M.Ing. / A one-year investigation on hot water consumption was conducted in South African developed and developing communities of Johannesburg to determine the personal and household average daily consumption of hot water as well as the average hourly (in summer and in winter) and monthly patterns. The motivation for this research project was to provide to engineers and water heaters manufacturers reliable experimental data on hot water consumption from various categories of dwellings. The existing sources of information in South Africa being extremely limited and results of estimations. The necessary information was collected from hourly and monthly measurements taken by monitoring hot water systems in different dwellings including, houses (300 units), traditional houses (90 units), shacks (200 units), apartments (123 units), townhouses (90 units). For the purpose of this study, the selected (not statistically) dwellings were classified into three categories, which are: high-density dwellings representing the developing communities, medium-density and low-density dwellings which represent the developed communities. The results of measurements show that, in general, people living in developed communities (low-density dwellings) use at least 1.4 times more hot water than those of developing communities (high-density dwellings). The patterns of hot water consumption have been determined for monthly and hourly consumption. The former is divided in four sections: summer weekdays, winter weekdays, summer weekends and winter weekends. The differences between sections are the specific times of peaks and the consumption. The results of this study should be of great assistance to engineers and water heaters designers in analysing existing systems for performance improvement, and in sizing more efficient and suitable systems to South African use.

The main topic of thesis is a measurement realized on the fireplace-insert. Thesis is consists of three parts. First part is focused on wood combustion and overview of fireplace-inserts construction. Second part contains the description of fireplace-insert Bety and accomplished construction changes. Third and main part is consists from measurements, calculations and finally assessments of measurement´s configurations.

This thesis deals with the fuel change for hot water boilers with wattage of 116.3 MW. At first a stoichiometric calculation is drawn. Calculation of pressure loss in pipeline follows. Consequential part elaborates on calculation of parallel connected heating surfaces following with a draft of regenerative air heater Ljungtröm. Conclusively, a calculation is carried out to verify the functionality of the serial connection of the heating surfaces.

The building Norra Djurgården 43:12 on the main campus of the Royal Institute of Technology (KTH)  in Stockholm will be retrofitted as students from the exter- nal campus Haninge will be moved there. This occasion is supposed to be used to improve the facility’s energy efficiency. Potential for this exists for both the space and the water heating system. The effect of decreasing the supply temperature to the radiators was examined  based on equations for the heat transfer. It was calcu- lated that lowering the supply temperature by 5 K would reduce the space heating demand by 25 %, i.e. 94.25 MWh a−1  and avoid emissions of 9.9 t CO2 a−1. Due to high heat losses from the secondary district heating circuit on KTH property to the ground, an alternative for the domestic hot water supply at times without space heating demand, i.e. from May to September, was considered.  Two systems were designed which can completely cover the demand and were evaluated in terms of both energy and economic efficiency. The daily domestic hot water demand  as well as the peak demand were modelled especially for this purpose. A system com- prising ten flat panel solar thermal collectors with a total aperture area of 23.3 m2 and an auxiliary heat pump of 7.5 kW capacity was calculated to achieve a maximum coefficient of performance (COP) of 9.13 in June. In spite of the low operation cost, the system has a negative Net Present Value as the fixed capital investment is very high. The more competitive option is the installation of a heat pump of 12.22 kW capacity which is supposed to use waste heat from the server room.  