Wood pellet markets in Russia

Bioenergy came to Russia through wood pellets. On account of prevalence of oil and gas in the Russian economy «bioenergy» has come with a great delay. Certainly, there were many woodworking enterprises and even municipal boiler-houses using wood waste and fire wood for energy reception, but this activity was not purposeful. More likely it was connected with necessity of waste recycling and with the organization of heat supply in the remote areas of the country. However, in 2001 was founded the first pellet plant in Russia. The purpose of this work was to analyze wood pellets market in Russia, investigate current situation on the home and export market, evaluates supply and demand development, opportunities for wood pellets manufactures in Russia, the main manufactures in Russian market; cost and prices for wood pellets in Russia. Also the work was intended to give better understanding of the main problems of wood pellets industry in Russia. Besides, this work had updated information about Russian customs and logistic systems.

Methods for assessing the sustainability of integrated municipal waste management and

The general striving to bring down the number of municipal landfills and to increase the reuse and recycling of waste-derived materials across the EU supports the debates concerning the feasibility and rationality of waste management systems. Substantial decrease in the volume and mass of landfill-disposed waste flows can be achieved by directing suitable waste fractions to energy recovery. Global fossil energy supplies are becoming more and more valuable and expensive energy sources for the mankind, and efforts to save fossil fuels have been made. Waste-derived fuels offer one potential partial solution to two different problems. First, waste that cannot be feasibly re-used or recycled is utilized in the energy conversion process according to EU’s Waste Hierarchy. Second, fossil fuels can be saved for other purposes than energy, mainly as transport fuels. This thesis presents the principles of assessing the most sustainable system solution for an integrated municipal waste management and energy system. The assessment process includes: · formation of a SISMan (Simple Integrated System Management) model of an integrated system including mass, energy and financial flows, and · formation of a MEFLO (Mass, Energy, Financial, Legislational, Other decisionsupport data) decision matrix according to the selected decision criteria, including essential and optional decision criteria. The methods are described and theoretical examples of the utilization of the methods are presented in the thesis. The assessment process involves the selection of different system alternatives (process alternatives for treatment of different waste fractions) and comparison between the alternatives. The first of the two novelty values of the utilization of the presented methods is the perspective selected for the formation of the SISMan model. Normally waste management and energy systems are operated separately according to the targets and principles set for each system. In the thesis the waste management and energy supply systems are considered as one larger integrated system with one primary target of serving the customers, i.e. citizens, as efficiently as possible in the spirit of sustainable development, including the following requirements: · reasonable overall costs, including waste management costs and energy costs; · minimum environmental burdens caused by the integrated waste management and energy system, taking into account the requirement above; and · social acceptance of the selected waste treatment and energy production methods. The integrated waste management and energy system is described by forming a SISMan model including three different flows of the system: energy, mass and financial flows. By defining the three types of flows for an integrated system, the selected factor results needed in the decision-making process of the selection of waste management treatment processes for different waste fractions can be calculated. The model and its results form a transparent description of the integrated system under discussion. The MEFLO decision matrix has been formed from the results of the SISMan model, combined with additional data, including e.g. environmental restrictions and regional aspects. System alternatives which do not meet the requirements set by legislation can be deleted from the comparisons before any closer numerical considerations. The second novelty value of this thesis is the three-level ranking method for combining the factor results of the MEFLO decision matrix. As a result of the MEFLO decision matrix, a transparent ranking of different system alternatives, including selection of treatment processes for different waste fractions, is achieved. SISMan and MEFLO are methods meant to be utilized in municipal decision-making processes concerning waste management and energy supply as simple, transparent and easyto- understand tools. The methods can be utilized in the assessment of existing systems, and particularly in the planning processes of future regional integrated systems. The principles of SISMan and MEFLO can be utilized also in other environments, where synergies of integrating two (or more) systems can be obtained. The SISMan flow model and the MEFLO decision matrix can be formed with or without any applicable commercial or free-of-charge tool/software. SISMan and MEFLO are not bound to any libraries or data-bases including process information, such as different emission data libraries utilized in life cycle assessments.

