Emulation of an OWC Ocean Energy Plant With PMSG and Irregular Wave Model

Ocean energy is a promising resource for renewable electricity generation that presents many advantages, such as being more predictable than wind energy, but also some disadvantages such as large and slow amplitude variations in the generated power. This paper presents a hardware-in-the-loop prototype that allows the study of the electric power profile generated by a wave power plant based on the oscillating water column (OWC) principle. In particular, it facilitates the development of new solutions to improve the intermittent profile of the power fed into the grid or the test of the OWC behavior when facing a voltage dip. Also, to obtain a more realistic model behavior, statistical models of real waves have been implemented.

Design and installation, total energy plant-central equipment building, Summit Plaza Apartments : "Operation Breakthrough site", Jersey City, New Jersey /

"Previous edition current."

Energy from waste (EfW): a feasibility study on the economic and the environmental co-benefits of biogas production within rural communities

Energy from waste (E/W) technologies in the form o f biogas plants, CHP plants and other municipal solid waste (MSW) conversion technologies, have been gaining steady ground in the provision o f energy throughout Europe and the UK. Urban Waste Water Treatment Plants (UWWTP) are utilising much o f the same biochemical processes common to these E/W plants. Previous studies on Centralised Anaerobic Digestion (CAD) within Ireland found that the legislative and economic conditions were not conducive to such an operation on the grounds o f low energy price for electric and heat energy, and due to the restrictive nature o f the allowable feedstocks. Recent changes to the Irish REFIT tariff on energy produced from Anaerobic digestion; alterations to the regulation o f the allowable use o f animal by products(ABP); the recent enactment o f the Renewable Energy D irective (09/28/EC) and a subsequent review o f the draft Biowaste Directive (2001) required that the issue o f decentralised energy production in Ireland be reassessed. In this instance the feasibility study is based on a extant rural community, centred around the village o f Woodford Co Galway. The review found that the prevailing conditions were now such that it was technically and economically feasible for this biochemical process to provide energy and waste treatment facilities at the above location. The review also outlines the last item which is preventing this process from becoming achievable, specifically the lack o f a digestate regulation on land spreading which deals specifically with biowaste. The study finds that the implementation o f the draft EU biowaste regulations, with amendments for Cr and Hg levels to match the proposed Irish regulation for compost, would ensure that Ireland has some o f the most restrictive regulations in Europe for this application. The delay in completing this piece o f legislation is preventing national energy and waste issues from being resolved in a planned and stepwise fashion. A proposed lay out for the new Integrated Waste from Energy Plant (IW/EP) is presented. Budget economic projections and alternative revenue streams are outlined. Finally a review o f the national policies regarding the Rural Development Plan (RDP), the Rural Planning Guidelines (RPG) and the National Renewable Energy Action Plan (NREAP) are examined against the relevant EU directives.

Impacts of plant-based foods in ancestral hominin diets on the metabolism and function of gut microbiota in vitro

Ancestral human populations had diets containing more indigestible plant material than present-day diets in industrialized countries. One hypothesis for the rise in prevalence of obesity is that physiological mechanisms for controlling appetite evolved to match a diet with plant fiber content higher than that of present-day diets. We investigated how diet affects gut microbiota and colon cells by comparing human microbial communities with those from a primate that has an extreme plant-based diet, namely, the gelada baboon, which is a grazer. The effects of potato (high starch) versus grass (high lignin and cellulose) diets on human-derived versus gelada-derived fecal communities were compared in vitro. We especially focused on the production of short-chain fatty acids, which are hypothesized to be key metabolites influencing appetite regulation pathways. The results confirmed that diet has a major effect on bacterial numbers, short-chain fatty acid production, and the release of hormones involved in appetite suppression. The potato diet yielded greater production of short-chain fatty acids and hormone release than the grass diet, even in the gelada cultures, which we had expected should be better adapted to the grass diet. The strong effects of diet on hormone release could not be explained, however, solely by short-chain fatty acid concentrations. Nuclear magnetic resonance spectroscopy found changes in additional metabolites, including betaine and isoleucine, that might play key roles in inhibiting and stimulating appetite suppression pathways. Our study results indicate that a broader array of metabolites might be involved in triggering gut hormone release in humans than previously thought. IMPORTANCE: One theory for rising levels of obesity in western populations is that the body's mechanisms for controlling appetite evolved to match ancestral diets with more low-energy plant foods. We investigated this idea by comparing the effects of diet on appetite suppression pathways via the use of gut bacterial communities from humans and gelada baboons, which are modern-day primates with an extreme diet of low-energy plant food, namely, grass. We found that diet does play a major role in affecting gut bacteria and the production of a hormone that suppresses appetite but not in the direction predicted by the ancestral diet hypothesis. Also, bacterial products were correlated with hormone release that were different from those normally thought to play this role. By comparing microbiota and diets outside the natural range for modern humans, we found a relationship between diet and appetite pathways that was more complex than previously hypothesized on the basis of more-controlled studies of the effects of single compounds.

