Continuous versus single bolus enteral nutrition: comparison of energy metabolism in humans.

Continuous respiratory exchange measurements were performed on five women and five men for 1 h before and 6 h after the administration of a milkshake (53% carbohydrates, 30% lipid, and 17% protein energy) given either as a single bolus dose or continuously during 3 h using a nasogastric tube. The energy administered corresponded to 2.3 times the postabsorptive resting energy expenditure. Resting energy expenditure, respiratory quotient, plasma glucose, and insulin concentrations increased sooner and steeper, and plasma free fatty acids levels decreased earlier with the meal ingested as a single dose than with continuous administration. The magnitude of nutrient-induced thermogenesis was greater (P less than 0.01) with the single dose (means +/- SE, 10.0 +/- 0.6%) than with the continuous administration (8.1 +/- 0.5%). The overall (6 h) substrate balances were not significantly different between the two modes of administration. It is concluded that the mode of enteral nutrient administration influences the immediate thermogenic response as well as changes in respiratory quotient, glycemia, and insulinemia; however, the overall nutrient balance was not affected by the mode of enteral nutrient administration.

Jäähdytykseen ja täyssuolanpoistoon perustuva lauhteen puhdistus soodakattilalaitoksella

Tämän diplomityön oleellisempana tavoitteena oli tutkia ioninvaihtohartsien pitkäaikaista toiminnallista lämpötilakestävyyttä kirjallisuustutkimuksin ja kuormituskokein. Lisaksi työssä optimoitiin taloudellisesti ja teknisesti paras kytkentävaihtoehto soodakattilan lauhteenpuhdistuslaitokselle. Tässä diplomityössä selvitettiin myös soodakattilan ulospuhallusveden sisältämien veden jälkiannostelukemikaalien ja epäpuhtauksien vaikutusta ioninvaihtohartsien vanhenemiseen.; Ioninvaihtohartsien lämpötilakestävyyteen liittyvät koeajot suoritettiin Stora Enso Laminating Papers Oy Kotkan tehtaalla. Koeajoja varten oli erikseen suunniteltu koeajolaitteisto, jossa lauhdenäytettä puhdistettiin patruunasuotimella ja sekavaihtimella. Sekavaihtimessa käytettiin vahvoja anioni- ja kationihartseja. Koeajoja oli yhteensä neljäkappaletta ja niissä tutkittiin hartsien lämpötilakestävyyttä ja anionihartsin silikaatti-vuodon riippuvuutta lämpötilasta. Lämpötilakestävyyskoeajoissa käytetyt hartsit lähetettiin Rohm and Haasille analysoitavaksi. Lopulta koeajojen tuloksia verrattiin kirjallisuudessa esitettyihin aikaisempiin tutkimuksiin. Lauhteenpuhdistuslaitoksen kytkentävaihtoehtojen optimoinnissa käytettiin apuna Kotkan ja UPM-Kymmene Oyj Pietarsaaren tehtaiden kokemuksia. Kytkentävaihtoehtojen energiataseet laskettiin kuudelle eri laitokselle, joiden syöttöveden virtaukset olivat 37 -180 kg/s. Lisaksi selvitettiin kytkentävaihtoehtojen investointikustannukset ja kertakäyttöhartsien vuotuiset kustannukset laitokselle, jossa syöttöveden virtaus oli 67 kg/s. Ulospuhalluksen talteenottojärjestelmän energiataseet laskettiin kuudelle eri laitokselle, joiden syöttöveden virtaukset olivat 37 - 180 kg/s. Laskelmien lähtökohtana käytettiin kunkin soodakattilan ulospuhallusveden määriä, jotka selvitettiin tehdasvierailujen yhteydessä. Ulospuhallusveden epäpuhtauksien ja jälkiannostelukemikaalien pitoisuudet arvioitiin kattilaveden perusteella. Aikaisempien kokemusten perusteella arvioitiin, että ulospuhallusvesi johdettaisiin lisäveden valmistukseen ennen suolanpoistosarjoja. loninvaihtohartsien kuormituskokeiden ja kirjallisuustutkimusten perusteella oli selkeästi nähtävissä, että etenkin anionihartsin kapasiteetti heikkeni nopeasti lämpötilan ollessa yli 60 °C. Kationihartsin suolanpoistolle kriittinen lämpötilaraja on 100 °C.Lisäksi yli 60 °C:ssa anionihartsi ei pysty poistamaan silikaattia lauhteesta. Seuraavaksi on esitelty lauhteenpuhdistuslaitoksen optimikytkentävaihtoehdot sekä vanhoille että uusille laitoksille. Vanhalle laitokselle, jossa lauhteet on puhdistettu aikaisemmin mekaanisella suotimella ja lisäveden puhdistuksessa on käytetty sekavaihdinta, paras kytkentävaihto on erilliset sekavaihtimet lauhteelle ja lisävedelle. Uudelle ja vanhalle laitokselle, jossa lauhteet on puhdistettu aikaisemmin mekaanisella suotimella ja lisäveden puhdistuksessa ei ole käytetty sekavaihdinta, paras kytkentävaihto on yhteiset sekavaihtimet lauhteelle ja lisävedelle. Lauhteen puhdistuksessa käytetyt sekavaihtimen toimintalämpötila on 45 °C molemmissa kytkentävaihtoehdoissa. Kertakäyttöhartsien käyttö osoittautui suuressa mittakaavassa kannattamattomaksi. Tämä asia tarvinnee kuitenkin jatkotutkimuksia. Ulospuhallusveden talteenotolla saadaan energiasäästöä 6-53 k¤/a riippuenlaitoksesta. Etenkin soodakattilalaitoksissa, joissa soodakattila ja vedenkäsittelylaitos sijaitsevat lähellä toisiaan, kannattaa ulospuhallusvesi johtaa lisäveden valmistukseen. Jos edellä mainittujen laitosten etäisyydet kasvavat, saattavat ulospuhallusjärjestelmän investointi-kustannukset nousta kohtuuttoman suureksi. Tämä työ osoitti myös, että ulospuhallusveden epäpuhtauksilla ei ole merkittävää vaikutusta kemiallisesti puhdistetun veden laatuun ennen suolanpoistolaitosta ja ioninvaihtohartsien vanhenemiseen.