Intracellular membrane trafficking in Osteoclasts The role of direct Rab protein – Rac 1 interactions in the targeting of intracellular vesicles

Osteoclasts are cells responsible for bone resorption. These cells undergo extensive membrane re-organization during their polarization for bone resorption and form four distinct membrane domains, namely the ruffled border, the basolateral membrane, the sealing zone and the functional secretory domain. The endocytic/biosynthetic pathway and transcytotic route(s) are important for the resorption process, since the endocytic/biosynthetic pathway brings the specific vesicles to the ruffled border whereas the transcytotic flow is believed to transport the degraded bone matrix away from the resorption lacuna to the functional secretory domain. In the present study, we found a new transcytotic route from the functional secretory domain to the ruffled border, which may compensate membrane loss from the ruffled border during the resorption process. We also found that lipid rafts are essential for the ruffled border-targeted late endosomal pathways. A small GTP-binding protein, Rab7, has earlier been shown to regulate the late steps of the endocytic pathway. In bone-resorbing osteoclasts it is involved in the formation of the ruffled border, which displays several features of late endosomal membranes. Here we discovered a new Rab7-interacting protein, Rac1, which is another small GTP-binding protein and binds to the GTP-form of Rab7 in vitro. We demonstrated further that Rab7 colocalizes with Rac1 at the fusion zone of the ruffled border in bone-resorbing osteoclasts. In other cell types, such as fibroblast-like cells, this colocalization is mainly perinuclear. Because Rac1 is known to control the actin cytoskeleton through its effectors, we suggest that the Rab7-Rac1 interaction may mediate late endosomal transport between microtubules and microfilaments, thus enabling endosomal vesicles to switch tracks from microtubules to microfilaments before their fusion to the ruffled border. We then studied the role of Rab-Rac1 interaction in the slow recycling pathway. We revealed that Rac1 also binds directly to Rab11 and to some other but not all Rab-proteins, suggesting that Rab-Rac1 interaction could be a general regulatory mechanism to direct the intracellular vesicles from microtubule mediated transport to actin filament mediated transport and vice versa. On the basis of our results we thus propose a new hypothesis for these GTPases in the regulation of intracellular membrane flow.

Water circulations for effective bleaching of high-brightness mechanical pulps

The amount of water available is usually restricted, which leads to a situation where a complete understanding of the process, including water circulations and the influence of water components, is essential. The main aim of this thesis was to clarify the possibilities for the efficient use of residual peroxide by means of water circulation rearrangements. Rearranging water circulations and the reduction of water usage may cause new problems, such as metal induced peroxide decomposition that needs to be addressed. This thesis introduces theoretical methods of water circulations to combine two variables; effective utilization of residual peroxide and avoiding manganese in the alkaline peroxide bleaching stage. Results are mainly based on laboratory and mill site experiments concerning the utilization of residual peroxide. A simulation model (BALAS) was used to evaluate the manganese contents and residual peroxide doses. It was shown that with optimum recirculation of residual peroxide the brightness can be improved or chemical costs can be decreased. From the scientific perspective, it was also very important to discover that recycled peroxide was more effective pre-bleaching agent compared to fresh peroxide. This can be due to the organic acids i.e. per acetic acid in wash press filtrate that have been formed in alkaline bleaching stage. Even short retention time was adequate and the activation of residual peroxide using sodium hydroxide was not necessary. There are several possibilities for using residual peroxide in practice regarding bleaching. A typical modern mechanical pulping process line consist of defibering, screening, a disc filter, a bleach press, high consistency (HC) peroxide bleaching and a wash press. Furthermore there usually is not a particular medium consistency (MC) pre-bleaching stage that includes additional thickening equipment. The most advisable way to utilize residual peroxide in this kind of process is to recycle the wash press filtrate to the dilution of disc filter pulp (low MC pre-bleaching stage). An arrangement such as this would be beneficial in terms of the reduced convection of manganese to the alkaline bleaching stage. Manganese originates from wood material and will be removed to the water phase already in the early stages of the process. Recycling residual peroxide prior to the disc filter is not recommended because of low consistencies. Regarding water circulations, the novel point of view is that, it would be beneficial to divide water circulations into two sections and the critical location for the division is the disc filter. Both of these two sections have their own priority. Section one before the disc filter: manganese removal. Section two after the disc filter: brightening of pulp. This division can be carried out if the disc filter pulp is diluted only by wash press filtrate before the MC storage tower. The situation is even better if there is an additional press after the disc filter, which will improve the consistency of the pulp. This has a significant effect on the peroxide concentration in the MC pre-bleaching stage. In terms of manganese content, it is essential to avoid the use of disc filter filtrate in the bleach press and wash press showers. An additional cut-off press would also be beneficial for manganese removal. As a combination of higher initial brightness and lower manganese content, the typical brightness increase varies between approximately 0.5 and 1% ISO units after the alkaline peroxide bleaching stage. This improvement does not seem to be remarkable, but as it is generally known, the final brightness unit is the most expensive and difficult to achieve. The estimation of cost savings is not unambiguous. For example in GW/TMP mill case 0.6% ISO units higher final brightness gave 10% savings in the costs of bleaching chemicals. With an hypothetical 200 000 ton annual production, this means that the mill could save in the costs of bleaching chemicals more than 400 000 euros per year. In general, it can be said that there were no differences between the behavior of different types of processes (GW, PGW, TMP and BCTMP). The enhancement of recycling gave a similar response in all cases. However, we have to remember that the utilization of residual peroxide in older mills depends a great deal on the process equipment, the amount of water available and existing pipeline connections. In summary, it can be said that processes are individual and the same solutions cannot be applied to all cases.

