989 resultados para once-through boiler


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In this study, a model for the unsteady dynamic behaviour of a once-through counter flow boiler that uses an organic working fluid is presented. The boiler is a compact waste-heat boiler without a furnace and it has a preheater, a vaporiser and a superheater. The relative lengths of the boiler parts vary with the operating conditions since they are all parts of a single tube. The present research is a part of a study on the unsteady dynamics of an organic Rankine cycle power plant and it will be a part of a dynamic process model. The boiler model is presented using a selected example case that uses toluene as the process fluid and flue gas from natural gas combustion as the heat source. The dynamic behaviour of the boiler means transition from the steady initial state towards another steady state that corresponds to the changed process conditions. The solution method chosen was to find such a pressure of the process fluid that the mass of the process fluid in the boiler equals the mass calculated using the mass flows into and out of the boiler during a time step, using the finite difference method. A special method of fast calculation of the thermal properties has been used, because most of the calculation time is spent in calculating the fluid properties. The boiler was divided into elements. The values of the thermodynamic properties and mass flows were calculated in the nodes that connect the elements. Dynamic behaviour was limited to the process fluid and tube wall, and the heat source was regarded as to be steady. The elements that connect the preheater to thevaporiser and the vaporiser to the superheater were treated in a special way that takes into account a flexible change from one part to the other. The model consists of the calculation of the steady state initial distribution of the variables in the nodes, and the calculation of these nodal values in a dynamic state. The initial state of the boiler was received from a steady process model that isnot a part of the boiler model. The known boundary values that may vary during the dynamic calculation were the inlet temperature and mass flow rates of both the heat source and the process fluid. A brief examination of the oscillation around a steady state, the so-called Ledinegg instability, was done. This examination showed that the pressure drop in the boiler is a third degree polynomial of the mass flow rate, and the stability criterion is a second degree polynomial of the enthalpy change in the preheater. The numerical examination showed that oscillations did not exist in the example case. The dynamic boiler model was analysed for linear and step changes of the entering fluid temperatures and flow rates.The problem for verifying the correctness of the achieved results was that there was no possibility o compare them with measurements. This is why the only way was to determine whether the obtained results were intuitively reasonable and the results changed logically when the boundary conditions were changed. The numerical stability was checked in a test run in which there was no change in input values. The differences compared with the initial values were so small that the effects of numerical oscillations were negligible. The heat source side tests showed that the model gives results that are logical in the directions of the changes, and the order of magnitude of the timescale of changes is also as expected. The results of the tests on the process fluid side showed that the model gives reasonable results both on the temperature changes that cause small alterations in the process state and on mass flow rate changes causing very great alterations. The test runs showed that the dynamic model has no problems in calculating cases in which temperature of the entering heat source suddenly goes below that of the tube wall or the process fluid.

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"Contract AT(30-1)-2789."

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Tässä työssäon tarkasteltu yleisesti höyrykattiloiden säilöntää. Erilaisten säilöntämenetelmien perustietojen lisäksi työssä on pyritty selvittämään eri kattilatyypeille ominaiset säilöntätavat. Märkäsäilönnän jälkeistä käyttöönottoa on pohdittu selvittämällä laskennallisesti, onko tarpeen vaihtaa kattilaan vahvasti kemikaloidun säilöntäliuoksen tilalle puhtaampaa syöttövettä. Esimerkkinä on käytetty Voikkaan paperitehtaan höyryvoimalaitoksen kattila K13:ta. Työtä tehdessä on käytetty apuna aihetta käsittelevää kirjallisuutta, jota on saatu höyrykattiloita säilöviltä voimalaitoksilta, kemikaalitoimittajilta sekä asiantuntijoiden tekemistä luentomonisteista. Lieriökattiloiden höyrypuoli säilötään lähes poikkeuksetta märkänä, sillä se on vaikea tyhjentää täysin kosteudesta. Läpivirtauskattilalaitoksella käytetään usein sekä kuiva- että märkäsäilöntää. Savukaasupuolen korroosio ehkäistään useinmiten pitämällä kattila niin lämpimänä, että kastepistealituksia ei tapahdu.

