Painediffusöörin suunnitteluperusteiden kehittäminen

Pesu on tärkeä osa sellun tuotantoprosessia. Eräs tapa toteuttaa sellun pesu on käyttää painediffusööriä. Painediffusööri toimii syrjäytyspesuperiaatteella, eli poistaa sellu-massasta keittolipeää paineistetun pesuveden avulla. Työssä on kehitetty painediffusöörin suunnittelun lähtökohtia keräämällä tietoa laitteen toiminnasta, rakenteesta, valmistuksesta sekä nykyisistä epäkohdista, joihin esitetään parannusmahdollisuuksia. Tärkeimmät kehitysalueet laitteessa ovat valmistus-toleranssien väljentäminen sekä sihdin pystysuuntaisen liikkeen tuottaminen. Laitteen valmistustoleranssit on analysoitu perusteellisesti, ja niiden väljentämis-mahdollisuuksia on tutkittu. Väljentämiseen ehdotetaan erilaisia keinoja. Sihdin liike tuotetaan tällä hetkellä hydrauliikalla. Hydrauliikkakomponenteille on koottu mitoitusohjeita, joiden jälkeen esitellään keinoja hydrauliikkajärjestelmän kehittämiseen. Lopuksi esitellään muita lineaarisen liikkeen tuottamisvaihtoehtoja, joilla hydrauliikan voisi korvata. Rakenteessa käytetyille valmistusmateriaaleille on etsitty olemassa olevat yleisimpien materiaalistandardien mukaiset nimikkeet materiaalinvalinnan helpottamiseksi jatkossa. Pääasiallisten valmistusmateriaalien lisäksi on kerätty tietoa myös vaihtoehtoisista konstruktiomateriaaleista sekä materiaalinvalinnasta ja tuotesuunnittelusta yleensä.

Design and implementation of a multipurpose reactor for scale-up studies

In the theoretical part, the different polymerisation catalysts are introduced and the phenomena related to mixing in the stirred tank reactor are presented. Also the advantages and challenges related to scale-up are discussed. The aim of the applied part was to design and implement an intermediate-sized reactor useful for scale-up studies. The reactor setting was tested making one batch of Ziegler–Natta polypropylene catalyst. The catalyst preparation with a designed equipment setting succeeded and the catalyst was analysed. The analyses of the catalyst were done, because the properties of the catalyst were compared to the normal properties of Ziegler–Natta polypropylene catalyst. The total titanium content of the catalyst was slightly higher than in normal Ziegler–Natta polypropylene catalyst, but the magnesium and aluminium content of the catalyst were in the normal level. By adjusting the siphonation tube and adding one washing step the titanium content of the catalyst could be decreased. The particle size of the catalyst was small, but the activity was in a normal range. The size of the catalyst particles could be increased by decreasing the stirring speed. During the test run, it was noticed that some improvements for the designed equipment setting could be done. For example more valves for the chemical feed line need to be added to ensure inert conditions during the catalyst preparation. Also nitrogen for the reactor needs to separate from other nitrogen line. With this change the pressure in the reactor can be kept as desired during the catalyst preparation. The proposals for improvements are presented in the applied part. After these improvements are done, the equipment setting is ready for start-up. The computational fluid dynamics model for the designed reactor was provided by cooperation with Lappeenranta University of Technology. The experiments showed that for adequate mixing with one impeller, stirring speed of 600 rpm is needed. The computational fluid dynamics model with two impellers showed that there was no difference in the mixing efficiency if the upper impeller were pumping downwards or upwards.