Kuljetusten suunnittelujärjestelmän toteutus

Kuusakoski Oy on maailmanlaajuisesti toimiva kierrätysyritys, jolla on yli 100 toimipistettä 10 eri maassa. Toimipisteistä osa pelkästään vastaanottaa kierrätysmateriaalia, osassa suoritetaan myös kierrätysmateriaalin jatkojalostusta. Lisäksi Kuusakoski Oy tarjoaa kierrätysmateriaalin noutopalvelua asiakkailleen. Edellä mainituista syistä kuljetus ja logistiikka nousevat yrityksen toiminnassa merkittävään rooliin. Tässä diplomityössä tehtiin Kuusakoski Oy:n kuljetusten suunnittelujärjestelmän toteutus. Järjestelmän toteutuksen teknisessä tutkimisessa keskityttiin kolmeen pääaiheeseen: ohjelmistoarkkitehtuuriin, karttapalvelujen sekä ajoneuvopäätteen ja toimistosovellusten väliseen rajapintaan. Diplomityön empiirisessä osuudessa käsitellään järjestelmän toimintaa sekä tietokannan että käyttöliittymän näkökulmasta.

Yhdyskuntalietteiden terminen käsittely ja prosessissa syntyvän tuhkan jalostaminen fosforilannoitteeksi Lappeenrannan alueella

Tässä diplomityössä on selvitetty yhdyskuntalietteiden ominaisuuksia sekä käsittelymenetelmiä keskittyen termiseen käsittelyyn, jolla tässä työssä tarkoitetaan lietteen termistä kuivausta ja polttoa. Työssä on myös selvitetty lietteen poltossa syntyvän tuhkan ominaisuuksia ja niiden sopivuutta lannoitteen raaka-aineena. Fosforimalmin varannot ovat rajalliset ja olettavaa on, että helposti hyödynnettävissä oleva fosforimalmi loppuu noin sadan vuoden kuluessa, mikäli fosforin kulutus pysyy nykyisellä tasolla. Kun lietettä poltetaan, jää lietteessä oleva fosfori tuhkaan. Lietteenpoltossa syntyvät tuhkat sisältävät fosforin lisäksi erilaisia haitta-aineita, joten tuhkan sisältämää fosforia ei kyetä hyödyntämään ilman käsittelyä. Työn case-osassa on selvitetty Lappeenrannan alueella syntyvä yhdyskuntalietemäärä sekä sen hyötykäyttömahdollisuudet alueellisessa lietteen polttolaitoksessa. Lappeenrannan tapauksessa syntyvä lietetuhkan määrä on arvioitu ja määritetty paljonko tuhkasta olisi tulevaisuudessa mahdollisuus jalostaa fosforilannoitetta. Tutkimuksen lopputuloksena voidaan todeta, että lietteen poltto ja polton tuhkan käyttö lannoitteena ei vielä kokonaisprosessina ole toteutettavissa oleva vaihtoehto, mutta teknologisen kehityksen jatkuessa se voisi olla potentiaalinen vaihtoehto yhdyskuntalietteen ja lietetuhkan käsittelyn kokonaisratkaisuksi.

