Orientador: Ivonete Ávila / Resumo: O crescimento populacional e o progresso tecnológico têm levado a crescente demanda por recursos naturais e energia, resultando na intensificação de impactos ambientais. O setor de energia é um dos principais emissores de CO2 antropogênico, principalmente devido a utilização de combustíveis fósseis, o que tem levado à busca por soluções tecnológicas visando a redução dos impactos ambientais associados à sua geração. Nesse contexto, esse trabalho visa realizar uma avaliação de desempenho ambiental da geração de energia elétrica das centrais termelétricas Fernando Gasparian e Piratininga com inserção da técnica de captura de CO2 por oxicombustão. Essa avaliação é realizada por meio de uma proposta conceitual própria que inclui avaliação do ciclo de vida (ACV) e avaliação termodinâmica com bases exergéticas. A avaliação termodinâmica abrange a operação das termelétricas, por meio de análise energética e exergética utilizando a teoria do custo exergético e o método CExC (cumulative exergy consumption). A ACV abrange desde a extração dos recursos até o fim de vida das instalações, utilizando os métodos de contabilização de recursos CED (cumulative energy demand), CExD (cumulative exergy demand) e CML IA baseline. Os resultados da avaliação termodinâmica permitiram verificar que a câmara de combustão é a principal destruidora de exergia e a inserção da técnica de oxicombustão impõe maior penalidade energética por causa da inserção dos componentes de separação de ar e processamento ... (Resumo completo, clicar acesso eletrônico abaixo) / Abstract: Population growth and technological progress have led to an increasing demand for natural resources and energy, resulting in the intensification of environmental impacts. The energy sector is one of the main emitters of anthropogenic CO2, mainly due to the use of fossil fuels, which has led to the search for technological solutions aimed at reducing the environmental impacts associated with its generation. In this context, this work aims to carry out an environmental performance evaluation of the electric power generation at the Fernando Gasparian and Piratininga thermoelectric plants with the insertion of the CO2 capture technique by oxy-combustion. This assessment is carried out through a conceptual proposal that includes life cycle assessment (LCA) and thermodynamic assessment with exergetic bases. Thermodynamic evaluation covers the operation of thermoelectric plants, through energy and exergetic analysis using the theory of exergetic cost and the CExC method (cumulative exergy consumption). ACV covers everything from resource extraction to the end of the facility's life, using the resource accounting methods CED (cumulative energy demand), CExD (cumulative exergy demand) and CML IA baseline. The results of the thermodynamic evaluation allowed to verify that the combustion chamber is the main destroyer of exergy and the insertion of the oxy-combustion technique imposes a greater energy penalty due to the insertion of the air separation unit and CO2 processing unit for CO2... (Complete abstract click electronic access below) / Doutor