The intrinsic mechanisms of softwood fiber damage in brown stock fiber line unit operations Lappeenranta 2010

The effects of pulp processing on softwood fiber properties strongly influence the properties of wet and dry paper webs. Pulp strength delivery studies have provided observations that much of the strength potential of long fibered pulp is lost during brown stock fiber line operations where the pulp is merely washed and transferred to the subsequent processing stages. The objective of this work was to study the intrinsic mechanisms which maycause fiber damage in the different unit operations of modern softwood brown stock processing. The work was conducted by studying the effects of industrial machinery on pulp properties with some actions of unit operations simulated in laboratory scale devices under controlled conditions. An optical imaging system was created and used to study the orientation of fibers in the internal flows during pulp fluidization in mixers and the passage of fibers through the screen openings during screening. The qualitative changes in fibers were evaluated with existing and standardized techniques. The results showed that each process stage has its characteristic effects on fiber properties: Pulp washing and mat formation in displacement washers introduced fiber deformations especially if the fibers entering the stage were intact, but it did not decrease the pulp strength properties. However, storage chests and pulp transfer after displacement washers contributed to strength deterioration. Pulp screening proved to be quite gentle, having the potential of slightly evening out fiber deformations from very deformed pulps and vice versa inflicting a marginal increase in the deformation indices if the fibers were previously intact. Pulp mixing in fluidizing industrial mixers did not have detrimental effects on pulp strength and had the potential of slightly evening out the deformations, provided that the intensity of fluidization was high enough to allow fiber orientation with the flow and that the time of mixing was short. The chemical and mechanical actions of oxygen delignification had two distinct effects on pulp properties: chemical treatment clearly reduced pulp strength with and without mechanical treatment, and the mechanical actions of process machinery introduced more conformability to pulp fibers, but did not clearly contribute to a further decrease in pulp strength. The chemical composition of fibers entering the oxygen stage was also found to affect the susceptibility of fibers to damage during oxygen delignification. Fibers with the smallest content of xylan were found to be more prone to irreversibledeformations accompanied with a lower tensile strength of the pulp. Fibers poor in glucomannan exhibited a lower fiber strength while wet after oxygen delignification as compared to the reference pulp. Pulps with the smallest lignin content on the other hand exhibited improved strength properties as compared to the references.

Kalvonpesuprosessit paperiteollisuuden sovelluksissa

Tämän työn tarkoituksena oli löytää tehokas ja taloudellinen pesuaine/pesuaineyhdistelmä kahdelle nanosuodatuskalvolle, joiden läpi on suodatettu paperitehtaan kirkassuodosta ja hiomon kiertovettä. Työssä tutkittiin myös sitä, kestävätkö tutkitut kalvot vetyperoksidia. Työssä havaittiin, että tutkituista kalvoista huokoisempi ei puhdistunut millään tutkituista pesuaineista/pesuaineyhdistelmistä. Tiiviimmän kalvon vesivuo palautui hyvin kahdella tutkituista pesuaineista. Palautuminen oli todennäköisesti seurausta siitä, että pesuaine irrotti lian kalvon pinnasta ja modifioi sen jälkeen kalvon pintaa. Työssä havaittiin myös, että huokoisempi kalvo kestää hyvin toistuvaa vetyperoksidikäsittelyä. Tiiviimpi kalvo puolestaan ei kestä toistuvaa käsittelyä vetyperoksidilla. Vetyperoksidia voidaan kuitenkin käyttää satunnaisesti apuna tiiviimpienkin kalvojen pesussa.

Online Ultrasound Measurements of Membrane Compaction

There are several filtration applications in the pulp and paper industry where the capacity and cost-effectiveness of processes are of importance. Ultrafiltration is used to clean process water. Ultrafiltration is a membrane process that separates a certain component or compound from a liquid stream. The pressure difference across the membrane sieves macromolecules smaller than 0.001-0.02 μm through the membrane. When optimizing the filtration process capacity, online information about the conditions of the membrane is needed. Fouling and compaction of the membrane both affect the capacity of the filtration process. In fouling a “cake” layer starts to build on the surface of the membrane. This layer blocks the molecules from sieving through the membrane thereby decreasing the yield of the process. In compaction of the membrane the structure is flattened out because of the high pressure applied. The higher pressure increases the capacity but may damage the structure of the membrane permanently. Information about the compaction is needed to effectively operate the filters. The objective of this study was to develop an accurate system for online monitoring of the condition of the membrane using ultrasound reflectometry. Measurements of ultrafiltration membrane compaction were made successfully utilizing ultrasound. The results were confirmed by permeate flux decline, measurements of compaction with a micrometer, mechanical compaction using a hydraulic piston and a scanning electron microscope (SEM). The scientific contribution of this thesis is to introduce a secondary ultrasound transducer to determine the speed of sound in the fluid used. The speed of sound is highly dependent on the temperature and pressure used in the filters. When the exact speed of sound is obtained by the reference transducer, the effect of temperature and pressure is eliminated. This speed is then used to calculate the distances with a higher accuracy. As the accuracy or the resolution of the ultrasound measurement is increased, the method can be applied to a higher amount of applications especially for processes where fouling layers are thinner because of smaller macromolecules. With the help of the transducer, membrane compaction of 13 μm was measured in the pressure of 5 bars. The results were verified with the permeate flux decline, which indicated that compaction had taken place. The measurements of compaction with a micrometer showed compaction of 23–26 μm. The results are in the same range and confirm the compaction. Mechanical compaction measurements were made using a hydraulic piston, and the result was the same 13 μm as obtained by applying the ultrasound time domain reflectometry (UTDR). A scanning electron microscope (SEM) was used to study the structure of the samples before and after the compaction.

