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Supercritical carbon dioxide extraction of bioactive compounds from microalgae and volatile oils from aromatic plants

The Journal of supercritical fluids, 2011-12, Vol.60, p.21-27

2011

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Antioxidant Activities of the Supercritical and Conventional Satureja montana Extracts

Journal of food science, 2009-11, Vol.74 (9), p.C713-C717

2009

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Rotenone coprecipitation with biodegradable polymers by supercritical assisted atomization

The Journal of supercritical fluids, 2013-09, Vol.81, p.48-54

2013

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Supercritical fluid extraction of wormwood ( Artemisia absinthium L.)

The Journal of supercritical fluids, 2011-02, Vol.56 (1), p.64-71

2011

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Mathematical modelling of supercritical CO2 extraction of volatile oils from aromatic plants

Chemical engineering science, 2010-06, Vol.65 (11), p.3579-3590

2010

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Supercritical CO2 extraction of Persea indica: Effect of extraction parameters, modelling and bioactivity of its extracts

The Journal of supercritical fluids, 2011-06, Vol.57 (2), p.120-128

2011

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Supercritical fluid extraction of Spanish sage essential oil: Optimization of the process parameters and modelling

The Journal of supercritical fluids, 2009-06, Vol.49 (2), p.174-181

2009

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Viscosities of the ternary mixture (cyclohexane+tetrahydrofuran+chlorocyclohexane) at 298.15 and 313.15 K

Fluid phase equilibria, 1999-10, Vol.164 (1), p.143-155

1999

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Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure

The Journal of chemical thermodynamics, 2010-02, Vol.42 (2), p.291-303

2010

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Viscosities of the ternary mixture (1-butanol+ n-hexane+1-chlorobutane) at 298.15 K and 313.15 K

Fluid phase equilibria, 1998-10, Vol.152 (1), p.133-148

1998

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Supercritical antisolvent fractionation of ryanodol from Persea indica

The Journal of supercritical fluids, 2011-12, Vol.60, p.16-20

2011

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Viscosities of the ternary mixture (1-butanol + n-hexane + 1-butylamine) at the temperatures 298.15 and 313.15 K

Fluid phase equilibria, 1996-09, Vol.124 (1), p.147-159

1996

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Densities and Viscosities of the Ternary Mixtures 1-Butanol + 1-Chlorobutane + 1-Butylamine and 2-Methyl-1-propanol + 1-Chlorobutane + 1-Butylamine at 298.15 K

Journal of chemical and engineering data, 1996, Vol.41 (1), p.37-42

1996

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Vapor−Liquid Equilibria for the Binary Systems of 1-Butanol with Some Halohydrocarbons at 40.0 and 101.3 kPa

Journal of chemical and engineering data, 1997-01, Vol.42 (1), p.132-136

1997

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Mathematical modelling of supercritical CO 2 extraction of volatile oils from aromatic plants

Chemical engineering science, 2010, Vol.65 (11), p.3579-3590

2010

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Supercritical CO 2 extraction of Persea indica: Effect of extraction parameters, modelling and bioactivity of its extracts

The Journal of supercritical fluids, 2011, Vol.57 (2), p.120-128

2011

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Vapour-liquid equilibrium for the binary systems of 2-methyl-1-propanol with some halohydrocarbons at 40.0 and 101.3 kPa

Fluid phase equilibria, 1997, Vol.134 (1), p.163-174

1997

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Isobaric vapour-liquid equilibrium for the binary systems of 2-butanol with some halohydrocarbons at 40.0 and 101.3 kPa

Thermochimica acta, 1997-11, Vol.306 (1), p.85-92

1997

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Isobaric VLE data for the binary systems dibromomethane with isomeric butanols at 40.0 and 101.3 kPa

Fluid phase equilibria, 1995-07, Vol.108 (1), p.185-198

1995

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The evolution of hyssop oil composition in the supercritical extraction curve

The Journal of supercritical fluids, 2009-05, Vol.49 (1), p.37-44

2009

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Supercritical Extraction and Separation of Antioxidants from Residues of the Wine Industry

