995 resultados para Flue gas equipment


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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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Kaasutuksen kannattavuus ja toteutustapa on ollut tarkea ja useiden tutkimuksien kohde. Biomassan kaasutuksen ja siina kaytettavien laitteiden nykytila on epavarma. Niinpa lisatutkimukselle ja tarkasteluille on edelleen tarvetta. Tama tyo keskittyy nykyisin kaytettavien kaasutusprosessien ja laitteiden tarkasteluun. Tyossa kaydaan lapi useita uusimpia kaasutusprojekteja ja esitetaan niista tutkimustarpeita. Lisaksi kaasutusprosessissa pitaa saada hallintaan niille tyypillisia ongelmia kuten kaasun puhdistus, kaasun kasittely, biomassan kasittely ja kaasuttimen muuraus, joista esitetaan lisatietoa. Edelleen esitetaan kaasutusprosessien taydellinen luokittelu. On huomattava etta biomassan kaasutusta tarvitaan jotta saadaan toteutettua EUn hahmotteleman ja saataman energiapolitiikan vaatima kasvu ja kehitys.

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The present review summarizes the most relevant results of our research group obtained recently in the field of unimolecular reaction dynamics. The following processes are specifically analyzed: the isomerization, dissociation and elimination in methyl nitrite, the fragmentation reactions of the mercaptomethyl cation, the C-CO dissociation in the acetyl and propionyl radicals, and the decomposition of vinyl fluoride. In all the cases, only state- or energy-selected systems are considered. Special emphasis is paid to the possibility of systems exhibiting non-statistical behavior.

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One of the primary goals for food packages is to protect food against harmful environment, especially oxygen and moisture. The gas transmission rate is the total gas transport through the package, both by permeation through the package material and by leakage through pinholes and cracks. The shelf life of a product can be extended, if the food is stored in a gas tight package. Thus there is a need to test gas tightness of packages. There are several tightness testing methods, and they can be broadly divided into destructive and nondestructive methods. One of the most sensitive methods to detect leaks is by using a non destructive tracer gas technique. Carbon dioxide, helium and hydrogen are the most commonly used tracer gases. Hydrogen is the lightest and the smallest of all gases, which allows it to escape rapidly from the leak areas. The low background concentration of H2 in air (0.5 ppm) enables sensitive leak detection. With a hydrogen leak detector it is also possible to locate leaks. That is not possible with many other tightness testing methods. The experimental work has been focused on investigating the factors which affect the measurement results with the H2leak detector. Also reasons for false results were searched to avoid them in upcoming measurements. From the results of these experiments, the appropriate measurement practice was created in order to have correct and repeatable results. The most important thing for good measurement results is to keep the probe of the detector tightly against the leak. Because of its high diffusion rate, the HZ concentration decreases quickly if holding the probe further away from the leak area and thus the measured H2 leaks would be incorrect and small leaks could be undetected. In the experimental part hydrogen, oxygen and water vapour transmissions through laser beam reference holes (diameters 1 100 μm) were also measured and compared. With the H2 leak detector it was possible to detect even a leakage through 1 μm (diameter) within a few seconds. Water vapour did not penetrate even the largest reference hole (100 μm), even at tropical conditions (38 °C, 90 % RH), whereas some O2 transmission occurred through the reference holes larger than 5 μm. Thus water vapour transmission does not have a significant effect on food deterioration, if the diameter of the leak is less than 100 μm, but small leaks (5 100 μm) are more harmful for the food products, which are sensitive to oxidation.

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The gas-phase ion-molecule reactions of the Me3SiN(H)SiMe2+ ion, obtained by electron ionization from Me3SiN(H)SiMe3, have been studied in a Fourier transform ion cyclotron resonance spectrometer in order to understand the mechanistic details of an important chemical system presently used in film formation. This silyl cation has been observed to undergo addition reactions at electron rich centers to form stable adducts that may undergo further methane elimination in the case of alcohols and amines. The most important feature of these reactions is the fact that a metathesis type reaction can be observed in the presence of H2O, and other hydrogen labile substrates like alcohols, leading to the formation of the corresponding oxygen-containing ion, i.e. Me3SiOSiMe2+. For alcohols (ROH), facile formation of a tertiary product ion, presumably corresponding to an Me3Si-O-Si(Me)=O+-R structure with elimination of an amine reveals the strong tendency of these nitrogen-containing ions to undergo metathesis type reactions with oxygen containing substrates.