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In the last years, the European countries have paid increasing attention to renewable sources and greenhouse emissions. The Council of the European Union and the European Parliament have established ambitious targets for the next years. In this scenario, biomass plays a prominent role since its life cycle produces a zero net carbon dioxide emission. Additionally, biomass can ensure plant operation continuity thanks to its availability and storage ability. Several conventional systems running on biomass are available at the moment. Most of them are performant either in the large-scale or in the small power range. The absence of an efficient system on the small-middle scale inspired this thesis project. The object is an innovative plant based on a wet indirectly fired gas turbine (WIFGT) integrated with an organic Rankine cycle (ORC) unit for combined heat and power production. The WIFGT is a performant system in the small-middle power range; the ORC cycle is capable of giving value to low-temperature heat sources. Their integration is investigated in this thesis with the aim of carrying out a preliminary design of the components. The targeted plant output is around 200 kW in order not to need a wide cultivation area and to avoid biomass shipping. Existing in-house simulation tools are used: They are adapted to this purpose. Firstly the WIFGT + ORC model is built; Zero-dimensional models of heat exchangers, compressor, turbines, furnace, dryer and pump are used. Different fluids are selected but toluene and benzene turn out to be the most suitable. In the indirectly fired gas turbine a pressure ratio around 4 leads to the highest efficiency. From the thermodynamic analysis the system shows an electric efficiency of 38%, outdoing other conventional plants in the same power range. The combined plant is designed to recover thermal energy: Water is used as coolant in the condenser. It is heated from 60°C up to 90°C, ensuring the possibility of space heating. Mono-dimensional models are used to design the heat exchange equipment. Different types of heat exchangers are chosen depending on the working temperature. A finned-plate heat exchanger is selected for the WIFGT heat transfer equipment due to the high temperature, oxidizing and corrosive environment. A once-through boiler with finned tubes is chosen to vaporize the organic fluid in the ORC. A plate heat exchanger is chosen for the condenser and recuperator. A quasi-monodimensional model for single-stage axial turbine is implemented to design both the WIFGT and the ORC turbine. The system simulation after the components design shows an electric efficiency around 34% with a decrease by 10% compared to the zero-dimensional analysis. The work exhibits the system potentiality compared to the existing plants from both technical and economic point of view.

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From the boiler design point of view, it is imperative to know and understand the operation of the boiler. Since comprehensive measurement of a large furnace is impossible, the furnace can be modeled in order to study its behavior and phenomena. This requires the used model to be validated to correspond with the physical furnace behavior. In this thesis, a three dimensional furnace model is validated to match a bituminous coal utilizing, supercritical once-through circulating fluidized bed combustor based on measurement data. The validated model is used for analyzing the furnace heat transfer. Other heat transfer analysis methods are energy balance method based on tube surface temperature measurements and a method based on measured temperature difference between the tube crest and the fin. The latter method was developed in the thesis using Fluent-software. In the theory part, literature is reviewed and the fundamental aspects of circulating fluidized bed are discussed. These aspects are solid particle behavior in fluidization known as hydrodynamics, behavior of fuel and combustion and heat transfer. Fundamental aspects of modeling are also presented.

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The outflow-concentration-time profiles for lignocaine (lidocaine) and its metabolites have been measured after bolus impulse administration of [C-14]lignocaine into the perfused rat liver. Livers from female Sprague-Dawley rats were perfused in a once-through fashion with red-blood-cell-free Krebs-Henseleit buffer containing 0 or 2% bovine serum albumin. Perfusate flow rates of 20 and 30 mL min(-1) were used and both normal and retrograde flow directions were employed. Significant amounts of metabolite were detected in the effluent perfusate soon after lignocaine injection. The early appearance of metabolite contributed to bimodal outflow profiles observed for total C-14 radioactivity. The lignocaine outflow profiles were well characterized by the two-compartment dispersion model, with efflux rate << influx rate. The profiles for lignocaine metabolites were also characterized in terms of a simplified two-compartment dispersion model. Lignocaine was found to be extensively metabolized under the experimental conditions with the hepatic availability ranging between 0.09 and 0.18. Generally lignocaine and metabolite availability showed no significant change with alterations in perfusate flow rate from 20 to 30 mt min(-1) or protein content from 0 to 2%. A significant increase in lignocaine availability occurred when 1200 mu M unlabelled lignocaine was added to the perfusate. Solute mean transit times generally decreased with increasing flow rate and with increasing perfusate protein content. The results confirm that lignocaine pharmacokinetics in the liver closely follow the predictions of the well-stirred model. The increase in lignocaine availability when 1200 mu M unlabelled lignocaine was added to the perfusate is consistent with saturation of the hydroxylation metabolic pathways of lignocaine metabolism.

