Mixing in rotating drums

Tämän diplomityön tarkoitus on parantaa meesauunin toiminnallista tehokkuutta tehostamalla lämmönsiirtoa. Lämmönsiirron parantamiseksi kehitetään erilaisia nostinratkaisuja. Kokeita suoritetaan käyttäen eri sekoitinratkaisuja ja erilaisia prosessiparametreja. Työn kirjallisuusosassa esitetään meesauuni sekä rumpumaisten uunien toiminta. Työssä selvitetään myös sekoituksen analysointiin käytettäviä tapoja ja laskukaavoja. Kirjallisuusosassa keskitytään myös rummussa tapahtuviin fysikaalisiin ilmiöihin sekä erilaisten fluidien reologiaan. Työn kokeellisessa osassa käytettiin LUT Kemiantekniikalla suunniteltua pilot -kokoluokan rumpu-uunia, jolla kokeitaan suoritettiin, käyttäen erilaisia sekoitinratkaisuja ja sekoitusprosessiparametreja. Kokeissa käytettiin myös eri viskositeetin omaavia materiaaleja. Valitut materiaalit olivat vesi, CMC (karboksimetyyliselluloosa) ja kiinteä meesa. Kokeiden tuloksena löydettiin nostinratkaisuja, joilla sekoittumista ja lämmönsiirtoa pystytään parantamaan sekä pidentämään viipymäaikaa.

Entsyymien talteenotto ja kierrätys selluloosaetanolin valmistuksessa

Bioetanolin valmistus selluloosapitoisista raaka-aineista vaatii selluloosapolymeerien pilkkomisen liukoisiksi sokereiksi. Tämä voidaan toteuttaa entsymaattisella hydrolyysillä. Selluloosan pilkkomiseen tarkoitetut entsyymit, sellulaasit, ovat entsymaattisen hydrolyysin jälkeen sitoutuneet joko kiintoainefaasiin tai ovat nestemäisessä faasissa ns. vapaina entsyymeinä. Prosessin taloudellisuuden kannalta on erityisen tärkeää minimoida siinä käytettävien entsyymien tarve, sillä tehokkaat entsyymivalmisteet ovat suhteellisen kalliita. Yksi varteenotettava vaihtoehto bioetanoliprosessin saamiseksi taloudellisemmaksi on käytettyjen entsyymien talteenotto ja kierrätys. Työn tarkoituksena oli selvittää kirjallisuudesta, millaisia menetelmiä on kehitetty entsyymien talteenottoon ja kierrätykseen lignoselluloosasta valmistettavan bioetanolin valmistuksessa. Työssä on keskitytty tuoreisiin tutkimuksiin ja menetelmien käyttökelpoisuuteen ja taloudellisuuteen. Viime vuosina sellulaasien talteenotto- ja kierrätysmenetelmiä koskevat tutkimukset ovat keskittyneet pääasiassa käsittelemään nanopartikkelien avulla tapahtuvaa entsyymien immobilisointia, ultrasuodatusta, erilaisia desorptiomenetelmiä, kiinteän hydrolyysijäännöksen kierrättämistä, tuoreen substraatin lisäämistä sekä myös tislausvaiheen jälkeistä entsyymien kierrättämistä. Jotta kierrätysmenetelmä olisi tehokas, tulisi sen pyrkiä säilyttämään entsyymien aktiivisuuksia, sokerisaantoa menettämättä ja sisältää sekä neste-, että kiintoainefaasista tapahtuva kierrätys. Jokaisella kierrätysmenetelmällä on hyvät ja huonot puolensa. Entsyymien talteenottoastetta saadaan kuitenkin parannettua yhdistämällä erilaisia menetelmiä. Useista tutkimuksista huolimatta, taloudellisinta ja käyttökelpoisinta entsyymien talteenotto- ja kierrätysmenetelmää ei ole vielä saavutettu.

