Generation of reconstituted human plasma-derived secretory-like IgA and IgM and their protective effect on intestinal epithelium

Les muqueuses sont les membranes tapissant les cavités du corps, tel que le tube digestif, et sont en contact direct avec l'environnement extérieur. Ces surfaces subissent de nombreuses agressions pouvant être provoquées par des agents pathogènes (bactéries, toxines ou virus). Cela étant, les muqueuses sont munies de divers mécanismes de protection dont notamment deux protéines-clés permettant de neutraliser les agents pathogènes : les anticorps ou immunoglobulines sécrétoires A (SIgA) et M (SIgM). Ces anticorps sont, d'une part, fabriqués au niveau de la muqueuse sous forme d'IgA et IgM. Lorsqu'ils sont sécrétés dans l'intestin, ils se lient à une protéine appelée pièce sécrétoire et deviennent ainsi SIgA et SïgM. La présence de la pièce sécrétoire est essentielle pour que les anticorps puissent fonctionner au niveau de la muqueuse. D'autre part, ces anticorps sont également fabriqués dans d'autres parties du corps en général et se retrouvent dans le sang sous forme d'IgA et IgM Chez l'homme, des thérapies basées sur l'injection d'anticorps donnent de bons résultats depuis de nombreuses années notamment dans le traitement des infections. Bien qu'un certain nombre d'études ont montré le rôle protecteur des anticorps de type IgA et IgM, ceux-ci ne sont que rarement utilisés dans les thérapies actuelles. La principale raison de cette faible utilisation réside dans la production ou la purification des IgA/IgM ou SIgA/SIgM (la forme active au niveau des muqueuses) qui est difficile à réaliser à large échelle. Ainsi, le but de la thèse était (1) d'étudier la possibilité d'employer des IgA et des IgM provenant du sang humain pour générer des SIgA et SIgM et (2) de voir si ces anticorps reconstitués pouvaient neutraliser certains agents pathogènes au niveau des muqueuses. Tout d'abord, une analyse biochimique des IgA et des IgM issues du sang a été effectuée. Nous avons observé que ces anticorps avaient des caractéristiques similaires aux anticorps naturellement présents au niveau des muqueuses. De plus, nous avons confirmé que ces anticorps pouvaient être associés à une pièce sécrétoire produite en laboratoire pour ainsi donner des SIgA et SIgM reconstituées. Ensuite, la fonctionnalité des anticorps reconstitués a été testée grâce à un modèle de couche unique de cellules intestinales différenciées (monocouches) en laboratoire imitant la paroi de l'intestin. Ces monocouches ont été infectées par une bactérie pathogène, Shigella flexneri, responsable de la shigellose, une maladie qui provoque des diarrhées sanglantes chez l'homme. L'infection des monocouches par les bactéries seules ou combinées aux SIgA et SIgM reconstituées a été analysée. Nous avons observé que les dommages des cellules étaient moins importants lorsque les SIgA étaient présentes. Il apparaît que les SIgA neutralisent les bactéries en se fixant dessus, ce qui provoque leur agrégation, et diminuent l'inflammation des cellules. La protection s'est montrée encore plus efficace avec les SIgM. De plus, nous avons vu que les SIgA et SIgM pouvaient diminuer la sécrétion de facteurs nocifs produits par les bactéries. Utilisant le même modèle des monocouches, la fonctionnalité des IgA issues du sang humain a aussi été testée contre une toxine sécrétée par une bactérie appelée Clostridium diffìcile. Cette bactérie peut être présente naturellement dans l'intestin de personnes saines, cependant elle peut devenir pathogène dans certaines conditions et être à l'origine de diarrhées et d'inflammations de l'intestin via la sécrétion de toxines. Des préparations d'anticorps contenant une certaine proportion de SIgA reconstituées ont amené à une diminution des dommages et de l'inflammation des monocouches causés par la toxine. L'ensemble de ces résultats prometteurs, montrant que des SIgA et SIgM reconstituées peuvent protéger la paroi de l'intestin des infections bactériennes, nous conduisent à approfondir la recherche sur ces anticorps dans des modèles animaux. L'aboutissement de ce type de recherche permettrait de tester, par la suite, l'efficacité sur l'homme de traitements des infections des muqueuses par injection d'anticorps de type SIgA et SIgM reconstituées. Les muqueuses, telle que la muqueuse gastrointestinale, sont des surfaces constamment exposées à l'environnement et leur protection est garantie par une combinaison de barrières mécaniques, physicochimiques et immunologiques. Parmi les divers mécanismes de protection immunologiques, la réponse humorale spécifique joue un rôle prépondérant et est assurée par les immunoglobulines sécrétoires de type A (SIgA) et M (SIgM). Les thérapies basées sur l'administration d'IgG apportent d'importants bénéfices dans le domaine de la santé. Bien que des études sur les animaux aient montré que l'administration par voie muqueuse d'IgA polymérique (plgA) ou SIgA pouvaient protéger des infections, des IgA/SIgA n'ont été utilisées qu'occasionnellement dans les thérapies. De plus, des études précliniques et cliniques ont démontré que l'administration par voie systémique de préparations enrichies en IgM pouvait aussi protéger des infections. Cependant, l'administration par voie muqueuse d'IgM/SIgM purifiées n'a pas été examinée jusqu'à présent. La principale raison est que la purification ou là production des IgA/SIgA et IgM/SIgM est difficile à réaliser à large échelle. Le but de ce travail de thèse était d'examiner la possibilité d'associer des IgA et IgM polyclonals purifiées à partir du plasma humain avec une pièce sécrétoire recombinante humaine afin de générer des SIgA et SIgM reconstituées fonctionnelles. Tout d'abord, une analyse biochimique des IgA et IgM issues du plasma humain a été