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Academic literature on the topic 'Carbon Capture Processes'

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Published: 10 December 2022
Last updated: 28 January 2023

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Journal articles on the topic "Carbon Capture Processes"

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Wall, Terry F. "Combustion processes for carbon capture." Proceedings of the Combustion Institute 31, no. 1 (January 2007): 31–47. http://dx.doi.org/10.1016/j.proci.2006.08.123.

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Agrawal, Aatish Dhiraj. "Carbon Capture and Storage." International Journal for Research in Applied Science and Engineering Technology 9, no. 9 (September 30, 2021): 1891–94. http://dx.doi.org/10.22214/ijraset.2021.38294.

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Abstract: Rapid industrialization and sudden growth of population around the globe from the 18th century onwards ultimately led to the uncontrolled growth of manufacturing and energy producing industries. To make processes economical industries side lined the environment which began showing its effects from the past 50 years. Ever since Global Warming (commonly attributed to the unhealthy quantities of greenhouse gasses) starting to take up the centre stage, environmentalist and chemical engineers around the globe felt the need to reinvent our industrial processes to balance economy with environmental health. Through the medium of this report we intend to highlight yet another essential need of the hour that not only has the potential to reverse the damage of high carbon release by industries but also maintain economics of plant operation. Although Carbon capture is already a subject that is in study by scientists and engineers around the globe we intend to contribute and understand its plausibility using technology and simulation as a tool to facilitate better understanding of Co2 extraction from flue gasses
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Benson, Sally M., and Franklin M. Orr. "Carbon Dioxide Capture and Storage." MRS Bulletin 33, no. 4 (April 2008): 303–5. http://dx.doi.org/10.1557/mrs2008.63.

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Reducing CO2 emissions from the use of fossil fuel is the primary purpose of carbon dioxide capture and storage (CCS). Two basic approaches to CCS are available.1,2 In one approach, CO2 is captured directly from the industrial source, concentrated into a nearly pure form, and then pumped deep underground for long-term storage (see Figure 1). As an alternative to storage in underground geological formations, it has also been suggested that CO2 could be stored in the ocean. This could be done either by dissolving it in the mid-depth ocean (1–3 km) or by forming pools of CO2 on the sea bottom where the ocean is deeper than 3 km and, consequently, CO2 is denser than seawater. The second approach to CCS captures CO2directly from the atmosphere by enhancing natural biological processes that sequester CO2 in plants, soils, and marine sediments. All of these options for CCS have been investigated over the past decade, their potential to mitigate CO2 emissions has been evaluated,1 and several summaries are available.1,3,4
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Han, Yang, and W. S. Winston Ho. "Moving beyond 90% Carbon Capture by Highly Selective Membrane Processes." Membranes 12, no. 4 (April 1, 2022): 399. http://dx.doi.org/10.3390/membranes12040399.

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A membrane-based system with a retentate recycle process in tandem with an enriching cascade was studied for >90% carbon capture from coal flue gas. A highly CO2-selective facilitated transport membrane (FTM) was utilized particularly to enhance the CO2 separation efficiency from the CO2-lean gases for a high capture degree. A techno-economic analysis showed that the retentate recycle process was advantageous for ≤90% capture owing to the reduced parasitic energy consumption and membrane area. At >90% capture, the enriching cascade outperformed the retentate recycle process since a higher feed-to-permeate pressure ratio could be applied. An overall 99% capture degree could be achieved by combining the two processes, which yielded a low capture cost of USD47.2/tonne, whereas that would be USD 42.0/tonne for 90% capture. This FTM-based approach for deep carbon capture and storage can direct air capture for the mitigation of carbon emissions in the energy sector.
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Jones, Christopher W, and Edward J Maginn. "Materials and Processes for Carbon Capture and Sequestration." ChemSusChem 3, no. 8 (August 17, 2010): 863–64. http://dx.doi.org/10.1002/cssc.201000235.

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Ritchie, Sean. "Atmospheric carbon capture." Boolean 2022 VI, no. 1 (December 6, 2022): 191–96. http://dx.doi.org/10.33178/boolean.2022.1.31.

