Tesis sobre el tema "CO2 capture and conversion"
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Brandvoll, Øyvind. "Chemical looping combustion : fuel conversion with inherent CO2 capture". Doctoral thesis, Norwegian University of Science and Technology, Department of Energy and Process Engineering, 2005. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-1203.
Texto completoChemical looping combustion (CLC) is a new concept for fuel energy conversion with CO2 capture. In CLC, fuel combustion is split into seperate reduction and oxidation processes, in which a solid carrier is reduced and oxidized, respectively. The carrier is continuously recirculated between the two vessels, and hence direct contact between air and suel is avoided. As a result, a stoichiometric amount of oxygen is transferred to the fuel by a regenerable solid intermediate, and CLC is thus a varient of oxy-fuel combustion. In principle, pure CO2 can be obtained from the reduction exhaust by condensation of the produced water vapor. The termodynamic potential and feasibility of CLC has been studied by means of process simulatons and experimental studies of oxygen carriers. Process simulations have focused on parameter sensitivity studies of CLC implemented in 3 power cycles; CLC-Combined Cycle, CLC-Humid Air Turbine and CLC-Integrated Steam Generation. Simulations indicate that overall fuel conversion ratio, oxidation temperature and operating pressure are among the most imortant process parameters in CLC. A promising thermodynamic potentail of CLC has been found, with efficiencies comparable to, - or better than existing technologies for CO2 capture. The proposed oxygen carrier nickel oxide on nickel spinel (NiONiA1) has been studied in reduction with hydrogen, methane and methane/steam as well as oxidation with dry air. It has been found that at atmosphereic pressure and temperatures above 600° C, solid reduction with dry methane occurs with overall fuel conversion of 92%. Steam methane reforming is observed along with methane cracking as side reactions, yealding an overall selectivity of 90% with regard to solid reduction. If steam is added to the reactant fuel, coking can be avoided. A methodology for long term investigation of solid chemical activity in a batch reactor is proposed. The method is based on time variables for oxidaton. The results for NiONiA1 do not rule out CLC as a viable alternative for CO2 capture, but long term durability studies along with realistic testing of the carrier in a continuous rig is needed to firmly conclude. For comparative purposes a perovskite was synthesized and tested in CLC, under similar conditions as NiONiA1. The results indicate that in a moving bed CLC application, perovskites have inherent disadvantages as compared to simpler compounds, by virtue of low relative oxygen content.
Kim, Hyung Rae. "Chemical Looping Process for Direct Conversion of Solid Fuels In-Situ CO2 Capture". The Ohio State University, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=osu1250605561.
Texto completoMARCHESE, MARCO. "Conversion of industrial CO2 to value-added fuels and chemicals via Fischer-Tropsch upgrade". Doctoral thesis, Politecnico di Torino, 2021. http://hdl.handle.net/11583/2914540.
Texto completoShokouhfar, Nasrin. "Synthèse et caractérisation de nouvelles armatures métal-organique à base de zirconium à partir de ligands carboxylates et étude de leur application dans l'adsorption et la détection des pollutions de l'eau et la capture et la conversion du CO2 et N2". Electronic Thesis or Diss., Université de Lille (2022-....), 2023. http://www.theses.fr/2023ULILN058.
