Sequentially aerated membrane biofilm reactors for autotrophic nitrogen removal: microbial community composition and dynamics

Membrane-aerated biofilm reactors performing autotrophic nitrogen removal can be successfully applied to treat concentrated nitrogen streams. However, their process performance is seriously hampered by the growth of nitrite oxidizing bacteria (NOB). In this work we document how sequential aeration can bring the rapid and long-term suppression of NOB and the onset of the activity of anaerobic ammonium oxidizing bacteria (AnAOB). Real-time quantitative polymerase chain reaction analyses confirmed that such shift in performance was mirrored by a change in population densities, with a very drastic reduction of the NOB Nitrospira and Nitrobacter and a 10-fold increase in AnAOB numbers. The study of biofilm sections with relevant 16S rRNA fluorescent probes revealed strongly stratified biofilm structures fostering aerobic ammonium oxidizing bacteria (AOB) in biofilm areas close to the membrane surface (rich in oxygen) and AnAOB in regions neighbouring the liquid phase. Both communities were separated by a transition region potentially populated by denitrifying heterotrophic bacteria. AOB and AnAOB bacterial groups were more abundant and diverse than NOB, and dominated by the r-strategists Nitrosomonas europaea and Ca. Brocadia anammoxidans, respectively. Taken together, the present work presents tools to better engineer, monitor and control the microbial communities that support robust, sustainable and efficient nitrogen removal

Novel Bioconjugates of Aminolevulinic Acid with Nucleosides

Esters and amino acid derivatives of 5-aminolevulinic acid (ALA) are efficient prodrugs for the production of protoporphyrin IX (PpIX), which has been used in photodynamic cancer therapy (PDT). The synthesis of novel bioconjugates combining ALA with adenosine and thymidine is reported. The novel bioconjugates have been made using a robust methodology. The new class of prodrugs contains one, two, or three ALA per molecule. Preliminary cell tests in human cancer cell lines indicate that the thymidine conjugate of ALA is an efficient prodrug for PDT.

1,2-Dimethylindole-3-sulfonyl (MIS) as protecting group for the side chain of arginine

The protection of arginine (Arg) side chains is a crucial issue in peptide chemistry because of the propensity of the basic guanidinium group to produce side reactions. Currently, sulfonyl-type protecting groups, such as 2,2,5,7,8-pentamethylchroman (Pmc) and 2,2,4,6,7-pentamethyldihydrobenzofurane (Pbf), are the most widely used for this purpose. Nevertheless, Arg side chain protection remains problematic as a result of the acid stability of these two compounds. This issue is even more relevant in Arg-rich sequences, acid-sensitive peptides and large-scale syntheses. The 1,2-dimethylindole-3-sulfonyl (MIS) group is more acid-labile than Pmc and Pbf and can therefore be a better option for Arg side chain protection. In addition, MIS is compatible with tryptophan-containing peptides.

Etude de la toxicité hépatique de la cocaïne associée à de l'alcool: Effets de l'éthanol sur le métabolisme de la cocaïne dan les hépatocytes de rat en suspension et dans un modèle enzymatique humain