Microscopic simulation of pigment coating consolidation

The control of coating layer properties is becoming increasingly important as a result of an emerging demand for novel coated paper-based products and an increasing popularity of new coating application methods. The governing mechanisms of microstructure formation dynamics during consolidation and drying are nevertheless, still poorly understood. Some of the difficulties encountered by experimental methods can be overcome by the utilisation of numerical modelling and simulation-based studies of the consolidation process. The objective of this study was to improve the fundamental understanding of pigment coating consolidation and structure formation mechanisms taking place on the microscopic level. Furthermore, it is aimed to relate the impact of process and suspension properties to the microstructure of the coating layer. A mathematical model based on a modified Stokesian dynamics particle simulation technique was developed and applied in several studies of consolidation-related phenomena. The model includes particle-particle and particle-boundary hydrodynamics, colloidal interactions, Born repulsion, and a steric repulsion model. The Brownian motion and a free surface model were incorporated to enable the specific investigation of consolidation and drying. Filter cake stability was simulated in various particle systems, and subjected to a range of base substrate absorption rates and system temperatures. The stability of the filter cake was primarily affected by the absorption rate and size of particles. Temperature was also shown to have an influence. The consolidation of polydisperse systems, with varying wet coating thicknesses, was studied using imposed pilot trial and model-based drying conditions. The results show that drying methods have a clear influence on the microstructure development, on small particle distributions in the coating layer and also on the mobility of particles during consolidation. It is concluded that colloidal properties can significantly impact coating layer shrinkage as well as the internal solids concentration profile. Visualisations of particle system development in time and comparison of systems at different conditions are useful in illustrating coating layer structure formation mechanisms. The results aid in understanding the underlying mechanisms of pigment coating layer consolidation. Guidance is given regarding the relationship between coating process conditions and internal coating slurry properties and their effects on the microstructure of the coating.

Uso do leite de vaca in natura no controle de oídio na cultura da gérbera

Gerbera (Gerbera jamesonii) is one of the most popular ornamental plants in the world, used as cut or vase flower. The experiment aimed to evaluate the effect of milk in natura to control powdery mildew (Erysiphe cichoracearum) on gerbera. The treatments tested were: two concentrations of cow's milk in natura (8 and 16%), with and without adjuvant (vegetal oil), three fungicides (fenarimol -6 g a.i.100 L-1 H2O, chlorothalonil -150 g a.i.100 L-1 H2O and azoxystrobin + mineral oil - 10 g a.i.100 L-1 H2O) and control treatment. The area under the disease progress curve (AUDPC) was calculated for each plot based on disease severity. Milk in natura applied with adjuvant controlled the disease and did not allow the infection and development of pathogen. The addition of adjuvant improves the efficiency of milk in natura, but it requires subsequent washing of plants with H2O + detergent. The fungicide fenarimol promoted the best control and also the best gerbera visual aspect. The fungicide azoxystrobin + mineral oil and the chlorothalonil were phytotoxic to gerbera plants, affecting the aspect of leaves and flowers.