Texto completoThis thesis investigates the synthesis and characterization of Zr-based metal-organic frameworks (MOFs) and their applications in water treatment and solar fuel production. MOFs are porous materials composed of metal ions and organic linkers that exhibit tuneable structures and functionalities. These properties make them suitable for various applications, such as gas storage, catalysis, sensing, drug delivery, etc.Water treatment is the process of removing contaminants from water to make it safe and clean for human use. One of the main contaminants in water are dyes, which are widely used in the textile, paper, and leather industries. Dye pollution can cause serious problems for aquatic life, human health, and aesthetic quality of water. To remove dyes from water, we synthesized a new Zr-MOF called TMU-66, which has a hollow sphere shape and an N-oxide functional group. TMU-66 can efficiently and selectively adsorb dye molecules through various interactions, such as electrostatic attraction, π-π stacking, and coordination bonding. TMU-66 exhibited and adsorption capacity of 472 mg/g for Congo red dye at pH 6.8 and 25 °C, one of the highest values achieved for MOF-based adsorbents so far.Solar fuel production is the process of converting solar energy into chemical fuels that can be stored and used later. One of the most promising fuels is ammonia (NH3), which can be produced from nitrogen (N2) and water (H2O) using sunlight as the energy source. This process is called N2 photoreduction or photocatalytic nitrogen fixation. However, this process is challenging because N2 is very stable and difficult to break apart. We modified another Zr-MOF called MOF-808 by adding a nitro group to its linker. The modified framework is able to absorb visible light and transfer electrons to N2 molecules. We also combined MOF-808/NIP with another material called g-C3N4, which can enhance light absorption and electron transfer. The resulting composite, MOF-808/NIP@g-C3N4, can produce up to 490 μmol ammonia per gram of composite per hour under visible light and ambient conditions.In summary, the objectives of this thesis work were to investigate the potential of MOFs for two distinct applications, utilizing a conceptual design approach that incorporated bandgap engineering, structure modulation, and heterojunction composite materials. The findings revealed that MOFs can absorb water impurities and function as photocatalysts to achieve ammonia production through solar-powered N2 photoreduction. This breakthrough has the potential to foster the creation of more effective and environmentally conscious technologies that tackle worldwide water pollution and ammonia production issues. These technologies are crucial in safeguarding our planet and guaranteeing a stable future
Ramkumar, Shwetha. "CALCIUM LOOPING PROCESSES FOR CARBON CAPTURE". The Ohio State University, 2010. http://rave.ohiolink.edu/etdc/view?acc_num=osu1274882053.
Texto completoDaza, Yolanda Andreina. "Closing a Synthetic Carbon Cycle: Carbon Dioxide Conversion to Carbon Monoxide for Liquid Fuels Synthesis". Scholar Commons, 2016. http://scholarcommons.usf.edu/etd/6079.
Texto completoTrompelt, Michael. "Untersuchung von Möglichkeiten zur Wirkungsgradsteigerung von braunkohlegefeuerten IGCC-Kraftwerken mit CO2-Abtrennung". Doctoral thesis, Technische Universitaet Bergakademie Freiberg Universitaetsbibliothek "Georgius Agricola", 2015. http://nbn-resolving.de/urn:nbn:de:bsz:105-qucosa-158214.
Texto completoDanaci, Simge. "Optimisation et intégration de catalyseurs structurés en réacteurs structurés pour la conversion de CO₂ en méthane". Thesis, Université Grenoble Alpes (ComUE), 2017. http://www.theses.fr/2017GREAI041/document.
Texto completoIn this doctoral study, the three dimensional fibre deposition (3DFD) technique has been applied to develop and manufacture advanced multi-channelled catalytic support structures. By using this technique, the material, the porosity, the shape and size of the channels and the thickness of the fibres can be controlled. The aim of this research is to investigate the possible benefits of 3D-designed structured supports for CO2 methanation in terms of activity, selectivity and stability and the impact of specific properties introduced in the structural design of the supports
Zeng, Liang. "Multiscale Study of Chemical Looping Technology and Its Applications for Low Carbon Energy Conversions". The Ohio State University, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=osu1354722135.
Texto completoOlivieri, Luca <1987>. "Polymeric membranes for CO2 capture". Doctoral thesis, Alma Mater Studiorum - Università di Bologna, 2016. http://amsdottorato.unibo.it/7418/4/olivieri_luca_tesi.pdf.
Texto completoOlivieri, Luca <1987>. "Polymeric membranes for CO2 capture". Doctoral thesis, Alma Mater Studiorum - Università di Bologna, 2016. http://amsdottorato.unibo.it/7418/.
Texto completoXu, Shaojun. "Plasma-assisted conversion of CO2". Thesis, University of Manchester, 2017. https://www.research.manchester.ac.uk/portal/en/theses/plasmaassisted-conversion-of-co2(19c87dfa-ba79-47ea-a63d-0a0026a03bba).html.
Texto completoDugstad, Tore y Esben Tonning Jensen. "CO2 Capture from Coal fired Power Plants". Thesis, Norwegian University of Science and Technology, Department of Energy and Process Engineering, 2008. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-9770.
