Relevant bibliographies by topics / Reversible CO2 capture

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  1. Journal articles
  2. Dissertations / Theses
  3. Book chapters
  4. Conference papers
  5. Reports

Academic literature on the topic 'Reversible CO2 capture'

Author: Grafiati
Published: 4 June 2021
Last updated: 15 February 2022

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Journal articles on the topic "Reversible CO2 capture"

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Yang, Hongwei, Abdullah M. Khan, Youzhu Yuan, and Shik Chi Tsang. "Mesoporous Silicon Nitride for Reversible CO2 Capture." Chemistry - An Asian Journal 7, no. 3 (January 13, 2012): 498–502. http://dx.doi.org/10.1002/asia.201100615.

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Gupta, Kapil, Shubra Singh, and M. S. Ramachandra Rao. "Fast, reversible CO2 capture in nanostructured Brownmillerite CaFeO2.5." Nano Energy 11 (January 2015): 146–53. http://dx.doi.org/10.1016/j.nanoen.2014.10.016.

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Ma, Rui, Pan Hu, Li Xu, Jinxu Fan, Yutang Wang, Muqian Niu, and Shenming Tao. "Nanostructured polyethylenimine decorated palygorskite for reversible CO2 capture." Materials Express 7, no. 4 (August 1, 2017): 253–60. http://dx.doi.org/10.1166/mex.2017.1374.

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Lin, Yu-Jeng, and Gary T. Rochelle. "Approaching a reversible stripping process for CO2 capture." Chemical Engineering Journal 283 (January 2016): 1033–43. http://dx.doi.org/10.1016/j.cej.2015.08.086.

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Hanusch, Jan M., Isabel P. Kerschgens, Florian Huber, Markus Neuburger, and Karl Gademann. "Pyrrolizidines for direct air capture and CO2 conversion." Chemical Communications 55, no. 7 (2019): 949–52. http://dx.doi.org/10.1039/c8cc08574a.

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Pollet, Pamela, and Charles Liotta. "Sustainable Chemistry: Reversible reaction of CO2 with amines." French-Ukrainian Journal of Chemistry 4, no. 1 (2016): 14–22. http://dx.doi.org/10.17721/fujcv4i1p14-22.

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The reaction of primary and secondary amines with CO2 has been successfully leveraged to develop sustainable processes. In this article, we review specific examples that use the reversible reaction of CO2 with amines to synergistically enhance reaction and recovery of the products. The three cases of interest highlighted herein are: (i) reversible protection of amines, (ii) reversible ionic liquids for CO2 capture and chemical transformations, and (iii) reversible gels of ethylene diamine. These examples demonstrate that the reversible reaction of amines with CO2 is one of the tools in the sustainable technology’s toolbox.
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Mishra, Ashish Kumar, and Sundara Ramaprabhu. "Nanostructured polyaniline decorated graphene sheets for reversible CO2 capture." Journal of Materials Chemistry 22, no. 9 (2012): 3708. http://dx.doi.org/10.1039/c2jm15385h.

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Barzagli, Francesco, Sarah Lai, and Fabrizio Mani. "Novel non-aqueous amine solvents for reversible CO2 capture." Energy Procedia 63 (2014): 1795–804. http://dx.doi.org/10.1016/j.egypro.2014.11.186.

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Wielend, Dominik, Dogukan Hazar Apaydin, and Niyazi Serdar Sariciftci. "Anthraquinone thin-film electrodes for reversible CO2 capture and release." Journal of Materials Chemistry A 6, no. 31 (2018): 15095–101. http://dx.doi.org/10.1039/c8ta04817g.

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Nousir, Saadia, Vasilica-Alisa Arus, Tze Chieh Shiao, Nabil Bouazizi, René Roy, and Abdelkrim Azzouz. "Organically modified activated bentonites for the reversible capture of CO2." Microporous and Mesoporous Materials 290 (December 2019): 109652. http://dx.doi.org/10.1016/j.micromeso.2019.109652.

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Dissertations / Theses on the topic "Reversible CO2 capture"

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Momin, Farhana. "Reaction of sulfur dioxide (SO2) with reversible ionic liquids (RevILs) for carbon dioxide (CO2) capture." Thesis, Georgia Institute of Technology, 2012. http://hdl.handle.net/1853/47525.