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Background and purpose: In planning to meet evidence based needs for radiotherapy, guidelines for the provision of capital and human resources are central if access, quality and safety are not to be compromised. A component of the ESTRO-HERO (Health Economics in Radiation Oncology) project is to document the current availability and content of guidelines for radiotherapy in Europe. Materials and methods: An 84 part questionnaire was distributed to the European countries through their national scientific and professional radiotherapy societies with 30 items relating to the availability of guidelines for equipment and staffing and selected operational issues. Twenty-nine countries provided full or partial evaluable responses. Results: The availability of guidelines across Europe is far from uniform. The metrics used for capital and human resources are variable. There seem to have been no major changes in the availability or specifics of guidelines over the ten-year period since the QUARTS study with the exception of the recent expansion of RTT staffing models. Where comparison is possible it appears that staffing for radiation oncologists, medical physicists and particularly RTTs tend to exceed guidelines suggesting developments in clinical radiotherapy are moving faster than guideline updating. Conclusion: The efficient provision of safe, high quality radiotherapy services would benefit from the availability of well-structured guidelines for capital and human resources, based on agreed upon metrics, which could be linked to detailed estimates of need

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Background: Documenting the distribution of radiotherapy departments and the availability of radiotherapy equipment in the European countries is an important part of HERO the ESTRO Health Economics in Radiation Oncology project. HERO has the overall aim to develop a knowledge base of the provision of radiotherapy in Europe and build a model for health economic evaluation of radiation treatments at the European level. The aim of the current report is to describe the distribution of radiotherapy equipment in European countries. Methods: An 84-item questionnaire was sent out to European countries, principally through their national societies. The current report includes a detailed analysis of radiotherapy departments and equipment (questionnaire items 2629), analyzed in relation to the annual number of treatment courses and the socio-economic status of the countries. The analysis is based on validated responses from 28 of the 40 European countries defined by the European Cancer Observatory (ECO). Results: A large variation between countries was found for most parameters studied. There were 2192 linear accelerators, 96 dedicated stereotactic machines, and 77 cobalt machines reported in the 27 countries where this information was available. A total of 12 countries had at least one cobalt machine in use. There was a median of 0.5 simulator per MV unit (range 0.31.5) and 1.4 (range 0.44.4) simulators per department. Of the 874 simulators, a total of 654 (75%) were capable of 3D imaging (CT-scanner or CBCToption). The number of MV machines (cobalt, linear accelerators, and dedicated stereotactic machines) per million inhabitants ranged from 1.4 to 9.5 (median 5.3) and the average number of MV machines per department from 0.9 to 8.2 (median 2.6). The average number of treatment courses per year per MV machine varied from 262 to 1061 (median 419). While 69% of MV units were capable of IMRT only 49% were equipped for image guidance (IGRT). There was a clear relation between socio-economic status, as measured by GNI per capita, and availability of radiotherapy equipment in the countries. In many low income countries in Southern and Central-Eastern Europe there was very limited access to radiotherapy and especially to equipment for IMRT or IGRT. Conclusions: The European average number of MV machines per million inhabitants and per department is now better in line with QUARTS recommendations from 2005, but the survey also showed a significant heterogeneity in the access to modern radiotherapy equipment in Europe. High income countries especially in Northern-Western Europe are well-served with radiotherapy resources, other countries are facing important shortages of both equipment in general and especially machines capable of delivering high precision conformal treatments (IMRT, IGRT)

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Neste Oil has introduced plant oils and animal fats for the production of NExBTL renewable diesel, and these raw materials differ from the conventional mineral based oils. One subject of new raw materials study is thermal degradation, or in another name pyrolysis, of these organic oils and fats. The aim of this master’s thesis is to increase knowledge on thermal degradation of these new raw materials, and to identify possible gaseous harmful thermal degradation compounds. Another aim is to de-termine the health and environmental hazards of identified compounds. One objective is also to examine the formation possibilities of hazardous compounds in the produc-tion of NExBTL-diesel. Plant oils and animal fats consist mostly of triglycerides. Pyrolysis of triglycerides is a complex phenomenon, and many degradation products can be formed. Based on the literature studies, 13 hazardous degradation products were identified, one of which was acrolein. This compound is very toxic and dangerous to the environment. Own pyrolysis experiments were carried out with rapeseed and palm oils, and with a mix-ture of palm oil and animal fat. At least 12 hazardous compounds, including acrolein, were analysed from the gas phase. According to the experiments, the factors which influence on acrolein formation are the time of the experiment, the sphere (air/hydrogen) in which the experiment is carried out, and the characteristics of the used oil. The production of NExBTL-diesel is not based on pyrolysis. This is why thermal degradation is possible only when abnormal process conditions prevail.

