Gelatin as an additive in bio-based barrier films

The main objective of the present study was to verify the approach on starch-gelatin blending for the paperboard coating formulations with enhanced barrier and mechanical properties. Based on that, another objective was to find out, how the approach will function with wood-based polysaccharides (CMC, EHEC and HPC) by analyzing their barrier properties and convertibility. The last objective was to find out, if pigments can be used in the composition of polysaccharide-protein blends without causing any negative effect on stated properties. The whole process chain of the barrier coating development was studied in the research. The methodology applied included pilot-scale coating and converting trials for the evaluation of mechanical properties of obtained coatings, namely their exposure to cracking with the loss of barrier properties. The results obtained indicated that the combination of starch with gelatin, in fact, improves the grease barrier properties and flexibility of starch-based coatings, thereby confirming the offered approach. The similar results were obtained for CMC, exhibited elevated barrier properties and surface coverage, proving that the approach also functions with wood-based polysaccharides. The introduction of equal amounts of talc gave various effects at different gelatin dosages on barrier properties of wood-based polysaccharides. Mainly, the elevation of grease barrier properties was observed. The convertibility of talc-filled coatings was not sufficient.

Biodegradable packaging materials in 2013 and their feasibility in chocolate industry

The development of biopolymers has been rapid in recent years and the range of available bioplastics is increasing continuously, driven by a growing demand for sustainable solutions. There are several key drivers behind this growth. The oil reservoirs are decreasing which is causing a price increase for the traditional plastic materials and therefore the gap to bioplastics’ price is getting smaller. In addition, other environmental topics, such as waste disposal and green production, have become more and more important factors for institutes, companies and consumers. Legislation and directives have to be taken into account as well in decision making concerning different packaging materials. The new environmental law with waste disposal responsibility will also have an effect on the packaging business. Therefore a need has risen to study closer the current offering closer of bio-based materials that could be used in chocolate packaging. In this Master’s Thesis the bioplastics’, and especially biodegradable materials’ technical properties and their development, availability, possible existing products in the markets, waste disposal possibilities and consumers attitude towards environmental friendly packaging is studied. This is a case study where the offering of biodegradable materials was investigated during March 2013 for Fazer Confectionary.

Value co-creation in bio-based chemicals value network

The purpose of this Master’s thesis is to study value co-creation in emerging value network. The main objective is to examine how value is co-created in bio-based chemicals value network. The study provides insights to different actors’ perceived value in the value network and enlightens their motivations to commit to the collaborative partnerships with other actors. Empirical study shows that value co-creation is creation of mutual value for both parties of the relationship by combining their non-competing resources to achieve a common goal. Value co-creation happens in interactions, and trust, commitment and information sharing are essential prerequisites for value co-creation. Value co-creation is not only common value creation, but it is also value that emerges for each actor because of the co-operation with the other actor. Even though the case companies define value mainly in economic terms, the other value elements like value of the partnership, knowledge transfer and innovation are more important for value co-creation.

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.