Superkondensaattoreiden valmistus selluloosageeleistä ja hiilimustasta

Tässä työssä tavoitteena oli selvittää selluloosageelien soveltuvuutta superkondensaattorien elektrodimateriaaliksi. Superkondensaattoreiden elektrodit valmistetaan yleensä hyvin huokoisesta hiilimateriaalista. Näin ollen selluloosageeliin joukkoon sekoitettiin sähkönjohtavuutta parantamaan hiilimustaa. Kirjallisessa osassa keskityttiin superkondensaattorin toimintaperiaatteeseen, rakenteeseen ja yleisimmin käytössä oleviin elektrodimateriaaleihin. Yksityiskohtaisemmin paneuduttiin selluloosan käyttöön superkondensaattorien rakennemateriaalina. Kokeellisessa osassa valmistettiin erilaisia selluloosageelejä ja tämän jälkeen elektrodeja hiilimusta-selluloosageeli-seoksesta. Eri sekoitustapojen vaikutusta elektrodin sähköisiin ominaisuuksiin tarkasteltiin sekoittamalla hiilimustaa selluloosageeliin kahdella eri tavalla; korkeapainehajottajalla ja sekoittimella. Tämän lisäksi selvitettiin myös eri kuivaustapojen ja kuivauslämpötilojen vaikutusta elektrodiarkkien ominaisuuksiin. Arkkien sähköiset ominaisuudet määritettiin syklistä voltammetriaa (SV) käyttäen. Saavutetut tulokset osoittivat, että selluloosageelin valmistus on yksi kriittisimmistä kohdista elektrodimateriaalin valmistuksessa. Riittävä entsyymikäsittely vaaditaan, jotta saadaan muodostettua sopiva geeli, johon hiilimusta-partikkelit saadaan takertumaan. Hiilimustan sekoitustavalla sekä elektrodiarkin kuivauslämpötilalla ja – tavalla on myös suuresti vaikutusta elektrodin sähköisiin ominaisuuksiin.

Intensification of hemicellulose hot-water extraction from spruce wood by parameter tuning

The growing population on earth along with diminishing fossil deposits and the climate change debate calls out for a better utilization of renewable, bio-based materials. In a biorefinery perspective, the renewable biomass is converted into many different products such as fuels, chemicals, and materials, quite similar to the petroleum refinery industry. Since forests cover about one third of the land surface on earth, ligno-cellulosic biomass is the most abundant renewable resource available. The natural first step in a biorefinery is separation and isolation of the different compounds the biomass is comprised of. The major components in wood are cellulose, hemicellulose, and lignin, all of which can be made into various end-products. Today, focus normally lies on utilizing only one component, e.g., the cellulose in the Kraft pulping process. It would be highly desirable to utilize all the different compounds, both from an economical and environmental point of view. The separation process should therefore be optimized. Hemicelluloses can partly be extracted with hot-water prior to pulping. Depending in the severity of the extraction, the hemicelluloses are degraded to various degrees. In order to be able to choose from a variety of different end-products, the hemicelluloses should be as intact as possible after the extraction. The main focus of this work has been on preserving the hemicellulose molar mass throughout the extraction at a high yield by actively controlling the extraction pH at the high temperatures used. Since it has not been possible to measure pH during an extraction due to the high temperatures, the extraction pH has remained a “black box”. Therefore, a high-temperature in-line pH measuring system was developed, validated, and tested for hot-water wood extractions. One crucial step in the measurements is calibration, therefore extensive efforts was put on developing a reliable calibration procedure. Initial extractions with wood showed that the actual extraction pH was ~0.35 pH units higher than previously believed. The measuring system was also equipped with a controller connected to a pump. With this addition it was possible to control the extraction to any desired pH set point. When the pH dropped below the set point, the controller started pumping in alkali and by that the desired set point was maintained very accurately. Analyses of the extracted hemicelluloses showed that less hemicelluloses were extracted at higher pH but with a higher molar-mass. Monomer formation could, at a certain pH level, be completely inhibited. Increasing the temperature, but maintaining a specific pH set point, would speed up the extraction without degrading the molar-mass of the hemicelluloses and thereby intensifying the extraction. The diffusion of the dissolved hemicelluloses from the wood particle is a major part of the extraction process. Therefore, a particle size study ranging from 0.5 mm wood particles to industrial size wood chips was conducted to investigate the internal mass transfer of the hemicelluloses. Unsurprisingly, it showed that hemicelluloses were extracted faster from smaller wood particles than larger although it did not seem to have a substantial effect on the average molar mass of the extracted hemicelluloses. However, smaller particle sizes require more energy to manufacture and thus increases the economic cost. Since bark comprises 10 – 15 % of a tree, it is important to also consider it in a biorefinery concept. Spruce inner and outer bark was hot-water extracted separately to investigate the possibility to isolate the bark hemicelluloses. It was showed that the bark hemicelluloses comprised mostly of pectic material and differed considerably from the wood hemicelluloses. The bark hemicelluloses, or pectins, could be extracted at lower temperatures than the wood hemicelluloses. A chemical characterization, done separately on inner and outer bark, showed that inner bark contained over 10 % stilbene glucosides that could be extracted already at 100 °C with aqueous acetone.

