Дисертації з теми "Cooling of coils"

Orientador: Paulo César Razuk
Banca: Augusto Ronchi Junior
Banca: Waldemar Gastoni Venturini Filho
Resumo: A fermentação alcólica, processo central da indústria cervejeira é um processo que libera uma grande quantidade de calor. Sendo assim, os recipientes de fermentação devem estar equipados com instalações de refrigeração para o correto controle da temperatura. A presente pesquisa tem como objetivo a análise da troca de calor de fermentadores cilindrocônicos dotados de sistema de refrigeração direta através de serpentina meia-cana. Para a consecução desse objetivo foi necessária a elaboração de um roteiro de cálculo seguro baseado em equações e experiências encontradas em renomadas literaturas. A análise dos resultados encontrados foi realizada a partir dos valores obtidos através do programa de cálculo atualmente utilizado em uma das maiores empresas fornecedoras deste tipo de equipamento para o mercado cervejeiro, a Dedini Indústrias de Base. Constatou-se que os valores obtidos pelo roteiro apresentado na presente dissertação foram maiores do que os calculados no programa, concluindo-se que as diferenças e dificuldades de resfriamento encontradas em equipamentos semelhantes fornecidos a clientes distintos podem ter origem na quantidade de refrigerante. As estimativas para o coeficiente global de transferência de calor independem do roteiro de cálculo seguido, pois há uma variação máxima de 3,5 % nos resultados para o cálculo deste. O mesmo é verificado para as vazões mássicas de amônia requerida, onde esta variação é ainda menor (cerca de 3,0%)
Abstract: Alcoholic fermentation, brewery industry's central process that liberates a great amount of heat. Therefore, the fermentation containers should be equipped with cooling installations for correct temperature control. The present research aims to analyze the heat exchange in cylindroconical fermenters endowed with a halp-pipe coil direct cooling system. To achieve this objective, the elaboration of a sate calculation route based on equations and experiences found in renowned references was necessary. The validation of the results was accomplished from the values obtained through the calculation program now used in one the largest supplying companies of this kind of equipment for the brewer market, Dedini indústrias de Base. It was verified that the flow of ammonia for the cooling system obtained by the itinerary introduced in the present article was larger than the one calculated in the program, and it can be concluded that the differences and cooling difficulties found in similar equipments supplied to different customers can have origin in the amount of ammonia used in the cooling system. The values for the overal heat transfer coefficient do not depend on the calculation itinerary followed, because there is a maximum variation of 3.5% in the results for the calculation of the coeffiecient. The same is verified for the mass flows of requested ammonia, where this variation is still smaller (about 3.0%)
Mestre

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)
A fermentação alcólica, processo central da indústria cervejeira é um processo que libera uma grande quantidade de calor. Sendo assim, os recipientes de fermentação devem estar equipados com instalações de refrigeração para o correto controle da temperatura. A presente pesquisa tem como objetivo a análise da troca de calor de fermentadores cilindrocônicos dotados de sistema de refrigeração direta através de serpentina meia-cana. Para a consecução desse objetivo foi necessária a elaboração de um roteiro de cálculo seguro baseado em equações e experiências encontradas em renomadas literaturas. A análise dos resultados encontrados foi realizada a partir dos valores obtidos através do programa de cálculo atualmente utilizado em uma das maiores empresas fornecedoras deste tipo de equipamento para o mercado cervejeiro, a Dedini Indústrias de Base. Constatou-se que os valores obtidos pelo roteiro apresentado na presente dissertação foram maiores do que os calculados no programa, concluindo-se que as diferenças e dificuldades de resfriamento encontradas em equipamentos semelhantes fornecidos a clientes distintos podem ter origem na quantidade de refrigerante. As estimativas para o coeficiente global de transferência de calor independem do roteiro de cálculo seguido, pois há uma variação máxima de 3,5 % nos resultados para o cálculo deste. O mesmo é verificado para as vazões mássicas de amônia requerida, onde esta variação é ainda menor (cerca de 3,0%)
Alcoholic fermentation, brewery industry's central process that liberates a great amount of heat. Therefore, the fermentation containers should be equipped with cooling installations for correct temperature control. The present research aims to analyze the heat exchange in cylindroconical fermenters endowed with a halp-pipe coil direct cooling system. To achieve this objective, the elaboration of a sate calculation route based on equations and experiences found in renowned references was necessary. The validation of the results was accomplished from the values obtained through the calculation program now used in one the largest supplying companies of this kind of equipment for the brewer market, Dedini indústrias de Base. It was verified that the flow of ammonia for the cooling system obtained by the itinerary introduced in the present article was larger than the one calculated in the program, and it can be concluded that the differences and cooling difficulties found in similar equipments supplied to different customers can have origin in the amount of ammonia used in the cooling system. The values for the overal heat transfer coefficient do not depend on the calculation itinerary followed, because there is a maximum variation of 3.5% in the results for the calculation of the coeffiecient. The same is verified for the mass flows of requested ammonia, where this variation is still smaller (about 3.0%)