Formation of polyelectrolyte multilayers and polyelectrolyte complexes in dual polymer treatment of papermaking pulp

The goal of this study was to find a new approach to modify chemically the properties of paper by improving fiber quality. This Master’s thesis includes the multiple polymer treatment in general and themeasurement methods with which the formation of multilayers and complexes can be noticed. The treatment by an oppositely charged dual polymer system is a good approach to increase paper strength. In this work, starch, a cationic polymer, and carboxymethyl cellulose (CMC), an anionic polymer, were used step-by-step to improve paper strength. The adsorption of cationic starch and CMC on cellulose fibers were analyzed via polyelectrolyte titration. The results showed that paper strength was enhanced slightly with a layer-by-layer assembly of the polymers. However, if the washing stage, which was required for layer-by-layer assembly, was eliminated, the starch/CMC complex was deposited on fibers more efficiently, and the paper strength was improved more significantly.

Lämpötilan vaikutus kalvojen likaantumiseen erityisesti adsorptiolla

Työssä tutkittiin lämpötilan vaikutusta kalvon likaantumiseen mustalipeällä ja puuperäisellä hydrolysaatilla lämpötiloissa 20, 45 ja 70 °C:tta. Työn tavoitteena oli löytää lämpötila, jossa tutkimuksessa käytetyt puuperäiset liuokset likasivat kalvoja mahdollisimman vähän. Tutkimuksessa käytettiin Alfa Lavalin UFX5-ultrasuodatuskalvoa sekä Microdyn-Nadirin ultrasuodatuskalvoa UP010 ja nanosuodatuskalvoa NP010. Ennen puuperäisten liuosten adsorboimista kalvoihin säilöntäaineet poistettiin kalvoista sekä kalvojen toiminta stabiloitiin esikäsittelemällä kalvot. Esikäsittelyssä kalvoja pestiin alkalisella pesuaineella, puristettiin 8 bar:n paineessa sekä huuhdeltiin vedellä ja etikkahapolla. Esikäsitellyt kalvot karakterisoitiin mittaamalla malliaineliuoksen vuo ja malliaineiden retentiot suodattamalla polyetyleeniglykoliliuosta kolmikennosuodattimella paineissa 2, 4 ja 6 bar. Tämän jälkeen kalvot altistettiin lämpötiloissa 20, 45 ja 70 °C:tta mustalipeälle ja hydrolysaatille. Altistuksen jälkeen karakterisointi tehtiin uudelleen, jotta vuoarvoja ja retentioita vertaamalla voitiin arvioida altistuksen aikana tapahtunutta kalvojen likaantumista. Adsorboituneen lian puhdistusta kalvoista tutkittiin pesemällä kalvoja alkalisella pesuliuoksella 20 °C:ssa tehdyn altistuksen jälkeen. Mustalipeälle altistettujen kalvojen likaantuminen oli vähäisintä kokeissa, joissa lämpötila oli 20 °C. Alfa Lavalin UFX5-kalvolla 70 °C:ssa tehdyssä kokeessa kalvon likaantuminen oli myös erittäin vähäistä, sillä permeabiliteetti pieneni mustalipeäaltistuksen seurauksena alle 5 %. Hydrolysaatille altistetut kalvot likaantuivat adsorptiolla vähiten Alfa Laval UFX5-kalvoilla 20 °C:ssa tehdyissä kokeissa ja 45 °C:ssa Microdyn-Nadir NP010-kalvoilla tehdyissä kokeissa. Kokeiden perusteella tutkituista vaihtoehdoista korkein tutkimuksessa käytetty lämpötila 70 °C ja Alfa Lavalin UFX5-kalvo soveltuvatkin parhaiten mustalipeän kalvosuodatukseen adsorptiivisen likaantumisen kannalta.