effectuée par buvardage de western et Chromatographie. Ces molécules avaient des caractéristiques biochimiques similaires à celles des immunoglobulines issues de la muqueuse. L'association entre plgA ou IgM issues du plasma humain et la pièce sécrétoire recombinante humaine a été confirmée, ainsi que la stoechiométrie 1:1 de l'association. Comme dans les conditions physiologiques, cette association permettait de retarder la dégradation des SIgA et SIgM reconstituées exposées à des protéases intestinales. Ensuite, la fonctionnalité et le mode d'action des IgA et IgM issues du plasma humain, ainsi que des SIgA et SIgM reconstituées, ont été explorés grâce à un modèle in vitro de monocouches de cellules intestinales épithéliales polarisées de type Caco-2, qui imite l'épithélium intestinal. Les monocouches ont été infectées par un pathogène entérique, Shigella flexneri, seul ou combiné aux immunoglobulines issues du plasma humain ou aux immunoglobulines sécrétoires reconstituées. Bien que les dommages des monocouches aient été retardés par les plgA et SIgA reconstituées, les IgM et SIgM reconstituées se sont montrées supérieures dans le maintien de l'intégrité des cellules. Une agrégation bactérienne et une diminution de l'inflammation des monocouches ont été observées avec les plgA et SIgA reconstituées. Ces effets étaient augmentés avec les IgM et SIgM reconstituées. De plus, il s'est révélé que les deux types d'immunoglobulines de type sécrétoire reconstituées agissaient directement sur la virulence des bactéries en réduisant leur sécrétion de facteurs de virulence. La fonctionnalité des IgA issues du plasma humain a aussi été testée contre la toxine A de Clostridium difficile grâce au même modèle de monocouches de cellules épithéliales. Nous avons démontré que des préparations enrichies en IgA provenant du plasma humain pouvaient diminuer les dommages et l'inflammation des monocouches induits par la toxine. L'ensemble de ces résultats démontrent que des IgA et IgM de type sécrétoire peuvent être générées à partir d'IgA et IgM issues du plasma humain en les associant à la pièce sécrétoire et que ces molécules protègent l'épithélium intestinal contre des bactéries pathogènes. Ces molécules pourraient dès lors être testées dans des modèles in vivo. Le but final serait de les utiliser chez l'homme à des fins d'immunisation passive dans le traitement de pathologies associées à la muqueuse telles que les infections. - Mucosal surfaces, such as gastrointestinal mucosa, are constantly exposed to the external environment and their protection is ensured by a combination of mechanical, physicochemical and immunological barriers. Among the various immunological defense mechanisms, specific humoral mucosal response plays a crucial role and is mediated by secretory immunoglobulins A (SIgA) and M (SIgM). Immunoglobulin therapy based on the administration of IgG molecules leads important health benefits. Even though animal studies have shown that mucosal application of polymeric IgA (plgA) or SIgA provided protection against infections, IgA/SIgA have been only used occasionally for therapeutic application. Moreover, preclinical and clinical studies have demonstrated that systemic administration of IgM-enriched preparations could also afford protection against infections. Nevertheless, mucosal application of purified IgM/SIgM has not been examined. The main reason is that the purification or production of IgA/SIgA and IgM/SIgM at large scale is difficult to achieve. The aim of this PhD project was to examine the possibility to associate polyclonal human plasma-derived IgA and IgM with recombinant human secretory component (SC) to generate functional secretoiy-like IgA and IgM. First, biochemical analysis of human plasma IgA and IgM was performed by western blotting and chromatography. These molecules exhibited the same biochemical features as mucosa-derived antibodies (Abs). The association between human plasma plgA or IgM and recombinant human SC was confirmed, as well as the 1:1 stoichiometry of association. Similarly to physiological conditions, this association delayed the degradation of secretory-like IgA or IgM by intestinal proteases. Secondly, the function activity and the mode of action of human plasma IgA and IgM, as well as secretory-like IgA and IgM were explored using an in vitro model of polarized intestinal epithelial Caco-2 cell monolayers mimicking intestinal epithelium. Cell monolayers were infected with an enteropathogen, Shigella flexneri, alone or in combination to plasma Abs or secretory-like Abs. Even though plasma plgA and secretoiy-like IgA resulted in a delay of bacteria-induced damages of cell monolayers, plasma IgM and secretory-like IgM were shown to be superior in maintenance of cell integrity. Polymeric IgA and secretory-like IgA induced bacterial aggregation and decreased cell monolayer inflammation, effects further amplified with IgM and secretory-like IgM. In addition, both secretory-like Abs directly impacted on bacterial virulence leading to a reduction in secretion of virulence factors by bacteria. The functionality of human plasma IgA was also tested against Clostridium difficile toxin A using Caco-2 cell monolayers. Human plasma IgA- enriched preparations led to a diminution of cell monolayer damages and a decrease of cellular inflammation induced by the toxin. The sum of these results demonstrates that secretory-like IgA and IgM can be generated from purified human plasma IgA and IgM associated to SC and that these molecules are functional to protect intestinal epithelium from bacterial infections. These molecules could be now tested using in vivo models. The final goal would be to use them by passive immunization in the treatment of mucosa-associated pathologies like infections in humans.

