Numerical Analysis on a Dual-Loop Waste Heat Recovery System Coupled with an ORC for Vehicle Applications

The internal combustion (IC) engines exploits only about 30% of the chemical energy ejected through combustion, whereas the remaining part is rejected by means of cooling system and exhausted gas. Nowadays, a major global concern is finding sustainable solutions for better fuel economy which in turn results in a decrease of carbon dioxide (CO2) emissions. The Waste Heat Recovery (WHR) is one of the most promising techniques to increase the overall efficiency of a vehicle system, allowing the recovery of the heat rejected by the exhaust and cooling systems. In this context, Organic Rankine Cycles (ORCs) are widely recognized as a potential technology to exploit the heat rejected by engines to produce electricity. The aim of the present paper is to investigate a WHR system, designed to collect both coolant and exhausted gas heats, coupled with an ORC cycle for vehicle applications. In particular, a coolant heat exchanger (CLT) allows the heat exchange between the water coolant and the ORC working fluid, whereas the exhausted gas heat is recovered by using a secondary circuit with diathermic oil. By using an in-house numerical model, a wide range of working conditions and ORC design parameters are investigated. In particular, the analyses are focused on the regenerator location inside the ORC circuits. Five organic fluids, working in both subcritical and supercritical conditions, have been selected in order to detect the most suitable configuration in terms of energy and exergy efficiencies.

Heat fluxes between the Guadalquivir river and the Gulf of Cádiz Continental Shelf

An 18-year time series of daily sea surface temperature of Gulf of Cadiz and an 18-month time series of temperature collected in the vicinity of the Guadalquivir estuary mouth have been analyzed to investigate the heat exchange between the estuary and the adjacent continental shelf. The first time identifies a continental shelf area where seasonal thermal oscillation signal (amplitudes and phase) changes abruptly. In order to explain this anomaly, the second data set allows a description of thermal fluctuations in a wide range of frequencies and an estimation of the upstream heat budget of the Guadalquivir estuary. Results show that high frequency thermal signal, diurnal and semidiurnal, and water flux signal through Guadalquivir mouth, mainly semidiurnal, apparently interact randomly to give a small exchange of thermal energy at high frequency. There is no trace, at the estuary's mouth, of daily heat exchanges with intertidal mudflats probably because it tends to cancel on daily time scales. Results also show that fluctuations of estimated air-sea fluxes force fluctuations of temperature in a quite homogeneous estuarine, with a delay of 20 days. The along-channel thermal energy gradient reaches magnitudes of 300-400 J m-4 near the mouth during the summer and winter and drives the estuary-shelf exchange of thermal energy at seasonal scale. Particularly, the thermal heat imported by the estuary from the shelf area during late fall-winter-early spring of 2008/2009 is balanced by the thermal heat that the estuary exports to the shelf area during late spring-summer of 2008. In summary, Guadalquivir river removes/imports excess of thermal energy towards/from the continental shelf seasonally, as a mechanism to accommodate excess of heat from one side respect to the other side.

A correct enthalpy relationship as thermal comfort index for livestock

Researchers working with thermal comfort have been using enthalpy to measure thermal energy inside rural facilities, establishing indicator values for many situations of thermal comfort and heat stress. This variable turned out to be helpful in analyzing thermal exchange in livestock systems. The animals are exposed to an environment which is decisive for the thermoregulatory process, and, consequently, the reactions reflect states of thermal comfort or heat stress, the last being responsable for problems of sanity, behavior and productivity. There are researchers using enthalpy as a qualitative indicator of thermal environment of livestock such as poultry, cattle and hogs in tropical regions. This preliminary work intends to check different enthalpy equations using information from classical thermodynamics, and proposes a direct equation as thermal comfort index for livestock systems.

Auditoria e optimização energética à secção de impregnação de uma indústria têxtil

Mestrado em Engenharia Química

Recuperação do calor de um efluente primário para aquecimento de lamas de um reactor anaeróbio