The UK building stock accounts for about half of all energy consumed in the UK. A large portion of the energy is consumed by nondomestic buildings. Offices and retail are the most energy intensive typologies within the nondomestic building sector, typically accounting for over 50% of the nondomestic buildings’ total energy consumption. Heating, ventilating and air conditioning (HVAC) systems are the largest energy end use in the nondomestic sector, with energy consumption close to 50% of total energy consumption. Different HVAC systems have different energy requirements when responding to the same building heating and cooling demands. On the other hand, building heating and cooling demands depend on various parameters such as building fabrics, glazing ratio, building form, occupancy pattern, and many others. HVAC system energy requirements and building energy demands can be determined by mathematical modelling. A widely accepted approach among building professionals is to use building energy simulation tools such as EnergyPlus, IES, DOE2, etc. which can analyse in detail building energy consumption. However, preparing and running simulations in such tools is usually very complicated, time consuming and costly. Their complexity has been identified as the biggest obstacle. Adequate alternatives to complex building energy simulation tools are regression models which can provide results in an easier and faster way. This research deals with the development of regression models that enable the selection of HVAC systems for office buildings. In addition, the models are able to predict annual heating, cooling and auxiliary energy requirements of different HVAC systems as a function of office building heating and cooling demands. For the first part of the data set development used for the regression analysis, a data set of office building simulation archetypes was developed. The four most typical built forms (open plan sidelit, cellular sidelit, artificially lit open plan and composite sidelit cellular around artificially lit open plan built form) were coupled with five types of building fabric and three levels of glazing ratio. Furthermore, two measures of reducing solar heat gains were considered as well as implementation of daylight control. Also, building orientation was included in the analysis. In total 3840 different office buildings were then further coupled with five different HVAC systems: variable air volume system; constant air volume system; fan coil system with dedicated air; chilled ceiling system with embedded pipes, dedicated air and radiator heating; and chilled ceiling system with exposed aluminium panels, dedicated air and radiator heating. The total number of models simulated in EnergyPlus, in order to develop the input database for regression analysis, was 23,040. The results clearly indicate that it is possible to form a reliable judgement about each different HVAC system’s heating, cooling and auxiliary energy requirements based only on office building heating and cooling demands. High coefficients of determination of the proposed regression models show that HVAC system requirements can be predicted with high accuracy. The lowest coefficient of determination among cooling regression models was 0.94 in the case of the CAV system. HVAC system heating energy requirement regression models had a coefficient of determination above 0.96. The auxiliary energy requirement models had a coefficient of determination above 0.95, except in the case of chilled ceiling systems where the coefficient of determination was around 0.87. This research demonstrates that simplified regression models can be used to provide design decisions for the office building HVAC systems studied. Such models allow more rapid determination of HVAC systems energy requirements without the need for time-consuming (hence expensive) reconfigurations and runs of the simulation program.

The diploma thesis aims to prepare a study of the cooling system of a multifunctional building with regard to climate change predicted until the middle of the 21st century. The work includes determining the heat load of refrigerated rooms and designing measures to reduce heat gains in the summer. Diploma thesis includes design of a cooling system with fan-coil units as end appliances with the necessary hydraulic calculations. A single-stage absorption cooling unit is used as the considered cooling source, to which a free cooling heat exchanger is assigned. The design of the cooling source includes the necessary hydraulic calculations and dimensioning of the system ensuring its functional operation. Part of the diploma thesis is drawing documentation of cooling technology and connection of fan-coil units.