If both the cooling power and the heating  power are considered as the benefit, the Net Present Value calculates to about 274,500 SEK, otherwise it is still almost 99,000 SEK (ap- proximately 32,000 EUR and 11,500 EUR respectively).  These figures are based on an operation cycle of one year, i.e. if the heat pump contributes to the space heating supply from October to March. Compared to the use of outside air as a heat source, the COP is increased by 83 % or 10 % respectively, depending on the definition of the benefit. The reduction in the district heating demand calculated to 24.48 MWh a−1 provided the building can be disconnected from the KTH distribution network from May to September. At the same time, emissions of 2.57 t CO2 a−1  could be avoided. In conclusion, the installation of a heat pump using waste heat from the server room appears to be a solution which is both energy efficient and economical. / Das Gebäude Norra Djurgården  43:12 auf dem Hauptcampus der Königlichen Tech- nischen Hochschule (KTH)  in Stockholm wird renoviert werden, da der Vorlesungs- betrieb des externen Campus Haninge zukünftig zum Teil dort stattfinden wird. Bei dieser Gelegenheit soll die Energieeffizienz  des Gebäudes gesteigert werden. Poten- tial hierfür besteht sowohl beim Heizen als auch in der Warmwasserbereitung. Die Auswirkungen einer verringerten Vorlauftemperatur zu den Heizkörpern wurden auf Grundlage von Gleichungen zur Wärmeübertragung betrachtet. Es wurde berech- net, dass die Verringerung der Vorlauftemperatur um 5 K den Heizbedarf um 25 % reduzieren würde, d. h. um 94,25 MWh a−1, und damit Emissionen in Höhe von 9,9 t CO2 a−1 vermieden werden könnten. Aufgrund hoher Wärmeverluste vom sekundären Fernwärmekreislauf  zum Boden auf dem Gelände der KTH wurde eine Alternative  für die Warmwasserbereitung zu Zeiten ohne Heizbedarf, d.h. von Mai bis September, in Erwägung gezogen. Zwei Systeme, welche den Bedarf vollständig abdecken können, wurden entwick- elt und sowohl auf ihre Energieeffizienz  als auch auf ihre Wirtschaftlichkeit  hin geprüft. Der tägliche Warmwasserbedarf  sowie der Spitzenbedarf  wurden eigens zu diesem Zweck modelliert. Für ein Hybridsystem, welches aus zehn Flachkollek- toren mit einer gesamten Aperturfläche von 23,3 m2  und einer Wärmepumpe mit 7,5 kW Leistung besteht, wurde eine maximale Leistungszahl von 9,13 im Juni ermittelt. Trotz der geringen Betriebskosten ist der Kapitalwert negativ, da die Investitionskosten sehr hoch sind. Die konkurrenzfähige Alternative ist die Installa- tion einer Wärmepumpe mit 12,22 kW Leistung, welche die Abwärme der Computer im Serverraum nutzen soll. Werden sowohl die Kälte- als auch die Wärmeleistung als Nutzen angesehen, berechnet  sich der Kapitalwert zu etwa 32.000 EUR, ohne Miteinbeziehung der Kälteleistung zu 11.500 EUR. Diese Zahlen beziehen sich auf einen ganzjährigen Betrieb, d. h. die Wärmepumpe trägt von Oktober bis März zur Heizleistung bei. Verglichen mit der Nutzung von Außenluft als Wärmequelle kann die Leistungszahl um 83 % bzw. 10 % gesteigert werden, je nach Definition des Nutzens. Die Verringerung des Fernwärmebedarfs wurde zu 24,48 MWh a−1 berech- net, vorausgesetzt das Gebäude kann von Mai bis September vom Verteilernetz der KTH abgekoppelt werden. Gleichzeitig ermöglicht dies Emissionseinsparungen von 2,57 t CO2 a−1. Zusammenfassend erscheint  die Installation einer Wärmepumpe, welche die Abwärme im Serverraum nutzt, als eine sowohl energieeffiziente als auch wirtschaftliche Lösung. / Byggnaden Norra Djurgården  43:12 på Kungliga Tekniska Högskolans (KTH:s) hu- vudcampus i Stockholm kommer att renoveras då studenter från den externa cam- pusen Haninge kommer att  flyttas dit. Detta tillfälle  skall nu utnyttjas  för att effektivisera byggnadens energiprestation.  Potentialen för energieffektivisering finns därtill  i både uppvärmningen och varmvattenberedningen. I detta arbete har ef- fekten av sänkt tilloppstemperatur till radiatorerna studerats.  