995 resultados para Buried heat sources
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Given their central role in mercury (Hg) excretion and suitability as reservoirs, bird feathers are useful Hg biomonitors. Nevertheless, the interpretation of Hg concentrations is still questioned as a result of a poor knowledge of feather physiology and mechanisms affecting Hg deposition. Given the constraints of feather availability to ecotoxicological studies, we tested the effect of intra-individual differences in Hg concentrations according to feather type (body vs. flight feathers), position in the wing and size (mass and length) in order to understand how these factors could affect Hg estimates. We measured Hg concentration of 154 feathers from 28 un-moulted barn owls (Tyto alba), collected dead on roadsides. Median Hg concentration was 0.45 (0.076-4.5) mg kg(-1) in body feathers, 0.44 (0.040-4.9) mg kg(-1) in primary and 0.60 (0.042-4.7) mg kg(-1) in secondary feathers, and we found a poor effect of feather type on intra-individual Hg levels. We also found a negative effect of wing feather mass on Hg concentration but not of feather length and of its position in the wing. We hypothesize that differences in feather growth rate may be the main driver of between-feather differences in Hg concentrations, which can have implications in the interpretation of Hg concentrations in feathers. Finally, we recommend that, whenever possible, several feathers from the same individual should be analysed. The five innermost primaries have lowest mean deviations to both between-feather and intra-individual mean Hg concentration and thus should be selected under restrictive sampling scenarios.
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Determining the appropriate level of integration is crucial to realizing value from acquisitions. Most prior research assumes that higher integration implies the removal of autonomy from target managers, which in turn undermines the functioning of the target firm if it entails unfamiliar elements for the acquirer. Using a survey of 86 acquisitions to obtain the richness of detail necessary to distinguish integration from autonomy, the authors argue and find that integration and autonomy are not the opposite ends of a single continuum. Certain conditions (e.g., when complementarity rather than similarity is the primary source of synergy) lead to high levels of both integration and autonomy. In addition, similarity negatively moderates the relationship between complementarity and autonomy when the target offers both synergy sources. In contrast, similarity does not moderate the link between complementarity and integration. The authors' findings advance scholarly understanding about the drivers of implementation strategy and in particular the different implementation strategies acquiring managers deploy when they attempt to leverage complementarities, similarities, or both.
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En collectant plus de deux millions de tweets reliés au centenaire de la Grande Guerre, de nombreuses questions méthodologiques se sont posées, interrogeant par exemple la notion de corpus, les relations entre historien.ne.s et archivistes, le traitement du passé à une ère de données massives. Cette intervention se penche sur l'une de ces questions: comment fonder une recherche sur des sources primaires en flux? Comment résoudre la contradiction inhérente entre l'archive, réputée figée, et les données nées numériques qui sont émises en flux?
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The present study shows that with liquid nitrogen stored inocula of Saccharomyces cerevisiae, and standardized experimental procedure, flow microcalorimetry can be a valuable tool for monitoring in real time the alcoholic fermentation processes on line. The avaliation of cultural conditions contained different carbon sources for alcohol fermentation (sucrose, glucose, fructose, manose, maltose, galactose, molasses, honey and sugar cane) and their effects on the heat output recording is discussed. Some examples of diauxic growth is given, where the microcalorimeters serves to detect the temporal order of succession of alternating metabolic pathways.
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This study considered the current situation of biofuels markets in Finland. The fact that industry consumes more than half of the total primary energy, widely applied combined heat and power production and a high share of solid biomass fuels in the total energy consumption are specific to the Finnish energy system. Wood is the most important source of bioenergy in Finland, representing 21% of the total energy consumption in 2006. Almost 80% of the wood-based energy is recovered from industrial by-products and residues. Finland has commitment itself to maintaining its greenhouse gas emissions at the 1990 level, at the highest, during the period 2008–2012. The energy and climate policy carried out in recent years has been based on the National Energy and Climate introduced in 2005. The Finnish energy policy aims to achieve the target, and a variety of measures are taken to promote the use of renewable energy sources and especially wood fuels. In 2007, the government started to prepare a new long-term (up to the year 2050) climate and energy strategy that will meet EU’s new targets for the reduction of green house gas emissions and the promotion of renewable energy sources. The new strategy will be introduced during 2008. The international biofuels trade has a substantial importance for the utilisation of bioenergy in Finland. In 2006, the total international trading of solid and liquid biofuels was approximately 64 PJ of which import was 61 PJ. Most of the import is indirect and takes place within the forest industry’s raw wood imports. In 2006, as much as 24% of wood energy was based on foreignorigin wood. Wood pellets and tall oil form the majority of export streams of biofuels. The indirect import of wood fuels increased almost 10% in 2004–2006, while the direct trade of solid and liquid biofuels has been almost constant.