Sellulaasit ja niiden käyttö teollisuudessa

Kandidaatintyön kirjallisuuskatsauksessa esitellään selluloosan entsymaattisen hydrolyysin toimintamekanismi ja kerrotaan sellulaasien käytöstä aiheutuvista eduista ja haitoista eri teollisuussovelluksissa.

Selluloosapohjaisten superkondensaattorien valmistaminen hiilinanoputkista

Tämän työn tarkoitus on seuloa oleelliset prosessiparametrit superkondensaattoreiden elektrodikomposiittien valmistuksessa, jotka vaikuttavat kondensaattorin laatuun. Tarkoitus on tutkia parametreja, joiden avulla prosessia on mahdollista optimoida. Työn tarkoituksena on tutkia myös itse komponenttimateriaalien valmistusvaiheen sekoitusprosessia mitatulla ja laskennallisella seokseen siirtyvällä tehonkulutuksella. Työn kirjallisuusosassa esitetään superkondensaattoreiden rakennetta, toimintamekanismia ja ominaisuuksia sähköenergian varastoijana. Lisäksi tarkastellaan tavallisimpia kondensaattoreihin sisältyviä materiaaleja, erityisesti hiilinanoputkia ja selluloosakuituja. Sekoitusprosesseista tarkastellaan kokeellisessa osassa käytettävien sekoituslaitteita ja niiden toimintamekanismeja komponenttien sekoitusprosesseissa. Kokeellisessa osassa tutkimuskysymyksiksi asetettiin eri sekoitusparametrien (materiaalin määrä ja laatu sekä sekoitusajat) vaikutus superkondensaattorien elektrodiarkkien ominaiskapasitansseihin. Testit suoritettiin LUT Prosessien laboratoriossa, ja testeissä massojen sekoitukseen käytettiin roottoristaattoria ja ultraäänisekoitinta. Lisäksi tutkittiin prosessin skaalausta varten skaalatulla laitteistolla sekoitettuja massanäytteitä. Sekoitusprosessin riittävyyttä varten tutkittiin kokeellisesti käytettyjen sekoituslaitteiden tehonkulutusta. Lisäksi roottoristaattorille tehtiin laskentaohjelmalla virtaussimulaatio paikallisen tehonkulutuksen selvittämiseksi Testeissä todettiin tutkittujen parametrien vaikutus, mutta tulosten perusteella varsinaista optimointia ei kyetty tekemään. Tulokset kuitenkin antavat suunnan, johon prosessia voi optimointia varten kehittää. Myös sekoitukseen todettiin siirtyvän suuri määrä tehoa tutkituilla laitteilla, mitä voidaan pitää mahdollisesti riittävänä käytettyjen komponenttien sekoitukseen.

Feasibility of industrial implementation of laser cutting into paper making machine

