Synthese enzymatique d’esters de sucre au départ d’huiles végétales; Destain, Jacqueline ; Lognay, Georges et alPoster (2005, October 14) Detailed reference viewed: 13 (2 ULg) Sugar esters lipase mediated synthesis from vegetable oilsDestain, Jacqueline ; ; Lognay, Georges et alScientific conference (2005, September 19) Detailed reference viewed: 19 (2 ULg) Sugar esters lipase mediated synthesis from vegetable oilsDestain, Jacqueline ; ; Lognay, Georges et alPoster (2005, September) Detailed reference viewed: 13 (2 ULg) Formulation solide de la lipase de Yarrowia lipolytica; Destain, Jacqueline ; Thonart, Philippe ![]() Poster (2005, March 05) Detailed reference viewed: 3 (0 ULg) Etude de la production de xylanases par Penicillium canescens 10-10c en culture solide; Destain, Jacqueline ; Thonart, Philippe ![]() Poster (2005, March 05) Detailed reference viewed: 11 (0 ULg) THE TWO-PHASE BIOREACTOR WATER / SILICON - OIL : PROSPECTS IN THE OFF- GAS TREATMENTAldric, Jean-Marc ; Destain, Jacqueline ; Thonart, Philippe ![]() in Applied Biochemistry and Biotechnology (2005), 122(1-3), 707-719 ABSTRACT: A research was carried out to develop a biphasic biological reactor able to clean the gas effluents polluted by volatile organic compounds (V.O.C). Initially, Rhodococcus erythropolis T 902.1 ... [more ▼] ABSTRACT: A research was carried out to develop a biphasic biological reactor able to clean the gas effluents polluted by volatile organic compounds (V.O.C). Initially, Rhodococcus erythropolis T 902.1 had been selected on the basis of its capacity to degrade isopropyl-benzene (IPB). The effect of gas flow and IPB concentration on the biodegadation of IPB was evaluated. The results show that the use of silicon-oil allows large quantities of IPB to be absorbed within the medium of biological abatement. On the other hand, the biodegradation rate is directly correlated to the inlet flow of IPB. Thus, the reactor presents interesting opportunities in the biological treatment of gas effluents. [less ▲] Detailed reference viewed: 105 (12 ULg) Involvement of hexokinase HXK1 in glucose catabolite repression of LIP2 encoding extracellular lipase in the yeast Yarrowia lipolyticaFickers, Patrick ; ; Destain, Jacqueline et alin Current Microbiology (2005), 50(3), 133-137 The yeast Yarrowia lipolytica produces an extracellular lipase encoded by the LIP2 gene. However, very little is known about the mechanisms controlling its expression, especially on glucose media. In this ... [more ▼] The yeast Yarrowia lipolytica produces an extracellular lipase encoded by the LIP2 gene. However, very little is known about the mechanisms controlling its expression, especially on glucose media. In this work, the involvement of hexokinase Hxk1 in the glucose catabolite repression of LIP2 was investigated in a lipase overproducing mutant less sensitive to glucose repression. This mutant has a reduced capacity to phosphorylate hexose compared with the wild-type strain, but no differences could be observed between the HXK1 sequences in the two isolates. This suggested that the reduced phosphorylating activity of the mutant strain probably resulted from a modification in the level of HXK1 expression. However, overexpression of the HXK1 gene in this mutant led to a decrease of both LIP2 induction and extracellular lipase activity, suggesting that the hexokinase is involved in the glucose catabolite repression of LIP2 in Y lipolytica. [less ▲] Detailed reference viewed: 19 (0 ULg) Selection of new over-producing derivatives for the improvement of extracellular lipase production by the non-conventional yeast Yarrowia lipolyticaFickers, Patrick ; ; et alin Journal of Biotechnology (2005), 115(4), 379-386 The non-conventional yeast Yarrowia lipolytica produces an extracellular lipase encoded by the LIP2 gene. Mutant strains with enhanced productivity were previously obtained either by chemical mutagenesis ... [more ▼] The non-conventional yeast Yarrowia lipolytica produces an extracellular lipase encoded by the LIP2 gene. Mutant strains with enhanced productivity were previously obtained either by chemical mutagenesis or genetic engineering. In this work, we used one of these mutants, named LgX64.81 to select new overproducing strains following by amplification of the LIP2 gene. We also developed a process for lipase production in bioreactors and compared lipase production levels in batch and fed-batch cultures. Batch culture led to a lipase production of 26 450 U ml(-1) in a media containing olive oil and tryptone as carbon and nitrogen sources. Feeding of a combination of tryptone and olive oil at the end of the exponential growth phase yielded to lipase activity of 158 246 U ml(-1) after 80 h of cultivation. In