Os sistemas solares de aquecimento de água são uma forma de produção de energia não poluente, que já faz parte da matriz energética brasileira. O uso deste tipo de sistemas traz benefícios econômicos ao país e principalmente a quem os utiliza, devido à poupança no uso de outras fontes de energia para o aquecimento da água. No Brasil o aquecimento solar de água é realizado, principalmente, por coletores solares planos, tecnologia bem conhecida e fabricada no país a preços baixos. Mas atualmente há uma outra tecnologia que está sendo difundida no âmbito nacional, os coletores solares de tubos a vácuo, os quais estão sendo produzidos internacionalmente em uma escala maior, importados e comercializados a preços mais competitivos no mercado nacional. Por isto é necessário entender estes sistemas e o seu funcionamento para evitar erros na sua instalação e otimizar sua operação. Nesta dissertação é realizada uma análise comparativa de um sistema de aquecimento de água composto por um coletor solar de tubos de vidro a vácuo de extração de calor por transferência direta operando em circulação forçada com o mesmo sistema operando em circulação por termossifão. Esta comparação foi realizada determinando a energia anual que o sistema pode produzir para cada tipo de circulação, a qual foi calculada usando como referência a norma ISO 9459-2 e os dados climáticos da cidade de Porto Alegre do Estado do Rio Grande do Sul. Também foram realizadas medições da vazão em termossifão, entre o reservatório e o coletor solar, e foi determinado o coeficiente de perdas térmicas do tanque reservatório segundo os procedimentos da mesma norma. Para isto foi realizada a montagem de uma bancada experimental, com sensores e instrumentos de medida que foram calibrados. Para o sistema de aquecimento testado, os resultados mostram que o sistema trabalhando em circulação por termossifão produz maior quantidade de energia no ano do que o sistema em circulação forçada, onde se observou que a estratificação no tanque reservatório era menor. Também foi observado que a máxima vazão em termossifão para este sistema de aquecimento de água foi de 0,5 L/min. / Solar water heating systems are a method of clean energy production, which is already part of the Brazilian energy matrix. The use of these systems brings economic benefits to the country and especially who use them due to savings in the use of other sources of energy for heating water. In Brazil, the solar water heating is carried out mainly by flat solar collectors, which is a widely known technology because it is produced in the country at low prices. But recently, there is another technology that is being used named: evacuated solar collectors. These collectors are being worldwide produced on a large scale and they are imported and inserted at competitive prices in the domestic market. Therefore it is necessary to understand these systems and their operation to avoid errors in its installation and optimize their operation. In this work, it is accomplishing a comparative analysis of a solar water heating system composed by a water-in-glass evacuated tube solar collector working in forced circulation with the same system working in thermosyphon circulation. This comparison was performed by determining the annual energy that the system can produce for each type of circulation, which was calculated based on the ISO 9459-2 standard and the climatic data of the Porto Alegre city, state of the Rio Grande Do Sul. Also, it was performed thermosyphon measurements between the thermal reservoir and the solar collector, and it was calculated the heat loss coefficient from the reservoir tank according to the procedures of ISO 9459-2 standard. To do so, a testing bench was made, with sensors and measuring instruments which were calibrated before use. For the heating system tested, the results show that the system with thermosyphon circulation produces more annual energy than the forced circulation system where the water temperature stratification in the thermal reservoir was lower. Also, it was observed that the maximum thermosyphon flow for this solar water heating system was 0,5 L/min.