Chemical derivatization of galactoglucomannan for functional materials

In the framework of the biorefinery concept researchers aspire to optimize the utilization of plant materials, such as agricultural wastes and wood. For most of the known processes, the first steps in the valorisation of biomass are the extraction and purification of the individual components. The obtained raw products by means of a controlled separation can consecutively be modified to result in biofuels or biogas for energy production, but also in value-added products such as additives and important building blocks for the chemical and material industries. Considerable efforts are undertaken in order to substitute the use of oil-based starting materials or at least minimize their processing for the production of everyday goods. Wood is one of the raw materials, which have gained large attention in the last decades and its composition has been studied in detail. Nowadays, the extraction of water-soluble hemicelluloses from wood is well known and so for example xylan can be obtained from hardwoods and O-acetyl galactoglucomannans (GGMs) from softwoods. The aim of this work was to develop water-soluble amphiphilic materials of GGM and to assess their potential use as additives. Furthermore, GGM was also applied as a crosslinker in the synthesis of functional hydrogels for the removal of toxic metals and metalloid ions from aqueous solutions. The distinguished products were obtained by several chemical approaches and analysed by nuclear magnetic resonance spectroscopy (NMR), Fourier transform infrared spectroscopy (FTIR), size exclusion chromatography (SEC), thermal gravimetric analysis (TGA), scanning electron microscope SEM, among others. Bio-based surfactants were produced by applying GGM and different fatty acids as starting materials. On one hand, GGM-grafted-fatty acids were prepared by esterification and on the other hand, well-defined GGM-block-fatty acid derivatives were obtained by linking amino-functional fatty acids to the reducing end of GGM. The reaction conditions for the syntheses were optimized and the resultant amphiphilic GGM derivatives were evaluated concerning their ability to reduce the surface tension of water as surfactants. Furthermore, the block-structured derivatives were tested in respect to their applicability as additives for the surface modification of cellulosic materials. Besides the GGM surfactants with a bio-based hydrophilic and a bio-based hydrophobic part, also GGM block-structured derivatives with a synthetic hydrophobic tail, consisting of a polydimethylsiloxane chain, were prepared and assessed for the hydrophobization of surface of nanofibrillated cellulose films. In order to generate GGM block-structured derivatives containing a synthetic tail with distinguished physical and chemical properties, as well as a tailored chain length, a controlled polymerization method was used. Therefore, firstly an initiator group was introduced at the reducing end of the GGM and consecutively single electron transfer-living radical polymerization (SET-LRP) was performed by applying three different monomers in individual reactions. For the accomplishment of the synthesis and the analysis of the products, challenges related to the solubility of the reactants had to be overcome. Overall, a synthesis route for the production of GGM block-copolymers bearing different synthetic polymer chains was developed and several derivatives were obtained. Moreover, GGM with different molar masses were, after modification, used as a crosslinker in the synthesis of functional hydrogels. Hereby, a cationic monomer was used during the free radical polymerization and the resultant hydrogels were successfully tested for the removal of chromium and arsenic ions from aqueous solutions. The hydrogel synthesis was tailored and materials with distinguished physical properties, such as the swelling rate, were obtained after purification. The results generated in this work underline the potential of bio-based products and the urge to continue carrying out research in order to be able to use more green chemicals for the manufacturing of biorenewable and biodegradable daily products.

Biopohjaiset polymeerit dispersiopäällystyksessä

Työn aiheena oli tehdä muotoiltavissa oleva rasvankestävä pakkauskartonki. Polymeeridispersiopäällystettyjä pakkauskartonkeja käytetään kertakäyttöisissä tuotteissa kuten vuoissa, kupeissa ja lautasissa. Tuotteiden on kestettävä rasvaa niiden lopputarkoituksen mukaisesti. Pakkausala jatkaa vuosittaista kasvuaan vauhdilla. Uusia kierrätettäviä biopohjaisia ja luonnolle ystävällisempiä pakkaustuotteita on kehitettävä kasvun tyydyttämiseksi. Biopohjaiset pakkaustuotteet ovat mahdollisia ratkaisuja ympäristöön kohdistuvien ongelmien vähentämiseksi ja öljypohjaisten raaka-aineiden korvaajiksi. Diplomityön teoriaosuudessa keskityttiin dispersiopäällystyksessä käytettyihin biopolymeereihin ja niiden toimivuuteen suojaavina kalvoina. Teoriaosuudessa käsiteltiin myös rasvankestoa ja rasvankestävien tuotteiden materiaaliominaisuuksia. Kirjallisuuden perusteella havaittiin luonnonpolymeerien alhaisen kuiva-ainepitoisuuden ja korkean päällystemäärätarpeen muodostamat haasteet dispersiopäällystyksessä. Pohjakartongin karheudella ja tiiveydellä sekä suojaavan polymeerin kalvon rakenteella huomattiin olevan suuri merkitys rasvankeston saavuttamiseksi. Kokeellinen osa jakautui kolmeen osakokonaisuuteen: laboratoriokokeisiin, esipilotointiin ja varsinaiseen pilot-koeajoon. Esikokeiden perusteella suojaavat kalvot, joiden raaka-aineena käytettiin biopohjaisia dispersiopolymeerejä, antoivat riittäviä rasvankesto-ominaisuuksia, mutta eivät kestäneet konvertointia. Pienellä synteettisten polymeerien lisäyksellä pystyttiin parantamaan päällystettyjen kartonkien rasvankestoa sekä konvertoitavuutta. Pilot-koeajonäytteiden testaustulokset tukivat esikokeissa tehtyjä havaintoja. Tämän työn perusteella kohtuullinen lisäysmäärä synteettistä polymeeriä voi parantaa merkittävästi biopohjaisen suojaavan kalvon antamaa rasvankestoa sekä päällystetyn kartongin konvertoitavuutta.