Jätehuoltosuunnitelman laatiminen elektroniikka-alan yritykselle

Sähkö- ja elektroniikka-alan yritykset eivät yleensä kuormita merkittävästi ympäristöä, sillä teollisuudenalan suurimmat ympäristövaikutukset aiheutuvat alihankkijoiden ja komponenttivalmistajien toiminnasta. Yritysten oma toiminta perustuu pitkälti tuotekehitykseen ja tuotteiden loppukokoonpanoon valmiista komponenteista. Syntynyt jäte on tyypillisesti pääosin pakkausjätettä, metalleja, kaatopaikkajätettä ja vähäisessä määrin myös ongelmajätettä. Vähäisen ympäristökuormituksen johdosta yrityksiltä ei yleensä vaadita ympäristölupaa. Diplomityössä laadittiin jätehuoltosuunnitelma elektroniikka-alan yritykselle. Työ suoritettiin Kemppi Oy:n toimeksiannosta Lahdessa. Jätehuoltosuunnitelman noudattaminen parantaa yrityksen julkisuuskuvaa ja tuo kustannussäästöjä. Toimivan suunnitelman laatiminen vaatii kuitenkin aikaa ja muita resursseja. Jätehuollon toimivuus on tarkistettava säännöllisesti, etenkin silloin kun yrityksen toiminnan painopiste muuttuu. Käytännön osuudessa kartoitettiin edellisvuosien jätemäärät ja yrityksen jätehuollon tila. Jätehuoltosuunnitelman laatimiselle oli selkeä tarve, koska jätehuolto perustui osin kirjoittamattomiin sääntöihin ja vanhoihin tottumuksiin. Syntypaikkalajittelua tehostettiin lisäämällä jäteastioita ja -pisteitä jätteiden syntypaikoille. Lajittelua parannettiin myös laatimalla selkeät ohjeet ja kouluttamalla työntekijöitä.

Teollisuuden sivutuotteiden hyödyntäminen ekstruusion raaka-aineena

Ilmaston lämpeneminen ja luonnonvarojen ehtyminen ovat nostaneet ympäristöasiat erittäin ajankohtaisiksi ja kierrättämisen merkitys korostuu entisestään. Tässä diplomityössä on käsitelty teollisuuden jätteiden ja sivutuotteiden kierrättämistä puumuovikomposiitin raaka-aineeksi. Työssä on tutkittu Kaakkois-Suomessa olevia tärkeimpiä teollisuuden sivuainevirtoja puumuovikomposiitin kannalta sekä valmistettu puumuovikomposiittia hyödyntämällä kahta kaatopaikalle päätyvää jätettä. Kaakkois-Suomen teollisuuden jätteitä selvitettäessä löytyi paljon puumuovikomposiitin valmistamiseen soveltuvia jätteitä. Mekaanisen metsäteollisuuden sivutuotteita käytetään yleisesti puumuovikomposiitin valmistamiseen. Muita potentiaaliseksi havaittuja raakaaineita ovat mm. lentotuhka, lasikuitujäte, pakkauskartonki, muovijätteet ja vuorivillan valmistuksessa syntyvät jätteet. Koemateriaaleiksi valittiin puunpoltosta peräisin oleva lentotuhka ja vuorivillan valmistamisessa syntyvä vuorivillapöly. Materiaaleilla korvattiin puuta puumuovikomposiitissa ja valmistetulle komposiitille suoritettiin kokeita mekaanisten ominaisuuksien selvittämiseksi. Molempien materiaalien kohdalla ominaisuuksien havaittiin parantuneen ilman täyteainetta valmistettuun komposiittiin verrattuna.