Le but essentiel de notre travail a été d?étudier la capacité du foie, premier organe de métabolisation des xénobiotiques, à dégrader la cocaïne en présence d?éthanol, à l?aide de deux modèles expérimentaux, à savoir un modèle cellulaire (les hépatocytes de rat en suspension) et un modèle acellulaire (modèle reconstitué in vitro à partir d?enzymes purifiées de foie humain). La première partie a pour objectifs de rechercher les voies de métabolisation de la cocaïne qui sont inhibées et / ou stimulées en présence d?éthanol, sur hépatocytes isolés de rat. Dans ce but, une méthode originale permettant de séparer et de quantifier simultanément la cocaïne, le cocaéthylène et huit de leurs métabolites respectifs a été développée par Chromatographie Phase Gazeuse couplée à la Spectrométrie de Masse (CPG / SM). Nos résultats préliminaires indiquent que l?éthanol aux trois concentrations testées (20, 40 et 80 mM) n?a aucun effet sur la cinétique de métabolisation de la cocaïne. Notre étude confirme que l?addition d?éthanol à des cellules hépatiques de rat en suspension supplémentées en cocaïne résulte en la formation précoce de benzoylecgonine et de cocaéthylène. L?apparition retardée d?ecgonine méthyl ester démontre l?activation d?une deuxième voie de détoxification. La production tardive d?ecgonine indique une dégradation de la benzoylecgonine et de l?ecgonine méthyl ester. De plus, la voie d?oxydation intervenant dans l?induction du stress oxydant en produisant de la norcocaïne est tardivement stimulée. Enfin, notre étude montre une métabolisation complète de la concentration initiale en éthanol par les hépatocytes de rat en suspension. La deuxième partie a pour but de déterminer s?il existe d?autres enzymes que les carboxylesterases formes 1 et 2 humaines ayant une capacité à métaboliser la cocaïne seule ou associée à de l?éthanol. Pour ce faire, une méthode de micropurification par chromatographie liquide (Smart System®) a été mise au point. Dans le cadre de nos dosages in situ de la cocaïne, du cocaéthylène, de la benzoylecgonine, de l?acide benzoïque et de la lidocaïne, une technique par Chromatographie Liquide Haute Performance couplée à une Détection par Barrette de Diode (CLHP / DBD) et une méthode de dosage de l?éthanol par Chromatographie Phase Gazeuse couplée à une Détection par Ionisation de Flamme équipée d?un injecteur à espace de tête (espace de tête CPG / DIF) ont été développées. La procédure de purification nous a permis de suspecter la présence d?autres enzymes que les carboxylesterases formes 1 et 2 de foie humain impliquées dans le métabolisme de la cocaïne et déjà isolées. A partir d?un modèle enzymatique reconstitué in vitro, nos résultats préliminaires indiquent que d?autres esterases que les formes 1 et 2 de foie humain sont impliquées dans l?élimination de la cocaïne, produisant benzoylecgonine et ecgonine méthyl ester. De plus, nous avons montré que les sensibilités de ces enzymes à l?éthanol sont variables.<br/><br/>The main purpose of our work was to study the ability of the liver, as the first organ to metabolise xenobiotic substances, to degrade cocaine in the presence of ethanol. In order to do this, we used two experimental models, namely a cellular model (rat liver cells in suspension) and an a-cellular model (model reconstructed in vitro from purified human liver enzymes). The purpose of the first part of our study was to look for cocaine metabolising processes which were inhibited and / or stimulated by the presence of ethanol, in isolated rat liver cells. With this aim in mind, an original method for simultaneously separating and quantifying cocaine, cocaethylene and eight of their respective metabolites was developed by Vapour Phase Chromatography coupled with Mass Spectrometry (VPC / MS). Our preliminary results point out that ethanol at three tested concentrations (20, 40 et 80 mM) have no effect on the kinetic of metabolisation of cocaine. Our study confirms that the addition of alcohol to rat liver cells in suspension, supplemented with cocaine, results in the premature formation of ecgonine benzoyl ester and cocaethylene. The delayed appearance of ecgonine methyl ester shows that a second detoxification process is activated. The delayed production of ecgonine indicates a degradation of the ecgonine benzoyl ester and the ecgonine methyl ester. Moreover, the oxidising process which occurs during the induction of the oxidising stress, producing norcocaine, is stimulated at a late stage. Finally, our study shows the complete metabolisation of the initial alcohol concentration by the rat liver cells in suspension. The second part consisted in determining if enzymes other than human carboxylesterases 1 and 2, able to metabolise cocaine on its own or with alcohol, existed. To do this, a micropurification method us ing liquid phase chromatography (Smart System®) was developed. A technique based on High Performance Liquid Chromatography coupled with a Diode Array Detection (HPLC / DAD) in the in situ proportioning of cocaine, cocaethylene, ecgonine benzoyl ester, benzoic acid and lidocaine, and a method for proportioning alcohol by quantifying the head space using Vapour Phase Chromatography coupled with a Flame Ionisation Detection (head space VPC / FID) were used. The purification procedure pointed to the presence of enzymes other than the human liver carboxylesterases, forms 1 and 2, involved in the metabolism of cocaine and already isolated. The preliminary results drawn from an enzymatic model reconstructed in vitro indicate that human liver carboxylesterases, other than forms 1 and 2, are involved in the elimination of cocaine, producing ecgonine benzoyl ester and ecgonine methyl ester. Moreover, we have shown that the sensitivity of these enzymes to alcohol is variable.