Uuteaineet BCTMP-prosessissa

Diplomityö tehtiin M-real Joutsenon BCTMP-tehtaalle. Työn aiheena oli tehdä uuteaine- ja metallikartoitus eri prosessivaiheiden massoista ja suodoksista BCTMP-tehtaassa. BCTMPmassaa käytetään muun muassa elintarvikekartongin keskikerroksessa. Pakattaviin kartonkeihin suoraan kosketuksissa olevat elintarvikkeet ovat alttiita haju- ja makuvivahteille. Hajut ja maut voivat saada alkunsa kartongin komponenteista, kuten BCTMP-massasta, kartongin päällystysaineista ja kartongin jatkojalostuksessa käytetyistä painoväreistä. Diplomityön teoriaosuudessa keskityttiin puun lipofiilisiin uuteaineisiin ja erityisesti komponentteihin, jotka aiheuttavat haju- ja makuongelmia. Teoriaosuudessa käsiteltiin myös haju- ja makuominaisuuksien muodostumiseen vaikuttavia tekijöitä sekä kerrottiin mahdollisista uuteaineiden poistomenetelmistä. Teoriaosuudessa esiteltiin analysointimenetelmiä, joita käytettiin kokeellisessa osassa. Kokeellisessa osassa esiteltiin valmistettavan massan laatuspesifikaatiot ja toteutuneet laatutrendit. Samassa tutkittiin massan analysointimenetelmien tuloksien korrelaatioita kokonaisuuteaineiden toteamiseksi. Seuraavaksi käsiteltiin syksyllä 2010 ja talvella 2011 tehtyjä prosessin uuteainekartoituksia, jossa muun muassa tutkittiin eri prosessivaiheiden massojen ja suodoksien uuteainemääriä ja –komponentteja. Kartoituksien yhteydessä laskettiin prosessin uuteainetaseita ja prosessin pesutehokkuuksia. Samalla tutkittiin siirtymämetallimääriä, jotka osaltaan vaikuttavat haju- ja makuominaisuuksiin. Kokeellisen osan korrelaatiovertailuissa huomattiin, että merkittävin korrelaatio kokonaisuuteaineisiin on viimeisen massan pesuvaiheen suodoksen sameudella, liki 80 %. Heksanaalipotentiaalin ja uuteaineen korrelaatio oli myös noin 80 %. Valmiista massasta tehdyn kemiallisen hapen kulutuksen eli COD:n korrelaatio uuteaineisiin oli vain 38 %. Prosessikartoituksen tuloksista laskettujen pesuvaiheiden erotustehokkuudet olivat hyvät.

Pinta-aktiiviaineiden vaikutus kuitulinjan toimintaan

Työssä tutkittiin kahden eri pinta-aktiiviaineen A ja B käytön vaikutusta kahdella eri kuitulinjalla. Molempien pinta-aktiiviaineiden pääfunktiona oli vaikuttaa nes-teen pintajännitykseen, jolloin nesteen tunkeutumisnopeus kuitumatriisiin ja kui-tujen huokosiin paranee. Lisäksi pinta-aktiiviaineilla A ja B oli kyky stabiloida nesteeseen liuenneita uuteainekomponentteja, jolloin uudelleensaostumisen riski pienenee. Koeajoilla pyrittiin vaikuttamaan happidelignifiointivaiheen uuteainetasoihin, alkali- ja happiannoksiin sekä kappareduktioon. Lisäksi tarkasteltiin annostelun vaikutusta kuitulinjan pesurien toimintaan, uuteainetasojen kehittymiseen koko kuitulinjalla sekä valkaisun kemikaalikulutukseen. Työssä kokeiltiin myös pinta-aktiiviaineen B vaikutusta EOP-vaiheen uuteainetasoon. Työn kirjallisuusosassa perehdyttiin puun uuteaineisiin ja niiden käyttäytymiseen kuitulinjalla, pinta-aktiiviaineisiin, pesun teoriaan sekä kuitulinjan kemikaaliannosteluihin vaikuttaviin tekijöihin. Molemmissa koeajoissa pinta-aktiiviaineet A ja B annosteltiin massan joukkoon juuri ennen happivaihetta. EOP-vaiheeseen pinta-aktiiviaine B annostelu tehtiin D0-vaiheen pesurin jälkeiseen massaan. Asetoniuutemääritykset tehtiin massasta ennen happivaihetta, happivaiheen jälkeen ja valkaistulle massalle sekä pinta-aktiiviaine B koeajon yhteydessä EOP-vaiheen jälkeen. Pinta-aktiiviaineiden käytöllä havaittiin olevan positiivinen vaikutus kuitulinjan asetoniuutetasojen kehittymisessä. Verrattuna referenssijaksoon, oli happivaiheen alkali- ja happiannokset pienemmät pinta-aktiiviaineiden käytön aikana ilman, että saavutettu kappareduktio heikkeni. Pesurien toiminnan kannalta pinta-aktiiviaineiden käytöllä oli myönteisiä vaikutuksia pesutehokkuuden ja pesun ta-saisuuden kannalta. Lisäksi havaittiin valkaisussa merkittävä muutos D0- ja D1-vaiheiden klooridioksiveden käytössä ja EOP-vaiheen alkaliannoksessa.