New biomass derived carbon catalysts for biomass valorization

Due to diminishing petroleum reserves, unsteady market situation and the environmental concerns associated with utilization of fossil resources, the utilization of renewables for production of energy and chemicals (biorefining) has gained considerable attention. Biomass is the only sustainable source of organic compounds that has been proposed as petroleum equivalent for the production of fuels, chemicals and materials. In fact, it would not be wrong to say that the only viable answer to sustainably convene our future energy and material requirements remain with a bio-based economy with biomass based industries and products. This has prompted biomass valorization (biorefining) to become an important area of industrial research. While many disciplines of science are involved in the realization of this effort, catalysis and knowledge of chemical technology are considered to be particularly important to eventually render this dream to come true. Traditionally, the catalyst research for biomass conversion has been focused primarily on commercially available catalysts like zeolites, silica and various metals (Pt, Pd, Au, Ni) supported on zeolites, silica etc. Nevertheless, the main drawbacks of these catalysts are coupled with high material cost, low activity, limited reusability etc. – all facts that render them less attractive in industrial scale applications (poor activity for the price). Thus, there is a particular need to develop active, robust and cost efficient catalytic systems capable of converting complex biomass molecules. Saccharification, esterification, transesterification and acetylation are important chemical processes in the valorization chain of biomasses (and several biomass components) for production of platform chemicals, transportation fuels, food additives and materials. In the current work, various novel acidic carbons were synthesized from wastes generated from biodiesel and allied industries, and employed as catalysts in the aforementioned reactions. The structure and surface properties of the novel materials were investigated by XRD, XPS, elemental analysis, SEM, TEM, TPD and N2-physisorption techniques. The agro-industrial waste derived sulfonic acid functionalized novel carbons exhibit excellent catalytic activity in the aforementioned reactions and easily outperformed liquid H2SO4 and conventional solid acids (zeolites, ion-exchange resins etc). The experimental results indicated strong influence of catalyst pore-structure (pore size, pore-volume), concentration of –SO3H groups and surface properties in terms of the activity and selectivity of these catalysts. Here, a large pore catalyst with high –SO3H density exhibited the highest esterification and transesterification activity, and was successfully employed in biodiesel production from fatty acids and low grade acidic oils. Also, a catalyst decay model was proposed upon biodiesel production and could explain that the catalyst loses its activity mainly due to active site blocking by adsorption of impurities and by-products. The large pore sulfonated catalyst also exhibited good catalytic performance in the selective synthesis of triacetin via acetylation of glycerol with acetic anhydride and out-performed the best zeolite H-Y with respect to reusability. It also demonstrated equally good activity in acetylation of cellulose to soluble cellulose acetates, with the possibility to control cellulose acetate yield and quality (degree of substitution, DS) by a simple adjustment of reaction time and acetic anhydride concentration. In contrast, the small pore and highly functionalized catalysts obtained by hydrothermal method and from protein rich waste (Jatropha de-oiled waste cake, DOWC), were active and selective in the esterification of glycerol with fatty acids to monoglycerides and saccharification of cellulosic materials, respectively. The operational stability and reusability of the catalyst was found to depend on the stability of –SO3H function (leaching) as well as active site blocking due to adsorption of impurities during the reaction. Thus, our results corroborate the potential of DOWC derived sulfated mesoporous active carbons as efficient integrated solid acid catalysts for valorization of biomass to platform chemicals, biofuel, bio-additive, surfactants and celluloseesters.

CO2 Laser Cutting of Particleboard, HDF and MDF

The purpose of this thesis is to reveal how the laser cutting parameters influence lasercutting of particleboard, HDF and MDF. The literature review introduces the basic principle of CO2 laser, CO2 laser equipment and its usage in cutting of wood-based materials. The experimental part focuses on the discussion and analysis ofthe test data and attempts to draw conclusions on the influence of various parameters, including laser power, focal length of the lens and cutting gas, on the cutting speed and kerf quality. The tested materials include various thicknesses of particleboard, HDF and MDF samples. A TRUMPF TLF2700 HQ laser equipment was used for the experiments. To obtain valid data, the test samples must be completely cut through without any bonding of wood fibre. The maximum cutting speed is linear dependent on the laser power in thecondition that the other parameters are constant. For each thickness of a specific material type, there is a minimum laser power for cutting. Normally, the topand bottom kerf widths increase with the enhancement of laser power. There may be a critical laser power which can generate the minimum cross-sectional kerf width. Lens of larger focal length may achieve higher cutting speed. As the focal length becomes larger, the top kerf width tends to increase while the bottom andcross-sectional kerf widths to the opposite. Of all cutting gases, oxygen can help achieve higher cutting speed. The gas pressure of nitrogen does not seem to have strong influence on the cutting result. Generally, 2 bar air is more preferable for higher cutting speed. For particleboard and MDF samples of larger thickness than 12 mm, 2 bar argon can be used to reach remarkably higher cutting speed than the 5 bar. Generally, the 190.5 mm lens can produce smallest total kerf width. The kerf sides of thicker samples are darker than the thinner ones. The sample darkness tends to be lower as laser power increased. 63.5 mm lens seemed tocause more darkness than other lens. 5 bar cutting gases can produce less dark side kerfs than 2 bar ones. Oxygen normally causes darker kerfs than other gases. No distinct differences were found between nitrogen and argon.

