In this thesis technical nonionic surfactants are studied using multivariate techniques. The surfactants studied were alkyl ethoxylates (AEOs) and alkyl polyglucosides (APGs). The aquatic toxicity of the surfactants towards two organisms, a shrimp and a rotifer, was examined. The specified effect was lethality, LC50, as indicated by immobilisation. In a comparative study, the LC50 values obtained were used to develop two different types of model. In the log P model the toxicity was correlated to log P alone, while in the multivariate model several physicochemical variables, including log P, were correlated to the toxicity. The multivariate model gave smaller prediction errors than the log P model. Further, the change in reactivity when a surfactant mixture was added to dissolving pulp under alkaline conditions was studied, using the amount of residual cellulose as a measure of the reactivity. Ten AEO/APG mixtures were tested, and the mixture with greatest potential was studied in more detail. An optimum in the amount of added surfactant was found that seems to coincide, according to surface tension measurements, with the CMC.

Ce travail est consacré à la préparation de matériaux mésoporeux à partir de cristaux liquides formés avec des tensioactifs fluorés selon le mécanisme transcriptif LCT. Les paramètres de synthèse ont été optimisés pour la préparation de silices mésostructurées à partir de la phase hexagonale du système eau/C8F17C2H4(OCH2CH2)9OH. Les résultats montrent une corrélation entre le diamètre des pores des matériaux et les diamètres hydrophobes mesurés dans les cristaux liquides. L'incorporation de TiO2 dans une matrice silicatée selon la méthode de coprécipitation a été réalisée en utilisant soit des micelles (mécanisme d'auto-assemblage coopératif CTM), soit la phase hexagonale du système C8F17C2H4(OCH2CH2)9OH/eau (mécanisme transcriptif LCT). Dans les deux cas, l'incorporation de titane conduit à une perte de la structure et à une diminution de la surface spécifique. L'utilisation du mécanisme CTM favorise la formation de TiO2 anatase en surface du matériau, tandis que pour le mécanisme LCT, la substitution du silicium par le titane au coeur du matériau a été mise en évidence. Des films minces mésostructurés à base de TiO2 ont été réalisés à partir de la méthode EISA. Les analyses par diffraction des rayons X à incidence rasante couplées à des mesures de réflectivité ont permis de mettre en évidence la structure des films et de déterminer les épaisseurs des couches qui constituent les films. Enfin, une méthode originale de synthèse de matériaux mésoporeux organisés à base de TiO2 a été développée. La précipitation de TiO2 dans la mésophase hybride est déclenchée à l'aide d'un traitement par NH3 (g). La structure des matériaux est conservée après l'étape de calcination laquelle permet de cristalliser TiO2 en phase anatase. L'activité photocatalytique de ces matériaux a ensuite été testée sur la réaction de photodégradation du méthylorange / This work deals with the preparation of mesoporous materials from fluorinated liquid crystals via the LCT mechanism. Synthesis parameters have been optimized for the preparation of ordered mesoporous silica with the hexagonal H1 phase of water/C8F17C2H4(OCH2CH2)9OH system. Results show a correlation between pore diameters of materials and hydrophobic diameters measured in liquid crystals. According to the coprecipitation method, incorporation of TiO2 in a silica matrix, synthesized using micelles (via the cooperative templating mechanism CTM) or the hexagonal phase of C8F17C2H4(OCH2CH2)9OH/water system (via liquid crystal templating mechanism LCT). Both pathways lead to a loss of mesopore ordering and a decrease of the specific surface area when titania content increases. If materials are prepared via CTM mechanism TiO2 is present on the surface whereas TiO2 is in the bulk when LCT mechanism is used. Mesoporous thin films have been prepared via EISA method. Grazing incidence small angle X-Ray scattering and reflectivity analysis have been used to define the structure of films and the thickness of the different layers. Finally an original method has been developed for the preparation of ordered titania mesoporous materials. Precipitation of titania in the hybrid mesophase is activated by a NH3 treatment. The structure is preserved after calcination step which allow the formation of TiO2 anatase. Photocatalytic activity of these materials has been tested on the photodegradation of methylorange

