675 resultados para feedwater pumps
Resumo:
Tässä työssä tutkittiin lämpöpumppujärjestelmiä, joilla tuotetaan samaan aikaan kylmä- ja lämpötehoa. Höyryn puristus lämpöpumppu on yleisimmin käytetty lämpöpumpputyyppi ja sen pääkomponentit ovat kompressori, lauhdutin, paisuntaventtiili ja höyrystin. Lämpöpumppu tuottaa samaan aikaan kylmätehoa höyrystimellä ja lämpötehoa lauhduttimella. Lämpöpumpun toiminta-arvoihin vaikuttaa valittujen lämpötilatasojen lisäksi voimakkaasti valitun kiertoaineen termodynaamiset ominaisuudet sekä kompressorin painesuhteeseen verrannollinen isentrooppihyötysuhde. Uusissa lämpöpumpuissa käytetään HFC yhdisteitä sekä sekoituksia kiertoaineina, mutta myös luonnolliset aineet, kuten ammoniakki, ovat lupaavia korvikkeita CFC yhdisteille. Sopivia sovelluskohteita kylmä- ja lämpötehon yhteistuotannolle ovat kauppa- ja asuinrakennukset, hotellit, toimistot, elintarviketeollisuus ja -myymälät sekä vierekkäiset jää- ja uimahallit ja hiihtoputket. Kylmä- ja lämpötehon yhteistuotannolla voitaisiin saavuttaa merkittäviä säästöjä ja päästövähennyksiä. Esimerkiksi jäähallien kylmäkoneiden lauhdelämmön hyödyntämisessä olisi Suomessa potentiaalia 6-10 miljoonan euron vuotuisiin säästöihin. Kylmä- ja lämpötehon yhteistuotanto voidaan toteuttaa hyödyntämällä kylmäkoneen lauhdelämpöä toisella lämpöpumpulla. Toinen vaihtoehto on käyttää eri tilojen samanaikaiseen lämmittämiseen ja jäähdyttämiseen HPS lämpöpumppua tai moniyksikköistä lämpöpumppua.
Resumo:
This Master´s thesis investigates the performance of the Olkiluoto 1 and 2 APROS model in case of fast transients. The thesis includes a general description of the Olkiluoto 1 and 2 nuclear power plants and of the most important safety systems. The theoretical background of the APROS code as well as the scope and the content of the Olkiluoto 1 and 2 APROS model are also described. The event sequences of the anticipated operation transients considered in the thesis are presented in detail as they will form the basis for the analysis of the APROS calculation results. The calculated fast operational transient situations comprise loss-of-load cases and two cases related to a inadvertent closure of one main steam isolation valve. As part of the thesis work, the inaccurate initial data values found in the original 1-D reactor core model were corrected. The input data needed for the creation of a more accurate 3-D core model were defined. The analysis of the APROS calculation results showed that while the main results were in good accordance with the measured plant data, also differences were detected. These differences were found to be caused by deficiencies and uncertainties related to the calculation model. According to the results the reactor core and the feedwater systems cause most of the differences between the calculated and measured values. Based on these findings, it will be possible to develop the APROS model further to make it a reliable and accurate tool for the analysis of the operational transients and possible plant modifications.