Kaasutuskaasun puhdistus

Tässä diplomityössä on selvitetty hiilestä, jätteestä tai biopolttoaineesta kaasutetun kaasun märkä- ja kuivapuhdistusta. Kaasutuskaasun puhdistuksella voidaan likainen ja jopa ongelmallinen aines muuttaa tai puhdistaa sellaiseksi ympäristökelpoiseksi polttoaineeksi, että sitä voidaan käyttää nykyisissä kulutuskohteissa ongelmitta. Lisäkannustusta kaasutuskaasun puhdistus saa uusista EU-direktiiveistä, jotka tulevat rajoittamaan jätteiden läjittämistä kaatopaikoille. Loppusijoitukseen meneviä jätevirtoja voidaan energiakäytöllä pienentää huomattavasti.Työ on tehty PVO-Engineering Oy:n voimalaitostekniikan osastolle kevään 2001 aikana. Työn tavoitteena oli kasvattaa yrityksen tietomäärää kaasutuskaasun puhdistuksen osalta. Lisäksi pyrittiin selvittämään uuden keraamisen pussisuodatinmateriaalin käyttöä kaasutuskaasun kuumakuivasuodatuksessa. Työn ensimmäisessä osassa esitetään kaasutuskaasun koostumuksen ja syntymisen lisäksi tämän työn lähtökohdat ja tavoitteet. Toisessa osassa selvitetään kaasulle asetettavia vaatimuksia eri käyttötapojen mukaan. Kolmannessa ja neljännessä osassa selvitetään puhdistettavien komponenttien käyttäytymistä ja sopivia puhdistusmenetelmiä.Kaasutuskaasun puhdistustekniikka vaihtelee paljonkin riippuen kaasun käyttökohteesta. Eroja syntyy käyttökohteen asetettamista vaatimuksista polttoaineelle, kaasutettavan polttoaineen koostumuksesta ja laadun vaihtelusta. Puhdistuksessa keskitytään kloori -, rikki -, typpi - ja metalliyhdisteiden poistamiseen kaasuvirrasta. Erotuskyvyllä arvioituna eri puhdistusmenetelmistä tehokkaimpia ovat pesurisähkösuodatinyhdistelmät. Niiden suuret jätemäärät ovat kuitenkin iso ongelma. Kuumakuivapuhdistuksessa pyritään kehittämään menetelmä, jossa syntyvät jätemäärät ovat pieniä ja puhdistustulos on riittävä. Puhdistuksen apukeinona käytetään usein erilaisia katalyyttejä. Tunnetuimpia ovat erilaiset kalsiumpohjaiset materiaalit ja mineraalit. Katalyyteillä voidaan tehostaa tarpeellisia kemiallisia reaktioita puhdistusprosessissa. Kaikki puhdistukseen liittyvät ongelmat ovat kooltaan niin suuria, että niiden ratkaisemiseksi on tulevaisuudessa tehtävä lujasti töitä. Markkinanäkymät toimivalle puhdistustekniikalle ovat nykymaailmassa hyvät. Niinpä tuotekehitykseen laitetut panokset voivat tulevaisuudessa olla yritykselle kullan arvoisia.