La demande en énergie grandissante, les gisements d'uranium à faible teneur pourront être ceux exploités dans le futur. Le traitement conventionnel de minerais d'uranium utilise peu de procédés minéralurgiques de concentration permettant la réduction de consommation de réactifs de lixiviation. Le but de ce travail est de développer un procédé de valorisation visant l'amélioration du procédé d'exploitation (lixiviation alcaline en tas) prenant en compte la variabilité minéralogique et texturale du minerai. Le gisement de Trekkopje, est composé d'une calcrète et d'une gypscrète. Le minéral porteur de l'uranium est la carnotite (K2(UO2)2[VO4]2.3H2O). Les minéraux de gangue sont composés de silicates tels que le quartz, les feldspaths, les micas et de minéraux du calcium, la calcite et le gypse (analyses en DRX, ICP-MS). Un traitement d'images MEB a permis d'étudier les propriétés texturales et la surface exposée des inclusions dans les amas d'argiles (cf. Figure 1). Dans la calcrète broyée à -200 µm, 50 % de l'ensemble de la carnotite est en moyenne associée aux amas d'argiles, composés à 98 % de palygorskite, 2% d'illite, de montmorillonite et d'interstratifiés (analyses DRX et microsonde électronique de Castaing). La taille des grains de carnotite est à 95 % inférieure à 70 µm. La calcite est la principale inclusion dans les amas d'argiles avec un taux moyen d'inclusion de 12% tandis que celui de la carnotite s'élève à 5%. Le pourcentage de surface exposée moyen de ces minéraux, dans les amas, est de 6 % et de 3 %, respectivement, ceci indiquant que les inclusions ne devraient pas influencer le comportement des particules mixtes d'argile. Cependant, les essais de flottation sur minerai n'ont pas vérifié cette hypothèse. Trois voies de séparation minérales ont été proposées en fonction de l'aptitude des minéraux à consommer le réactif de lixiviation : les minéraux calciques des silicates, la palygorskite des minéraux de gangue et la carnotite des minéraux de gangue. Une étude des propriétés électrocinétiques en électrophorèse des silicates et des minéraux calciques a été réalisée afin de choisir les collecteurs et l'intervalle de pH optimal à une flottation sélective. Un pH basique proche de la neutralité est révélé optimal pour la séparation des minéraux de gangue avec des collecteurs cationiques ou anioniques en s'appuyant sur les valeurs de PIE des minéraux : silicates pH 1-2, palygorskite pH 3, francolite pH 3-4 et minéraux du calcium pH 9-10. Les isothermes d'adsorption des amines primaires avec un réactif nonionique obtenues par chromatographie gazeuse mettent en évidence leur coadsorption sur la surface des silicates à pH 8. La présence du réactif non ionique permet la formation d'une couche d'adsorption plus dense sur la surface minérale déduite des déplacements des bandes de vibration symétriques et asymétriques des groupements CH2, CH3 sur les spectres infrarouge en réflexion diffuse. La palygorskite est séparée de l'ensemble de minéraux calciques et silicates purs à pH 8, avec un mélange de collecteurs tels qu'une amine primaire et un alcool aliphatique sans utiliser de déprimants spécifiques. Une séparation nette entre minéraux du calcium et des silicates est réalisée à pH 8 en combinant l'oléate de sodium avec le même réactif nonionique. Des effets synergiques des mélanges de réactifs ioniques avec un réactif non ionique ont été mis en évidence avec un abaissement de la consommation en réactif ionique de deux à dix fois. Les essais de flottation en cellule mécanique de laboratoire de 1L sur le minerai ont confirmé les résultats obtenus en flottation des minéraux purs avec les collecteurs anioniques. L'élimination des minéraux du calcium (produit flotté contenant 25 % de l'uranium), des silicates (produit non flotté contenant 75 % de l'uranium) en utilisant une combinaison d'oléate de sodium et d'un alcool aliphatique est la voie de séparation par flottation retenue [...] / Due to the energy growing demand, uranium low grade ores may be those exploited in the future. Uranium ores conventional treatment doesn't often use mineral processing such as concentration methods for reducing leaching reagent consumption. The aim of this work is to develop an upgrading process to improve the operating process (alkaline heap leaching) taking into account the mineralogical and textural variability of the ore. The Trekkopje deposit is composed of calcrete and a gypscrete. The uranium bearing mineral is carnotite (K2 (UO2)2 [VO4]2.3H2O). The gangue minerals are composed by silicates, such as quartz, feldspars, micas and Ca-minerals, calcite and gypsum (XRD and ICP-MS analysis). A SEM image processing was used to study the textural properties and the exposed free