876 resultados para crystal morphology
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This work evaluated chemical interesterification of canola oil (CaO) and fully hydrogenated cottonseed oil (FHCSO) blends, with 20%, 25%, 30%, 35% and 40%(w/w) FHCSO content. Interesterification produced reduction of trisaturated and increase in monounsaturated and diunsaturated triacylglycerols contents, which caused important changes in temperatures and enthalpies associated with the crystallization and melting thermograms. It was verified reduction in medium crystal diameter in all blends, in addition crystal morphology modification. Crystallization kinetics revealed that crystal formation induction period and maximum solid fat content were altered according to FHCSO content in original blends and as a result of random rearrangement. Changes in Avrami constant (k) and exponent (n) indicated, respectively, that interesterification decreased crystallization rates and altered crystalline morphology. However, X-ray diffraction analyses showed randomization did not change the original crystalline polymorphism. The original and interesterified blends had significant predominance of beta` polymorph, which is interesting for several food applications. (C) 2009 Elsevier Ltd. All rights reserved.
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Blends of soybean oil (SO) and fully hydrogenated soybean oil (FHSBO), with 10, 20, 30, 40, and 50% (w/w) FHSBO content were interesterified under the following conditions: 20 min reaction time, 0.4% sodium methoxide catalyst, and 500 rpm stirring speed, at 100 A degrees C. The original and interesterified blends were examined for triacylglycerol composition, thermal behavior, microstructure, crystallization kinetics, and polymorphism. Interesterification produced substantial rearrangement of the triacylglycerol species in all the blends, reduction of trisaturated triacylglycerol content and increase in monounsaturated-disaturated and diunsaturated-monosaturated triacylglycerols. Evaluation of thermal behavior parameters showed linear relations with FHSBO content in the original blends. Blend melting and crystallization thermograms were significantly modified by the randomization. Interesterification caused significant reductions in maximum crystal diameter in all blends, in addition to modifying crystal morphology. Characterization of crystallization kinetics revealed that crystal formation induction period (tau (SFC)) and maximum solid fat content (SFC(max)) were altered according to FHSBO content in the original blends and as a result of the random rearrangement. Changes in Avrami constant (k) and exponent (n) indicated, respectively, that-as compared with the original blends-interesterification decreased crystallization velocities and modified crystallization processes, altering crystalline morphology and nucleation mechanism. X-ray diffraction analyses revealed that interesterification altered crystalline polymorphism. The interesterified blends showed a predominance of the beta` polymorph, which is of more interest for food applications.
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Blends of soybean oil (50) and fully hydrogenated soybean oil (FHSBO), with 10%, 20%, 30%, 40% and 50% FHSBO (w/w) content were interesterified under the following conditions: 0.4% sodium methoxide, 500 rpm stirring, 100 degrees C, 20 min. The original and interesterified blends were examined for triacylglycerol composition, melting point, solid fat content (SFC) and consistency. Interesterification caused considerable rearrangement of triacylglycerol species, reduction of trisaturated triacylglycerol content and increase in monounsaturated and diunsaturated triacylglycerols, resulting in lowering of respective melting points. The interesterified blends displayed reduced SFC at all temperatures and more linear melting profiles as compared with the original blends. Yield values showed increased plasticity in the blends after the reaction. Isosolid diagrams before and after the reaction showed no eutectic interactions. The 90:10, 80:20, 70:30 and 60:40 interesterified SO:FHSBO blends displayed characteristics suited to application, respectively, as liquid shortening, table margarine, baking/confectionery fat and all-purpose shortenings/biscuit-filing base. (C) 2009 Elsevier Ltd. All rights reserved.
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Introducing poly(ethylene oxide) surfactant to aluminum hydrate colloids can effectively direct the crystal growth of boehmite and the crystal morphology of final gamma-alumina crystallites. Fibrous crystallites of gamma-alumina about 3-4 nm thick and 30-60 nm long are obtained. They stack randomly, resulting in a structure with a low contact area between the fibers but with a very large porosity. Such a structure exhibits strong resistance to sintering when heated to high temperatures. A sample retains a BET surface area of 68 m(2)/g, after being heated to 1473 K. The surfactant molecules form micelles that interact with the colloid particles of aluminum hydroxide through hydrogen bonding. This interaction is not sufficient to change the intrinsic crystal structure of boehmite, but induces profound changes in the morphology of boehmite crystallites and their growth. The surfactant-induced fiber formation (SIFF) process has distinct features from templated synthesis but shows similarities in some respects to biomineralization processes in which inorganic crystals with complex morphological shapes can be formed in biological systems. SIFF offers an effective approach to create new nanostructures of inorganic oxide from aqueous media.