Covalent homodimers of murine secretory component induced by epitope substitution unravel the capacity of the polymeric Ig receptor to dimerize noncovalently in the absence of IgA ligand.

Recombinant secretory immunoglobulin A containing a bacterial epitope in domain I of the secretory component (SC) moiety can serve as a mucosal delivery vehicle triggering both mucosal and systemic responses (Corthésy, B., Kaufmann, M., Phalipon, A., Peitsch, M., Neutra, M. R., and Kraehenbuhl, J.-P. (1996) J. Biol. Chem. 271, 33670-33677). To load recombinant secretory IgA with multiple B and T epitopes and extend its biological functions, we selected, based on molecular modeling, five surface-exposed sites in domains II and III of murine SC. Loops predicted to be exposed at the surface of SC domains were replaced with the DYKDDDDK octapeptide (FLAG). Another two mutants were obtained with the FLAG inserted in between domains II and III or at the carboxyl terminus of SC. As shown by mass spectrometry, internal substitution of the FLAG into four of the mutants induced the formation of disulfide-linked homodimers. Three of the dimers and two of the monomers from SC mutants could be affinity-purified using an antibody to the FLAG, mapping them as candidates for insertion. FLAG-induced dimerization also occurred with the polymeric immunoglobulin receptor (pIgR) and might reflect the so-far nondemonstrated capacity of the receptor to oligomerize. By co-expressing in COS-7 cells and epithelial Caco-2 cells two pIgR constructs tagged at the carboxyl terminus with hexahistidine or FLAG, we provide the strongest evidence reported to date that the pIgR dimerizes noncovalently in the plasma membrane in the absence of polymeric IgA ligand. The implication of this finding is discussed in terms of IgA transport and specific antibody response at mucosal surfaces.

