The overall objective of this thesis is to evaluate the fundamentals of current low concentration CO2 separation technologies and to provide an alternate method using adsorption technology with existing as well as new adsorbents. Two different applications for the adsorption of CO2 are explored; Direct Air Capture (DAC) and excimer gas purification. The investigation of aerogels as possible adsorbent for these applications was also explored. The first application, DAC of CO2 using adsorbents, addresses climate change by reducing the amount of atmospheric CO2 levels that are directly correlated to global warming. Because of DAC being carbon negative, this field has gained significant attention in the literature. DAC as a CO2 reduction strategy was approached in two ways: 1. Chapter 2 investigates capturing and concentrating CO2 from 0.04% in the air to 95% to be able to sequester it into the ground. This research began by doing an adsorbent selection using pure gas gravimetric measurements on seven different commercially available type X zeolites that were determined to have potential for this separation. Breakthrough experiments were then carried out with the most promising zeolite by perturbing the bed with compressed ambient air. In the process studied, a basic four step temperature vacuum swing adsorption (TVSA) cycle was investigated comprising the following steps: pressurization, adsorption, blowdown, and desorption. Four different regeneration temperatures were tested along with four different gas space velocities. With this cycle configuration, CO2 was concentrated to 95% from 0.04% with total capture fractions as high as 81%. This study highlighted methods to reduce the energy consumption per ton of CO2 captured in the system as well as the potential of using low Si/Al ratio faujasite structured zeolites in DAC of CO2 for greenhouse gas reduction. 2. Chapter 3 expands on the research of Chapter 2 by capturing CO2 from 0.04% in the air and concentrating it to high purity CO2 levels where the cost for operating the process will be reimbursed through the value of the produced CO2. The goal of this research was to increase the CO2 to as high as possible because the purer the CO2, the more valuable it is. This research started by conducting an in-depth investigation into the pure gas adsorption of CO2, N2, O2, and Ar on the most promising zeolite from Chapter 2. The data was then fitted to the TD-Toth model which allowed for the evaluation of the TVSA cycle and showed the potential of reducing the pressure and/or elevating the temperature during the blowdown step in order to produce high purity CO2. To confirm this, the TVSA cycle was run on a fixed bed breakthrough experiment where high purity CO2 was produced between a concentration of 99.5% and 99.96% by lowering the blowdown pressure. By controlling the blowdown temperature, the concentration of the product was increased from 99.8% to 99.95%, however with a significant loss of CO2. This effect of N2, O2, and Ar desorbing during the blowdown step with CO2 desorbing during the evacuation step is shown graphically by measuring the concentration and flow rate of the exiting gas species. The results from this study show the potential for producing a valuable product of high purity CO2 from atmospheric concentrations. The second application in this thesis that is explored in Chapter 4 is the purification of trace impurities of CO2, CF4, COF2, and O2 from F2, Kr, and Ne for applications in excimer lasers. Due to the incompatibility of many adsorbents to F2 and HF, aluminas and polymeric adsorbents were selected as potentially compatible materials. To increase the compatibility of these adsorbents, the use of a cryo-cooler was determined to be feasible to precool the feed stream before separation, which increases the adsorption capacity and compatibility of the material to F2 and HF. To determine the adsorption potential in the low concentration of these adsorbents, the concentration pulse chromatographic technique was chosen to determine the Henry’s Law constants of CO2, CF4, and O2. This data was then plotted on the van’t Hoff plot and extrapolated to colder temperatures to determine the benefit of using a cryo-cooler. From this study, it was determined that HayeSep Q was the best polymeric adsorbent with significant adsorption of CO2 at temperatures below -50˚C while being the best performing CF4 adsorbent. AA-300 was the best performing alumina in this study while having significant adsorption of CF4 at temperatures below -135˚C. However, from a compatibility standpoint, both of these materials need to be tested to determine their robustness in the presence of F2 