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Työssä tutkittiin leijupetikiteyttimen toimivuutta sulfatiatsolikiteiden kasvunopeuksien mittaamisessa. Sulfatiatsoli on lääkeaine, jota käytetään antibioottina. Kirjallisuusosassa on käsitelty kiteytyksen perusteita sekä olosuhteiden vaikutuksia kidemorfologiaan. Koska kyseessä on lääkeaine, on työssä myös selvitetty tekijöitä, jotka vaikuttavat syntyvän kiteen polymorfimuotoon. Näitä ovat mm. siemenkiteen polymorfimuoto sekä käytetty liuotin. Kirjallisuusosassa on myös esitelty teollisia ja laboratoriomittakaavan leijupetikiteyttimiä. Kokeellisessa osassa on keskitytty testaamaan leijupetikiteyttimen toimintaa sekä etsimään sopivia olosuhteita kasvukokeiden suorittamiselle. Kokeissa tutkittiin ylikylläisyyden vaikutusta sulfatiatsolikiteen kasvuun. Kiteen kasvun seurantaan pyrittiin etsimään sopivia hiukkaskokoanalysaattoreita. Mittauksissa käytetyt laitteistot olivat PIA 4000 mod LUT on-line-videomikroskooppi ja laserdiffraktioon perustuva Coulter LS 130 off-line-partikkelikokoanalysaattori.
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In the oil industry, the paraffination phenomenon is a major problem during oil production, displacement and treatment. Paraffin deposition in subsea flowlines, surface equipment, production string or even in the reservoir, can cause significant and increasing oil losses. To minimize paraffin precipitation, the application of magnetic field in the petroleum path has been suggested based on empiric studies. In this study, we assembled a labscale magnetic conditioner to determine the influence of magnetic field on the physical-chemical properties of two fluids : oil and a paraffin mixture. We observed that magnetic field reduce sample aparent viscosity due to crystal morphology alteration.
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Diplomityön tarkoituksena oli tutkia nikkelin sulfidisaostuksessa syntyvien kiteiden morfologiaa ja siihen vaikuttavia parametreja. Syntyvien kiteiden kasvua ja morfologiaa tutkittiin kiteen muodostumisen ja kasvun teorioiden avulla. Saostuksen olosuhteet, kuten lämpötila, paine ja pH vaikuttavat muodostuvien kiteiden morfologiaan. Muilla parametreilla, kuten liuoksen ylikylläisyydellä, epäpuhtauksilla, lisäaineilla, sekoituksella ja reaktioajalla on myös suuri merkitys. Kokeiden avulla haluttiin liuoskoostumuksen, saostusolosuhteiden ja muiden komponenttien vaikutusta nikkelisulfidikiteiden morfologiaan. Kokeissa käytettiin kahta eri sulfidilähdettä: natriumvetysulfidia ja rikkivetyä. Puolipanoskokeissa nikkelipitoisuus oli 1,5 g/l, paine 101,3 kPa ja sekoitusnopeus 650 rpm. Saostuskokeet tehtiin natriumsulfaatti- 5 g/l ja ammoniumsulfaattiliuoksissa 300 g/l. Saostuskokeissa muuttujia olivat saostimen konsentraatio ja määrä, rauta- ja magne-siumepäpuhtaudet, lämpötila ja lisäaineet. Diplomityön kokeellisessa osassa morfologiaa tutkittiin suoraan valomikroskoopin ja pyyhkäisyelektronimikroskoopin (SEM) avulla. Morfologiaa tutkittiin myös epäsuorasti laskeutumisnopeuden, keskimääräisen partikkelikoon, ja ominaispinta-alamittausten avulla. Saostimen pitoisuuden vaikutukset partikkelimuotoon olivat pieniä, mutta vaikutukset ominaispinta-alaan ja partikkelikokoon olivat suuria. Natriumlauryylisul-faatti ja EDTA ohjasivat partikkelien rakennetta levymäisemmäksi, joka johti hitaaseen laskeutumisnopeuteen. Polyakryylihappo lisäaineena muuttaa partikkelien morfologiaa kuutiomaisemmaksi. Flokkulanttien ja raudan morfologiset vaikutukset olivat pieniä. Partikkelikoko ja omaispinta-ala pienenivät selvästi magnesiumpitoisuuden kasvaessa. Lämpötilan kasvattaminen lisäsi epäsäännöllisten kiteiden määrää ja muodostuneet kiteet olivat enemmän neulamaisia.