[pt] Devido a sua ampla gama de aplicações, o gás natural ocupa papel importante na matriz energética global. No Brasil, a descoberta do pré-sal transformou a história do país em relação a exploração de óleo e gás. Porém, o gás lá encontrado possui grandes quantidades de CO2 associado, que requerem remoção por existirem normas da ANP que limitam o gás natural comercializado a 3 por cento mol. Diversas tecnologias se mostraram capazes de realizar essa remoção, porém para altas quantidades de CO2, a tecnologia de membranas vem sendo destaque nas plataformas offshore de extração de petróleo. Seu reduzido footprint é um grande atrativo, devido ao espaço limitado das plataformas. O presente trabalho compara a área e volume ocupados e os pesos totais dos arranjos 3D de módulos de membranas fibra oca e espiral para a separação de CO2 do gás natural no pré-sal brasileiro. Para isso, foram construídas maquetes 3D no software Solidworks (marca registrada), baseando-se em dados de plantas reais offshore em operação e dados disponibilizados pelos principais fornecedores dos módulos de membrana, para tentar alcançar valores mais próximos da realidade. Foi constatado que os módulos fibra oca apresentam grande vantagem sobre os espirais em relação a área do módulo individual (8.340,91 m2 vs 26,24 m2 ) e ao número de módulos necessários (48 vs 15.120), e também em relação às plantas completas, tanto em área e volume, quanto em peso. Uma planta completa de módulos fibra oca ocuparia apenas 7,75 por cento do volume da planta de módulos espirais. O peso da primeira totalizaria 38,42 t em oposição a 765,62 t da segunda planta. / [en] Due to its wide range of applications, natural gas plays an important role in the global energy matrix. In Brazil, the discovery of the pre-salt transformed the country s history in relation to oil and gas exploration. However, the gas found there has large amounts of associated CO2, which require removal because there are ANP standards that limit commercialized natural gas to 3 percent mol. Several technologies have proven capable of achieving this removal, but for high amounts of CO2, membrane technology has been on the spotlight on offshore oil extraction platforms. Its reduced footprint is a major attraction, due to the limited space on the platforms. The present work compares the occupied area and volume and the total weights of 3D arrangements of hollow fiber and spiral wound membrane modules for the separation of CO2 from natural gas in the Brazilian pre-salt. To achieve this, 3D models were built in Solidworks (trademark) software, based on real offshore plants in operation and data provided by leading membrane module suppliers, in an attempt to achieve results closer to reality. It was found that hollow fiber modules offer significant advantages over spiral wound modules in relation to the membrane area of the individual module (8,340.91 m2 vs 26.24 m2 ) and the number of modules required (48 vs 15,120), and also in relation to complete plants, both in area and volume, as well as in weight. A complete hollow fiber module plant would occupy only 7.75 percent of the volume of the spiral wound module plant. The weight of the first would total 38.42 t as opposed to 765.62 t of the second plant.

No description available.

No description available.

No description available.

<p>In this work, two overarching global crises are addressed with an engineering lens; the COVID-19 pandemic and climate change. Regarding the latter, an investigation is completed into the fluxes of CO2 in the wake of a simple wind farm for identification of potentially beneficial siting of Direct Capture of CO2. In this analysis, large-eddy simulations are used to quantify scalar entrainment in the turbines’ wake for several empirical CO2 profiles. In instances with positive or a combination of CO2 gradients, it was found that the concentration of CO2 increased in wake through downward mixing and entrainment. In a negative CO2 gradient, the opposite was found, with the wind turbine mixing away the increased surface<br> concentration and entraining down lower concentration air from above. These findings were used to make recommendations on scenarios in which wind turbines were beneficial to Direct Capture plants.<br> In addition, as part of the ongoing response to the COVID-19 pandemic, an innovative new technology was designed and constructed; a prototype photoacoustic spectrometer for the rapid detection of viruses. With the vision to become a viral "breathalyzer", the primary stage of development involved the creation of a prototype for proof-of-concept of viral detection using PAS. An extensive literature review was completed to determine optimal<br> design, with several distinct innovations integrated with the end-product in mind; such as a pure silicon resonator cell and a light-emitting diode source for low-cost, portable detection.<br> This was estimated to be of sufficient quality to detect single virions, as found through Finite Element Analysis.<br> Additionally, the validation of a proposed improvement on the medical mask, named Hy-Cu, is shown. Through various tests, Hy-Cu was found to have greater breathability than KN95 or surgical masks, as well as comparable efficiency in filtration of viral droplets.<br> Additionally, the novel inclusion of a diamond-like carbon-coated copper mesh layer resulted in viral inactivation of 99% after a period of 2 hours, allowing Hy-Cu to be safely reused without risk of transmission.<br> </p> <p> </p>