På uppdrag av Sundsvall Energi AB har FVB Sverige AB påbörjat en förstudie kring etableringen av fjärrkyla i Sundsvall. Produktionsmedlen i det planerade nätet kommer att innefatta frikyla från akviferen och en kompressordriven kylmaskin. Det övergripande syftet med projektet har dels varit att ta fram en optimal framledningskurva, samt att ta reda på i vilken utsträckning frikylan kan nyttjas innan kylmaskinen måste användas som spetsproduktionsmedel. Projektet har inledningsvis fokuserat på att undersöka hur klimatet och kylbehovet ser uti Sundsvall. Kylbehovet granskades utifrån sex befintliga byggnader som nyttjar dricksvattenkyld fjärrkyla i Sundsvall. Därefter undersöktes olika typer av klimatsystem för att utröna vad de har för krav på framledningstemperaturen. Det konstaterades att kylbatterier var den komponent som kräver lägst framledningstemperatur, varför kyleffektberäkningar utfördes på dem. Resultatet ur kylbatteriberäkningarna fick motsvara den av fjärrkylenätet avgivna kyleffekten vid varierande utomhustemperatur. Genom att väga den avgivna kyleffekten vid varierande framledningstemperatur mot det erforderliga kyleffektbehovet vid varierande utomhustemperatur kunde framledningskurvan ta form. Akviferen antas hålla en temperatur på omkring 7°C till 9°C året runt, men utgångspunkten i detta projekt har varit att den konstant är 9°C. Under de förutsättningarna har framledningstemperaturen kunnat bestämmas till att vara 11°C under större delen av året, men att den sänks vid en utomhustemperatur på omkring 21°C i varierande grad ned till 6°C vid utomhustemperaturen 25°C. Med hjälp av framledningskurvan kunde därefter frikylans täckningsgrad bedömas. Resultatet visar att om framledningens temperatur höjs med 0,5–1,0°C i distributionsnätet kommer kylmaskinen att behöva vara i drift under 159 timmar per år. Om istället uppvärmningen blir 1,5° eller 2,0°C kommer kylmaskinen behöva vara i drift under 233 timmar respektive 325 timmar. Sammantaget har samtliga av projektets konkreta och verifierbara mål besvarats.
On behalf of Sundsvall Energi AB, FVB Sverige AB has initiated a preliminary study on the establishment of a district cooling system in Sundsvall. The main source for the cooling will be cool water drawn from the aquifer and a compressor chiller. The main purpose of this project has both been to provide the optimal supply temperature of the cooling network at different outdoor temperatures, and to find out to what extent the cool water from the aquifer can be used by itself as the cooling source. The project was initially focused on examining the climate and cooling demand in Sundsvall. The cooling demand was examined on the basis of six existing buildings that uses freshwater district cooling, and different types of climatesystems were then examined to ascertain what their requirements for the supply temperature are. Cooling coil batteries were found to be the component that requires the lowest supply temperature; therefore, the cooling power calculations were relied on them. The outcome of the cooling coil battery calculations was presumed to correspond to the cooling power of the network itself. By comparing the cooling power of the coil batteries at different supply temperatures and the cooling demand at different outdoor temperatures the main supply temperature for the district cooling network took shape. The aquifer is expected to maintain a temperature of approximately 7°C to 9°C, but in this project the temperature is set to exactly 9°C. On those premises the supply temperature of the cooling network could be set to 11°C for most of the year, but with a reduction of the supply temperature at outdoor temperatures around 21°C. Subsequently the supply temperature is reduced to 6°C at the outdoor temperature 25°C. Via the supply temperature curve, the aquifer cooling coverage ratio could be assessed. The result shows that if the supply temperature is raised between 0,5°C and 1,0°C in the distribution network the compressor chiller will have to be in operation for 159 hours per year. If instead the supply temperature is raised 1,5°C or 2,0°C, the compressor chiller must be in operation for 233 hours and 325 hours, respectively. In summary, all the goals and targets of the project have been completed.