Anchor or Accelerate – A Study on Cancer Cell Adhesion and Motility

Cell migration and adhesion to the extracellular matrix (ECM) are crucial in many biological and pathological processes such as morphogenesis, tissue repair, inflammatory responses, survival, and cancer. Cell-matrix adhesion is mediated by the integrin family of transmembrane receptors, which not only anchor cells to their surroundings, but also transmit bidirectional signalling at the cell surface and couple the ECM to the cytoskeleton. Another group of adhesion receptors are the syndecan proteoglycans, which engage the ECM and possess signalling activity in response to a variety of ligands. Cell migration is a complex process that requires spatial and temporal coordination of adhesion, cell contractility, intracellular traffic of integrins, and matrix turnover by matrix metalloproteinases (MMPs). Thus, integrins and syndecans, as well as MMPs, play essential roles in cancer cell migration and invasion. The understanding of the cooperation of syndecans and integrins was broadened in this thesis study. The results reveal that syndecan-1 functions in concert with 21 integrin in cell adhesion to collagen, whereas syndecan-4 is essential in 21 integrin-mediated matrix contraction. Finally, oncogenic K-Ras was shown to regulate 21 integrin, membrane-type 1 MMP, and syndecan-1 and -4 expression and their cooperation in cell invasion. Epithelial-mesenchymal transition (EMT) is fundamental during embryogenesis and organ development. Activation of EMT processes, including the upregulation of mesenchymal intermediate filament protein vimentin, has also been implicated in the acquisition of a malignant phenotype by epithelial cancer cells. Members of the protein kinase C (PKC) superfamily are involved in cell migration and various integrindependent cellular functions. One aim of this work was to shed light on the role of vimentin in the regulation of integrin traffic and cell motility. In addition, the mechanism by which vimentin participates in EMT was investigated. The results show that integrin recycling and motility are dependent on the PKC–mediated phosphorylation of vimentin. In addition, vimentin was found to be a positive regulator of EMT and regulate the expression of several migratory genes. Specifically, vimentin governs the expression of receptor tyrosine kinase Axl, which is implicated in tumour growth and metastasis. Taken together, the findings described in this thesis reveal novel aspects of the complex interplay between distinct cellular components: integrins, syndecans, and the vimentin cytoskeleton, which all contribute to the regulation of human cancer cell adhesion, migration, and invasion.

Effect of hydrodynamics on modelling, monitoring and control of crystallization

Crystallization is a purification method used to obtain crystalline product of a certain crystal size. It is one of the oldest industrial unit processes and commonly used in modern industry due to its good purification capability from rather impure solutions with reasonably low energy consumption. However, the process is extremely challenging to model and control because it involves inhomogeneous mixing and many simultaneous phenomena such as nucleation, crystal growth and agglomeration. All these phenomena are dependent on supersaturation, i.e. the difference between actual liquid phase concentration and solubility. Homogeneous mass and heat transfer in the crystallizer would greatly simplify modelling and control of crystallization processes, such conditions are, however, not the reality, especially in industrial scale processes. Consequently, the hydrodynamics of crystallizers, i.e. the combination of mixing, feed and product removal flows, and recycling of the suspension, needs to be thoroughly investigated. Understanding of hydrodynamics is important in crystallization, especially inlargerscale equipment where uniform flow conditions are difficult to attain. It is also important to understand different size scales of mixing; micro-, meso- and macromixing. Fast processes, like nucleation and chemical reactions, are typically highly dependent on micro- and mesomixing but macromixing, which equalizes the concentrations of all the species within the entire crystallizer, cannot be disregarded. This study investigates the influence of hydrodynamics on crystallization processes. Modelling of crystallizers with the mixed suspension mixed product removal (MSMPR) theory (ideal mixing), computational fluid dynamics (CFD), and a compartmental multiblock model is compared. The importance of proper verification of CFD and multiblock models is demonstrated. In addition, the influence of different hydrodynamic conditions on reactive crystallization process control is studied. Finally, the effect of extreme local supersaturation is studied using power ultrasound to initiate nucleation. The present work shows that mixing and chemical feeding conditions clearly affect induction time and cluster formation, nucleation, growth kinetics, and agglomeration. Consequently, the properties of crystalline end products, e.g. crystal size and crystal habit, can be influenced by management of mixing and feeding conditions. Impurities may have varying impacts on crystallization processes. As an example, manganese ions were shown to replace magnesium ions in the crystal lattice of magnesium sulphate heptahydrate, increasing the crystal growth rate significantly, whereas sodium ions showed no interaction at all. Modelling of continuous crystallization based on MSMPR theory showed that the model is feasible in a small laboratoryscale crystallizer, whereas in larger pilot- and industrial-scale crystallizers hydrodynamic effects should be taken into account. For that reason, CFD and multiblock modelling are shown to be effective tools for modelling crystallization with inhomogeneous mixing. The present work shows also that selection of the measurement point, or points in the case of multiprobe systems, is crucial when process analytical technology (PAT) is used to control larger scale crystallization. The thesis concludes by describing how control of local supersaturation by highly localized ultrasound was successfully applied to induce nucleation and to control polymorphism in reactive crystallization of L-glutamic acid.