Texto completoCoal is the most common fossil resource for power production worldwide and generates 40% of the worlds total electricity production. Even though coal is considered a pollutive resource, the great amounts and the increasing power demand leads to extensive use even in new developed power plants. To cover the world's future energy demand and at the same time limit our effect on global warming, coal fired power plants with CO2 capture is probably a necessity. An Integrated Gasification Combined Cycle (IGCC) Power Plant is a utilization of coal which gives incentives for CO2 capture. Coal is partially combusted in a reaction with steam and pure oxygen. The oxygen is produced in an air separation process and the steam is generated in the Power Island. Out of the gasifier comes a mixture of mainly H2 and CO. In a shift reactor the CO and additional steam are converted to CO2 and more H2. Carbon dioxide is separated from the hydrogen in a physical absorption process and compressed for storage. Hydrogen diluted with nitrogen from the air separation process is used as fuel in a combined cycle similar to NGCC. A complete IGCC Power Plant is described in this report. The air separation unit is modeled as a Linde two column process. Ambient air is compressed and cooled to dew point before it is separated into oxygen and nitrogen in a cryogenic distillation process. Out of the island oxygen is at a purity level of 95.6% and the nitrogen has a purity of 99.6%. The production cost of oxygen is 0.238 kWh per kilogram of oxygen delivered at 25°C and 1.4bar. The oxygen is then compressed to a gasification pressure of 42bar. In the gasification unit the oxygen together with steam is used to gasify the coal. On molar basis the coal composition is 73.5% C, 22.8% H2, 3.1% O2, 0.3% N2 and 0.3% S. The gasification temperature is at 1571°C and out of the unit comes syngas consisting of 66.9% CO, 31.1% H2, 1.4% H2O, 0.3% N2, 0.2% H2S and 0.1% CO2. The syngas is cooled and fed to a water gas shift reactor. Here the carbon monoxide is reacted with steam forming carbon dioxide and additional hydrogen. The gas composition of the gas out of the shift reactor is on dry basis 58.2% H2, 39.0% CO2, 2.4% CO, 0.2% N2 and 0.1% H2S. Both the gasification process and shift reactor is exothermal and there is no need of external heating. This leads to an exothermal heat loss, but parts of this heat is recovered. The gasifier has a Cold Gas Efficiency (CGE) of 84.0%. With a partial pressure of CO2 at 15.7 bar the carbon dioxide is easily removed by physical absorption. After separation the solvent is regenerated by expansion and CO2 is pressurized to 110bar to be stored. This process is not modeled, but for the scrubbing part an energy consumption of 0.08kWh per kilogram CO2 removed is assumed. For the compression of CO2, it is calculated with an energy consumption of 0.11kWh per kilogram CO2 removed. Removal of H2S and other pollutive unwanted substances is also removed in the CO2 scrubber. Between the CO2 removal and the combustion chamber is the H2 rich fuel gas is diluted with nitrogen from the air separation unit. This is done to increase the mass flow through the turbine. The amount of nitrogen available is decided by the amount of oxygen produced to the gasification process. Almost all the nitrogen produced may be utilized as diluter except from a few percent used in the coal feeding procedure to the gasifier. The diluted fuel gas has a composition of 50.4% H2, 46.1% N2, 2.1% CO and 1.4% CO2. In the Power Island a combined cycle with a gas turbine able to handle large H2 amounts is used. The use of steam in the gasifier and shift reactor are integrated in the heat recovery steam generator (HRSG) in the steam cycle. The heat removed from the syngas cooler is also recovered in the HRSG. The overall efficiency of the IGCC plant modeled is 36.8%. This includes oxygen and nitrogen production and compression, production of high pressure steam used in the Gasification Island, coal feeding costs, CO2 removal and compression and pressure losses through the processes. Other losses are not implemented and will probably reduce the efficiency.
DeLucia, David Earl. "Cyclic use of limestone for CO2 capture". Thesis, Massachusetts Institute of Technology, 1985. http://hdl.handle.net/1721.1/15136.
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Bibliography: leaf 150.
by David Earl DeLucia.
M.S.
Higby, Joshua. "Conversion of CO2 to higher alcohols". Thesis, Luleå tekniska universitet, Industriell miljö- och processteknik, 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:ltu:diva-83392.