Resumo:
The aim of this study is to form the experience-based knowledge of diabetics. The broader intent is to be able to transform this experience-based knowledge as an asset within caring. In this study, a theoretical contact for the empirical data is presented through phronesis, i.e. practical wisdom. Phronesis can be seen as the most suitable form of knowledge to be able to deepen the individual's understanding of experiencebased knowledge. For this research, hermeneutic phenomenology was chosen. Abductive reasoning was the method chosen to approach the data collected through repeated deep interviews with individuals with personal experience of diabetes and the use of insulin pumps. The abductive approach fascilitates a broader interpretation of the primary empirical results via a theory of philosophy of science, such as phronesis, the life-world and the negativity of the experience. The latent message of the empirical data is thereby also additionally highlighted. The synthesis reveals that experience-based knowledge arrives with time, it is personified and praxis-oriented, and before this time, the knowledge and security must be provided by the established care, by people close to the individual or by other external sources. The experience-based knowledge has strenghts and weaknesses. The knowledge is further categorized by the individual's ability to discern and make judgement. Additionally, the experience-based kowledge is a reflecting and action-based knowledge striving to improve the care provided. The experience-based knowledge held by the individual is potentially a great instrument towards improving general knowledge with possible practical applications within the diabetic care. Furthermost, in practical suggestions to fascilitate care. In generally applying knowledge gathered from the individual's experiental point of view, there are inherent risks. These risks could potentially be eliminated through the adoption of a concept where the established care could function as a quality guarantor. A concept taking into account the experiencebased knowledge as a source of information and knowledge in the care for diabetics. Co-created knowledge and understanding is a position found in both self-care and pump-treatment. It is also found through the optimal application of the experience-based knowledge of the individual as well as the knowledge found within the established care, in order to fascilitate well-being. This as expressed by the individual's phronesis-based knowledge.
Resumo:
Tässä työssä on tutkittu prosessihöyryn tuotantokustannusten optimointia Neste Oil Oy:n Naantalin jalostamolla. Työssä on keskitytty ennen kaikkea prosessi-höyryn tuotantoon öljynjalostamolla. Tavoitteena oli luoda yksinkertainen työkalu, jonka avulla voidaan vertailla höyryntuotantokustannuksia jalostamon tuotan-toyksiköissä. Samalla oli tarkoituksena kartoittaa höyryn tuotantomahdollisuudet yksiköissä. Työn tuloksena tehty Excel-pohjainen laskentataulukko on esitelty tässä työssä. Ohjelman tarkkuutta on mahdollista parantaa prosessikoeajojen avul-la. Jo nykyisellä laskentatarkkuudella ohjelma täyttää kuitenkin asetetut tavoitteet eli antaa mahdollisuuden vertailla helposti ja havainnollisesti tuotantokustannuksia yksiköiden välillä. Oman höyryntuotannon lisäksi Naantalin jalostamo ostaa höyryä viereiseltä Fortumin Naantalin voimalaitokselta. Ostohöyryn hinta on las-kettu työkalussa mukaan vertailuun. Työn perusteella ostohöyry on Naantalin ja-lostamon tapauksessa selkeästi omatuotantoa edullisempi vaihtoehto. Ero kustan-nuksissa syntyy käytettävästä polttoaineesta, joka jalostamon tapauksessa on ja-lostamo- eli polttokaasu. Nykyisen tasoisella raakaöljyn hinnalla tilanne säilynee tällaisena tulevaisuudessakin. Jalostamolta löytyi myös kohteita, joissa energiatehokkuutta on mahdollista kehit-tää nykyisen höyryverkon ulkopuolella. Esimerkkeinä tällaisista kohteista tässä työssä on tarkasteltu toisen jätelämpökattilan rakentamista nykyisen toiminnassa olevan rinnalle, sekä höyryturbiinien asentamista paineenalennuslinjoihin. Näistä hankkeista jätelämpökattila osoittautui erittäin suositeltavaksi investoinniksi.
Resumo:
This Master´s thesis illustrates how growing a business ties up the company´s working capital and what the cost of committed capital. In order to manage a company´s working capital in rapid business growth phase, the thesis suggests that by monitoring and managing the operating and cash conversion cycles of customers´ projects, a company can find ways to secure the required amount of capital. The research method of this thesis was based on literature reviews and case study research. The theoretical review presents the concepts of working capital and provides the background for understanding how to improve working capital management. The company in subject is a global small and medium-sized enterprise that manufactures pumps and valves for demanding process conditions. The company is expanding, which creates lots of challenges. This thesis concentrates to the company´s working capital management and its efficiency through the supply chain and value chain perspective. The main elements of working capital management are inventory management, accounts receivable management and accounts payable management. Prepayments also play a significant role, particularly in project-based businesses. Developing companies´ working capital management requires knowledge from different kind of key operations´ in the company, like purchasing, production, sales, logistics and financing. The perspective to develop and describe working capital management is an operational. After literature reviews the thesis present pilot projects that formed the basis of a model to monitor working capital in the case company. Based on analysis and pilot projects, the thesis introduces a rough model for monitoring capital commitments in short time period. With the model the company can more efficiently monitor and manage their customer projects.