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The steel industry produces, besides steel, also solid mineral by-products or slags, while it emits large quantities of carbon dioxide (CO2). Slags consist of various silicates and oxides which are formed in chemical reactions between the iron ore and the fluxing agents during the high temperature processing at the steel plant. Currently, these materials are recycled in the ironmaking processes, used as aggregates in construction, or landfilled as waste. The utilization rate of the steel slags can be increased by selectively extracting components from the mineral matrix. As an example, aqueous solutions of ammonium salts such as ammonium acetate, chloride and nitrate extract calcium quite selectively already at ambient temperature and pressure conditions. After the residual solids have been separated from the solution, calcium carbonate can be precipitated by feeding a CO2 flow through the solution. Precipitated calcium carbonate (PCC) is used in different applications as a filler material. Its largest consumer is the papermaking industry, which utilizes PCC because it enhances the optical properties of paper at a relatively low cost. Traditionally, PCC is manufactured from limestone, which is first calcined to calcium oxide, then slaked with water to calcium hydroxide and finally carbonated to PCC. This process emits large amounts of CO2, mainly because of the energy-intensive calcination step. This thesis presents research work on the scale-up of the above-mentioned ammonium salt based calcium extraction and carbonation method, named Slag2PCC. Extending the scope of the earlier studies, it is now shown that the parameters which mainly affect the calcium utilization efficiency are the solid-to-liquid ratio of steel slag and the ammonium salt solvent solution during extraction, the mean diameter of the slag particles, and the slag composition, especially the fractions of total calcium, silicon, vanadium and iron as well as the fraction of free calcium oxide. Regarding extraction kinetics, slag particle size, solid-to-liquid ratio and molar concentration of the solvent solution have the largest effect on the reaction rate. Solvent solution concentrations above 1 mol/L NH4Cl cause leaching of other elements besides calcium. Some of these such as iron and manganese result in solution coloring, which can be disadvantageous for the quality of the PCC product. Based on chemical composition analysis of the produced PCC samples, however, the product quality is mainly similar as in commercial products. Increasing the novelty of the work, other important parameters related to assessment of the PCC quality, such as particle size distribution and crystal morphology are studied as well. As in traditional PCC precipitation process, the ratio of calcium and carbonate ions controls the particle shape; a higher value for [Ca2+]/[CO32-] prefers precipitation of calcite polymorph, while vaterite forms when carbon species are present in excess. The third main polymorph, aragonite, is only formed at elevated temperatures, above 40-50 °C. In general, longer precipitation times cause transformation of vaterite to calcite or aragonite, but also result in particle agglomeration. The chemical equilibrium of ammonium and calcium ions and dissolved ammonia controlling the solution pH affects the particle sizes, too. Initial pH of 12-13 during the carbonation favors nonagglomerated particles with a diameter of 1 μm and smaller, while pH values of 9-10 generate more agglomerates of 10-20 μm. As a part of the research work, these findings are implemented in demonstrationscale experimental process setups. For the first time, the Slag2PCC technology is tested in scale of ~70 liters instead of laboratory scale only. Additionally, design of a setup of several hundreds of liters is discussed. For these purposes various process units such as inclined settlers and filters for solids separation, pumps and stirrers for material transfer and mixing as well as gas feeding equipment are dimensioned and developed. Overall emissions reduction of the current industrial processes and good product quality as the main targets, based on the performed partial life cycle assessment (LCA), it is most beneficial to utilize low concentration ammonium salt solutions for the Slag2PCC process. In this manner the post-treatment of the products does not require extensive use of washing and drying equipment, otherwise increasing the CO2 emissions of the process. The low solvent concentration Slag2PCC process causes negative CO2 emissions; thus, it can be seen as a carbon capture and utilization (CCU) method, which actually reduces the anthropogenic CO2 emissions compared to the alternative of not using the technology. Even if the amount of steel slag is too small for any substantial mitigation of global warming, the process can have both financial and environmental significance for individual steel manufacturers as a means to reduce the amounts of emitted CO2 and landfilled steel slag. Alternatively, it is possible to introduce the carbon dioxide directly into the mixture of steel slag and ammonium salt solution. The process would generate a 60-75% pure calcium carbonate mixture, the remaining 25-40% consisting of the residual steel slag. This calcium-rich material could be re-used in ironmaking as a fluxing agent instead of natural limestone. Even though this process option would require less process equipment compared to the Slag2PCC process, it still needs further studies regarding the practical usefulness of the products. Nevertheless, compared to several other CO2 emission reduction methods studied around the world, the within this thesis developed and studied processes have the advantage of existing markets for the produced materials, thus giving also a financial incentive for applying the technology in practice.
