956 resultados para constant pressure heat capacity
Resumo:
Tämän työn tarkoituksena on tarkastella tulevaisuuden kehitysnäkymien vaikutusta Vaasan kaukolämpötoimintaan. Komartekin Flowra 32 verkostolaskentaohjelman avulla tutkitaan kaukolämpöverkon siirtokykyä nykyisissä ja tulevaisuuden kuormitustilanteissa. Työn yhteydessä laaditaan kaukolämmityksen kasvuennuste seuraavalle kymmenelle vuodelle ja selvitetään mitoituslämpötilaa -29°C vastaava teho tilastollisen analyysin avulla. Lisäksi tutkitaan mahdollisia ratkaisuja huippu- ja varatehon tuottamiseksi. Tarkastelun kohteena on myös lämmön lyhytaikaisvarastoinnin kannattavuus energianhankintajärjestelmässä. Kaukolämpöverkon siirtokyky on tarkastelun perusteella kohtalaisen hyvä, mutta liittymistehojen kasvaessa paine-erot verkon häntäpäässä jäävät liian alhaisiksi. Paras ratkaisu paine-ero ongelmaan on rakentaa välipumppaamo Hovioikeudenpuistoon. Tarkastelun perusteella kaukolämmön varatehon lisätarve on kymmenen vuoden kuluttua noin 40 MW ja varatehoksi on kannattavinta rakentaa raskasta polttoöljyä käyttävä lämpökeskus. Lämmön lyhytaikaisvarastointi on nykyisillä energianhinnoilla kohtalaisen kannattavaa varsinkin, jos Kauppa- ja teollisuusministeriö myöntää hankkeelle täyden 30%:n investointiavustuksen.
Resumo:
Työn tavoitteena oli löytää painelajittimen roottorin keskeiset muuttujat ja ajoparametrit, kun pyritään jälkilajittelemaan valkaistua sellumassaa korkeassa sakeudessa, sekä näiden vaikutukset. Tavoitteena oli teknisesti onnistunut lajittelu korkeassa sakeudessa siten, että laitteen puhdistustehokkuus on hyvä, ominaisenergian kulutus on pieni ja kapasiteetti on korkea. Ensin tarkasteltiin kuitenkin teoreettisesti valkaistun sellumassan painelajittelun ongelmakenttää, keskeisten epäpuhtauksien poistoa jälkilajittelussa ja vertailtiin korkea- ja matalasakeuslajittelua. Lisäksi esiteltiin yleisellä tasolla koesuunnittelumenetelmien periaatteita ja menetelmiä sekä analyysiä so. mallinnus. Tätä taustaa vasten haluttiin myös kartoittaa ja esitellä painelajittimen keskeinen muuttujakenttä. Tämän jälkeen selvitettiin kokeellisesti miten ajettavan valkaistun mäntysellumassan sakeus, roottorin kehänopeus ja roottorin rakenteen muutokset vaikuttavat painelajittimen kapasiteettiin, rejektin sakeutumiskertoimeen, ominaisenergian kulutukseen ja puhdistustehokkuuteen. Vaikutusten ja parhaan roottorirakenteen sekä ajosuureiden määritys suoritettiin mallintamalla mittaustulokset lineaarisella regressioanalyysilla. Saatiin tärkeimmät vasteisiin vaikuttavat riippumattomat muuttujat ja niiden matemaattiset esityk-set, malliyhtälöt. Mallinnusta hyväksi käyttäen tarkasteltiin vielä erikseen yhden roottorin ajoa. Tärkeimpinä tuloksina saatiin selville, että puhdistustehokkuus on lähes vakio tietyllä roottorirakenteella riippumatta sakeudesta ja roottorin kehänopeudesta. Edullista puhdistustehokkuuden kannalta on käyttää ensisijaisesti isoa roottorin palaelementin korkeutta ja välystä suhteessa sihtirumpuun. Jälkilajittelu painelajittimella korkeassa sakeudessa kannattaa suorittaa pienellä roottorin kehänopeudella, runko- ja palaelementtivälyksellä suhteessa sihtirumpuun sekä suurella palaelementin korkeudella. Tällöin saavutetaan hyvä kompromissi ominaisenergian kulutuksen ja laitteen ajettavuuden osalta. Iso elementin korkeus ja pieni elementtivälys eivät aja massaa tehokkaasti laitteen alaosaan. Tällöin ei pyöritetä myöskään suurta massamäärää. Pieni elementtivälys mahdollistaa myös massan tehokkaamman leikkauksen, joka parantaa fluidisoitumista. Kitkavoimat ovat luonnollisesti ko. olosuhteissa suuremmat, joten ominais-energian kulutus kasvaa jonkin verran. Ratkaisevinta ominaisenergian kulutuksen kannalta on kuitenkin ajaa laitetta pienellä kehänopeudella.