Sakkaroosin hydrolyysi immobilisoidulla entsyymillä

Työssä tutkittiin sakkaroosin hydrolyysiä anioninvaihtohartseihin immobilisoidun entsyymin avulla tavoitteena löytää sellainen kantaja-entsyymi -yhdistelmä, jolla konversio halutuiksi lopputuotteiksi olisi mahdollisimman korkea. Työhön valittiin aikaisemmissa laboratoriokokeissa parhaita tuloksia saavuttaneet kantaja-entsyymi -parit. Entsyymeinä oli kaksi nestemäistä Saccharomyces cerevisiae -hiivasta eristettyjä entsyymivalmistetta. Kokeissa käytetyt kantajamateriaalit olivat erilaisia heikkoja anioninvaihtohartseja. Entsyymit immobilisoitiin kantajaan sekoitusreaktorissa ja niiden aktiivisuudet määritettiin sitomisen jälkeen. Hydrolyysikokeet tehtiin jatkuvatoimisessa kiintopetireaktorissa ja lisäksi panos-kokeina tutkittiin ominaisuuksiltaan erilaisten kantajien eroja hydrolyysissä. Reaktio-olosuhteet pidettiin kaikissa kokeissa samoina. Sakkaroosiliuoksen pitoisuus oli 50 p-%, reaktiolämpötila 50 oC ja pH 5. Kiintopetikolonnissa tutkittiin myös sakkaroosi-liuoksen viipymäajan vaikutusta sivutuotteiden syntyyn. Näytteet analysoitiin neste-kromatografilla. Kiintopetikolonnissa lyhimmän viipymäajan (15 min) kokeissa ainoastaan hitaimmilla kantaja-entsyymi -pareilla muodostui sivutuotteita, jotka hydrolyysireaktion edetessä kuitenkin hävisivät. Kun viipymäaikaa kasvatettiin sivutuotteiden synty väheni ja lopulta niitä ei havaittu syntyvän lainkaan. Hydrolyysin edetessä viipymäajan ollessa tarpeeksi pitkä pienet sivutuotekomponentit hävisivät sakkaroosin hajotessa kokonaan glukoosiksi ja fruktoosiksi. Verrattaessa partikkelikoon ja hartsimatriisin vaikutusta samaan entsyymiin sidottuna havaittiin, että niillä kummallakin on vaikutusta sekä sakkaroosin hydrolyysi-nopeuteen että sivutuotteiden muodostumiseen.

