Development of a Ceramic Membrane Filtration Equipment and Its Applicability for Different Wastewaters

In this thesis the membrane filtration equipment for plate type ceramic membranes was developed based on filtration results achieved with different kinds of wastewaters. The experiments were mainly made with pulp and board mill wastewaters, but some experiments were also made with a bore well water and a stone cutting mine wastewater. The ceramicmembranes used were alpha-alumina membranes with a pore size of 100 nm. Some ofthe membranes were coated with a gamma-alumina layer to reduce the membrane pore size to 10 nm, and some of them were modified with different metal oxides in order to change the surface properties of the membranes. The effects of operationparameters, such as cross-flow velocity, filtration pressure and backflushing on filtration performance were studied. The measured parameters were the permeateflux, the quality of the permeate, as well as the fouling tendency of the membrane. A dynamic membrane or a cake layer forming on top of the membrane was observed to decrease the flux and increase separa-tion of certain substances, especially at low cross-flow velocities. When the cross-flow velocities were increased the membrane properties became more important. Backflushing could also be used to decrease the thickness of the cake layer and thus it improved the permeate flux. However, backflushing can lead to a reduction of retentions in cases where the cake layer is improving them. The wastewater quality was important for the thickness of the dynamic membrane and the membrane pore size influenced the permeate flux. In general, the optimization of operation conditions is very important for the successful operation of a membrane filtration system. The filtration equipment with a reasonable range of operational conditions is necessary, especiallywhen different kinds of wastewaters are treated. This should be taken into account already in the development stage of a filtration equipment.

Aqueous Sol-gel Process for Nanocrystalline Photocatalytic Titania, Transparent Functional Coatings and Ceramic Membrane

The present thesis develops from the point of view of titania sol-gel chemistry and an attempt is made to address the modification of the process for better photoactive titania by selective doping and also demonstration of utilization of the process for the preparation of supported membranes and self cleaning films.A general introduction to nanomaterials, nanocrystalline titania and sol-gel chemistry are presented in the first chapter. A brief and updated literature review on sol-gel titania, with special emphasis on catalytic and photocatalytic properties and anatase to rutile transformation are covered. Based on critical assessment of the reported information the present research problem has been defined.The second chapter describes a new aqueous sol-gel method for the preparation of nanocrystalline titania using titanyl sulphate as precursor. This approach is novel since no earlier work has been reported in the same lines proposed here. The sol-gel process has been followed at each step using particle size, zeta potential measurements on the sol and thermal analysis of the resultant gel. The prepared powders were then characterized using X-ray diffraction, FTIR, BET surface area analysis and transmission electron microscopy.The third chapter presents a detailed discussion on the physico-chemical characterization of the aqueous sol-gel derived doped titania. The effect of dopants such as tantalum, gadolinium and ytterbium on the anatase to rutile phase transformation, surface area as well as their influence on photoactivity is also included. The fourth chapter demonstrates application of the aqueous sol-gel method in developing titania coatings on porous alumina substrates for controlling the poresize for use as membrane elements in ultrafiltration. Thin coatings having ~50 nm thickness and transparency of ~90% developed on glass surface were tested successfully for self cleaning applications.

Study and development of BaCe0.65Zr0.20Y0.1503-Δ (BCZY) – Gd0.2Ce0.8O2-Δ (GDC) dense ceramic membranes sysyem for high temperature H2 purification