Laser cutting implementation possibilities into paper making machine was studied as the main objective of the work. Laser cutting technology application was considered as a replacement tool for conventional cutting methods used in paper making machines for longitudinal cutting such as edge trimming at different paper making process and tambour roll slitting. Laser cutting of paper was tested in 70’s for the first time. Since then, laser cutting and processing has been applied for paper materials with different level of success in industry. Laser cutting can be employed for longitudinal cutting of paper web in machine direction. The most common conventional cutting methods include water jet cutting and rotating slitting blades applied in paper making machines. Cutting with CO2 laser fulfils basic requirements for cutting quality, applicability to material and cutting speeds in all locations where longitudinal cutting is needed. Literature review provided description of advantages, disadvantages and challenges of laser technology when it was applied for cutting of paper material with particular attention to cutting of moving paper web. Based on studied laser cutting capabilities and problem definition of conventional cutting technologies, preliminary selection of the most promising application area was carried out. Laser cutting (trimming) of paper web edges in wet end was estimated to be the most promising area where it can be implemented. This assumption was made on the basis of rate of web breaks occurrence. It was found that up to 64 % of total number of web breaks occurred in wet end, particularly in location of so called open draws where paper web was transferred unsupported by wire or felt. Distribution of web breaks in machine cross direction revealed that defects of paper web edge was the main reason of tearing initiation and consequent web break. The assumption was made that laser cutting was capable of improvement of laser cut edge tensile strength due to high cutting quality and sealing effect of the edge after laser cutting. Studies of laser ablation of cellulose supported this claim. Linear energy needed for cutting was calculated with regard to paper web properties in intended laser cutting location. Calculated linear cutting energy was verified with series of laser cutting. Practically obtained laser energy needed for cutting deviated from calculated values. This could be explained by difference in heat transfer via radiation in laser cutting and different absorption characteristics of dry and moist paper material. Laser cut samples (both dry and moist (dry matter content about 25-40%)) were tested for strength properties. It was shown that tensile strength and strain break of laser cut samples are similar to corresponding values of non-laser cut samples. Chosen method, however, did not address tensile strength of laser cut edge in particular. Thus, the assumption of improving strength properties with laser cutting was not fully proved. Laser cutting effect on possible pollution of mill broke (recycling of trimmed edge) was carried out. Laser cut samples (both dry and moist) were tested on the content of dirt particles. The tests revealed that accumulation of dust particles on the surface of moist samples can take place. This has to be taken into account to prevent contamination of pulp suspension when trim waste is recycled. Material loss due to evaporation during laser cutting and amount of solid residues after cutting were evaluated. Edge trimming with laser would result in 0.25 kg/h of solid residues and 2.5 kg/h of lost material due to evaporation. Schemes of laser cutting implementation and needed laser equipment were discussed. Generally, laser cutting system would require two laser sources (one laser source for each cutting zone), set of beam transfer and focusing optics and cutting heads. In order to increase reliability of system, it was suggested that each laser source would have double capacity. That would allow to perform cutting employing one laser source working at full capacity for both cutting zones. Laser technology is in required level at the moment and do not require additional development. Moreover, capacity of speed increase is high due to availability high power laser sources what can support the tendency of speed increase of paper making machines. Laser cutting system would require special roll to maintain cutting. The scheme of such roll was proposed as well as roll integration into paper making machine. Laser cutting can be done in location of central roll in press section, before so-called open draw where many web breaks occur, where it has potential to improve runability of a paper making machine. Economic performance of laser cutting was done as comparison of laser cutting system and water jet cutting working in the same conditions. It was revealed that laser cutting would still be about two times more expensive compared to water jet cutting. This is mainly due to high investment cost of laser equipment and poor energy efficiency of CO2 lasers. Another factor is that laser cutting causes material loss due to evaporation whereas water jet cutting almost does not cause material loss. Despite difficulties of laser cutting implementation in paper making machine, its implementation can be beneficial. The crucial role in that is possibility to improve cut edge strength properties and consequently reduce number of web breaks. Capacity of laser cutting to maintain cutting speeds which exceed current speeds of paper making machines what is another argument to consider laser cutting technology in design of new high speed paper making machines.

Rheological characterization of polysaccharide gels

In this Master’s Thesis work the rheological properties of different polysaccharide gels have been studied. The results of this study are used as a starting point for further investigations of potential applications. In order to understand rheological behavior of studied materials, the commercial hydrocolloids such as sodium carboxymethyl cellulose, xanthan gum and guar gum were used as reference and comparison material for rheological studies. As a part the rheological research the development and implementation of proper measurement methods for studied materials were carried out. In the literature review, short introductions of studied materials and application areas of rheological modifiers are summarized. In addition, basic rheological concepts and key fundamentals are explained. In the experimental part the focus was on the rheological characterization of aqueous suspensions of studied materials. Especially, gel strength and solution stability were investigated. The rheological measurements included both rotational and oscillatory measurements in different conditions, where several chemical and physical properties were measured with Anton Paar MCR302 dynamic rotational rheometer. Studied polysaccharide gels can be clearly defined to be shear thinning and thixotropic materials. They have strong gel forming properties even at low concentrations, which explains the superior thickening behavior for some of the samples. Along with rheological characterization of selected materials the factors behind different phenomena were investigated. To reveal value and potential use of polysaccharide gels the influence of various factors such as concentration, temperature and ionic strength were determined. The measurements showed a clear difference between studied materials under investigated external parameters.