surface of mineral inclusions in clay clusters. In calcrete milled to -200 µm, 50 % of all carnotite is associated with clay clusters, which are composed by 98 % of palygorskite, 2 % of illite, montmorillonite, and interbedded clays (XRD and microprobe analysis). The carnotite grain size is 95% less than 70 µm. Calcite is the main inclusion in clay clusters. Indeed, the calcite inclusions average rate in the clay clusters is 12 % and 5 % for carnotite inclusion. And the free exposed surface percentage of these minerals in clay clusters is 3 % and 6 %, thus indicating that the inclusions should not affect the behavior of mixed clay particles. However, ore flotation essays didn't verify this hypothesis. Three minerals separation have been proposed based on the mineral ability to consume leaching reagents: separating Ca-minerals from silicates, palygorskite from gangue minerals and carnotite from gangue minerals. A study of silicates and Ca-minerals electrokinetic properties (electrophoresis) was carried out to select the collectors and the optimum pH range for selective flotation. Basic pH near neutral was proved to be optimal for the separation of gangue minerals with cationic or anionic collectors (silicates IEP - pH 1-2, palygorskite IEP - pH 3, francolite IEP - pH 3-4 and IEP minerals calcium - pH 9 - 10). The adsorption isotherms of the primary amines with a nonionic reagent obtained by gay chromatography highlight their coadsorption on the silicates surface at pH 8. The presence of nonionic reagent allows to the formation of a compact layer on the mineral surface, derived from the displacement of the symmetric and asymmetric vibration groups CH2, CH3 of the infrared diffuse reflectance spectra. Palygorskite is separated from the pure Ca-minerals and silicates at pH 8, with a mixture of a primary amine and a nonionic reagent such as collectors, without using specific depressant. A clear separation of Ca-minerals and silicates is carried out at pH 8 by combining sodium oleate with aliphatic alcohols. The synergistic effects of ionic and nonionic reagents were highlighted with an ionic reagents consumption reduction by two to ten fold. The ore flotation tests have confirmed the results obtained in pure mineral flotation with anionic collectors. The removal of Ca-minerals (floated product containing 20 % of uranium), silicates (nonfloated product containing 80 % of uranium) using a combination of sodium oleate and an aliphatic alcohol is the separation by flotation chosen solution. This study led to exploitable results in solving the problem by coupling multi-scale approaches

Surfactants are one of the more ubiquitous contaminants in aquatic systems. Their importance as toxic components of pesticide formulations has, however, been largely overlooked. Amphibians particularly, as inhabitants of shallow, temporary and often lentic aquatic environments may be at risk from exposure to these chemicals when they enter aquatic systems. This thesis presents data on the toxicity of surfactants to amphibians. Several experimental exposures were conducted with embryo-larval, tadpole and adult developmental stages of the Australian species- Crinia insignifera, Helcioporus eyrei, Limnodynastes dorsalis and Litoria moorei and the exotic species- Bufo marinus and Xenopus laevis. Animals were variously exposed to glyphosate formulations that contain a high proportion of nonionic surfactants, or commercial pesticide wetting agents (alcohol alkoxylate and nonylphenol ethoxylate (NPE) surfactants). Feeding stage tadpoles of C.insignifera, H. eyrei, L. dorsalis and L. moorei were exposed to three commercial glyphosate formulations, glyphosate isopropylamine and glyphosate acid in static-renewal acute toxicity tests. The 48-h LC50 values for Roundup Herbicide (MON 2139) tested against tadpoles of C. insignifera, H. eyrei, L. dorsalis and L. moorei ranged between 8.1 and 32.2 mg/L (2.9 and 11.6 mg/L glyphosate acid equivalent (ae)), while the 48-h LC50 values for Roundup Herbicide tested against adult and newly metamorphosed C. insignifera ranged from 137-144 mg/L (49.4-51.8 mg/L ae). / Touchdown Herbicide (4 LC-E) tested against tadpoles of C. insignifera, H. eyrei, L. dorsalis and L. moorei was slightly less toxic than Roundup with 48-h LC50 values ranging between 27.3 and 48.7 mg/L (9.0 and 16.1 mg/L ae). Roundup Biactive (MON 77920) was practically non-toxic to tadpoles of the same four species producing 48-h LC50 values of 911 mg/L (328 mg/L ae) for L. moorei and >1000 mg/L (>360 mg/L ae) for C. insignifera, H. eyrei and L. dorsalis. Glyphosate isopropylamine was