The first main conclusion drawn from this dissertation concerns the amount of Pt deposited on the asymmetric layer of membrane produced by tape casting porosity shaping method. Three different amounts were investigated (0.15, 1.5 and 4.5 mg cm-2 ). The most optimal performance, based on H2 permeation performances, was attained when 1.5 mg cm-2 of Pt was deposited on the porous layer, resulting in a 0.642 mL min-1 cm-2 permeated H2 when 80% H2 in He was employed as the feed. Pt deposition method is influenced by the concentration of the Pt precursor, which results in different morphology of the catalyst. The second development focused on further optimization on tape casting membranes concerning the solvent employed for the Pt catalyst deposition. The same concentration of Pt was employed, depositing 1.5 mg cm-2 on the porous side of the membrane, but a mixture of acetone and water was employed as solvent. This mixture allowed the suppression of effects leading to poorly dispersed particles. As a result, it was possible to achieve 0.74 mL min-1 cm-2 at 750°C with 50% H2 in He. Lastly, first-ever permeation performance measurements into an innovative ceramic membrane type for hydrogen separation was investigated. In-depth research was done on a group of hierarchically-structured BaCe0.65Zr0.20Y0.15O3-δ(BCZY) - Gd0.2Ce0.8O2-δ(GDC) membranes produced by freeze casting porosity shaping method. Membranes were investigated observing the effect of deposition solvent and the effect of porous layer thickness. Employing a mixture of Acetone and water resulted in better hydrogen permeation at temperatures (T > 650°C), reaching 0.26 mL min-1 cm-2 at 750°C with 50% H2 in He. The reduction of porous layer thickness led to a hydrogen flow of 0.33 mL min-1 cm-2 , at 750°C with 50% H2 in He.

Combined in-fermenter extraction and cross-flow microfiltration for improved inclusion body processing

In this study we demonstrate a new in-fermenter chemical extraction procedure that degrades the cell wall of Escherichia coli and releases inclusion bodies (IBs) into the fermentation medium. We then prove that cross-flow microfiltration can be used to remove 91% of soluble contaminants from the released IBs. The extraction protocol, based on a combination of Triton X-100, EDTA, and intracellular T7 lysozyme, effectively released most of the intracellular soluble content without solubilising the IBs. Cross-flow microfiltration using a 0.2 mum ceramic membrane successfully recovered the granulocyte macrophagecolony stimulating factor (GM-CSF) IBs with removal of 91% of the soluble contaminants and virtually no loss of IBs to the permeate. The filtration efficiency, in terms of both flux and transmission, was significantly enhanced by infermenter Benzonase(R) digestion of nucleic acids following chemical extraction. Both the extraction and filtration methods exerted their efficacy directly on a crude fermentation broth, eliminating the need for cell recovery and re-suspension in buffer. The processes demonstrated here can all be performed using just a fermenter and a single cross-flow filtration unit, demonstrating a high level of process intensification. Furthermore, there is considerable scope to also use the microfiltration system to subsequently solubilise the IBs, to separate the denatured protein from cell debris, and to refold the protein using diafiltration. In this way refolded protein can potentially be obtained, in a relatively pure state, using only two unit operations. (C) 2004 Wiley Periodicals Inc.

Production of ellagitannins concentrate by UF-NF from tropical highland blackberries

Dissertation presented to Faculdade de Ciências e Tecnologia, Universidade Nova de Lisboa for obtaining the master degree in Membrane Engineering