An ethanol-based process to simultaneously extract and fractionate carotenoids from Mauritia flexuosa L. Pulp

Mauritia vinifera (buriti) is a palm tree that grows wild in different areas of Brazil, particularly in the Amazonian region. The buriti oil is rich in carotenoids, especially in β-carotene. The growing interest in other natural sources of β-carotene has stimulated the industrial use of buriti as a raw material for pulp oil extraction. Most processes are based on the conventional technologies, involving drying and pressing the pulp for oil recovery and further separation of carotenoids in a liquid phase using organics solvents. In the present work, the ethanol-based process was evaluated for simultaneous carotenoids recovering and fractionating from buriti pulp. The raw material and ethanol, 1:4 ratio, were placed in an erlenmeyer flask and maintained at 30rpm for 1 hour in a temperature-controlled bath at 65ºC. The mixture was filtered under vacuum and cooling at 10ºC to allow for the separation of the solvent in two phases. Carotenoids composition, determined by HPLC, has indicated a β-carotene concentration about 12 times greater in the lower phase than in the upper phase. The profile of the carotenoids in the denser phase is quite similar to that of raw buriti oil, and the concentration of total carotenoids is 40% higher than that of the original raw oil, making the ethanol-based process particularly attractive for industrial applications.

Easy introduction of maleimides at different positions of oligonucleotide chains for conjugation purposes

[2,5-Dimethylfuran]-protected maleimides were placed at both internal positions and the 3'-end of oligonucleotides making use of solid-phase synthesis procedures. A new phosphoramidite derivative and a new solid support incorporating the protected maleimide moiety were prepared for this purpose. In all cases maleimide deprotection (retro-Diels-Alder reaction) followed by reaction with thiol-containing compounds afforded the target conjugate.

Mittausmenetelmien kehittaminen kuplakolonnille

Kuplakolonnireaktoreiden CFD-mallinnus on talla hetkella voimakkaasti kehittyva tutkimusalue. Kaksifaasivirtauksen luotettava simulointi ja mallintaminen on haastavaa kuplakolonnireaktorissa tapahtuvien ilmioiden monimutkaisuuden vuoksi. Reaktorin kayttaytymiseen vaikuttavat tekijat, kuten kolonnin hydrodynamiikka ja aineensiirto, tulee tuntea hyvin ennen mallien tekoa. Tassa tyossa on kokeellisesti tutkittu erilaisten mittausmenetelmien soveltuvuutta kuplakolonnin hydrodynamiikan tutkimiseen. Mittausmenetelmissa on keskitytty erityisesti CFD-mallien vaatimiin paikallisiin mittauksiin. Lisaksi tyossa on arvioitu mittausmenetelmien soveltuvuutta j a luotettavuutta CFD-mallien validointiin. Tyon kirjallisuusosassa on perehdytty kuplakolonnireaktorin hydrodynaamiseen kayttaytymiseen ja siihen vaikuttaviin tekijoihin. Naita ovat mm. reaktorityypit, kaasun dispergointi, virtaustyypit ja -alueet, kaasun tilavuusosuus, kaasukuplan koko ja kuplan nousunopeus. Mittauksia tehtiin kahdessa erikokoisessa kuplakolonnissa, joista pienemman halkaisija oli 0,078 m ja suuremman 0,182 m. Molempien kolonnien nestepinnan korkeus oli 4,62 m. Mittaukset tehtiin vesijohtovedella ja epaorgaanisella prosessiliuoksella. Hydrodynaamisista ominaisuuksista mitattiin kaasun tilavuusosuus, kaasukuplan koko seka kaasukuplan nousunopeus. Kaasun tilavuusosuusmittaukset tehtiin paaasiassa paine-eromittauksella ja joissakin tapauksissa pinnanmittausmenetelmalla. Kuplakoko- ja kuplan nousunopeusmittaukset tehtiin suumopeusvideokameralla ja laser Doppler-anemometrilla. Mittauksissa kaytettiin kahdeksaa erilaista kaasunjakolaitetta, joilla selvitettiin kaasunjakolaitteen ominaisuuksien vaikutusta kolonnin hydrodynamiikkaan. Tuloksista havaittiin, etta nestefaasin ominaisuuksilla oli suuri vaikutus kolonnin hydrodynaamiseen kayttaytymiseen. En kaasunjakolaitteilla vesijohtovedella mitatut hydrodynaamiset ominaisuudet eivat poikenneet paljoa toisistaan, kun taas prosessiliuoksella kaasunjakolaitteiden valille saatiin huomattavat erot. Mittausmenetelmista laser Doppler-anemometri ei kaytettavissa olleella optiikalla soveltunut kaasukuplien mittaamiseen. Kuplat olivat menetelmalle liian suuria. Suumopeusvideokamerallaja paine-eromittauksella paastiin hyviin tuloksiin.