addition this production system developed for the extracellular lipase could also be applied for other heterologous protein production since we have demonstrated that LgX64.81 is an interesting alternative host strain. (C) 2004 Elsevier B.V. All rights reserved. [less ▲] Detailed reference viewed: 22 (0 ULg) The two-phase water/silicon oil bioreactor prospects in off-gas treatmentAldric, Jean-Marc ; Destain, Jacqueline ; Thonart, Philippe ![]() in Applied Biochemistry and Biotechnology (2005), 121(Spring), 707-719 Research was carried out to develop a biphasic biologic reactor able to clean the gas effluents polluted by volatile organic compounds. Initially, Rhodococcus erythropolis T 902.1 was selected on the ... [more ▼] Research was carried out to develop a biphasic biologic reactor able to clean the gas effluents polluted by volatile organic compounds. Initially, Rhodococcus erythropolis T 902.1 was selected on the basis of its capacity to degrade isopropylbenzene (IPB). The effect of gas flow and IPB concentration on the biodegadation of IPB was evaluated. The results show that the use of silicon oil allows large quantities of IPB to be absorbed within the medium of biologic abatement. On the other hand, the biodegradation rate was directly correlated to the inlet flow of IPB. Thus, the reactor presents interesting opportunities for the biologic treatment of gas effluents. [less ▲] Detailed reference viewed: 156 (6 ULg) Study of catalase production by an Aspergillus phoenicis mutant strain in date flour extract submerged cultures; ; Destain, Jacqueline et alin Biotechnologie, Agronomie, Société et Environnement = Biotechnology, Agronomy, Society and Environment [=BASE] (2005), 9(3), 173-178 The production of extracellular catalase in date flour submerged medium by a selected mutant Aspergillus phoenicis K30 (member of the Aspergillus niger group) was investigated. The strain was tested in ... [more ▼] The production of extracellular catalase in date flour submerged medium by a selected mutant Aspergillus phoenicis K30 (member of the Aspergillus niger group) was investigated. The strain was tested in 500 ml shake-flasks and in a 20 l bioreactor with date powder as a single carbon source. Extracellular catalase production reached 59 U ml-1 in both cases. This value is much greater than that of a wild-type strain (9.5 U ml-1). Microscopic examination showed that the extracellular catalase production was correlated with the ramified hyphals morphology in the external layer of the pellets. [less ▲] Detailed reference viewed: 20 (2 ULg) Expression of a synthetic gene encoding a Tribolium castaneum carboxylesterase in Pichia pastoris; ; et al in Protein Expression & Purification (2005), 42(2), 286-294 Detailed reference viewed: 19 (3 ULg) Structured mixing model for stirred bioreactors : an extension to the stochastic approachDelvigne, Frank ; Destain, Jacqueline ; Thonart, Philippe ![]() in Chemical Engineering Journal (2005) Detailed reference viewed: 12 (2 ULg) Estimation of bioreactor efficiency through structured hydrodynamic modeling case study of a Pichia pastoris fed-batch process.Delvigne, Frank ; El Mejdoub, Thami ; Destain, Jacqueline et alin Applied Biochemistry and Biotechnology (2005), 121-124 In this article, two theories are unified to investigate the effect of hydrodynamics on a specific bioprocess: the network-of-zones (NOZ) hydrodynamic structured modeling approach (developed by several ... [more ▼] In this article, two theories are unified to investigate the effect of hydrodynamics on a specific bioprocess: the network-of-zones (NOZ) hydrodynamic structured modeling approach (developed by several researchers but applied to only a few bioprocesses) and the effectiveness factor eta approach. Two process scales were investigated (20 and 500 L), and for each, hydrodynamics were quantified using an NOZ validated by homogeneity time measurements. Several impeller combinations inducing quite different hydrodynamics were tested at the 20-L scale. After this step, effectiveness factors were determined for each fermentation run. To achieve this, a perfectly mixed microbial kinetic model was evaluated by using simple Monod kinetics with a fed-batch mass balance. This methodology permitted determination of the effectiveness factor with more accuracy because of the relation with the perfect case deduced from the Monod kinetics. It appeared that for the small scale, eta decreased until reaching a value of approx 0.7 (30% from the ideal case) for the three impeller systems investigated. However, stirring systems that include hydrofoils seemed to maintain higher effectiveness factors during the course of the fermentation. This effect can be attributed