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The growing pharmaceutical interest, among others, in the polymorphic composition of the emerging solid end-products from production processes has been traced to the need for attainment of high product purity. This is more so as the presence of different polymorphs may constitute physical impurity of the product. Hence, the need for optimization of the yield of desired product component(s) through controlled crystallization kinetics for instance. This study was carried out to investigate the impact of pulsed electric field (PEF) irradiation on the crystal morphology of glycine obtained by cooling crystallization (without seeding) from commercial glycine sample in distilled deionized water solution. In doing so, three different pulse frequencies (294, 950 and 145 Hz) and a case without PEF were studied at three cooling rates (5, 10 and 20 ºC/h). The crystal products obtained were analyzed for polymorphic composition by powder x-ray diffraction (PXRD) and Fourier transform infrared (FTIR) spectroscopy while the particles characterization was done on Morphologi G3. The results obtained from this study showed that pulsed electric field irradiation had significant impact on metastability of the aqueous solution as well as on the polymorphic composition of the end product. With increasing PEF frequency applied, nucleation started earlier and the γ-glycine polymorph content of the product crystals increased. These were found to have been aided by cooling rate, as the most significant effect was observed at 5 ºC/h. It was also discovered that PEF application had no measurable impact on the pH of the aqueous solution as well as the size distribution of the particles. Cooling on the contrary was believed to be responsible for the broadening of the particle size distribution with a downward shift of the lower limit of the raw material from about 100 μm to between 10 and 50 μm.
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The aim of this thesis research work focused on the carbonate precipitation of magnesium using magnesium hydroxide Mg(OH)2 and carbon dioxide (CO2) gas at ambient temperature and pressure. The rate of dissolution of Mg(OH)2 and precipitation kinetics were investigated under different operating conditions. The conductivity and pH of the solution were inline monitored by a Consort meter and the solid samples gotten from the precipitation reaction were analysed by a laser diffraction analyzer Malvern Mastersizer to obtain particle size distributions (PSD) of crystal samples. Also the Mg2+ concentration profiles were determined from the liquid phase of the precipitate by ion chromatography (IC) analysis. Crystal morphology of the obtained precipitates were also investigated and discussed in this work. For the carbonation reaction of magnesium hydroxide in the present work, it was found that magnesium carbonate trihydrate (nesquehonite) was the main product and its formation occurred at a pH of around 7-8. The stirrer speed has a significant effect on the dissolution rate of Mg(OH)2. The highest obtained Mg2+ concentration level was 0.424 mol L-l for the 470 rpm and 0.387 mol L-1 for the 560 rpm which corresponded to the processing time of 45 mins and 40 mins respectively. The particle size distribution shows that the average particle size keeps increasing during the reaction as the CO2 is been fed to the system. The carbonation process is kinetically favored and simple as nesquehonite formation occurs in a very short time. It is a thermodynamically and chemically stable solid product, which allows for a long-term storage of CO2. Since the carbonation reaction is a complex system which includes dissolution of magnesium hydroxide particles, absorption of CO2, chemical reaction and crystallization, the dissolution of magnesium hydroxide was studied in hydrochloric acid (HCl) solvent with and without nitrogen (N2) inert gas. It was found on the dissolution part that the impeller speed had effect on the dissolution rate. The higher the impeller speed the higher the pH of the solution, although for the highest speed of 650rpm it was not the case. Therefore, it was concluded that the optimum speed of the stirrer was 560rpm. The influence of inert gas N2 on the dissolution rate of Mg(OH)2 particles could be seen based on measured pH, electric conductivity and Mg2+ concentration curves.
