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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
1

Foaming in Apple Wine

Mårtensson, Ellinor January 2010 (has links)
<p>At Kiviks Musteri AB, situated in the southeast part of Scania, a wide variety of products based on fruits and berries, are produced. One of these products is base apple wine, which is used for the production of cider and mulled wine and also is sold to other producers of cider. A foaming problem has occurred at some customers when the cider is bottled, and this problem has been traced to the base wine. The aim of this paper is to investigate what causes the foaming and how the foaming is affected by the clarifying agents used during the production of the wine. An investigation whether silica based antifoaming agents might be a solution of the problem will be performed. During the work fermentations, clarification and foaming tests will be performed in laboratory scale in Kivik. Tests with four different silica based antifoaming compounds are carried out and on these samples the surface tension and viscosity are measured to see how these factors correlate with the foaming when antifoaming agents are added to the wine. What is more, fermentations with a new yeast type and fermentations with less fruit are made to investigate if this could give better foaming properties in the wine.</p><p>The tests showed that it is probably proteins that are the main cause of the foaming, but an increase of the amount of bentonite, the clarifying agent reducing protein content in the wine, is not possible since this causes too much sediment. Antifoaming agents gave reduced foaming times, which were at an acceptable level, but when the wine was mixed to cider base and filtered the effect was lost. No significant differences were observed between the four antifoaming compounds. The test with the new yeast type gave no positive results when it came to foaming. The test with less fruit showed a decrease in foaming but not sufficient enough.</p>
2

Part 1: Employing conventional defoamer emulsions to enhance the flotation removal of flexographic news inks,

DeLozier, Greg. January 2003 (has links)
Thesis (Ph. D.)--Institute of Paper Science and Technology, Georgia Institute of Technology, 2003. / Includes bibliography.
3

Foaming in Apple Wine

Mårtensson, Ellinor January 2010 (has links)
At Kiviks Musteri AB, situated in the southeast part of Scania, a wide variety of products based on fruits and berries, are produced. One of these products is base apple wine, which is used for the production of cider and mulled wine and also is sold to other producers of cider. A foaming problem has occurred at some customers when the cider is bottled, and this problem has been traced to the base wine. The aim of this paper is to investigate what causes the foaming and how the foaming is affected by the clarifying agents used during the production of the wine. An investigation whether silica based antifoaming agents might be a solution of the problem will be performed. During the work fermentations, clarification and foaming tests will be performed in laboratory scale in Kivik. Tests with four different silica based antifoaming compounds are carried out and on these samples the surface tension and viscosity are measured to see how these factors correlate with the foaming when antifoaming agents are added to the wine. What is more, fermentations with a new yeast type and fermentations with less fruit are made to investigate if this could give better foaming properties in the wine. The tests showed that it is probably proteins that are the main cause of the foaming, but an increase of the amount of bentonite, the clarifying agent reducing protein content in the wine, is not possible since this causes too much sediment. Antifoaming agents gave reduced foaming times, which were at an acceptable level, but when the wine was mixed to cider base and filtered the effect was lost. No significant differences were observed between the four antifoaming compounds. The test with the new yeast type gave no positive results when it came to foaming. The test with less fruit showed a decrease in foaming but not sufficient enough.
4

Développement d'un système "générique" de production d'anticorps murins et recombinants par bioingénierie / Development of a generic system for the production of murine and recombinant antibodies by bioengineering