Uusien polyuretaanimateriaalien kehittäminen

Polyuretaanielastomeerit ovat jaksottaisia sekapolymeerejä, jotka muodostuvat vuoroittaisista joustavien ketjujen segmenteistä ja hyvin polaarisista kovista segmenteistä. Kemiallinen rakenne ja ominaisuudet riippuvat käytetyistä reaktiokomponenteista. Pehmeän segmentin muodostaa polyoli ja kovan segmentin muodostaa yleensä di-isosyanaatti ja ketjunjatkaja. Polyuretaanielastomeerien valmistus tapahtuu valamalla, jolloin reaktiokomponentit ovat nestemäisiä. Työssä tutkittiin kahta perusmateriaalia ja yhden lisäaineen vaikutusta niiden ominaisuuksiin. Erityisesti kiinnitettiin huomiota dynaamisiin ja mekaanisiin ominaisuuksiin ja verrattiin aineita keskenään. Käytettyjä karakterisointimenetelmiä olivat kontaktikulmamittaukset, DMTA-mittaukset, dynaaminen rasittaminen pyörityslaitteella, elektronimikroskopia, hydrolyysitesti, vetotesti ja kulutustesti. Tutkittujen materiaalien pääasiallinen käyttökohde on pyörä- tai telapinnoitteena. Työn aikana kehitettiin pyörityslaite, jolla voitiin tutkia pinnoitemateriaalin käyttäytymistä halutuissa rasitusolosuhteissa. Lisäaineen vaikutus dynaamisiin ominaisuuksiin oli negatiivinen tai olematon, sillä DMTA-testien perusteella lisäaine kasvatti materiaalien häviötekijää (tan d). Pyöritystestien perusteella lisäaineella ei ollut vaikutusta hystereesiin eli pinnoitemateriaalin lämpenemiseen testin aikana. Uusi tutkittu materiaali osoittautui dynaamisissa kokeissa paremmaksi kuin vanha tuotantomateriaali. Lisäaine kasvatti molempien tutkittujen aineiden pintaenergiaa kontaktikulmamittausten perusteella. Tuotantoaineen vetomurtolujuus kasvoi lisäaineen vaikutuksesta, mutta uuden aineen vetomurtolujuus pieneni. Lisäaineella oli lievä hydrolyysiltä suojaava vaikutus tutkituilla perusaineilla. Uusi tutkittu perusmateriaali sieti hydrolyysiä paremmin kuin tuotantomateriaali, koska sen valmistuksessa käytettiin polyeetteripolyolia ja tuotantomateriaalissa polyesteripolyolia.