O presente trabalho tem como principal objectivo o estudo da possibilidade de recuperação de calor de um efluente proveniente do tratamento primário da fábrica do grupo Portucel Soporcel (fábrica produtora de pasta de papel), para o aquecimento da corrente de lamas do digestor anaeróbio da SimRia S.A. – ETAR Norte, (ambas localizadas em Cacia, distrito de Aveiro). A solução consiste na implementação de um sistema de permuta térmica entre estas duas correntes, constituído fundamentalmente por dois permutadores de placas em espiral, montados em paralelo que operam em contra-corrente. Segundo este novo sistema de aquecimento, as lamas abandonam o digestor anaeróbio da mesma ETAR a um caudal de 110 m3/h, que se dividirá em duas linhas, sendo admitidas em cada permutador a 55 m3/h e a uma temperatura de 32 ºC regressando ao digestor a uma temperatura de 37 ºC (temperatura óptima a que ocorre a digestão anaeróbia das lamas). O efluente disponível, abandona o tratamento primário da Portucel, a 45 ºC e é encaminhado até aos permutadores da SimRia S.A., onde vai trocar calor com as lamas e regressa à Portucel a 40ºC, sendo admitido nas torres de arrefecimento da fábrica de papel. A nova instalação proposta pretende substituir a actual existente na ETAR em causa, em que a corrente de água que aquece as lamas, circula num circuito fechado entre um único permutador e uma caldeira, alimentada com o biogás que se produz no digestor anaeróbio, e que é responsável pelo controlo da temperatura da corrente de água. Pretende-se que a implementação deste novo método de aquecimento de lamas seja uma alternativa económica relativamente ao actual sistema, uma vez que vai substituir a corrente de biogás alimentada à caldeira podendo este recurso ser transformado em energia eléctrica e posteriormente comercializada. A análise financeira realizada ao projecto demonstrou que o projecto é rentável, uma vez que, a diferença entre todos ganhos e custos ao fim dos 10 anos de vida útil estimados é de cerca de 150 000,0 €. O período de retorno do investimento é alcançado no final dos primeiros 6 anos e a taxa interna de rentabilidade obtida foi de 36 %. Posteriormente incluiu-se neste estudo a possibilidade de tratamento das lamas geradas na fábrica da Portucel na ETAR da SimRia recorrendo a um terceiro digestor. Conclui-se que se trata duma opção vantajosa, uma vez que permite obter um caudal de biogás 44 m3/h, que convertido em potência permite obter 150 kW que poderá ser aproveitado para produção de energia ou comercializado gerando uma receita adicional de 130 000,0 €/ano para as entidades envolvidas.

Maximização da produção de paraxileno

Pretendeu-se, com o presente trabalho, efectuar um estudo sobre a possibilidade de aumentar a produção de paraxileno na unidade processual existente na refinaria da Galp no Porto. Foram estudados o conjunto de colunas T-0306 e T-0307 e a coluna T-0303, recorrendo ao uso do AspenPlus, na realização da simulação do processo nas condições actuais e para a realização da análise de sensibilidade, que permitiu verificar se o equipamento existente possui capacidade para satisfazer as necessidades exigidas pelo processo quando se pretende aumentar a produção. Com a simulação do processo, foi verificado que este já se encontra a laborar em condições óptimas. Na realização da análise de sensibilidade foram variados para o conjunto T-0306 e T- 0307, o caudal de alimentação entre 62780 e 95000 kg/h, o caudal de destilado da T-0306 entre 15833 e 23911 kg/h e o caudal de destilado da T-0307 entre 139 e os 235 kg/h. No caso da T-0303, foi variado o caudal de refinado entre 201240 e 304600 kg/h, o caudal de destilado e o caudal da corrente lateral, variam entre 77290 a 116930 kg/h. Pretendeu-se obter soluções que conseguissem cumprir as especificações relativas aos produtos obtidos, nomeadamente paraxileno com uma pureza de 99,6% e uma recuperação de 99%, tolueno com uma pureza de 97% e uma recuperação de 90% (T-0306 e T-0307). No caso da T- 0303, obter paraxileno com uma pureza de 2,23% e paradietilbenzeno com uma pureza de 99,0% e ambos com uma recuperação de 99%. Para as simulações que cumpriram as especificações anteriores, verificou-se se a energia transferida em aeroarrefecedores, fornalhas e permutadores excedem em 25% o seu valor de projecto. Em caso afirmativo isso significou o acréscimo de uma peça de equipamento idêntica à existente. A análise de sensibilidade permitiu concluir a separação é possível para os caudais actuais de extracto e refinado e para um aumento destes de 32, 40 e 50%. Foi ainda possível concluir que para os caudais actuais é necessária a colocação de novos aeroarrefecedores para as colunas T-0306 e T-0303 e de uma nova fornalha para a coluna T-0303. Para um aumento dos caudais de 32% para além das alterações referidas anteriormente é necessária a colocação de um novo aeroarrefecedor na coluna T-0307 e de uma nova fornalha da coluna T-0306. Se aumentarmos os caudais em 40% será também necessário o acréscimo de permutadores para a coluna T-0307. Para o aumento de 50%, os calores de permuta são excedidos em bastante mais do que 25%, em todos os aeroarrefecedores, permutadores e fornalhas. Uma vez que todas as colunas se encontram a funcionar acima da sua capacidade, concluiu-se que em ambos os casos seria necessária a montagem de uma segunda linha em paralelo e igual à existente. Implicando com esta alteração um investimento total de 10.439.574,36€.