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Centrifugal pumps are a notable end-consumer of electrical energy. Typical application of a centrifugal pump is the filling or emptying of a reservoir tank, where the pump is often operated at a constant speed until the process is completed. Installing a frequency converter to control the motor substitutes the traditional fixed-speed pumping system, allows the optimization of rotational speed profile for the pumping tasks and enables the estimation of rotational speed and shaft torque of an induction motor without any additional measurements from the motor shaft. Utilization of variable-speed operation provides the possibility to decrease the overall energy consumption of the pumping task. The static head of the pumping process may change during the pumping task. In such systems, the minimum rotational speed changes during reservoir filling or emptying, and the minimum energy consumption can’t be achieved with a fixed rotational speed. This thesis presents embedded algorithms to automatically identify, optimize and monitor pumping processes between supply and destination reservoirs, and evaluates the changing static head –based optimization method.
Resumo:
Tämä kandidaatintyö käsittelee lämpöpumppuja, niiden toimintaa ja niiden käytön tulevaisuutta. Työ on rajattu asuintalojen lämmittämiseen ja erityisesti käsitellään erillisiä pientaloja. Työn tavoite on esitellä lämpöpumppujen toimintaperiaate ja tekniikka, eri lämpöpumpputyypit ja niiden lämmönlähteet sekä lämpöpumppujen käyttöä rajoittavia tekijöitä. Lisäksi esitellään Suomen lämmitystapojen jakauma sekä pohditaan siihen tulevia muutoksia. Tilastojen pohjalta tehdään lopulta arvioita lämpöpumppujen käytön tulevaisuuden kehityksestä.
Resumo:
The systemic aspect of vascular damage induced by angiotensin II (ANG II) has been poorly explored in the literature. Considering the presence of ANG II and its specific receptor AT1, in several organs, all tissues might be potentially affected by its effects. The aims of this study were: To evaluate the early histological changes in the heart, liver and kidneys, produced by ANG II infusion, to evaluate the protective effect of losartan. Wistar rats were distributed into three groups: control (no treatment), treated with ANG II, and treated with ANG II + losartan. ANG II was continuously infused over 72 hours by subcutaneous osmotic pumps. Histological sections of the myocardium, kidneys and liver were stained and observed for the presence of necrosis. There were ANG II-induced perivascular inflammation and necrosis of the arteriolar wall in the myocardium, kidney, and liver by, which were partially prevented by losartan. There was no significant correlation between heart and kidney damage. Tissue lesion severity was lower than that of vascular lesions, without statistical difference between groups. ANG II causes vascular injury in the heart, kidneys and liver, indicating a systemic vasculotoxic effect; the mechanisms of damage/protection vary depending on the target organ; perivascular lesions may occur even when anti-hypertensive doses of losartan are used.