Syftet med den här studien är att göra en teknoekonomisk utvärdering av processer för förvätskning av CO2 med hjälp av Aspen Plus. Ett flertal förvätskningsprocesser från tidigare studier jämfördes och från dessa valdes två förvätskningsprocesser ut för fortsatta studier och simuleringar. Dessa två förvätskningsprocesser var ett internt kylt förvätskningssystem och ett externt kylt förvätskningssystem av Øi et al., Energy Procedia 86 (2016) 500-510, som kallats system A, samt av Seo et al., International Journal of Greenhouse Gas Control 35 (2015) 1-12 kallat system B. Dessa två olika processer simulerades för teknisk analys med hjälp av Aspen Plus. Aspen Economical Analyzer (AEA) användes för att göra den ekonomiska analysen. I dessa simuleringar användes ett massflöde på 45 ton/h inkluderat vatteninnehåll, i jämförelse med tidigare studier med högre massflöden runt 100 ton/h. Elektricitet-och kylbehovet undersöktes i ett flertal olika fall med varierande kyltemperatur mellan kompressorerna. Två fall med integrering av fjärrvärme samt två fall med en värmepump undersöktes också med varierande återgående temperatur på fjärrvärmevattnet. Detta gjordes för att undersöka hur mycket värme som kan tillvaratas från förvätskningsprocessen. Vidare bestämdes även investeringskostnader samt driftskostnader med hjälp av AEA. Från detta bestämdes även den årliga kostnaden av kapitalet, CAPEX, och kostnaden att förvätska CO2 räknades ut i form av €/ton.  Resultaten visade att integrering av fjärrvärme samt värmepumpar är användbart för att tillvarata på så mycket värme som möjligt från förvätskningssystemen. I de fall med en värmepump samt en återgående temperatur på 47°C i fjärrvärmenätet hade ett COP på 3.07 samt 3.15 för system A samt system B vardera. Kostanden att förvätska CO2 var 17.42 €/ton för system A samt 17.75 €/ton för system B utan använding av en värmepump samt en återgående temperatur på 47°C i fjärrvärmenätet. Vid integrering av en värmepump gick kostnaden av förvätskning upp till 20.85 €/ton för system A samt 21.69 €/ton för system B. Kostnaden av förvätskning dominerades av driftskostnader med kostnaden av kapitalet har en mindre påverkan. Utnyttjandegraden har även en stor påverkan på kostanden av förvätskning, då lägre kapaciteter visade sig leda till markant högre förvätskningskostnader. När intäkterna från fjärrvärmeproduktionen adderades till kostnadskalkylen, minskade kostnaden av förvätskning, speciellt för de system med en värmepump, där priset minskade till 10.26 €/ton för system A eller 10.98 €/ton för system B. I linje med tidigare studier pekar även dessa resultat på att det ekonomiska optimumet sammanfaller med energioptimum. Resultaten visade även att system A, det internt kylda systemet, hade den lägsta förvätskningskostanden och minsta elektricitetsförbrukningen med och utan värmepump, och därför är system A optimalt för småskalig CO2 förvätskning. / The aim of this study is to do a technoeconomical analysis on CO2 liquefaction systems using Aspen Plus. Several liquefaction systems from previous studies were compared, and from these, two liquefaction systems were chosen for further studies and simulations. These liquefaction systems were namely an internal liquefaction system and an external liquefaction system by Øi et al., Energy Procedia 86 (2016) 500-510, called system A and Seo et al., International Journal of Greenhouse Gas Control 35 (2015) 1-12, called system B. These systems were simulated for technical analysis using Aspen Plus, and Aspen Economical Analyzer (AEA) was used for economical studies. A small-scale liquefaction system was studied with a mass flow rate of 45 tonne/h including the water content, as compared to other studies with higher mass flow rates of around 100 tonne/h. The electricity demand and cooling demand were studied in several cases of interstage cooling between compressors. Furthermore, two cases of district heating as well as two cases of heat pumps were studied with varying return temperatures of the district heating water. This was done to study how much heat could be recovered from the liquefaction process. Furthermore, the capital expenses as well as the operating expenses were also determined using AEA. From this, the annual CAPEX and the cost of CO2 was calculated in terms of €/tonne CO2.  The results showed that district heating and heat pumps can be useful to recover heat from the liquefaction processes. The simulations that included a heat pump and assumed a return temperature of 47°C had a COP of 3.07 and 3.15 for system A and B respectively. The determined cost of production was 17.42 €/tonne for system A and 17.75 €/tonne for system B when not using a heat pump and a return temperature of 47°C in the district heating grid. However, when adding a heat pump the total production cost (TPC) increased to 20.85 €/tonne for system A, and 21.69 €/tonne for system B. It was also shown that the TPC is highly dominated by the operating expenses while the total capital investment has a smaller impact on the TPC. The capacity is also important for the TPC as lower capacities was shown to lead to significantly increased production costs. When taking the revenue streams from district heating into account the TPC was decreased, in particular for the systems including the heat pumps, where the TPC for system A was 10.26 €/tonne while for system B it was 10.98 €/tonne. In accordance with previous studies it was shown that the economical optimum is closely related to the energy optimum. It was concluded that as system A, the internal liquefaction system, had the lowest TPC and electricity input with and without the heat pump and thus it is the optimal configuration for small-scale CO2 liquefaction.