Uuttoprosessin suunnittelu

Teknologian kehitys ja prosessien tiukempi valvonta ovat alentaneet selluteollisuuden häviöitä tehden prosesseista suljetumpia. Valitettavasti nämä edistysaskeleet teknologiassa ovat lisänneet prosessiin kuulumattomien yhdisteiden määrää kemikaalien talteenottokierrossa. Näistä kemikaaleista haitallisimpia ovat kloridi- ja kaliumyhdisteet, jotka tulevat prosessiin raaka-aineiden ja prosessikemikaalien mukana. Kloridi ja kalium muodostavat emäksisissä liuoksissa epäorgaanisia liukoisia yhdisteitä, jotka rikastuvat lipeäkiertoon. Soodakattilassa kloridien läsnäolo alentaa tuhkan sulamislämpötilaa sekä tarttumispistettä, lisää korroosiota ja saostumien muodostumista kattilan pinnalle. Nämä seuraukset voivat vähentää vuosituotantoa ja nostaa korjauskustannuksia. Kaliumin ja kloridin rikastumista talteenottokiertoon voidaan estää poistamalla ne prosessista. Prosessiin kuulumattomat yhdisteet tulisi poistaa talteenottoprosessista ja säilyttää samalla korkea kemikaalien talteenottoprosentti. Koska kaliumin ja kloridin rikastumiskertoimet soodakattilan tuhkassa ovat korkeita, on tuhkan käsittely tehokasta. Kloridin ja kaliumin poistoon on kehitetty menetelmiä, joilla voidaan vähentää hyödyllisten kemikaalien häviöitä. Näitä menetelmiä ovat uutto, ioninvaihto, elektrodialyysi, jäähdytyskiteytys ja haihdutuskiteytys. Menetelmissä tuhka jaetaan kloridi- ja kaliumpitoiseen osaan ja natriumsulfaattipitoiseen osaan. Kloridi ja kalium poistetaan prosessista ja loput palautetaan lipeäkiertoon. Kloridin ja kaliumin poistoa tuhkasta tutkittiin uuttamalla tuhkaa vedellä. Parhaissa käyttöolosuhteissa natriumsulfaatin liukoisuus veteen on huomattavasti alhaisempi kuin kaliumkloridin liukoisuus veteen. Optimaalinen uuttolämpötila ja tuhka-vesisuhde määritettiin siten, että kloridi- ja kaliumpitoisuudet suodoksessa olivat mahdollisimman korkeat sekä natriumin ja muiden anioneiden pitoisuudet suodoksessa mahdollisimman alhaiset. Saatuja tuloksia käytettiin jatkuvatoimisen uuttoprosessin suunnittelussa.

Stabilization of the ionic form of weak acid cation exchange resins

Weak acid cation exchange (WAC) resins are used in the chromatographic separation of betaine from vinasse, a by-product of sugar industry. The ionic form of the resin determines the elution time of betaine. When a WAC-resin is in hydrogen form, the retention time of betaine is the longest and betaine elutes as the last component of vi-nasse from the chromatographic column. If the feed solution contains salts and its pH is not acidic enough to keep the resin undissociated, the ionic form of the hydrogen form resin starts to alter. Vinasse contains salts and its pH is around 5, it also contains weak acids. To keep the metal ion content (Na/H ratio) of the resin low enough to ensure successful separation of betaine, acid has to be added to either eluent (water) or vinasse. The aim of the present work was to examine by laboratory experiments which option requires less acid. Also the retention mechanism of betaine was investigated by measuring retention volumes of acetic acid and choline in different Na/H ratios of the resin. It was found that the resulting ionic form of the resin is the same regardless of whether the regeneration acid is added to the eluent or the feed solution (vinasse). Be-sides the salt concentration and the pH of vinasse, also the concentration of weak acids in the feed affects the resulting ionic form of the resin. The more buffering capacity vinasse has, the more acid is required to keep the ionic form of the resin desired. Vinasse was found to be quite strong buffer solution, which means relatively high amounts of acid are required to prevent the Na/H ratio from increasing too much. It is known that the retention volume of betaine decreases significantly, when the Na/H ratio increases. This is assumed to occur, because the amount of hydrogen bonds between the carboxylic groups of betaine and the resin decreases. Same behavior was not found with acetic acid. Choline has the same molecular structure as betaine, but instead of carboxylic group it has hydroxide group. The retention volume of choline increased as the Na/H ratio of the resin increased, because of the ion exchange reaction between choline cation and dissociated carboxylic group of the resin. Since the retention behavior of choline on the resin is opposite to the behavior of be-taine, the strong affinity of betaine towards hydrogen form WAC-resin has to be based on its carboxylic group. It is probable that the quaternary ammonium groups also affect the behavior of the carboxylic groups of betaine, causing them to form hydrogen bonds with the carboxylic groups of the resin.