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Human-generated carbon emissions are the leading cause of climate change. There is a global commitment to reduce carbon emissions, in an effort to limit climate change effects. Many climate change solutions involve the mitigation of carbon emissions, mitigation alone is not enough. Carbon Dioxide (CO2) can live in the atmosphere for over 100 years. If we were to switch to 100% renewable energies, we would still damage the planet with the stagnant CO2 from the 1920’s. To combat climate change, we need a solution that can remove this carbon. One such solution is carbon capture, one of our best weapons in tackling climate change. The replacement of fossil fuel energy will not happen in the next few years, maybe not even for decades. Therefore, carbon capture is a promising ‘bridge’ technology, while we reach a sustainable level of green energy production. Carbon capture technology development has largely focused on singular processes (typically absorption, adsorption and membranes) capturing carbon from industrial exhaust systems. Recently, studies have delved into the idea of combining two or more of these technologies into one more efficient system and employing them in the industrial exhaust systems but also capturing carbon from the atmosphere. This project aims to develop a hybrid membrane and adsorption unit to capture carbon directly from the atmosphere. The aim is to provide the technology necessary to remove carbon from the atmosphere more effectively and cheaper than earlier technologies.
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Maitland, G. C. "Carbon Capture and Storage: concluding remarks." Faraday Discussions 192 (2016): 581–99. http://dx.doi.org/10.1039/c6fd00182c.

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This paper aims to pull together the main points, messages and underlying themes to emerge from the Discussion. It sets these remarks in the context of where Carbon Capture and Storage (CCS) fits into the spectrum of carbon mitigation solutions required to meet the challenging greenhouse gas (GHG) emissions reduction targets set by the COP21 climate change conference. The Discussion focused almost entirely on carbon capture (21 out of 23 papers) and covered all the main technology contenders for this except biological processes. It included (chemical) scientists and engineers in equal measure and the Discussion was enriched by the broad content and perspectives this brought. The major underlying theme to emerge was the essential need for closer integration of materials and process design – the use of isolated materials performance criteria in the absence of holistic process modelling for design and optimisation can be misleading. Indeed, combining process and materials simulation for reverse materials molecular engineering to achieve the required process performance and cost constraints is now within reach and is beginning to make a significant impact on optimising CCS and CCU (CO2 utilisation) processes in particular, as it is on materials science and engineering generally. Examples from the Discussion papers are used to illustrate this potential. The take-home messages from a range of other underpinning research themes key to CCUS are also summarised: new capture materials, materials characterisation and screening, process innovation, membranes, industrial processes, net negative emissions processes, the effect of GHG impurities, data requirements, environment sustainability and resource management, and policy. Some key points to emerge concerning carbon transport, utilisation and storage are also included, together with some overarching conclusions on how to develop more energy- and cost-effective CCS processes through improved integration of approach across the science-engineering spectrum. The discussion was first-rate in the best traditions of Faraday Discussions and hopefully will foster and stimulate further cross-disciplinary interactions and holistic approaches.
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Andreoli, Enrico. "Materials and Processes for Carbon Dioxide Capture and Utilisation." C 3, no. 4 (May 19, 2017): 16. http://dx.doi.org/10.3390/c3020016.

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Nimmanterdwong, Prathana, Benjapon Chalermsinsuwan, and Pornpote Piumsomboon. "Emergy analysis of three alternative carbon dioxide capture processes." Energy 128 (June 2017): 101–8. http://dx.doi.org/10.1016/j.energy.2017.03.154.

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Della Moretta, Davide, and Jonathan Craig. "Carbon capture and storage (CCS)." EPJ Web of Conferences 268 (2022): 00005. http://dx.doi.org/10.1051/epjconf/202226800005.