Effekten har kvan- tifierats genom beräkningarna  med hjälp av välkända ekvationer för värmetrans- port.  Beräkningarna har visat att värmebehovet kunde minskas med 25 %, d.v.s. 94,25 MWh per år, genom en sänkning av tillopstemperaturen med 5 K. Följaktigen kunde CO2 emissionerna också minskas med ungefär 9,9 ton per år. Då värmeförlusterna från den primära fjärrvärmekretsen mellan maj och september är höga, har ett alternativ  för varmvattenberedningen för denna tidsperiod pre- senterats.  Två system har presenterats som kan fullständigt täcka behovet  och har analyserats beträffande både energieffektiviteten och lönsamhet. Det dagliga varmvattenbehovet samt spetsbehovet har modellerats just för detta syfte.  Den maxmimala värmefaktorn till ett system bestående av 10 plana solfångare med en total aperturarea (genomskinliga arean) på 23,3 m−2  och en värmepump  på 7,5 kW har uppskattats till 9,13 i juni.  Trots de låga driftskostnaderna är kapitalvärdet negativt eftersom investeringskostnaderna  var höga. Den andra lösningen innefat- tade installation av en värmepump på 12,22 kW som använder sig av spillvärmen från serverrummet. Om besparingen av både fjärrvärme och fjärrkyla  betraktas i lönsamhetsanalysen, beräknas kapitalvärdet till ungefär 247.500 SEK, respektive 99.000 SEK om bara det minskade fjärrvärmebehovet  betraktas. Dessa siffror är baserade på ett års drift, d.v.s. om värmepumpen står för uppvärmningen från ok- tober till mars. Jämfört med användningen av uteluft som värmekälla  ökar värme- faktorn med 10 %. Ökningen blir 83 % om i processens nytta inkorporeras både den värme som absorberats från serverrummet och den värme som används för varm- vattenberedning  och uppvärmning. Reduktionen i fjärrvärmebehovet har beräknats till 24,48 MWh per år, förutsatt att byggnaden kan kopplas ifrån KTH:s distribu- tionsnätverk mellan maj och september.  Samtidigt kunde CO2 emissionerna också reduceras med 2,57 ton per år. Sammanfattningsvis kan det konstaterats att instal- lationen av en värmepump,  som använder sig av spillvärmen från serverrummet, kan vara både en kostnads- och energieffektiv lösning för den undersökta byggnaden.

Pressurized hot water and DTPA-Sorbitol are two relatively new soil boron (B) extraction methods with potential to replace the cumbersome hot water extraction. The objective of this research is to produce data in support of acceptance or rejection of these two alternative B extractions. The three soil tests were used to extract B from samples of calcareous sand and silt loam and limed, loamy fine sand treated with 10 levels of B and incubated for 7 and 28 d. As B application increased so did extractable B with each extraction method. High correlations (r of 0.977 to 0.999) were observed between extractable B and rate of B application with all three methods. Hot water generally extracted the least and pressurized hot water the most B regardless of soil type, rate of application or duration of incubation. Greenhouse and field experiments were conducted on one limed acid and two alkaline soils naturally low in B to test alfalfa response to B fertilizer. Values from the three soil extraction methods were correlated to yield, B tissue concentration and total B removal of alfalfa. In greenhouse studies with varying levels of soil applied B, highly significant relationships exist between extractable soil B and both tissue B concentration and total B removal. Correlations between yield and extractable soil B were impossible to obtain because of a lack of alfalfa yield responses to applied boron. All three methods accurately predict plant B tissue concentrations and total B removal. The field experiment produced a significant positive relationship between total alfalfa yield and extractable B using hot water and pressurized hot water extractions, but not using DTPA-Sorbitol. The results observed in this research support pressurized hot water extraction as the better of the two alternatives to replace hot water extraction in a broad range of soil types.