and HF at room and reduced temperatures. Chapters 5 & 6 in this thesis explore the fundamentals of adsorption on aerogels as a prelude to using aerogels as possible adsorbents for DAC of CO2. This investigation into aerogels looks at silica aerogels and carbon aerogels, which are both industrially produced and explores their adsorption with relation to like materials such as silica gel and activated carbons. Both of these Chapters utilize experimentally determined adsorption isotherms of CO2, N2, O2, and Ar as well as characterization to determine adsorption trends in the materials. Some major conclusions for silica aerogels were that common surface modifications to make the material more resilient against water adsorption impacts the adsorption of CO2 significantly with roughly 4 fold difference in adsorption capacity. For carbon aerogels some major conclusions were that the adsorption was increasingly dominated by the heterogeneous nature of the surface at lower pressures and increasingly dominated by the pore size at the higher pressures. Both chapters discuss the adsorption of air along with ideas such as the influence of gas thermal conductivity in the pores with respects to adsorption. L'objectif général de cette thèse est d'évaluer les principes fondamentaux des technologies actuelles de séparation du CO2 à faible concentration et de fournir une méthode alternative utilisant la technologie d’adsorption avec des adsorbants actuels ainsi que d'en découvrir de nouveaux. Deux applications différentes pour l'adsorption du CO2 ont été explorées; la capture directe dans l’air ambient (CAD) et la purification des gaz excimères, ainsi que la recherche d'aérogels comme adsorbant possible pour ces applications. La première application, le CAD du CO2 utilisant des adsorbants, pourrait répondre aux changements climatiques puisque les niveaux de CO2 atmosphérique sont directement corrélés au réchauffement climatique. Dernièrement, le CAD a fait l'objet d'une attention particulière en tant que stratégie de réduction du CO2, par conséquent, deux voies différentes ont été explorées dans cette thèse: 1. Le chapitre 2 étudie la capture et la concentration du CO2 de 0,04% dans l'air à 95% afin de pouvoir l’enfermer dans la terre. Pour ce faire, une sélection d'adsorbant a été effectué en utilisant des mesures gravimétriques à gaz pur sur sept zéolithes de type X disponibles dans le commerce qui ont été déterminés comme ayant un potentiel pour cette séparation. Des expériences révolutionnaires ont ensuite été réalisées avec la zéolite la plus prometteuse en perturbant le lit avec de l'air ambiant comprimé. Dans le processus étudié, un cycle basique à quatre étapes d’adsorption modulée en température et pression (AMTP) a été étudié, comprenant les étapes suivantes: pressurisation, adsorption, purge et désorption. Quatre températures de régénération différentes ont été testées ainsi que quatre vitesses spatiales de gaz différents. Avec cette configuration de cycle, le CO2 était concentré à 95% de 0,04% avec des fractions de capture totales aussi élevées que 81%. Cette étude a mis en évidence des méthodes pour réduire la consommation d'énergie par tonne de CO2 captée dans le système ainsi que le potentiel d'utilisation de zéolithes structurées à base de faujasite à faible rapport Si/Al dans le CAD du CO2 pour la réduction des gaz à effet de serre. 2. Le chapitre 3 approfondit les recherches du chapitre 2 en capturant le CO2 de 0,04% dans l'air et en le concentrant à des niveaux de très haute pureté où le processus sera remboursé par la valeur du CO2 produit. L'objectif de cette partie était d'augmenter la pureté du CO2 le plus possible car plus le CO2 est pur, plus il est précieux. Une enquête approfondie sur l'adsorption de gaz pur de CO2, N2, O2 et Ar sur la zéolite la plus prometteuse du chapitre 2. Les données ont ensuite été ajustées au modèle TD-Toth qui a permis d'évaluer le cycle AMTP et a montré le potentiel de réduire la pression et/ou d'élever la température pendant l'étape de purge afin de produire du CO2 de haute pureté. Pour confirmer cela, le cycle AMTP a été fait par le biais d’une expérience dans un lit fixe où du CO2 de haute pureté a été produit entre une concentration de 99,5% et 99,96% en abaissant la pression de purge. En contrôlant la température de purge, la concentration du produit est passée de 99,8% à 99,95%, mais avec une perte importante de CO2. Cet effet de la désorption de N2, O2 et Ar pendant l'étape de purge avec la désorption du CO2 pendant l'étape d'évacuation est illustré graphiquement en mesurant la concentration et le débit des espèces de gaz sortant. Les résultats de cette étude montrent le potentiel