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Silylated amines, also known as reversible ionic liquids (RevILs), have been designed and structurally modified by our group for potential use as solvents for CO₂ capture from flue gas. An ideal CO₂ capture ionic liquid should be able to selectively and reversibly capture CO₂ and have tolerance for other components in flue gas, including SO₂, NO₂, and O₂. In this project, we study the reactivity, selectivity, uptake capacity, and reversibility of RevILs in the presence of pure SO₂ and mixed gas streams tosimulate flue gas compositions. Tripropylsilylamine (TPSA), a candidate CO₂ capture RevIL, reacts with pure SO₂ to form an ionic liquid consisting of an ammonium group and a salfamate group, supported by IR and NMR results. The resulting IL with pure SO₂ partially reverses when heated to temperatures of upto 500 C in the TGA. TGA analysis of the ionic liquid formed from a 4 vol% SO₂ in CO₂ mixture indicates a possible reversal temperature in the 86-163 C range.
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Willett, Erik Amos. "CO2 Capture on Polymer-Silica Composites from Molecular Modeling to Pilot Scale." University of Akron / OhioLINK, 2018. http://rave.ohiolink.edu/etdc/view?acc_num=akron152147716339683.

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Book chapters on the topic "Reversible CO2 capture"

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Glaser, Rainer, Paula O. Castello-Blindt, and Jian Yin. "Biomimetic Approaches to Reversible CO2 Capture from Air. N-Methylcarbaminic Acid Formation in Rubisco-Inspired Models." In New and Future Developments in Catalysis, 501–34. Elsevier, 2013. http://dx.doi.org/10.1016/b978-0-444-53882-6.00018-8.

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Conference papers on the topic "Reversible CO2 capture"

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Liu, Li. "Reversible Capture of CO2 by Cucurbit[7]uril Absorbent." In 2nd 2016 International Conference on Sustainable Development (ICSD 2016). Paris, France: Atlantis Press, 2017. http://dx.doi.org/10.2991/icsd-16.2017.39.

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Escosa, Jesu´s M., Cristo´bal Cortes, and Luis M. Romeo. "Repowering of Fossil Fuel Power Plants and Reversible Carbonation/Calcination Cycle for CO2 Abatement." In ASME 2005 International Mechanical Engineering Congress and Exposition. ASMEDC, 2005. http://dx.doi.org/10.1115/imece2005-79883.

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Fossil fuel power plants account for about a third of global carbon dioxide emissions. Coal is the major power-generation fuel, being used twice as extensively as natural gas (IEA, 2003). Moreover, on a global scale, coal demand is expected to double over the period to 2030; IEA estimates that 4500 GWe of new installed power will be required. Coal is expected to provide 40% of this figure. It is thus obvious that coal power plants must be operative to provide such amount of energy in the short term, at the same time reducing their CO2 emissions in a feasible manner and increasing their efficiency and capacity. However, the main technologies currently considered to effect CO2 capture, both post-and pre-combustion, introduce a great economic penalty and largely reduce the capacity and efficiency. One of these technologies involves the separation of CO2 from high temperature flue gases using the reversible carbonation reaction of CaO and the calcination of CaCO3. The process is able to simultaneously capture sulfur dioxide. The major disadvantage of this well-known concept is the great amount of energy consumption in the calcinator and auxiliary equipment. This paper proposes a new, feasible approach to supply this energy which leads to an optimal integration of the process within a conventional coal power plant. Calcination is accomplished in a kiln fired by natural gas, whereas a gas turbine is used to supply all the auxiliary power. Flue gases from the kiln and the gas turbine can substitute a significant part of the heat duty of the steam cycle heaters, thus accomplishing feed water repowering of the steam turbine. This novel CO2-capture cycle is proposed to be integrated with aging coal-fired power plants. The paper shows that an optimal integration of both elements represents one of the best methods to simultaneously achieve: a) an increase of specific generating capacity in a very short period of time, b) a significant abatement of CO2 emissions, and c) an increase of plant efficiency in a cost-effective way.
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Mastropasqua, Luca, Francesca Baia, Luca Conti, and Stefano Campanari. "Electrochemical Energy Storage and Synthetic Natural Gas Production Based on Reversible Molten Carbonate Cells." In ASME 2018 12th International Conference on Energy Sustainability collocated with the ASME 2018 Power Conference and the ASME 2018 Nuclear Forum. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/es2018-7344.