Optimization of the procedure for removing iron deposits on ceramic filter media

In this thesis, cleaning of ceramic filter media was studied. Mechanisms of fouling and dissolution of iron compounds, as well as methods for cleaning ceramic membranes fouled by iron deposits were studied in the literature part. Cleaning agents and different methods were closer examined in the experimental part of the thesis. Pyrite is found in the geologic strata. It is oxidized to form ferrous ions Fe(II) and ferric ions Fe(III). Fe(III) is further oxidized in the hydrolysis to form ferric hydroxide. Hematite and goethite, for instance, are naturally occurring iron oxidesand hydroxides. In contact with filter media, they can cause severe fouling, which common cleaning techniques competent enough to remove. Mechanisms for the dissolution of iron oxides include the ligand-promoted pathway and the proton-promoted pathway. The dissolution can also be reductive or non-reductive. The most efficient mechanism is the ligand-promoted reductive mechanism that comprises two stages: the induction period and the autocatalytic dissolution.Reducing agents(such as hydroquinone and hydroxylamine hydrochloride), chelating agents (such as EDTA) and organic acids are used for the removal of iron compounds. Oxalic acid is the most effective known cleaning agent for iron deposits. Since formulations are often more effective than organic acids, reducing agents or chelating agents alone, the citrate¿bicarbonate¿dithionite system among others is well studied in the literature. The cleaning is also enhanced with ultrasound and backpulsing.In the experimental part, oxalic acid and nitric acid were studied alone andin combinations. Also citric acid and ascorbic acid among other chemicals were tested. Soaking experiments, experiments with ultrasound and experiments for alternative methods to apply the cleaning solution on the filter samples were carried out. Permeability and ISO Brightness measurements were performed to examine the influence of the cleaning methods on the samples. Inductively coupled plasma optical emission spectroscopy (ICP-OES) analysis of the solutions was carried out to determine the dissolved metals.

Modeling of non-isothermalvapor membrane separation with thermodynamic models and generalized mass transfer equations

A rigorous unit operation model is developed for vapor membrane separation. The new model is able to describe temperature, pressure, and concentration dependent permeation as wellreal fluid effects in vapor and gas separation with hydrocarbon selective rubbery polymeric membranes. The permeation through the membrane is described by a separate treatment of sorption and diffusion within the membrane. The chemical engineering thermodynamics is used to describe the equilibrium sorption of vapors and gases in rubbery membranes with equation of state models for polymeric systems. Also a new modification of the UNIFAC model is proposed for this purpose. Various thermodynamic models are extensively compared in order to verify the models' ability to predict and correlate experimental vapor-liquid equilibrium data. The penetrant transport through the selective layer of the membrane is described with the generalized Maxwell-Stefan equations, which are able to account for thebulk flux contribution as well as the diffusive coupling effect. A method is described to compute and correlate binary penetrant¿membrane diffusion coefficients from the experimental permeability coefficients at different temperatures and pressures. A fluid flow model for spiral-wound modules is derived from the conservation equation of mass, momentum, and energy. The conservation equations are presented in a discretized form by using the control volume approach. A combination of the permeation model and the fluid flow model yields the desired rigorous model for vapor membrane separation. The model is implemented into an inhouse process simulator and so vapor membrane separation may be evaluated as an integralpart of a process flowsheet.

A Study on Fractionation and Ultrafiltration of Proteins with Characterized Modified and Unmodified Membranes

Membrane filtration has become increasingly attractive in the processing of both foodand biotechnological products. However, the poor selectivity of the membranes and fouling are the critical factors limiting the development of UF systems for the specific fractionation of protein mixtures. This thesis gives an overview on fractionation of proteins from model protein solutions or from biological solutions. An attempt was made to improve the selectivity of the available membranes by modifying the membranes and by exploiting the different electrostatic interactions between the proteins and the membrane pore surfaces. Fractionation and UF behavior of proteins in the model solutions and in the corresponding biological solutions were compared. Characterization of the membranes and protein adsorptionto the membrane were investigated with combined flux and streaming potential studies. It has been shown that fouling of the membranes can be reduced using "self-rejecting" membranes at pH values where electrostatic repulsion is achieved between the membrane and the proteins in solution. This effect is best shown in UF of dilute single protein solutions at low ionic strengths and low pressures. Fractionation of model proteins in single, binary, and ternary solutionshas been carried out. The results have been compared to the results obtained from fractination of biological solutions. It was generally observed that fractination of proteins from biological solutions are more difficult to carry out owingto the presence of non studied protein components with different properties. Itcan be generally concluded that it is easier to enrich the smaller protein in the permeate but it is also possible to enrich the larger protein in the permeateat pH values close to the isoelectric point of the protein. It should be possible to find an optimal flux and modification to effectively improve the fractination of proteins even with very similar molar masses.