Att koldioxidutsläppen neutraliseras är avgörande för att begränsa klimatförändringarna. Bioenergi i kombination med separation och lagring av koldioxid (BECCS) är en Teknik som kan generera negativa utsläpp. Det största hindret för dess storskaliga genomförande är de höga energikraven för processen. Detta projekt syftar till att kvantifiera energistraffen för lean solvent flash och modifikationer för multitrycksstrippning för att förbättra prestandan av koldioxidavskiljning (CC) i en kraftvärmeverksanläggning för förbränning av biomassa.  En jämviktsmodell utvecklades och validerades för att simulera en fullskalig CC genom kemisk absorption i Aspen Plus med kaliumkarbonat som lösningsmedel. Båda layoutändringarna resulterar i energipåföljder på 18-21 % för en kraftvärmeverk, medan energistraffet för baslinjeprocessen är 5 %. För ett kraftverk går straffen från 32 till 62 %. Detta visar hur en förbättring av processen kan minska kostnaderna för CCS, särskilt om värme anses vara en värdefull produkt. CCS i kraftvärmeverk har en mycket lägre energipåverkan än i kraftverk där värme inte återvinns. / Bio-energy with carbon capture and storage (BECCS) is a technology that can generate negative emissions. Hence it is recognized as a solution for becoming carbon neutral, which is essential for climate change mitigation. The main obstacle for its large scale implementation is the high energy requirements of the process. This thesis aims at quantifying the energy penalties for lean solvent flash and multi-pressure stripper layout modifications to improve the performance of carbon capture (CC) by means of absorption with a liquid solvent in a biomass-fired CHP plant. The work focuses on K2CO3 based solvents operated in a mixed temperature swing/pressure swing cycle witch is deemed advantageous for heat recovery.  An equilibrium model was developed and validated to simulate a full-scale CC by chemical absorption in Aspen Plus using potassium carbonate as solvent. Both layout modifications result in energy penalties of 18-21 % for a CHP plant, while the energy penalty for the baseline process is 28 %. For a power plant, the penalties go from 32 % to 62 % for the lean solvent flash and the multi-pressure stripper respectively. This shows how improving the process can reduce the costs of CCS, especially if heat is considered a valuable product. CCS in CHP plants has a much lower energy impact than in power plants where heat is not recovered.

