987 resultados para tube-fin heat exchanger


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Stricter environmental policies are shown necessary to ensure an effective pollutant emission control. It is expected for the present year of 2015, that Brazil will assume, at the 21th United Nation's Climate Change Conference (COP21), implementation of commitment to a low carbon economy. This positioning affects the industrial environment, so that is deemed necessary to search for new technologies, less aggressive to the environment, so the adequacies to the new emission policies do not cause a negative effect on production. Almost all of the processes performed in the steel industry demand burning fuel and, therefore, flue gases are sent to the atmosphere. In this present work is discussed the utilization of heat exchangers so, by recovering part of the available heat from the flue gases of certain industrial process, the combustion air is preheated. The combustion air preheat results in less energy requirement, i.e., less need of fuel consumption and, in addition, minor amount of pollutants to be emitted. Due to better fitting to the process, it is studied the utilization of spiral plate heat exchangers. The heat exchanger dimensioning is made by an iterative method implemented in the software Microsoft Excel. Subsequently are analyzed the gains in terms of process's thermal efficiency improvement and the percentage of fuel saving. The latter implies in reduction of the same percentage of greenhouse gases emission

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This study aims to analyze the capacity of a helical coil heat exchanger to reach the requested heat transfer rates by a sodium hypochlorite production process. This heat exchanger was installed in an experimental way in order to reuse a source of low-temperatures water in such a way to become a more economical alternative than the existing cooling tower. Firstly, the concepts related to the theory of heat transfer applicable to the case were introduced. Then, the mapping of the main information about the production process and the technical specification of the current cooling system equipment's was realized. Using the dimensions of the heat exchanger installed today as reference, the calculations for determining the ideal length of the coil to different flows of hot fluid were performed. Finally, it was concluded that the heat exchanger currently employed does not provide heat transfer rates required for the maximum flow rate value supported by the cooling tower

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The modernization of the world made the speed, accuracy and reliability of all existing processes become increasingly necessary. For this evolution to occur every day, the evolution of the equipment was strategic, but not as much as needed. It is necessary for such equipment to ensure its function and, in case of failure, an early diagnosis to prevent loss. Therefore the evolution of maintainability and reliability in equipment is also paramount. Thus, the growth of forms of maintenance was driven by this scenario, forming maintenance philosophies. Among many, there is the RCM, which have its focus on the identification, parameters development and performance preview. One of those methodologies from this idea is the FMEA, process that has been studied and implemented this work, aiming the anticipation of failure modes and guidance for the use of a heat exchanger and a pump. This implementation has the aid of another process of RCM, the PHA, which was also shown and implemented, these results being used to start the FMEA process. The results show the activities with the highest chance of failure, presenting also the measures to be taken to avoid or minimize them. It is shown, in this paper, concern with the valves because they maintain control and system security, and its flaws related to accidents with possible danger to people and the whole system, emphasizing the priority of action

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The classic conservative approach for thermal process design can lead to over-processing, especially for laminar flow, when a significant distribution of temperature and of residence time occurs. In order to optimize quality retention, a more comprehensive model is required. A model comprising differential equations for mass and heat transfer is proposed for the simulation of the continuous thermal processing of a non-Newtonian food in a tubular system. The model takes into account the contribution from heating and cooling sections, the heat exchange with the ambient air and effective diffusion associated with non-ideal laminar flow. The study case of soursop juice processing was used to test the model. Various simulations were performed to evaluate the effect of the model assumptions. An expressive difference in the predicted lethality was observed between the classic approach and the proposed model. The main advantage of the model is its flexibility to represent different aspects with a small computational time, making it suitable for process evaluation and design. (C) 2012 Elsevier Ltd. All rights reserved.