Os sistemas solares de aquecimento de água são uma forma de produção de energia não poluente, que já faz parte da matriz energética brasileira. O uso deste tipo de sistemas traz benefícios econômicos ao país e principalmente a quem os utiliza, devido à poupança no uso de outras fontes de energia para o aquecimento da água. No Brasil o aquecimento solar de água é realizado, principalmente, por coletores solares planos, tecnologia bem conhecida e fabricada no país a preços baixos. Mas atualmente há uma outra tecnologia que está sendo difundida no âmbito nacional, os coletores solares de tubos a vácuo, os quais estão sendo produzidos internacionalmente em uma escala maior, importados e comercializados a preços mais competitivos no mercado nacional. Por isto é necessário entender estes sistemas e o seu funcionamento para evitar erros na sua instalação e otimizar sua operação. Nesta dissertação é realizada uma análise comparativa de um sistema de aquecimento de água composto por um coletor solar de tubos de vidro a vácuo de extração de calor por transferência direta operando em circulação forçada com o mesmo sistema operando em circulação por termossifão. Esta comparação foi realizada determinando a energia anual que o sistema pode produzir para cada tipo de circulação, a qual foi calculada usando como referência a norma ISO 9459-2 e os dados climáticos da cidade de Porto Alegre do Estado do Rio Grande do Sul. Também foram realizadas medições da vazão em termossifão, entre o reservatório e o coletor solar, e foi determinado o coeficiente de perdas térmicas do tanque reservatório segundo os procedimentos da mesma norma. Para isto foi realizada a montagem de uma bancada experimental, com sensores e instrumentos de medida que foram calibrados. Para o sistema de aquecimento testado, os resultados mostram que o sistema trabalhando em circulação por termossifão produz maior quantidade de energia no ano do que o sistema em circulação forçada, onde se observou que a estratificação no tanque reservatório era menor. Também foi observado que a máxima vazão em termossifão para este sistema de aquecimento de água foi de 0,5 L/min. / Solar water heating systems are a method of clean energy production, which is already part of the Brazilian energy matrix. The use of these systems brings economic benefits to the country and especially who use them due to savings in the use of other sources of energy for heating water. In Brazil, the solar water heating is carried out mainly by flat solar collectors, which is a widely known technology because it is produced in the country at low prices. But recently, there is another technology that is being used named: evacuated solar collectors. These collectors are being worldwide produced on a large scale and they are imported and inserted at competitive prices in the domestic market. Therefore it is necessary to understand these systems and their operation to avoid errors in its installation and optimize their operation. In this work, it is accomplishing a comparative analysis of a solar water heating system composed by a water-in-glass evacuated tube solar collector working in forced circulation with the same system working in thermosyphon circulation. This comparison was performed by determining the annual energy that the system can produce for each type of circulation, which was calculated based on the ISO 9459-2 standard and the climatic data of the Porto Alegre city, state of the Rio Grande Do Sul. Also, it was performed thermosyphon measurements between the thermal reservoir and the solar collector, and it was calculated the heat loss coefficient from the reservoir tank according to the procedures of ISO 9459-2 standard. To do so, a testing bench was made, with sensors and measuring instruments which were calibrated before use. For the heating system tested, the results show that the system with thermosyphon circulation produces more annual energy than the forced circulation system where the water temperature stratification in the thermal reservoir was lower. Also, it was observed that the maximum thermosyphon flow for this solar water heating system was 0,5 L/min.

Les systèmes électriques occupent de nos jours une place de plus en plus importante dans le domaine du transport aérien, ferroviaire et automobile. Ce progrès s'est accompagné de la miniaturisation des systèmes(convertisseurs) qui nécessitent un refroidissement très performant. Alors que les systèmes de refroidissement traditionnels atteignent leurs limites, une des solutions consiste à utiliser des boucles fluides diphasiques reposant sur le changement de phase liquide-vapeur du fluide de travail, en particulier les boucles diphasiques gravitaires. L'objectif de cette thèse est double: proposer un modèle détaillé de la boucle ainsi qu'un modèle réduit capable de calculer les variables en tout point de la boucle et en tout instant mais beaucoup