Critical flux and fouling in ultrafiltration of proteins

In this thesis different parameters influencing critical flux in protein ultrafiltration and membrane foul-ing were studied. Short reviews of proteins, cross-flow ultrafiltration, flux decline and criticalflux and the basic theory of Partial Least Square analysis (PLS) are given at the beginning. The experiments were mainly performed using dilute solutions of globular proteins, commercial polymeric membranes and laboratory scale apparatuses. Fouling was studied by flux, streaming potential and FTIR-ATR measurements. Critical flux was evaluated by different kinds of stepwise procedures and by both con-stant pressure and constant flux methods. The critical flux was affected by transmembrane pressure, flow velocity, protein concentration, mem-brane hydrophobicity and protein and membrane charges. Generally, the lowest critical fluxes were obtained at the isoelectric points of the protein and the highest in the presence of electrostatic repulsion between the membrane surface and the protein molecules. In the laminar flow regime the critical flux increased with flow velocity, but not any more above this region. An increase in concentration de-creased the critical flux. Hydrophobic membranes showed fouling in all charge conditionsand, furthermore, especially at the beginning of the experiment even at very low transmembrane pressures. Fouling of these membranes was thought to be due to protein adsorption by hydrophobic interactions. The hydrophilic membranes used suffered more from reversible fouling and concentration polarisation than from irreversible foul-ing. They became fouled at higher transmembrane pressures becauseof pore blocking. In this thesis some new aspects on critical flux are presented that are important for ultrafiltration and fractionation of proteins.

Regenerated cellulose ultrafiltration membranes in the treatment of pulp and paper mill process waters

Ultrafiltration (UF) is widely applied in different separation processes in the pulp and paper industry. The growing need to protect the environment, a lack of pure water and an interest in producing high-value chemicals from compounds present in process waters will probably lead to an increase in the use of UF in the pulp and paper industry. The efficiency and cost-effectiveness of a UF process depends on the applied membrane. The membrane should have a high and stable filtration capacity, a particular selectivity and a long operational lifetime. To meet these requirements a membrane should have a low fouling tendency. In addition, it should withstand the prevailing operational and chemical conditions. This thesis evaluates the performance and applicability of the regenerated cellulose (RC) membranes 00030T and C2 in the treatment of pulp and paper mill process waters based on the requirements above. The results demonstrated that both the tested RC membranes fulfilled well the requirement of high filtration capacity. In addition, in the filtration of a paper mill clear filtrate (CF) the RC membranes were not as greatly affected by variations in the CF quality as a polysulphone membrane. Furthermore, due to their extreme hydrophilicity and weak charge the fouling tendency of the membranes can be expected to be low in pulp and paper mill filtration applications. It is, however, known that fouling cannot be totally avoided even when the membrane is chosen very carefully. This study indicated that carbohydrates influenced negatively on permeability and caused fouling in the filtration of groundwood mill circulation water. Thus, a pre-treatment effectively reducing the amount of carbohydrates might help to maintain a stable capacity. However, the results of the thesis also showed that the removal of some of the possible foulants might just increase the harmful effect of others. Multivariate examination was useful in the understanding of the complicated factors causing the unstable capacity. The thesis also revealed that the 00030T and C2 membranes can be used at high pressure (max. tested pressure 12 bar). The C2 membrane, having a sponge-like substructure, was more pressure resistant, and its performance was more stable at high pressure compared to the UCO30T membrane containing macrovoids in its substructure. Both tested membranes can, according to the results, also be used at temperatures as high as 70°C in acidic, neutral and alkaline conditions. However, the use at extreme conditions might cause faster ageing of the membranes compared to ageing in neutral conditions. The thesis proved that both the tested RC membranes are very suitable for pulp and paper mill applications and that the membranes can be utilised in processes operating in challenging conditions. Thus, they could be used in more demanding applications than supposed earlier.

Fractionation of Wood Extracts

The aim of this thesis was to fractionate wood extracts into pure fractions using membrane technology, to observe membrane behaviour in solvents and to study the effect of conditioning on membrane performance. Four different wood extracts were used in the performed filtrations. In the literature part, the focus was on the effect of different solvent properties on polymeric membranes, especially on their retention and flux. Solute properties, such as shape, polarity and charge, were examined. Transport models, membrane stability and ways to improve the stability, when solvents were filtered, were also discussed. The experimental part consisted of a series of filtrations, where the effect of the wood extracts and solvent concentration on solute retention was observed. Polymeric and ceramic membranes were tested under different conditions and the solute analyses were performed with GC and GC-MS. It was discovered that it is possible to fractionate wood extracts using membrane technology to some extent, but more research must be done to understand the mechanisms behind the various interactions between the solvent and the membrane. Conditioning was also considered as an important part of the membrane pre-treatment.