de production d'un produit précieux de CO2 de haute pureté à partir des concentrations atmosphériques. La deuxième application de cette thèse qui est explorée au Chapitre 4 est la purification des traces d'impuretés de CO2, CF4, COF2 et O2 de F2, Kr et Ne pour des applications dans les lasers à excimère. En raison de l'incompatibilité de nombreux adsorbants avec le F2 et le HF, les alumines et les adsorbants polymères ont été sélectionnés comme matériaux potentiellement compatibles. Pour augmenter la compatibilité de ces adsorbants, l'utilisation d'un cryoréfrigérant a été jugée possible pour pré-refroidir le flux d'alimentation avant la séparation, ce qui augmente la capacité d'adsorption et la compatibilité du matériau en F2 et HF. Pour déterminer le potentiel d'adsorption dans la faible concentration de ces adsorbants, la technique de chromatographie pulsée de concentration a été choisie pour déterminer les constantes de la loi de Henry de CO2, CF4 et O2. Ces données ont ensuite été tracées sur le graphique van’t Hoff et extrapolées à des températures plus froides pour déterminer les avantages de l’utilisation d’un cryoréfrigérant. À partir de cette étude, il a été déterminé que HayeSep Q était le meilleur adsorbant polymère avec une adsorption significative de CO2 à des températures inférieures à -50 ° C tout en étant l'adsorbant CF4 le plus performant. L'AA-300 était l'alumine la plus performante de cette étude tout en ayant une adsorption significative de CF4 à des températures inférieures à -135 °C. Cependant, du point de vue de la compatibilité, ces deux matériaux doivent être testés pour déterminer leur robustesse en présence de F2 et de HF à température ambiante et réduite. Les chapitres 5 et 6 explorent les principes fondamentaux de l'adsorption sur les aérogels en prélude à l'utilisation d'aérogels comme adsorbants possibles pour le CAD du CO2. Cette enquête sur les aérogels examine les aérogels de silice et les aérogels de carbone, qui sont tous les deux fabriqués industriellement et explore leur adsorption par rapport à des matériaux similaires tels que le gel de silice et les charbons actifs. Ces deux chapitres utilisent des isothermes d'adsorption déterminés expérimentalement de CO2, N2, O2 et Ar ainsi que la caractérisation pour déterminer les tendances d'adsorption dans les matériaux. Certaines conclusions majeures pour les aérogels de silice étaient que les modifications de surface courantes pour rendre le matériau plus résistant à l'adsorption d'eau ont un impact significatif sur l'adsorption de CO2 avec une différence d'environ 4 fois dans la capacité d'adsorption. Pour les aérogels de carbone, certaines conclusions majeures étaient que l'adsorption était de plus en plus dominée par la nature hétérogène de la surface à des pressions plus faibles et de plus en plus dominée par la taille des pores aux pressions plus élevées. Les deux chapitres discutent de l'adsorption d'air ainsi que des idées telles que l'influence de la conductivité thermique du gaz dans les pores en ce qui concerne l'adsorption.

Millennium Development Goal 1 (MDG 1) on halving extreme poverty is measured with the international poverty line. The purpose of the study is to evaluate the measurement of MDG 1 by reviewing the robustness of the international poverty line and some of its national sub-reports. There are at least two problems in assessing a reliable poverty line, namely what constitutes extreme poverty and what kind of life situation this refers to. Through a qualitative content analysis, the study shows that the selected national reports lack a reliable reference for human dietary energy requirements pivotal for estimating a fair threshold for food needs. In the case that a reliable source was used, the activity level was prone to a wide range of interpretations and lacked procedural consistency.  The FAO (2011) has presented minimum dietary energy requirements that are below the references used in the national reports, which could shift the poverty line. The study also shows that the concept of “extreme poverty” has been used inconsistently. MDG 1 identifies extreme poverty as the inability to meet basic food- and non-food needs. The international poverty line is based on a myriad of national poverty lines ranging from minimum- to generous needs, where extreme poverty is defined as people barely having enough for the food component alone. These two variables create obstacles in setting a reliable international poverty line. A small shift in the international poverty line changes the poverty rates substantially, making it difficult for poverty programs and MDG 1 in truly identifying the people in most need of help.