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The research activity described in this thesis is focused mainly on the study of finite-element techniques applied to thermo-fluid dynamic problems of plant components and on the study of dynamic simulation techniques applied to integrated building design in order to enhance the energy performance of the building. The first part of this doctorate thesis is a broad dissertation on second law analysis of thermodynamic processes with the purpose of including the issue of the energy efficiency of buildings within a wider cultural context which is usually not considered by professionals in the energy sector. In particular, the first chapter includes, a rigorous scheme for the deduction of the expressions for molar exergy and molar flow exergy of pure chemical fuels. The study shows that molar exergy and molar flow exergy coincide when the temperature and pressure of the fuel are equal to those of the environment in which the combustion reaction takes place. A simple method to determine the Gibbs free energy for non-standard values of the temperature and pressure of the environment is then clarified. For hydrogen, carbon dioxide, and several hydrocarbons, the dependence of the molar exergy on the temperature and relative humidity of the environment is reported, together with an evaluation of molar exergy and molar flow exergy when the temperature and pressure of the fuel are different from those of the environment. As an application of second law analysis, a comparison of the thermodynamic efficiency of a condensing boiler and of a heat pump is also reported. The second chapter presents a study of borehole heat exchangers, that is, a polyethylene piping network buried in the soil which allows a ground-coupled heat pump to exchange heat with the ground. After a brief overview of low-enthalpy geothermal plants, an apparatus designed and assembled by the author to carry out thermal response tests is presented. Data obtained by means of in situ thermal response tests are reported and evaluated by means of a finite-element simulation method, implemented through the software package COMSOL Multyphysics. The simulation method allows the determination of the precise value of the effective thermal properties of the ground and of the grout, which are essential for the design of borehole heat exchangers. In addition to the study of a single plant component, namely the borehole heat exchanger, in the third chapter is presented a thorough process for the plant design of a zero carbon building complex. The plant is composed of: 1) a ground-coupled heat pump system for space heating and cooling, with electricity supplied by photovoltaic solar collectors; 2) air dehumidifiers; 3) thermal solar collectors to match 70% of domestic hot water energy use, and a wood pellet boiler for the remaining domestic hot water energy use and for exceptional winter peaks. This chapter includes the design methodology adopted: 1) dynamic simulation of the building complex with the software package TRNSYS for evaluating the energy requirements of the building complex; 2) ground-coupled heat pumps modelled by means of TRNSYS; and 3) evaluation of the total length of the borehole heat exchanger by an iterative method developed by the author. An economic feasibility and an exergy analysis of the proposed plant, compared with two other plants, are reported. The exergy analysis was performed by considering the embodied energy of the components of each plant and the exergy loss during the functioning of the plants.

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BTES (borehole thermal energy storage)systems exchange thermal energy by conduction with the surrounding ground through borehole materials. The spatial variability of the geological properties and the space-time variability of hydrogeological conditions affect the real power rate of heat exchangers and, consequently, the amount of energy extracted from / injected into the ground. For this reason, it is not an easy task to identify the underground thermal properties to use when designing. At the current state of technology, Thermal Response Test (TRT) is the in situ test for the characterization of ground thermal properties with the higher degree of accuracy, but it doesn’t fully solve the problem of characterizing the thermal properties of a shallow geothermal reservoir, simply because it characterizes only the neighborhood of the heat exchanger at hand and only for the test duration. Different analytical and numerical models exist for the characterization of shallow geothermal reservoir, but they are still inadequate and not exhaustive: more sophisticated models must be taken into account and a geostatistical approach is needed to tackle natural variability and estimates uncertainty. The approach adopted for reservoir characterization is the “inverse problem”, typical of oil&gas field analysis. Similarly, we create different realizations of thermal properties by direct sequential simulation and we find the best one fitting real production data (fluid temperature along time). The software used to develop heat production simulation is FEFLOW 5.4 (Finite Element subsurface FLOW system). A geostatistical reservoir model has been set up based on literature thermal properties data and spatial variability hypotheses, and a real TRT has been tested. Then we analyzed and used as well two other codes (SA-Geotherm and FV-Geotherm) which are two implementation of the same numerical model of FEFLOW (Al-Khoury model).

