Phase behaviour and density of model reservoir fluids at high temperature and pressure

Fluid phase equilibria, 1999-06, Vol.158, p.783-794

1999

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5.1.4 PROPERTIES OF PURE FLUIDS: VISCOSITY OF PURE FLUID

Heat exchanger design update, 2006, Vol.13 (2), p.17

Fenghour, A.

2006

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5.2.3 PROPERTIES OF MIXTURES OF FLUIDS: VISCOSITY OF FLUID MIXTURES

Heat exchanger design update, 2006, Vol.13 (3), p.9

Fenghour, A.

2006

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The Viscosity of Ammonia

Journal of physical and chemical reference data, 1995-09, Vol.24 (5), p.1649-1667

1995

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5.1.5 Surface tension of pure liquids

Heat exchanger design update, 2005, Vol.12 (2), p.4

Fenghour, A.

2005

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5.2.4 Surface tension of liquid mixtures

Heat exchanger design update, 2005, Vol.12 (2), p.4

Fenghour, A.

2005

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Densities of (water + methane) in the temperature range 430 K to 699 K and at pressures up to 30 MPa

The Journal of chemical thermodynamics, 1996-04, Vol.28 (4), p.447-458

1996

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Amount-of-substance density of CO2at temperatures from 329 K to 698 K and pressures up to 34 MPa

The Journal of chemical thermodynamics, 1995-02, Vol.27 (2), p.219-223

1995

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The excess enthalpy of (steam + ethane) in the supercritical region up to T= 699.4 K and p = 25.3 MPa

International journal of thermophysics, 2000, Vol.21 (1), p.85-93

2000

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The excess enthalpy of (steam + carbon dioxide) in the supercritical region up to T = 698.2 K and p = 25.5 MPa

The Journal of chemical thermodynamics, 1997, Vol.29 (11), p.1253-1260

1997

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Automated isochoric apparatus for the measurement of density of fluid mixtures at temperatures from 298.15 K to 773.15 K and pressures up to 40 MPa: results for helium and for nitrogen

The Journal of chemical thermodynamics, 1993-07, Vol.25 (7), p.831-845

1993

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5.1.3 PROPERTIES OF PURE FLUIDS: VAPOUR PRESSURE, ENTHALPIES OF VAPORISATION AND BOILING AND MELTING POINTS OF PURE FLUIDS

Heat exchanger design update, 2002, Vol.9 (3-4), p.13

Fenghour, A.

2002

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Two-fluid corresponding states model: a new mixing rule approximation

Fluid phase equilibria, 1996-10, Vol.125 (1), p.33-43

1996

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5.1.1. PROPERTIES OF PURE FLUIDS: CRITICAL PROPERTIES OF PURE COMPONENTS

Heat exchanger design update, 2001, Vol.8 (2), p.6

Fenghour, A.

2001

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5.2.7. PROPERTIES OF MIXTURES OF FLUID: CRTTICAL PROPERTIES OF MIXTURES

Heat exchanger design update, 2001, Vol.8 (2), p.9

Fenghour, A.

2001

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5.2.1 PROPERTIES OF MIXTURES OF FLUIDS: Density of fluid mixtures

Heat exchanger design update, 2001, Vol.8 (4), p.8

Fenghour, A.

2001

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5.1.2 PROPERTIES OF PURE FLUIDS: Density of pure fluids

Heat exchanger design update, 2001, Vol.8 (3), p.24

Fenghour, A.

2001

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Amount-of-substance density of CH4at temperatures from 322.5 K to 700 K and pressures up to 35 MPa

The Journal of chemical thermodynamics, 1995-02, Vol.27 (2), p.213-218

1995

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Densities of (water + nitrogen) in the temperature range 533 K to 703 K and at pressures up to 31 MPa

The Journal of chemical thermodynamics, 1993-09, Vol.25 (9), p.1151-1159

1993

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The excess enthalpy of (steam + carbon dioxide) in the supercritical region up toT= 698.2 K andp= 25.5 MPa

The Journal of chemical thermodynamics, 1997-11, Vol.29 (11), p.1253-1260

1997

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The Viscosity of Carbon Dioxide

Densities and bubble points of binary mixtures of carbon dioxide and n-heptane and ternary mixtures of n-butane, n-heptane and n-hexadecane

Densities and bubble points of ternary mixtures of methane, n-butane and n-hexadecane and quaternary mixtures of methane, n-butane, n-heptane and n-hexadecane

Phase behaviour and density of (methane+ n-butane)

Densities of (water + carbon dioxide) in the temperature range 415 K to 700 K and pressures up to 35 MPa

Phase behaviour and density of model reservoir fluids at high temperature and pressure

5.1.4 PROPERTIES OF PURE FLUIDS: VISCOSITY OF PURE FLUID

5.2.3 PROPERTIES OF MIXTURES OF FLUIDS: VISCOSITY OF FLUID MIXTURES

The Viscosity of Ammonia

5.1.5 Surface tension of pure liquids

5.2.4 Surface tension of liquid mixtures

Densities of (water + methane) in the temperature range 430 K to 699 K and at pressures up to 30 MPa

Amount-of-substance density of CO2at temperatures from 329 K to 698 K and pressures up to 34 MPa

The excess enthalpy of (steam + ethane) in the supercritical region up to T= 699.4 K and p = 25.3 MPa

The excess enthalpy of (steam + carbon dioxide) in the supercritical region up to T = 698.2 K and p = 25.5 MPa

Automated isochoric apparatus for the measurement of density of fluid mixtures at temperatures from 298.15 K to 773.15 K and pressures up to 40 MPa: results for helium and for nitrogen

5.1.3 PROPERTIES OF PURE FLUIDS: VAPOUR PRESSURE, ENTHALPIES OF VAPORISATION AND BOILING AND MELTING POINTS OF PURE FLUIDS

Two-fluid corresponding states model: a new mixing rule approximation

5.1.1. PROPERTIES OF PURE FLUIDS: CRITICAL PROPERTIES OF PURE COMPONENTS

5.2.7. PROPERTIES OF MIXTURES OF FLUID: CRTTICAL PROPERTIES OF MIXTURES

5.2.1 PROPERTIES OF MIXTURES OF FLUIDS: Density of fluid mixtures

5.1.2 PROPERTIES OF PURE FLUIDS: Density of pure fluids

Amount-of-substance density of CH4at temperatures from 322.5 K to 700 K and pressures up to 35 MPa

Densities of (water + nitrogen) in the temperature range 533 K to 703 K and at pressures up to 31 MPa

The excess enthalpy of (steam + carbon dioxide) in the supercritical region up toT= 698.2 K andp= 25.5 MPa

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