<p>Conventional end-of-pipe solutions for wastewater treatment have been criticized from a sustainable view-point, in particular regarding recycling of nutrients. The integration of hydroponic cultivation into a wastewater treatment system has been proposed as an ecological alternative, where nutrients can be removed from the wastewater through plant uptake; however, cultivation of plants in a temperate climate, such as Sweden, implies that additional energy is needed during the colder and darker period. Thus, treatment capacity, additional energy usage and potential value of products are important aspects considering the applicability of hydroponic wastewater treatment in Sweden.</p><p>To enable the investigation of hydroponic wastewater treatment, a pilot plant was constructed in a greenhouse located at Överjärva gård, Solna, Sweden. The pilot plant consisted of several steps, including conventional biological processes, hydroponics, algal treatment and sand filters. The system treated around 0.56-0.85 m3 domestic wastewater from the Överjärva gård area per day. The experimental protocol, performed in an average of twice per week over a period of three years, included analysis and measurements of water quality and physical parameters. In addition, two studies were performed when daily samples were analysed during a period of two-three weeks. Furthermore, the removal of pathogens in the system, and the microbial composition in the first hydroponic tank were investigated.</p><p>Inflow concentrations were in an average of around 475 mg COD/L, 100 mg Tot-N/L and 12 mg Tot-P/L. The results show that 85-90% of COD was removed in the system. Complete nitrification was achieved in the hydroponic tanks. Denitrification, by means of pre-denitrification, occurred in the first anoxic tank. With a recycle ratio of 2.26, the achieved nitrogen removal in the system was around 72%. Approximately 4% of the removed amount of nitrogen was credited to plant uptake during the active growth period. Phosphorus was removed by adsorption in the anoxic tank and sand filters, natural chemical precipitation in the algal step induced by the high pH, and assimilation in plants, bacteria and algae. The main removal occurred in the algal step. In total, 47% of the amount of phosphorus was removed. Significant recycling of nitrogen and phosphorus through harvested biomass has not been shown. The indicators analysed for pathogen removal showed an achieved effluent quality comparable to, or better than, for conventional secondary treatment. The microbial composition was comparable to other nitrifying biological systems. The most abundant phyla were Betaproteobacteria and Planctomycetes.</p><p>In Sweden, a hydroponic system is restricted to greenhouse applications, and the necessary amount of additional energy is related to geographic location. In conclusion, hydroponic systems are not recommended too far north, unless products are identified that will justify the increased energy usage. The potential for hydroponic treatment systems in Sweden lies in small decentralized systems where the greenness of the system and the possible products are considered as advantages for the users.</p>

Conventional end-of-pipe solutions for wastewater treatment have been criticized from a sustainable view-point, in particular regarding recycling of nutrients. The integration of hydroponic cultivation into a wastewater treatment system has been proposed as an ecological alternative, where nutrients can be removed from the wastewater through plant uptake; however, cultivation of plants in a temperate climate, such as Sweden, implies that additional energy is needed during the colder and darker period. Thus, treatment capacity, additional energy usage and potential value of products are important aspects considering the applicability of hydroponic wastewater treatment in Sweden. To enable the investigation of hydroponic wastewater treatment, a pilot plant was constructed in a greenhouse located at Överjärva gård, Solna, Sweden. The pilot plant consisted of several steps, including conventional biological processes, hydroponics, algal treatment and sand filters. The system treated around 0.56-0.85 m3 domestic wastewater from the Överjärva gård area per day. The experimental protocol, performed in an average of twice per week over a period of three years, included analysis and measurements of water quality and physical parameters. In addition, two studies were performed when daily samples were analysed during a period of two-three weeks. Furthermore, the removal of pathogens in the system, and the microbial composition in the first hydroponic tank were investigated. Inflow concentrations were in an average of around 475 mg