Resumo:
Työn teoriaosassa esitetään kirjallisuudessa esiintyviä teoreettisia ja kokeellisia yhtälöitä nesteen nopeuden, kaasun tilavuusosuuden, painehäviön ja lämmönsiirron laskemiseksi. Lisäksi käsitellään airlift-reaktoreiden toimintaa, rakennetta ja teollisia sovelluksia, sekä sekoitusta ja geometrian vaikutusta airlift-reaktoreiden hydrodynaamisiin ominaisuuksiin. Kokeellisessa osassa kuvataan käytetty koelaitteisto ja mittausmenetelmät sekä esitetään saadut koetulokset. Koelaitteisto on viidellä nousuputkella varustettu ulkoisen kierron airlift-reaktori. Kokeellisessa osassa pyritään ratkaisemaan tällaisessa reaktorissa mahdollisesti esiintyviä ongelmia, kuten "slug flown" muodostuminen nousuputkissa sekä fluidien epätasainen jakautuminen nousuputkiin. Lisäksi tutkitaan erilaisten muuttujien, kuten kaasun tilavuusvirran, nesteen viskositeetin, suutinkoon ja nesteen jakoputken rakenteen, vaikutusta kaasun tilavuusosuuteen ja nesteen nopeuteen nousuputkissa. Nesteen nopeudet mitataan merkkiainemenetelmällä ja kaasun tilavuusosuudet manometrimenetelmällä. Lämmönsiirtoa tutkitaan mittaamalla lämpötilaeroja nousuputkissa NiCr-Ni –termoelementeillä. Mittaustulosten perusteella muokataan korrelaatiot kaasun tilavuusosuudelle ja nesteen tyhjäputkinopeudelle. Korrelaatioista lasketut tulokset sopivat kohtuullisen hyvin yhteen mitattujen tulosten kanssa. "Slug flown" ei todettu muodostuvan ongelmaksi 2.5 mPa s pienemmillä viskositeetin arvoilla 2 metriä pitkissä ja 19 mm halkaisijaltaan olevissa putkissa. Lisäksi todettiin, että kaasu- ja nestefaasien jakautumisongelmat voidaan ratkaista rakenteellisesti.
Resumo:
Exercising in the heat induces thermoregulatory and other physiological strain that can lead to impairments in endurance exercise capacity. The purpose of this consensus statement is to provide up-to-date recommendations to optimise performance during sporting activities undertaken in hot ambient conditions. The most important intervention one can adopt to reduce physiological strain and optimise performance is to heat acclimatise. Heat acclimatisation should comprise repeated exercise-heat exposures over 1-2 weeks. In addition, athletes should initiate competition and training in a euhydrated state and minimise dehydration during exercise. Following the development of commercial cooling systems (eg, cooling-vest), athletes can implement cooling strategies to facilitate heat loss or increase heat storage capacity before training or competing in the heat. Moreover, event organisers should plan for large shaded areas, along with cooling and rehydration facilities, and schedule events in accordance with minimising the health risks of athletes, especially in mass participation events and during the first hot days of the year. Following the recent examples of the 2008 Olympics and the 2014 FIFA World Cup, sport governing bodies should consider allowing additional (or longer) recovery periods between and during events, for hydration and body cooling opportunities, when competitions are held in the heat.