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Demand for power is growing every day, mainly due to emerging economies in countries such as China, Russia, India, and Brazil. During the last 50 years steam pressure and temperature in power plants have been continuously raised to improve thermal efficiency. Recent efforts to improve efficiency leads to the development of a new generation of heat recovery steam generator, where the Benson once-through technology is applied to improve the thermal efficiency. The main purpose of this paper is to analyze the mechanical behavior of a high pressure superheater manifold by applying finite element modeling and a finite element analysis with the objective of analyzing stress propagation, leading to the study of damage mechanism, e.g., uniaxial fatigue, uniaxial creep for life prediction. The objective of this paper is also to analyze the mechanical properties of the new high temperature resistant materials in the market such as 2Cr Bainitic steels (T/P23 and T/P24) and also the 9-12Cr Martensitic steels (T/P91, T/P92, E911, and P/T122). For this study the design rules for construction of power boilers to define the geometry of the HPSH manifold were applied.

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Tämä diplomityö on osa projektia, joka tähtää ylikriittisellä painealueella toimivan läpivirtaustekniikkaan perustuvan kiertoleijukattilan toteuttamiseen. Diplomityössä määritetään mittausten perusteella vaaka- ja pystysuuntaisia lämmönsiirtoprofiileja kaupallisen kiertoleijukattilan tulipesässä. Lisäksi samaisen kattilan tulipesä mallinnetaan ja mallin parametrejä säädetään niin, että mallin tulokset saadaan vastaamaan mitattuja tuloksia mahdollisimman hyvin. Työn tavoitteena on antaa lisätietoa tulipesässä vapautuvan lämpötehon jakautumisesta tulipesän eri osien kesken. Diplomityön kirjallisuuskatsauksessa käsitellään kiertoleijukattilan tulipesän perusilmiöitä kuten leijutusta, lämmönsiirtoa, hydrodynamiikkaa ja palamista sekä tutustutaan muutamiin tulipesämalleihin. Lisäksi tarkastellaan ylikriittisen läpivirtauskattilan tarjoamia etuja perinteisiin kattilaratkaisuihin nähden. Diplomityössä on myös esitelty työhön liittyvä mittausprojekti.

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The results shown in this thesis are based on selected publications of the 2000s decade. The work was carried out in several national and EC funded public research projects and in close cooperation with industrial partners. The main objective of the thesis was to study and quantify the most important phenomena of circulating fluidized bed combustors by developing and applying proper experimental and modelling methods using laboratory scale equipments. An understanding of the phenomena plays an essential role in the development of combustion and emission performance, and the availability and controls of CFB boilers. Experimental procedures to study fuel combustion behaviour under CFB conditions are presented in the thesis. Steady state and dynamic measurements under well controlled conditions were carried out to produce the data needed for the development of high efficiency, utility scale CFB technology. The importance of combustion control and furnace dynamics is emphasized when CFB boilers are scaled up with a once through steam cycle. Qualitative information on fuel combustion characteristics was obtained directly by comparing flue gas oxygen responses during the impulse change experiments with fuel feed. A one-dimensional, time dependent model was developed to analyse the measurement data Emission formation was studied combined with fuel combustion behaviour. Correlations were developed for NO, N2O, CO and char loading, as a function of temperature and oxygen concentration in the bed area. An online method to characterize char loading under CFB conditions was developed and validated with the pilot scale CFB tests. Finally, a new method to control air and fuel feeds in CFB combustion was introduced. The method is based on models and an analysis of the fluctuation of the flue gas oxygen concentration. The effect of high oxygen concentrations on fuel combustion behaviour was also studied to evaluate the potential of CFB boilers to apply oxygenfiring technology to CCS. In future studies, it will be necessary to go through the whole scale up chain from laboratory phenomena devices through pilot scale test rigs to large scale, commercial boilers in order to validate the applicability and scalability of the, results. This thesis shows the chain between the laboratory scale phenomena test rig (bench scale) and the CFB process test rig (pilot). CFB technology has been scaled up successfully from an industrial scale to a utility scale during the last decade. The work shown in the thesis, for its part, has supported the development by producing new detailed information on combustion under CFB conditions.

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Tässä kirjallisuustyössä tutustutaan kolmeen kaupallisissa painevesilaitoksissa käytettyyn höyrystinkonstruktioon: U-putkipystyhöyrystimeen, U-putkivaakahöyrystimeen ja läpivirtaushöyrystimeen. Työssä tutustutaan näiden ratkaisujen erityispiirteisiin ja vertaillaan niitä keskenään.