Azolium-based systems: application of an anion exchange resin (A- form) method and 1H NMR analysis of the charged-assisted (CH)+·anion hydrogen bonds

The counteranion exchange of quaternary 1,2,3-triazolium salts was examined using a simple method that permitted halide ions to be swap for a variety of anions using an anion exchange resin (A¯ form). The method was applied to 1,2,3-triazolium-based ionic liquids and the iodideto- anion exchange proceeded in excellent to quantitative yields, concomitantly removing halide impurities. Additionally, an anion exchange resin (N3¯ form) was used to obtain the benzyl azide from benzyl halide under mild reaction. Likewise, following a similar protocol, bis(azidomethyl)arenes were also synthesized in excellent yields. The results of a proton NMR spectroscopic study of simple azolium-based ion pairs are discussed, with attention focused on the significance of the charged-assisted (CH)+···anion hydrogen bonds of simple azolium systems such as 1-butyl-3-methylimidazolium and 1-benzyl-3-methyl-1,2,3-triazolium salts.

Azolium-based systems: application of an anion exchange resin (A- form) method and 1H NMR analysis of the charged-assisted (CH)+·anion hydrogen bonds

The counteranion exchange of quaternary 1,2,3-triazolium salts was examined using a simple method that permitted halide ions to be swap for a variety of anions using an anion exchange resin (A¯ form). The method was applied to 1,2,3-triazolium-based ionic liquids and the iodideto- anion exchange proceeded in excellent to quantitative yields, concomitantly removing halide impurities. Additionally, an anion exchange resin (N3¯ form) was used to obtain the benzyl azide from benzyl halide under mild reaction. Likewise, following a similar protocol, bis(azidomethyl)arenes were also synthesized in excellent yields. The results of a proton NMR spectroscopic study of simple azolium-based ion pairs are discussed, with attention focused on the significance of the charged-assisted (CH)+···anion hydrogen bonds of simple azolium systems such as 1-butyl-3-methylimidazolium and 1-benzyl-3-methyl-1,2,3-triazolium salts.

Azolium-based systems: application of an anion exchange resin (A- form) method and 1H NMR analysis of the charged-assisted (CH)+·anion hydrogen bonds

The counteranion exchange of quaternary 1,2,3-triazolium salts was examined using a simple method that permitted halide ions to be swap for a variety of anions using an anion exchange resin (A¯ form). The method was applied to 1,2,3-triazolium-based ionic liquids and the iodideto- anion exchange proceeded in excellent to quantitative yields, concomitantly removing halide impurities. Additionally, an anion exchange resin (N3¯ form) was used to obtain the benzyl azide from benzyl halide under mild reaction. Likewise, following a similar protocol, bis(azidomethyl)arenes were also synthesized in excellent yields. The results of a proton NMR spectroscopic study of simple azolium-based ion pairs are discussed, with attention focused on the significance of the charged-assisted (CH)+···anion hydrogen bonds of simple azolium systems such as 1-butyl-3-methylimidazolium and 1-benzyl-3-methyl-1,2,3-triazolium salts.