practically non-toxic producing no mortality amongst tadpoles of any of the four species over 48 h, at concentrations between 503 and 684 mg/L (343 and 466 mg/L ae). The toxicity of technical grade glyphosate acid (48-h LC50, 81.2-121 mg/L) is likely to be due to acid intolerance. Feeding stage tadpoles of B. marinus, X laevis, C. insignifera, H.eyrei, L. dorsalis and L. moorei were exposed to NPE and alcohol alkoxylate in static renewal acute toxicity tests. All species exhibited non-specific narcosis following exposure to both these surfactants. The 48-h EC50 values for NPE ranged between 1.1 mg/L (mild narcosis) and 12.1 mg/L (full narcosis). The 48-h EC50 values for alcohol alkoxylate ranged between 5.3 mg/L (mild narcosis) and 25.4 mg/L (full narcosis). Xenopus laevis was the most sensitive species tested. The sensitivity of the other five species was size dependent with larger species displaying greater tolerance. Replicate acute toxicity tests with B. marinus exposed to NPE at 30 degrees celsius over 96 hours indicated that the narcotic effects were not particularly time dependant. / The mean 24, 48, 72 and 96-h EC50 (mild narcosis) were 3.6, 3.7, 3.5 and 3.5 mg/L respectively. The mean 24, 48, 72, and 96-h EC50 (full narcosis) values were 4.0, 4.1, 4.2 and 4.0 respectively. Acute toxicity tests with B. marinus exposed to NPE at 30 degrees celsius under conditions of low dissolved oxygen (0.8-2.3 mg/L) produced a two to threefold increase in toxicity. The 12-h EC50 values ranged from 1.4 to 2.2 mg/L. The embryotoxicity of NPE was determined in X. laevis, L. adelaidensis and C. insignifera using a Frog Embryo Teratogenesis assay-Xenopus (FETAX). The 96-h LC50, EC50 and MCIG (LOEC) values for X. laevis were 3.9 to 5.4 mg/L, 2.8 to 4.6 mg/L and 1.0 to 3.0 mg/L respectively. The 140-h LC50, ECSO and MCIG values for L. adelaidensis were 9.2 mg/L, 8.8 mg/L and 5.1 to 6.0 ing/L respectively. The 134-h LC50, EC50 and MCIG values for C. insignifera were 6.4 mg/L, 4.5 mg/L and 4.0 mg/L respectively. Teratogenicity indices for the three species ranged between 1.0 and 1.6 indicating either no or low teratogenicity. Xenopus laevis was the more sensitive of the three species and the only species that displayed indisputable terata. The acute toxicity data indicated that the amphibian species tested were of similar sensitivity to fish and some invertebrates. Developmental retardation and oestrogenic effects following exposure to nonylphenol ethoxylate were indicated by sublethal toxicity tests. Crinia insignifera embryos were exposed during early embryogenesis to sublethal concentrations of NPE. / Exposure to NPE did not affect either weight nor size (snout-vent length) at metamorphosis. Exposure to 5.0mg/L NPE resulted in a significant delay in the time required to reach metamorphosis. Also, exposure to 3.0 mg/L NPE for the first 6 days of embryonic development or exposure to 5.0 mg/L NPE from day 2 to day 6 resulted in a statistically significant predominance in the female phenotype amongst metamorphosing froglets. Exposure for the first five days to 1.5 ing/L or 3.0 mg/L NPE had no effect on sex ratio. The results indicated that exposure to NPEs has endocrine disruptive effects in this species and that a narrow window of susceptibility exists for the induction of predominantly female phenotype. This study has also followed the degradation of a mixture of NPE oligomers and the concomitant formation of individual oligomers in static die-away tests with and without illumination in freshwater. Over 33 days in darkness there was a progressive and complete loss of long chain oligomers (NPEO(subscript)8-17), transient increases and subsequent loss of short to medium chain oligomers (NPE0(subscript)4-7), and large persistent increases (approximately 1000%) in short chain oligomers (NPE0(subscript)1-3). In the presence of illumination, biodegradation was retarded and heterotrophic bacterial proliferation was inhibited. After 33 days there was complete loss of long chain oligomers (NPE0(subscript)9-17), incomplete loss of medium chain oligomers (NPE0(subscript)6.8) and increases in short chain oligomers (NPE0(subscript)1-5). / This thesis discusses the importance of persistent metabolites of NPE degradation as it pertains to the habitat, developmental time frame and ecology of amphibians. Degradation of NPE is likely to occur over a time frame that is longer than that required for complete embryogenesis and metamorphosis of many species of amphibians, and may easily encompass those critical stages of development during which oestrogenic metabolites can affect development.