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Better models are needed for radiative heat transfer in boiler furnaces. If the process is known better, combustion in the furnace can be optimized to produce low emissions. It makes the process to be environmental friendly. Furthermore, if there is a better model of the furnace it can more fully explain what is happening inside the furnace. Using of the model one can quickly and easily analyze how it operates with bio fuels, moist fuels or difficult fuels and improve the operation. Models helps with better estimation of furnace dimensions and result in more accurate understanding of operation. Key component lacking in these models is radiative heat transfer in particle laden gases. If there are no particles than radiative heat transfer can be calculated approximately. There are two problems with current models when used with flow modeling. The first one is a need to account for a particle laden gas and the second one is an absence of a fast algorithm. Fast calculation is needed if radiative heat transfer calculation is done for a large CDF model. Computations slow down if time is required for calculating radiative properties over and over again. This thesis presents a band model for radiative heat transfer in boiler furnaces. Advantage is a quickness of calculation and account of particles in the process.
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This thesis gathers knowledge about ongoing high-temperature reactor projects around the world. Methods for calculating coolant flow and heat transfer inside a pebble-bed reactor core are also developed. The thesis begins with the introduction of high-temperature reactors including the current state of the technology. Process heat applications that could use the heat from a high-temperature reactor are also introduced. A suitable reactor design with data available in literature is selected for the calculation part of the thesis. Commercial computational fluid dynamics software Fluent is used for the calculations. The pebble-bed is approximated as a packed-bed, which causes sink terms to the momentum equations of the gas flowing through it. A position dependent value is used for the packing fraction. Two different models are used to calculate heat transfer. First a local thermal equilibrium is assumed between the gas and solid phases and a single energy equation is used. In the second approach, separate energy equations are used for the phases. Information about steady state flow behavior, pressure loss, and temperature distribution in the core is obtained as results of the calculations. The effect of inlet mass flow rate to pressure loss is also investigated. Data found in literature and the results correspond each other quite well, considered the amount of simplifications in the calculations. The models developed in this thesis can be used to solve coolant flow and heat transfer in a pebble-bed reactor, although additional development and model validation is needed for better accuracy and reliability.
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The radiocarbon dating of the soil organic matter (SOM) is a polemic subject, due mainly to the complexity of the formation of the soils and to the variable contamination from several sources. Soil samples from 4 different Brazilian localities were submitted to physical and chemical pre-treatment for the extraction of humin fraction, which is the most stable organic compound and theoretically the oldest and representative of the age of the SOM. The radiocarbon dating obtained from the total SOM and their humin fractions are compared to the 14C ages from buried charcoals at similar depths. The radiocarbon ages obtained from such charcoals are, in most of the cases, concordant within the experimental errors of those obtained on humin fractions, or are in average 10% higher, with one exception. Thus, the ages on humin fractions could be assumed as the minimum ages for the associated soils, while the results obtained on total SOM, even at depths until 200 cm, exhibit pronounced contamination effect by modern carbon, rejuvenating their ages.
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The optimal design of a heat exchanger system is based on given model parameters together with given standard ranges for machine design variables. The goals set for minimizing the Life Cycle Cost (LCC) function which represents the price of the saved energy, for maximizing the momentary heat recovery output with given constraints satisfied and taking into account the uncertainty in the models were successfully done. Nondominated Sorting Genetic Algorithm II (NSGA-II) for the design optimization of a system is presented and implemented inMatlab environment. Markov ChainMonte Carlo (MCMC) methods are also used to take into account the uncertainty in themodels. Results show that the price of saved energy can be optimized. A wet heat exchanger is found to be more efficient and beneficial than a dry heat exchanger even though its construction is expensive (160 EUR/m2) compared to the construction of a dry heat exchanger (50 EUR/m2). It has been found that the longer lifetime weights higher CAPEX and lower OPEX and vice versa, and the effect of the uncertainty in the models has been identified in a simplified case of minimizing the area of a dry heat exchanger.