Functionalisation of spruce O-acetyl-galactoglucomannans for barrier and composite applications

The increasing use of energy, food, and materials by the growing population in the world is leading to the situation where alternative solutions from renewable carbon resources are sought after. The growing use of plastics depends on the raw-oil production while oil refining are politically governed and required for the polymer manufacturing is not sustainable in terms of carbon footprint. The amount of packaging is also increasing. Packaging is not only utilising cardboard and paper, but also plastics. The synthetic petroleum-derived plastics and inner-coatings in food packaging can be substituted with polymeric material from the renewable resources. The trees in Finnish forests constitute a huge resource, which ought to be utilised more effectively than it is today. One underutilised component of the forests is the wood-derived hemicelluloses, although Spruce Oacetyl-galactoglucomannans (GGMs) have previously shown high potential for material applications and can be recovered in large scale. Hemicelluloses are hydrophilic in their native state, which restrains the use of them for food packaging as non-dry item. To cope with this challenge, we intended to make GGMs more hydrophobic or amphiphilic by chemical grafting and consequently with the focus of using them for barrier applications. Methods of esterification with anhydrides and cationic etherification with a trimethyl ammonium moiety were established. A method of controlled synthesis to obtain the desired properties by the means of altering temperature, reaction time, the quantity of the reagent, and even the solvent for purification of the products was developed. Numerous analytical tools, such as NMR, FTIR, SEC-MALLS/RI, MALDI-TOF-MS, RP-HPLC and polyelectrolyte titration were used to evaluate the products from different perspectives and to acquire parallel proofs of their chemical structure. Modified GGMs with different degree of substitution and the correlating level of hydrophobicity was applied as coatings on cartonboard and on nanofibrillated cellulose-GGM films to exhibit barrier functionality. The water dispersibility in processing was maintained with GGM esters with low DS. The use of chemically functionalised GGM was evaluated for the use as barriers against water, oxygen and grease for the food packaging purposes. The results show undoubtedly that GGM derivatives exhibit high potential to function as a barrier material in food packaging.

Analytics for the modified kraft pulps

Tämän diplomityön tavoitteena on kehittää sopiva analyyttinen menetelmä muokatun kraft-sellukuidun substituutioasteen (DS) kvantitatiivista määrittämistä varten. Muokkauksella tarkoitetaan tässä yhteydessä joko kovalenttisesti tai adsorption avulla tapahtuvaa molekyylin kiinnittymistä sellukuidun pinnalle. Työn kirjallisuusosuudessa käsitellään lyhyesti eri muokkaustapoja ja yhdisteitä joiden avulla voidaan saavuttaa haluttuja ominaisuuksia sellusta valmistetuille lopputuotteille. Lisäksi kirjallisuusosuudessa käydään läpi käyttötarkoitukseen soveltuvimpia suoria ja epäsuoria analyysimenetelmiä. Analyysimenetelmistä kaikkein lupaavimpia testattiin työn kokeellisessa osassa. Diplomityön kokeellisessa osassa keskityttiin kehittämään muokatulle sellulle kvantitatiivista menetelmää DS:n määrittämiseksi Fourier-muunnos infrapuna-vaimennettu kokonaisheijastus (FTIR-ATR) spektrometrillä. Kirjallisuuskatsauksessa ei löytynyt yhtään dokumentoitua tutkimusta, jossa FTIR-ATR menetelmää olisi käytetty muokatun sellukuidun kvantitatiiviseen tutkimukseen. Muiden analyysimenetelmien, kuten alkuaineanalyysin, termogravimetrisen analyysin (TGA) ja valomikroskopian avulla pyrittiin tuottamaan lisätietoa muokkauksesta. Kvantitatiivisen FTIR-ATR menetelmän kehitykseen käytetyt muokatut sellukuidut olivat selluloosa-asetaattia ja selluloosa betainaattia. Saatujen tulosten perusteella muokattujen sulfiitti- ja kraft sellukuitujen DS:n kvantitatiivinen määrittäminen on mahdollista FTIR-ATR menetelmällä. Vähäinen kalibrointipisteiden määrä vaikeutti tarkan analyysimenetelmän tekemistä. Kehitetyn menetelmän suurimpina ongelmina olivat kiinteiden näytteiden heterogeenisyys sekä mahdollisten epäpuhtauksien tunnistaminen. Jatkotutkimusten avulla kehitettyä menetelmää on kuitenkin mahdollista käyttää muokattujen sellukuitujen jatkuvaan analysointiin selluteollisuudessa.