Resumo:
Catalunya és un dels territoris on hi ha hagut més auge del sector de la cervesa artesana, i són molt nombroses les microcerveseries i les botigues especialitzades on es poden trobar els recursos materials necessaris, a més de ser centres difusió de coneixements relacionats. Així, doncs, aquest projecte està emmarcat en un context que permet el desenvolupament de tècniques d’elaboració de cervesa artesana. Aquest projecte es basa en la construcció d’un equip amb materials reutilitzats i amb un pressupost limitat que permet reproduir a petita escala els processos d’elaboració que es duen a terme en les microcerveseries artesanes actuals. El projecte s’ha assentat sobre la comprensió dels fonaments teòrics i pràctics del procés d’elaboració de cervesa, i amb l’experiència inicial d’elaboració de cervesa amb un equip bàsic de tipus homebrewer. Per minimintzar costos els tancs s’han construït a partir de barrils de cervesa i les parts sobrants s’han aprofitat per a altres elements. S’han emprat elements quotidians com una olla a pressió i s’ha construït un sistema regulador de pressió (per al tanc de fermentació cilindrocònic isobàric construït) en lloc d’adquirir-lo. S’ha posat l’èmfasi en minimitzar la necessitat de manipulació manual durant l’elaboració. Per tant, s’han instal·lat els components de l’equip formant un circuit tancat amb sistema de bombeig, i s’ha incorporat un sistema que permet el control i la lectura de les temperatures de cada procés. Altres elements són el sistema de filtres amb mecanisme de tub en forma d’ela (que permet l’extracció del most dels tanc de maceració i de cocció d’una manera efectiva i sense necessitat de manipulació) i el sistema de dutxa (que permet automatitzar el procés de rentat i filtrat). Un element que distingeix aquest equip d’altres equips emprats en algunes microcerveseries artesanes és el tanc de fermentació cilindrocònic isobàric amb vàlvula controladora de pressió, que permet prescindir de la doble fermentació en ampolla, ja que permet aprofitar el gas carbònic produït durant la fermentació per la carbonatació de la cervesa. Es pot concloure que gràcies a les seves característiques, l’equip permet realitzar successives elaboracions obtenint el mateix producte amb les mateixes característiques organolèptiques, principalement gràcies a la cambra de fermentació, que permet realitzar les etapes de fermentació, maduració i clarificació controlant la temperatura desitjada; al tanc de maceració amb aïllament, que permet realitzar el procés a temperatura constant sense pèrdues tèrmiques i al sistema de control de temperatura de totes les etapes. L’únic inconvenient és que, degut a la manca pressupostària, ha estat impossible l’adquisició d’un sistema d’embotellament isobàric que permeti realitzar l’embotellament sense pèrdues del gas carbònic. Per tant, el producte final pot embotellar-se amb una lleugera pèrdua de gas o es pot emmagatzemar en el mateix fermentador cilindrocònic per al seu consum directe, a l’estil d’alguns brewpubs.