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Maapallon ilmasto lämpenee koko ajan kasvihuonekaasujen määrän lisääntyessä ilmakehässä. Merkittävin ihmisten aiheuttama päästöjen lähde on fossiilisten polttoaineiden käyttö energiantuotannossa ja liikenteessä, jonka vuoksi on tärkeää lisätä uusiutuvien energialähteiden käyttöä. Tämän diplomityön tavoitteena oli selvittää esimerkkialueena olevan maaseutuyhteiskunnan mahdollisuutta olla energiaomavarainen ja materiaalikierroiltaan suljettu, jos alueen tarvitsema sähkö ja lämpö tuotettaisiin paikallisilla biomassavaroilla kahdella rinnakkaisella pienen mittakaavan CHP-laitoksella. Tarkastellut laitokset olivat anaerobisen mädätyksen ja polttokennojen yhdistelmä sekä termisen käsittelyn ja ORC-prosessin yhdistelmä. Työssä tehdyt laskelmat osoittivat, että esimerkkialue saisi tuotettua omilla biomassavaroillaan tarvitsemastaan sähköstä 75 % ja lämmöstä 90 % esimerkkilaitosten avulla. Laskelmissa ei kuitenkaan huomioitu kesä- ja talvikuukausien välistä eroa lämmön kulutuksessa, jonka vuoksi molemmat laitokset eivät voisi toimia koko ajan täydellä teholla. Lisäksi tuotetun lämmön hyötykäyttöä rajoittaa riittävän laajan kaukolämpöverkon puuttuminen esimerkkialueelta. Nykyisen kaukolämpöverkon avulla saataisiin hyödynnettyä vain kolmasosa ORC-prosessilla tuotetusta lämpöenergiasta. Laskelmat osoittivat myös, että alueen kasvihuonekaasupäästöt pienenisivät 21 % eli noin 6 000 hiilidioksidiekvivalenttitonnia vuodessa, jos suurin osa energiasta tuotettaisiin omista biomassavaroista CHP-laitosten avulla ja mädätyksen seurauksena syntyvä reaktorijäännös korvaisi kemiallisten lannoitteiden käytön.
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Euroopan unionissa pyritään lisäämään uusiutuvien energialähteiden käyttöä. Tämän työn tavoitteena oli selvittää Parikkalan kunnan alueella muodostuvat biomassat sekä tutkia niiden hyötykäyttömahdollisuuksia sähkön, lämmön sekä lannoitteiden tuotannossa. Käsiteltäviä biomassoja ovat eläintilojen lietteet ja lannat, biojätteet ja yhdyskuntalietteet, vesistöjen kunnostuksessa syntyvät biomassat sekä peltobiomassat ja metsäbiomassa. Mädätyksen kannalta olennaisinta on materiaalien kosteus ja haihtuvan orgaanisen aineksen pitoisuus sekä siitä saatava biokaasumäärä. Poltossa polttoaineen kuiva-aineen lämpöarvo ja kosteus määrittelevät saadun hyödyn. Kompostoinnissa on tärkeää huolehtia riittävästä ilman saannista ja riittävästä viipymäajasta. Hyödynnettäessä biokaasua sähkön ja lämmön yhteistuotannossa on tärkeää löytää hyötykäyttö myös muodostuvalle lämmölle. Poltosta saatavan tuhkan hyötykäyttö onnistuu metsälannoitteena, kun poltetaan turvetta tai puuta. Kompostia voidaan hyödyntää maanparannusaineena. Parikkalan alueella tarkasteltiin biomassojen nykyistä ja mahdollista tulevaa hyötykäyttöä. Tarkastelu tehtiin skenaarioiden avulla. Skenaarioihin kuuluvat mädätyksen ja polton maksimipotentiaalit sekä keskitetyn ja hajautetun käsittelyn skenaariot. Alueelta on saatavissa paljon biomassoja, joista massaltaan suurin on eläintilojen lannat. Alueella on hankaluutena löytää sopiva kulutuskohde biokaasusta tuotetulle lämmölle, mutta sopivana kohteena voisi toimia alueella oleva suuri sikala tai lämpökeskukset.
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This study illustrates the different types of plate heat exchangers that are commonly used in various domestic and industrial applications. The main purpose of this paper was to devise a methodology that is capable of calculating optimum number of plates in the design of a plate heat exchanger. To obtain the appropriate number of plates, typically several iterations must be made before a final acceptable design is completed, since plate amount depends on many factors such as, flow velocities, physical properties of the streams, flow channel geometry, allowable pressure drop, plate dimensions, and the gap between the plates. The methodology presented here can be used as a general guide for designing a plate heat exchanger. To investigate the effects of relevant parameters on the thermal-hydraulic design of a plate heat exchanger, several experiments were carried out for single-phase and counter flow arrangement with two brazed plate heat exchangers by varying the flow rates and the inlet temperatures of the fluid streams. The actual heat transfer coefficients obtained based on the experiment were nearly close to the calculated values and to improve the design, a correction factor was introduced. Besides, the effect of flow channel velocity on the pressure drop inside the unit is presented.
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It is often reasonable to convert old boiler to bubbling fluidized bed boiler instead of building a new one. Converted boiler consists of old and new heat surfaces which must be fitted to operate together. Prediction of heat transfer in not so ideal conditions sets challenges for designers. Two converted boilers situated in Poland were studied on the grounds of acceptance tests and further studies. Calculation of boiler process was performed with boiler design program. Main interest was heat transfer in superheaters and factors affecting it. Theory for heat transfer is presented according to information found from literature. Results obtained from experimental studies and calculations have been compared. With correct definitions calculated parameters corresponded well to measured data at boiler maximum design load. However overload situations revealed to be difficult to model at least without considering changes in the combustion process which requires readjustments to the design program input values.