COD/L, 100 mg Tot-N/L and 12 mg Tot-P/L. The results show that 85-90% of COD was removed in the system. Complete nitrification was achieved in the hydroponic tanks. Denitrification, by means of pre-denitrification, occurred in the first anoxic tank. With a recycle ratio of 2.26, the achieved nitrogen removal in the system was around 72%. Approximately 4% of the removed amount of nitrogen was credited to plant uptake during the active growth period. Phosphorus was removed by adsorption in the anoxic tank and sand filters, natural chemical precipitation in the algal step induced by the high pH, and assimilation in plants, bacteria and algae. The main removal occurred in the algal step. In total, 47% of the amount of phosphorus was removed. Significant recycling of nitrogen and phosphorus through harvested biomass has not been shown. The indicators analysed for pathogen removal showed an achieved effluent quality comparable to, or better than, for conventional secondary treatment. The microbial composition was comparable to other nitrifying biological systems. The most abundant phyla were Betaproteobacteria and Planctomycetes. In Sweden, a hydroponic system is restricted to greenhouse applications, and the necessary amount of additional energy is related to geographic location. In conclusion, hydroponic systems are not recommended too far north, unless products are identified that will justify the increased energy usage. The potential for hydroponic treatment systems in Sweden lies in small decentralized systems where the greenness of the system and the possible products are considered as advantages for the users. / QC 20101014

Purpose: This degree project aims to study how different choices regarding the size, location and type of windows affect daylight entry in an apartment building in Västerås. We have chosen to calculate the energy requirement when changing the window type, size and shielding factor. The purpose is also to come up with solution proposals that balance daylight input and energy for a smaller energy need in the apartment building. Method: The research method is based on a literature study that will lay the foundation for the work and a case study where a visit to the concerned building has been carried out. Interviews have also been conducted with experts in daylight and energy issues. Energy calculations and daylight- related calculations have also been made using the computer program Daylight Visualizer. The goal of the program is to find out the value of the daylight factor in two different apartments on two different floors. In each apartment, three different rooms in three different latitudes (north, west, and south) have been studied. Results: The results present several factors that affect daylight intake. These are screening angles, orientation, room height, room depth, building structure and placement of balconies. The properties of the windows in terms of daylight transmittance (LT value) and solar heat gain (g value) are very important to get a good result regarding both daylight and heat in the building. The balance between daylight and solar heat gain to reducing the energy needs for heating during the winter and cooling during the summer. The result based on the computer program for the first window alternative show that that the value of the daylight factor in all three rooms on the 12th floor (third floor) was between 0.59–0.31% and on the 19th floor (tenth floor) 1.01– 0.91%. The calculations of the energy balance show as monthly results, and the calculated annual need for active heating is about 27 MWh / year. The corresponding result according to calculations by the consulting company Kadesjös is approximately 59 MWh / year, but the difference between its calculations has not been studied further in this degree project. Conclusions: The calculation results indicate that the building has a very limited energy requirement for active heating in relation to its size and this is logical given that the heat losses are relatively small in terms of transmission, Exhaust and supply air ventilation with heat recovery (FTX system), and air leakage. The heat losses through window glazing in this case constitute to only about 12% of the building's total heat losses.

This paper introduces a new model for electric vehicle mobility and energy consumption in urban traffic networks. The model couples the vehicle mobility described by a set of ODEs over a graph capturing the Origin-destination motion for urban networks,and the energy consumption associate to this mobility patterns. This model is illustrated in a simple pedagogic example showing its capabilities, such as keeping track of the vehicle state of charge, current energy and available storage.