Development of a new 3D OpenFOAM® solver to model the cooling stage in profile extrusion

[Excerpt] The advantages resulting from the use of numerical modelling tools to support the design of processing equipment are almost consensual. The design of calibration systems in profile extrusion is not an exception . H owever , the complex geome tries and heat exchange phenomena involved in this process require the use of numerical solvers able to model the heat exchange in more than one domain ( calibrator and polymer), the compatibilization of the heat transfer at the profile - calibrator interface and with the ability to deal with complex geometries. The combination of all these features is usually hard to find in commercial software. Moreover , the dimension of the meshes required to ob tain accurate results, result in computational times prohibitive for industrial application. (...)

Levylämmönsiirtimen mitoitus ja optimointi erityisesti lämpöpumpuissa

Työn tavoitteena on laatia käsikirjamainen läpileikkaus levylämmönsiirtimen rakenteesta ja käytöstä lämpöpumppulaitteistoissa. Kylmäprosessin tarkastelun lisäksi on eri lähteistä haettu yhtälöitä lämmönsiirron ja painehäviönlaskentaan. Lähdeaineistona on käytetty lämmönsiirron oppikirjoja, joiden lisäksi on käyty läpi suuri joukko tieteellisen tutkimuksen julkaisemia tutkimusraportteja levylämmönsiirtimen mitoituksesta erilaisissa käyttökohteissa. Oppikirjoissa ei ole esitetty varsinaisesti levylämmönsiirtimen laskentamenetelmiä, vaan niissä esitetään lämmönsiirron perusyhtälöt. Varsinainen lämmönsiirtolevyprofiilin laskentaan perustuva lähdeaineisto on löytynyt lämmönsiirtoon erikoistuneista julkaisuista. Lämmönsiirto tapahtuu aina kuumemmasta kylmempään tilaan. Lämmönsiirto eri virtausaineiden välillä toteutetaan lämmönsiirtimien avulla. Lämmönsiirrintyyppejä on olemassa lukuisia, joista yksi yleisesti käytetty tyyppi on levylämmönsiirrin. Tässä konstruktiossa on mahdutettu paljon lämmönsiirtopintaa ulkomitoiltaan pieneen tilaan. Tämä siirrintyyppi on eduksi silloin, kun virtaavat aineet ovat puhtaita ja niillä ei ole likaavaa vaikutusta lämmönsiirtopinnoille. Lämpöpumpulla tarkoitetaan laitetta, jolla voidaan käyttää hyödyksi lämmönlähteen matalaa lämpötilatasoa nostamalla lämpötilatasoa kompressorin puristustyön avulla korkeampaan lämpötilatasoon. Lämpöpumppulaitteiston toiminta perustuu kylmäprosessin toimintaan. Kylmäprosessin läpikäynti auttaa lukijaa hahmottamaan, millainen prosessi on kysymyksessä ja mitä komponentteja liittyy kylmäprosessiin. Tässä diplomityössä esitetyt yhtälöt antavat suuntaa, millä tavalla levylämmönsiirtimien ominaisuuksia voidaan laskea ja mitkä tekijät vaikuttavat siirtimien mitoittamiseen. Tarkemmat vaihdinkohtaiset laskentakorrelaatiot muotoutuvat vasta sitten, kun valmis tuote on testattu laboratorio-olosuhteissa ja siitä on saatu lämpötila-, virtaus- ja painesuhteet selville. Tämän jälkeen voidaan mittaustuloksiin perustuen rakentaa matemaattinen malli, jolla laskennallisesti määritelläänvaihtimien ominaisuudet. Lisäksi on esitetty yleisiä tapoja, joilla voidaan määritellä lämmönsiirtimien lämpöpintoja.