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One of the biggest issues associated to Carbon Capture and Utilisation (CCU) applications involves the exploitation of the captured CO2 as a valuable consumable. An interesting application is the conversion of CO2 into renewable fuels via electrochemical reduction at high temperature. Still unexplored in the literature is the possibility of employing a Molten Carbonate Electrolysis Cell (MCEC) to directly converting CO2 and H2O into H2, CO and eventually CH4, if a methanation process is envisaged. The introduction of this concept into a reversible system — similarly to the process proposed with reversible solid-oxide cells — allows the creation of a cycle which oxidises natural gas to produce CO2 and then employs the same CO2 and excess renewable energy to produce renewable natural gas. The result is a system able to perform electrochemical storage of excess renewable energy (from wind or solar) and if/when required sell renewable natural gas to the grid. In this work, a simulation of a reversible Molten Carbonate Cell (rMCC) is proposed. The reference MCFC technology considered is that from FuelCell Energy (USA) whose smaller stack is rated at 375 kW (DC). A simplified 0D stack model is developed and calibrated against experimental data. The Balance of Plant (BoP) is in common between the two operation modes MCFC and MCEC. In the former case, natural gas is electrochemically oxidised in the fuel compartment which receives carbonate ions (CO32−) from the air compartment, fed with air enriched with CO2 produced during electrolysis mode. The CO2 in the anode off gas stream is then purified and stored. In electrolysis mode, the stored CO2 is mixed with process H2O and sent to the fuel compartment of the MCEC; here, electrolysis and internal methanation occur. An external chemical reactor finalises the production of methane for either natural gas grid injection or storage and reuse in fuel cell mode. A thermodynamic analysis of the system is performed the yearly round-trip efficiency is assessed considering an assumed availability operating time of 7000 h/y. Finally, the overall green-house gas emission is assessed.
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Vierling, Matthieu, Frederic Geiger, Jean-Francois Brilhac, Sophie Dorge, David Habermacher, Habiba Nouali, Jean-Louis Guichard, et al. "Novel Desulfurization Concept Using a Regenerable Adsorbent." In ASME Turbo Expo 2020: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2020. http://dx.doi.org/10.1115/gt2020-16222.

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Abstract Sulfur oxides, abbreviated to SOx, refer to both sulfur dioxide (SO2) and sulfur trioxide (SO3) that are gaseous pollutants emitted by the combustion of low-grade fuels, including heavy oils, sour gases and coal. Current Flue Gas Desulfurization (FGD) technologies mainly use limestone or CaO (quicklime) as sulfur scavenger. They consume water and produce significant stocks of calcium sulfate, a non-regenerable solid that has limited market outlets and is sometimes considered as waste. To tackle this problem, a multi-partner team has launched a two-phase program in order to develop a new, regenerative FGD concept. This partnership includes a GE Power team (Belfort, France), three research laboratories (IS2M-MPC, LGRE from University of Haute Alsace, Mulhouse and ICB-UTBM-LERMPS, Belfort), a ceramic material testing center (ICAR, Moncel les Luneville, France) and a consultancy organization skilled in materials (Zephir Alsace, Mulhouse). The main objective was to design a regenerable adsorbent that would not release any solid waste but would allow instead the recovery of sulfur in the form of H2SO4 (sulfuric acid) which is a valuable chemical commodity. A first subprogram, executed from September 2012 through March 2015 and called “DeSOx New Gen”, enabled the different partners to identify and test at lab scale a regenerable and durable adsorbent. This adsorbent, used initially in powder form, involved an organized mesoporous silica (SiO2), which was used as a support and was impregnated with copper oxide (CuO) likely to undergo reversible sulfation. Such binary system proved capable of achieving large numbers of successive adsorption/regeneration cycles (more than fifteen attained in the lab) without undergoing substantial activity loss. A second subprogram, initiated in September 2017 and called “AdSOx”, aimed to obtain and test a bead-shaped form of the previously developed adsorbent in view of industrial applications. This product in bead-shaped adsorbent was then evaluated in 2019 in a pilot combustion rig, the flue gases of which were representative of a real industrial combustion installation in terms of SOx, NOx, CO, CO2, H2O and PM (particulate matter). In these rig tests, the performances of the adsorbent for the capture of SOx, including its capability to be regenerated for multi-cyclic use, have been assessed in fluidized bed and most recently in fixed bed conditions. This paper outlines the most significant steps and outcomes of this collaborative two-phase development program. It also illustrates the interesting capabilities of mesoporous materials for the design of highly active sorption and catalytic systems.
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Reports on the topic "Reversible CO2 capture"

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Eckert, Charles, and Charles Liotta. Reversible Ionic Liquids as Double-Action Solvents for Efficient CO2 Capture. Office of Scientific and Technical Information (OSTI), September 2011. http://dx.doi.org/10.2172/1084025.

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Charles Eckert and Charles Liotta. Reversible Ionic Liquids as Double-Action Solvents for Efficient CO{sub 2} Capture. Office of Scientific and Technical Information (OSTI), September 2011. http://dx.doi.org/10.2172/1048880.

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