Outplanting performace of eucalyptus clonal cuttings produced in different containers and substrates

The objective of this work was to evaluate the outplanting growth of Eucalyptus grandis e E. saligna clones, produced by cuttings in tubes (50cm³) and in pressed blocks (40x60x07cm) - 175 cm³/ seedlings, with different substrates (BT - sugarcane bagasse+sugarcane filter cake; AR - carbonized rice hull + eucalyptus bark; TF - peat). The experiment was arranged in a randomized block design, in a 2x7 factorial (2 clones and 7 treatments), with four replicates with 25 plants. Survival was evaluated two months later. Plant growth was monitored through height and ground level diameter at 20, 40, 60, 120 and 180 days after outplanting. To evaluate the effect of the containers on stem and root biomass in both clones, 180 days after outplanting, the cuttings grown in BT substrate with fertilizer were selected. One plant per plot of each clone, grown in tubes and in pressed blocks was selected. The E. grandis and E. saligna cuttings grown in pressed blocks with sugarcane bagasse+sugarcane filter cake presented greater height and diameter after out planting. Both clones presented larger root, bark, log and branch biomass production in plants produced in the block system. Cuttings of E. saligna grown in pressed blocks showed 80% most wood biomass 180 days after outplanting, compared to that grown in tubes. In E. grandis, the differences in diameter and height, in function of the cutting production system, decreased along time, while in E. saligna these differences increased along the evaluation period.

Improvement of Surface Strength of Paper

Offset printing is a popular printing method that is especially suitable for large and fast print jobs. Newspapers, magazines and books are typical examples of products printed with offset method. In high volume printing production high efficiency is essential. Offset printing uses tacky inks that cause serious stress to the paper surface. Dusting and linting are terms that describe how loose and weakly bonded particles are removed from the paper surface in the printing process. The removed particles accumulate in the process causing deteriorating print quality. This forces the printing operators to stop production for washing and cleaning. Time and money are lost. Dusting and linting tendency of paper can be decreased by improving the surface strength of paper. In the present work a method to increase the surface strength of paper was studied. In the literature part offset printing method and challenges related to offset printing are presented. A review of new methods for surface sizing of paper is also presented. The experimental part presents trials where an apparatus for improving paper surface strength was tested and developed in mill scale. Laboratory work supporting the actual mill scale operations is also presented. The acquired results provide a solid base of information to make decisions on how to proceed with research in the present field of study.