The effect of cationic-anionic polyelectrolyte multilayer surface treatment on inkjet ink spreading and print quality

The focus of the work reported in this thesis was to study and to clarify the effect of polyelectrolyte multilayer surface treatment on inkjet ink spreading, absorption and print quality. Surface sizing with a size press, film press with a pilot scale coater, and spray coating, have been used to surface treat uncoated wood-free, experimental wood-free and pigmentcoated substrates. The role of the deposited cationic (polydiallydimethylammonium chloride, PDADMAC) and anionic (sodium carboxymethyl cellulose, NaCMC) polyelectrolyte layers with and without nanosilica, on liquid absorption and spreading was studied in terms of their interaction with water-based pigmented and dye-based inkjet inks. Contact angle measurements were made in attempt to explain the ink spreading and wetting behavior on the substrate. First, it was noticed that multilayer surface treatment decreased the contact angle of water, giving a hydrophilic character to the surface. The results showed that the number of cationic-anionic polyelectrolyte layers or the order of deposition of the polyelectrolytes had a significant effect on the print quality. This was seen for example as a higher print density on layers with a cationic polyelectrolyte in the outermost layer. The number of layers had an influence on the print quality; the print density increased with increasing number of layers, although the increase was strongly dependent on ink formulation and chemistry. The use of nanosilica clearly affected the rate of absorption of polar liquids, which also was seen as a higher density of the black dye-based print. Slightly unexpected, the use of nanosilica increased the tendency for lateral spreading of both the pigmented and dye-based inks. It was shown that the wetting behavior and wicking of the inks on the polyelectrolyte coatings was strongly affected by the hydrophobicity of the substrate, as well as by the composition or structure of the polyelectrolyte layers. Coating only with a cationic polyelectrolyte was not sufficient to improve dye fixation, but it was demonstrated that a cationic-anionic-complex structure led to good water fastness. A threelayered structure gave the same water fastness values as a five-layered structure. Interestingly, the water fastness values were strongly dependent not only on the formed cation-anion polyelectrolyte complexes but also on the tendency of the coating to dissolve during immersion in water. Results showed that by optimizing the chemistry of the layers, the ink-substrate interaction can be optimized.