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Power transformer is the most expensive equipment on a substation. It is always necessary to get needed benefit with the lowest expenses. Producing of power transformers with reduced insulation strength is one of the possible ways to reduce expenses. Exploitation of such transformers was begun in the end of 70-th in the last century. Protection from overvoltages was done with valve-type magnetic combined surge arresters with increased blanking voltage during switching overvoltages. Nowadays there is the necessity of replacement of those devices. That’s why modernized nonlinear surge arrester was invented. This master’s thesis is focused on the use research of that modernized device in comparison with usual nonlinear surge arresters. The goal is to show the lightning overvoltages level using different types of nonlinear surge arresters and then calculations of the lightning protection reliability.

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Hajupäästöillä tarkoitetaan tavallisesti teollisen toiminnan aiheuttamia hajuaineiden päästöjä ympäristöön. Suomessa ympäristölainsäädäntö ei varsinaisesti kiellä hajuaineiden päästöjä mutta edellyttää kuitenkin, ettei niistä aiheudu merkittävää viihtyvyyshaittaa. Tässä työssä tutkittiin hajupäästöjä Saint-Gobain Rakennustuotteet Oy:n Hyvinkään lasivillatehtaalla. Tavoitteena työssä oli selvittää, mikä on tehtaan aiheuttamien päästöjen hajuvaikutus, ja mitä hajuyhdisteitä valmistusprosessissa muodostuu. Lisäksi työssä selvitettiin miten hajupäästöjä pystyttäisiin vähentämään. Työn kokeellisten tutkimusten aikana kerättiin tietoa hajun esiintymisestä valitulta tarkasteluajanjaksolta sekä mitattiin mm. tehtaan savukaasujen hajupitoisuutta ja koostumusta. Mittauksissa kaasunäytteiden hajupitoisuudeksi saatiin 170 HY/m3, joka kuvaa suhteellisen mietoa hajua. Näytteistä analysoidut haihtuvat orgaaniset yhdisteet olivat suurelta osin peräisin lasivillan valmistuksessa käytetystä sideaineesta, jota lisätään tuotteen joukkoon kuidutusvaiheessa. Ympäristöstä otetuista näytteistä ei kuitenkaan havaittu piipun yhdisteitä, mikä viittaisi siihen, että mittausjaksonaikana tehtaan päästöjen leviäminen ympäristöön on tapahtunut melko pieninä pitoisuuksina. Lisäksi on mahdollista, että ulkoilmassa yhdisteissä tapahtuu kemiallista muutuntaa ja hajontaa, jonka seurauksena yhdisteet muuttuvat. Tehtaan hajuhaitat vaikuttaisivat tutkimustulosten mukaan johtuvan savupainumaksi kutsutusta ilmiöstä. Savupainumaan vaikuttavat kaasun lämpömäärä sekä ympäristön olosuhteet ja topografia. Hajuhaittojen poistamiseksi olisi muodostuvia hajuyhdisteitä pystyttävä vähentämään 95-100 %.

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Tämä diplomityö tutkii korroosionestoa polymeerin ekstruusiolinjalla. Kirjallisuusosassa käsitellään ekstruusiolinjaa, linjalla valmistettavia tuotteita ja niiden jatkojalostusta. Lisäksi kirjallisuusosassa käydään läpi linjalla ilmeneviä korroosiotyyppejä, korroosiota eri prosessilaitteissa, korroosionestossa käytettäviä inhibiittoreita ja eri materiaalien korroosiokestävyyden kartoitusta. Kokeellisessa osassa tutkittiin perushartsin kuivauksen vaikutusta ekstruuderin kaasutilan metanoli-, happi- ja kosteuspitoisuuksiin. Kokeellisessa osassa tutkittiin myös korroosioinhibiittorien I1 ja I2 vaikutusta korroosionestoon, seuraamalla korrodoivalla alueella olleiden ruuvielementtien painohäviöitä. Kaapelitestauksessa selvitettiin inhibiittorien käytön vaikutukset matalajännitekaapelin laatuun. Kuivauksella ei todettu olevan vaikutusta korroosionestoon. Metanolipitoisuus pysyi korkeana ja happipitoisuuden aleneminen ei ollut merkittävää. Kosteuspitoisuuden suuruusluokka selvitettiin. Kuivauksesta huolimatta se pysyi korkeana. Inhibiittorien käytöstä huolimatta ruuvielementit korrodoituivat, mutta inhibiittoria I2 käytettäessä tutkittujen ruuvielementtien painohäviöt olivat pienempiä referenssiajoon verrattuna. Inhibiittori I2:lla ei todettu olevan negatiivisia vaikutuksia matalajännitekaapelin laatuun suoritetuissa ikääntymis- sähköominaisuus- ja ristisilloittumisnopeustesteissä.