Simulação interactiva do mercado de energia eléctrica

A área de comercialização de energia eléctrica conheceu uma profunda mudança após a liberalização do sector eléctrico, que levou à criação de algumas entidades, as quais gerem os mercados de electricidade europeus. Relativamente a Portugal e Espanha, durante esse processo de liberalização, deu-se também um acordo que os levou à criação de um mercado conjunto, um mercado Ibérico (MIBEL). Dentro deste mercado estão contemplados dois operadores, sendo que um deles representa o pólo Português (OMIP) e o outro representa o pólo Espanhol (OMEL). O OMIP contempla os mercados a prazo, ou futuros, normalmente apresenta contratos de energia comercializada com durabilidade de semanas, meses, trimestres, semestres ou mesmo anos. Diariamente estes contratos poderão vencer no OMEL, que engloba os mercados, diário e intradiário. Este, ao contrário do OMIP negoceia para o dia seguinte (mercado diário) ou para uma determinada altura do dia (mercado intra diário). O mercado diário será o exemplo usado para a criação do simulador interactivo do mercado de energia eléctrica. Este será composto por diversos utilizadores (jogadores), que através de uma plataforma HTML irão investir em centrais de energia eléctrica, negociar licitações e analisar o funcionamento e resultados deste mercado. Este jogo subdividir-se-á então em 3 fases: 1. Fase de investimento; 2. Fase de venda (licitações); 3. Fase de mercado. Na fase do investimento, o jogador terá a possibilidade de adquirir unidades de geração de energia eléctrica de seis tipos de tecnologia: 1. Central a Carvão; 2. Central de Ciclo Combinado; 3. Central Hídrica; 4. Central Eólica; 5. Central Solar; 6. Central Nuclear. Com o decorrer das jogadas o jogador poderá aumentar a sua capacidade de investimento, com a venda de energia, sendo o vencedor aquele que mais saldo tiver no fim do número de jogadas previamente definidos, ou aquele que mais depressa atingir o saldo definido como limite pelo administrador do jogo. A nível pedagógico este simulador é muito interessante pois para além de o utilizador ficar a conhecer as tecnologias em causa e as vantagens e desvantagens das centrais de energia renovável e das centrais a combustíveis fósseis, este ganha igualmente uma sensibilidade para questões de nível ambiental, tais como o aumento dos gases de estufa e o degelo resultante do aquecimento global provocado por esses gases. Para além do conhecimento adquirido na parte de energia eléctrica este jogo dará a conhecer ao utilizador o funcionamento do mercado da energia eléctrica, bem como as tácticas que este poderá usar a seu favor neste tipo de mercado.

