Search Results - "Urieta, J.S."

Refine Results
  1. 1

    Supercritical carbon dioxide extraction of bioactive compounds from microalgae and volatile oils from aromatic plants by Palavra, A.M.F., Coelho, J.P., Barroso, J.G., Rauter, A.P., Fareleira, J.M.N.A., Mainar, A., Urieta, J.S., Nobre, B.P., Gouveia, L., Mendes, R.L., Cabral, J.M.S., Novais, J.M.

    Published in The Journal of supercritical fluids (01-12-2011)
    “…[Display omitted] ► Bioactive compounds from microalgae and volatile oils from aromatic plants were obtained by supercritical extraction. ► The extraction…”
    Get full text
    Journal Article
  2. 2

    Antioxidant Activities of the Supercritical and Conventional Satureja montana Extracts by Grosso, C, Oliveira, A.C, Mainar, A.M, Urieta, J.S, Barroso, J.G, Palavra, A.M.F

    Published in Journal of food science (01-11-2009)
    “…The antioxidant activities of the volatile and the nonvolatile fractions from Satureja montana obtained by supercritical fluid extraction (SFE) and by…”
    Get full text
    Journal Article
  3. 3

    Viscosities of the ternary mixture (1-butanol+ n-hexane+1-chlorobutane) at 298.15 K and 313.15 K by Domı́nguez, M, Santafé, J, López, M.C, Royo, F.M, Urieta, J.S

    Published in Fluid phase equilibria (15-10-1998)
    “…Viscosities of the ternary mixture (1-butanol+ n-hexane+1-chlorobutane) and the binary mixture ( n-hexane+1-chlorobutane) have been measured at 298.15 K and…”
    Get full text
    Journal Article
  4. 4

    Viscosities of the ternary mixture (cyclohexane+tetrahydrofuran+chlorocyclohexane) at 298.15 and 313.15 K by Gascón, I, Lafuente, C, Cea, P, Royo, F.M, Urieta, J.S

    Published in Fluid phase equilibria (06-10-1999)
    “…Viscosities of the ternary mixture (cyclohexane+tetrahydrofuran+chlorocyclohexane) and the binary mixtures (cyclohexane+tetrahydrofuran and…”
    Get full text
    Journal Article
  5. 5

    Viscosities of the ternary mixture (1-butanol + n-hexane + 1-butylamine) at the temperatures 298.15 and 313.15 K by Domínguez, M, Pardo, J, López, M.C, Royo, F.M, Urieta, J.S

    Published in Fluid phase equilibria (15-09-1996)
    “…Viscosities of the ternary mixture {1-butanol + n-hexane + 1-butylamine} and the binary mixtures {1-butanol + n-hexane}, {1-butanol + 1-butylamine} and {…”
    Get full text
    Journal Article
  6. 6

    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 by Domínguez, Magdalena, Rodríguez, Santiago, López, M. Carmen, Royo, Félix M, Urieta, José S

    “…Densities and viscosities at 298.15 K of the ternary mixtures 1-butanol + 1-chlorobutane + 1-butylamine and 2-methyl-1-propanol + 1-chlorobutane + 1-butylamine…”
    Get full text
    Journal Article
  7. 7

    Supercritical fluid extraction of wormwood ( Artemisia absinthium L.) by Martín, L., Mainar, A.M., González-Coloma, A., Burillo, J., Urieta, J.S.

    Published in The Journal of supercritical fluids (01-02-2011)
    “…[Display omitted] ▶ Supercritical fluid extraction of growth-controlled Artemisia absinthium L. optimized. ▶ Modelling of the extraction results carried out…”
    Get full text
    Journal Article
  8. 8

    Isobaric vapour-liquid equilibrium for the binary systems of 2-butanol with some halohydrocarbons at 40.0 and 101.3 kPa by Artigas, H., Lafuente, C., Tovar, C.A., Alvarez-Cerdeirina, C., Urieta, J.S.

    Published in Thermochimica acta (17-11-1997)
    “…Isobaric vapour-liquid equilibrium at 40.0 and 101.3 kPa is reported for the binary systems 2-butanol with chlorocyclohexane, chlorobenzene, bromocyclohexane…”
    Get full text
    Journal Article
  9. 9

    Vapor−Liquid Equilibria for the Binary Systems of 1-Butanol with Some Halohydrocarbons at 40.0 and 101.3 kPa by Artigas, Héctor, Lafuente, Carlos, Cea, Pilar, Royo, Félix M, Urieta, José S

    Published in Journal of chemical and engineering data (01-01-1997)
    “…Isobaric vapor−liquid equilibrium measurements at 40.0 and 101.3 kPa are reported for 1-butanol + chlorocyclohexane, + chlorobenzene, + bromocyclohexane, +…”
    Get full text
    Journal Article
  10. 10

    Vapour-liquid equilibrium for the binary systems of 2-methyl-1-propanol with some halohydrocarbons at 40.0 and 101.3 kPa by Artigas, H., Lafuente, C., López, M.C., Royo, F.M., Urieta, J.S.