Synthesis of percarboxylic acids in microreactor

Percarboxylic acids are commonly used as disinfection and bleaching agents in textile, paper, and fine chemical industries. All of these applications are based on the oxidative potential of these compounds. In spite of high interest in these chemicals, they are unstable and explosive chemicals, which increase the risk of synthesis processes and transportation. Therefore, the safety criteria in the production process should be considered. Microreactors represent a technology that efficiently utilizes safety advantages resulting from small scale. Therefore, microreactor technology was used in the synthesis of peracetic acid and performic acid. These percarboxylic acids were produced at different temperatures, residence times and catalyst i.e. sulfuric acid concentrations. Both synthesis reactions seemed to be rather fast because with performic acid equilibrium was reached in 4 min at 313 K and with peracetic acid in 10 min at 343 K. In addition, the experimental results were used to study the kinetics of the formation of performic acid and peracetic acid. The advantages of the microreactors in this study were the efficient temperature control even in very exothermic reaction and good mixing due to the short diffusion distances. Therefore, reaction rates were determined with high accuracy. Three different models were considered in order to estimate the kinetic parameters such as reaction rate constants and activation energies. From these three models, the laminar flow model with radial velocity distribution gave most precise parameters. However, sulfuric acid creates many drawbacks in this synthesis process. Therefore, a ´´greener´´ way to use heterogeneous catalyst in the synthesis of performic acid in microreactor was studied. The cation exchange resin, Dowex 50 Wx8, presented very high activity and a long life time in this reaction. In the presence of this catalyst, the equilibrium was reached in 120 second at 313 K which indicates a rather fast reaction. In addition, the safety advantages of microreactors were investigated in this study. Four different conventional methods were used. Production of peracetic acid was used as a test case, and the safety of one conventional batch process was compared with an on-site continuous microprocess. It was found that the conventional methods for the analysis of process safety might not be reliable and adequate for radically novel technology, such as microreactors. This is understandable because the conventional methods are partly based on experience, which is very limited in connection with totally novel technology. Therefore, one checklist-based method was developed to study the safety of intensified and novel processes at the early stage of process development. The checklist was formulated using the concept of layers of protection for a chemical process. The traditional and three intensified processes of hydrogen peroxide synthesis were selected as test cases. With these real cases, it was shown that several positive and negative effects on safety can be detected in process intensification. The general claim that safety is always improved by process intensification was questioned.

Supramolecular polymers azo-containing : photo-responsive block copolymer elastomers and homopolymers

Beaucoup d'efforts dans le domaine des matériaux polymères sont déployés pour développer de nouveaux matériaux fonctionnels pour des applications spécifiques, souvent très sophistiquées, en employant des méthodes simplifiées de synthèse et de préparation. Cette thèse porte sur les polymères photosensibles – i.e. des matériaux fonctionnels qui répondent de diverses manières à la lumière – qui sont préparés à l'aide de la chimie supramoléculaire – i.e. une méthode de préparation qui repose sur l'auto-assemblage spontané de motifs moléculaires plus simples via des interactions non covalentes pour former le matériau final désiré. Deux types de matériaux photosensibles ont été ciblés, à savoir les élastomères thermoplastiques à base de copolymères à blocs (TPE) et les complexes d'homopolymères photosensibles. Les TPEs sont des matériaux bien connus, et même commercialisés, qui sont généralement composés d’un copolymère tribloc, avec un bloc central très flexible et des blocs terminaux rigides qui présentent une séparation de phase menant à des domaines durs isolés, composés des blocs terminaux rigides, dans une matrice molle formée du bloc central flexible, et ils ont l'avantage d'être recyclable. Pour la première fois, au meilleur de notre connaissance, nous avons préparé ces matériaux avec des propriétés photosensibles, basé sur la complexation supramoléculaire entre un copolymère tribloc simple parent et une petite molécule possédant une fonctionnalité photosensible via un groupe azobenzène. Plus précisément, il s’agit de la complexation ionique entre la forme quaternisée d'un copolymère à blocs, le poly(méthacrylate de diméthylaminoéthyle)-poly(acrylate de n-butyle)-poly(méthacrylate de diméthylaminoéthyle) (PDM-PnBA-PDM), synthétisé par polymérisation radicalaire par transfert d’atomes (ATRP), et l'orange de méthyle (MO), un composé azo disponible commercialement comportant un groupement SO3 -. Le PnBA possède une température de transition vitreuse en dessous de la température ambiante (-46 °C) et les blocs terminaux de PDM complexés avec le MO ont une température de transition vitreuse élevée (140-180 °C, en fonction de la masse molaire). Des tests simples d'élasticité montrent que les copolymères à blocs complexés avec des fractions massiques allant de 20 à 30% présentent un caractère élastomère. Des mesures d’AFM et de TEM (microscopie à force atomique et électronique à ii transmission) de films préparés à l’aide de la méthode de la tournette, montrent une corrélation entre le caractère élastomère et les morphologies où les blocs rigides forment une phase minoritaire dispersée (domaines sphériques ou cylindriques courts). Une phase dure continue (morphologie inversée) est observée pour une fraction massique en blocs rigides d'environ 37%, ce qui est beaucoup plus faible que celle observée pour les copolymères à blocs neutres, dû aux interactions ioniques. La réversibilité de la photoisomérisation a été démontrée pour ces matériaux, à la fois en solution et sous forme de film. La synthèse du copolymère à blocs PDM-PnBA-PDM a ensuite été optimisée en utilisant la technique d'échange d'halogène en ATRP, ainsi qu’en apportant d'autres modifications à la recette de polymérisation. Des produits monodisperses ont été obtenus à la fois pour la macroamorceur et le copolymère à blocs. À partir d'un seul copolymère à blocs parent, une série de copolymères à blocs partiellement/complètement quaternisés et complexés ont été préparés. Des tests préliminaires de traction sur les copolymères à blocs complexés avec le MO ont montré que leur élasticité est corrélée avec la fraction massique du bloc dur, qui peut être ajustée par le degré de quaternisation et de complexation. Finalement, une série de complexes d'homopolymères auto-assemblés à partir du PDM et de trois dérivés azobenzènes portant des groupes (OH, COOH et SO3) capables d'interactions directionnelles avec le groupement amino du PDM ont été préparés, où les dérivés azo sont associés avec le PDM, respectivement, via des interactions hydrogène, des liaisons ioniques combinées à une liaison hydrogène à travers un transfert de proton (acidebase), et des interactions purement ioniques. L'influence de la teneur en azo et du type de liaison sur la facilité d’inscription des réseaux de diffraction (SRG) a été étudiée. L’efficacité de diffraction des SRGs et la profondeur des réseaux inscrits à partir de films préparés à la méthode de la tournette montrent que la liaison ionique et une teneur élevée en azo conduit à une formation plus efficace des SRGs.