Texto completoIn this work, a thermodynamic analysis for CO2 hydrogenation by co-feeding ethanol to higher alcohols was performed with the HSC software package. The results suggested a high pressure and a low temperature for the reaction. However, it yielded low equilibrium compositions for the higher alcohols even at a high pressure of 100 bar at 300C . Increasing the equilibrium compositions for the higher alcohols can be done by removing water. A mathematical model was used to analyse the rate-limiting step in a process for the production of higher alcohols from CO2. In this process, reverse water gas shift (RWGS) reaction was used to convert CO2 to CO, subsequently, the obtained CO reacts with ethanol and hydrogen to produce higher alcohols directly. The mathematical model was developed in MATLAB to simulate how the reaction could behave by feeding CO2, H2 and ethanol at different pressures ranging from 10-200 bars. The water removal effect on the equilibrium is measured in terms of CO2 conversion by achieving 95% for removing water. The results indicated that the process can be used to convert CO2 to higher alcohols and at a lower pressure. The limiting factor for CO2 hydrogenation is the reaction mechanism, it’s an urgent problem for the development of the catalysts. In this model it was assumed to be a logistic function. The conversion of CO2 into higher alcohols is an important problem that is required to be addressed by more experimental verifications to understand the mechanism. The literature review shows that there is no available membrane for removal of water for the process currently, due to the harsh process conditions, mainly because of the membrane stability. However, membrane technology is a promising method for separation of water/organic mixtures that can be studied further in the future.
Ingvarsdóttir, Anna. "Comparison of direct air capture technology to point source CO2 capture in Iceland". Thesis, KTH, Kemiteknik, 2020. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-289164.
Texto completoIt is well known that climate change due to global warming is one of the greatest crises facing the Earth. It is a huge challenge for mankind to reduce CO2 emissions, the major cause of global warming. Mitigation measures are not enough. Technologies to remove the CO2 from the atmosphere are considered necessary, so the temperature rise does not exceed 1.5°C as stated in the Paris Agreement. Direct air capture (DAC) is a new technology that can remove carbon dioxide directly from the atmosphere. Currently, this method is expensive, up to 1000 USD per ton CO2 removed. This high cost is mostly due to the relatively low concentration of CO2 in the ambient air, leading to a large unit to capture the gas and therefore high capital investment. The technology is very energy-intensive, either electrical or thermal, and to make direct air capture more efficient the plant needs to be powered with energy that has no or very low CO2 emissions. The energy in Iceland is low cost and its production has a very low carbon footprint. This thesis aims to find out if the direct air capture method will be more feasible than a point source CO2 capture in Iceland due to good access to low-cost and clean energy. The learning curve for direct air capture was studied along with scenarios for its technological development. Two different direct air capture technologies were analyzed, one that is powered by a large amount of electricity and one powered mostly by thermal energy. Three different point source cases in Iceland were studied for comparison. For the best-case scenario, where the learning rate is high and technological improvements are significant, the levelized cost of direct air capture is lower than levelized cost of point source capture. The cost of energy affects the levelized cost of direct air capture today but with technical development, the energy needed is expected to go down, and therefore the effect of energy cost will be lower. However, it is still important, concerning contribution to reducing global warming, that the energy powering the direct air capture plant has a low carbon footprint, which can be assured in Iceland. On the contrary, if the learning rate of the direct air capture technology is low and no technical improvements occur in solvents or sorbents the direct air capture technology is and will be more expensive than point source capture considering both located in Iceland. The high learning rate and development in technology are dependent on the pressure to reach the goals of the Paris Agreement. It is therefore vital for direct air capture that the demand for carbon removal measures is enhanced due to pressure to reach the Paris Agreement goals. Furthermore, direct air capture has more potential to affect climate change than point source capture as direct air capture can be a carbon-negative technology if coupled with the permanent storage of CO2. The point source capture can only be a carbon-neutral technology if coupled with the permanent storage of CO2.
Hu, Yukun. "CO2 capture from oxy-fuel combustion power plants". Licentiate thesis, KTH, Energiprocesser, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-48666.
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Westman, Snorre Foss. "Power plant with CO2 capture based on adsorption". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-18504.
Texto completoEkre, Kjetil Vinjerui. "Novel Processes for Power Plant with CO2 Capture". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-19372.
Texto completoChampagne, Scott. "Steam Enhanced Calcination for CO2 Capture with CaO". Thèse, Université d'Ottawa / University of Ottawa, 2014. http://hdl.handle.net/10393/30905.
Texto completoParker, Qamreen. "Molecular simulations of ionic liquids for CO2 capture". Thesis, University College London (University of London), 2018. http://discovery.ucl.ac.uk/10048467/.
Texto completoAmara, Soumia. "CO2 capture in industry using chilled ammonia process". Thesis, KTH, Energiprocesser, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-292504.
Texto completoHiggins, Stuart James. "Design and Optimization of Post-Combustion CO2 Capture". Diss., Virginia Tech, 2016. http://hdl.handle.net/10919/80003.
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Molinder, Roger Axel. "CO2 capture materials for sorption enhanced steam reforming". Thesis, University of Leeds, 2012. http://etheses.whiterose.ac.uk/2871/.