Chemical changes in biomass during torrefaction

Torrefaction is moderate thermal treatment (~200-300 °C) of biomass in an inert atmosphere. The torrefied fuel offers advantages to traditional biomass, such as higher heating value, reduced hydrophilic nature, increased its resistance to biological decay, and improved grindability. These factors could, for instance, lead to better handling and storage of biomass and increased use of biomass in pulverized combustors. In this work, we look at several aspects of changes in the biomass during torrefaction. We investigate the fate of carboxylic groups during torrefaction and its dependency to equilibrium moisture content. The changes in the wood components including carbohydrates, lignin, extractable materials and ashforming matters are also studied. And at last, the effect of K on torrefaction is investigated and then modeled. In biomass, carboxylic sites are partially responsible for its hydrophilic characteristic. These sites are degraded to varying extents during torrefaction. In this work, methylene blue sorption and potentiometric titration were applied to measure the concentration of carboxylic groups in torrefied spruce wood. The results from both methods were applicable and the values agreed well. A decrease in the equilibrium moisture content at different humidity was also measured for the torrefied wood samples, which is in good agreement with the decrease in carboxylic group contents. Thus, both methods offer a means of directly measuring the decomposition of carboxylic groups in biomass during torrefaction as a valuable parameter in evaluating the extent of torrefaction. This provides new information to the chemical changes occurring during torrefaction. The effect of torrefaction temperature on the chemistry of birch wood was investigated. The samples were from a pilot plant at Energy research Center of the Netherlands (ECN). And in that way they were representative of industrially produced samples. Sugar analysis was applied to analyze the hemicellulose and cellulose content during torrefaction. The results show a significant degradation of hemicellulose already at 240 °C, while cellulose degradation becomes significant above 270 °C torrefaction. Several methods including Klason lignin method, solid state NMR and Py-GC-MS analyses were applied to measure the changes in lignin during torrefaction. The changes in the ratio of phenyl, guaiacyl and syringyl units show that lignin degrades already at 240 °C to a small extent. To investigate the changes in the extractives from acetone extraction during torrefaction, gravimetric method, HP-SEC and GC-FID followed by GC-MS analysis were performed. The content of acetone-extractable material increases already at 240 °C torrefaction through the degradation of carbohydrate and lignin. The molecular weight of the acetone-extractable material decreases with increasing the torrefaction temperature. The formation of some valuable materials like syringaresinol or vanillin is also observed which is important from biorefinery perspective. To investigate the change in the chemical association of ash-forming elements in birch wood during torrefaction, chemical fractionation was performed on the original and torrefied birch samples. These results give a first understanding of the changes in the association of ashforming elements during torrefaction. The most significant changes can be seen in the distribution of calcium, magnesium and manganese, with some change in water solubility seen in potassium. These changes may in part be due to the destruction of carboxylic groups. In addition to some changes in water and acid solubility of phosphorous, a clear decrease in the concentration of both chlorine and sulfur was observed. This would be a significant additional benefit for the combustion of torrefied biomass. Another objective of this work is studying the impact of organically bound K, Na, Ca and Mn on mass loss of biomass during torrefaction. These elements were of interest because they have been shown to be catalytically active in solid fuels during pyrolysis and/or gasification. The biomasses were first acid washed to remove the ash-forming matters and then organic sites were doped with K, Na, Ca or Mn. The results show that K and Na bound to organic sites can significantly increase the mass loss during torrefaction. It is also seen that Mn bound to organic sites increases the mass loss and Ca addition does not influence the mass loss rate on torrefaction. This increase in mass loss during torrefaction with alkali addition is unlike what has been found in the case of pyrolysis where alkali addition resulted in a reduced mass loss. These results are important for the future operation of torrefaction plants, which will likely be designed to handle various biomasses with significantly different contents of K. The results imply that shorter retention times are possible for high K-containing biomasses. The mass loss of spruce wood with different content of K was modeled using a two-step reaction model based on four kinetic rate constants. The results show that it is possible to model the mass loss of spruce wood doped with different levels of K using the same activation energies but different pre-exponential factors for the rate constants. Three of the pre-exponential factors increased linearly with increasing K content, while one of the preexponential factors decreased with increasing K content. Therefore, a new torrefaction model was formulated using the hemicellulose and cellulose content and K content. The new torrefaction model was validated against the mass loss during the torrefaction of aspen, miscanthus, straw and bark. There is good agreement between the model and the experimental data for the other biomasses, except bark. For bark, the mass loss of acetone extractable material is also needed to be taken into account. The new model can describe the kinetics of mass loss during torrefaction of different types of biomass. This is important for considering fuel flexibility in torrefaction plants.

Kartoitus Kaakkois-Suomen jätelietteistä, lietteen tuottajista ja käsittelymenetelmistä

In this thesis the sludge of Southeastern-Finland, the companies which produce sludge and the current methods and those still in development have been surveyed. 85 % of the waste sludge from industry comes from forest industries. The sludge from municipal waste water treatment plants is mostly used as a raw material for bioplants. The sludge from forest industry is mostly incinerated. New circulation methods increase the recycling value of the waste by creating new products but they still lack a full-scale plant. The political pressure from Europe and the politics driven by the government of Finland will drive circular economy forward and thus uplifting the processing options of waste slurries. This work is divided in two parts, first contains the survey and the second contains the experimental part and the operational methods based on the survey. In the experimental part wet hard sheet waste sludge was de-watered with shaking filter and the applications for waste sludge from cellulose factory were considered. The results are, that the wet hard sheet waste sludge can be dewatered to high enough total solids content for the inteded use. Also, the cellulose waste sludge has too high Cd content in almost all of the batches to be used as a land improment.