We are at a time when energy efficiency and the reduction in the use of non-renewable energy is an important objective in all aspects and will continue to be so, therefore it is necessary to try to reduce energy and heat losses in the systems used in homes and, in particular, in the domestic hot water (DHW) system. This study aims to find out the advantages and disadvantages of an innovative pipe-in-pipe (PIP) system for DHW circulation with respect to the conventional system of two separate pipes. Previous studies have shown that DHW circulation is indeed an important point of energy losses in the home and that it is possible to reduce these losses by using the innovative system under study. The properties and coefficients defining the heat transfer system have been obtained for both the traditional and innovative systems by using empirical equations and iterative processes, indicating a 32% reduction in heat losses in favour of the pipe-in-pipe system. However, this result has been obtained in a kind of case study, using some simplifying assumptions, needed to accomplish to work within limited time. So the result could vary if a somewhat different system is studied, which is why it is necessary to carry out further studies and research on this subject in order optimize DHW systems in buildings.

No description available.

Solar Domestic Hot Water (SDHW) systems collect energy from the sun to heat the household water. In the context of a system energy balance, numerical simulations were conducted using the commercial software “TRNSYS-17” to study the SDHW system performance (solar fraction) influenced by the critical parameters in various sizes of the thermal storage tank (TES) tank. The key parameters were the magnitude of the collector mass flow rate, degree of thermal stratification within the TES tank, and the duration of the mass flows through the collector. An empirical correlation was obtained to determine the operating collector mass flow rate and TES volume to deliver the peak system performance. The correlation was preliminarily verified with different weather data. The studies showed that the optimal collector mass flow rate occurred when the same amount of total daily household demand passed through the collector. Furthermore, when the twofold amount of the household demand passed through the collector, the optimal dimensionless tank volume became insensitive to the change of collector flow rate and remained constant at 0.84. Researchers discovered that promoting thermal stratification within the TES tank would enhance system performance. Thermal stratification within a TES improves the system performance by sending colder water to the solar collector and hotter water to the household. This research challenges the research community’s focus on thermal stratification by showing that solar fraction is directly related to the solar collector heat losses. As such, the role of the TES tank is to supply cold fluid to the collector to minimize collector losses. Thermal stratification in the top portion of the tank is thus unimportant in influencing solar fraction. In this research, the pump is turned on/off by monitoring the temperature difference between the collector inlet and outlet. Different pump control strategies at different collector mass flow rates were implemented to adjust the pump-on time. The studies showed the system performance was negligibly affected (~0.5%) by employing different pump control strategies while the collector mass flow rate was held constant. / Thesis / Master of Applied Science (MASc)

The following conclusions appear to have merit: 1) The heat obtained from cooling milk in a mechanical farm milk cooler may be used for preheating a quantity of water. 2) The amount of water heated and the temperature to which it is heated are functions of the heat obtainable from the milk cooler and refrigeration equipment. 3) The percentage of available heat from the condenser that is available in the water passed to the electric water heater is a function of: (a) the design of the condenser-to-water heat transfer system, (b) the size and shape of the storage tank, and (c) the losses from the storage tank. 4) The savings in cost of electric energy for operation of the electric water heater are appreciable when heat extracted from cooling milk is used to pre-heat water. In this study, the savings amounted to slightly more than 30 percent. However, a large quantity of heated water passed to the overflow tank. A savings of 54 percent could be realized when the water drawn from the pre-heat tank into the water heater was raised from 62 F - 120 F in the pre-heat tank. 5) Without the assistance of a competent refrigeration mechanic, the technical problems involved make it inadvisable for the individual farmer to attempt a conversion of current milk cooling equipment for the additional function of heating water. 6) This study indicates that greater savings may be effected with a refrigeration unit and condensing unit specifically designed for heating water, using the basic principles outlined in this study. / Master of Science