Denna studie fokuserar på balansgången mellan krav på energieffektivitet och bevarandet avkulturarv i kontexten av kulturhistoriska byggnader. Syftet är att utforska hur förvaltning ochvärdering av dessa byggnader kan påverkas av framtida energikrav, med särskild fokus på depotentiella konsekvenser som detta kan medföra för fastighetsägare, förvaltare och andraintressenter. Studien använder en kombination av en litteraturstudie samt en kvalitativ studiebaserad på semistrukturerade intervjuer med fastighetsägare och fastighetsvärderare. Decentrala fynden visar att det är utmanande att energieffektivisera kulturhistoriska byggnadertill de nivåer som krävs, samt att värderingen av sådana byggnader kräver en särskildskicklighet i att balansera subjektiva preferenser med objektiva kriterier, givet marknadensolika preferenser. Energieffektivisering av kulturhistoriska byggnader kan öka dess marknadsvärde genom attsänka driftskostnader och göra fastigheter mer attraktiva för miljömedvetna investerare.Vidare kan sådana åtgärder vara svåra att implementera utan att kompromissa medbyggnadens kulturella och historiska värde. Värderingen av kulturhistoriska fastigheterkräver därför både teknisk och kulturell expertis, samt en djup förståelse förmarknadsdynamiken. Studien identifierar ett kunskapsgap på marknaden gällande dettarelativt nya problem. Avslutningsvis betonas vikten av att navigera genom dessa komplexafrågor för att bevara vårt kulturella arv samtidigt som vi adresserar dagens utmaningar, såsombehovet av energieffektivitet och hållbarhet. / This study focuses on the trade-off between energy efficiency requirements and thepreservation of cultural heritage in the context of cultural historical buildings. The aim is toexplore how the management and valuation of these buildings may be affected by futureenergy requirements, with a particular focus on the potential consequences this may have forproperty owners, managers and other stakeholders. The study uses a combination of literaturestudy and a qualitative study based on semi-structured interviews with property owners andproperty appraisers. The central findings show that it is challenging to make heritagebuildings energy efficient to the required levels, and that the valuation of such buildingsrequires a special skill in balancing subjective preferences with objective criteria, given thedifferent preferences of the market. Energy efficiency of heritage buildings can increase their commercial value by loweringoperating costs and making properties more attractive to environmentally consciousinvestors. However, such measures can be difficult to implement without compromising thecultural value of the building. The valuation of heritage properties therefore requires bothtechnical and cultural expertise. The study identifies a knowledge gap in the market regardingthis relatively new problem. It concludes by emphasizing the importance of navigatingthrough these complex issues to preserve our cultural heritage while addressing today'schallenges, such as the need for energy efficiency and sustainability.

Vid byggande av hus med källargrund vill de flesta kunna använda den ytan som en del av bostaden samt för aktiviteter såsom olika hobbyverksamheter. När källaren nyttjas som bostad krävs fuktskydd och värmeisolering i golv och väggar. Man vill ha en torr källare så möjlighet att välja ytskikt finns.När man väljer material i källaryttergrundmuren väljer man med hänsyn till överbyggnadens konstruktion. Exempel på material är murad vägg av betonghålblock, murad vägg av lättbetongblock, murad vägg av lättklinkerblock, platsgjuten betong, stående källarväggselement av lättbetong, stående källarväggselement av lättklinker och betongelement. Är det ett flerbostadshus med källaryttergrundmur byggs det nästan enbart av platsgjuten betong medan det vid småhus i regel utförs av lättbetong, lättklinker samt element av lättbetong och lättklinkerbetong.Utöver material för den bärande konstruktionen måste även material för tilläggsisolering och fuktisolering väljas. Utan isoleringen uppfyller inte byggnaden de energikrav som finns. Likaså måste de flesta ytterväggrundmurar förses med någon typ av fuktisolering. Vad är då det bästa sättet att bygga en fuktsäker källare med eventuellt tillkommande krav? / When building houses with a basement, most people want to use that area as part of the accommodation as well as activities such as various hobby activities. When the basement is used like the rest of the house, as a warm living area, moisture protection and thermal insulation are required in both floors and walls. One wants a dry basement so the possibility of choosing surface layers is available.When selecting materials within the basement wall, it is with regards of the construction above. Examples of materials are brick walls of concrete boulders, brick walls of aerated concrete, brick walls of haydite blocks, cast concrete, standing concrete wall elements of aerated concrete, standing brick wall elements of haydite and concrete elements. If it is a multi-storey house with basement terraced ground, it is almost exclusively made of cast concrete, but for individual buildings it is usually made of aerated concrete, haydite and elements of aerated concrete and haydite concrete.In addition to material for the supporting structure, additional insulation and moisture insulation materials must also be selected. Without isolation, the building does not meet the energy requirements. Likewise, most exterior walls must be provided with some type of moisture insulation. What is then the best way to build a moisture proof basement with any additional requirements?