Antitromboottisten lääkeaineiden enantiomeerien kromatografinen fraktiointi

Suuri osa käytössä olevista lääkeaineista on kiraalisia yhdisteitä. Lääkevalmisteet sisältävät yhdisteen enantiomeerien ominaisuuksista riippuen joko yksittäistä enantiomeeria tai näiden seosta. Antitromboottisiin eli veren hyytymistä estäviin lääkeaineisiin kuuluvat varfariini ja rivaroksabaani ovat kiraalisia yhdisteitä, joiden enantiomeerien ominaisuudet poikkeavat antitromboottisen vaikutuksen voimakkuuden suhteen. Varfariinia käytetään kliinisesti enantiomeeriensa raseemisena seoksena, kun taas rivaroksabaani on käytössä lääkevalmisteena puhtaana S-enantiomeerinaan. Lääkeaineen enantiomeerien erottaminen toisistaan on tärkeää esimerkiksi enantiomeerien puhdistamiseksi, lääkevalmisteen oikean koostumuksen varmistamiseksi tai yksittäisten enantiomeerien käyttäytymisen arvioimiseksi elimistössä. Tässä kirjallisuustyössä käsiteltiin nestekromatografian käyttöä antitromboottisiin lääkeaineisiin kuuluvien antikoagulanttien enantiomeerien fraktioinnissa. Kirjallisuudesta saadun tiedon perusteella arvioitiin, millä erotusmateriaaleilla ja millaisissa koeolosuhteissa varfariinin sekä rivaroksabaanin enantiomeerit tulisi erottaa toisistaan. Varfariinin enantiomeerien erotukseen parhaiten sopivaksi erotusmateriaaliksi todettiin kirjallisuuden perusteella kiraalinen vankomysiinipohjainen stationaarifaasi (Chirobiotic V) metanolin, etikkahapon ja veden seoksen toimiessa eluenttina. Eluentin virtausnopeudella 0,3 mL/min ja pienellä injektiotilavuudella varfariinin enantiomeerit saatiin erottumaan täydellisesti ja nopeasti toisistaan. Kirjallisuuden perusteella rivaroksabaanin enantiomeerien erotuksessa erotusmateriaalina toimii parhaiten kiraalinen selluloosapohjainen stationaarifaasi (Chiralcel OD-RH), kun eluenttina käytetään n-heksaanin ja isopropanolin seosta virtausnopeudella 1 mL/min. Varfariinin ja rivaroksabaanin enantiomeerien fraktiointiin parhaiten sopivia menetelmiä voidaan käyttää eri tilanteissa, kuten lääkevalmisteiden laadunvarmistuksessa tai enantiomeerien erotuksessa niiden synteesin jälkeen.

Hemiselluloosien talteenotto paineistetulla kuumavesiuutolla tuotetuista puu-uutteista

Puunjalostusteollisuus keskittyy tällä hetkellä lähinnä sellun ja paperin tuotantoon. Sellun tuotannossa käytetään puun komponenteista vain selluloosa. Puun muita pääkomponentteja ovat hemiselluloosa ja ligniini. Nämä yhdisteet ovat mahdollisia tulevaisuuden biomateriaalien lähtöaineita, mutta tähän mennessä ne on jätetty käyttämättä hyödyksi. Paineistettu kuumavesiuutto on menetelmä, jolla hemiselluloosat ja ligniinit olisi mahdollista erottaa puumateriaalista ennen sellunkeittoa, ja sen jälkeen fraktioida uutteesta erilleen jatkojalostusta varten. Fraktioinnista on tehty tutkimusta monella erilaisella menetelmällä ja eri menetelmiä yhdistelemällä. Tämä kandidaatin työ on kirjallinen työ, jossa käsitellään paineistettua kuumavesiuuttoa, sekä eri yksikköoperaatioita ja niiden mahdollisuuksia hemiselluloosan erotukseen puu-uutteista. Membraanisuodatus on menetelmä, jolla puu-uutteesta saadaan erotettua konsentroitu hemiselluloosafraktio. Membraanisuodatuksessa on kuitenkin puu-uutteiden tapauksessa havaittu ongelmia muun muassa kalvon likaantumisen kanssa. Yhdistämällä muutamia eri yksikköoperaatioita, saadaan parannettua membraanisuodatuksen tehoa, sekä hemiselluloosan puhtautta ja saantoa. Näitä mahdollisia yksikköoperaatioita ovat adsorptio, hapetus, saostus, kromatografiset menetelmät ja neste-nesteuutto.