Procedia engineering, 2012, Vol.42, p.1762-1766

2012

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Excess volumes of (1,2-dichloroethane or 1,2-dibromoethane + butan-1-ol or butan-2-ol or 2-methylpropan-1-ol or 2-methylpropan-2-ol) at the temperatures 298.15 K and 313.15 K

The Journal of chemical thermodynamics, 1994-11, Vol.26 (11), p.1173-1178

1994

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Supercritical carbon dioxide extraction of volatiles from Satureja fruticosa Béguinot

Flavour and fragrance journal, 2007-09, Vol.22 (5), p.438-442

2007

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Solubility of 13 non-polar gases (He, Ne, Ar, Kr, Xe, H 2, D 2, N 2, CH 4, C 2H 4, C 2H 6, CF 4 and SF 6) in 2-methyltetrahydrofuran at 273.15 to 303.15 K and 101.33 kPa partial pressure of gas

Fluid phase equilibria, 1993-01, Vol.87 (2), p.285-294

1993

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Excess molar volumes and vapour pressures of (benzene + each of several isomers of butanol)

The Journal of chemical thermodynamics, 1993, Vol.25 (5), p.679-685

1993

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Supercritical carbon dioxide extraction of bioactive compounds from microalgae and volatile oils from aromatic plants

Antioxidant Activities of the Supercritical and Conventional Satureja montana Extracts

Rotenone coprecipitation with biodegradable polymers by supercritical assisted atomization

Supercritical fluid extraction of wormwood ( Artemisia absinthium L.)

Mathematical modelling of supercritical CO2 extraction of volatile oils from aromatic plants

Supercritical CO2 extraction of Persea indica: Effect of extraction parameters, modelling and bioactivity of its extracts

Supercritical fluid extraction of Spanish sage essential oil: Optimization of the process parameters and modelling

Viscosities of the ternary mixture (cyclohexane+tetrahydrofuran+chlorocyclohexane) at 298.15 and 313.15 K

Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure

Viscosities of the ternary mixture (1-butanol+ n-hexane+1-chlorobutane) at 298.15 K and 313.15 K

Supercritical antisolvent fractionation of ryanodol from Persea indica

Viscosities of the ternary mixture (1-butanol + n-hexane + 1-butylamine) at the temperatures 298.15 and 313.15 K

Densities and Viscosities of the Ternary Mixtures 1-Butanol + 1-Chlorobutane + 1-Butylamine and 2-Methyl-1-propanol + 1-Chlorobutane + 1-Butylamine at 298.15 K

Vapor−Liquid Equilibria for the Binary Systems of 1-Butanol with Some Halohydrocarbons at 40.0 and 101.3 kPa

Mathematical modelling of supercritical CO 2 extraction of volatile oils from aromatic plants

Supercritical CO 2 extraction of Persea indica: Effect of extraction parameters, modelling and bioactivity of its extracts

Vapour-liquid equilibrium for the binary systems of 2-methyl-1-propanol with some halohydrocarbons at 40.0 and 101.3 kPa

Isobaric vapour-liquid equilibrium for the binary systems of 2-butanol with some halohydrocarbons at 40.0 and 101.3 kPa

Isobaric VLE data for the binary systems dibromomethane with isomeric butanols at 40.0 and 101.3 kPa

The evolution of hyssop oil composition in the supercritical extraction curve

Supercritical Extraction and Separation of Antioxidants from Residues of the Wine Industry

Excess volumes of (1,2-dichloroethane or 1,2-dibromoethane + butan-1-ol or butan-2-ol or 2-methylpropan-1-ol or 2-methylpropan-2-ol) at the temperatures 298.15 K and 313.15 K

Supercritical carbon dioxide extraction of volatiles from Satureja fruticosa Béguinot

Solubility of 13 non-polar gases (He, Ne, Ar, Kr, Xe, H 2, D 2, N 2, CH 4, C 2H 4, C 2H 6, CF 4 and SF 6) in 2-methyltetrahydrofuran at 273.15 to 303.15 K and 101.33 kPa partial pressure of gas

Excess molar volumes and vapour pressures of (benzene + each of several isomers of butanol)

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