Examensarbetet utförs under sista årets energiingenjörsstudier vid Mälardalens högskola. Med hjälp av Ramböll Västerås utfördes en energiuppföljning av energiförbrukningen vid Hälleborgs äldreboende beläget på Bäckby i Västerås åt Västerås stad. Hälleborgs äldreboende stod klart och var fullt inflyttat våren 2015. Boendet byggdes för att möta det ökade behovet av vårdplatser i Västerås kommun. Vid byggnationen ställde kommunen ett byggkrav på 60 kWh/(m2,år) köpt energi vilket var hårdare än de gällande byggkraven som gällde i Sverige vid dåvarande tidpunkt. Under projekteringen av byggnaden ändrades kravet till 70 kWh/(m2,år) viktad energi där fjärrvärmen viktas med 1 och elen med 2.  Ändringen uppkom efter att behovet av kyla kunde lösas med ett borrhålslager vilket ger möjlighet att ta tillvara på värmen som kyls bort via värmepumpar. Byggnadens värmebehov tillgodoses av både värmepumpar och fjärrvärme vilket innebär olika energikrav enligt BBR, viktningen görs för att få ett mellanting mellan kraven för byggnad med el uppvärmning och byggnad utan eluppvärmning. Examensarbetet går ut på att utreda om byggnadens energianvändning går att följa upp efter ett år i drift. Genom att försöka beräkna förbrukningen och på den vägen upptäcka problem som behöver åtgärdas till 2 årsuppföljning 2017. Det har under arbetets gång visat sig att anläggningens mätsystem inte fungerar som tänkt vad det gäller överföring mellan fastighetens mätssystem och Västerås stads mätdata hanteringssystem Momentum. Men även när mätdatainformationen skulle hämtas manuellt visades sig att det endast fanns för ett fåtal datum vilket gjorde det omöjligt att ställa upp en årsenergi. För att kontrollera att mätningen fungerade som det skulle ställdes en sammanställning upp för perioden 2015-02-22 och 2016-03-24 vilket visade att all elproduktion inte registreras i de interna mätarna. Fjärrvärmen var enda energienhet som kunde verifieras då den förbrukningen hämtades från fjärrvärmeleverantören Mälarenergi AB. Fjärrvärmeförbrukningen uppgick till 29 kWh/ kWh/(m2,år) mot projekterade 11.7 kWh/ kWh/(m2,år). För att kunna utföra en korrekt energiuppföljning och visa tappvarmvatten förbrukningen behöver fastigheten uppdateras med fler mätare. Dels behövs en mätare som mäter levererad fjärrvärmeenergi till tappvarmvattnet och det rekommenderas även att registrera en flödesmätare på tappvarmvattnet till verksamheten. Det bör även undersökas vilka elförbrukningar som inte omfattas av internmätning för att kunna skilja verksamhets- och fastighetsenergi åt. Elenergin för undermätarna var 555 406 kWh för perioden 2015-02-22 och 2016-03-24 och motsvarnade 924 025 kWh för nätägaren Mälarenergi i perioden 2015-05-01 till 2016-04-30. För att kunna utföra en balans ska undermätarna uppgå till samma förbrukning som huvudmätaren för samma mät period. Byggnaden uppfyller idag inte förutsättningar för att kunna göra en korrekt energiuppföljning. / In order to reach the 20/20 goals (meaning 20% lower energy consumption until 2020) the energy requirements on buildings must get tougher and tougher. The city of Västerås has from year 2011 set its own energy requirements on all sold estates to 60 kWh/(m2,year). When the city needed to build the new Hälleborgs elderly care center, their aim was to reach this limited energy consumption. Soon, during the planning stage, they changed this requirement to 70 kWh/(m2,year) weighted energy. The reason for this was because they were using two heating systems, one was a electric heat pump and the second was district heating. Because of higher average age in the society, the need for more elderly care centers arise even in Västerås. In the spring 2015 Hälleborgs elderly care center was completed and occupied. 