Höyrynkehitin-vedenlämmitin-energialaitoksen kunnossapidon tuotteistaminen

Työn tavoitteena on luoda ehdotus toimintamalliksi, jolla Polarmatic Oy:n valmistaman Turbomatic-energialaitoksen kunnossapitotoimintaa voitaisiin suorittaa. Kunnossapito on yrityksessä mielenkiinnon kohteena, koska asiakkaiden suunnalta on asiaa kohtaan ollut kiinnostusta. Toimintamallia on tarkoitus muuttaa vikoja ehkäiseväksi ja suunnitelmallisemmaksi. Nykyinen käyttö vikaantumiseen asti aiheuttaa ennakoimatonta korjaustarvetta. Työssä tutustutaan kunnossapitopalvelun tuotteistamiseen ja tuotteistamisprosessiin. Palvelun tuotteistaminen on prosessi, jossa asiakkaalle tarjottava palvelumääritellään, suunnitellaan ja kuvataan. Asiantuntijapalvelun, tässä tapauksessa kunnossapitopalvelun, tarjoaminen lähtee aina tuotteen syvällisestä tuntemuksesta. Turbomaticin kunnossapidon suunnittelua varten työssä käydään läpi energialaitoksen tekninen kuvaus, huoltokohteet ja vikaantuminen. Tiedot on kerätty Polarmaticin henkilökunnan haastatteluista. Kunnossapidon teoriaan ja palvelun tuotteistamiseen tutustutaan kirjallisuuden ja ajankohtaisen lähdemateriaalin avulla. Lisäksi työssä perehdytään muiden yritysten tarjoamiin kunnossapitopalveluihin internetsivuilta. Tulokseksi työstä saadaan toimintaehdotus kunnossapidon järjestämisestä. Vuosihuollon suorittamista varten on työssä liitteenä vuosihuollon tarkastuspöytäkirja. Lisäksi vuosihuoltotarjousten tekoa varten on tehty laskentaohjelma.

Seisokkien aiheuttamat kustannukset ja tulonmenetykset ongelma- ja yhdyskuntajätteen termisessä käsittelyssä

Tämän opinnäytetyön tarkoituksena oli selvittää seisokkitunnista aiheutuvat kustannukset ja tulonmenetykset eri polttolinjoille ja niiden kombinaatioille Ekokem Oy Ab:n jätteenpolttolaitoksessa. Työ suoritettiin tarkastelemalla prosessitietokantaan tallentunutta tietoa sekä keräämällä tietoa haastatteluilla. Jätetulon menetyksen määrittelytavalla oli keskeinen vaikutus tulonmenetysten muodostumiseen. Muita kustannuksiin ja tulonmenetyksiin vaikuttavia tekijöitä olivat vuodenaika, seisokin pituus ja energiantoimituksen sopimukset. Kaikissa seisokeissa ei välttämättä aiheudu välitöntä jätetulon menetystä, mutta käsittelemättä jäävän jätteen voidaan silti nähdä aiheuttavan tilapäisvarastoinnin tarvetta, josta aiheutuu kustannuksia. Tämän vuoksi eri polttolinjojen jätetulon menetys laskettiin kahdella tavalla olettaen ensin kaiken polttamatta jäävän jätteen aiheuttavan jätetulon menetystä sekä siten, että jätetulon menetys ja mahdollisesta varastoinnista aiheutuvat kustannukset arvioitiin kokemusperäisesti. Jätetulon todellisten menetysten määräytyminen voi tapahtua kummalla tavalla hyvänsä riippuen seisokkihetkellä vallitsevista olosuhteista. Kustannukset ja tulonmenetykset laskettiin kolmelle eripituiselle ajanjaksolle ja jaettiin tuntihinnoiksi. Työssä käsitellyille eri seisokkitilanteille saatiin 131 eri tuntihintaa kun muuttujia vaihdeltiin. Suurimmat kustannukset ja tulonmenetykset muodostuivat jätevoimalan seisokista lämmityskaudella. Tämä johtui siitä, että jätevoimalassa poltettavaa yhdyskuntajätettä ei pystytä varastoimaan toisin kuin ongelmajätteitä. Jätevoimalan seisokkitunti voi lämmityskaudella maksaa enimmillään 2600 €/h, josta menetetyn jätetulon osuus on liki puolet. Lisäksi jätevoimalan höyryntuotanto on yli puolet kokonaistuotannosta.