Building the map of innovation for membrane materials (Ceramic membranes)

This work proposes a method of visualizing the trend of research in the field of ceramic membranes from 1999 to 2006. The presented approach involves identifying problems encountered during research in the field of ceramic membranes. Patents from US patent database and articles from Science Direct(& by ELSEVIER was analyzed for this work. The identification of problems was achieved with software Knowledgist which focuses on the semantic nature of a sentence to generate series of subject action object structures. The identified problems are classified into major research issues. This classification was used for the visualization of the intensity of research. The image produced gives the relation between the number of patents, with time and the major research issues. The identification of the most cited papers which strongly influence the research of the previously identified major issues in the given field was also carried out. The relations between these papers are presented using the metaphor of social network. The final result of this work are two figures, a diagram showing the change in the studied problems a specified period of time and a figure showing the relations between the major papers and groups of the problems

Ultrasuodatuskalvojen valinta, likaantuminen ja puhdistus entsyymiliuosten suodatuksessa

Ultrasuodatus on tehokas entsyymiliuosten konsentrointi- ja puhdistusmenetelmä. Prosessin ongelmana on kuitenkin kalvojen likaantumisesta johtuva suodatuksen aikainen vuon pienentyminen ja kalvojen hankala puhdistaminen. Oikeilla kalvovalinnoilla ja optimaalisilla pesustrategioilla voidaan suodatus- ja pesuaikoja lyhentää ja nain parantaa suodatusprosessin tehokkuutta ja tuotteen laatua. Työn kirjallisessa osassa on käsitelty entsyymiliuosten ja polymeerikalvojen suodatusprosessiin vaikuttavia ominaisuuksia. Työssä on esitelty myös pesuaineiden ja pesukemikaalien ominaisuuksia sekä pesuprosessiin vaikuttavia tekijöitä. Työn kokeellinen osa koostui kahdesta osasta. Työn ensimmäisessä osassa etsittiin entsyymiliuosten ultrasuodatusprosessiin sopivaa kalvoa vertailemalla kalvojen permeabiliteetteja, hydrofiilisyytta, varausta ja peseytyvyyttä. Suodatuksissa käytettiin kahta Roal Oy:n tuottamaa entsyymiliuosta ja suodatukset tehtiin DSS Labstak M20-laitteistolla. Työn toisen osan tarkoituksena oli etsiä entsyymiliuosten suodatuksessa käytettävien kalvojen likaantumisen syyt sekä tehokas puhdistusaine kalvojen pesuun. Tehokasta pesuainetta etsittiin liotuskokeilla ja laboratoriomittakaavan poikkivirtauslaitteistolla. Analysointeja tehtiin muun muassa FTIR- spektroskoopilla, vuomittauksilla, pyyhkäisyelektronimikroskoopilla ja kontaktikulmamittauksilla. Entsyymiliuosten suodatuksiin sopivan kalvon etsinnässä testattujen kalvojen välillä oli suuria eroja niin permeabiliteeteissa kuin likaantumisessa ja puhdistumisessa, mutta mikään kalvoista ei erottunut ylivoimaisesti parhaaksi. Pesuaineista kaupalliset membraanien puhdistukseen tarkoitetut emäksiset pesuaineet osoittautuivat tehokkaimmiksi lian poistajiksi.

Treatment of oily wastewater by ultrafiltration: The effect of different operating and solution conditions

In many industries, such as petroleum production, and the petrochemical, metal, food and cosmetics industries, wastewaters containing an emulsion of oil in water are often produced. The emulsions consist of water (up to 90%), oils (mineral, animal, vegetable and synthetic), surfactants and other contaminates. In view of its toxic nature and its deleterious effects on the surrounding environment (soil, water) such wastewater needs to be treated before release into natural water ways. Membrane-based processes have successfully been applied in industrial applications and are considered as possible candidates for the treatment of oily wastewaters. Easy operation, lower cost, and in some cases, the ability to reduce contaminants below existing pollution limits are the main advantages of these systems. The main drawback of membranes is flux decline due tofouling and concentration polarisation. The complexity of oil-containing systems demands complementary studies on issues related to the mitigation of fouling and concentration polarisation in membranebased ultrafiltration. In this thesis the effect of different operating conditions (factors) on ultrafiltration of oily water is studied. Important factors are normally correlated and, therefore, their effect should be studied simultaneously. This work uses a novel approach to study different operating conditions, like pressure, flow velocity, and temperature, and solution properties, like oil concentration (cutting oil, diesel, kerosene), pH, and salt concentration (CaCl2 and NaCl)) in the ultrafiltration of oily water, simultaneously and in a systematic way using an experimental design approach. A hypothesis is developed to describe the interaction between the oil drops, salt and the membrane surface. The optimum conditions for ultrafiltration and the contribution of each factor in the ultrafiltration of oily water are evaluated. It is found that the effect on permeate flux of the various factors studied strongly depended on the type of oil, the type of membrane and the amount of salts. The thesis demonstrates that a system containing oil is very complex, and that fouling and flux decline can be observed even at very low pressures. This means that only the weak form of the critical flux exists for such systems. The cleaning of the fouled membranes and the influence of different parameters (flow velocity, temperature, time, pressure, and chemical concentration (SDS, NaOH)) were evaluated in this study. It was observed that fouling, and consequently cleaning, behaved differently for the studied membranes. Of the membranes studied, the membrane with the lowest propensity for fouling and the most easily cleaned was the regenerated cellulose membrane (C100H). In order to get more information about the interaction between the membrane and the components of the emulsion, a streaming potential study was performed on the membrane. The experiments were carried out at different pH and oil concentration. It was seen that oily water changed the surface charge of the membrane significantly. The surface charge and the streaming potential during different stages of filtration were measured and analysed being a new method for fouling of oil in this thesis. The surface charge varied in different stages of filtration. It was found that the surface charge of a cleaned membrane was not the same as initially; however, the permeability was equal to that of a virgin membrane. The effect of filtration mode was studied by performing the filtration in both cross-flow and deadend mode. The effect of salt on performance was considered in both studies. It was found that salt decreased the permeate flux even at low concentration. To test the effect of hydrophilicity change, the commercial membranes used in this thesis were modified by grafting (PNIPAAm) on their surfaces. A new technique (corona treatment) was used for this modification. The effect of modification on permeate flux and retention was evaluated. The modified membranes changed their pore size around 33oC resulting in different retention and permeability. The obtained results in this thesis can be applied to optimise the operation of a membrane plant under normal or shock conditions or to modify the process such that it becomes more efficient or effective.