Resumo:
TVO suunnittelee reaktoritehon 10 %:n korotusta Olkiluoto 1 ja 2 -voimalaitoksille. Reaktoriteho nostetaan 2500 MW:sta 2750 MW:iin polttoaineen rikastusastetta nostamalla ja pääkiertovirtausta kasvattamalla. Samalla syöttövesivirtaus reaktoriin ja tuorehöyryvirtaus turpiineille kasvaa. Lauhteenpuhdistusjärjestelmän kapasiteettia ei voida kuitenkaan kasvattaa, joten massavirran lisäys toteutetaan ottamalla käyttöön korkeapainesivulauhteen eteenpäinpumppaus. Lauhteen esilämmityslinjojen, lauhteenpuhdistuksen ja syöttövesipumppujen massavirta säilyy siten nykyisellään. Muita merkittäviä tehonkorotukseen liittyviä laitosmuutoksia ovat pääkiertopumppujen uusinta ja korkeapaineturpiinin muutokset. Tehonkorotetun prosessin käytettävyyden varmistamiseksi tehdään häiriöanalyysejä Apros-prosessisimulointiohjelmistoa käyttäen. OL1 ja OL2 -laitoksista on olemassa validoitu 2500 MW:n laitosmalli, josta muokatulla 2750 MW:n laitosmallilla simuloinnit tehdään. Häiriöanalyysien avulla selvitetään säätöjärjestelmien kyky pitää prosessin tila hallinnassa ilman suojausautomaation laukeamista. Simuloituihin tapauksiin kuuluu pumppujen ja venttiilien vikaantumistapauksia sekä turpiini- ja reaktoripuolen pikasulku- ja osittaispikasulkutapauksia. Myös meriveden lämpötilan vaikutusta häiriötilanteisiin tarkastellaan. Analyysien perusteella voimalaitosten ohjaus- ja suojausautomaatio toimivat hyvin myös korotetulla teholla. Tehonkorotuksen jälkeiset suuremmat massavirrat aiheuttavat kuitenkin voimakkaampia reaktoripaineen ja -tehon vaihteluita varsinkin venttiilien sulkeutumistapauksissa. Simuloinnit osoittivat, että tehonkorotus 2500 MW:sta 2750 MW:iin on mahdollinen, mutta aiheuttaa pieniä muutoksia laitoksen suojausjärjestelmien laukaisurajoihin.
Resumo:
Suurnopeustekniikasta on tehty tutkimusta 1980-luvulta lähtien. On havaittu, että tiettyjen energiateknisten sovellusten hyötysuhde paranee, kun käytetään selkeästi tavanomaista suurempaa pyörimisnopeutta. Suurnopeuspumppuja on totuttu näkemään lähinnä erikoiskohteissa, kuten avaruustekniikassa. Tämän työn tarkoituksena on kartoittaa, voiko suurnopeuspumppuja käyttää tavallisissa teollisuussovelluksissa, joissa tarvitaan korkeapaineista vettä. Työssä selvitetään pumppujen laskentaan ja valintaan liittyvää käsitteistöä, sekä luodaan kirjallisuuskatsaus suurnopeuspumppujen kehitykseen. Työn tarkoituksena on myöskin luoda valmiuksia suurnopeuspumppujen tutkimukseen ja arviointiin.
Resumo:
The pumping processes requiring wide range of flow are often equipped with parallelconnected centrifugal pumps. In parallel pumping systems, the use of variable speed control allows that the required output for the process can be delivered with a varying number of operated pump units and selected rotational speed references. However, the optimization of the parallel-connected rotational speed controlled pump units often requires adaptive modelling of both parallel pump characteristics and the surrounding system in varying operation conditions. The available information required for the system modelling in typical parallel pumping applications such as waste water treatment and various cooling and water delivery pumping tasks can be limited, and the lack of real-time operation point monitoring often sets limits for accurate energy efficiency optimization. Hence, alternatives for easily implementable control strategies which can be adopted with minimum system data are necessary. This doctoral thesis concentrates on the methods that allow the energy efficient use of variable speed controlled parallel pumps in system scenarios in which the parallel pump units consist of a centrifugal pump, an electric motor, and a frequency converter. Firstly, the suitable operation conditions for variable speed controlled parallel pumps are studied. Secondly, methods for determining the output of each parallel pump unit using characteristic curve-based operation point estimation with frequency converter are discussed. Thirdly, the implementation of the control strategy based on real-time pump operation point estimation and sub-optimization of each parallel pump unit is studied. The findings of the thesis support the idea that the energy efficiency of the pumping can be increased without the installation of new, more efficient components in the systems by simply adopting suitable control strategies. An easily implementable and adaptive control strategy for variable speed controlled parallel pumping systems can be created by utilizing the pump operation point estimation available in modern frequency converters. Hence, additional real-time flow metering, start-up measurements, and detailed system model are unnecessary, and the pumping task can be fulfilled by determining a speed reference for each parallel-pump unit which suggests the energy efficient operation of the pumping system.