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Carbon Capture and Storage (CCS) is an important tool for the decarbonization of the energy system to achieve the mid-century global climate change targets. CO2 is captured using different industrial processes that involve membrane filtering or enhanced combustion. The CO2 is then transported, preferably by pipeline, to a storage site where it is injected into a permeable reservoir. Sealing capacity of the storage site is of paramount importance for safe CO2 sequestration, to avoid any geological leakage. Each CCS project must have a dedicated MMV (Measurement, Monitoring and Verification) programme to ensure conformance with the expected evolution of the CO2 plume and its containment within the storage site. Eni is committed to the implementation of CCS, with several ongoing projects.
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Dissertations / Theses on the topic "Carbon Capture Processes"

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Ramkumar, Shwetha. "CALCIUM LOOPING PROCESSES FOR CARBON CAPTURE." The Ohio State University, 2010. http://rave.ohiolink.edu/etdc/view?acc_num=osu1274882053.

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Phalak, Nihar. "Calcium Looping Processes for Pre- and Post-Combustion Carbon Dioxide Capture Applications." The Ohio State University, 2013. http://rave.ohiolink.edu/etdc/view?acc_num=osu1366802833.

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Griffiths, Owen Glyn. "Environmental life cycle assessment of engineered nanomaterials in carbon capture and utilisation processes." Thesis, University of Bath, 2014. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.629663.

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CO2 is a waste product from a number of human activities such as fossil fuel power generation, industrial manufacturing processes, and transport. The rising concentration of CO2 in the atmosphere is heating the planet’s surface via the well-established greenhouse effect; a mechanism for many irreversible climate change impacts. Coupled to this is the ever-increasing global pressure over the availability and access to fossil fuel reserves; the foundations of modern society. In recognition of this CO2 is gaining renewed interest as a carbon feedstock, a changing of attitude viewing it as an asset rather than waste. Carbon capture and utilisation (CCU) technologies are attempting to make use of it. However, little quantitative assessment work has been done to assessand verify such potentials. This thesis applies the principles and framework of the life cycle assessment (LCA) - environmental management tool to early stage CO2 utilisation laboratory processes. All processes employ engineered nanomaterials (ENM) to perform this function, a material class leading the way in the challenges of efficient and feasible CO2 chemistry. The LCA contribution in this thesis acts as a measuring and a guiding tool for technology developers, in the first instance to document the cradle-to-gate impacts of a number of formed ENMs. Appreciating the net environmental benefits of ENM uptake within society has yet to be wholly established, and the unavailability of data is recognised as a major factor. The work of this thesis will thus contribute to knowledge gaps, and be informative to wider community seeking to quantify technical performance benefits of ENMs in the context of net life cycle impact burdens. Finally the actual CCU processes are assessed, initially within the confines of the laboratory but further expanded for consideration at more industrially relevant scales. The potential for sound CCU performance were found achievable under best case conditions, with net GHG impact reductions over the life cycle, and the potential for lower impact carbon products, even carbon negative. However other environmental impacts such as ozone depletion, toxic emissions and the consumption of precious metalores are impacts that require consideration in the use of such technologies.
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HARO, HERBERTH ARTURO VASQUEZ. "NUMERICAL INVESTIGATION OF AMINE BASED ABSORPTION PROCESSES FOR CARBON DIOXIDE CAPTURE IN CCS PROJECTS." PONTIFÍCIA UNIVERSIDADE CATÓLICA DO RIO DE JANEIRO, 2009. http://www.maxwell.vrac.puc-rio.br/Busca_etds.php?strSecao=resultado&nrSeq=15511@1.

