References of "Thonart, Philippe"
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See detailA 5,6-Dihydro-Isopyoverdin From Azomonas Macrocytogenes
Michalke, R.; Taraz, K.; Budzikiewicz, H. et al

in Zeitschrift Fur Naturforschung C-A Journal of Biosciences (1997), 52(11-12),

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See detailThe Degradation Of L-Tyrosine To Phenol And Benzoate In Pig Manure - The Role Of 4-Hydroxy-Benzoate
Antoine, P.; Taillieu, X.; Thonart, Philippe ULg

in Applied Biochemistry and Biotechnology (1997), 63-5

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See detailLipase from Yarrowia lipolytica.
Destain, Jacqueline ULg; Weber, D.; Thonart, Philippe ULg

in Mededelingen van de Faculteit Landbouwkundige en Toegepaste Biologische Wetenschappen (Rijksuniversiteit te Gent) (1997), 62(4a),

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See detailImprovement Of Lipase Production From Yarrowia Lipolytica
Destain, Jacqueline ULg; Weber, D.; Thonart, Philippe ULg

in Biotechnology Letters (1997), 19(2),

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See detailSurface-active properties of surfactin iturin A mixtures produced by Bacillus subtilis
Razafindralambo, Hary ULg; Popineau, Yves; Deleu, Magali ULg et al

in Langmuir (1997), 13(23), 6026-6031

Surface-active properties including dynamic adsorption, monolayer stability, micelle forming capacity, and foaming aptitudes of surfactin-C-15/iturin A-C-15 mixtures were studied. Surfactin-C-15 and ... [more ▼]

Surface-active properties including dynamic adsorption, monolayer stability, micelle forming capacity, and foaming aptitudes of surfactin-C-15/iturin A-C-15 mixtures were studied. Surfactin-C-15 and iturin A-C-15 molecules interact in synergism on the most surface-active properties evaluated at 20 degrees C at the air-water interface and in aqueous solution (pH 8.0). The synergism is positive on the adsorption effect, monolayer stability, foam density, and liquid stability in foam, whereas it is negative on the adsorption rate. No synergism occurs an micelle forming capacity, but surfactin-C-15 and iturin A-C-15 form mixed micelles when the solution contains a low proportion of surfactin-C-15.ses the synergistic effect is maximum when surfactin-C-15 and iturin A-C-15 molecules are mixed in a 2:3 ratio. This is attributed to the surfactin/iturin A complex formation resulting from specific interactions among two surfactin-C-15 molecules and three iturin A-C-15 molecules. A model of such a complex formation is proposed. [less ▲]

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See detailLes bacs à graisse : une solution aux problèmes des matières grasses pour les PME
Thonart, Philippe ULg; Destain, Jacqueline ULg; Zgoulli, S. et al

in Tribune de l'Eau (La) (1997), 586/2

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See detailLa problématique de la matière grasse : aspects théoriques
Thonart, Philippe ULg; Destain, Jacqueline ULg; Antoine, P. et al

in Tribune de l'Eau (La) (1997), 586/2

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See detailEtude comparative de la décontamination microbiologique, avec ou sans Biosol, de terres d'excavation contaminées par des hydrocarbures
Verstaete, W.; Van Eyck, L.; Thonart, Philippe ULg et al

in Tribune de l'Eau (La) (1997), 587/3

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See detailEffect of drying and long term conservation on bioremediation properties of Rhodococcus erythropolis
Weekers, F.; Jacques, P.; Springael, D. et al

in Mededelingen van de Faculteit Landbouwkundige en Toegepaste Biologische Wetenschappen (Rijksuniversiteit te Gent) (1997), 62/4b

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See detailProduction et conditionnement des bactéries lactiques isolées du Lben Tunisien.
Hamdi, M.; Cornelius, C.; Ben Amor, K. et al

Poster (1996, November)

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See detailEvaluation des potentialités aromatisantes des lactocoques isolées du Lben Tunisien.
Mahjoub, A.; Ben Amor, K.; Cornelius, C. et al

Poster (1996, November)

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See detailEvidence and purification of a novel bacterial dehydrogenase : a vanillin : NAD (P) oxydoreductase.
Bare, G.; Moukil, M.; Swiatkowski, Th. et al

Poster (1996, August)

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See detailThe degradation of L-tyrosine to phenol and benzoate in pig manure. The role of 4-hydroxy-benzoate
Antoine, P.; Taillieu, X.; Verstraete, W. et al

Poster (1996, May)

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See detailStudy on the production of a xylanolytic complex from Penicillium canescens 10.10c .
Gaspar, A.; Roques, G.; Cosson, T. et al

Poster (1996, May)

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See detailSelection of hydrocarbon degrading bacteria based on drying resistance criteria.
Jacques, Ph.; Weekers, F.; Bastiaens, L. et al

Poster (1996, May)

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See detailProduction of sulfur from gypsum as an industrial byproduct
Hiligsmann, Serge ULg; Deswaef, Sophie; Taillieu, Xavier et al

in Applied Biochemistry and Biotechnology (1996), 57-8

Biological sulfate reduction was investigated at the bench and pilot scales in order to determine optimum culture conditions. Efficient strains of sulfate-reducing bacteria (SRB) were selected by ... [more ▼]

Biological sulfate reduction was investigated at the bench and pilot scales in order to determine optimum culture conditions. Efficient strains of sulfate-reducing bacteria (SRB) were selected by classical microbiological methods and by mutagenesis. Improvement factors, including stripping, scale-up, sulfate,and organic substrate concentrations, have been studied in batch bioreactors. Two types of pilot-scale bioreactors have been adopted, the first being completely mixed with free cells and the second having two stages with immobilized cells on a fixed bed. An overall bioconversion capacity of 11 kg/m(3) . d of gypsum and 1.2 kg/m(3) . d of dissolved organic carbon has been achieved in the two-stage bioreactor. [less ▲]

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See detailTreatment of gypsum waste in a two stage anaerobic reactor
Deswaef, Sophie; Salmon, Thierry ULg; Hiligsmann, Serge ULg et al

in Water Science & Technology (1996), 34(5-6), 367-374

The reduction of high concentrations of gypsum (up to 110 kg/m(3)) is investigated in a two stage immobilised cell bioreactor. The first stage is mainly colonised by a consortium of acidogenic bacteria ... [more ▼]

The reduction of high concentrations of gypsum (up to 110 kg/m(3)) is investigated in a two stage immobilised cell bioreactor. The first stage is mainly colonised by a consortium of acidogenic bacteria and sulphate reducing bacteria oxidising volatile fatty acids with more than 2 carbons (mainly, butyrate and propionate). The gypsum consumption rate is rather high (ii kg/m(3).day). Most of acetate remains unconverted in this first stage. It is partially converted in the second stage (residence time : 12 days) which is predominantly colonised by acetate oxidising bacteria The gypsum consumption rate is much lower than in the first stage : 3 kg/m(3).day. With both stages, it is possible to reach an almost complete conversion of gypsum with an overall capacity of 6.1 kg gypsum/m(3).day. We propose also a very simple model to describe the different transformation rates. It allows us to clearly identify the activity levels of the different types of sulphate reducing bacteria in both stages. Copyright (C) 1996 IAWQ. [less ▲]

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