Hiilijalanjäljen laskeminen purku- ja korjausrakentamiskohteille

Tämä opinnäytetyö on tehty yhteistyössä Lappeenrannan teknillisen yliopiston ja Enviroc Oy:n kanssa. Työn tarkoituksena on ollut kehittää suomalaisiin olosuhteisiin soveltuva laskentamalli purku- ja korjausrakentamiskohteiden hiilijalanjäljelle. Kehitettyä mallia voi käyttää yrityksessä lainsäädännön vaatimusten noudattamisen todentamiseen sekä purku- ja korjausrakentamiskohteiden toimintatapojen vertailuun. Työssä käsitellään purku- ja korjausrakentamiskohteiden hiilijalanjälkeen vaikuttavia asioita, joita ovat työmaan energiankulutus sekä syntyvien jätteiden lajittelu, kuljetukset, käsittely ja hyödyntäminen tai loppusijoitus. Laskentamalli on kehitetty laskemalla esimerkkikohteille hiilijalanjäljet elinkaarimallintamisen avulla. Työssä on tarkasteltu myös vaihtoehtoisia jäteskenaarioita sekä laskentamallin luotettavuutta. Työn lopputuloksena on saatu kolmen eri kokoluokan esimerkkikohteen hiilijalanjäljet ja laskentamallin periaatekaaviot. Jätteiden toimituspisteiden ja jätejakeiden kulkureittien vaihtelevuuden sekä eri kohteista muodostuvien erityyppisten jätejakeiden johdosta yhden kokonaisvaltaisen laskentamallin kehittäminen on haasteellista. Myös tietojen hankinta kohteista ja jatkokäsittelyistä ja etenkin primääritietojen saaminen on ongelmallista. Tämänhetkinen laskentamalli perustuu enimmäkseen sekundääritietoihin ja arvioihin, joten mallin luotettavuuden lisäämiseksi olisi panostettava primääritiedon määrän lisäämiseen. Laskennan perusteella jäteskenaariovaihtoehdoista lajitteleva toimintamalli osoittautui hiilijalanjäljen kannalta suotuisimmaksi pienemmissä kohteissa ja käsittelylaitospainotteinen malli suuressa kohteessa. Merkittäviä tekijöitä kohteiden hiilijalanjälkien muodostumiselle olivat metallien käsittely, jätteiden poltto sekä neitsytraaka-aineista valmistetun teräksen ja fossiilisten polttoaineiden vältetyt päästöt. Merkittävimmiksi kasvihuonekaasuiksi purku- ja korjausrakentamiskohteiden laskennassa osoittautuivat hiilidioksidin lisäksi halogenoidut hiilivedyt ja metaani.

Komposiittien käyttö tämän päivän koneenrakennuksessa

Komposiitit ovat yhdistelmämateriaaleja, jotka koostuvat kahdesta tai useammasta eri materiaalista. Komposiitit ovat kiinnostavia tämän päivän koneenrakennukselle niiden korkean vahvuuden ja jäykkyyden suhteesta niiden kevyeeseen painoon nähden. Kuitulujitteisten komposiittien ja laminaattien valmistukseen on monia eri menetelmiä ja ne eroavat toisistaan lähinnä hartsin levittämistapojen sekä kuitujen asettelutapojen perusteella. Komposiittien työstäminen on vaikeaa, mikä johtuu niiden epähomogeenisesta ja anistrooppisesta laadusta ja komposiittien sisältävien lujitteiden korkeasta abrasiivisesta vaikutuksesta. Tavanomaisia työstömenetelmiä, kuten sorvausta, porausta ja jyrsimistä käytetään komposiittien työstämiseen. Kuitujen suuntaus komposiiteissa vaikuttaa paljon niiden työstämiseen. Ultraäänisen tärinän käyttäminen kuitulujitteisia komposiitteja sorvattaessa parantaa työstetyn kappaleen pinnanlaatua. Komposiittimateriaalien kiinnittäminen metalleihin eroaa selvästi muiden materiaalien kiinnittämisestä. Komposiittien yhdistämisen yhteydessä on otettava huomioon monia eri asioita, kiinnitysreikien valmistuksesta käytettäviin kiinnikkeisiin. Komposiittien kierrätys ja hävittäminen on tärkeä osa niiden elinkaarta, eikä niiden kierrätykseen ole tällä hetkellä hyviä ja kustannustehokkaita kierrätysmenetelmiä. Tällä hetkellä kierrättäminen tuleekin kalliimmaksi, kuin käytettyjen komposiittien vieminen kaatopaikalle.