Betaiinin tuotannon sivujakeiden mikrosuodattaminen teräskeraamisella kalvolla

Betaiini on ammoniumyhdiste, jota käytetään esimerkiksi eläinten rehussa, kosmetiikassa ja lääkkeissä. Danisco Animal Nutrition Finnfeeds Finland Oy:n Naantalin tehdas on maailman johtava betaiinin tuottaja ja raaka-aineena tehtaalla käytetään melassierotuksesta saatavaa betaiinimelassia. Kiteisen betaiinin puhdistusprosessin yhteydessä syntyybetaiinipitoisia sivujakeita, jotka sisältävät huomattavan määrän betaiinia, minkä takia niiden jatkokäsittely on tärkeää. Betaiinin tuotannon sivujakeet ovat erittäin vaikeasti suodattuvia orgaanisia liuoksia, joiden koostumuksia ei täysin tunneta. Tämän työn tarkoituksena oli puhdistaa betaiinin tuotannon sivujakeita mikrosuodattamalla niitä teräskeraamisella kalvolla. Työn kokeellisessa osassa suoritettiin suodatusparametrien eli pH:n, lämpötilan, TMP:n ja betaiiniliuoksen kuiva-ainepitoisuuden optimointi sekä konsentrointikokeita. Mikrosuodatus suoritettiin Graver Technologiesin Scepter-putkimoduulilla, joka toimi ohivirtausperiaatteella ja jonka huokoskoko oli 0,1 ¿m. Scepter-moduuli koostui ruostumattomasta teräksestä sintratuista putkimoduuleista, joissa erottavana kerroksena toimi TiO2. Esikokeiden perusteella todettiin ettei pH:lla ollut suurta vaikutusta suodatukseen. Permeaattivuo kasvoi selvästi lämpötilan ja TMP:nkasvaessa. Vuo taas huononi ja permeaatin sameus lisääntyi selvästi 35 % korkeammissa kuiva-ainepitoisuuksissa. Konsentrointikokeet suoritettiin betaiiniliuoksen refraktrometrisessa kuiva-ainepitoisuudessa, BetRk, 35 %, 80 °C lämpötilassa ja betaiiniliuoksen omassa pH:ssa (pH 8-9,5). Esikokeiden tulosten perusteella konsentrointikokeet suoritettiin TMP:ssa 0,6; 0,8 ja 1,0 bar. Betaiinin tuotannonsivujakeiden konsentrointikokeissa saannoksi saatiin 95 %. Suodatustuloksista havaittiin, että betaiinin tuotannon sivujakeen erä vaikutti voimakkaasti suodatuksen toimivuuteen. Konsentrointikokeissa suodatukset suoritettiin sekäuusilla mikrosuodatusmoduuleilla että vanhalla moduulilla, joka oli jo kulunut.Kulumisen ei kuitenkaan havaittu huonontavan suodatustehokkuutta. Konsentrointikokeiden perusteella voidaan laitteiston pesuväliksi arvioida noin viikko ja pesu tulisi suorittaa sekä emäksisellä että happamalla pesuaineella.

Pigmenttien suodatus

Työn tavoitteena oli tutkia neljän eri koesuotimen soveltuvuutta pigmenttilietteen kiintoainepitoisuuden nostoon. Työssä käytetyt suotimet olivat Larox PF 0,1, Certus-CU-0047, Crossflow-koesuodin ja Steuerung ET06-linko. Suodinväliaineena Larox PF 0,1-suotimessa ja Crossflow-koesuotimessa käytettiin Tamfelt Oyj:n suodinkankaita. Certus-CU-0047-suotimessa suodinväliaineena toimi keraaminen membraani. Työn kirjallisuusosassa tarkasteltiin partikkelien karakterisointia, suodatuksen teoriaa, kakkusuodatusta, suodinväliaineista suodinkankaita ja membraaneja. Lisäksi tarkasteltiin paperin päällystämiseen käytettyjen pigmenttien ominaisuuksia ja niiden suodatusta. Kokeet suoritettiin Larox PF 0,1, Certus-CU-0047 ja Crossflow-koesuotimella vakiopainesuodatuksena yhdellä paineella. Steuerung ET06-lingon kokeet suoritettiin vakiovirtaussuodatuksena käyttäen kolmea eri virtausnopeutta ja kolmea eri lingon ja ruuvin kierrossuhdetta. Työssä suodatettiin neljää erilaista pigmenttilietettä. Suodoksista otettiin näytteitä niiden sameuden määrittämiseksi. Larox Pf 0,1-suotimella ja Steuerung ET06-dekantterilingolla saatiin nostettua pigmenttilietteen kiintoainepitoisuutta erittäin hyvin. Loput kaksi suodinta eivät sovellu tähän tarkoitukseen ollenkaan. Vakiopainesuodatuksissa suodatusajat muodostuivat kuitenkin liian pitkiksi. Suodoksien kiintoainepitoisuudet olivat suurimmaksi osaltaan pieniä lukuun ottamatta tiettyjä suodinkankaita. Lietteen 2 kiintoainepitoisuuden nostaminen oli kaikilla suotimilla erittäin vaikeaa, muut lietteet suodattuivat kohtuullisen hyvin. Näiden kokeiden perusteella voidaan sanoa, että varsinkin vakiovirtaussuodatus soveltuu hyvin ainakin tiettyjen pigmenttilietteiden kiintoainepitoisuuden nostoon.