Membrane emulsification in preparation of single site catalyst

In the theory part the membrane emulsification was studied. Emulsions are used in many industrial areas. Traditionally emulsions are prepared by using high shear in rotor-stator systems or in high pressure homogenizer systems. In membrane emulsification two immiscible liquids are mixed by pressuring one liquid through the membrane into the other liquid. With this technique energy could be saved, more homogeneous droplets could be formed and the amount of surfactant could be decreased. Ziegler-Natta and single-site catalysts are used in olefin polymerization processes. Nowadays, these catalysts are prepared according to traditional mixing emulsification. More homogeneous catalyst particles that have narrower particle size distribution might be prepared with membrane emulsification. The aim of the experimental part was to examine the possibility to prepare single site polypropylene catalyst using membrane emulsification technique. Different membrane materials and solidification techniques of the emulsion were examined. Also the toluene-PFC phase diagram was successfully measured during this thesis work. This phase diagram was used for process optimization. The polytetrafluoroethylene membranes had the largest contact angles with toluene and also the biggest difference between the contact angles measured with PFC and toluene. Despite of the contact angle measurement results no significant difference was noticed between particles prepared using PTFE membrane or metal sinter. The particle size distributions of catalyst prepared in these tests were quite wide. This would probably be fixed by using a membrane with a more homogeneous pore size distribution. It is also possible that the solidification rate has an effect on the particle sizes and particle morphology. When polymeric membranes are compared PTFE is probably still the best material for the process as it had the best chemical durability.

Identification of extractives and polysaccharides as foulants in membrane filtration of pulp and paper mill effluents

The search for new renewable materials has intensified in recent years. Pulp and paper mill process streams contain a number of potential compounds which could be used in biofuel production and as raw materials in the chemical, food and pharmaceutical industries. Prior to utilization, these compounds require separation from other compounds present in the process stream. One feasible separation technique is membrane filtration but to some extent, fouling still limits its implementation in pulp and paper mill applications. To mitigate fouling and its effects, foulants and their fouling mechanisms need to be well understood. This thesis evaluates fouling in filtration of pulp and paper mill process streams by means of polysaccharide model substance filtrations and by development of a procedure to analyze and identify potential foulants, i.e. wood extractives and carbohydrates, from fouled membranes. The model solution filtration results demonstrate that each polysaccharide has its own fouling mechanism, which also depends on the membrane characteristics. Polysaccharides may foul the membranes by adsorption and/or by gel/cake layer formation on the membrane surface. Moreover, the polysaccharides interact, which makes fouling evaluation of certain compound groups very challenging. Novel methods to identify wood extractive and polysaccharide foulants are developed in this thesis. The results show that it is possible to extract and identify wood extractives from membranes fouled in filtration of pulp and paper millstreams. The most effective solvent was found to be acetone:water (9:1 v/v) because it extracted both lipophilic extractives and lignans at high amounts from the fouled membranes and it was also non-destructive for the membrane materials. One hour of extraction was enough to extract wood extractives at high amounts for membrane samples with an area of 0.008 m2. If only qualitative knowledge of wood extractives is needed a simplified extraction procedure can be used. Adsorption was the main fouling mechanism in extractives-induced fouling and dissolved fatty and resin acids were mostly the reason for the fouling; colloidal fouling was negligible. Both process water and membrane characteristics affected extractives-induced fouling. In general, the more hydrophilic regenerated cellulose (RC) membrane fouled less that the more hydrophobic polyethersulfone (PES) and polyamide (PA) membranes independent of the process water used. Monosaccharide and uronic acid units could also be identified from the fouled synthetic polymeric membranes. It was impossible to analyze all monosaccharide units from the RC membrane because the analysis result obtained contained degraded membrane material. One of the fouling mechanisms of carbohydrates was adsorption. Carbohydrates were not potential adsorptive foulants to the sameextent as wood extractives because their amount in the fouled membranes was found to be significantly lower than the amount of wood extractives.