The first part of this thesis is concerned with thestructure-property relationships in nonionic surfactantsystems. The main aim was to investigate how the surfactantstructure influences the adsorption at interfaces andinteractions between surfactant coated interfaces.Particularly, the effect of the structure of the surfactantheadgroups was investigated. These were sugar-based headgroupwith varying size and flexibility and poly(ethylene oxide)based headgroups with or without an additional amide or estergroup. The hydrophobic part of the surfactant consisted mostlyof straight alkyl chains, except for one type of poly(ethyleneoxide) based surfactant with a dehydroabietic hydrophobe. The main technique that was used is the surface forcetechnique, with which the forces acting between two adsorbedsurfactant layers on hydrophilic or hydrophobic surfaces can bemeasured. These forces are important for e.g. the stability ofdispersions. The hydrophilic surfaces employed were glass andmica, whereas the hydrophobic surfaces were silanized glass andhydrophobized mica. The adsorption behavior on hydrophilicsurfaces is highly dependent on the type of headgroup andsurface, whereas similar results were obtained on the two typesof hydrophobic surfaces. To better understand how the surfaceforces are affected by the surfactant structure, measurementsof adsorbed amount and theoretical mean-field latticecalculations were carried out. The results show that the sugarsurfactant layers and poly(ethylene oxide) surfactant layersgive rise to very different surface forces, but that the forcesare more similar within each group. The structure-propertyrelationships for many other physical properties have beenstudied as well. These include equilibrium and dynamicadsorption at the liquid-vapor interface, micelle size, micelledynamics, and wetting. The second part in this thesis is about the aggregationbetween cationic polyelectrolytes and an anionic surfactant.The surface force technique was used to study the adsorption ofa low charged cationic polyelectrolyte on mica, and theaggregation between the adsorbed polyelectrolyte with theanionic surfactant. The aggregation in bulk was studied withturbidimetry, small angle neutron scattering (SANS), and smallangle x-ray scattering (SAXS). An internal hexagonal aggregatestructure was found for some of the bulk aggregates. <b>Keywords:</b>nonionic surfactant, sugar surfactant,poly(ethylene oxide), amide, ester, polyelectrolyte, SDS,hydrophobic surface, glass surface, mica, adsorption,aggregation, micelle size, surface forces, wetting, dynamicsurface tension, NMR, TRFQ, SANS, SAXS, mean-field latticecalculations.

The investigations are related to the influence of nonionic polyethoxylated surfactant on Tin- and Tin-Silver depositions. Cyclovoltammetry, electrochemical depositions in Hull cell, with quartz crystal microbalance, impedance spectroscopy, X-ray diffraction, REM and others were used as methods of characterization. / Die Untersuchungen befasssen sich mit dem Einfluss von nichtionischen polyethoxylierten Tenside auf die Zinn- und Zinn-Silber-Abscheidung, die durch Zyklovoltammetrie, Abscheidungen in der Hullzelle, mit der elektrochemischen Quarzmikrowaage, der Impedanzspektroskopie, Röntgendiffraktometrie, Rasterelektronenmikroskopie und Tensiometrie charakterisiert wurden.