to oxygen transfer performance or to homogenization efficiency exhibited by the hydrofoils. To distinguish the oxygen transfer from the homogenization component of the effectiveness factor, these phenomena were analyzed separately. After determining the evolution of etaO2 linked to oxygen transfer for each of the fermentation runs, the NOZ model was employed to quantify substrate gradient appearance. After this step, another effectiveness factor, etamix, related to mixing was defined. Consequently, it is possible to distinguish the relative importance of the mixing effect and oxygen transfer on a given bioprocess. The results have highlighted an important scale effect on the bioprocess that can be analyzed using the NOZ model. [less ▲] Detailed reference viewed: 38 (4 ULg) Bioreactor hydrodynamic effect on Escherichia coli physiology: experimental results and stochastic simulations.Delvigne, Frank ; Destain, Jacqueline ; Thonart, Philippe ![]() in Bioprocess and Biosystems Engineering (2005), 28(2), 131-7 A microorganism circulating in a bioreactor can be submitted to hydrodynamic conditions inducing a significant effect on its physiology. The mixing time exhibited by the stirred bioreactor and the ... [more ▼] A microorganism circulating in a bioreactor can be submitted to hydrodynamic conditions inducing a significant effect on its physiology. The mixing time exhibited by the stirred bioreactor and the circulation of microorganisms are both involved in this reacting system. The mixing component determines the intensity of the concentration gradient and the circulation component determines the way in which the microorganism is exposed to this gradient. These two components linked to the experimental evaluation of microbial physiology can be analysed by a structured stochastic model in the case of a partitioned or "scale-down" reactor (SDR). A stochastic model indeed enables to simulate the mixing process as well as the circulation of microorganisms in SDRs. The superimposition of mixing and circulation processes determines the concentration profile experienced by a microorganism in the reactor. In the present case, the glucose concentration experienced by Escherichia coli has been modelled during a fed-batch culture. In this context, the use of a stochastic hydrodynamic model has permitted to point out an interesting feed pulse retardant effect in the SDRs. Nevertheless, the metabolic response of E. coli is not easy to interpret because of the possible simultaneous developments of overflow metabolism and mixed acid fermentation induced by the strong glucose concentration in the reactor. [less ▲] Detailed reference viewed: 32 (2 ULg) Traitement biologique d’un effluent de l’industrie des olives; Aldric, Jean-Marc ; Destain, Jacqueline et alin Tribune de l'Eau (La) (2005) Detailed reference viewed: 49 (15 ULg) Utilization of methyloleate in production of microbial lipaseDestain, Jacqueline ; Fickers, Patrick ; et alin Applied Biochemistry and Biotechnology (2005), 121(Spring), 269-277 In this article, we report the development and optimization of an industrial culture medium for the production of extracellular lipase in the yeast Yarrowia lipolytica. Until now olive oil in combination ... [more ▼] In this article, we report the development and optimization of an industrial culture medium for the production of extracellular lipase in the yeast Yarrowia lipolytica. Until now olive oil in combination with glucose was used as the carbon source and inducer for the production of lipase. Our results demonstrate that methyloleate, a cheap hydrophobic compound, could efficiently substitute olive oil as the inducer and carbon source for lipase production. A new process of lipase production was developed yielding a twofold increase in the level of production compared with the levels in previous reports. [less ▲] Detailed reference viewed: 32 (0 ULg) Methyl Oleate Modulates Lip2 Expression In The Lipolytic Yeast Yarrowia Lipolytica; Destain, Jacqueline ; Thonart, Philippe ![]() in Biotechnology Letters (2005), 27(22), Detailed reference viewed: 6 (0 ULg) Immobilisation and adsorption techniques enhance the efficiency of an antilisterial strain of Lactobacillus curvatus THT 030550 in cold-smoked salmon.; ; Destain, Jacqueline et alPoster (2004, December 17) Detailed reference viewed: 9 (0 ULg) The two-phase Reactor Water/Silicon-Oil : Prospects in the off-gas treatment; Destain, Jacqueline ; Thonart, Philippe ![]() Poster (2004, May) Detailed reference viewed: 2 (0 ULg) Utilization of methyloleate in the production of Yarrowia lipolytica.Destain, Jacqueline ; ; et alPoster (2004, May) Detailed reference viewed: 5 (0 ULg) |
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