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La réduction de la taille des particules jusqu’à l’obtention de nanocristaux est l’une des approches utilisées afin d’améliorer la pénétration cutanée des médicaments à usage topique. Nous proposons que la fabrication d’une formulation semi solide (hydrogel) à base de nanosuspension de docosanol, aboutira à une diffusion du principe actif supérieure à celle du produit commercial Abreva®, à travers des membranes synthétiques de polycarbonates. Le broyage humide est la technique proposée pour la production des nanoparticules de docosanol. Nous proposons aussi la préparation d’une formulation semi-solide (hydrogel) à usage topique à partir de la nanosuspension de docosanol. La nanosuspension de docosanol est obtenue par dispersion du docosanol en solution aqueuse en présence du polymère stabilisant hydroxypropylcellulose (HPC) et du surfactant laurylsulfate de sodium (SDS) suivi d’un broyage humide à faible ou à haute énergie. L’hydrogel de docosanol nanoformulé est préparé à l’aide de la nanosuspension de docosanol qui subit une gélification par le carbopol Ultrez 21 sous agitation mécanique suivie d’une neutralisation au triéthanolamine TEA. La taille des particules de la nanosuspension et de l’hydrogel a été déterminée par diffusion dynamique de la lumière (DLS). Une méthode analytique de chromatographie liquide à haute performance (HPLC) munie d’un détecteur évaporatif (ELSD) a été développée et validée pour évaluer la teneur de docosanol dans les préparations liquides, dans les différentes nanosuspensions et dans les hydrogels de docosanol. L’état de cristallinité des nanocristaux dans la nanosuspension et dans l’hydrogel a été étudié par calorimétrie différentielle à balayage. La morphologie de la nanosuspension et de l’hydrogel de docosanol a été examinée par microscopie électronique à balayage (MEB). Les propriétés rhéologiques et de stabilité physique à différentes températures ont été aussi étudiées pour la formulation semi-solide (hydrogel). De même, la libération in vitro du docosanol contenu dans l’hydrogel et dans le produit commercial Abreva® a été étudiée à travers deux membranes de polycarbonates de taille de pores 400 et 800 nm. Dans le cas de nanosuspensions, des cristaux de docosanol de taille nanométrique ont été produits avec succès par broyage humide. Les nanoparticules de tailles variant de 197 nm à 312 nm ont été produites pour des pourcentages différents en docosanol, en polymère HPC et en surfactant SDS. Après lyophilisation, une augmentation de la taille dépendant de la composition de la formulation a été observée tout en restant dans la gamme nanométrique pour la totalité presque des formulations étudiées. Dans le cas des hydrogels examinés, la taille moyenne des particules de docosanol est maintenue dans la gamme nanométrique avant et après lyophilisation. L’analyse thermique des mélanges physiques, des nanosuspensions et des hydrogels de docosanol a révélé la conservation de l’état de cristallinité des nanocristaux de docosanol après broyage et aussi après gélification. L’examen par microscopie électronique à balayage (MEB) a montré que la nanosuspension et l’hydrogel ont tous deux une morphologie régulière et les nanoparticules ont une forme sphérique. De plus les nanoparticules de la nanosuspension ont presque la même taille inférieure à 300 nm en accord avec le résultat obtenu par diffusion dynamique de la lumière (DLS). Les nanoparticules de l’hydrogel ont une légère augmentation de taille par rapport à celle de la nanosuspension, ce qui est en accord avec les mesures de DLS. D’après les mesures rhéologiques, l’hydrogel de docosanol a un comportement pseudoplastique et un faible degré de thixotropie. L’étude de stabilité physique a montré que les formulations d’hydrogel sont stables à basse température (5°C) et à température ambiante (21°C) pendant une période d’incubation de 13 semaines et instable au-delà de 30°C après deux semaines. La méthode HPLC-ELSD a révélé des teneurs en docosanol comprises entre 90% et 110% dans le cas des nanosuspensions et aux alentours de 100% dans le cas de l’hydrogel. L’essai de diffusion in vitro a montré qu’il y a diffusion de docosanol de l’hydrogel à travers les membranes de polycarbonates, qui est plus marquée pour celle de pore 800 nm, tandis que celui du produit commercial Abreva® ne diffuse pas. Le broyage humide est une technique bien adaptée pour la préparation des nanosuspensions docosanol. Ces nanosuspensions peuvent être utilisée comme base pour la préparation de l’hydrogel de docosanol nanoformulé.