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The objective of this paper was to show the potential additional insight that result from adding greenhouse gas (GHG) emissions to plant performance evaluation criteria, such as effluent quality (EQI) and operational cost (OCI) indices, when evaluating (plant-wide) control/operational strategies in wastewater treatment plants (WWTPs). The proposed GHG evaluation is based on a set of comprehensive dynamic models that estimate the most significant potential on-site and off-site sources of CO2, CH4 and N2O. The study calculates and discusses the changes in EQI, OCI and the emission of GHGs as a consequence of varying the following four process variables: (i) the set point of aeration control in the activated sludge section; (ii) the removal efficiency of total suspended solids (TSS) in the primary clarifier; (iii) the temperature in the anaerobic digester; and (iv) the control of the flow of anaerobic digester supernatants coming from sludge treatment. Based upon the assumptions built into the model structures, simulation results highlight the potential undesirable effects of increased GHG production when carrying out local energy optimization of the aeration system in the activated sludge section and energy recovery from the AD. Although off-site CO2 emissions may decrease, the effect is counterbalanced by increased N2O emissions, especially since N2O has a 300-fold stronger greenhouse effect than CO2. The reported results emphasize the importance and usefulness of using multiple evaluation criteria to compare and evaluate (plant-wide) control strategies in a WWTP for more informed operational decision making

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Chemical-looping combustion (CLC) is a novel combustion technology with inherent separation of the greenhouse gas CO2. The technique typically employs a dual fluidized bed system where a metal oxide is used as a solid oxygen carrier that transfers the oxygen from combustion air to the fuel. The oxygen carrier is looping between the air reactor, where it is oxidized by the air, and the fuel reactor, where it is reduced by the fuel. Hence, air is not mixed with the fuel, and outgoing CO2 does not become diluted by the nitrogen, which gives a possibility to collect the CO2 from the flue gases after the water vapor is condensed. CLC is being proposed as a promising and energy efficient carbon capture technology, since it can achieve both an increase in power station efficiency simultaneously with low energy penalty from the carbon capture. The outcome of a comprehensive literature study concerning the current status of CLC development is presented in this thesis. Also, a steady state model of the CLC process, based on the conservation equations of mass and energy, was developed. The model was used to determine the process conditions and to calculate the reactor dimensions of a 100 MWth CLC system with bunsenite (NiO) as oxygen carrier and methane (CH4) as fuel. This study has been made in Oxygen Carriers and Their Industrial Applications research project (2008 – 2011), funded by the Tekes – Functional Material program. I would like to acknowledge Tekes and participating companies for funding and all project partners for good and comfortable cooperation.

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The thesis examines System Integration and original equipment manufacturer (OEM) channel in the St. Petersburg drives market. The aim of the study was to increase understanding the relationship between OEM and SI and producers, problems and ongoing trends. The collected data was analyzed in order to find out which features of a power electronic drive product exercise a significant influence for the Russian companies decision. An essential part of this study was interviews as primary information sources, organized with SI and OEM companies which represented the basic SPb industry segments. The wholesalers and end users are left out from the analysis. The collected data was analyzed in order to find out which features of a power electronic drive product exercise a significant influence for the Russian companies decision.

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The quenching of the photoluminescence of Si nanopowder grown by plasma-enhanced chemical vapor deposition due to pressure was measured for various gases ( H2, O2, N2, He, Ne, Ar, and Kr) and at different temperatures. The characteristic pressure, P0, of the general dependence I(P)=I0exp(-P/P0) is gas and temperature dependent. However, when the number of gas collisions is taken as the variable instead of pressure, then the quenching is the same within a gas family (mono- or diatomic) and it is temperature independent. So it is concluded that the effect depends on the number of gas collisions irrespective of the nature of the gas or its temperature