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Teollisuuden jäähdytysjärjestelmiä tarvitaan prosessien lämpötilan ja paineen hal-litsemiseen. Vesi on käytetyin lämmönsiirtoaine hyvän saatavuutensa, halvan hin-nan ja korkean lämmönsiirtokyvyn ansiosta. Jäähdytysjärjestelmät jaetaan kolmeen päätyyppiin, joita ovat läpivirtausjäähdytys, suljettu ja avoin kiertojäähdytys. Kullakin järjestelmätyypillä on tyypilliset alatyyppinsä. Avoimella kiertojär-jestelmällä on eniten alatyyppejä, joista yleisin on jäähdytystorni. Jäähdytystorneja on kolmea tyyppiä: märkä-, kuiva ja hybriditorni. Kullakin järjestelmätyypillä on ominaiset piirteensä käyttökohteiden, ympäristövaikutusten, ohjattavuuden, investointi- ja käyttökulujen suhteen, joita tässä työssä esitellään. Työssä tutkitaan teollisuuden jäähdytysjärjestelmien esittelyn lisäksi erään ali-painekaasunpoistimen soveltuvuutta suljetun kiertojäähdytysjärjestelmän kaasun-poistoon. Suljettuun kiertojäähdytysjärjestelmään jää ilmaa täyttövaiheessa ja kul-keutuu liuenneena käytettävän jäähdytysveden mukana. Muodostuva ylikylläinen seos synnyttää veden sekaan ilmakuplia, jotka aiheuttavat korroosiota kemiallisesti ja kuluttamalla. Lisäksi kaasukuplat vievät tilavuutta nesteeltä. Tämä pienentää järjestelmän jäähdytystehoa merkittävästi, koska kaasun lämmönsiirtokyky verrat-tuna veden lämmönsiirtokykyyn on pieni. Työssä esitellään myös muita mahdolli-sia suljetun järjestelmän kaasulähteitä ja niiden aiheuttamia ongelmia. Alipainekaasunpoistimen kaasunerotustehokkuutta mitattiin jäähdytysvesinäyttei-den selkeytymisnopeudella ja lämmönsiirtimien tehon paranemisella. Kahden viikon tarkastelujaksolla selkeytymisajat paranivat 36–60 % eri mittauspaikoissa ja lämmönsiirtimien tehot paranivat 6–29 %. Järjestelmään kuitenkin jäi merkittävä määrä kaasua, vaikka laitteen käyttöä jatkettiin tarkastelujakson jälkeen, joten tavoitteisiin ei päästy. Tutkitun alipainekaasunpoistolaitteen ei todettu soveltuvan tehdasympäristöön kestämättömyyden, hankalakäyttöisyyden ja tehottomuuden takia. Tulokset kuitenkin osoittavat, että kaasunerotuksella on merkittävä vaikutus suljetun jäähdytysjärjestelmän toimivuuteen ja saavutettavaan jäähdytystehoon.

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Kaikkein yleisin käytössä oleva ydinpolttoainekierto on nykyisin avoin, jossa käytetty ydinpolttoaine loppusijoitetaan suoraan ilman jälleenkäsittelyä. Nykyisin kehitteillä olevat uuden sukupolven ydinreaktorit ovat kuitenkin pääosin suunniteltu osittain tai kokonaan suljetuille ydinpolttoainekierroille, jossa käytetty polttoaine jälleenkäsitellään ja osa materiaaleista kierrätetään. Tämän työn tavoitteena oli arvioida näitä kehittyneitä ydinpolttoainekiertoja ympäristövaikutusten ja taloudellisuuden suhteen. Työn yleisluonteista vertailua varten valittiin neljä erilaista kehittynyttä polttoainekiertoskenaariota, joita verrattiin avoimeen polttoainekiertoon erilaisten parametrien avulla. Parametreinä käytettiin muun muassa uraanin kulutusta, loppusijoitettavan jätteen määrää, aktiivisuutta ja lämmöntuottoa sekä käytönaikaisten radioaktiivisten päästöjen määrää. Yleislounteisen arvioinnin lisäksi työssä tarkasteltiin polttoainekiertoa myös Suomen näkökulmasta. Nykyistä polttoainekiertoa verrattiin kahteen erilaiseen tulevaisuuden versioon. Kestävän kehityksen osalta kehittyneet polttoainekierrot vähensivät ympäristövaikutusten määrää avoimeen polttoainekiertoon verrattuna. Kehittyneiden polttoainekiertojen kustannukset olivat avoimen polttoainekierron kustannuksia suuremmat. Kokonaiskustannuksissa ero oli kaikilla vertailuskenaarioilla alle 20 %, mutta polttoainekiertokustannuksissa kustannusten kasvu oli välillä 27-45 % riippuen skenaariosta. Suomen tapauksessa tulokset olivat hyvin samankaltaisia. Uraanin kulutus ja loppusijoitettavan jätteen määrä väheni kehittyneempien polttoainekiertojen johdosta. Polttoainekiertokustannukset nousivat noin puolitoistakertaisiksi, mutta vaikutus kokonaiskustannuksiin oli vain noin 10 %. Johtopäätöksenä voidaan todeta, ettäydinpolttoainekierron ympäristövaikutuksia on mahdollista vähentää osittain tai kokonaan suljettujen polttoainekiertojen avulla. Vaikka polttoainekierron kustannukset kasvavat, niiden vaikutus ydinsähkön kokonaiskustannuksiin ei ole niin merkittävä.