Pellettien laatu ja ominaisuudet eri raaka-aineilla ja niiden seoksilla

Diplomityö tehtiin osana Vapon toteuttamaa monivuotista pelletin kehitysohjelmaa. Kehitysohjelma koostuu useista pienemmistä osaprojekteista, jotka täydentävät toinen toisiaan. Pellettien raaka-ainepohjan laajentaminen on eräs näistä osaprojekteista. Tutkimustyön tavoitteena oli selvittää erilaisten potentiaalisten bioraaka-aineiden soveltuvuutta pelletointiin joko sellaisenaan tai erilaisina seoksina. Raaka-aineiden pelletoitavuutta tutkittiin kenttäolosuhteissa mobiilipelletointilaitoksella. Laitoksen pääkomponentit muodostivat Kahl C 38–780 tasomatriisipuristin, jäähdytin ja täryseula. Pelletointikokeissa tutkittuja raaka-aineita olivat mäntysahanpuru, männynkuori, harvennusranka, haapa, koivu, jyrsinturve ja ruokohelpi. Raaka-aineiden irtotiheys käyttökosteudessa vaihteli välillä 73–244 kg/m3 ja keskimääräinen kosteuspitoisuus 6,5–15 %. Useissa tapauksissa säkitettyjä raaka-aineita säkkikostutettiin haluttuun kosteuspitoisuuteen ennen pelletointia. Säkkikostutettujen raaka-aineiden kosteuspitoisuudet vaihtelivat tällöin välillä 12–14 m- %. Valtaosa tutkituista raaka-aineista ja niiden seoksista pystyttiin pelletoimaan puristimen matriisilla 8/40 mm, jossa puristuskanavan halkaisija oli 8 mm ja kanavan suoran osan pituus 40 mm. Vaikeuksia tuotti ainoastaan pelkän koivupurun ja ruokohelven pelletointi. Käytetty matriisi oli kanavapituudeltaan liian pitkä koivupurun pelletointiin nostaen puristusvastuksen suureksi. Ruokohelven pelletoinnin vaikeudet johtuivat pääasiassa pelletointiin liian karkeasta raaka-aineesta. Myös matriisia 8/55 mm kokeiltiin, mutta se osoittautui liian ”tiukaksi” valtaosalle puuraaka-aineista. Ainoastaan jyrsinturpeen pelletointi onnistui tällä matriisilla. Männynkuoren pelletointia ei matriisilla 8/55 mm yritetty. Kenttäkokeissa valmistetuista pelleteistä määritettiin erilaisia ominaisuuksia, kuten keskipituus, kosteuspitoisuus, irtotiheys, hienoaineksen määrä ja käsittelykestävyys. Lujuus mitattiin sekä Ligno-testillä että CEN-rummutuslujuuden määrityksellä. Lisäksi pelleteille määritettiin alkuaineanalyysi, tuhkapitoisuus ja lämpöarvo ENAS Oy:n laboratoriossa Jyväskylässä. Ligno-testauksessa parhaimman luokan pelletin tulee yltää arvoon 97,5 %. Pelletoitaessa raaka-aineita ja niiden seoksia tasomatriisikoneella sopivalla matriisilla yllettiin usein näihin tai parempiin tuloksiin. Puumateriaaleilla raaka-aineen optimaalinen lähtökosteus oli välillä 12–14 m- % ja turpeella sekä ruokohelvellä 14–16 m- %. Pelletointi onnistui tällöin vaivattomasti, kunhan sopivat puristimen ajoparametrit oli löydetty. Pellettiä alkoi muodostua matriisin puristuskanavien lämpötilan kohotessa noin 70 ºC. Pellettien lämpötila stabiilitilanteessa heti pelletoinnin jälkeen oli useissa tapauksissa 80–90 ºC. Pelletoinnin aikainen tehontarve vaihteli välillä 90–150 kWh/t, ollen suurimmillaan irtotiheydeltään keveillä materiaaleilla. Raaka-aineen suuri partikkelikoko kasvatti puristimen tehontarvetta. Tämä havaittiin selvästi lisättäessä karkeaa ruokohelpisilppua eri raaka-aineiden joukkoon. Kestävyydeltään erinomaisia pellettejä saatiin, kun raaka-aineena oli jyrsinturve, harvennusranka tai mäntypuru. Varsinkin jyrsinturpeen ja harvennusrangan seoksesta valmistetut pelletit osoittautuivat erittäin kestäviksi. Myös jyrsinturpeen ja ruokohelven sekä mäntypurun ja ruokohelven seoksien pelleteille määritettiin hyviä kestävyysarvoja. Männynkuoresta valmistetut pelletit jäivät Ligno-testauksessa kestävyydeltään alle 97,5 % rajan. Pääsyynä tähän oli kuoren pelletointiin käytetyn matriisin 8/40 mm liian lyhyet puristuskanavat.

Fractionation of Hen Egg and Oat Lipids with supercritical Fluids Chemical and functional Properties of Fractions