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Il Test di Risposta Termica (Thermal Response Test-TRT) (Mogenson,1983) è il test esistente con il più alto grado di accuratezza per la caratterizzazione del reservoir geotermico superficiale. Il test consiste in una simulazione in situ del funzionamento di un sistema a circuito chiuso di sfruttamento dell’energia geotermica, per un periodo limitato di tempo, attraverso l’iniezione o estrazione di calore a potenza costante all’interno del geo-scambiatore (Borehole Heat Exchanger-BHE). Dall’analisi della variazione delle temperature del fluido circolante, è possibile avere una stima delle proprietà termiche medie del volume del reservoir geotermico interessato dal test. Le grandezze principali per la caratterizzazione di un serbatoio geotermico sono la conduttività termica (λ), la capacità termica volumetrica (c), la temperatura indisturbata del suolo (Tg) e la resistenza termica del pozzo (Rb); la loro determinazione è necessaria per il corretto progettazione degli geo-scambiatori. I risultati del TRT sono tuttavia sensibili alle condizioni al contorno spazio-temporali quali ad es.: variazione della temperatura del terreno, movimento d’acqua di falda, condizioni metereologiche, eventi stagionali, ecc. Questo lavoro vuole: i) introdurre uno studio sui problemi di caratterizzazione del reservoir geotermico superficiale, in particolare analizzando l’effetto che il movimento d’acqua di falda ha sui parametri termici; ii) analizzare la sensitività dei risultati del test alle variabilità dei parametri caratteristici del funzionamento delle attrezzature. Parte del lavoro della mia tesi è stata svolta in azienda per un periodo di 4 mesi presso la “Groenholland Geo Energy systems” che ha sede ad Amsterdam in Olanda. Tre diversi esperimenti sono stati realizzati sullo stesso sito (stratigrafia nota del terreno: argilla, sabbia fine e sabbia grossa) usando una sonda profonda 30 metri e diversi pozzi per l’estrazione d’acqua e per monitorare gli effetti in prossimità del geo scambiatore. I risultati degli esperimenti sono stati molto diversi tra di loro, non solo in termini di dati registrati (temperature del fluido termovettore), ma in termini dei valori dei parametri ottenuti elaborando i dati. In particolare non è sufficiente adottare il modello classico della sorgente lineare infinita (Infinite Line Source Solution- ILS) (Ingersoll and Plass, 1948), il quale descrive il trasferimento di calore per conduzione in un mezzo omogeneo indefinito a temperatura costante. Infatti, lo scambio di calore avviene anche tramite convezione causata dal movimento d’acqua di falda, non identificabile mediante gli approcci classici tipo CUSUM test (Cumulative Sum test) (Brown e altri,1975) Lo studio della tesi vuole dare un quadro di riferimento per correlare la variabilità dei risultati con la variabilità delle condizioni al contorno. L’analisi integra le metodologie classiche (ILS) con un approccio geostatistico utile a comprendere i fenomeni e fluttuazioni che caratterizzano il test. Lo studio delle principali variabili e parametri del test, quali temperatura in ingresso e uscita del fluido termovettore, portata del fluido e potenza iniettata o estratta, è stato sviluppato mediante: il variogramma temporale, ovvero la semivarianza dell’accrescimento, che esprime il tipo di autocorrelazione temporale della variabile in esame; la covarianza incrociata temporale, ovvero la covarianza fra due variabili del sistema, che ne definisce quantitativamente il grado di correlazione in funzionamento del loro sfasamento temporale. L’approccio geostatistico proposto considera la temperatura del fluido Tf come una funzione aleatoria (FA) non stazionaria nel tempo (Chiles, 1999), il cui trend è formalmente definito, ma deve essere identificato numericamente. Si considera quindi un classico modello a residuo; in cui la FA è modellizzata come la somma di un termine deterministico, la media (il valore atteso) m(t),coincidente col modello descritto dalla teoria della sorgente lineare infinità, e di un termine aleatorio, la fluttuazione, Y(t). Le variabili portata e potenza sono invece considerate delle funzioni aleatorie stazionarie nel tempo, ovvero a media costante. Da questo studio di Tesi si sono raggiunte delle conclusioni molto importanti per lo studio del TRT: Confronto tra gli esperimenti in estrazione di calore, con e senza movimento d’acqua di falda: si studia l’effetto indotto dalla falda sul TRT. E’ possibile caratterizzare quantitativamente l’incremento della conducibilità termica equivalente legata a fenomeni convettivi dovuti al movimento d’acqua di falda. Inoltre, i variogrammi sperimentali evidenziano periodicità simili nei due casi e legate al funzionamento della pompa di calore e della componentistica associata ed alla circolazione del fluido termovettore all’interno della sonda. Tuttavia, la componente advettiva ha un effetto di smorzamento sulle piccole periodicità dei variogrammi, ma di aumento dell’ampiezza delle periodicità maggiori a causa del funzionamento della pompa di calore che deve fornire maggiore energia al sistema per bilanciare le dispersioni dovute al movimento d’acqua di falda. Confronto fra estrazione ed iniezione di calore, con movimento d’acqua di falda: si studia la significatività dei risultati nei due casi. L’analisi delle variografie evidenzia significative differenze nella struttura dei variogrammi sperimentali. In particolare, nel test con iniezione di calore i variogrammi sperimentali delle temperature hanno valori sistematicamente inferiori, circostanza che assicura una migliore precisione nella stima dei parametri termici. Quindi eseguire il TRT in iniezione di calore risulta più preciso. Dall’analisi dei variogrammi sperimentali delle singole variabili quali temperatura del fluido in ingresso e uscita all’interno del geoscambiatore è stato confermato il fenomeno di smorzamento delle oscillazioni da parte del terreno. Dall’analisi delle singole variabili del test (temperature, potenza, portata) è stata confermata l’indipendenza temporale fra portate e temperature. Ciò è evidenziato dalle diverse strutture dei variogrammi diretti e dalle covarianze incrociate prossime a zero. Mediante correlogrami è stato dimostrato la possibilità di calcolare il tempo impiegato dal fluido termovettore per circolare all’interno della sonda. L’analisi geostatistica ha permesso quindi di studiare in dettaglio la sensitività dei risultati del TRT alle diverse condizioni al contorno, quelle legate al reservoir e quelle legate al funzionamento delle attrezzature