moins gourmand en temps de calcul. Concernant tout d'abord le modèle détaillé, les équations de l'écoulement monodimensionnel et compressible du fluide à l'état monophasique et diphasique en régime transitoire sont résolues par la méthode d 'Euler explicite et par la méthode des volumes finis. Le mélange liquide-vapeur se comporte comme un mélange homogène, en équilibre mécanique et thermique. Les lois de fermeture du modèle sont déduites des lois d'état du type "Stiffened Gas". En ce qui concerne le modèle réduit, une extension de la méthode d'identification modale est proposée. La structure du modèle réduit est tout d'abord déterminée en effectuant la projection de Galerkine des équations de conservation continues. Ensuite les paramètres dumodèle réduit sont identifiés par la résolution d'un problème d'optimisation. Le modèle réduit ainsi construit est alors validé sur plusieurs cas présentant des dynamiques différentes. / Today, electrical systems are becoming increasingly important in the air, rail and automotive sectors.The immediate consequence of this progress is the miniaturization of systems (converters) requiring very important cooling means. Whereas conventional cooling solutions are reaching their limit, an alternative one can be sought in two-phase loops based on the liquid-vapor phase change of a working fluid, in particular two-phase loop thermosyphon. The objective of this thesis is twofold : to propose a detailed model of a two phase loop thermosyphon as well as a reduced model able to calculate the variables at any location of the loop at any time with a much smaller computing time. First, the equation of the transient one-dimensional compressible one-phase and two-phase fluid flow is solved using the explicit Euler method of order 1 and the finite volume method. The liquid-vapor mixture is modeled as a homogeneous mixture at mechanical and thermal equilibrium. The closure laws of the model are deduced from the "Stiffened Gas" state laws. For the reduced model, an extension of the modal identification method is proposed. The structure of the reduced model is first determined carrying out the Galerkin projection of the continuous conservation equations.Then the parameters of the model are identified by the resolution of an optimization problem. The reduced model thus constructed is then validated on several cases with different dynamics

L'objectif de cette étude est de concevoir un système de refroidissement passif au sein d'un data center. La solution qui a été choisie est la boucle thermosiphon, combinant le free cooling et le refroidissement par changement de phase. Cette technologie offre de la simplicité et de la compacité. De plus, en l'associant avec des échangeurs de chaleur à micro-canaux, elle est capable d'absorber de grandes quantités de flux de chaleur avec un faible débit du réfrigérant. La boucle thermosiphon est composée d'un évaporateur à mini-canaux et à courants parallèles, d'un condenseur à air, d'un riser et d'un downcomer. Un prototype expérimental a été construit afin de caractériser les transferts de chaleur entre le réfrigérant et la chaleur créée. Des études expérimentales sont introduites. L'influence du taux de chargement et de la puissance électrique est détaillée et analysée. En parallèle, un modèle numérique a été développé pour prédire les caractéristiques du réfrigérant en fonction des paramètres géométriques et climatiques. Une comparaison avec les résultats expérimentaux est également effectuée. Enfin, la boucle thermosiphon est améliorée avec l'ajout d'un second évaporateur. Les tests sont effectués avec des puissances plus importantes. Une nouvelle conception d'une boucle thermosiphon et les limites du prototype sont présentées. / The objective of this study is to build a passive cooling system in a data center. The chosen solution is the loop thermosyphon, combining free cooling and two-phase cooling. This technology offers simplicity and compactness. Furthermore, by associating with micro-channels heat exchangers, it is able to remove higher heat fluxes while working with smaller mass flow rate of coolant. The thermosyphon is composed by mini-channel parallel-flow evaporator, an air condenser, a riser and a downcomer. The experimental setup has been built to characterize the heat transfer between the working fluid and the provided heat. An experimental study is introduced. The effect of the fill ratio and the input power is specified and analyzed. In parallel, a numerical model has been developed to predict the fluid properties in function of geometrical and climatic parameters. A comparison between experimental and numerical results is also carried out. Finally, the loop thermosyphon is upgraded with a second mini-channel parallel flow evaporator. Tests are conducted with huger heat flux. A new design of loop thermosyphon and the limits of the prototype are introduced.

