Recovery of acid and base from brackish water by bipolar membrane electrodialysis

Nesta dissertação pretendeu-se estudar a viabilidade do uso de eletrodiálise com membranas bipolares (BM) na recuperação de ácido clorídrico e de hidróxido de sódio a partir de um efluente industrial que contém 1.4 mol/L de cloreto de sódio. Estas membranas mostraram ser uma ferramenta eficiente para a produção de ácidos e bases a partir do respetivo sal. Foi feita uma seleção de diferentes membranas bipolares (Neosepta, Fumatech e PCA) e aniónicas (PC-SA e PC-ACID 60) na tentativa de encontrar a combinação mais adequada para o tratamento do efluente. Dependendo do critério, o melhor arranjo de membranas é o uso de PC-ACID 60 (membrana aniónica), PC-SK (membrana catiónica) e membranas bipolares do tipo Neosepta para maior pureza dos produtos; membranas bipolares Fumatech para maior eficiência de dessalinização e membranas bipolares PCA para um maior grau de dessalinização. Tecnologicamente foi possível obter uma dessalinização de 99.8% em quatro horas de funcionamento em modo batch com recirculação de todas as correntes. Independentemente da combinação usada é recomendável que o processo seja parado quando a densidade de corrente deixa de ser máxima, 781 A/m2. Assim é possível evitar o aumento de impurezas nos produtos, contra difusão, descida instantânea do pH e uma dessalinização pouco eficiente. A nível piloto o principal fornecedor de membranas e unidade de tratamento “stack” é a marca alemã PCA. Sendo assim realizaram-se ensaios de repetibilidade, contra difusão, avaliação económica e upscaling utilizando as membranas bipolares PCA. A nível económico estudou-se o uso de dois tipos de unidades de tratamento; EDQ 380 e EDQ 1600, para diferentes níveis de dessalinização (50, 75 e 80%). Tendo em conta a otimização económica, é recomendável uma dessalinização máxima de 80%, uma vez que a eficiência de processo a este ponto é de 40%. A aplicação do método com a unidade EDQ 1600 para uma dessalinização de 50% é a mais vantajosa economicamente, com custos de 16 €/m3 de efluente tratado ou 0,78 €/kg Cl- removido. O número de unidades necessárias é 4 posicionados em série.

Purification of complex biopharmaceuticals with new processes, advanced analytics and computer-aided process design tools

Dissertação para obtenção do Grau de Mestre em Biotecnologia

Effect of high pressure processing on the microbiology of skin-vacuum packaged sliced meat products: cooked pork ham, dry cured pork ham and marinated beef loin

High hydrostatic pressure is being increasingly investigated in food processing. It causes microbial inactivation and therefore extends the shelf life and enhances the safety of food products. Yeasts, molds, and vegetative cells of bacteria can be inactivated by pressures in the range of 200 to 700 MPa. Microorganisms are more or less sensitive to pressure depending on several factors such as type, strain and the phase or state of the cells. In general, Gram-positive organisms are usually more resistant than Gram-negative. High pressure processing modifies the permeability of the cell membrane, the ion exchange and causes changes in morphology and biochemical reactions, protein denaturations and inhibition of genetic mechanisms. High pressure has been used successfully to extend the shelf life of high-acid foods such as refrigerated fruit juices, jellies and jams. There is now an increasing interest in the use of this technology to extend the shelf life of low-acid foods such as different types of meat products.

Nanopartícul·les core-shell estabilitzades en polímer amb propietats calítiques i bactericides medioambientalment segure