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Die oberflächennahe Geothermie leistet im Bereich der Nutzung regenerativer Wärme einen wichtigen Beitrag zum Klima- und Umweltschutz. Um die technische Nutzung oberflächennaher Geothermie zu optimieren, ist die Kenntnis der Beschaffenheit des geologischen Untergrundes ausschlaggebend. Die vorliegende Dissertation befasst sich mit der Bestimmung verschiedener Untergrundparameter an einem Erdwärmesondenfeld. Es wurden Untersuchungen zur Bestimmung der Wärmeleitfähigkeit wie der enhanced Thermal Response Test (eTRT), sowie eine Untergrund-Temperaturüberwachung im ersten Betriebsjahr durchgeführt. Die Überwachung zeigte keine gegenseitige Beeinflussung einzelner Sonden. Ein Vergleich zwischen dem geplanten und dem tatsächlichem Wärmebedarf des ersten Betriebsjahres ergab eine Abweichung von ca. 35%. Dies zeigt, dass die Nutzungsparameter der Anlage deren Effizienz maßgeblich beeinflussen können. Der am Beispielobjekt praktisch durchgeführte eTRT wurde mittels numerischer Modellierung auf seine Reproduzierbarkeit hin überprüft. Bei einem rein konduktiven Wärmetransport im Untergrund betrug die maximale Abweichung der Messung selbst unter ungünstigen Bedingungen lediglich ca. 6% vom zu erwartenden Wert. Die Detektion von grundwasserdurchflossenen Schichten ist in den Modellen ebenfalls gut abbildbar. Problematisch bleibt die hohe Abhängigkeit des Tests von einer konstanten Wärmezufuhr. Lediglich die Bestimmung der Wärmeleitfähigkeit über das Relaxationsverhalten des Untergrundes liefert bei Wärmeeintragsschwankungen hinreichend genaue Ergebnisse. Die mathematische Nachbearbeitung von fehlerhaften Temperaturkurven bietet einen Einstiegspunkt für weiterführende Forschung.