Jätteenpolton typenoksidipäästöjen vähentäminen

Työn tavoitteena oli selvittää jätteenpolton typenoksidipäästöjen puhdistusmahdollisuuksia. Työssä käydään läpi typen oksidien muodostuminen poltossa ja typen oksidien poistomenetelmät. Poistomenetelmiä käsiteltäessä painotus on arinapoltossa ja erityisesti selektiivisessä ei-katalyyttimenetelmässä (SNCR). Työn kokeellinen osa tehtiin Ekokem Oy Ab:n jätevoimalassa Riihimäellä. Kokeellisessa osassa selvitettiin ensin ammoniakkiveden massavirran, SNCR-laitteiston veden massavirran ja räjähdysnuohouksen vaikutusta typenoksidipitoisuuteen. Samalla selvitettiin muita typenoksidipitoisuuteen vaikuttavia tekijöitä sekä SNCR-laitteiston puhdistustehokkuus. Sen jälkeen selvitettiin parhaita toiminta-arvoja öljyisen veden massavirralle, SNCR-laitteiston massavirralle ja primääri- ja sekundääri-ilman suhteelle typenoksidipitoisuuden, ammoniakki-slip:n, ilokaasupitoisuuden, ammoniakkiveden kulutuksen ja höyryn tuotannon kannalta. Tulokseksi saatiin, että ammoniakkiveden massavirran lisääminen pienentää typenoksidipitoisuutta, mutta voi aiheuttaa ammoniakkipäästön. Paras SNCR-laitteiston veden massavirta on suurin tutkittu, 800 kg/h, jolloin typenoksidipitoisuus sekä typenoksidipitoisuuden hetkittäinen vaihtelu, ammoniakkiveden kulutus ja ammoniakkipäästö ovat pienimmät. Samalla tosin höyryn virtaama pienenee. SNCR-laitteiston puhdistustehokkuudeksi saatiin 60 %. Räjähdysnuohouksella ei ole havaittavaa, eikä öljyisen veden massavirralla merkittävää vaikutusta typenoksidipitoisuuteen. Ammoniakkiveden kulutuksen kannalta paras öljyisen veden määrä on 600 kg/h, kun taas ammoniakki-slip:n kannalta paras öljyisen veden määrä on 950 kg/h. Primääri-ilman osuuden pienentäminen pienentää ammoniakki-slip:iä ja ammoniakkiveden kulutusta.

Toimintaohjeistus HSY:n jätteenpolton materiaalivirtojen hallintaan

Vantaan Energia rakentaa ympäristövaatimukset täyttävän jätevoimalan Itä-Vantaan Långmossebergeniin. Jätevoimalassa tullaan käyttämään polttoaineena kierrätykseen kelpaamatonta syntypaikkalajiteltua yhdyskuntajätettä sekä maakaasua. Helsingin seudun ympäristöpalvelut -kuntayhtymä HSY tulee toimittamaan noin 80 % vuosittaisesta jätepolttoaineesta. Tässä työssä on esitetty toimintamalli HSY:n jätteenpolton materiaalivirtojen hallitsemiseksi. Toimintamallin tarkoituksena on antaa ohjeistus jätteiden materiaalivirtojen käsittelymenetelmistä ennen jätteenpolttolaitosta. Lisäksi toimintamallin tarkoituksena on saada vähennettyä pohjakuonan määrää. Toimintamalli sisältää ohjeistuksen kotitalouksien sekajätteen, pienjäteasemien sekajätteen, sekalaisen rakennus- ja purkujätteen sekä kaupan- ja teollisuuden jätteiden käsittelytavoista. Jätevirtojen koostumusta on selvitetty kirjallisuudesta löytyvien tietojen perusteella ja tietoja on täydennetty kesällä 2013 suoritetun lajittelututkimuksen tiedoilla. Tutkimuksen tuloksista selvisi, että pienjäteasemien sekajätteiden lajittelua tehostamalla HSY:llä pystytään tekemään merkittäviä taloudellisia säästöjä. Tutkimuksessa selvisi, että kipsilevy olisi kannattavinta kerätä omalle lavalleen pienjäteasemilla. Sekalaisen rakennus- ja purkujätteen osalta todettiin, että sitä ei kannata ohjata suoraan jätevoimalalle poltettavaksi, eikä sitä voida sijoittaa käsittelemättömänä kaatopaikalle vuoden 2020 jälkeen. Tästä syystä työssä on ehdotettu, että sekalainen rakennus- ja purkujäte ohjattaisiin lajittelulaitokselle käsiteltäväksi ennen sen loppusijoittamista. Tutkimuksen tulosten perusteella voidaan myös todeta, että toimintamallia noudattamalla, pohjakuonan määrää on mahdollista vähentää lähes puolella alkuperäisestä arviosta.