Mitigating greenhouse gas emissions from the Swedish industry is central in reaching set up environmental goals on a national level and fighting climate change that results in economic, environmental and social disasters on a global scale. The efforts of mitigating greenhouse gas emissions from the Swedish industry have historically focused on investing in renewable technologies that have no emissions from production. However, to rapidly decrease emissions of greenhouse gases, such as carbon dioxide, could be done by sequestering the gas from point sources at the industry sites and thereafter transport it to geological formations on- and offshore in a process more commonly known as Carbon Capture and Storage. Even so, the Carbon Capture and Storage technology is relatively new and has not yet been implemented on an industrial scale in Sweden. The real potential of Carbon Capture and Storage in relation to helping the Swedish industry in reaching set up national and international environmental goals is therefore unknown. Here we show, via a literature review and performing interviews with stakeholders from the investigated field, that there is a big potential for Carbon Capture and Storage to mitigate carbon dioxide emissions from the Swedish industry and create negative emission rates by storing emissions originated from biogenic sources.   Our results demonstrate that there are regulatory, economic, environmental, and social measures that are needed to create a future market for Carbon Capture and Storage and trading with negative emissions. These include evaluating domestic storage sites, changing laws and regulations, and sharing knowledge between countries and companies to create a wider understanding of the technology. We anticipate that our study on the dynamics of a Carbon Capture and Storage market will help stakeholders to identify levers and restraints in the current market so that the transition towards net zero emissions will accelerate, especially when having the national 2045 net zero emission objective in mind. Nonetheless, there is a great need for research to understand such a market, and more specifically to create a consensus between stakeholders on a national and global level when creating it. / Att minska växthusgasutsläppen från den svenska industrin är centralt för att nå nationella och globala klimatmål och vidare bekämpa klimatförändringar som på en global skala resulterar i ekonomiska, miljömässiga och samhälleliga katastrofer. Historiskt sett har åtgärderna för att minska utsläppen av växthusgaser främst legat på satsningar inom förnybara tekniker där utsläppen från produktion är nästintill noll. Däremot behövs åtgärder för att snabbt minska utsläppen av växthusgaser, såsom koldioxid, där detta kan göras genom att avskilja koldioxiden från industriernas punktkällor och sedan lagra gasen på land och till havs genom en process som är mer känd under namnet koldioxidavskiljning och lagring. Trots detta är koldioxidavskiljning och lagring en relativt ny teknik som inte har tillämpats på industriell skala i Sverige. Teknologins verkliga potential för att uppfylla nationella och globala klimatmål är därför outforskad. Studien visar, genom en litteraturstudie och semistrukturerade intervjuer med intressenter inom forskningsområdet, att tekniken koldioxidavskiljning och lagring har stor potential när det kommer till att minska koldioxidutsläpp från den svenska industrin och även när det kommer till att skapa negativa emissioner av koldioxid genom lagring av biogen koldioxid.   Resultatet visar att det är regulatoriska, ekonomiska, miljömässiga och samhälleliga åtgärder som är nödvändiga för att skapa en framtida marknad för koldioxidavskiljning och lagring och handel med negativa utsläpp. Dessa innefattar utvärdering av inhemska lagringsplatser, ändring av lagar och regler samt att sprida och dela kunskap mellan länder och företag för att skapa en vidare förståelse av teknologin. Vi förutser att användningsområdet för studien av en framtida marknad för koldioxidavskiljning och lagring kan hjälpa intressenter inom forskningsområdet att identifiera åtgärder som kan verka som hävarm och även hinder för en framtida utveckling mot nettonollutsläpp. Detta då de svenska miljökvalitetsmålen fastslår att nettonollutsläpp senast ska nås år 2045. Däremot behövs vidare studier för att förstå en framtida marknad för koldioxidavskiljning och lagring samt negativa emissioner, mer specifikt behövs konsensus mellan intressenter på en nationell och global nivå för att skapa en sådan marknad.

Carbon dioxide capture, transportation, and storage has been identified as the most promising way to reduce anthropogenic carbon dioxide (CO2) released into the atmosphere. Efforts made to achieve this purpose include the Paris (Climate) Accord. This agreement seeks to encourage countries to take the issue of rising global temperatures seriously. With nearly all countries signing this agreement, many CCTS projects are expected. Pipelines are employed in the transportation of CO2. CO2 fluids contain impurities that affect the fluid properties and flow dynamics, but pipelines are mostly designed assuming that the CO2 fluid is pure. CO2 pipeline fluids contain at least 90 % CO2 with the balance made up of impurities. The impurities include nitrogen, methane, oxygen, hydrogen, sulphur dioxide, hydrogen sulphide, carbon monoxide, ammonia, argon, etc. The effects of the impurities are studied using simulation software; Aspen HYSYS, gPROMS and HydraFlash. The results show that all impurities impacted negatively on transportation. At equal concentrations, hydrogen had the greatest effect on fluid properties and hydrogen sulphide the least impact. At the specified allowable concentration, nitrogen had the worst effect on pressure loss (32.1 %) in horizontal pipeline, density, and critical pressure. Carbon monoxide (with only 0.2-mol %) had the smallest effect in pressure drop (0.3 %). Analysis of supercritical and subcritical (or liquid) CO2 fluid transportation shows that subcritical fluids have higher densities (more volume transported) and lower pressure losses than supercritical fluids. Subcritical fluid transportation would therefore have lower pipeline transportation costs than supercritical fluids. Also, soil heat conductivity has greater effect than ambient temperature in buried pipelines. Simple equations that approximate binary CO2 fluid properties from pure CO2 properties were developed and presented.