The thermal performance of two thermosyphons with different geometries was experimentally investigated in this study. The first thermosyphon utilized a 310 mm long vertical evaporator and a 385 mm long condenser section that was inclined at 5 degrees from the vertical. The second was an elbow configuration with a 140 mm long vertical evaporator and a 190 mm long condenser oriented 8 degrees from the horizontal. Both thermosyphons were made of internally grooved copper tubing with an outer diameter of 15.87 mm, wall thickness of 0.5 mm and a nominal groove height of 0.3 mm. Tests were performed over a range of input heat fluxes where the condenser was cooled by flowing water around the condenser with inlet temperature of 10°C, 20°C, and 35°C. The effects of incrementally increasing and decreasing heat flux was investigated for the elbow thermosyphon. Temperature measurements along the thermosyphon were taken when incrementally changing the heat flux from 0.5 to 11 W/m2 for the first thermosyphon and 0.3 to 6 W/m2 for the second thermosyphon. Internal flow regimes were characterized using temperature transient profiles and compared to existing flow regime maps for closed thermosyphons suggested by Smith et al. (2018: Part a and Part b) and Terdoon et al. (1997). The temperature transients along the evaporator for the first thermosyphon settled to a more uniform profile as heat flux was increased. For the second thermosyphon the temperature profiles suggested a change to a more dynamic flow in the evaporator at heat flux of approximately 6 W/m2. The elbow thermosyphon showed evidence of a significant hysteresis in the evaporator performance at moderate heat fluxes between 2 and 8 W/cm2. Comparisons were made between the two thermosyphons to study the effects of inclination angle and the feasibility of angle corrections to the Nusselt film condensation model from Guichet and Jouhara (2020). A modification to the Rohsenow condensation model from Guichet and Jouhara (2020) was recommended for the first thermosyphon showing good representation of the condenser performance. The evaporator performance results were compared to existing models from the literature. / Thesis / Master of Applied Science (MASc)

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Thesis (MScEng (Mechanical and Mechatronic Engineering))--University of Stellenbosch, 2010. / ENGLISH ABSTRACT: A reactor cavity cooling system (RCCS) is used in the PBMR to protect the concrete citadel surrounding the reactor from direct nuclear radiation impingement and heat. The speci ed maximum operating temperature of the concrete structure is 65 ±C for normal operating conditions and 125 ±C for emergency shut-down conditions. A conceptual design of an entirely passive RCCS suitable for the PBMR was done by using closed loop thermosyphon heat pipes (CLTHPs) to remove heat from a radiation heat shield over a horizontal distance to an annular cooling dam placed around the PBMR. The radiation shield is placed in the air space between the Reactor Pressure Vessel (RPV) and the concrete citadel, 180 mm from the concrete citadel. A theoretical heat transfer model of the RCCS was created. The theoretical model was used to develop a computer program to simulate the transient RCCS response during normal reactor operation, when the RCCS must remove the excess generated heat from the reactor cavity and during emergency shut-down conditions, when the RCCS must remove the decay heat from the reactor cavity. The main purpose of the theoretical model is to predict the surface temperature of the concrete citadel for di erent heat generation modes in the reactor core and ambient conditions. The theoretical model assumes a 1D geometry of the RCCS. Heat transfer by both radiation and convection from the RPV to the radiation heat shield (HS) is calculated. The heat shield is modelled as a n. The n e ciency was determined with the experimental work. Conduction through the n is considered in the horizontal direction only. The concrete structure surface is heated by radiation from the outer surface of the heat shield as well as by convection heat transfer from the air between the heat shield and the concrete structure surface. The modelling of the natural convection closed loop thermosyphon heat pipes in the RCCS is done by using the Boussinesq approximation and the homogeneous ow model. An experiment was built to verify the theoretical model. The experiment is a full scale model of the PBMR in the horizontal, or