Heat pumps have been identified as an efficient alternative to traditional boilers for the production of sanitary hot water (SHW). The high water temperature lift (usually from 10ºC to 60ºC) involved in this application has conditioned the type of used solutions. On the one hand, transcritical cycles have been considered as one of the most suitable solutions to overcome the high water temperature lift. Nevertheless, the performance of the transcritical CO2 heat pump is quite dependent on the water inlet temperature, which in many cases is above 10ºC. Furthermore, performance highly depends on the rejection pressure, which needs to be controlled to work at the optimum point in any condition. On the other hand, for the subcritical systems, subcooling seems to be critical for the heat pump performance when working at high temperature lifts, but there is not any published work that optimizes subcooling in the SHW application for these systems. Therefore, the subcritical cycle should require a systematic study on the subcooling that optimizes COP depending on the external conditions, in the same way as it has been done for the rejection pressure in the transcritical cycle. The aim of this thesis is to investigate the role of subcooling in the performance of a Propane water-to-water heat pump for SHW production, in the application of heat recovery from any water source. Two different approaches to overcome the high degree of subcooling were designed and built to test them in the laboratory: 1) Subcooling is made at the condenser: The active refrigerant charge of the system is controlled by a throttling valve. Subcooling is controlled independently at any external condition. 2) Subcooling is made in a separate heat exchanger, the subcooler. Subcooling is not controlled, it depends on the external condition and the heat transfer at the subcooler. The heat pumps were tested at different water temperatures at the evaporator inlet (10ºC to 35ºC) and condenser inlet (10ºC to 55ºC), while the water production temperature was usually fixed to 60¿C. The obtained results have shown that COP depends strongly on subcooling. In the nominal condition (20¿C/15¿C for the inlet/outlet water temperature at the evaporator and 10ºC/60ºC for the inlet/outlet water temperature in the heat sink), the optimum subcooling was about 43 K with a heating COP of 5.61, which is about 31% higher than the same cycle working without subcooling. Furthermore, the system with subcooling has been proved experimentally as being capable of producing water up to 90¿C and has shown a higher COP than some CO2 commercial products (catalog data reference). / Las bombas de calor han sido identificadas como una alternativa eficaz a las calderas tradicionales para la producción de agua caliente sanitaria (ACS). El elevado salto de temperatura del agua que normalmente tiene lugar en esta aplicación (por lo general de 10ºC a 60ºC) ha condicionado el tipo de soluciones que se utilizan. Por un lado, los ciclos transcríticos han sido considerados como una de las mejores soluciones para trabajar con los elevados saltos de temperatura del agua. Sin embargo, el rendimiento de la bomba de calor transcrítica con CO2 es bastante dependiente de la temperatura de entrada del agua, que en muchos casos está por encima de los 10¿C. Además, el rendimiento depende en gran medida de la presión de descarga, la cual necesita ser controlada con el fin de trabajar en el punto óptimo en cualquier condición externa. Por otra parte, para los sistemas subcríticos, el subenfriamiento parece ser crítico para el buen funcionamiento de la bomba de calor cuando se trabaja con elevados saltos de temperatura del agua, pero no hay ningún trabajo publicado en el que optimicen el subenfriamiento para la aplicación de ACS en estos sistemas. Por lo tanto, los sistemas subcríticos requieren de un estudio sistemático para buscar el subcooling óptimo y maximizar el COP en función de las condiciones externas, de la misma forma que se ha hecho para la presión de descarga en los ciclos transcríticos. El objetivo de esta tesis es investigar el papel del subenfriamiento en el rendimiento de una bomba de calor trabajando con Propano para la producción de ACS, en la aplicación de recuperación de calor de cualquier fuente de agua (agua- agua). Dos enfoques diferentes para superar el alto grado de subenfriamiento fueron diseñados y construidos para ponerlos a prueba en el laboratorio: 1) El subenfriamiento se hace en el condensador: La carga activa de refrigerante del sistema se controla con una válvula de estrangulación. De esta manera, el subenfriamiento puede ser controlado de forma independiente a cualquier condición externa. 