Hen eggs and oats (Avena Sativa) are important materials for the food industry. Today, instead of merely satisfying the feeling of hunger, consumers are asking for healthier, biologically active and environmentally friendly products. The growing awareness of consumers’ increasing demands presents a great challenge to the food industry to develop more sustainable products and utilise modern and effective techniques. The modification of yolk fatty acid composition by means of feed supplements is well understood. Egg yolk phospholipids are polar lipids and are used in several applications including food, cosmetics, pharmaceuticals, and special nutrients. Egg yolk phospholipids are excellent emulsifiers, typically sold as mixtures of phospholipids, triacylglycerols, and cholesterol. However, highly purified and characterised phospholipids are needed in several sophisticated applications. Industrial fractionation of phospholipids is usually based on organic solvents. With these fractionation techniques, some harmful residues of organic solvents may cause problems in further processing. The objective of the present study was to investigate the methods to improve the functional properties of eggs, to develop techniques to isolate the fractions responsible for the specific functional properties of egg yolk lipids, and to apply the developed techniques to plant-based materials, too. Fractionation techniques based on supercritical fluids were utilised for the separation of the lipid fractions of eggs and oats. The chemical and functional characterisation of the fractions were performed, and the produced oat polar lipid fractions were tested as protective barrier in encapsulation processes. Modifying the fatty acid compositions of egg yolks with different types of oil supplements in feed had no affect on their functional or sensory properties. Based on the results of functional and sensory analysis, it is evident that eggs with modified fatty acid compositions are usable in several industrial applications. These applications include liquid egg yolk products used in mayonnaise and salad dressings. Egg yolk powders were utilised in different kinds of fractionation processes. The precipitation method developed in this study resembles the supercritical anti-solvent method, which is typically used in the pharmaceutical industry. With pilot scale supercritical fluid processes, non-polar lipids and polar lipids were successfully separated from commercially produced egg yolk powder and oat flakes. The egg and oat-based polar lipid fractions showed high purities, and the corresponding delipidated fractions produced using supercritical techniques offer interesting starting materials for the further production of bioactive compounds. The oat polar lipid fraction contained especially digalactosyadiacylglycerol, which was shown to have valuable functional properties in the encapsulation of probiotics.

Characterisation of Laser Beam and Paper Material Interaction

It is known already from 1970´s that laser beam is suitable for processing paper materials. In this thesis, term paper materials mean all wood-fibre based materials, like dried pulp, copy paper, newspaper, cardboard, corrugated board, tissue paper etc. Accordingly, laser processing in this thesis means all laser treatments resulting material removal, like cutting, partial cutting, marking, creasing, perforation etc. that can be used to process paper materials. Laser technology provides many advantages for processing of paper materials: non-contact method, freedom of processing geometry, reliable technology for non-stop production etc. Especially packaging industry is very promising area for laser processing applications. However, there are only few industrial laser processing applications worldwide even in beginning of 2010´s. One reason for small-scale use of lasers in paper material manufacturing is that there is a shortage of published research and scientific articles. Another problem, restraining the use of laser for processing of paper materials, is colouration of paper material i.e. the yellowish and/or greyish colour of cut edge appearing during cutting or after cutting. These are the main reasons for selecting the topic of this thesis to concern characterization of interaction of laser beam and paper materials. This study was carried out in Laboratory of Laser Processing at Lappeenranta University of Technology (Finland). Laser equipment used in this study was TRUMPF TLF 2700 carbon dioxide laser that produces a beam with wavelength of 10.6 μm with power range of 190-2500 W (laser power on work piece). Study of laser beam and paper material interaction was carried out by treating dried kraft pulp (grammage of 67 g m-2) with different laser power levels, focal plane postion settings and interaction times. Interaction between laser beam and dried kraft pulp was detected with different monitoring devices, i.e. spectrometer, pyrometer and active illumination imaging system. This way it was possible to create an input and output parameter diagram and to study the effects of input and output parameters in this thesis. When interaction phenomena are understood also process development can be carried out and even new innovations developed. Fulfilling the lack of information on interaction phenomena can assist in the way of lasers for wider use of technology in paper making and converting industry. It was concluded in this thesis that interaction of laser beam and paper material has two mechanisms that are dependent on focal plane position range. Assumed interaction mechanism B appears in range of average focal plane position of 3.4 mm and 2.4 mm and assumed interaction mechanism A in range of average focal plane position of 0.4 mm and -0.6 mm both in used experimental set up. Focal plane position 1.4 mm represents midzone of these two mechanisms. Holes during laser beam and paper material interaction are formed gradually: first small hole is formed to interaction area in the centre of laser beam cross-section and after that, as function of interaction time, hole expands, until interaction between laser beam and dried kraft pulp is ended. By the image analysis it can be seen that in beginning of laser beam and dried kraft pulp material interaction small holes off very good quality are formed. It is obvious that black colour and heat affected zone appear as function of interaction time. This reveals that there still are different interaction phases within interaction mechanisms A and B. These interaction phases appear as function of time and also as function of peak intensity of laser beam. Limit peak intensity is the value that divides interaction mechanism A and B from one-phase interaction into dual-phase interaction. So all peak intensity values under limit peak intensity belong to MAOM (interaction mechanism A one-phase mode) or to MBOM (interaction mechanism B onephase mode) and values over that belong to MADM (interaction mechanism A dual-phase mode) or to MBDM (interaction mechanism B dual-phase mode). Decomposition process of cellulose is evolution of hydrocarbons when temperature is between 380- 500°C. This means that long cellulose molecule is split into smaller volatile hydrocarbons in this temperature range. As temperature increases, decomposition process of cellulose molecule changes. In range of 700-900°C, cellulose molecule is mainly decomposed into H2 gas; this is why this range is called evolution of hydrogen. Interaction in this range starts (as in range of MAOM and MBOM), when a small good quality hole is formed. This is due to “direct evaporation” of pulp via decomposition process of evolution of hydrogen. And this can be seen can be seen in spectrometer as high intensity peak of yellow light (in range of 588-589 nm) which refers to temperature of ~1750ºC. Pyrometer does not detect this high intensity peak since it is not able to detect physical phase change from solid kraft pulp to gaseous compounds. As interaction time between laser beam and dried kraft pulp continues, hypothesis is that three auto ignition processes occurs. Auto ignition of substance is the lowest temperature in which it will spontaneously ignite in a normal atmosphere without an external source of ignition, such as a flame or spark. Three auto ignition processes appears in range of MADM and MBDM, namely: 1. temperature of auto ignition of hydrogen atom (H2) is 500ºC, 2. temperature of auto ignition of carbon monoxide molecule (CO) is 609ºC and 3. temperature of auto ignition of carbon atom (C) is 700ºC. These three auto ignition processes leads to formation of plasma plume which has strong emission of radiation in range of visible light. Formation of this plasma plume can be seen as increase of intensity in wavelength range of ~475-652 nm. Pyrometer shows maximum temperature just after this ignition. This plasma plume is assumed to scatter laser beam so that it interacts with larger area of dried kraft pulp than what is actual area of beam cross-section. This assumed scattering reduces also peak intensity. So result shows that assumably scattered light with low peak intensity is interacting with large area of hole edges and due to low peak intensity this interaction happens in low temperature. So interaction between laser beam and dried kraft pulp turns from evolution of hydrogen to evolution of hydrocarbons. This leads to black colour of hole edges.