Los Intereses geoestatégicos de Rusia, Brasil y Estados Unidos en la Cuenca Amazónica periodo 2004-2008

La Cuenca Amazónica es el nuevo escenario geoestratégico redefinido de Halford Mackinder: el Green Heart Land, el cual refleja los intereses geoestratégicos de diferentes potencias mundiales como Brasil, Rusia y Estados Unidos, los cuales actuan bajos sus propios intereses nacionales. Su interacción deja como consecuencia la elaboración de una nueva estructura en el Sistema Internacional bajo nuevas nociones de seguridad, las cuales dinamizan las fichas del ajedrez mundial descrito por Zbniew Brzezinski.

SOCIAL MONOGAMY AND BIPARENTAL CARE OF THE NEOTROPICAL SOUTHERN BAMBOO RAT (KANNABATEOMYS AMBLYONYX)

We analyzed social patterns indicative of the mating system and parental care in a population of the southern bamboo rat (Kannabateomys amblyonyx). This arboreal rodent feeds exclusively on bamboo stems and leaves. We conducted fieldwork from August 2003 to October 2004 in southern Brazil (30 degrees 20`-30 degrees 27`S, 50 degrees 50`-51 degrees 05`W), in patches of introduced Chinese bamboo (Bambusa tuldoides). We captured 18 individuals, 7 of which were adults that received radiotransmitters and were followed from 1 to 12 months. Another 5 animals (adults or subadults) received colored collars. We observed paternal care, delayed juvenile dispersal, and reduced degree of sexual dimorphism, all of which are traits typical of social monogamy. Mated males showed a direct parental behavioral repertoire similar to that of females (with the obvious exception of nursing), including grooming, huddling, and food provisioning. Potential monogamy in this species seems to be a flexible strategy linked to low density of bamboo patches. Females were confined to widely spaced., small home ranges, decreasing the possibility of male defense of and access to > 1 female. The arboreal habits of the species possibly increase the risk of inexperienced young falling from trees or else being depreciated when moving exposed through branches. This risk is probably reduced by the extensive biparental care observed, including the providing of low-energy plant food to young in the nest.

Integrated pulp and paper mill planning and scheduling

This article describes a real-world production planning and scheduling problem occurring at an integrated pulp and paper mill (P&P) which manufactures paper for cardboard out of produced pulp. During the cooking of wood chips in the digester, two by-products are produced: the pulp itself (virgin fibers) and the waste stream known as black liquor. The former is then mixed with recycled fibers and processed in a paper machine. Here, due to significant sequence-dependent setups in paper type changeovers, sizing and sequencing of lots have to be made simultaneously in order to efficiently use capacity. The latter is converted into electrical energy using a set of evaporators, recovery boilers and counter-pressure turbines. The planning challenge is then to synchronize the material flow as it moves through the pulp and paper mills, and energy plant, maximizing customer demand (as backlogging is allowed), and minimizing operation costs. Due to the intensive capital feature of P&P, the output of the digester must be maximized. As the production bottleneck is not fixed, to tackle this problem we propose a new model that integrates the critical production units associated to the pulp and paper mills, and energy plant for the first time. Simple stochastic mixed integer programming based local search heuristics are developed to obtain good feasible solutions for the problem. The benefits of integrating the three stages are discussed. The proposed approaches are tested on real-world data. Our work may help P&P companies to increase their competitiveness and reactiveness in dealing with demand pattern oscillations. (C) 2012 Elsevier Ltd. All rights reserved.