Isentropic Exergy and Pressure of the Shock Wave Caused by the Explosion of a Pressure Vessel

An accidental burst of a pressure vessel is an uncontrollable and explosion-like batch process. In this study it is called an explosion. The destructive effectof a pressure vessel explosion is relative to the amount of energy released in it. However, in the field of pressure vessel safety, a mutual understanding concerning the definition of explosion energy has not yet been achieved. In this study the definition of isentropic exergy is presented. Isentropic exergy is the greatest possible destructive energy which can be obtained from a pressure vessel explosion when its state changes in an isentropic way from the initial to the final state. Finally, after the change process, the gas has similar pressure and flow velocity as the environment. Isentropic exergy differs from common exergy inthat the process is assumed to be isentropic and the final gas temperature usually differs from the ambient temperature. The explosion process is so fast that there is no time for the significant heat exchange needed for the common exergy.Therefore an explosion is better characterized by isentropic exergy. Isentropicexergy is a characteristic of a pressure vessel and it is simple to calculate. Isentropic exergy can be defined also for any thermodynamic system, such as the shock wave system developing around an exploding pressure vessel. At the beginning of the explosion process the shock wave system has the same isentropic exergyas the pressure vessel. When the system expands to the environment, its isentropic exergy decreases because of the increase of entropy in the shock wave. The shock wave system contains the pressure vessel gas and a growing amount of ambient gas. The destructive effect of the shock wave on the ambient structures decreases when its distance from the starting point increases. This arises firstly from the fact that the shock wave system is distributed to a larger space. Secondly, the increase of entropy in the shock waves reduces the amount of isentropic exergy. Equations concerning the change of isentropic exergy in shock waves are derived. By means of isentropic exergy and the known flow theories, equations illustrating the pressure of the shock wave as a function of distance are derived. Amethod is proposed as an application of the equations. The method is applicablefor all shapes of pressure vessels in general use, such as spheres, cylinders and tubes. The results of this method are compared to measurements made by various researchers and to accident reports on pressure vessel explosions. The test measurements are found to be analogous with the proposed method and the findings in the accident reports are not controversial to it.

Prosessihyötysuhteen parantamiskohteiden kartoitus painevesireaktorityyppisessä ydinvoimalaitoksessa

Työn tavoitteena on kartoittaa painevesireaktorityyppisen ydinvoimalaitoksen prosessihyötysuhteen parantamiskohteita. Aluksi kirjallisuudesta etsitään hyötysuhteen parantamiskeinoja ideaalisessa höyryvoimalaitosprosessissa. Näistä valitaan sopivimmat tarkastelun kohteeksi todellisessa voimalaitoksessa: syöttöveden esilämmityksen tehostaminen väliottohöyryvirtausta kasvattamalla ja syöttöveden esilämmittimen lämmönsiirtopintaa lisäämällä. Tarkastelussa pyritään löytämään paras mahdollinen hyötysuhde väliottohöyrylinjojen putkikokoa sekä esilämmittimien putkien lukumäärää muuttamalla. Diskreetin optimoinnin iteraatioaskel määritetään hyötysuhteen osittaisderivaattojen avulla. Tehtäviä muutoksia simuloidaan APROS-simulointiohjelmalla, jossa käytetään Loviisan voimalaitoksesta tehtyä mallia VVER-440. Työssä havaittiin, että pelkkiä väliottohöyrylinjojen putkikokoja – ja massavirtaa – kasvattamalla Loviisan voimalaitoksen hyötysuhdetta voidaan parantaa parhaimmillaan 32,75%:sta 32,85%:iin. Syöttöveden esilämmittimien lämmönsiirtopintaa lisäämällä saadaan suurempi parannus hyötysuhteeseen: 32,75%:sta 32,99%:iin. Näissä tapauksissa muutettiin kaikkia väliottohöyrylinjoja tai syöttöveden esilämmittimien lämpöpintoja. Työssä tarkasteltiin myös joitakin pienempiä muutoskohteita, joista paras hyötysuhteen kasvu saatiin korkeapaine-esilämmittimien lämmönsiirtopintaa kasvattamalla sekä toisen väliottohöyrylinjan (RD12) ja sitä vastaavan syöttöveden esilämmittimen muutosten yhteisvaikutuksena.

The influence of the season of the year and of dilution on the development of swine manure and wood shaves co-composting

The objective of this research was to study the influence of factors related to the proper management of pig manure (lower dilution) and the season of the year in the progress of the co-composting of pig manure with wood shavings and in the final quality of the compost resulting from the treatments. In the first experiment, two types of swine manure were used: a diluted one (2% Dry Matter - DM), typical from the management usually used in Brazil, and a more concentrated one (6% DM). The manures were incorporated into the wood shavings (6L:1kg) over the course of four weeks. The development of composting was accompanied by monitoring of temperatures inside the piles and the emission of CO2 and CH4 gases during 65 days, including the period of incorporation. The results showed that the diluted manure does not provide the minimum conditions for starting the process. After the incorporation period, any biomass heating was observed and neither the aerobic or anaerobic respiration of the microorganisms, resulting in a compost with low quality. In the second experiment, which evaluated composting in winter and summer during 85 days, it was found that the heat exchange with the environment influences the temperature generated within the piles. The lower temperatures significantly reduced the methanogenesis on the biomass.