Hydrodynamics and Heat Transfer in an Airlift Reactor

Työn teoriaosassa esitetään kirjallisuudessa esiintyviä teoreettisia ja kokeellisia yhtälöitä nesteen nopeuden, kaasun tilavuusosuuden, painehäviön ja lämmönsiirron laskemiseksi. Lisäksi käsitellään airlift-reaktoreiden toimintaa, rakennetta ja teollisia sovelluksia, sekä sekoitusta ja geometrian vaikutusta airlift-reaktoreiden hydrodynaamisiin ominaisuuksiin. Kokeellisessa osassa kuvataan käytetty koelaitteisto ja mittausmenetelmät sekä esitetään saadut koetulokset. Koelaitteisto on viidellä nousuputkella varustettu ulkoisen kierron airlift-reaktori. Kokeellisessa osassa pyritään ratkaisemaan tällaisessa reaktorissa mahdollisesti esiintyviä ongelmia, kuten "slug flown" muodostuminen nousuputkissa sekä fluidien epätasainen jakautuminen nousuputkiin. Lisäksi tutkitaan erilaisten muuttujien, kuten kaasun tilavuusvirran, nesteen viskositeetin, suutinkoon ja nesteen jakoputken rakenteen, vaikutusta kaasun tilavuusosuuteen ja nesteen nopeuteen nousuputkissa. Nesteen nopeudet mitataan merkkiainemenetelmällä ja kaasun tilavuusosuudet manometrimenetelmällä. Lämmönsiirtoa tutkitaan mittaamalla lämpötilaeroja nousuputkissa NiCr-Ni –termoelementeillä. Mittaustulosten perusteella muokataan korrelaatiot kaasun tilavuusosuudelle ja nesteen tyhjäputkinopeudelle. Korrelaatioista lasketut tulokset sopivat kohtuullisen hyvin yhteen mitattujen tulosten kanssa. "Slug flown" ei todettu muodostuvan ongelmaksi 2.5 mPa s pienemmillä viskositeetin arvoilla 2 metriä pitkissä ja 19 mm halkaisijaltaan olevissa putkissa. Lisäksi todettiin, että kaasu- ja nestefaasien jakautumisongelmat voidaan ratkaista rakenteellisesti.

Fischer-Tropsch Slurry Bubble Column Reactor Modeling

The literature part of the work reviews overall Fischer-Tropsch process, Fischer-Tropsch reactors and catalysts. Fundamentals of Fischer-Tropsch modeling are also presented. The emphasis is on the reactor unit. Comparison of the reactors and the catalysts is carried out to choose the suitable reactor setup for the modeling work. The effects of the operation conditions are also investigated. Slurry bubble column reactor model operating with cobalt catalyst is developed by taking into account the mass transfer of the reacting components (CO and H2) and the consumption of the reactants in the liquid phase. The effect of hydrostatic pressure and the change in total mole flow rate in gas phase are taken into account in calculation of the solubilities. The hydrodynamics, reaction kinetics and product composition are determined according to literature. The cooling system and furthermore the required heat transfer area and number of cooling tubes are also determined. The model is implemented in Matlab software. Commercial scale reactor setup is modeled and the behavior of the model is investigated. The possible inaccuraries are evaluated and the suggestions for the future work are presented. The model is also integrated to Aspen Plus process simulation software, which enables the usage of the model in more extensive Fischer-Tropsch process simulations. Commercial scale reactor of diameter of 7 m and height of 30 m was modeled. The capacity of the reactor was calculated to be about 9 800 barrels/day with CO conversion of 75 %. The behavior of the model was realistic and results were in the right range. The highest uncertainty to model was estimated to be caused by the determination of the kinetic rate.