Resumo:
Tämän diplomityön tarkoituksena on selvittää alueellisen lämmön- ja sähköntuotannon laskentamenetelmävalintojen vaikutuksia kasvihuonekaasupäästöihin. Työn tutkimuskysymyksenä on, onko mahdollista, että laskentamenetelmän valinnalla on suurempi vaikutus alueen kasvihuonekaasupäästöihin kuin energiantuotantotekniikan valinnalla. Laskentamenetelmävalinnoista tutkitaan tarkemmin CHP-laitoksen päästöjen allokointitavan ja sähkönpäästöjen määrittämisen vaikutuksia kasvihuonekaasupäästöihin. Tutkimusmenetelminä työssä on käytetty kirjallisuuskatsausta sekä tapaustutkimusta. Kirjallisuuskatsauksen aineistona käytetään tieteellisiä artikkeleita ja tutkimusraportteja. Tapaustutkimuksessa tutkitaan yksittäistä case-kohdetta, joka on Tampereen Härmälänrannan uudisrakennusalue, ja jossa vertaillaan maalämpöpumppua ja kaukolämpöä alueen lämmitysratkaisuina. Työn tuloksena todetaan, että on olemassa sellaisia tilanteita, joissa laskentamenetelmän valinnalla on suurempi vaikutus alueen kasvihuonekaasupäästöihin kuin energiantuotantotekniikan valinnalla. Lisäksi case-tarkastelun perusteella huomataan, että laskentamenetelmävalinnoilla on sitä suurempi merkitys, mitä enemmän CHP-laitoksessa käytetään uusiutuvaa polttoainetta. Työn johtopäätöksenä voidaan todeta, että energiantuotannon kasvihuonekaasupäästölaskennassa on syytä ymmärtää ja huomioida eri laskentamenetelmävalintojen vaikutus esitettyihin tuloksiin.
Resumo:
The steel industry produces, besides steel, also solid mineral by-products or slags, while it emits large quantities of carbon dioxide (CO2). Slags consist of various silicates and oxides which are formed in chemical reactions between the iron ore and the fluxing agents during the high temperature processing at the steel plant. Currently, these materials are recycled in the ironmaking processes, used as aggregates in construction, or landfilled as waste. The utilization rate of the steel slags can be increased by selectively extracting components from the mineral matrix. As an example, aqueous solutions of ammonium salts such as ammonium acetate, chloride and nitrate extract calcium quite selectively already at ambient temperature and pressure conditions. After the residual solids have been separated from the solution, calcium carbonate can be precipitated by feeding a CO2 flow through the solution. Precipitated calcium carbonate (PCC) is used in different applications as a filler material. Its largest consumer is the papermaking industry, which utilizes PCC because it enhances the optical properties of paper at a relatively low cost. Traditionally, PCC is manufactured from limestone, which is first calcined to calcium oxide, then slaked with water to calcium hydroxide and finally carbonated to PCC. This process emits large amounts of CO2, mainly because of the energy-intensive calcination step. This thesis presents research work on the scale-up of the above-mentioned ammonium salt based calcium extraction and carbonation method, named Slag2PCC. Extending the scope of the earlier studies, it is now shown that the parameters which mainly affect the calcium utilization efficiency are the solid-to-liquid ratio of steel slag and the ammonium salt solvent solution during extraction, the mean diameter of the slag particles, and the slag composition, especially the fractions of total calcium, silicon, vanadium and iron as well as the fraction of free calcium oxide. Regarding extraction kinetics, slag particle size, solid-to-liquid ratio and molar concentration of the solvent solution have the largest effect on the reaction rate. Solvent solution concentrations above 1 mol/L NH4Cl cause leaching of other elements besides calcium. Some of these such as iron and manganese result in solution coloring, which can be disadvantageous for the quality of the PCC product. Based on chemical composition analysis of the produced PCC samples, however, the product quality is mainly similar as in commercial products. Increasing the novelty of the work, other important parameters related to assessment of the PCC quality, such as particle size distribution and crystal morphology are studied as well. As in traditional PCC precipitation process, the ratio of calcium and carbonate ions controls the particle shape; a higher value for [Ca2+]/[CO32-] prefers precipitation of calcite polymorph, while vaterite forms when carbon species are present in excess. The third main polymorph, aragonite, is only formed at elevated temperatures, above 40-50 °C. In general, longer precipitation times cause transformation of vaterite to calcite or aragonite, but also result in particle agglomeration. The chemical equilibrium of ammonium and calcium ions and dissolved ammonia controlling the solution pH affects the particle sizes, too. Initial pH of 12-13 during the carbonation favors nonagglomerated particles with a diameter