Membrane properties of structurally modified ceramides : effects on lipid lateral distribution and sphingomyelin-interactions in artificial bilayer membranes

Ceramides comprise a class of sphingolipids that exist only in small amounts in cellular membranes, but which have been associated with important roles in cellular signaling processes. The influences that ceramides have on the physical properties of bilayer membranes reach from altered thermodynamical behavior to significant impacts on the molecular order and lateral distribution of membrane lipids. Along with the idea that the membrane physical state could influence the physiological state of a cell, the membrane properties of ceramides have gained increasing interest. Therefore, membrane phenomena related to ceramides have become a subject of intense study both in cellular as well as in artificial membranes. Artificial bilayers, the so called model membranes, are substantially simpler in terms of contents and spatio-temporal variation than actual cellular membranes, and can be used to give detailed information about the properties of individual lipid species in different environments. This thesis focuses on investigating how the different parts of the ceramide molecule, i.e., the N-linked acyl chain, the long-chain sphingoid base and the membrane-water interface region, govern the interactions and lateral distribution of these lipids in bilayer membranes. With the emphasis on ceramide/sphingomyelin(SM)-interactions, the relevance of the size of the SMhead group for the interaction was also studied. Ceramides with methylbranched N-linked acyl chains, varying length sphingoid bases, or methylated 2N (amide-nitrogen) and 3O (C3-hydroxyl) at the interface region, as well as SMs with decreased head group size, were synthesized and their bilayer properties studied by calorimetric and fluorescence spectroscopic techniques. In brief, the results showed that the packing of the ceramide acyl chains was more sensitive to methyl-branching in the mid part than in the distal end of the N-linked chain, and that disrupting the interfacial structure at the amide-nitrogen, as opposed to the C3-hydroxyl, had greater effect on the interlipid interactions of ceramides. Interestingly, it appeared that the bilayer properties of ceramides could be more sensitive to small alterations in the length of the long-chain base than what was previously reported for the N-linked acyl chain. Furthermore, the data indicated that the SM-head group does not strongly influence the interactions between SMs and ceramides. The results in this thesis illustrate the pivotal role of some essential parts of the ceramide molecules in determining their bilayer properties. The thesis provides increased understanding of the molecular aspects of ceramides that possibly affect their functions in biological membranes, and could relate to distinct effects on cell physiology.

Structural properties of lipid reconstructs and lipid composition of normotensive and hypertensive rat vascular smooth muscle cell membranes

Multiple cell membrane alterations have been reported to be the cause of various forms of hypertension. The present study focuses on the lipid portion of the membranes, characterizing the microviscosity of membranes reconstituted with lipids extracted from the aorta and mesenteric arteries of spontaneously hypertensive (SHR) and normotensive control rat strains (WKY and NWR). Membrane-incorporated phospholipid spin labels were used to monitor the bilayer structure at different depths. The packing of lipids extracted from both aorta and mesenteric arteries of normotensive and hypertensive rats was similar. Lipid extract analysis showed similar phospholipid composition for all membranes. However, cholesterol content was lower in SHR arteries than in normotensive animal arteries. These findings contrast with the fact that the SHR aorta is hyporeactive while the SHR mesenteric artery is hyperreactive to vasopressor agents when compared to the vessels of normotensive animal strains. Hence, factors other than microviscosity of bulk lipids contribute to the vascular smooth muscle reactivity and hypertension of SHR. The excess cholesterol in the arteries of normotensive animal strains apparently is not dissolved in bulk lipids and is not directly related to vascular reactivity since it is present in both the aorta and mesenteric arteries. The lower cholesterol concentrations in SHR arteries may in fact result from metabolic differences due to the hypertensive state or to genes that co-segregate with those that determine hypertension during the process of strain selection.