Estado da arte da cromatografia gasosa de alta resolução e alta temperatura

The developments in stationary phase synthesis and capillary column technology, have opened new perspectives in analysis of high molecular mass compounds (³600 daltons) and thermolabile organic compounds by High Temperature High Resolution Gas Chromatography (HT-HRGC). HT-HRGC is a new analytical borderline and its application to the analysis of high molecular mass compounds is still in its infancy. The apolar and medium polar gum phases can now be operated at temperatures up to 400-480ºC, being used for the analysis of n-alcanes up to C-100, lipids, oligosaccharides, industrial resins, polyglycerols, cyclodextrins, porphyrins, etc. This technique should play a leading role as a powerful tool, for many different analysis types, in multidisciplinary fields of Science.

Use of the Optical Cantilever Microphone in Photoacoustic Spectroscopy

A novel cantilever pressure sensor was developed in the Department of Physics at the University of Turku in order to solve the sensitivity problems which are encountered when condenser microphones are used in photoacoustic spectroscopy. The cantilever pressure sensor, combined with a laser interferometer for the measurement of the cantilever movements, proved to be highly sensitive. The original aim of this work was to integrate the sensor in a photoacoustic gas detector working in a differential measurement scheme. The integration was made successfully into three prototypes. In addition, the cantilever was also integrated in the photoacoustic FTIR measurement schemes of gas-, liquid-, and solid-phase samples. A theoretical model for the signal generation in each measurement scheme was created and the optimal celldesign discussed. The sensitivity and selectivity of the differential method were evaluated when a blackbody radiator and a mechanical chopper were used with CO₂, CH4, CO, and C2H4 gases. The detection limits were in the sub-ppm level for all four gases with only a 1.3 second integration time and the cross interference was well below one percent for all gas combinations other than those between hydrocarbons. Sensitivity with other infrared sources was compared using ethylene as an example gas. In the comparison of sensitivity with different infrared sources the electrically modulated blackbody radiator gave a 35 times higher and the CO2-laser a 100 times lower detection limit than the blackbody radiator with a mechanical chopper. As a conclusion, the differential system is well suited to rapid single gas measurements. Gas-phase photoacoustic FTIR spectroscopy gives the best performance, when several components have to be analyzed simultaneously from multicomponent samples. Multicomponent measurements were demonstrated with a sample that contained different concentrations of CO₂, H₂O, CO, and four different hydrocarbons. It required an approximately 10 times longer measurement time to achieve the same detection limit for a single gas as with the differential system. The properties of the photoacoustic FTIR spectroscopy were also compared to conventional transmission FTIR spectroscopy by simulations. Solid- and liquid-phase photoacoustic FTIR spectroscopy has several advantages compared to other techniques and therefore it also has a great variety of applications. A comparison of the signal-to-noise ratio between photoacoustic cells with a cantilever microphone and a condenser microphone was done with standard carbon black, polyethene, and sunflower oil samples. The cell with the cantilever microphone proved to have a 5-10 times higher signal-to-noise ratio than the reference detector, depending on the sample. Cantilever enhanced photoacoustics will be an effective tool for gas detection and analysis of solid- and liquid-phase samples. The preliminary prototypes gave good results in all three measurement schemes that were studied. According to simulations, there are possibilities for further enhancement of the sensitivity, as well as other properties, of each system.