2) El subenfriamiento se hace en un intercambiador de calor separado, el subenfriadador. El subenfriamiento no se controla, este depende de la condición externa y de la transferencia de calor en el subenfriadador. Las bombas de calor se ensayaron a diferentes temperaturas del agua a la entrada del evaporador (10ºC a 35ºC) y entrada del condensador (10ºC a 55ºC), mientras que la temperatura de producción de agua, normalmente, se fija a 60¿C. Los resultados obtenidos han demostrado que el COP depende mucho del subenfriamiento. En las condiciones nominales (20ºC/15ºC para la temperatura del agua de entrada/salida en el evaporador y 10ºC/60ºC para la temperatura del agua de entrada/salida en el condensador), el subenfriamiento óptimo fue aproximadamente de 43 K con un COP de calentamiento de 5,61, que es alrededor del 31% más alto que el mismo ciclo trabajando sin subenfriamiento. Además, el sistema con subenfriamiento ha probado de forma experimental, que es capaz de producir agua hasta los 90ºC, y ha mostrado un COP más alto que algunos productos comerciales que trabajan con CO2 (datos de referencia del catálogo). / Les bombes de calor han estat identificades com una alternativa eficaç a les calderes tradicionals per a la producció d'aigua calenta sanitària (ACS). L'elevat salt de temperatura de l'aigua que normalment té lloc en aquesta aplicació (en general de 10ºC a 60ºC) ha condicionat el tipus de solucions que s'utilitzen. Per una banda, els cicles transcrítics s'han considerat com una de les millors solucions per tal de treballar amb els elevats salts de temperatura de l'aigua. No obstant això, el rendiment de la bomba de calor transcrítica amb CO2 és bastant dependent de la temperatura d'entrada de l'aigua, que en molts casos està per damunt de 10¿C. A més, el rendiment depèn en gran mesura de la pressió de descarrega, la qual necessita ser controlada per tal de treballar en el punt òptim a qualsevol condició externa. Per altra banda, per als sistemes subcrítics, el sub-refredament sembla ser crític per al funcionament de la bomba de calor quan es treballa amb elevats salts de temperatura de l'aigua, però no hi ha cap treball publicat en el qual optimitzen el sub-refredament per a l'aplicació d'ACS en aquests sistemes. Per tant, els sistemes subcrítics requereixen d'un estudi sistemàtic per tal de buscar el subcooling òptim i maximitzar el COP en funció de les condicions externes, en la mateixa forma que s'ha fet per la pressió de descarrega en els cicles transcrítics. L'objectiu d'aquesta tesi és investigar el paper del sub-refredament en el rendiment d'una bomba de calor treballant amb Propà per a la producció d'ACS, en l'aplicació de recuperació de calor de qualsevol font d'aigua (aigua-aigua). Dos enfocaments diferents per tal de superar l'alt grau de sub-refredament van ser dissenyats i construïts per posar-los a prova en el laboratori: 1) El sub-refredament es fa en el condensador: La càrrega activa de refrigerant del sistema es controla amb una vàlvula d'estrangulació. D'aquesta manera, el sub-refredament pot ser controlat de forma independent en qualsevol condició externa. 2) El sub-refredament es fa en un intercanviador de calor separat, el sub-refredador. El sub-refredament no es controla, este depèn de la condició externa i de la transferència de calor al sub-refredador. Les bombes de calor es van assajar a diferents temperatures de l'aigua a l'entrada de l'evaporador (10ºC a 35ºC) i a l'entrada del condensador (10ºC a 55ºC), mentre que la temperatura de producció d'aigua, normalment, es fixa a 60¿C. Els resultats obtinguts han demostrat que el COP depèn molt del sub-refredament. En les condicions nominals (20ºC/15ºC per a la temperatura de l'aigua d'entrada/eixida a l'evaporador i 10ºC/60ºC per a la temperatura de l'aigua d'entrada/eixida en el condensador), el sub-refredament òptim és aproximadament de 43 K amb un COP d'escalfament de 5,61, que és al voltant del 31% més alt que el mateix cicle treballant sense sub-refredament. A més, el sistema amb sub-refredament ha provat de forma experimental, que és capaç de produir aigua fins als 90ºC, i ha mostrat un COP més alt que alguns productes comercials que treballen amb CO2 (dades de referència del catàleg). / Pitarch I Mocholí, M. (2017). High capacity heat pump development for sanitary hot water production [Tesis doctoral]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/81858