Les aciers à haute résistance (AHSS) ont été largement utilisés dans le cadre d’applications automobiles visant à améliorer la sécurité et l’allègement des structures. Afin d'atteindre les objectifs en termes de propriétés mécaniques, ces nouveaux aciers sont composés de teneurs en éléments d’alliages beaucoup plus élevés (par exemple silicium et manganèse) que les aciers usuels. En conséquence, l'AHSS est susceptible de subir une oxydation interne sélective lors du refroidissement des bobines d’acier. L'oxydation sélective interne, en particulier l'oxydation aux joints de grains (GBO), est actuellement l'un des principaux obstacles à la production de ces aciers. Elle réduit le nombre de cycles avant la rupture de fatigue et rend ainsi difficile l’obtention des spécifications du client. Par conséquent, ce travail de thèse était axé sur l'effet de plusieurs paramètres sur le comportement à l’oxydation interne sélective. Parmi eux, l'impact de la décarburation, l'influence de la température de bobinage et de la couche de calamine, l'effet de différentes teneurs en silicium et / ou en manganèse et leur comportement en diffusion. De plus, l'impact de la désorientation des joints de grains sur l'oxydation interne a également été étudié. Des alliages modèles à base de fer binaires / ternaires ainsi que des aciers industriels ont été étudiés via un large ensemble de techniques expérimentales. Ces analyses ont mis en évidence une décarburation stable pour tous les échantillons étudiés qui n'a pas d'impact sur l'oxydation interne sélective pour une longue exposition aux conditions isothermes. Les profondeurs d’oxydation aux joints de grain ont été examinées selon les différentes configurations de tests et se sont révélées sensibles aux teneurs en silicium ou en manganèse. Pour certaines d'entre elles, différents comportements de diffusion du silicium ont été identifiés vis-à-vis de l'oxydation des joints de grains, en fonction des températures. Considérant quelques hypothèses restrictives, l'application de la théorie de l'oxydation interne sélective de Wagner a permis de déterminer le coefficient de diffusion de l'oxygène aux joints de grain. Pour surmonter certaines limites du modèle de Wagner, un modèle d'oxydation sélective a été appliqué pour comprendre l'effet de différents paramètres sur la pénétration de l'oxygène à l'intérieur du métal et principalement sur la profondeur des joints de grain affectée par l'oxydation sélective. Les connaissances acquises à partir de ce travail de thèse aideront à comprendre et à limiter l'oxydation sélective interne (principalement l’oxydation aux joints de grain) dans les aciers avec des compositions complexes en éléments d’alliage. En outre, les résultats peuvent être utilisés pour évaluer les paramètres d’un modèle d'oxydation sélective
Advanced high-strength steels (AHSS) have been widely used in automotive industry to improve safety and fuel economy. In order to reach the mechanical properties targets, these new steels are composed by much higher alloy contents (e.g. silicon and manganese) than usual steels. As consequence, the AHSS may suffer of selective internal oxidation during the cooling of hot coil. The selective internal oxidation, especially the grain boundary oxidation (GBO), is currently one of the main obstacles to the production of these steels. It reduces the number of cycles before fatigue failure and thus, makes it difficult to reach the specifications of the customer. Therefore, this PhD work was focused on the effect of several parameters on selective internal oxidation behavior. Among them, the impact of decarburization, the influence of coiling temperature and the mill scale, the effect of different silicon and/or manganese contents and their diffusion behavior. Moreover, the impact of grain boundary misorientation on grain boundary oxidation was also investigated. Either binary/ternary iron-based model alloys as well as industrial steels were investigated by a large set of experimental techniques. This analysis showed a stable decarburization for all investigated samples that does not impact the selective internal oxidation for long exposure time in isothermal conditions. The GBO depths were examined according to the different test configurations and were found dependent for some cases on silicon or manganese content. For some of them, different silicon diffusion behaviors were identified with regards to grain boundary oxidation depending on temperatures. Considering some restrictive hypotheses, the application of Wagner’s theory of selective internal oxidation allowed determining the grain boundary diffusion coefficient of oxygen. To overcome some limitations of Wagner’s model, a model of selective oxidation has been applied to understand the effect of different parameters on the penetration of oxygen inside the metal and principally on the grain boundary depth affected by selective oxidation. The knowledge acquired from this PhD work will help to understand and limit the selective internal oxidation (mainly GBO) in new steels with complex alloy compositions. Furthermore, the results may be used to assess a model of selective oxidation