Aquest projecte de doctorat és un treball interdisciplinari adreçat a l’obtenció de nous nanocompòsits (NCs) funcionals sintetitzats a partir de materials polimèrics bescanviadors d’ions que són modificats amb nanopartícules metàl•liques (NPMs) de diferent composició. Els materials desenvolupats s’avaluen en funció de dues possibles aplicacions: 1) com a catalitzadors de reaccions orgàniques d’interès actual (NCs basats en pal•ladi) i, 2) la seva dedicació a aplicacions bactericides en el tractament d’aigües domèstiques o industrials (NCs basats en plata). El desenvolupament de nanomaterials és de gran interès a l’actualitat donades les seves especials propietats, l’aprofitament de les quals és la força impulsora per a la fabricació de nous NCs. Les nanopartícules metàl•liques estabilitzades en polímer (Polymer Stabilized Metal Nanoparticles, PSNPM) s’han preparat mitjançant la tècnica in-situ de síntesi intermatricial (Inter-matrix synthesis, IMS) que consisteix en la càrrega seqüencial dels grups funcionals de les matrius polimèriques amb ions metàl•lics, i la seva posterior reducció química dins de la matriu polimèrica de bescanvi iònic. L’estabilització en matrius polimèriques evita l’agregació entre elles (self-aggreagtion), un dels principals problemes coneguts de les NPs. Pel desenvolupament d’aquesta metodologia, s’han emprat diferents tipus de matrius polimèriques de bescanvi iònic: membrana Sulfonated PolyEtherEtherKetone, SPEEK, així com fibres sintètiques basades en polypropilè amb diferents tipus de grups funcionals, que ens permeten el seu ús com a filtres en la desinfecció de solucions aquoses o com a material catalitzador. Durant el projecte s’ha anat avançant en l’optimització del material nanocomposite final per a les aplicacions d’interès, en quant activitat i funcionalitat de les nanopartícules i estabilitat del nanocomposite. Així, s’ha optimitzat la síntesi de NPs estabilitzades en resines de bescanvi iònic, realitzant un screening de diferents tipus de resines i la seva avaluació en aplicacions industrials d’interès.

Metallic and nonmetallic shine in luster: An elastic ion backscattering study

Luster is a metal glass nanocomposite layer first produced in the Middle East in early Islamic times ( 9th AD) made of metal copper or silver nanoparticles embedded in a silica-based glassy matrix. These nanoparticles are produced by ion exchange between Cu+ and Ag+ and alkaline ions from the glassy matrix and further growth in a reducing atmosphere. The most striking property of luster is its capability of reflecting light like a continuous metal layer and it was unexpectedly found to be linked to one single production parameter: the presence of lead in the glassy matrix composition. The purpose of this article is to describe the characteristics and differences of the nanoparticle layers developed on lead rich and lead free glasses. Copper luster layers obtained using the ancient recipes and methods are analyzed by means of elastic ion backscattering spectroscopy associated with other analytical techniques. The depth profile of the different elements is determined, showing that the luster layer formed in lead rich glasses is 5–6 times thinner and 3–4 times Cu richer. Therefore, the metal nanoparticles are more densely packed in the layer and this fact is related to its higher reflectivity. It is shown that lead influences the structure of the metal nanoparticle layer through the change of the precipitation kinetics

Sunitinib-eluting beads for chemoembolization: methods for in vitro evaluation of drug release.

Drug-eluting microspheres are used for embolization of hypervascular tumors and allow for local controlled drug release. Although the drug release from the microspheres relies on fast ion-exchange, so far only slow-releasing in vitro dissolution methods have been correlated to in vivo data. Three in vitro release methods are assessed in this study for their potential to predict slow in vivo release of sunitinib from chemoembolization spheres to the plasma, and fast local in vivo release obtained in an earlier study in rabbits. Release in an orbital shaker was slow (t50%=4.5h, 84% release) compared to fast release in USP 4 flow-through implant cells (t50%=1h, 100% release). Sunitinib release in saline from microspheres enclosed in dialysis inserts was prolonged and incomplete (t50%=9 days, 68% release) due to low drug diffusion through the dialysis membrane. The slow-release profile fitted best to low sunitinib plasma AUC following injection of sunitinib-eluting spheres. Although limited by lack of standardization, release in the orbital shaker fitted best to local in vivo sunitinib concentrations. Drug release in USP flow-through implant cells was too fast to correlate with local concentrations, although this method is preferred to discriminate between different sphere types.

Trypsin cleaves acid-sensing ion channel 1a in a domain that is critical for channel gating.