Yakoub, Walid 25 October 2017 (has links)
Les anticorps monoclonaux (AcM) sont des protéines ayant une reconnaissance antigénique spécifique utilisée pour le développement de réactifs thérapeutiques et diagnostiques. La production commerciale est réalisée en cultivant des cellules hôtes dans des bioréacteurs spécifiques. La densité cellulaire et le métabolisme cellulaire sont des paramètres clés pour le rendement élevé des AcM. Bioréacteur à fibres creuses (HFB), une cartouche contenant des fibres poreuses emballées, est l'un des systèmes de production disponibles dans le commerce. Si la densité de cellules obtenue peut conduire à un rendement élevé, le coût de l'ensemble du dispositif, y compris les pompes et les cartouches très coûteuses, empêche son utilisation de petites unités. Comme une alternative économique, nous avons proposé ici d'étudier le potentiel des modules de dialyse de polysulfone du commerce, classiquement employés dans le traitement de l'insuffisance rénale en phase terminale. Cependant, la membrane de polysulfone native a démontré une adsorption de protéines non spécifique significative préjudiciable à la production d'AcMs. De plus des enjeux normatifs viennent se greffer à ces problématiques scientifiques et technico-économiques, avec le cas des normes (ISO 13485/ AC S99-104/ GMP FDA /BPF…) qui imposent des méthodes de travail normalisées. Ce travail de thèse consiste en la conception d’un bioréacteur jetable, sur la base d’une cartouche de dialyse médicale à fibres creuses. Ce système doit offrir toutes les garanties en termes de production, de facilité d’utilisation, de stérilité, et permettre de concentrer les produits de cytoculture. La méthodologie scientifique a été couplée à une démarche qualité. La gestion de ce projet a été couplé à l’analyse de risques. En effet ce projet a été divisé en ses 5 composantes élémentaires décrite par Ishikawa par la méthode des 5 M. L’analyse de risque a consisté au calcul d’indice de criticité par la méthode AMDEC de chacune de ses familles de risques. Cette approche nous a permis de formaliser deux axes de recherche : i) la mise en œuvre d’une oxygénation efficace du milieu de culture (chapitre 4) et ii) les moyens de limiter le colmatage dans le module à fibres creuses pour obtenir une culture cellulaire conforme aux objectifs (chapitre 5). Le taux d’oxygénation est un facteur à prendre en compte dans un processus de culture cellulaire. L’oxygène peut être supplémenté selon deux modes, le mode passif ou le mode actif [Ozturk et Palsson 1990; Zhang S. et al 1992]. Il existe 2 types de système d’oxygénation : les système dit passif ou les échanges se font a travers une paroi de silicone et un système actif par aération directe dans le milieu de culture. Ce système est de loin l'opération la plus simple pour fournir de l'oxygène. Cependant, lorsque celui-ci est utilisé pour apporter de l’oxygène à des cultures de cellules mammifères, cela peut engendrer des altérations cellulaires. Des agents protecteurs chimiques peuvent être utilisés pour réduire les dommages cellulaires et la formation de mousse [Kamase et Moo-yung 1990; van Der pol L.A et al 1993]. Nos études ont démontré que l'addition d'agents anti-mousse peut entraîner une diminution du coefficient de transfert de masse d’O2 en phase liquide (Kl) [Kamase et Moo-yung 1990]. Nous avons établi l’efficacité de l’utilisation d’un polymère silice/silicone pour éliminer la mousse sur des cultures bactériennes et de cellules mammifères. Afin de limiter ces phénomènes de colmatage, les fibres de polysulfone ont été traitées avec plusieurs tensioactifs (acide pluronique F127, D-limonen et différentes huiles de silicone) qui ont conduit à une diminution significative de l'adsorption protéique. L'effet de ces surfactants sur les performances de filtration et sur la cytotoxicité a été étudié. Certains d'entre eux n'ont pas influencé ces paramètres alors que d'autres ont présenté des effets négatifs. / Monoclonal Antibodies (mAbs) are proteins with specific antigen recognition used for development of both therapeutic and diagnostic reagents. Commercial production is achieved by growing host cells in specific bioreactors. Cell density and cell metabolism are key parameters for high yield of mAbs. Hollow fiber bioreactor (I-IFB), a cartridge containing packed porous fibres, is one of the system for production commercially available. If the cell density achieved can lead to high yield, the cost of the whole device, including pumps and very expensive cartridges prevents its use of small units. As an economical alternative, we proposed here to investigate the potential of commercial polysulfone dialysis modules, classically employed in the treatment of end stage renal failure. However, the native polysulfone membrane demonstrated a significant non-specific protein adsorption detrimental to mAbs production. Moreover normative issues are added to these scientific and techno-economic issues, with the case of standards (ISO 13485 / AC S99-104 / GMP FDA / BPF ...) which impose standard working methods. This thesis consists of the design of a disposable bioreactor, based on a hollow-fiber medical dialysis cartridge. This system must offer all the guarantees in terms of production, ease of use, sterility, and allow to concentrate the cytoculture products. Scientific methodology has been coupled with a quality approach. The management of this project was coupled with the risk analysis. Indeed this project was divided into its 5 elementary components describe by Ishikawa by the 5M method. The risk analysis consisted in the calculation of the criticality index by the AMDEC method of each of its families of risks. This approach allowed us to formalize two research axes: i) the implementation of an effective oxygenation of the culture medium (chapter 4) and ii) the means of limiting the clogging in the hollow fiber module to obtain a culture consistent with the objectives (Chapter 5). The rate of oxygenation is a factor to be taken into account in a cell culture process. Oxygen can be supplemented in two modes, passive mode or active mode [Ozturk and Palsson 1990; Zhang S. et al 19921. There are two types of oxygenation system: the so-called passive system or the exchanges are made through a silicone wall and an active system by direct aeration in the culture medium. This system is by far the simplest operation for providing oxygen. However, when it is used to supply oxygen to mammalian cell cultures, this can cause cellular damage. Chemical protective agents can be used to reduce cell damage and DKamase and Moo-yung 1990 foam formation; van Der pol L.A. et al 1993 Cl. Our studies have shown that the addition of antifoaming agents can lead to a decrease in the liquid phase (K2) mass transfer coefficient of D Kamase and Moo-yung 1990C]. We have established the effectiveness of using a silica / silicone polymer to remove foam on bacterial and mammalian cell cultures. In order to limit these adsorption phenomena, polysulfone fibers were treated with several surfactants (pluronic acid F 127, D-limonen, and different silicone oils) which led to a significant decrease in protein adsorption. The effect of such surfactants on the filtration performances and on cytotoxicity were investigated. Some of the them did not influence these parameters while some presented negative effects. Finally, different cell culture parameters (cells densities, production yield, flow properties, fouling) were studied, as well as the performance of the bioreactor in perfusion continuous mode. The bioreactor was maintained in continuous mode for fifteen days and the production yield per batch was 250 mg of AcMs. The results obtained in this work allowed us to define the next steps to be taken, and are the subject of the Perspectives section.

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