<p>The first part of this thesis is concerned with thestructure-property relationships in nonionic surfactantsystems. The main aim was to investigate how the surfactantstructure influences the adsorption at interfaces andinteractions between surfactant coated interfaces.Particularly, the effect of the structure of the surfactantheadgroups was investigated. These were sugar-based headgroupwith varying size and flexibility and poly(ethylene oxide)based headgroups with or without an additional amide or estergroup. The hydrophobic part of the surfactant consisted mostlyof straight alkyl chains, except for one type of poly(ethyleneoxide) based surfactant with a dehydroabietic hydrophobe.</p><p>The main technique that was used is the surface forcetechnique, with which the forces acting between two adsorbedsurfactant layers on hydrophilic or hydrophobic surfaces can bemeasured. These forces are important for e.g. the stability ofdispersions. The hydrophilic surfaces employed were glass andmica, whereas the hydrophobic surfaces were silanized glass andhydrophobized mica. The adsorption behavior on hydrophilicsurfaces is highly dependent on the type of headgroup andsurface, whereas similar results were obtained on the two typesof hydrophobic surfaces. To better understand how the surfaceforces are affected by the surfactant structure, measurementsof adsorbed amount and theoretical mean-field latticecalculations were carried out. The results show that the sugarsurfactant layers and poly(ethylene oxide) surfactant layersgive rise to very different surface forces, but that the forcesare more similar within each group. The structure-propertyrelationships for many other physical properties have beenstudied as well. These include equilibrium and dynamicadsorption at the liquid-vapor interface, micelle size, micelledynamics, and wetting.</p><p>The second part in this thesis is about the aggregationbetween cationic polyelectrolytes and an anionic surfactant.The surface force technique was used to study the adsorption ofa low charged cationic polyelectrolyte on mica, and theaggregation between the adsorbed polyelectrolyte with theanionic surfactant. The aggregation in bulk was studied withturbidimetry, small angle neutron scattering (SANS), and smallangle x-ray scattering (SAXS). An internal hexagonal aggregatestructure was found for some of the bulk aggregates.</p><p><b>Keywords:</b>nonionic surfactant, sugar surfactant,poly(ethylene oxide), amide, ester, polyelectrolyte, SDS,hydrophobic surface, glass surface, mica, adsorption,aggregation, micelle size, surface forces, wetting, dynamicsurface tension, NMR, TRFQ, SANS, SAXS, mean-field latticecalculations.</p>

<p>Adsorption on solid surfaces from solution is a fundamental property of a surfactant. It might even be the most important aspect of surfactant behavior, since it influences many applications, such as cleaning, detergency, dispersion, separation, flotation, and lubrication. Consequently, fundamental investigations of surfactant adsorption are relevant to many areas.</p><p>The main aim of this thesis has been to elucidate the adsorption properties, primarily on the solid/water interface, of a particular class of polyhydroxyl based surfactants: the alkyl glucosides. By the use of ellipsometry, the equilibrium and kinetic aspects of adsorption on titanium dioxide with respect to structural effects has been studied. Furthermore, the effects of small amounts of cationic surfactant additives on the adsorption on silica have been investigated. The results have been compared with similar studies for other nonionic surfactants.</p><p>We have found that the surfactant structure has a strong effect on the adsorption properties. An increase in the surfactant chain length increases the cooperativity of the system. An increase in the head group polymerization decreases the cooperativity and the plateau adsorbed amount at equilibrium. The effect of surfactant structure on the adsorption kinetics depends on the concentration relative to the cmc, while the there is a decrease in the rate of desorption with increasing hydrophobic chain length independent of the concentration. The adsorption/desorption process is concluded to be diffusion driven, as suggested by the model used. When comparing these results with studies on ethylene oxide based surfactants, we conclude that the two types of surfactants exhibit similar trends on surfaces onto which they adsorb.