Texto completoBernadet, Sophie. "Conversion photocatalytique du CO2 sur monolithes poreux". Thesis, Bordeaux, 2018. http://www.theses.fr/2018BORD0172/document.
Texto completoIn the current context of developing novel non-fossil energy sources while minimizing the environmental impact, solar-driven-fuel-production by exploiting anthropogenic CO2 emissions appears to be a solution with great potential. The main challenge in artificial photo-induced processes concerns the two-dimensional character of the systems used, due to the low photon penetration depth. This thesis work focuses on the development of alveolar solid foams, derived from integrative chemistry and bearing a hierarchically organized porosity. By TiO2 precursor impregnation, self-standing photocatalysts were synthesized and provided a photon penetration increase by an order of magnitude. Moreover, these solids limit back-reactions by a dilution effect, while ensuring high selectivity towards alkane generations. A kinetic model, based on a mixed formalism of Langmuir-Hinshelwood and Eley-Rideal, is proposed to describe material behavior
TARRARAN, LOREDANA. "Microbial CO2 conversion to value-added products". Doctoral thesis, Politecnico di Torino, 2022. http://hdl.handle.net/11583/2967854.
Texto completoNogalska, Adrianna. "Ambient carbon dioxide capture and conversion via membranes". Doctoral thesis, Universitat Rovira i Virgili, 2018. http://hdl.handle.net/10803/664718.
Texto completoEl cambio climático causado por el aumento del contenido de CO2 en la atmósfera está causando gran preocupación hoy en día. La constante necesidad de generación de energía verde nos inspiró a desarrollar un sistema fotosintético artificial. El sistema funciona como una hoja, donde el CO2 se capta directamente del aire a través de los poros de la membrana y pasa a los siguientes compartimentos para convertirse finalmente en metanol o otros hidrocarburos y sera utilizado como combustible. El objetivo principal del trabajo es revelar la influencia de los contactores de membrana basados en polisulfona sobre la tasa de captura de CO2 atmosférico mediante absorción química en soluciones acuosas. Las membranas de láminas planas que varían en morfología se prepararon por precipitación y se sometieron a caracterización de morfología interna y de la superficie. La membrana de polisulfona se modificó con una serie de aditivos conocidos por la afinidad de CO2, tales como: nenopartículas de ferrita, carbón activado y enzimas. Además, la compatibilidad entre las membranas y la solución absorbente se evaluó en términos de medidas de hinchamiento y ángulo de contacto. Además, se realizaron estudios preliminares sobre la conversión de CO2 capturada en combustibles con el uso de una unidad electroreductora. Los estudios mostraron que el sistema basado en polisulfona tiene una asimilación de CO2 superior en comparación con el rendimiento de una hoja. Además, los mejores resultados se obtuvieron utilizando una membrana en blanco y sin modificar, lo que proporciona un bajo costo de producción. Además, se logró la conversión de bicarbonato a ácido fórmico, dando un comienzo prometedor para mejorar en el trabajo futuro.
The climate change caused by the increased CO2 content in the atmosphere is raising a lot of concern nowadays. The constant need for sustainable green energy generation inspired us to develop an artificial photosynthetic system. The system works as a leaf, where CO2 is captured directly from air through the membrane pores and passes to the next compartments to be finally converted to methanol or other hydrocarbons and to be further used as fuel in fuel cells. The main scope of the work is to reveal the influence of polysulfone -based membrane contactors on atmospheric CO2 capture rate by chemical sorption into absorbent aqueous solutions. Flat sheet membranes that vary in morphology were prepared by immersion precipitation and undergo internal morphology and surface characterization. The polysulfone membrane was modified with a number of additives known for the CO2 affinity such as: ferrite nenoparticles, activated carbon and enzymes. Moreover, the compatibility between membranes and absorbent solution was evaluated in terms of swelling and contact angle measurements. Additionally, preliminary studies concerning the captured CO2 conversion to fuels were performed with use of electro-reductive unit. Studies showed that the polysulfone based system has superior CO2 assimilation compared to a leaf performance. Moreover, the best results were obtained using blank and unmodified membrane, providing a low production cost. Furthermore, the conversion of bicarbonate to formic acid was achieved, giving a promising start to be improved in future work.
Bilsbak, Vegard. "Conditioning of CO2 coming from a CO2 capture process for transport and storage purposes". Thesis, Norwegian University of Science and Technology, Department of Energy and Process Engineering, 2009. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-9943.