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A 2D porous material, Cu-3(tmen)(3)(tma)(2)(H2O)(2)(.)6.5H(2)O [tmen = N,N,N',N'-tetramethylethane-1,2-diamine; tmaH(3) = 1,3,5-benzenetricarboxylic acid/trimesic acid], has been synthesized and characterized by X-ray single crystal analysis, variable temperature magnetic measurements, IR spectra and XRPD pattern. The complex consists of 2D layers built by three crystallographically independent Cu(tmen) moieties bridged by tma anions. Of the three copper ions, Cu(1) and Cu(2) present distorted square pyramidal coordination geometry, while the third exhibits a severely distorted octahedral environment. The Cu(1)(tmen) and Cu(2)(tmen) building blocks bridged by tma anions give rise to chains with a zig-zag motif, which are cross-connected by Cu(3)(tmen)-tma polymers sharing metal ions Cu(2) through pendant tma carboxylates. The resulting 2D architecture extends in the crystallographic ab-plane. The adjacent sheets are embedded through the Cu(3)(tmen) tma chains, leaving H2O-filled channels. There are 6.5 lattice water molecules per formula unit, some of which are disordered. Upon heating, the lattice water molecules get eliminated without destroying the crystal morphology and the compound rehydrated reversibly on exposure to humid atmosphere. Magnetic data of the complex have been fitted considering isolated irregular Cu-3 triangles (three different J parameters) by applying the CLUMAG program. The best fit indicates three close comparable J parameters and very weak antiferromagnetic interactions are operative between the metal centers. (C) 2004 Elsevier B.V. All rights reserved.
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The renewed interest in magnetite (Fe3O4) as a major phase in different types of catalysts has led us to study the oxidation–reduction behaviour of its most prominent surfaces. We have employed computer modelling techniques based on the density functional theory to calculate the geometries and surface free energies of a number of surfaces at different compositions, including the stoichiometric plane, and those with a deficiency or excess of oxygen atoms. The most stable surfaces are the (001) and (111), leading to a cubic Fe3O4 crystal morphology with truncated corners under equilibrium conditions. The scanning tunnelling microscopy images of the different terminations of the (001) and (111) stoichiometric surfaces were calculated and compared with previous reports. Under reducing conditions, the creation of oxygen vacancies in the surface leads to the formation of reduced Fe species in the surface in the vicinity of the vacant oxygen. The (001) surface is slightly more prone to reduction than the (111), due to the higher stabilisation upon relaxation of the atoms around the oxygen vacancy, but molecular oxygen adsorbs preferentially at the (111) surface. In both oxidized surfaces, the oxygen atoms are located on bridge positions between two surface iron atoms, from which they attract electron density. The oxidised state is thermodynamically favourable with respect to the stoichiometric surfaces under ambient conditions, although not under the conditions when bulk Fe3O4 is thermodynamically stable with respect to Fe2O3. This finding is important in the interpretation of the catalytic properties of Fe3O4 due to the presence of oxidised species under experimental conditions.
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In this work, KHSO(4):Mn crystals doped with Mn and K(2)SO(4) were synthesized using an aqueous solution method. The samples were exposed to ionizing radiation in order to observe the effects on their physical properties. Raman spectroscopy was used to identify the structure of the crystals by detecting the vibrational frequencies of the crystalline lattice. Electron paramagnetic resonance (EPR) was used to study the creation of paramagnetic centers arising from exposure to ionizing radiation. This new synthesis method produces high quality K(2)SO(4) and KHSO(4):Mn crystals and allows control of structural, morphological, optical and magnetic properties. (C) 2009 Elsevier B.V. All rights reserved,
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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)