</p><p>Adsorption from binary surfactant solutions is even more interesting than adsorption from single surfactant solutions, since it brings us one step closer to the systems used in applications. In addition, adsorption from a mixture can be very different from adsorption from any of the single surfactants in the mixture. Alkyl glucosides alone do not adsorb on silica, but addition of small amounts of a cationic surfactant to the alkyl glucoside solution allows for adsorption on silica. A comparison between the adsorption and bulk properties has shown that mixed micellization explains most, but not all, effects of the coadsorption properties. Changing the pH in the mixed systems reveals that a surfactant with a pH-dependent charge and the ability to adapt its charge to the environment, e.g. a surface, enhances the adsorbed amount over a wider range of pH values than a purely cationic surfactant.</p><p>It is well known that alkyl glucosides and ethylene oxides adsorb differently on different types of hydrophilic surfaces. As a consequence, replacing ethylene oxides with alkyl glucosides might not be all straight-forward; however, we have shown that the effect of the surface can be eliminated by the use of a cosurfactant.</p>

In dieser Arbeit wird ein industriell genutzter Metallreiniger auf Basis nichtionischer Tenside untersucht. Dabei werden ausschließlich Messmethoden verwendet, die sich auch für eine industrielle Fertigung eignen. Zu Anfang enthält die Arbeit kurze Abrisse zum gegenwärtigen Kenntnisstand bezüglich der Inhaltstoffe industriell genutzten Reiniger, der Analytik von Tensiden in Reinigern und der Adsorption der Tenside auf Feststoffoberflächen. Im Mittelpunkt der Arbeit steht neben der Charakterisierung und Analyse des Reinigers die quantitative Bestimmung der im Reiniger enthaltenen Tenside in industriellen Reinigungsbädern. Mit Hilfe der Hochleistungsflüssigkeitschromatografie mit einem Verdampfungs - Lichtstreudetektor wird die quantitative Verteilung der Tenside in Reinigungsbädern unter verschiedenen der industriellen Fertigung entsprechenden Bedingungen untersucht. Die Adsorption der im Reiniger enthaltenen Tenside auf der Metalloberfläche unter Fertigungsbedingungen wird mit Fluoreszenzspektroskopie und IR-Spektroskopie quantitativ bestimmt. Im letzten Kapitel wird auf die Umsetzung der gefundenen Ergebnisse in die industrielle Praxis eingegangen.

Made available in DSpace on 2015-03-03T15:02:47Z (GMT). No. of bitstreams: 1 IzabellyLL_TESE.pdf: 7496453 bytes, checksum: d39fc896ff5d9d4982952835ef786c26 (MD5) Previous issue date: 2013-07-12 / The molecular distillation is show as an alternative for separation and purification of various kinds of materials. The process is a special case of evaporation at high vacuum, in the order from 0.001 to 0.0001 mmHg and therefore occurs at relatively lower temperatures, preserves the material to be purified. In Brazil, molecular distillation is very applied in the separation of petroleum fractions. However, most studies evaluated the temperature of the evaporator, condenser temperature and flow such variables of the molecular distillation oil. Then, to increase the degree of recovery of the fraction of the distillate obtained in the process of the molecular distillation was evaluated the use nonionic surfactants of the class of nonylphenol ethoxylate, molecules able to interact in the liquid-liquid and liquid-vapor interface various systems. In this context, the aim of this work was to verify the influence of commercial surfactant (Ultranex-18 an Ultranex-18-50) in the molecular distillation of a crude oil. The physicochemical characterization of the oil was realized and the petroleum shown an API gravity of 42?, a light oil. Initially, studied the molecular distillation without surfactant using star design experimental (2H ? ) evaluated two variables (evaporator temperature and condenser temperature) and answer variable was the percentage in distillate obtained in the process (D%). The best experimental condition to molecular distillation oil (38% distillate) was obtained at evaporator and condenser temperatures of 120 ?C and 10 ? C, respectively. Subsequently, to determine the range of surfactant concentration to be applied in the process, was determined the critical micellar concentration by the technique of scattering X-ray small angle (SAXS). The surfactants Ultranex-18 an Ultranex-18-50 shown the critical micelle concentration in the range of 10-2 mol/L in the hydrocarbons studied. Then, was applied in the study of distillation a concentration range from 0.01 to 0.15 mol/L of the surfactants (Ultranex- 