Surface characterization of chemically modified fiber, wood and paper

Inorganic-organic sol-gel hybrid coatings can be used for improving and modifying properties of wood-based materials. By selecting a proper precursor, wood can be made water repellent, decay-, moisture- or UV-resistant. However, to control the barrier properties of sol-gel coatings on wood substrates against moisture uptake and weathering, an understanding of the surface morphology and chemistry of the deposited sol-gel coatings on wood substrates is needed. Mechanical pulp is used in production of wood-containing printing papers. The physical and chemical fiber surface characteristics, as created in the chosen mechanical pulp manufacturing process, play a key role in controlling the properties of the end-use product. A detailed understanding of how process parameters influence fiber surfaces can help improving cost-effectiveness of pulp and paper production. The current work focuses on physico-chemical characterization of modified wood-based materials with surface sensitive analytical tools. The overall objectives were, through advanced microscopy and chemical analysis techniques, (i) to collect versatile information about the surface structures of Norway spruce thermomechanical pulp fiber walls and understand how they are influenced by the selected chemical treatments, and (ii) to clarify the effect of various sol-gel coatings on surface structural and chemical properties of wood-based substrates. A special emphasis was on understanding the effect of sol-gel coatings on the water repellency of modified wood and paper surfaces. In the first part of the work, effects of chemical treatment on micro- and nano-scale surface structure of 1st stage TMP latewood fibers from Norway spruce were investigated. The chemicals applied were buffered sodium oxalate and hydrochloric acid. The outer and the inner fiber wall layers of the untreated and chemically treated fibers were separately analyzed by light microscopy, atomic force microscopy and field-emission scanning electron microscopy. The selected characterization methods enabled the demonstration of the effect of different treatments on the fiber surface structure, both visually and quantitatively. The outer fiber wall areas appeared as intact bands surrounding the fiber and they were clearly rougher than areas of exposed inner fiber wall. The roughness of the outer fiber wall areas increased most in the sodium oxalate treatment. The results indicated formation of more surface pores on the exposed inner fiber wall areas than on the corresponding outer fiber wall areas as a result of the chemical treatments. The hydrochloric acid treatment seemed to increase the surface porosity of the inner wall areas. In the second part of the work, three silane-based sol-gel hybrid coatings were selected in order to improve moisture resistance of wood and paper substrates. The coatings differed from each other in terms of having different alkyl (CH3–, CH3-(CH2)7–) and fluorocarbon (CF3–) chains attached to the trialkoxysilane sol-gel precursor. The sol-gel coatings were deposited by a wet coating method, i.e. spraying or spreading by brush. The effect of solgel coatings on surface structural and chemical properties of wood-based substrates was studied by using advanced surface analyzing tools: atomic force microscopy, X-ray photoelectron spectroscopy and time-of-flight secondary ion spectroscopy. The results show that the applied sol-gel coatings, deposited as thin films or particulate coatings, have different effects on surface characteristics of wood and wood-based materials. The coating which has a long hydrocarbon chain (CH3-(CH2)7–) attached to the silane backbone (octyltriethoxysilane) produced the highest hydrophobicity for wood and wood-based materials.