Solid acid-catalyzed dehydration/Beckmann rearrangement of aldoximes: towards high atom efficiency green processes

Rare earth metal ion exchanged (La3+, Ce3+, RE3+) KFAU-Y zeolites were prepared by simple ion-exchange methods and have been characterized using different physico-chemical techniques. In this paper a novel application of solid acid catalysts in the dehydration/ Beckmann rearrangement of aldoximes; benzaldoxime and 4-methoxybenzaldoxime is reported. Dehydration/Beckmann rearrangement reactions of benzaldoxime and 4-methoxybenzaldoxime is carried out in a continuous down flow reactor at 473K. 4-Methoxybenzaldoxime gave both Beckmann rearrangement product (4-methoxyphenylformamide) and dehydration product (4-methoxybenzonitrile) in high overall yields. The difference in behavior of the aldoximes is explained in terms of electronic effects. The production of benzonitrile was near quantitative under heterogeneous reaction conditions. The optimal protocol allows nitriles to be synthesized in good yields through the dehydration of aldoximes. Time on stream studies show a fast decline in the activity of the catalyst due to neutralization of acid sites by the basic reactant and product molecules.

Effect of cycling on the magnetization of ion exchanged magnetic nanocomposite based on polystyrene

Magnetic nanocomposites containing iron oxide particles embedded in a polymer matrix have been synthesized using the method of ion exchange. They have been characterized by using low temperature and room temperature magnetic measurements and Mo¨ ssbauer spectroscopy. The iron content in these samples has also been determined. The results have been analysed and explained. The physical and chemical properties of these nanocomposite materials are different from those of the bulk. Some of the unique properties of these materials find application in information storage, color imaging, ferrofluids and magnetic refrigeration

Effects of orange juice formulation on prebiotic functionality using an in vitro colonic model sytem

A three-stage continuous fermentative colonic model system was used to monitor in vitro the effect of different orange juice formulations on prebiotic activity. Three different juices with and without Bimuno, a GOS mixture containing galactooligosaccharides (B-GOS) were assessed in terms of their ability to induce a bifidogenic microbiota. The recipe development was based on incorporating 2.75g B-GOS into a 250 ml serving of juice (65°Brix of concentrate juice). Alongside the production of B-GOS juice, a control juice - orange juice without any additional Bimuno and a positive control juice, containing all the components of Bimuno (glucose, galactose and lactose) in the same relative proportions with the exception of B-GOS were developed. Ion Exchange Chromotography analysis was used to test the maintenance of bimuno components after the production process. Data showed that sterilisation had no significant effect on concentration of B-GOS and simple sugars. The three juice formulations were digested under conditions resembling the gastric and small intestinal environments. Main bacterial groups of the faecal microbiota were evaluated throughout the colonic model study using 16S rRNA-based fluorescence in situ hybridization (FISH). Potential effects of supplementation of the juices on microbial metabolism were studied measuring short chain fatty acids (SCFAs) using gas chromatography. Furthermore, B-GOS juices showed positive modulations of the microbiota composition and metabolic activity. In particular, numbers of faecal bifidobacteria and lactobacilli were significantly higher when B-GOS juice was fermented compared to controls. Furthermore, fermentation of B-GOS juice resulted in an increase in Roseburia subcluster and concomitantly increased butyrate production, which is of potential benefit to the host. In conclusion, this study has shown B-GOS within orange juice can have a beneficial effect on the fecal microbiota.