Reagenssin pinta-aktiivisuuden hyödyntäminen sinkin uutossa

Työssä tutkittiin sinkin uutossa käytettävän di(2-etyyliheksyyli)fosforihappo (D2EHPA) -uuttoreagenssin faasikäyttäytymistä ja miten laimentimen koostumus, lämpötila ja orgaanisen faasin sinkkipitoisuus vaikuttavat faasitasapainoon. Laimentimen vaikutuksen havaittiin olevan pientä, kun taas lämpötilan nostaminen yli huoneenlämpötilan leventää faasidiagrammin yksifaasialuetta. Pienet orgaanisen faasin sinkkipitoisuudet eivät juuri vaikuta faasitasapainoon. Sinkin ja D2EHPA:n moolisuhteen ollessa välillä 0,1–0,2 kompleksin rakenne ilmeisesti muuttuu. Sinkkipitoisuuden kasvaessa yksifaasialue muodostuu pienemmillä ammoniakkimäärillä. Suurilla orgaanisen faasin sinkkipitoisuuksilla ja ammoniakkimäärillä muodostuu orgaanisen faasin ja vesifaasin välille kolmas nestefaasi. D2EHPA:n (40 p %) vesipitoisuuden ja viskositeetin pH riippuvuutta tutkittiin, kun laimentimena oli alifaattinen hiilivetyliuotin. Nostettaessa pH yli 3,5:n uuttoreagenssi alkoi muodostaa käänteismisellejä, jolloin orgaanisen faasin vesipitoisuus ja viskositeetti kasvoivat eksponentiaalisesti. Sinkin mukana uuttautuu epäpuhtauksia kuten Al3+, Co2+, Cu2+, Na+, Ni2+, Cl- ja F-. Takaisinuuton kautta epäpuhtaudet joutuvat talteenottoelektrolyysiin, jossa ne voivat vaikuttaa tuotteen laatuun ja laskea virtahyötysuhdetta. Tarkoituksena oli tutkia väheneekö epäpuhtauksien myötäuuttautuminen jollakin tietyllä sinkin latausasteella. Fluoridin ja kuparin uuttautumisen havaittiin vähenevän vasta, kun sinkin pitoisuus orgaanisessa faasissa oli yli 20 g/L lämpötilasta riippumatta. Fluoridi uuttautuu mahdollisesti alumiinikompleksina ja/tai fluorihappona. Koboltin ja nikkelin myötäuuttautumisen havaittiin vähenevän, kun sinkin latausaste oli yli 10 g/L. Natrium ja kloridi eivät myötäuuttautuneet.

Counter-current Washing of Filter Cakes

The main objective of this thesis was to compare the efficiency of counter-current and co-current filter cake washing techniques. Filter cake washing is a common unit operation which is used in the chemical process industry for improving the recovery of the liquid phase or for purifying the solid phase of the filter cake. Counter-current displacement washing is more difficult to arrange and it requires additional process equipment but the advantage of counter-current method is that the consumption of wash water that is required for achieving certain filter cake purity may be considerably decreased when compared to the co-current washing method. This is true especially for materials that are difficult to wash. The literature part of this thesis consists of a review of filter cake washing in general, including the basic principles of co-current and counter-current techniques, and a description of the structure and operation of a horizontal vacuum belt filter, which is the equipment considered in the experimental part of this thesis. Also the most common cake washing models are introduced. The experiments were performed by washing wheat apatite filter cakes in a laboratory scale vacuum filter by using both co-current and counter-current washing methods. The main results of these tests were the washing curves that relate the purity of the filter cake to the amount of wash liquid used. Comparison between the obtained washing curves showed that both washing methods could be efficiently applied for achieving good washing results. The differences between the wash liquid consumptions in the co-current and counter-current washing methods were found to be surprisingly small but this is most probably explained by the relatively good washing characteristics of the apatite cakes. The washing models introduced in the literature part were compared with the results obtained from the experiments and it was found out that the studied cake washing processes could be described

Critical behavior of a water monolayer under hydrophobic confinement

The properties of water can have a strong dependence on the confinement. Here, we consider a water monolayer nanoconfined between hydrophobic parallel walls under conditions that prevent its crystallization. We investigate, by simulations of a many-body coarse-grained water model, how the properties of the liquid are affected by the confinement. We show, by studying the response functions and the correlation length and by performing finite-size scaling of the appropriate order parameter, that at low temperature the monolayer undergoes a liquid-liquid phase transition ending in a critical point in the universality class of the two-dimensional (2D) Ising model. Surprisingly, by reducing the linear size L of the walls, keeping the walls separation h constant, we find a 2D-3D crossover for the universality class of the liquid-liquid critical point for L/h=~50, i.e. for a monolayer thickness that is small compared to its extension. This result is drastically different from what is reported for simple liquids, where the crossover occurs for , and is consistent with experimental results and atomistic simulations. We shed light on these findings showing that they are a consequence of the strong cooperativity and the low coordination number of the hydrogen bond network that characterizes water.