Biopolttoaineiden on-line -laadunmittauksen hyödyt energiantuotannossa

Biopolttoaineet ovat tärkeä energianlähde suomalaisessa energiantuotannossa. Biopoltto- aineille on kuitenkin ominaista laadun vaihtelevuus. Yksi tärkeimmistä laatutekijöistä on kosteus, joka vaikuttaa myös polttoaineen energiasisältöön. Laatutekijät puolestaan vai- kuttavat polttoainekäsittelyyn, polttoprosessiin ja koko laitoksen hyötysuhteeseen. Tämän työn tarkoituksena oli tutkia voisiko biopolttoaineiden online-laadunmittaus tuoda lisäarvoa energiantuotantolaitokselle. Esimerkkinä käytettiin yhtä online-laadunmittaus- sovellusta, InrayFuel-röntgenmittausjärjestelmää. Sillä voidaan seurata biopolttoaineiden kosteutta ja polttoaineen sisältämiä vierasaineita. Työssä on laadittu kustannusanalyysi, jolla pyritään selvittämään, onko nykyisen kertaluontoisen mittausmenetelmän korvaami- nen jatkuvatoimisella kannattavaa. Esimerkkilaitoksena on Etelä-Savon Energian Pur- sialan voimalaitos, jossa röntgenmittausjärjestelmään on testattu. Saatujen tulosten mukaan investoiminen esimerkkimittausjärjestelmään maksaisi itsensä takaisin alle vuodessa. Kun laitoksella pystytään seuraamaan polttoaineen laatua jatkuva- toimisesti, laadunhallinta paranee ja sitä kautta voidaan saavuttaa kustannussäästöjä. Polt- toaineesta johtuvat häiriötilanteet vähenevät, polttoaine on mahdollista optimoida edulli- semmaksi polton kannalta ja poltto-olosuhteita voidaan säätää paremmin, jolloin päästöt vähenevät ja hyötysuhde kasvaa. Työssä käytetty laskenta analysoi kuitenkin hyvin ylei- sellä tasolla, sillä käytössä ei ollut laitoksen omaa taselaskentajärjestelmää. Laskenta siis sisältää paljon oletuksia. Tämän ja rohkaisevien tulosten vuoksi tutkimusta jatkuvatoimi- sen laadunmittauksen hyödyistä kannattaa tehdä enemmän.

Graphene from Graphite by Chemical and Physical Techniques.

Graphene is a material with extraordinary properties. Its mechanical and electrical properties are unparalleled but the difficulties in its production are hindering its breakthrough in on applications. Graphene is a two-dimensional material made entirely of carbon atoms and it is only a single atom thick. In this work, properties of graphene and graphene based materials are described, together with their common preparation techniques and related challenges. This Thesis concentrates on the topdown techniques, in which natural graphite is used as a precursor for the graphene production. Graphite consists of graphene sheets, which are stacked together tightly. In the top-down techniques various physical or chemical routes are used to overcome the forces keeping the graphene sheets together, and many of them are described in the Thesis. The most common chemical method is the oxidisation of graphite with strong oxidants, which creates a water-soluble graphene oxide. The properties of graphene oxide differ significantly from pristine graphene and, therefore, graphene oxide is often reduced to form materials collectively known as reduced graphene oxide. In the experimental part, the main focus is on the chemical and electrochemical reduction of graphene oxide. A novel chemical route using vanadium is introduced and compared to other common chemical graphene oxide reduction methods. A strong emphasis is placed on electrochemical reduction of graphene oxide in various solvents. Raman and infrared spectroscopy are both used in in situ spectroelectrochemistry to closely monitor the spectral changes during the reduction process. These in situ techniques allow the precise control over the reduction process and even small changes in the material can be detected. Graphene and few layer graphene were also prepared using a physical force to separate these materials from graphite. Special adsorbate molecules in aqueous solutions, together with sonic treatment, produce stable dispersions of graphene and few layer graphene sheets in water. This mechanical exfoliation method damages the graphene sheets considerable less than the chemical methods, although it suffers from a lower yield.