main heat transfer, direction, but is only a 2 m high section. The experiments showed that the convection heat transfer between the RPV and the HS cannot be modelled with simple natural convection theory. A Nusselt number correlation developed especially for natural convection in enclosed rectangles found in literature was used to model the convection heat transfer. The Nusselt number was approximately 3 times higher than that which classic convection theory suggested. An optimisation procedure was developed where 121 di erent combinations of n sizes and heat pipe sizes could be used to construct a RCCS once a cooling dam size was chosen. The purpose of the optimisation was to nd the RCCS with the lowest total mass. A cooling dam with a diameter of 50 m was chosen. The optimal RCCS radiation heat shield that operates with the working uid only in single phase has 243 closed loop thermosyphon heat pipes constructed from 62.72 mm ID pipes and 25 mm wide atbar ns. The total mass of the single phase RCCS is 225 tons. The maximum concrete structure temperature is 62.5 ±C under normal operating conditions, 65.8 ±C during a PLOFC emergency shut-down condition and 80.9 ±C during a DLOFC emergency shut-down condition. In the case where one CLTHP fails and the adjacent two must compensate for the loss of cooling capacity, the maximum concrete structure temperature for a DLOFC emergency shut-down will be 87.4 ±C. This is 37.6 ±C below the speci ed maximum temperature of 125 ±C. The RCCS design is further improved when boiling of the working uid is induced in the CLTHP. The optimal RCCS radiation heat shield that operates with the working uid in a liquid-vapour mixture, or two phase ow, has 338 closed loop thermosyphon heat pipes constructed from 38.1 mm ID pipes and 20 mm wide atbar ns. The total mass of the two phase RCCS is 198 tons, 27 tons less than the single phase RCCS. The maximum concrete structure temperature is 60 ±C under normal operating conditions, 2.5 ±C below that of the single phase RCCS. During a PLOFC emergency shut-down condition, the maximum concrete structure temperature is 62.3 ±C, 3.5 ±C below that of the single phase RCCS and still below the normal operating temperature of the single phase RCCS. By inducing two phase ow in the CLTHP, the maximum temperature of the working uid is xed equal to the saturation temperature of the working uid at the vacuum pressure. This property of water is used to limit the concrete structure temperature. This e ect is seen in the transient response of the RCCS where the concrete structure temperature increases until boiling of the working uid starts and then the concrete structure temperature becomes constant irrespective of the heat load on the RCCS. An increased heat load increases the quality of the working uid liquid-vapour mixture. Working uid qualities approaching unity causes numerical instabilities in the theoretical model. The theoretical model cannot capture the heat transfer to a control volume with a density lower than approximately 20 kg/m3. This limits the extent to which the two phase RCCS can be optimised. Recommendations are made relating to future work on how to improve the theoretical model in particular the convection modelling in the reactor cavities as well as the two phase ow of the working uid. Further recommendations are made on how to improve the basic design of the heat shield as well as the cooling section of the CLTHPs. / AFRIKAANSE OPSOMMING: 'n Reaktor lug spasie verkoelingstelsel (RLSVS) word in die PBMR gebruik om die beton wat die reaktor omring te beskerm teen direkte stralingskade en hitte. Die gespesi seerde maksimum temperatuur van die beton is 65 ±C onder normale bedryfstoestande en 125 ±C gedurende die noodtoestand afskakeling van die reaktor. 'n Konseptuele ontwerp van 'n geheel en al passiewe RLSVS geskik vir die PBMR is gedoen deur gebruik te maak van geslote lus termo-sifon (GLTSe) om hitte van die stralingskerm te verwyder oor a horisontale afstand na 'n ringvormige verkoelingsdam wat rondom die reaktor geposisioneer is. Die stralingskerm word in die lug spasie tussen die reaktor drukvat (RDV) en die beton geplaas, 180 mm vanaf die beton. 