Maidon ja heran mikrosuodatus

Työssä selvitettiin uudenaikaisten polymeerikalvojen soveltuvuutta maidon sekä heran mikrosuodatukseen. Kirjallisessa osassa perehdyttiin maidon ja heran koostumuksiin, mikrobikantoihin sekä erilaisiin maidon sekä heran rasvanpoisto- ja puhdistusmenetelmiin. Tämän lisäksi käsiteltiin mikrosuodatusmenetelmiä sekä niiden käyttöä heran ja maidon käsittelyssä meijeriteollisuudessa. Kokeellisessa osassa verrattiin kahdella eri suodatuslaitteistolla keraami- ja polymeerikalvojen suodatusominaisuuksia separoidun raakamaidon sekä heran poikkivirtausmikrosuodatuksessa. Tavoitteena oli erottaa suodatettavista liuoksista mikrobit sekä jäännösrasva ja tuottaa puhdasta, proteiinipitoista maitoa / heraa. Koeajoissa otetuista näytteistä analysoitiin ainesosakoostumus sekä mikrobipitoisuudet. Tuloksista määritettiin retentioarvot ja näiden perusteella vertailtiin polymeeri- ja keraamikalvojen erotustehokkuutta. Lisäksi kalvojen toimivuutta arvioitiin vuoarvojen avulla. Raakamaidon suodatuksissa polymeerikalvot pidättivät täydellisesti tai lähes täydellisesti jäännösrasvan ja mikrobit, mutta myös kaseiiniproteiinin. Tästä syystä yksikään polymeerikalvoista ei sovellu puhtaan maidon suodatukseen. Keraamikalvot soveltuvat tähän selkeästi paremmin ja yksikään toinen testatuista kalvoista ei päässyt samalle tasolle meijeriteollisuudessa jo käytössä olevan Membralox 1,4 μm -keraamikalvon kanssa. Heran suodatuksissa polymeerikalvot pidättivät täydellisesti tai lähes täydellisesti rasvan ja mikrobit, mutta keraamikalvo päästi huomattavasti enemmän haluttuja proteiineja permeaattiin. Membralox 0,8 μm -keraamikalvo pidätti täydellisesti mikrobit, mutta päästi jonkin verran jäännösrasvaa permeaattiin. Näin ollen kalvovalinta on kompromissi permeaatin puhtauden ja proteiinin saannon välillä. Keraamikalvojen vuohäviöt olivat merkittävästi pienemmät kuin polymeerikalvoilla molempien syöttöliuosten kanssa. Lisäksi keraamikalvojen puhdistus oli huomattavasti nopeampaa ja helpompaa. Tästä syystä keraamiset kalvot soveltuvat polymeerisiä paremmin maidon ja heran mikrosuodatukseen.

Metalli-ionin ja hapon erotus toisistaan kalvosuodatuksella

Työn tarkoituksena oli kuparin ja hapon erottaminen toisistaan malliaineliuoksesta membraanitekniikalla. Kaivannaisteollisuudessa happoja käytetään metalleiden liuottamiseen. Lisäksi happamia jätevesiä syntyy sulfidikaivoksissa, sadeveden liuottaessa metalleja. Raskasmetallit ovat erittäin myrkyllistä vesieliöille. Työn tavoitteena oli saada happo ja metalli hyödynnettävään muotoon. Työn kokeellisessa osassa vertailtiin kahta polymeeristä ja keraamista membraania hapon ja metallin erotuksessa. Mittauksissa käytetyt membraanit olivat: AMS Technologies A-3012 ja A-3014 sekä Inopor ® Type SKR. Syöttöliuos sisälsi kuparisulfaattia ja rikkihappoa. Suodatukset tehtiin 30 ºC lämpötilassa useissa paineissa ja pH-arvoissa. Polymeeristen membraanien suodatusnäytteistä saadut retentiot kuparille olivat vastaavia aikaisempien tutkimusten tuloksien kanssa. A-3012 kalvon kuparin retentio oli 95 % ja A-3014 kalvolle kuparin retentio oli 90 %. Lisäksi mittausten korkeimmissa pH-arvoissa (2,9-2,3) happo konsentroitui permeaattiin. Polymeerisillä membraaneilla ei ollut merkkejä kalvon likaantumisesta tai hajoamisesta. Keraamisella membraanilla mitatut tulokset eivät olleet vastaavia aikaisempien tutkimusten tuloksien kanssa. Kuparin retentio olivat 2 ja 20 prosentin välillä, eikä liuoksen pH eronnut syötön ja permeaatin välillä. Tulosten perusteella molemmat tutkitut polymeeriset membraanit soveltuvat kuparin erottamiseen happamasta liuoksesta. Mittauksissa käytetty keraaminen membraani ei sovellu tähän tehtävään.