Acid-sensing ion channels (ASICs) are neuronal Na(+) channels that are members of the epithelial Na(+) channel/degenerin family and are transiently activated by extracellular acidification. ASICs in the central nervous system have a modulatory role in synaptic transmission and are involved in cell injury induced by acidosis. We have recently demonstrated that ASIC function is regulated by serine proteases. We provide here evidence that this regulation of ASIC function is tightly linked to channel cleavage. Trypsin cleaves ASIC1a with a similar time course as it changes ASIC1a function, whereas ASIC1b, whose function is not modified by trypsin, is not cleaved. Trypsin cleaves ASIC1a at Arg-145, in the N-terminal part of the extracellular loop, between a highly conserved sequence and a sequence that is critical for ASIC1a inhibition by the venom of the tarantula Psalmopoeus cambridgei. This channel domain controls the inactivation kinetics and co-determines the pH dependence of ASIC gating. It undergoes a conformational change during inactivation, which renders the cleavage site inaccessible to trypsin in inactivated channels.

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.

Nanosuodatuksen käyttö voimalaitoksen lisäveden valmistuksessa

Työssä selvitettiin nanosuodatuksen soveltuvuutta ja kannattavuutta voimalaitoksen lisäveden valmistuksessa. Kirjallisuusselvityksen ja nanosuodatuskokeiden tavoitteena oli arvioida nanosuodatukseen perustuvien lisäveden valmistusprosessien toiminnallista ja taloudellista kilpailukykyä perinteisiin prosesseihin verrattuna. Voimalaitoksen lisävedellä tarkoitetaan vesi-höyrykiertoon syötettävää vettä, joka korvaa kierrossa menetetyn veden. Nykyisin se valmistetaan vesijohto- tai pintavedestä käänteisosmoosiin ja ioninvaihtoon perustuvilla menetelmillä. Nanosuodatus on käänteisosmoosin tapaan kalvotekniikkaan perustuva erotusprosessi. Kaikki kalvot poistivat orgaanisen aineksen tehokkaasti (>90 %). Suolaretentioissa oli suuria eroja kalvojen välillä, vaikka kalvotoimittajien ilmoittamat retentiot olivat samaa tasoa. NF90-kalvo tuotti puhtainta permeaattia. Kahden kalvon (NF90 ja ESNA1-LF2) kohdalla havaittiin vuon alenemista, kun vuo oli kokeiden alussa noin 30 ja 40 L/m2/h. Likaantumisen merkkejä ei havaittu minkään kalvon kohdalla, kun vuoarvo oli maltillinen (n. 20 L/m2/h). Raakaveden vaikutus NF90-permeaatin laatuun oli vähäinen. Muilla kalvoilla raakaveden vaikutus permeaatin laatuun oli merkittävä. Investointi- ja käyttökustannusten perusteella nanosuodatukseen perustuvat lisäveden valmistusprosessit ovat kilpailukykyisiä nykyisiin lisäveden valmistusprosesseihin verrattuna. Pintavettä raakavetenä käyttävät nanosuodatusprosessit maksavat itsensä takaisin 3–5 vuodessa vesijohtovettä raakavetenä käyttävään käänteisosmoosiprosessiin verrattuna.