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Solar energy is the most abundant persistent energy resource. It is also an intermittent one available for only a fraction of each day while the demand for electric power never ceases. To produce a significant amount of power at the utility scale, electricity generated from solar energy must be dispatchable and able to be supplied in response to variations in demand. This requires energy storage that serves to decouple the intermittent solar resource from the load and enables around-the-clock power production from solar energy. Practically, solar energy storage technologies must be efficient as any energy loss results in an increase in the amount of required collection hardware, the largest cost in a solar electric power system. Storing solar energy as heat has been shown to be an efficient, scalable, and relatively low-cost approach to providing dispatchable solar electricity. Concentrating solar power systems that include thermal energy storage (TES) use mirrors to focus sunlight onto a heat exchanger where it is converted to thermal energy that is carried away by a heat transfer fluid and used to drive a conventional thermal power cycle (e.g., steam power plant), or stored for later use. Several approaches to TES have been developed and can generally be categorized as either thermophysical (wherein energy is stored in a hot fluid or solid medium or by causing a phase change that can later be reversed to release heat) or thermochemical (in which energy is stored in chemical bonds requiring two or more reversible chemical reactions).

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A Probabilistic Safety Assessment (PSA) is being developed for a steam-methane reforming hydrogen production plant linked to a High-Temperature Gas Cooled Nuclear Reactor (HTGR). This work is based on the Japan Atomic Energy Research Institute’s (JAERI) High Temperature Test Reactor (HTTR) prototype in Japan. This study has two major objectives: calculate the risk to onsite and offsite individuals, and calculate the frequency of different types of damage to the complex. A simplified HAZOP study was performed to identify initiating events, based on existing studies. The initiating events presented here are methane pipe break, helium pipe break, and PPWC heat exchanger pipe break. Generic data was used for the fault tree analysis and the initiating event frequency. Saphire was used for the PSA analysis. The results show that the average frequency of an accident at this complex is 2.5E-06, which is divided into the various end states. The dominant sequences result in graphite oxidation which does not pose a health risk to the population. The dominant sequences that could affect the population are those that result in a methane explosion and occur 6.6E-8/year, while the other sequences are much less frequent. The health risk presents itself if there are people in the vicinity who could be affected by the explosion. This analysis also demonstrates that an accident in one of the plants has little effect on the other. This is true given the design base distance between the plants, the fact that the reactor is underground, as well as other safety characteristics of the HTGR. Sensitivity studies are being performed in order to determine where additional and improved data is needed.

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Efficient high speed propulsion requires exploiting the cooling capability of the cryogenic fuel in the propulsion cycle. This paper presents the numerical model of a combined cycle engine while in air turbo-rocket configuration. Specific models of the various heat exchanger modules and the turbomachinery elements were developed to represent the physical behavior at off-design operation. The dynamic nature of the model allows the introduction of the engine control logic that limits the operation of certain subcomponents and extends the overall engine operational envelope. The specific impulse and uninstalled thrust are detailed while flying a determined trajectory between Mach 2.5 and 5 for varying throttling levels throughout the operational envelope.