18 and 50). The use of the nonionic surfactant increased the percentage of hydrocarbons in the range from 5 to 9 carbons in comparison to the process carried out without surfactant, and in some experimental conditions the fraction of light compounds in the distilled was over 700% compared to the conventional process. The study showed that increasing the degree of ethoxylation of Ultranex18 to Ultranex-50, the compounds in the range of C5 to C9 reduced the percentage in the distilled, since the increase of the hydrophilic part of the surfactant reduces its solubility in the oil. Finally, was obtained an increase in the degree of recovery of light hydrocarbons, comparing processes with and without surfactant, obtained an increase of 10% and 4% with Ultranex-18 and Ultranex-50, respectively. Thus, it is concluded that the Ultranex- 18 surfactant showed a higher capacity to distillation compared with Ultranex-50 and the application of surfactant on the molecular distillation from petroleum allowed for a greater recovery of light compounds in distillate / A destila??o molecular apresenta-se como uma alternativa para separa??o e purifica??o de diversos tipos de materias. O processo ? um caso especial de evapora??o a alto v?cuo, na ordem 0,001 a 0,0001 mmHg, e consequentemente, ocorre ? temperaturas relativamente mais baixas, preservando ao m?ximo o material a ser purificado. No Brasil, a destila??o molecular ? muito aplicada na separa??o de fra??es de petr?leo. No entanto, boa parte dos estudos relacionados a destila??o molecular de petr?leo avalia apenas as vari?veis do processo, tais como: a temperatura do evaporador, temperatura do condensador, vaz?o e etc. Dessa forma, com o prop?sito de favorecer a destila??o molecular, visando aumentar o grau de recupera??o da fra??o do destilado obtido no processo, avaliou-se a aplica??o de tensoativos n?o i?nicos da classe do nonilfenol etoxilado, uma vez que tais mol?culas apresentam a capacidade de interagir na interface l?quido-l?quido e l?quido-vapor de diversos sistemas. Portanto, o objetivo deste trabalho foi verificar a influ?ncia de tensoativo comerciais do tipo Ultranex-18 e Ultranex-50 na destila??o molecular de um petr?leo bruto. Nesse estudo, realizou-se a caracteriza??o f?sico-qu?mica do petr?leo a ser destilado, determinando-se que o mesmo apresentava um grau API de 42?, o que confere a amostra a ser destilada uma caracter?stica de fra??o leve. Na etapa do estudo das destila??es moleculares realizadas sem tensoativo, aplicou-se um planejamento estrela (2K ? ) com duas vari?veis (temperatura do evaporador e temperatura do condensador), tendo como resposta a porcentagem de destilado obtida no processo (%D). Verificou-se que a melhor condi??o experimental para a destila??o molecular do petr?leo estudado foi aplicando uma temperatura do evaporador de 120?C e do condensador de 10?C, obtendo-se uma porcentagem de destilado de 38 %. Posteriormente, para determinar uma faixa de concentra??o de tensoativo a ser aplicado no processo determinou-se a concentra??o micelar critica aplicando a t?cnica de espalhamento de raio-X de baixo ?ngulo (SAXS). Atrav?s da t?cnica, constatou-se que para os tensoativos da classe do nonilfenois etoxilados a concentra??o micelar cr?tica encontra-se na faixa de 10-2 mol/L para os hidrocarbonetos estudados. A partir dessa constata??o, aplicou-se no estudo das destila??es com tensoativo (Ultranex-18 e 50) uma faixa de concentra??o entre 0,01 a 0,15 mol/L. Nesta etapa, verificou-se que a presen?a do tensoativo n?o i?nico aumentou a destila??o de hidrocarbonetos na faixa de 5 a 9 carbonos em compara??o ao processo realizado sem tensoativo, e que em alguns casos a fra??o de compostos leves no destilado do processo foi superior a 700 % em rela??o ao processo convencional. O estudo mostrou que o aumento do grau de etoxila??o do Ultranex-18 para o Ultranex-50, reduziu a porcentagem de compostos destilados na faixa de C5 a C9, uma vez que o aumento da parte hidrof?lica do tensoativo reduz sua solubilidade no petr?leo. Finalmente, verificou-se que o aumento no grau de recupera??o de hidrocarbonetos leves, comparando os processos com o tensoativo e sem tensoativo, resultou em um aumento de 10 % para o processo empregando o Ultranex-18 e 4% para o Ultranex-50. Dessa forma, conclui-se que o Ultranex-18 apresentou maior capacidade de destila??o frente ao Ultranex-50 e que a aplica??o de tensoativo na destila??o molecular de petr?leo favoreceu o processo, j? que houve o aumento da concentra??o de compostos leves obtidos