Adsorption Isotherms for Removal of Linoleic Acid from Ethanolic Solutions Using the Strong Anion Exchange Resin Amberlyst A26 OH

Adsorption isotherms for the removal of linoleic acid from aqueous ethanol were measured using a strong anion exchange resin (Amberlyst A26 OH). The data for linoleic acid were compared with previously published results for oleic acid. The equilibrium data were correlated using the Langmuir and Freundlich isotherms. Lower average deviations between experimental and calculated results were obtained with the Langmuir model. The capacity of the resin for adsorbing linoleic acid was evaluated at different water contents in ethanol, 100 w = 0.50 to 15.27, and at 298.15 K. The water content in ethanol does not influence significantly the equilibrium behavior, and the strong anion exchange resin has a good performance in the removal of linoleic acid from the liquid phase.

Modificação estrutural de bentonitas nacionais : caracterização e estudos de adsorção

São apresentados os aspectos teóricos, práticos e bibliográficos envolvidos no desenvolvimento da tese de doutorado intitulada Modificação estrutural de bentonitas nacionais: caracterização e estudos de adsorção. O trabalho consistiu no desenvolvimento de um material adsorvente a partir de bentonitas, do tipo montmorilonitas, modificadas estruturalmente com o objetivo de aumentar sua capacidade de adsorção de poluentes, orgânicos e inorgânicos. O estudo visa incrementar o valor agregado deste recurso mineral e insere-se na área de tratamento de efluentes líquidos usando adsorventes não tradicionais, eficientes e de baixo custo em substituição ao carvão ativado ou às resinas de troca iônica. Foram estudadas as propriedades físicas e químicas; distribuição de tamanho de partículas, área superficial, potenciais eletrocinéticos, capacidade de troca catiônica, composição mineralógica, morfologia superficial e espaçamento basal, bem como as propriedades adsorptivas dos argilominerais não tratados e modificados, não modificadas e pilarizadas respectivamente. Também são discutidos os mecanismos de adsorção envolvidos e o desenvolvimento de um reator contínuo (adsorção em flocos) e de separação sólido/líquido. As modificações estruturais dos argilominerais foram realizadas via homoionização com cloreto de cálcio e posterior intercalação com compostos orgânicos com ação quelante de metais. A FENAN, bentonita obtida pela intercalação com Orto Fenantrolina (OF), foi a que apresentou melhor viabilidade técnica em termos de adsorção, adsorção/dessorção, floculação e de acumulação de poluentes na forma floculada e não floculada. Adicionalmente os estudos de reversibilidade da intercalação revelaram a alta estabilidade da OF na FENAN, em soluções fortemente ácidas, onde aproximadamente 90% da OF permanece ligada à superfície da argila. A quantidade de OF adsorvida na forma de unidades micelares foi de 112 mg por grama de bentonita a pH 8,5 ± 0,5. A caracterização das bentonitas, via difração de Raios X, análise térmica, microscopia eletrônica de varredura e por microscopia de força atômica, revelou que as FENAN possuem um comportamento estrutural muito estável ao longo da seqüência de adsorção/dessorção e que após a adsorção de poluentes inorgânicos, o quelato metálico formado apresenta alta estabilidade dentro da estrutura da organobentonita. A capacidade de acumulação alcançada nas FENAN foi de 110 mg de Cu/g de bentonita, valor superior à de diversos materiais adsorventes alternativos propostos em outros trabalhos similares. Os estudos de acumulação das FENAN floculadas – FENANFLOC, indicaram que a presença de floculante, na quantidade utilizada, não afeta significativamente a capacidade de remoção das bentonitas modificadas. Este comportamento apresentado, permitiu o desenvolvimento do Reator Expandido de Flocos Adsorventes (REFA), cujas características e parâmetros operacionais são discutidos em detalhe. Finalmente, os resultados são discutidos em termos dos fenômenos interfaciais envolvidos e dos potenciais práticos deste novo adsorvente e da nova técnica de adsorção em flocos no REFA.