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Direct Steam Generation (DSG) in Linear Fresnel (LF) solar collectors is being consolidated as a feasible technology for Concentrating Solar Power (CSP) plants. The competitiveness of this technology relies on the following main features: water as heat transfer fluid (HTF) in Solar Field (SF), obtaining high superheated steam temperatures and pressures at turbine inlet (500ºC and 90 bar), no heat tracing required to avoid HTF freezing, no HTF degradation, no environmental impacts, any heat exchanger between SF and Balance Of Plant (BOP), and low cost installation and maintenance. Regarding to LF solar collectors, were recently developed as an alternative to Parabolic Trough Collector (PTC) technology. The main advantages of LF are: the reduced collector manufacturing cost and maintenance, linear mirrors shapes versus parabolic mirror, fixed receiver pipes (no ball joints reducing leaking for high pressures), lower susceptibility to wind damages, and light supporting structures allowing reduced driving devices. Companies as Novatec, Areva, Solar Euromed, etc., are investing in LF DSG technology and constructing different pilot plants to demonstrate the benefits and feasibility of this solution for defined locations and conditions (Puerto Errado 1 and 2 in Murcia Spain, Lidellin Newcastle Australia, Kogran Creek in South West Queensland Australia, Kimberlina in Bakersfield California USA, Llo Solar in Pyrénées France,Dhursar in India,etc). There are several critical decisions that must be taken in order to obtain a compromise and optimization between plant performance, cost, and durability. Some of these decisions go through the SF design: proper thermodynamic operational parameters, receiver material selection for high pressures, phase separators and recirculation pumps number and location, pipes distribution to reduce the amount of tubes (reducing possible leaks points and transient time, etc.), etc. Attending to these aspects, the correct design parameters selection and its correct assessment are the main target for designing DSG LF power plants. For this purpose in the recent few years some commercial software tools were developed to simulatesolar thermal power plants, the most focused on LF DSG design are Thermoflex and System Advisor Model (SAM). Once the simulation tool is selected,it is made the study of the proposed SFconfiguration that constitutes the main innovation of this work, and also a comparison with one of the most typical state-of-the-art configuration. The transient analysis must be simulated with high detail level, mainly in the BOP during start up, shut down, stand by, and partial loads are crucial, to obtain the annual plant performance. An innovative SF configurationwas proposed and analyzed to improve plant performance. Finally it was demonstrated thermal inertia and BOP regulation mode are critical points in low sun irradiation day plant behavior, impacting in annual performance depending on power plant location.

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The supercritical Rankine power cycle offers a net improvement in plant efficiency compared with a subcritical Rankine cycle. For fossil power plants the minimum supercritical steam turbine size is about 450MW. A recent study between Sandia National Laboratories and Siemens Energy, Inc., published on March 2013, confirmed the feasibility of adapting the Siemens turbine SST-900 for supercritical steam in concentrated solar power plants, with a live steam conditions 230-260 bar and output range between 140-200 MWe. In this context, this analysis is focused on integrating a line-focus solar field with a supercritical Rankine power cycle. For this purpose two heat transfer fluids were assessed: direct steam generation and molten salt Hitec XL. To isolate solar field from high pressure supercritical water power cycle, an intermediate heat exchanger was installed between linear solar collectors and balance of plant. Due to receiver selective coating temperature limitations, turbine inlet temperature was fixed 550ºC. The design-point conditions were 550ºC and 260 bar at turbine inlet, and 165 MWe Gross power output. Plant performance was assessed at design-point in the supercritical power plant (between 43-45% net plant efficiency depending on balance of plantconfiguration), and in the subcritical plant configuration (~40% net plant efficiency). Regarding the balance of plant configuration, direct reheating was adopted as the optimum solution to avoid any intermediate heat exchanger. One direct reheating stage between high pressure turbine and intermediate pressure turbine is the common practice; however, General Electric ultrasupercritical(350 bar) fossil power plants also considered doubled-reheat applications. In this study were analyzed heat balances with single-reheat, double-reheat and even three reheating stages. In all cases were adopted the proper reheating solar field configurations to limit solar collectors pressure drops. As main conclusion, it was confirmed net plant efficiency improvements in supercritical Rankine line-focus (parabolic or linear Fresnel) solar plant configurations are mainly due to the following two reasons: higher number of feed-water preheaters (up to seven)delivering hotter water at solar field inlet, and two or even three direct reheating stages (550ºC reheating temperature) in high or intermediate pressure turbines. However, the turbine manufacturer should confirm the equipment constrains regarding reheating stages and number of steam extractions to feed-water heaters.