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A series of bis-triazinylphenanthroline ligands (BTPhens) was synthesized by modifying the triazine substituents. It was found that varying these substituents altered the solubilities of the ligands in a number of non-polar solvents. Thus C5-BTPhen showed significantly higher solubility in octanol than C1-BTPhen. The high solubility of C5-BTPhen and its complexes was exploited to facilitate the NMR titration experiments. These experiments shown that the dominant species in solution were the 1:2 complexes [Ln(III)(BTPhen)2], even at high Ln concentrations, and that the relative stability of the 2:1 to 1:1 BTPhen-Ln complexes varied with different lanthanides. C5-BTPhen therefore shows considerable promise for a once-through selective actinide separation process.

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The study of the motivation to practice physical activities is relevant once through this it is possible to develop intervention strategies for sedentary population. In this way, the present dissertation aimed to adapt and validate for the Brazilian context the Motives for Physical Activity Measure Revised (MPAM-R). It was investigated yet the relation of some socio-demographic variables (age, gender, Body Mass Index - BMI, types of physical activity; way to practice and time of practice) and the participants means in the motives studied. The physical activity (PA) is defined as any bodily movement produced by skeletal muscles resulting in energy expenditure above the basal level. However, in the present study it was considered motivation for two types of PA: the physical exercises and sports. The Self-Determination Theory (SDT) underlay this research, once it has been used in the sportive context, beyond the facto of it was used as theoretical base to the development of MPAM-R. To attain the proposed goals, it was accomplished translations to Portuguese of the original English scale. Next, was carried out the semantic analysis and the judge analysis. For the empirical analysis of items, participated 309 practitioner of PA, classified in physical exercises practitioners and sports practitioners, with ages between 16 and 74 years, distributed equally by sex. They answered the final version in Portuguese of the MPAM-R and socio-demographic questions. The data was collected in Natal/RN, where the researcher approached people in some places where the PA is practiced, following she communicated that their involvement will be spontaneous and their responses will be confidential. The obtained results pointed the confirmation of the existence of five factors in the final version of the instrument, that was composed by 26 items that presented the following statistics indexes: x² (289) = 757.75, p < 0.000, x²/DF = 2.62, with GFI of 0.83, AGFI of 0.80 and RMSEA of 0.07. The reliability (Cronbach Alpha) of the complete instrument was 0.90, and the indexes of each factor were considered satisfactory too: Enjoyment (α = 0.88), Health (α = 0.84), Appearance (α = 0.79), Competence (α = 0.85) and Social (α = 0.75). It was observed that, in general, the main motive presented by the participants to practice PA was Health. It was verified yet, that women and aged had a higher mean in the Health factor; among the exercise practitioners was found a higher mean in the Appearance factor; and a higher mean in the Social factor was found among those that practice PA with accompaniment. It was concluded that the MPAM-R presented satisfactory psychometric parameters, became it useful in futures researches. Moreover, proposed the accomplishment of new studies that considered others variables to the intent of the better understanding of motivation to practice physical activity

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Seven rib-eye rolls, lip on (112A), were each cut into eight 2.54 centimeter thick steaks starting from the blade end. Steaks were randomly assigned to one of four treatment groups; 1) round versus square cores using Instron [inst1], 2) round versus square cores using Warner- Bratzler [inst2], 3) Instron versus Warner-Bratzler using round cores [rdsq1], and 4) Instron versus Warner- Bratzler using square cores [rdsq2]. Subsequently, steaks from each group were broiled in a General Electric industrial broiler grill to an internal temperature of 63 §C. Steaks were held overnight at 2 §C. Two steaks from each rib were placed into each instrument/core treatment group. Steaks were then divided into three sections identified as: a) lateral, b) medial, and c) central. Three 1.27 centimeter cores from each section were taken from each steak for a total of nine cores per steak and sheared once through the center. The results indicated that there was a significant difference ( p> .05) between round and square cores for both Warner- Bratzler and Instron. In all mean groups tested, square cores had higher shear values than did round cores. There was no indication of differences between instruments, and no significant interactions between instruments and core types.