Syntypaikkalajitellun sekajätteen koostumuksen sekä palamisteknisten ominaisuuksien selvitys Etelä-Karjalan alueella

Etelä-Karjalan alueen lajittelututkimuksen tavoitteena oli selvittää alueella syntyvän syntypaikkalajitellun sekajätteen koostumus sekä jätteen palamistekniset ominaisuudet. Palamisteknisinä ominaisuuksina selvitettiin jätteen kosteuspitoisuus, tuhkapitoisuus sekä tehollinen lämpöarvo saapumistilassa. Lisäksi pyrittiin löytämään ratkaisuja kaatopaikkakuormituksen pienentämiselle. Saatuja tuloksia verrattiin aiemmin Suomessa tehtyihin jätekoostumustutkimuksiin ja palamisteknisten ominaisuuksien selvityksiin. Lajittelututkimuksen tulosten perusteella erilliskeräys tarvitsee tehostamista. Biohajoavaa jätettä alueelta kerätyistä otoksista oli 51 m-%, josta biojätettä oli noin 24 m-%. Lisäksi jätteestä kierrätykseen kelpaavia jakeita oli 21 m-%. Palamisteknisten ominaisuuksien määrityksessä tulokset olivat kuivajätteen osalta seuraavat: kosteuspitoisuus 29 %, tehollinen lämpöarvo saapumistilassa 15 MJ/kg ja tuhkapitoisuus kuiva-aineesta 16 %. Tutkimuksesta saadut tulokset ovat linjassa referenssitutkimusten tulosten kanssa. Kaatopaikkakuormituksen vähentämisessä keskeisiä toimenpiteitä ovat tiedotus ja neuvonta. Lisäksi erilliskeräyspisteiden sijoittelulla ja määrän lisäämisellä voidaan saada vähennettyä kierrätyskelpoisen jätteen loppusijoitusta kaatopaikalle. Kierrätyskelvottomien jakeiden poltolla saadaan myös pienennettyä kaatopaikalle loppusijoitettavan jätteen määrää. Syntypaikkalajitellun sekajätteen seassa oli runsaasti polttokelpoista materiaalia. Massapolttoon kelpaavaa jätteestä oli 92 m-% ja energiajätteeseen kelpaavaa 47 m-%. Näistä 13 m-% oli kierrätykseen kelpaavaa jaetta, joka tulisi ohjata kierrätykseen.

Waste Stream Investigation from Perspective of Changing Waste Legislation at Green Sand Foundries

The update of the Finnish legislation concerning waste was unavoidable, to comply with the European Union (EU) requirements defined in the EU-Directive on Waste. The new waste law updates were enacted into the Finnish legislation on the 11.03.2011 and targeted for applicability by the 11.03.2012. This thesis investigates the implications of the new amendments to the waste legislation from the perspective of green sand foundries. The investigations are conducted by comparing two of Componenta’s green sand foundries and evaluating their waste streams. Additionally, the impacts of legislation amendments are critiqued on their environmental and economic aspects. The study’s comparison of waste fractions at the two foundries reveals that sand is dominant in absolute tonnage and costs. The increments of waste taxes forces foundries to focus on waste management, recycling and disposing. The new legislation’s promotion of material efficiency, also guides foundries towards the prevention of waste. A potential preventive measure is to regenerate waste sand resulting to cost savings on both raw-materials and waste management. However, the lack of absolute targets for waste prevention or recycling rates discourages the interests towards creating or adopting new technologies and methods for the waste handling.

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.