Beaucoup d'expériences et d'applications utilisant des molécules froides nécessitent d'avoir un échantillon de molécules froides à la fois en translation, en vibration et en rotation. Cette thèse se situe dans la même thématique, elle a pour objectif la généralisation de la méthode du pompage optique qui a permis de refroidir la vibration des molécules de Césium par un laser large bande dont les fréquences correspondantes aux transitions partant du niveau vibrationnel fondamental ont été supprimées. Nous avons, par exemple, réalisé un transfert de la population moléculaire dans un niveau vibrationnel pré-sélectionné. Nous avons ensuite démontré que le refroidissement vibrationnel est aussi efficace avec une source de lumière non cohérente. Enfin, une technique de conversion électronique a été démontrée et qui a permis de transférer les molécules formées dans l'état électronique métastable a3Σu+ vers l'état électronique fondamental X1Σg+. Finalement, l'application de cette méthode sur la rotation a été étudié, les résultats préliminaires montrent que le processus marche efficacement ce qui ouvre des perspectives sur le refroidissement lasers des molécules.

Neste trabalho apresentamos a construção e teste de um sistema experimental que nos permite produzir um fluxo intenso de átomos lentos. Discutimos o desenho e construção do solenóide que compensa o efeito Doppler que surge durante o processo de desaceleração, as câmaras de vácuo, o forno que gera o feixe atômico e o sistema ótico utilizado. Estudamos a técnica de desaceleração de átomos pelo ajuste Zeeman. Uma nova técnica de observação que consiste no acompanhamento da fluorescência do feixe ao longo do caminho de desaceleração é usada, o que nos permite uma observação direta do processo.
This work presents the development and test of an experimental set-up which allows to produce a very strong slow motion atomic beam. We discuss the calculation and construction of the solenoid to compensate the Doppler effect arising during the deceleration process, vacuum chambers, the oven which produces the atomic beam and the optical system used. We have studied the Zeeman-tuned technique to slow an atomic beam of sodium atoms. A new technique to study the deceleration which Consist in monitoring the fluorescence along the deceleration path is used, which allow us a direct observation of the process.

Baigiamajame magistro darbe nagrinėjama problema – dideli energijos poreikiai vėsinimui biurų pastatuose, dėl vis didėjančių mikroklimato kokybės reikalavimų, didesnių šilumos pritekėjimų į patalpas ir šilumos išsiskyrimų dėl naudojamos įrangos. Problemos sprendimui darbe suprojektuotos keturios oro kondicionavimo sistemos su skirtingais šilumnešiais: oru, vandeniu ir freonu. Atsižvelgiant į šilumnešio tipą suprojektuotos ventiliatorinių konvektorių, aktyviųjų šalčio sijų, freoninė ir orinė vėsinimo sistemos. Oro kondicionavimo sistemos analizuojamos remiantis realaus tipinio administracinio pastato pavyzdžiu. Lyginamoms sistemoms buvo atlikti hidrauliniai ir aerodinaminiai skaičiavimai, įvertintos sistemų pradinės investicijos, apskaičiuotos energijos sąnaudos ir eksploatacijos išlaidos. Ekonominio skaičiavimo metu buvo įvertintas sistemų atsipirkimo laikas ir atlikta elektros kainų jautrumo analizė. Šio tyrimo rezultatai parodo, kokia sistema iš visų darbe nagrinėtųjų sistemų yra tinkamiausia biurų pastatams, pagal efektyvų elektros energijos naudojimą ir pradines investicijas.
The final master's work deals with the problem of high energy needs for cooling in office buildings, due to the growing of higher quality requirements for microclimate, higher heat gains in premises and equipment heat emissions used in. To solve the problem four different types of cooling systems with different coolants: air, water and refrigerant are designed at work. Depending on the type of coolant were designed fan coil units, active chilled beams, variable refrigerant volume system and air cooling systems. Air conditioning systems are analyzed on the basis of an example of the real typical office building. The hydraulic and aerodynamic calculations were made, initial investments, energy expenditures and operating costs were estimated for the compared systems. The pay-back time of the systems was assessed and the sensitivity analysis of electricity prices was carried out by economic calculations. The results of this investigation show, which system of all analysed systems at work is the most appropriate for office buildings, according to the efficient use of electricity and the initial investments.