Biomass Gasification - Process analysis and dimensioning aspects for downdraft units and gas cleaning lines

In such territories where food production is mostly scattered in several small / medium size or even domestic farms, a lot of heterogeneous residues are produced yearly, since farmers usually carry out different activities in their properties. The amount and composition of farm residues, therefore, widely change during year, according to the single production process periodically achieved. Coupling high efficiency micro-cogeneration energy units with easy handling biomass conversion equipments, suitable to treat different materials, would provide many important advantages to the farmers and to the community as well, so that the increase in feedstock flexibility of gasification units is nowadays seen as a further paramount step towards their wide spreading in rural areas and as a real necessity for their utilization at small scale. Two main research topics were thought to be of main concern at this purpose, and they were therefore discussed in this work: the investigation of fuels properties impact on gasification process development and the technical feasibility of small scale gasification units integration with cogeneration systems. According to these two main aspects, the present work was thus divided in two main parts. The first one is focused on the biomass gasification process, that was investigated in its theoretical aspects and then analytically modelled in order to simulate thermo-chemical conversion of different biomass fuels, such as wood (park waste wood and softwood), wheat straw, sewage sludge and refuse derived fuels. The main idea is to correlate the results of reactor design procedures with the physical properties of biomasses and the corresponding working conditions of gasifiers (temperature profile, above all), in order to point out the main differences which prevent the use of the same conversion unit for different materials. At this scope, a gasification kinetic free model was initially developed in Excel sheets, considering different values of air to biomass ratio and the downdraft gasification technology as particular examined application. The differences in syngas production and working conditions (process temperatures, above all) among the considered fuels were tried to be connected to some biomass properties, such elementary composition, ash and water contents. The novelty of this analytical approach was the use of kinetic constants ratio in order to determine oxygen distribution among the different oxidation reactions (regarding volatile matter only) while equilibrium of water gas shift reaction was considered in gasification zone, by which the energy and mass balances involved in the process algorithm were linked together, as well. Moreover, the main advantage of this analytical tool is the easiness by which the input data corresponding to the particular biomass materials can be inserted into the model, so that a rapid evaluation on their own thermo-chemical conversion properties is possible to be obtained, mainly based on their chemical composition A good conformity of the model results with the other literature and experimental data was detected for almost all the considered materials (except for refuse derived fuels, because of their unfitting chemical composition with the model assumptions). Successively, a dimensioning procedure for open core downdraft gasifiers was set up, by the analysis on the fundamental thermo-physical and thermo-chemical mechanisms which are supposed to regulate the main solid conversion steps involved in the gasification process. Gasification units were schematically subdivided in four reaction zones, respectively corresponding to biomass heating, solids drying, pyrolysis and char gasification processes, and the time required for the full development of each of these steps was correlated to the kinetics rates (for pyrolysis and char gasification processes only) and to the heat and mass transfer phenomena from gas to solid phase. On the basis of this analysis and according to the kinetic free model results and biomass physical properties (particles size, above all) it was achieved that for all the considered materials char gasification step is kinetically limited and therefore temperature is the main working parameter controlling this step. Solids drying is mainly regulated by heat transfer from bulk gas to the inner layers of particles and the corresponding time especially depends on particle size. Biomass heating is almost totally achieved by the radiative heat transfer from the hot walls of reactor to the bed of material. For pyrolysis, instead, working temperature, particles size and the same nature of biomass (through its own pyrolysis heat) have all comparable weights on the process development, so that the corresponding time can be differently depending on one of these factors according to the particular fuel is gasified and the particular conditions are established inside the gasifier. The same analysis also led to the estimation of reaction zone volumes for each biomass fuel, so as a comparison among the dimensions of the differently fed gasification units was finally accomplished. Each biomass material showed a different volumes distribution, so that any dimensioned gasification unit does not seem to be suitable for more than one biomass species. Nevertheless, since reactors diameters were found out quite similar for all the examined materials, it could be envisaged to design a single units for all of them by adopting the largest diameter and by combining together the maximum heights of each reaction zone, as they were calculated for the different biomasses. A total height of gasifier as around 2400mm