Texto completoVITTONI, CHIARA. "Hybrid Organic-Inorganic Materials for CO2 Capture and Utilization". Doctoral thesis, Università del Piemonte Orientale, 2018. http://hdl.handle.net/11579/97188.
Texto completoBusu, Alice. "Development of PVA/PDA nanocomposite membranes for CO2 capture". Master's thesis, Alma Mater Studiorum - Università di Bologna, 2020.
Buscar texto completoBaig, Yasir. "Technology qualification for IGCC power plant with CO2 Capture". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2011. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-14712.
Texto completoSamari, Mohammad. "CO2 Capture from Dilute Sources via Lime-Based Sorbents". Thèse, Université d'Ottawa / University of Ottawa, 2014. http://hdl.handle.net/10393/30978.
Texto completoStene, Henrik Sørskår y Ole Marius Moen. "Power Plant with CO2 Capture based on PSA Cycle". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2014. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-26240.
Texto completoBiyouki, Zeinab Amrollahi. "Thermodynamic analysis of CO2 capture processes for power plants". Doctoral thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2014. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-26380.
Texto completoAli, Usman. "Process simulation of power generation systems with CO2 capture". Thesis, University of Sheffield, 2017. http://etheses.whiterose.ac.uk/16011/.
Texto completoEsam, Odette Amana. "CO2 Capture on Porous Adsorbents Containing Surface Amino Groups". Digital Commons @ East Tennessee State University, 2013. https://dc.etsu.edu/etd/2304.
Texto completoGILLONO, MATTEO. "3D printable materials for CO2 capture and separation technologies". Doctoral thesis, Politecnico di Torino, 2020. http://hdl.handle.net/11583/2827712.
Texto completoAmado, Verónica Catarina Ferreira. "“One-pot” enzymatic conversion of CO2 to methanol". Master's thesis, Faculdade de Ciências e Tecnologia, 2013. http://hdl.handle.net/10362/10900.
Texto completoMOROSANU, EDUARD ALEXANDRU. "Catalytic processes for CO2 conversion into Synthetic Methane". Doctoral thesis, Politecnico di Torino, 2020. http://hdl.handle.net/11583/2841162.
Texto completoLIENDO, CASTILLO FREDDY JESUS. "CO2 conversion through the synthesis of CaCO3 nanoparticles". Doctoral thesis, Politecnico di Torino, 2021. http://hdl.handle.net/11583/2907014.
Texto completoKolle, Joel Motaka. "Mesoporous Organosilicas for CO2 Capture and Utilization: Reaction Insight and Material Development". Thesis, Université d'Ottawa / University of Ottawa, 2020. http://hdl.handle.net/10393/40464.
Texto completoErrey, Olivia Claire. "Variable capture levels of carbon dioxide from natural gas combined cycle power plant with integrated post-combustion capture in low carbon electricity markets". Thesis, University of Edinburgh, 2018. http://hdl.handle.net/1842/33240.
Texto completoYstad, Paul Andreas Marchioro. "Power Plant with CO2 Capture based on Absorption : Integration Study". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2010. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-11057.
Texto completoLeifsen, Henning. "Post-Combustion CO2 Capture Using Chemical Absorption : Minimizing Energy Requirement". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2007. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-12865.
Texto completoJohnsen, Erik Lien. "Optimization based design of an IRCC process with CO2 capture". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for industriell økonomi og teknologiledelse, 2011. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-15070.
Texto completoRustenberg, Karin Hveding. "X-ray Studies of Capture, Storage and Release of CO2". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for fysikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-18889.
Texto completoSymonds, Robert. "Development of a Continuous Calcium Looping Process for CO2 Capture". Thesis, Université d'Ottawa / University of Ottawa, 2017. http://hdl.handle.net/10393/36454.
Texto completoWangen, Dan Jakob. "Life Cycle Assessment of Power Generation Technologies with CO2 Capture". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-19393.
Texto completoLlorente, Manso Ricardo. "CO2 capture in power plants- using the oxy-combustion principle". Thesis, Norges teknisk-naturvitenskapelige universitet, Institutt for energi- og prosessteknikk, 2013. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-22791.
Texto completoSkinnemoen, Maria Magnussen. "Process Simulation of Oxy-combustion CO2 Capture in Cement Plant". Thesis, Norges Teknisk-Naturvitenskapelige Universitet, Institutt for elkraftteknikk, 2014. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-27337.
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