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The literature part of the work reviews overall Fischer-Tropsch process, Fischer-Tropsch reactors and catalysts. Fundamentals of Fischer-Tropsch modeling are also presented. The emphasis is on the reactor unit. Comparison of the reactors and the catalysts is carried out to choose the suitable reactor setup for the modeling work. The effects of the operation conditions are also investigated. Slurry bubble column reactor model operating with cobalt catalyst is developed by taking into account the mass transfer of the reacting components (CO and H2) and the consumption of the reactants in the liquid phase. The effect of hydrostatic pressure and the change in total mole flow rate in gas phase are taken into account in calculation of the solubilities. The hydrodynamics, reaction kinetics and product composition are determined according to literature. The cooling system and furthermore the required heat transfer area and number of cooling tubes are also determined. The model is implemented in Matlab software. Commercial scale reactor setup is modeled and the behavior of the model is investigated. The possible inaccuraries are evaluated and the suggestions for the future work are presented. The model is also integrated to Aspen Plus process simulation software, which enables the usage of the model in more extensive Fischer-Tropsch process simulations. Commercial scale reactor of diameter of 7 m and height of 30 m was modeled. The capacity of the reactor was calculated to be about 9 800 barrels/day with CO conversion of 75 %. The behavior of the model was realistic and results were in the right range. The highest uncertainty to model was estimated to be caused by the determination of the kinetic rate.
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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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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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In the Russian Wholesale Market, electricity and capacity are traded separately. Capacity is a special good, the sale of which obliges suppliers to keep their generating equipment ready to produce the quantity of electricity indicated by the System Operator. The purpose of the formation of capacity trading was the maintenance of reliable and uninterrupted delivery of electricity in the wholesale market. The price of capacity reflects constant investments in construction, modernization and maintenance of power plants. So, the capacity sale creates favorable conditions to attract investments in the energy sector because it guarantees the investor that his investments will be returned.
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The goal of this thesis was to make a dimensioning tool to determine the plastic capacity of the boiler supporting header. The capacity of the header is traditionally determined by using FE-method during the project phase. By using the dimensioning tool the goal is to ensure the capacity already in the proposal phase. The study began by analyzing the headers of the ongoing projects by using FE-method. For the analytical solution a plain header was analyzed without the effects of branches or lug. The calibration of parameters in the analytical solution was made using these results. In the analytical solution the plastic capacity of the plastic hinges in the header was defined. The stresses caused by the internal pressure as well as the normal and shear forces caused by the external loading reduced the plastic moment. The final capacity was determined by using the principle of virtual work. The weakening effect of the branches was taken into account by using pressure areas. Also the capacity of the punching shear was defined. The results from the FE-analyses and the analytical solution correlate with each other. The results from the analytical solution are conservative but give correct enough results when considering the accuracy of the used method.
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When using appropriate inflation pressures and load capacity (ballast), it may obtain a higher yield and prolongation of the life of the tire, besides it may minimize the problems of loss of traction, increased slippage and fuel consumption. This study aimed to evaluate the fuel consumption of a tractor operating with new and worn tires in three conditions of ballasting and three inflation pressures, when driving on compacted soil with vegetation cover. The experiment was conducted at the experimental unit from the Department of Animal Science, Federal University of Lavras, state of Minas Gerais, Brazil, in an agricultural soil compacted by cattle trampling and with vegetation cover. It was used a tractor 4x2 with front wheel assist, of a 65.62 kW engine power. The tires were of R1 type, diagonal (front: 12.4 to 24; and rear: 18.4 to 30), the average height of the clutches of the new tires were 0.3 and 0.35 m for front and rear tires, respectively, and for the worn tires were 0.018 and 0.0045 m, for the front and the rear tires, respectively. The results showed advantages for the tractor equipped with new tires.
Resumo:
The tire inflation pressure, among other factors, determines the efficiency in which a tractor can exert traction. It was studied the effect of using two tire inflation pressures, 110.4 kPa in the front and rear wheels, 124.2 kPa in the front wheel and 138 kPa in the rear wheels, the energetic efficiency of an agricultural tractor of 147 kW of engine power, in the displacement speed of 6.0 km.h-1, on track with firm surface, with the tractor engine speed of 2000 rpm. For each condition of the tire pressure, the tested tractor was subjected to constant forces in the drawbar of 45 kN and 50 kN, covering 30 meters. It was used a randomized complete block with a 2x2 factorial arrangement (tire pressure and drawbar power) with four replications, totaling 16 experimental units. Data were subjected to analysis of variance, using the Tukey test at 5% probability for comparison averages. The lowest hourly and specific fuel consumption, the lowest slippage of the wheelsets and the highest efficiency in the drawbar was obtained with the tire inflation pressure of 110.4 kPa in the front and rear tires of the tractor, highlighting that lower pressures improve energetic and operational performance of the tractor.