Kalvosuodatuksen ja adsorption yhdistäminen biojalostamon erotusprosesseissa

Tässä diplomityössä tutkittiin kalvosuodatuksen ja adsorption yhdistämistä biojalostamon erotusprosesseissa. Työn kirjallisuusosassa käsitellään hemiselluloosien erottamista puusta, kalvosuodatusta hemiselluloosien käsittelyssä sekä hemiselluloosien pilkkomista sokereiksi ja sokereiden kromatografista erotusta. Kokeellisessa osassa tutkittiin hemiselluloosahydrolysaatin fraktioimista kalvosuodatuksella ja adsorbenttikäsittelyn vaikutusta hydrolysaatin suodatettavuuteen. Kokeellisessa osassa tutkittiin myös fraktioinnin vaikutusta hartsien likaantumiseen happohydrolyysin jälkeisessä kromatografisessa erotuksessa. Työssä kokeiltiin useita erilaisia kalvoja, mutta suurin osa suodatuksista tehtiin regeneroidusta selluloosasta valmistetulla kalvolla UC030 ja polyeetterisulfoni kalvolla UFX5. Esikäsittelyyn käytettiin XAD16 adsorbenttia ja hartsien likaantumista tutkittiin CS12GC Na+ hartsilla. Suodatuskokeet tehtiin sekä laboratoriomittakaavan Amicon-suodattimella että pilot-mittakaavan CR- suodattimella. Työn tulokset osoittivat, että konsentroituneen hemiselluloosafraktion tuottaminen tehokkaasti ei onnistu kalvosuodatuksella ilman esikäsittelyä. Kalvon likaantumisen vuoksi permeaattivuo laski hyvin nopeasti niin alhaiseksi, ettei suodatuksen jatkaminen olisi taloudellisesti kannattavaa. Hydrolysaatin esikäsittely XAD16 adsorbentillä poisti tehokkaasti kalvoja likaavia uuteaineita ja ligniiniä. Adsorbenttikäsittelyn jälkeen hydrolysaatin suodattaminen onnistui ilman permeaattivuon huomattavaa alenemista toisessa suodatusvaiheessa ja saatiin aikaiseksi hyvin konsentroitunut hemiselluloosafraktio.

Metabolism of diglycine and triglycine by non-filtering kidneys

We have studied the metabolism of diglycine and triglycine in the isolated non-filtering rat kidney. Kidneys from adult male Wistar Kyoto rats weighing 250-350 g were perfused with Krebs-Henseleit solution containing either 1 mM diglycine or triglycine. The analysis of the peptide residues and their components was performed using an amino acid microanalyzer utilizing ion exchange chromatography. Diglycine was degraded to a final concentration of 0.09 mM after 120 min (91%); this degradation occurred predominantly during the first hour, with a 56% reduction of the initial concentration. The metabolism of triglycine occurred similarly, with a final concentration of 0.18 mM (82%); during the first hour there was a 67% reduction of the initial concentration of the tripeptide. Both peptides produced glycine in increasing concentrations, but there was a slightly lower recovery of glycine, suggesting its utilization by the kidney as fuel. The hydrolysis of triglycine also produced diglycine, which was also hydrolyzed to glycine. The results of the present study show the existence of functional endothelial or contraluminal membrane peptidases which may be important during parenteral nutrition.

High expression of human carboxypeptidase M in Pichia pastoris: Purification and partial characterization

Carboxypeptidase M (CPM) is an extracellular glycosylphosphatidyl-inositol-anchored membrane glycoprotein, which removes the C-terminal basic residues, lysine and arginine, from peptides and proteins at neutral pH. CPM plays an important role in the control of peptide hormones and growth factor activity on the cell surface. The present study was carried out to clone and express human CPM in the yeast Pichia pastoris in order to evaluate the importance of this enzyme in physiological and pathological processes. The cDNA for the enzyme was amplified from total placental RNA by RT-PCR and cloned in the vector pPIC9, which uses the methanol oxidase promoter and drives the expression of high levels of heterologous proteins in P. pastoris. The cpm gene, after cloning and transfection, was integrated into the yeast genome, which produced the active protein. The recombinant protein was secreted into the medium and the enzymatic activity was measured using the fluorescent substrate dansyl-Ala-Arg. The enzyme was purified by a two-step protocol including gel filtration and ion-exchange chromatography, resulting in a 1753-fold purified active protein (16474 RFU mg protein-1 min-1). This purification protocol permitted us to obtain 410 mg of the purified protein per liter of fermentation medium. SDS-PAGE showed that recombinant CPM migrated as a single band with a molecular mass similar to that of native placental enzyme (62 kDa), suggesting that the expression of a glycosylated protein had occurred. These results demonstrate for the first time the establishment of a method using P. pastoris to express human CPM necessary to the development of specific antibodies and antagonists, and the analysis of the involvement of this peptidase in different physiological and pathological processes