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El consumo de energía es responsable de una parte importante de las emisiones a la atmósfera de CO2, que es uno de los principales causantes del efecto invernadero en nuestro planeta. El aprovechamiento de la energía solar para la producción de agua caliente, permite economizar energía y disminuir el impacto del consumo energético sobre el medio ambiente y por tanto un menor impacto medioambiental. El objetivo de la presente investigación consiste en estudiar el aprovechamiento solar para el calentamiento de los fangos en los digestores anaerobios mediante agua caliente circulando en el interior de un serpentín que rodea la superficie de dicho digestor, como apoyo a los métodos convencionales del calentamiento de fangos como la resistencia eléctrica o el intercambiador de calor mediante la energía obtenida por el gas metano producido en la digestión anaerobia. Para el estudio se utilizaron 3 digestores, dos delos cuales se calentaron con agua caliente en el interior de un serpentín (uno aislado mediante una capa de fibra de vidrio y poliuretano y otro sin aislar).El tercer digestor no tenía calentamiento exterior con el objetivo de observar su comportamiento y comparar su evolución con el resto de los digestores .La comparación de los digestores 1 y 2 nos permitió estudiar la conveniencia de proveer de aislamiento al digestor. La transferencia de calor mediante serpentín de cobre dio valores comprendidos entre 83 y 92%. La aplicación de la instalación a una depuradora a escala real para mantenimiento en el interior del digestor a T=32ºC en diferentes climas: climas templados, cálidos y fríos, consistió en el cálculo de la superficie de colectores solares y superficie de serpentín necesario para cubrir las necesidades energéticas anuales de dicho digestor, así como el estudio de rentabilidad de la instalación, dando los mejores resultados para climas cálidos con períodos de retorno de 12 años y una tasa interna de rentabilidad (TIR) del 16% obteniendo una cobertura anual del 79% de las necesidades energéticas con energía solar térmica. Energy consumption accounts for a significant part of the emissions of CO2, which is one of the main causes of the greenhouse effect on our planet. The use of solar energy for hot water production. can save energy and reduce the impact of energy consumption on the environment and therefore a reduced environmental impact. The objective of this research is to study the solar utilization for heating the sludge in anaerobic digesters by hot water circulating inside a coil surrounding the surface of digester, to support conventional heating methods sludge as the electrical resistance or heat exchanger by energy generated by the methane gas produced in the anaerobic digestion. To study 3 digesters used two models which are heated with hot water within a coil (one insulated by a layer of fiberglass and polyurethane and other uninsulated) .The third digester had no external heating in order to observe their behavior and compare their evolution with the rest of the .The comparison digesters digesters 1 and 2 allowed us to study the advisability of providing insulation to the digester. Heat transfer through copper coil gave values between 83 and 92%. The installation application to a treatment for maintaining full scale within the digester at T = 32ºC in different climates: temperate, warm and cold climates, consisted of calculating the surface area of solar collectors and coil required to cover the annual energy needs of the digester, and the study of profitability of the installation, giving the best results for hot climates with return periods of 12 years and an internal rate of return (IRR) of 16% achieving an annual coverage of 79 % of energy needs with solar energy.

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In endotherms insects, the thermoregulatory mechanisms modulate heat transfer from the thorax to the abdomen to avoid overheating or cooling in order to obtain a prolonged flight performance. Scarabaeus sacer and S. cicatricosus, two sympatric species with the same habitat and food preferences, showed daily temporal segregation with S. cicatricosus being more active during warmer hours of the day in opposition to S. sacer who avoid it. In the case of S. sacer, their endothermy pattern suggested an adaptive capacity for thorax heat retention. In S. cicatricosus, an active ‘heat exchanger’ mechanism was suggested. However, no empirical evidence had been documented until now. Thermographic sequences recorded during flight performance showed evidence of the existence of both thermoregulatory mechanisms. In S. sacer, infrared sequences showed a possible heat insulator (passive thermal window), which prevents heat transfer from meso- and metathorax to the abdomen during flight. In S. cicatricosus, infrared sequences revealed clear and effective heat flow between the thorax and abdomen (abdominal heat transfer) that should be considered the main mechanism of thermoregulation. This was related to a subsequent increase in abdominal pumping (as a cooling mechanism) during flight. Computer microtomography scanning, anatomical dissections and internal air volume measurements showed two possible heat retention mechanisms for S. sacer; the abdominal air sacs and the development of the internal abdominal sternites that could explain the thermoregulation between thorax and abdomen. Our results suggest that interspecific interactions between sympatric species are regulated by very different mechanisms. These mechanisms create unique thermal niches for the different species, thereby preventing competition and modulating spatio-temporal distribution and the composition of dung beetle assemblages.