Novel asymmetric geopolymer membranes for oil/water emulsions separation

In this study, it was investigated the possibility of using a geopolymeric membrane as an alternative to the expensive ceramic ones. The goal was to synthesise a low-cost membrane made entirely of geopolymer that can perform equally to commercial membranes. This study initially investigated the feasibility of preparing a microporous support suitable for microfiltration through casting and pressing techniques. Subsequently, a selective geopolymeric layer was developed and deposited on the support, with the capability to operate within the microfiltration range and to effectively separate oil from oil-water emulsions. In order to evaluate the performance, the properties of the geopolymeric supports obtained through pressing were carefully evaluated during the experimentation phase investigating the effect of varying parameters such as sodium silicate content, water content, and applied pressure. The results obtained from these evaluations showed that it is possible to produce supports with excellent porosity and highly controlled narrow pore size distributions. The most promising geopolymeric pressed support was then used for the deposition of a selective layer on its surface. Following physical characterization, it was confirmed that the resulting geopolymer membrane was suitable for use in the microfiltration range. Subsequently, the membrane was tested for its ability to separate oil from water using various emulsions prepared with different surfactants at different concentrations and pH. The results revealed that the fluxes were highly dependent on the electrostatic interaction between the membrane and the emulsion, with best results being obtained with emulsions prepared using anionic surfactants. The rejection rate of the membrane was also found to be extremely high, with values over 95%, comparable to a commercial ceramic membrane. This suggests that geopolymer membranes are suitable alternatives to ceramic membranes, offering the added benefits of lower cost and reduced environmental impact during production.

Building the map of innovation for membrane materials (Ceramic membranes)

This work proposes a method of visualizing the trend of research in the field of ceramic membranes from 1999 to 2006. The presented approach involves identifying problems encountered during research in the field of ceramic membranes. Patents from US patent database and articles from Science Direct(& by ELSEVIER was analyzed for this work. The identification of problems was achieved with software Knowledgist which focuses on the semantic nature of a sentence to generate series of subject action object structures. The identified problems are classified into major research issues. This classification was used for the visualization of the intensity of research. The image produced gives the relation between the number of patents, with time and the major research issues. The identification of the most cited papers which strongly influence the research of the previously identified major issues in the given field was also carried out. The relations between these papers are presented using the metaphor of social network. The final result of this work are two figures, a diagram showing the change in the studied problems a specified period of time and a figure showing the relations between the major papers and groups of the problems

Manufacture of ceramic membranes for application in demulsification process for cross-flow microfiltration

This paper describes the manufacture of tubular ceramic membranes and the study of their performance in the demulsification of soybean oil/water emulsions. The membranes were made by iso-static pressing method and micro and macro structurally characterized by SEM, porosimetry by mercury intrusion and determination of apparent density and porosity. The microfiltration tests were realized on an experimental workbench, and fluid dynamic parameters, such as transmembrane flux and pressure were used to evaluate the process relative to the oil phase concentration (analysed by TOC measurements) in the permeate. The results showed that the membrane with pores` average diameter of 1.36 mu m achieved higher transmembrane flux than the membrane with pores` average diameter of 0.8 mu m. The volume of open pores (responsible for the permeation) was predominant in the total porosity, which was higher than 50% for all tested membranes. Concerning demulsification, the monolayer membranes were efficacious, as the rejection coefficient was higher than 99%.