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ABSTRACT The objective of this study was to evaluate the thermoregulatory response of dairy buffaloes in pre-milking and post-milking. To identify animal thermoregulatory capacity, skin surface temperatures were taken by an infrared thermometer (SST), a thermographic camera (MTBP) as well as respiratory rate records (RR). Black Globe and Humidity Index (BGHI), radiating thermal load (RTL) and enthalpy (H) were used to characterize the thermal environment. Artificial Neural Networks analyzed those indices as well as animal physiological data, using a single layer trained with the least mean square (LMS) algorithm. The results indicated that pre-milking and post-milking environments reached BGHI, RR, SST and MTBP values above thermal neutrality zone for buffaloes. In addition, limits of surface skin temperatures were mostly influenced by changing ambient conditions to the detriment of respiratory rates. It follows that buffaloes are sensitive to environmental changes and their skin temperatures are the best indicators of thermal comfort in relation to respiratory rate.
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ABSTRACT For drip irrigation design and management, it is necessary to know the relation between flow and pressure acting on emitters. In the case of subsurface drip irrigation, the backpressure phenomenon may change the hydraulic characteristics of emitters. Thus, this study aimed at determining such relationship between flow and pressure of different driplines in surface and subsurface conditions; aiming to find possible differences in hydraulic behavior. We tested four emitter types; two pressure compensating (D5000 and Hydro PCND) and two non-pressure compensating (TalDrip and Jardiline). Emitter flow rates were attained in atmospheric conditions and submerged in water, in which submergence levels represented backpressure. Assays were performed using inlet pressures of 80, 100, 120, and 150 kPa for the Hydro PCND dripline and 25, 50, 100, and 150 kPa for the other ones; the backpressures were of 0.49, 1.47, 2.45, 4.41 and 6.37 kPa with four replications. The emitters had their proportionality constants and discharge exponents changed in submerged applications, representing backpressure effect. Non-pressure compensating emitters had their discharge exponent decreased, while in pressure compensating ones, it was increased. Backpressure reduced emitter flow rates at all evaluated pressures.
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Today the limitedness of fossil fuel resources is clearly realized. For this reason there is a strong focus throughout the world on shifting from fossil fuel based energy system to biofuel based energy system. In this respect Finland with its proven excellent forestry capabilities has a great potential to accomplish this goal. It is regarded that one of the most efficient ways of wood biomass utilization is to use it as a feedstock for fast pyrolysis process. By means of this process solid biomass is converted into liquid fuel called bio-oil which can be burnt at power plants, used for hydrogen generation through a catalytic steam reforming process and as a source of valuable chemical compounds. Nowadays different configurations of this process have found their applications in several pilot plants worldwide. However the circulating fluidized bed configuration is regarded as the one with the highest potential to be commercialized. In the current Master’s Thesis a feasibility study of circulating fluidized bed fast pyrolysis process utilizing Scots pine logs as a raw material was conducted. The production capacity of the process is 100 000 tonne/year of bio-oil. The feasibility study is divided into two phases: a process design phase and economic feasibility analysis phase. The process design phase consists of mass and heat balance calculations, equipment sizing, estimation of pressure drops in the pipelines and development of plant layout. This phase resulted in creation of process flow diagrams, equipment list and Microsoft Excel spreadsheet that calculates the process mass and heat balances depending on the bio-oil production capacity which can be set by a user. These documents are presented in the current report as appendices. In the economic feasibility analysis phase there were at first calculated investment and operating costs of the process. Then using these costs there was calculated the price of bio-oil which is required to reach the values of internal rate of return of 5%, 10%, 20%, 30%, 40%, and 50%.