would be obtained in this case. Besides, by arranging air injecting nozzles at different levels along the reactor, gasification zone could be properly set up according to the particular material is in turn gasified. Finally, since gasification and pyrolysis times were found to considerably change according to even short temperature variations, it could be also envisaged to regulate air feeding rate for each gasified material (which process temperatures depend on), so as the available reactor volumes would be suitable for the complete development of solid conversion in each case, without even changing fluid dynamics behaviour of the unit as well as air/biomass ratio in noticeable measure. The second part of this work dealt with the gas cleaning systems to be adopted downstream the gasifiers in order to run high efficiency CHP units (i.e. internal engines and micro-turbines). Especially in the case multi–fuel gasifiers are assumed to be used, weightier gas cleaning lines need to be envisaged in order to reach the standard gas quality degree required to fuel cogeneration units. Indeed, as the more heterogeneous feed to the gasification unit, several contaminant species can simultaneously be present in the exit gas stream and, as a consequence, suitable gas cleaning systems have to be designed. In this work, an overall study on gas cleaning lines assessment is carried out. Differently from the other research efforts carried out in the same field, the main scope is to define general arrangements for gas cleaning lines suitable to remove several contaminants from the gas stream, independently on the feedstock material and the energy plant size The gas contaminant species taken into account in this analysis were: particulate, tars, sulphur (in H2S form), alkali metals, nitrogen (in NH3 form) and acid gases (in HCl form). For each of these species, alternative cleaning devices were designed according to three different plant sizes, respectively corresponding with 8Nm3/h, 125Nm3/h and 350Nm3/h gas flows. Their performances were examined on the basis of their optimal working conditions (efficiency, temperature and pressure drops, above all) and their own consumption of energy and materials. Successively, the designed units were combined together in different overall gas cleaning line arrangements, paths, by following some technical constraints which were mainly determined from the same performance analysis on the cleaning units and from the presumable synergic effects by contaminants on the right working of some of them (filters clogging, catalysts deactivation, etc.). One of the main issues to be stated in paths design accomplishment was the tars removal from the gas stream, preventing filters plugging and/or line pipes clogging At this scope, a catalytic tars cracking unit was envisaged as the only solution to be adopted, and, therefore, a catalytic material which is able to work at relatively low temperatures was chosen. Nevertheless, a rapid drop in tars cracking efficiency was also estimated for this same material, so that an high frequency of catalysts regeneration and a consequent relevant air consumption for this operation were calculated in all of the cases. Other difficulties had to be overcome in the abatement of alkali metals, which condense at temperatures lower than tars, but they also need to be removed in the first sections of gas cleaning line in order to avoid corrosion of materials. In this case a dry scrubber technology was envisaged, by using the same fine particles filter units and by choosing for them corrosion resistant materials, like ceramic ones. Besides these two solutions which seem to be unavoidable in gas cleaning line design, high temperature gas cleaning lines were not possible to be achieved for the two larger plant sizes, as well. Indeed, as the use of temperature control devices was precluded in the adopted design procedure, ammonia partial oxidation units (as the only considered methods for the abatement of ammonia at high temperature) were not suitable for the large scale units, because of the high increase of reactors temperature by the exothermic reactions involved in the process. In spite of these limitations, yet, overall arrangements for each considered plant size were finally designed, so that the possibility to clean the gas up to the required standard degree was technically demonstrated, even in the case several contaminants are simultaneously present in the gas stream. Moreover, all the possible paths defined for the different plant sizes were compared each others on the basis of some defined operational parameters, among which total pressure drops, total energy losses, number of units and secondary materials consumption. On the basis of this analysis, dry gas cleaning methods proved preferable to the ones including water scrubber technology in al of the cases, especially because of the high water consumption provided by water scrubber units in ammonia adsorption process. This result is yet connected to the possibility to use activated carbon units for ammonia removal and Nahcolite adsorber for chloride acid. The very high efficiency of this latter material is also remarkable. Finally, as an estimation of the overall energy loss pertaining the gas cleaning process, the total enthalpy losses estimated for the three plant sizes were compared with the respective gas streams energy contents, these latter obtained on the basis of low heating value of gas only. This overall study on gas cleaning systems is thus proposed as an analytical tool by which different gas cleaning line configurations can be evaluated, according to the particular practical application they are adopted for and the size of cogeneration unit they are connected to.