of 1 μm and smaller, while pH values of 9-10 generate more agglomerates of 10-20 μm. As a part of the research work, these findings are implemented in demonstrationscale experimental process setups. For the first time, the Slag2PCC technology is tested in scale of ~70 liters instead of laboratory scale only. Additionally, design of a setup of several hundreds of liters is discussed. For these purposes various process units such as inclined settlers and filters for solids separation, pumps and stirrers for material transfer and mixing as well as gas feeding equipment are dimensioned and developed. Overall emissions reduction of the current industrial processes and good product quality as the main targets, based on the performed partial life cycle assessment (LCA), it is most beneficial to utilize low concentration ammonium salt solutions for the Slag2PCC process. In this manner the post-treatment of the products does not require extensive use of washing and drying equipment, otherwise increasing the CO2 emissions of the process. The low solvent concentration Slag2PCC process causes negative CO2 emissions; thus, it can be seen as a carbon capture and utilization (CCU) method, which actually reduces the anthropogenic CO2 emissions compared to the alternative of not using the technology. Even if the amount of steel slag is too small for any substantial mitigation of global warming, the process can have both financial and environmental significance for individual steel manufacturers as a means to reduce the amounts of emitted CO2 and landfilled steel slag. Alternatively, it is possible to introduce the carbon dioxide directly into the mixture of steel slag and ammonium salt solution. The process would generate a 60-75% pure calcium carbonate mixture, the remaining 25-40% consisting of the residual steel slag. This calcium-rich material could be re-used in ironmaking as a fluxing agent instead of natural limestone. Even though this process option would require less process equipment compared to the Slag2PCC process, it still needs further studies regarding the practical usefulness of the products. Nevertheless, compared to several other CO2 emission reduction methods studied around the world, the within this thesis developed and studied processes have the advantage of existing markets for the produced materials, thus giving also a financial incentive for applying the technology in practice.
Resumo:
The basis of this thesis was to optimize heat pump that uses multiple heat sources to get competitive heating system for residential building when life cycle costs are considered. The objectives were to compile necessary information to calculate life cycle costs for heating system of residential building and start to compose of designing program for heat pump based heating systems. Examinations were made for the purchase energy need of residential building. Features of heat pump, considered refrigerant and potential heat sources were examined to find out heat production potential of heat pumps. Necessary information for life cycle cost calculation was also examined. Collected data was used in two case analyses to design selected heat production systems and calculate their life cycle costs. On the basis of case analyses heat pump based hybrid heat production systems are very competitive on life cycle cost comparison against district heating when residential building uses a lot of energy. New buildings use considerably less energy and achieved energy cost savings with heat pump systems may not be enough to cover the relatively high investment cost in reasonable time period compared to district heating system. The calculation method was found to require further development to at least include the cooling energy need of the building. Cooling demand will continue to grow in the future, which improves the heat pump based heat production systems competitiveness compared to other systems.
Resumo:
Pumping systems account for up to 22 % of the energy consumed by electrical motors in European industry. Many studies have shown that there is also a lot of potential for energy savings in these systems with the improvement of devices, flow control or surrounding sys-tem. The best method for more energy efficient pumping has to be found for each system separately. This thesis studies how energy saving potential in reservoir pumping system is affected by surrounding variables, such as the static head variation and friction factor. The objective is to create generally applicable graphs to quickly compare methods for reducing pumping system’s energy costs. The gained results are several graphs showcasing how the chosen variables affect energy saving potential of the pumping system in one specific case. To judge if these graphs are generally applicable, more testing with different pumps and environments are required.