    Published in Fluid phase equilibria (1997)
    “…A dynamic recirculating still was employed to measure isobaric vapour-liquid equilibrium at 40.0 and 101.3 kPa for the binary systems 2-methyl-1-propanol with…”
    Get full text
    Journal Article
  11. 11
  12. 12

    Supercritical fluid extraction of Spanish sage essential oil: Optimization of the process parameters and modelling by Langa, E., Porta, G. Della, Palavra, A.M.F., Urieta, J.S., Mainar, A.M.

    Published in The Journal of supercritical fluids (01-06-2009)
    “…The objective of the work was to optimize the extraction of Spanish sage essential oil by supercritical fluid (SFE). Different extraction conditions were…”
    Get full text
    Journal Article
  13. 13

    Rotenone coprecipitation with biodegradable polymers by supercritical assisted atomization by Martin, L., Liparoti, S., Della Porta, G., Adami, R., Marqués, J.L., Urieta, J.S., Mainar, A.M., Reverchon, E.

    Published in The Journal of supercritical fluids (01-09-2013)
    “…⿢Supercritical assisted atomization was used to produce rotenone⿿polymer composite microparticles.⿢Drying of emulsion by supercritical assisted…”
    Get full text
    Journal Article
  14. 14
  15. 15

    Isobaric VLE data for the binary systems dibromomethane with isomeric butanols at 40.0 and 101.3 kPa by Rodríguez, V., Lafuente, C., Santafé, J., Royo, F.M., Urieta, J.S.

    Published in Fluid phase equilibria (01-07-1995)
    “…Isobaric vapour-liquid equilibrium data at 40.0 and 101.3 kPa for the binary systems dibromomethane with 1-butanol, 2-butanol, 2-methyl-1-propanol and…”
    Get full text
    Journal Article
  16. 16

    Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure by Alfaro, P., Langa, E., Martínez-López, J.F., Urieta, J.S., Mainar, A.M.

    Published in The Journal of chemical thermodynamics (01-02-2010)
    “…This work presents the measurements of the density, speed of sound, refractive index and enthalpy of binary mixtures containing {1,8-cineole + 1-alkanol…”
    Get full text
    Journal Article
  17. 17

    Supercritical antisolvent fractionation of ryanodol from Persea indica by Martín, L., González-Coloma, A., Adami, R., Scognamiglio, M., Reverchon, E., Porta, G. Della, Urieta, J.S., Mainar, A.M.

    Published in The Journal of supercritical fluids (01-12-2011)
    “…[Display omitted] ► Supercritical antisolvent fractionation of Persea indica optimized. ► HPLC–MS quantification of ryanodol. ► Influence of density, mole…”
    Get full text
    Journal Article
  18. 18

    Mathematical modelling of supercritical CO 2 extraction of volatile oils from aromatic plants by Grosso, C., Coelho, J.P., Pessoa, F.L.P., Fareleira, J.M.N.A., Barroso, J.G., Urieta, J.S., Palavra, A.F., Sovová, H.

    Published in Chemical engineering science (2010)
    “…The modelling of the experimental data of the extraction of the volatile oil from six aromatic plants (coriander, fennel, savoury, winter savoury, cotton…”
    Get full text
    Journal Article
  19. 19

    Supercritical CO 2 extraction of Persea indica: Effect of extraction parameters, modelling and bioactivity of its extracts by Martín, L., González-Coloma, A., Díaz, C.E., Mainar, A.M., Urieta, J.S.

    “…[Display omitted] ► Supercritical fluid extraction of Persea indica, species with bioactive properties. ► Yields, compositions and bioactivity of different…”
    Get full text
    Journal Article
  20. 20

    The evolution of hyssop oil composition in the supercritical extraction curve by Langa, E., Cacho, J., Palavra, A.M.F., Burillo, J., Mainar, A.M., Urieta, J.S.

    Published in The Journal of supercritical fluids (01-05-2009)
    “…This work studies the evolution of hyssop oil composition along the CO 2 supercritical extraction curve, under changing extraction conditions, and compares the…”
    Get full text
    Journal Article