碩士
中原大學
機械工程研究所
95
Abstract This study is focusing what the variation of cooling coils pipe pitch and deposit direction, which will affect the temperature distribution of the epitaxy produce zone for rotation dick type of MOCVD system, the cooling coils is at the bottom of the reaction chamber. In other, we also consider what the different if they has exhaust device at reaction chamber too. From the simulation results, we find the variation factors have no evidence affect. The reason for this result which maybe the reaction chamber and cooling coils temperature differential is so much. In fact, if two sides temperature differential is so much for a heat exchange system, it does not fit the heat exchange system general design rules. In other word, the heat exchange efficient or ability is not the main consider factor, so the simulation results can be accepted. The purpose of the cooling coils is maintain the uniform temperature distribution at the epitaxy produce zone, and let the chip face or thickness are very uniform and accordance. In the past, this design technique is obtained by experiences or testing methods, now they can use numerical simulation technique to approve the tried and test proceed. Especially, they can’t by the traditional design method, ex. geometrical structure or medium flow distribution. This study purpose is used the package software to do many simulation cases, and then to erect many epitaxy process technique or reference index. In addition, for the practice, the operation conditions which for chemical reaction at reaction chamber (ex. mass transfer problem), materials, and reactor exhaust velocity etc, or different produce batch, the temperature of the medium coolant should be cooperate to change. The proceed also can be used analogically this simulation model to simulate a series simulation, to erect the performance or operation diagram of reaction temperature v. s. medium coolant flow rate (or water inlet temperature) for different installations, to provide a set authority for end user or operator. This is another purpose for our study, too.

碩士
國立臺北科技大學
能源與冷凍空調工程系碩士班
99
Makeup air unit (MAU) uses a series of cooling coils for cooling and removing water vapor from the makeup outdoor air. This study uses heat exchanger computer modeling to study the cooling coil design, the chilled water supply temperature, the parallel and series designs of the water loop for two cooling coils. The above variations are investigated for the effects on the energy use of chillers, chilled water pumps, and also supply fans. The total performance and cost effectiveness is assessed under the conditions of satisfying the dew point requirements of clean room operation. It has been found that under parallel flow an increase of 1℃ for chilled water would cause a 7.3% decrease of energy use for the water side, 6.1% for the airside, and 6.7% for the system as a whole. With two different temperatures of chilled water design is used, energy saving for the water side is 30.5%, 28.4% for the airside, and 26.4% for the system as a whole. However when series flow is used the energy use for the water side reduces by 9.9% compared to single temperature paralle flow, but the fan energy increases by 39.9%. As the whole the energy use reduces by 6.4%. However the cost of the coils would increase by 15%. Further when equal chilled water flow rate is used, energy use reduces by 31.4% and 11.9% respectively for the water side and the airside, and 30.5% for the total system. In this case the cost of the coils would increase by about 30%. In comparison parallel flow increases the coil capacity by 1.12 times. Total assessement of cost effectivenss gives the 12℃/5℃parallel flow design a higher merit.

In hot rolled steel strip production the processed material are after the cooling section coiled into coils. Coils do normally weigh around 20 tons with a diameter of 2 m and heights equal to the strip width e.g. 0.8-1.4m. When processing HSLA (High Strength Low Alloy) steel grades the initial/coiling temperature is about 650°C but to achieve the full strength enhancement potential from the subsequent precipitation hardening the cooling history is crucial to control. A too high cooling rate will disable diffusion of alloying elements before the destined material properties have been achieved. This may result in downgraded or in worst case even scraped material. Having comprehensive knowledge of the thermal history is essential in controlling coiled material properties and in understanding root-causes for different mechanisms. A 2D thermo-mechanical FE model has in this licentiate work been developed to predict the transient temperature distribution as a function of position and stress state in coils when cooling. The model accounts for the imperfect and pressure dependent contact conditions between adjacent laps that cause anisotropic thermal properties in radial and axial directions. The imperfect contact is in a macroscopic level caused by oxide, dust, water and strip shape properties inherited from up-stream processes and in a microscopic level by surface conditions like roughness and slope of asperities etc. The stresses formed under coiling and cooling has a strong influence on the contact conditions and the thermal heat conductive properties in radial direction. In this model the total stress state during cooling is approximated as a combination of initial stresses set by the coiler and the thermally induced stresses caused by thermal gradients.The thermo-mechanical model developed and explained in this licentiate thesis has proven to be able to predict the thermal cooling of coils with good agreement in comparison with the performed measurements campaigns. Furthermore does the model form an accurate platform to be used in a continuing work for further investigations where the thermal trajectory and stresses have an influence e.g. on coil-set effects as length and cross bow or mechanical properties.