Nanopore size growth and ultrafiltration performance of SnO2 ceramic membranes prepared by sol-gel route

Supported ceramic membranes have been produced by the sol-casting procedure from aqueous colloidal suspensions prepared by the sol-gel route. Coatings on a tubular alumina support have been successfully performed leading to crack free layers. Samples have been sintered at 400, 500 and 600 degreesC, and the effect of heating treatment on the nanostructure and on the ultrafiltration properties are analyzed. The characterization has been done by high resolution scanning electron microscopy, nitrogen adsorption-desorption isotherms, water permeation and cut-off determination using polyethylene glycol standard solutions. The micrographs have revealed that grains and pore size increase with the temperature, whereas their shape remains invariant. This results is in agreements with N-2 adsorption-desorption analyses, which have revealed that the mean pore size diameter increases from 4 to 10 nm as the sintering temperature increases from 400 to 600 degreesC, while the total porosity remains constant. Furthermore, the tortuosity, calculated from water permeability, is essentially invariant with the sintering temperatures. The membranes cut-off, determined with a retention rate equal to 95%, are 3500, 6500 and 9000 g . mol(-1) for 400, 500 and 600 degreesC, respectively, showing that the permeation properties of SnO2 ultrafiltration membranes can easily be controlled by sintering condition.

Demulsification of water/sunflower oil emulsions by a tangential filtration process using chemically impregnated ceramic tubes

A tangential filtration process was implemented in this study using porous ceramic tubes made of alpha-alumina produced by the slip-casting technique. These tubes were sintered at 1450 degrees C and characterized by mercury intrusion porosimetry, which revealed a mean pore size of 0.5 mu m. The tubes were chemically impregnated with a zirconium citrate solution, after which they were calcined and heat treated at temperatures of up to 600 and 900 degrees C to eliminate volatile organic compounds and transform the zirconium citrate into zirconium oxide impregnated in the alumina in the form of nanoparticle agglomerates. The microporous pipes were tested on a microfiltration hydraulic system to analyze their performance in the demulsification of sunflower oil and water mixtures. The fluid-dynamic parameters of Reynolds number and transmembrane pressure were varied in the process. The volume of permeate was analyzed by measuring the Total Organic Carbon concentration (TOC), which indicated 99% of oil phase retention. The emulsified mixture was characterized by optical microscopy, while the morphology and composition of the impregnated microporous tubes were analyzed by scanning electron microscopy (SEM). Quantification of the TOC values for the tube impregnated once at 600 degrees C showed the best demulsification performance, with the concentration on permeate smaller than 10 mg/L. The impregnated tube sintered once at 900 degrees C presented low carbon concentration (smaller than 20 mg/L), has the advantage of presenting the greatest trans-membrane flux in relation to the other microporous tube. (c) 2006 Elsevier B.V. All rights reserved.

Study of structural surface modified tin oxide membrane prepared by sol-gel route sintered at 400 degrees C

This work describes the chemical modification by Tiron(R) molecules of the surface of SnO2 nanoparticles used to prepare nanoporous membranes. Samples prepared with Tiron(R) content between 1 and 20 wt% and fired at 400 C were characterised by X-Ray Powder Diffraction (XRPD), Extended X-ray Absorption Fine Structure (EXAFS), N-2 adsorption isotherms analysis and permeation experiments. XRPD and EXAFS results show a continuous reduction of crystallite size by increasing the Tiron(R) contents until 7.5 wt%. The control exercised by Tiron(R) modifying agent in crystallite growth allows the fine tuning of the average pore size that can be screened from 0.4 to 4 nm as the amount of grafted molecules decreases from 10 to 0 wt%. In consequence, the membrane cut-off can be screened from 1500 to 3500 g.mol(-1).