2 year after the building was complete, the contractor has to do an energy monitoring and see if the goal 70 kWh/m2 is reached. In this bachelor thesis all information will be tested and the aim is to try to make a energy monitoring and figure out what needs to be done to be able to performe the energy monitoring 2017. During the work the biggest problem has been to get the right information. The system that should keep all the measured data (Momentum) was found not to have the connection to the building. When we try to pick the data by hand from the building it was not complete. So the conclusion is that the building is not ready to energy monitoring jet. This is because the building needs more time to be stable and adjust the technical systems. It also needs more points of energy measurments and flowmeters in order to get the heating water consumption. In the electric system first the net owners energy meter is installed, then the building has own meters at each electric central to separate customers consumption from building consumption. When groups of energy is summarized, it is just half of the net owners consumption. This is because some of the energy in the building is not registered. One of the electric energy’s that not is registered is the commercial kitchen, but the difference is to big that it need to be evaluated what’s missed.

I detta examensarbete studeras kommande energikrav för byggnader i Sverige och i synnerhet kraven på specifik energianvändning. Detta mot bakgrund av EU-kommissionens och EU-parlamentets direktiv, EPBD2, om nära nollenergibyggnader 2020. Därefter bearbetas ett förslag på en ny ytterväggskonstruktion som med lägre U-värde än den befintliga ytterväggen ska sänka Fiskarhedenvillans olika hustypers specifika energianvändning. Syftet med sänkningen är att möjliggöra för Fiskarhedenvillan att uppfylla de kommande energikraven. Det är många parametrar som måste uppfyllas och det nya ytterväggsförslaget analyseras förutom ur energisynpunkt även med hänsyn till statik, fukt och kostnad. Beräkningar för statik och specifik energianvändning har gjorts för ett referenshus. Resultatet av att byta ut den befintliga ytterväggskonstruktionen mot det framarbetade förslaget med ca 33 % lägre U-värde gav endast en sänkning med ca 6 % av den specifika energianvändningen. För att sänka referenshusets specifika energianvändning ytterligare bör även resterande delar av klimatskalet förbättras samt ett annat uppvärmningssätt väljas. Avslutningsvis diskuteras resultatet och vi lämnar rekommendationer för fortsatta studier. / This thesis studies future energy requirements for buildings in Sweden and in particular the requirements for specific energy use. This is in light of the European Commission and European Parliament Directive, EPBD2, on nearly-zero energy buildings 2020. A proposal for a new exterior wall construction in Fiskarhedenvillan houses with lower U-value than the existing exterior wall is analyzed. The purpose of the new wall is to reduce the specific energy use to enable Fiskarhedenvillan to meet the future energy requirements. There are many parameters that must be considered. The proposed new exterior wall construction is analyzed not only from the energy point of view but also with regard to statics, moisture and cost. Calculations for the statics and the specific energy use have been made for a reference building. The changed design of the exterior wall resulted in a reduction of the U-value with 33 % but only 6 % of the specific energy use. A further reduction of the specific energy use for the reference house requires improved design of the remaining building envelope and a new heating method. Furthermore the results are discussed and recommendations for further studies are given,