'n Teoretiese hitteoordrag model van die RLSVS was geskep. Die teoretiese model was gebruik vir die ontwikkeling van 'n rekenaar program wat die transiënte gedrag van die RLSVS sal simuleer gedurende normale bedryfstoestande, waar die oorskot gegenereerde hitte verwyder moet word vanuit die reaktor lug spasie, asook gedurende noodtoestand afskakeling van die reaktor, waar die afnemingshitte verwyder moet word. Die primêre doel van die teoretiese model is om the oppervlak temperatuur van die beton te voorspel onder verskillende bedryfstoestande asook verskillende omgewingstoestande. Die teoretiese model aanvaar 'n 1D geometrie van die RLSVS. Hitte oordrag d.m.v. straling asook konveksie vanaf die RDV na die stralingskerm word bereken. The stralingskerm word gemodelleer as 'n vin. Die vin doeltre endheid was bepaal met die eksperimente wat gedoen was. Hitte geleiding in die vin was slegs bereken in die horisontale rigting. Die beton word verhit deur straling vanaf die agterkant van die stralingskerm asook deur konveksie vanaf die lug tussen die stralingskerm en die beton. The modellering van die natuurlike konveksie GLTS hitte pype word gedoen deur om gebruik te maak van die Boussinesq benadering en die homogene vloei model. 'n Eksperiment was vervaardig om the teoretiese model te veri eer. Die eksperiment is 'n volskaal model van die PBMR in die horisontale, of hoof hitteoordrag, rigting, maar is net 'n 2 m hoë snit. Die eksperimente het gewys dat die konveksie hitte oordrag tussen die RDV en die stralingskerm nie met gewone konveksie teorie gemodelleer kan word nie. 'n Nusselt getal uitdrukking wat spesi ek ontwikkel is vir natuurlike konveksie in geslote, reghoekige luggapings wat in die literatuur gevind was, was gebruik om die konveksie hitteoordrag te modelleer. Die Nusselt getal was ongeveer 3 maal groter as wat klassieke konveksie teorie voorspel het. 'n Optimeringsprosedure was ontwikkel waar 121 verskillende kombinasies van vin breedtes en pyp groottes wat gebruik kan word om 'n RLSVS te vervaardig nadat 'n toepaslike verkoelingsdam diameter gekies is. Die doel van die optimering was om die RLSVS te ontwerp wat die laagste totale massa het. 'n Verkoelingsdam diameter van 50 m was gekies. Die optimale RLSVS stralingskerm, waarvan die vloeier slegs in die vloeistof fase bly, bestaan uit 243 GLTSe wat van 62.72 mm binne diameter pype vervaardig is met 25 mm breë vinne. The totale massa van die enkel fase RLSVS is 225 ton. Die maksimum beton temperatuur is 62.5 ±C vir normale bedryfstoestande, 65.8 ±C vir 'n PLOFC noodtoestand afskakeling en is 80.9 ±C vir 'n DLOFC noodtoestand afskakeling. In die geval waar een GLTS faal gedurende 'n DLOFC noodtoestand afskakeling en die twee naasgeleë GLTSe moet kompenseer vir die vermindering in verkoelings kapasiteit, is die maksimum beton temperatuur 87.4 ±C. Dit is 37.6 ±C laer as die gespesi seerde maksimum temperatuur van 125 ±C. Die RLSVS ontwerp kan verder verbeter word wanneer die vloeier in die GLTSe kook. Die optimale RLSVS stralingskerm met die vloeier wat kook, of in twee fase vloei is, bestaan uit 338 GLTSe wat van 38.1 mm binne diameter pype vervaardig is met 20 mm breë vinne. The totale massa van die twee fase vloei RLSVS is 198 ton, 27 ton ligter as die enkel fase RLSVS. Die maksimum beton temperatuur is 60 ±C vir normale bedryfstoestande, 2.5 ±C laer as die enkel fase RLSVS. Gedurende 'n PLOFC noodtoestand afskakeling is die maksimum beton temperatuur 62.3 ±C, 3.5 ±C laer as die enkel fase RLSVS en nogtans onder die maksimum beton temperatuur van die enkel fase RLSVS vir normale bedryfstoestande. Deur om koking te veroorsaak in die GLTS word die maksimum temperatuur van die vloeier vasgepen gelyk aan die versadigings temperatuur van die vloeier by die vakuüm druk. Hierdie einskap van water word gebruik om 'n limiet te sit op die maksimum temperatuur van die beton. Hierdie e ek kan gesien word in die transiënte gedrag van die RLSVS waar die beton temperatuur styg tot en met koking plaasvind en dan konstant raak ongeag van die hitte belasting op die RLSVS. 'n Toename in die hitte belasting veroorsaak net 'n toename in die kwaliteit van die vloeistof-gas mengsel. Mengsel kwaliteite van 1 nader veroorsaak numeriese onstabiliteite in die teoretiese model. The teoretiese model kan nie die hitteoordrag beskryf na 'n kontrole volume wat 'n digtheid het laer as ongeveer 20 kg/m3. Hierdie plaas 'n limiet op die optimering van die twee fase RLSVS. Aanbevelings was gemaak met betrekking tot toekomstige werk aangaande die verbetering van die teoretiese model met spesi eke klem op die modellering van konveksie in die reaktor asook die modellering van twee fase vloei. Verdere aanbevelings was gemaak aangaande die verbetering van die stralingskerm ontwerp asook die ontwerp van die verkoeling van die GLTSe.