Dynaamisen lämmönsiirtomallin kehittäminen

Dynaamisia simulointimalleja tarvitaan, jotta voidaan tarkastella järjestelmän käyttäytymistä ajan funktiona. Simulointimallilla voidaan simuloida järjestelmän lähtö erilaisilla herätteillä. Mallin avulla saadaan myös tarkempi käsitys järjestelmästä ja sen osa-alueista, koska simulointimallista voidaan tarkastella sellaisia asioita, jotka voivat olla oikeasta järjestelmästä vaikeasti mitattavia. Tässä työssä kehitetään LUT Energian hyötysuhdemittapaikan keskikokoista kalorimetriä approksimoiva dynaaminen lämmönsiirtomalli käyttäen Matlab® Simulink -ohjelmistoa. Kehitetyn lämmönsiirtomallin tarkkuutta arvioidaan todellisella järjestelmällä tehdyillä mittauksilla. Työssä käytetään karkeita approksimaatioita, jotka tulee korvata tarkemmilla matemaattisilla malleilla jatkokehitystä varten. Työssä kehitetty dynaaminen lämmönsiirtomalli approksimoi todellisen järjestelmän vastetta lämmitysvaiheessa keskimääräisenvirheen ±0,19 °C tarkkuudella.

Numerical and experimental investigation of thermal louvers for space applications

Thermal louvers, using movable or rotating shutters over a radiating surface, have gained a wide acceptance as highly efficient devices for controlling the temperature of a spacecraft. This paper presents a detailed analysis of the performance of a rectangular thermal louver with movable blades. The radiative capacity of the louver, determined by its effective emittance, is calculated for different values of the blades opening angle. Experimental results obtained with a prototype of a spacecraft thermal louver show good agreement with the theoretical values.

Modeling of temperature regimes in a furnace of bubbling fluidized bed boiler

The work is mainly focused on the technology of bubbling fluidized bed combustion. Heat transfer and hydrodynamics of the process were examined in the work in detail. Special emphasis was placed on the process of heat exchange in a freeboard zone of bubbling fluidized bed boiler. Operating mode of bubbling fluidized bed boiler depends on many parameters. To assess the influence of some parameters on a temperature regime inside the furnace a simplified method of zonal modeling was used in the work. Thus, effects of bed material fineness, excess air ratio and changes in boiler load were studied. Besides the technology of combustion in bubbling fluidized bed, other common technologies of solid fuels combustion were reviewed. In addition, brief survey of most widely used types of solid fuel was performed in the work.

Luonnonkiertovirtauksen kääntyminen pystyhöyrystimen lämmönvaihtoputkissa

Diplomityössä tutkitaan virtauksen kääntymistä Lappeenrannan teknillisen yliopiston PWR PACTEL –koelaitteiston pystyhöyrystimen lämmönvaihtoputkissa käyttäen APROS–prosessisimulointiohjelmaa. Työn teoriaosassa esitellään pystyhöyrystimillä varustettuja koelaitteistoja, erityisesti PWR PACTEL ja sen höyrystin. Lisäksi esitellään virtauksen kääntymisestä tehtyjä havaintoja ja käsitellään kääntymistä teoreettisesta näkökulmasta. Simulointiosan alussa esitellään työssä käytetty APROS –prosessisimulointiohjelma, sekä sen avulla höyrystimestä luodut mallit. Työssä on tutkittu virtauksen käännöstapahtumaa simuloimalla useita eri transienttitilanteita pienillä primäärimassavirroilla. Simulaatiotapauksissa havaittiin virtauksen kääntyvän höyrystimen eripituisissa lämmönvaihtoputkissa, tilanteesta riippuen pääosin lyhimmissä tai toisiksi lyhimmissä lämmönvaihtoputkissa. Transienttien eri vaiheiden, ts. primäärimassavirran muutos- ja tasaantumisvaiheiden pituuden havaittiin vaikuttavan siihen, minkä pituisissa putkissa kääntyminen tapahtuu ja missä järjestyksessä.