Horizontal, but not vertical, biotic interactions affect fine-scale plant distribution patterns in a low-energy system

Studies of species range determinants have traditionally focused on abiotic variables (typically climatic conditions), and therefore the recent explicit consideration of biotic interactions represents an important advance in the field. While these studies clearly support the role of biotic interactions in shaping species distributions, most examine only the influence of a single species and/or a single interaction, failing to account for species being subject to multiple concurrent interactions. By fitting species distribution models (SDMs), we examine the influence of multiple vertical (i.e., grazing, trampling, and manuring by mammalian herbivores) and horizontal (i.e., competition and facilitation; estimated from the cover of dominant plant species) interspecific interactions on the occurrence and cover of 41 alpine tundra plant species. Adding plant-plant interactions to baseline SDMs (using five field-quantified abiotic variables) significantly improved models' predictive power for independent data, while herbivore-related variables had only a weak influence. Overall, abiotic variables had the strongest individual contributions to the distribution of alpine tundra plants, with the importance of horizontal interaction variables exceeding that of vertical interaction variables. These results were consistent across three modeling techniques, for both species occurrence and cover, demonstrating the pattern to be robust. Thus, the explicit consideration of multiple biotic interactions reveals that plant-plant interactions exert control over the fine-scale distribution of vascular species that is comparable to abiotic drivers and considerably stronger than herbivores in this low-energy system.

Reduction of specific energy consumption of a thermomechanical pulping plant

Kuumahiertoprosessi on erittäin energiaintensiivinen prosessi, jonka energianominaiskulutus (EOK) on yleisesti 2–3.5 MWh/bdt. Noin 93 % energiasta kuluu jauhatuksessa jakautuen niin, että kaksi kolmasosaa kuluu päälinjan ja yksi kolmasosa rejektijauhatuksessa. Siksi myös tämän työn tavoite asetettiin vähentämään energian kulutusta juuri pää- ja rejektijauhatuksessa. Päälinjan jauhatuksessa tutkimuskohteiksi valittiin terityksen, tehojaon ja tuotantotason vaikutus EOK:een. Rejektijauhatuksen tehostamiseen pyrittiin yrittämällä vähentää rejektivirtaamaa painelajittelun keinoin. Koska TMP3 laitoksen jauhatuskapasiteettia on nostettu 25 %, tavoite oli nostaa päälinjan lajittelun kapasiteettia saman verran. Toisena tavoitteena oli pienentää rejektisuhdetta pää- ja rejektilajittelussa ja siten vähentää energiankulutusta rejektijauhatuksessa. Näitä tavoitteita lähestyttiin vaihtamalla päälinjan lajittimiin TamScreen-roottorit ja rejektilajittimiin Metso ProFoil-roottorit ja optimoimalla kuitufraktiot sihtirumpu- ja prosessiparametrimuutoksin. Syöttävällä terätyypillä pystyttiin vähentämään EOK:ta 100 kWh/bdt, mutta korkeampi jauhatusintensiteetti johti myös alempiin lujuusominaisuuksiin, korkeampaan ilmanläpäisyyn ja korkeampaan opasiteettiin. Myös tehojaolla voitiin vaikuttaa EOK:een. Kun ensimmäisen vaiheen jauhinta kuormitettiin enemmän, saavutettiin korkeimmillaan 70 kWh/bdt EOK-vähennys. Tuotantotason mittaamisongelmat heikensivät tuotantotasokoeajojen tuloksia siinä määrin, että näiden tulosten perusteella ei voida päätellä, onko EOK tuotantotasoriippuvainen vai ei. Päälinjan lajittelun kapasiteettia pystyttiin nostamaan TS-roottorilla vain 18 % jääden hieman tavoitetasosta. Rejektilajittelussa pystyttiin vähentämään rejektimäärää huomattavasti Metso ProFoil-roottorilla sekä sihtirumpu- ja prosessiparametrimuutoksin. Lajittamokehityksellä saavutettu EOK-vähennys arvioitiin massarejektisuhteen pienentymisen ja rejektijauhatuksessa käytetyn EOK:n avulla olevan noin 130 kWh/bdt. Yhteenvetona voidaan todeta, että tavoite 300 kWh/bdt EOK-vähennyksestä voidaan saavuttaa työssä käytetyillä tavoilla, mikäli niiden täysi potentiaali hyödynnetään tuotannossa.