Godkänd; 2014; 20141127 (vith); Nedanstående person kommer att hålla licentiatseminarium för avläggande av teknologie licentiatexamen. Namn: Mats Karlberg Ämne: Materialmekanik/Material Mechanics Uppsats: Thermo-Mechanical Modelling of Hot Strip Coil Cooling Process Examinator: Professor Lars-Erik Lindgren, Institutionen för teknikvetenskap och matematik, Luleå tekniska universitet Diskutant: Tekn dr Daniel Berglund, Gestamp Hardtech AB, Luleå Tid: Torsdag den 18 december 2014 kl 11,00 Plats: C305, Luleå tekniska universitet

The controlled cooling of steel strips is required to attain the high quality standards of flat-rolled steels employed in important industries such as the automobile, petro-chemical, house-appliances and construction. Strict control of the temperature of the strip during cooling in the hot-strip runout table is necessary, but little success has been reached in the optimization of the heat removal since no real understanding of the physical mechanisms involved has been attained. Given that the experimental measurements of the local heat-transfer coefficients may involve very complex procedures, the modeling of the boiling mechanisms is presented as the best way to obtain the local thermal response of steel strips during their processing, and mathematical models for the runout table and subsequent coil cooling are presented as powerful tools to predict the thermal and the microstructural response of the steel. The runout table model is unique in the sense that it is mechanistic in nature and predicts the local heat-transfer coefficients during cooling. The model adopts the extrapolation of the "macrolayer evaporation mechanism" into the forced-flow transition boiling regime. The analysis in terms of the nucleation process, fluid flow, liquid-solid contact area, and the liquid-vapor interface instability allow succesful prediction of pilotplant and full-scale operations and of the most fundamental microscopic parameters measured elsewhere. The liquid-solid contact found in the transition boiling regime is responsible for most of the heat released, and explains why previous assumptions with regard to film boiling failed to account for the effect of variables such as water temperature or strip velocity on the cooling process. This study shows that bottom jet cooling is much lower than top cooling not only because of the smaller contact but also because of the inherently lower stability of the liquid-vapor interface of the latter.

碩士
國立臺北科技大學
冷凍與低溫科技研究所
89
This research is to investigate the defect of an air conditioner that evaporates and blows the moisture on the cooling coil back to the room space during compressor off cycle. This results are in thermal discomfort owning to the rising of humidity inside conditioned space. Experiments and numerical simulations were performed with changing various parameters such as coil layout, supply air velocity, fin pitch, evaporator coil spacing tube diameter and its surface temperature. In order to reduce the moisture blowing back to the minimal extend. Two window-type air conditioners A and B were tested and the temperatures on cooling coil and air side, air flow rate as well as power consumptions under various conditions were obtained. The experimental results show that the amount of condensate on coil evaporating back to room space is very small using the newer air conditioner A for the hydrophilic coating of evaporator coil. It is also found that the refrigerant equilibrium time needed upon compressor sheeting down is about 30 minutes. On the other hand, the moisture blowing back to the space makes the cooling load rising about 19﹪ at supply air flow rate 193.8 CFM during the 30 minutes of equilibrium time when using the order air conditioner B. A 3D simulation model was also established based on computational fluid dynamics to evaluate this phenomena. The numerical results using B as benchmark shows that, the restrain of total heat blowing back when off cycle under various conditions. When the coil layout was changed from staggered type to in-line type, the air velocity decreased from 1.182m/s to 0.4m/s, the fin pitch was changed from 14FPI (fin per inch) to 10FPI, tube surface temperature was changed are 0.3﹪, 1.1﹪, 1.5﹪and 80﹪ respectively. While the effects of changing evaporator tube spacing and diameter on reducing the total heat blowing back are very small.