Sewage Sludge Electro-Dewatering

Original sludge from wastewater treatment plants (WWTPs) usually has a poor dewaterability. Conventionally, mechanical dewatering methods are used to increase the dry solids (DS) content of the sludge. However, sludge dewatering is an important economic factor in the operation of WWTPs, high water content in the final sludge cake is commonly related to an increase in transport and disposal costs. Electro‐dewatering could be a potential technique to reduce the water content of the final sludge cake, but the parameters affecting the performance of electro‐dewatering and the quality of the resulting sludge cake, as well as removed water, are not sufficiently well known. In this research, non‐pressure and pressure‐driven experiments were set up to investigate the effect of various parameters and experimental strategies on electro‐dewatering. Migration behaviour of organic compounds and metals was also studied. Application of electrical field significantly improved the dewatering performance in comparison to experiments without electric field. Electro‐dewatering increased the DS content of the sludge from 15% to 40 % in non‐pressure applications and from 8% to 41% in pressure‐driven applications. DS contents were significantly higher than typically obtained with mechanical dewatering techniques in wastewater treatment plant. The better performance of the pressure‐driven dewatering was associated to a higher current density at the beginning and higher electric field strength later on in the experiments. The applied voltage was one of the major parameters affecting dewatering time, water removal rate and DS content of the sludge cake. By decreasing the sludge loading rate, higher electrical field strength was established between the electrodes, which has a positive effect on an increase in DS content of the final sludge cake. However interrupted voltage application had anegative impact on dewatering in this study, probably because the off‐times were too long. Other factors affecting dewatering performance were associated to the original sludge characteristics and sludge conditioning. Anaerobic digestion of the sludge with high pH buffering capacity, polymer addition and freeze/thaw conditioning had a positive impact on dewatering. The impact of pH on electro‐dewatering was related to the surface charge of the particles measured as zeta‐potential. One of the differences between electro‐dewatering and mechanical dewatering technologies is that electro‐dewatering actively removes ionic compounds from the sludge. In this study, dissolution and migration of organic compounds (such as shortchain fatty acids), macro metals (Na, K, Ca, Mg, Fe) and trace metals (Ni, Mn, Zn, Cr) was investigated. The migration of the metals depended on the fractionation and electrical field strength. These compounds may have both negative and positive impacts on the reuse and recycling of the sludge and removed water. Based on the experimental results of this study, electro‐dewatering process can be optimized in terms of dewatering time, desired DS content, power consumption and chemical usage.

Identification of extractives and polysaccharides as foulants in membrane filtration of pulp and paper mill effluents

The search for new renewable materials has intensified in recent years. Pulp and paper mill process streams contain a number of potential compounds which could be used in biofuel production and as raw materials in the chemical, food and pharmaceutical industries. Prior to utilization, these compounds require separation from other compounds present in the process stream. One feasible separation technique is membrane filtration but to some extent, fouling still limits its implementation in pulp and paper mill applications. To mitigate fouling and its effects, foulants and their fouling mechanisms need to be well understood. This thesis evaluates fouling in filtration of pulp and paper mill process streams by means of polysaccharide model substance filtrations and by development of a procedure to analyze and identify potential foulants, i.e. wood extractives and carbohydrates, from fouled membranes. The model solution filtration results demonstrate that each polysaccharide has its own fouling mechanism, which also depends on the membrane characteristics. Polysaccharides may foul the membranes by adsorption and/or by gel/cake layer formation on the membrane surface. Moreover, the polysaccharides interact, which makes fouling evaluation of certain compound groups very challenging. Novel methods to identify wood extractive and polysaccharide foulants are developed in this thesis. The results show that it is possible to extract and identify wood extractives from membranes fouled in filtration of pulp and paper millstreams. The most effective solvent was found to be acetone:water (9:1 v/v) because it extracted both lipophilic extractives and lignans at high amounts from the fouled membranes and it was also non-destructive for the membrane materials. One hour of extraction was enough to extract wood extractives at high amounts for membrane samples with an area of 0.008 m2. If only qualitative knowledge of wood extractives is needed a simplified extraction procedure can be used. Adsorption was the main fouling mechanism in extractives-induced fouling and dissolved fatty and resin acids were mostly the reason for the fouling; colloidal fouling was negligible. Both process water and membrane characteristics affected extractives-induced fouling. In general, the more hydrophilic regenerated cellulose (RC) membrane fouled less that the more hydrophobic polyethersulfone (PES) and polyamide (PA) membranes independent of the process water used. Monosaccharide and uronic acid units could also be identified from the fouled synthetic polymeric membranes. It was impossible to analyze all monosaccharide units from the RC membrane because the analysis result obtained contained degraded membrane material. One of the fouling mechanisms of carbohydrates was adsorption. Carbohydrates were not potential adsorptive foulants to the sameextent as wood extractives because their amount in the fouled membranes was found to be significantly lower than the amount of wood extractives.