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COORDENAÇÃO DE APERFEIÇOAMENTO DO PESSOAL DE ENSINO SUPERIOR
Absorção é um processo no qual os componentes de uma corrente gasosa são separados através do uso de um solvente líquido. O processo pode ser simplesmente físico ou seguido por uma reação química. Na indústria, um processo de absorção importante é a remoção de dióxido de carbono (CO2), usando uma solução aquosa de monoethanolamina (MEA), dos gases de combustão expelidos pelas plantas alimentadas por combustíveis fosseis tais como: as usinas de geração de energia, a indústria farmacêutica, a indústria de petróleo, etc. Os projetos desenvolvidos por grandes corporações usualmente são cercados de sigilo, e as companhias evitam a divulgação de suas soluções tecnológicas. Além disso, no Brasil pouco tem-se publicado a respeito. Neste trabalho, apresenta-se um modelo simples que simula a absorção de CO2 em solução aquosa de MEA. O modelo envolve as equações de conservação de massa, quantidade de movimento e energia, podendo predizer o comportamento geral do processo de absorção. Os resultados das simulações da absorção de CO2 em contracorrente com uma coluna de filme líquido foram comparados com dados experimentais disponíveis apresentando uma boa concordância.
Absorption is a process where the components of a gaseous stream are separated through the use of a liquid solvent. The process may be simply physical or be followed by a chemical reaction. In industry, one of the most important absorption processes is the removal of carbon dioxide (CO2), by using an aqueous solution of monoethanolamine (MEA), from flue gases exhausted by fossil-fuel-fired power plants, the pharmaceutical industry, the petroleum industry, etc. The projects developed by large companies usually are surrounded by secrecy and the companies avoid dissemination of their technological solutions. In addition, there is almost nothing published in Brazil about this subject. In this work, we present a simple model that simulates the absorption of CO2 by a MEA based aqueous solution. The model involves the equations for the conservation of mass, momentum, and energy, and may predict the general behavior of the absorption process. Results for the simulation of the absorption of CO2 in a countercurrent liquid film contactor were compared with available experimental data, presenting good agreement.
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Bocciardo, Davide. "Optimisation and integration of membrane processes in coal-fired power plants with carbon capture and storage." Thesis, University of Edinburgh, 2015. http://hdl.handle.net/1842/10560.

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This thesis investigates membrane gas separation and its application to post-combustion carbon capture from coal-fired power plants as alternative to the conventional amine absorption technology. The attention is initially focused on membrane module modelling, with the aim of obtaining more detailed predictions of the behaviour of the separation though spiral-wound and hollow-fibre modules. Both one- and bi-dimensional models are implemented, compared and tested for different separations. Module geometry is investigated as well as the effect on the performances due to possible fabrication defects. A key part of the work involves the integration of the customised models into UniSim® Design, the Honeywell process simulator. Thanks to the developed interface, multi-stage process designs are developed, compared with the available literature and linked to a rigorous economic analysis. In particular, a long-term indicator such as the Levelised Cost Of Electricity (LCOE) is evaluated and parametric analyses are conducted with respect to both material and process parameters.
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Di, Biase Emanuela. "Systematic development of predictive molecular models of high surface area activated carbons for the simulation of multi-component adsorption processes related to carbon capture." Thesis, University of Edinburgh, 2015. http://hdl.handle.net/1842/16155.

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Adsorption in porous materials is a promising technology for CO2 capture and storage. Particularly important applications are adsorption separation of streams associated with the fossil fuel power plants operation, as well as natural gas sweetening. High surface area activated carbons are a promising family of materials for these applications, especially in the high pressure regimes. As the streams under consideration are generally multi-component mixtures, development and optimization of adsorption processes for their separation would substantially benefit from predictive simulation models. In this project we combine experimental data and molecular simulations to systematically develop a model for a high surface area carbon material, taking activated carbon Maxsorb MSC-30 as a reference. Our study starts from the application of the well-established slit pore model, and then evolves through the development of a more realistic model, based on a random packing of small graphitic fragments. In the construction of the model, we introduce a number of constraints, such as the value of the accessible surface area, concentration of the surface groups and pore volume, to bring the properties of the model structure close to the reference porous material. Once a plausible model is developed, its properties are further tuned through comparison between simulated and experimental results for carbon dioxide and methane. The model is then validated by predictions for the same species at different conditions and by prediction of other species involved in the carbon capture processes. The model is applied to simulate the separations involved in pre and post combustion capture processes and sweetening of sour natural gas, using realistic conditions and compositions for the multicomponent mixtures. Finally, it is used to explore the effect of water in pre and post combustion separations.
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Garcia-Gutierrez, Pelayo. "Carbon Capture and Utilisation processes : a techno-economic assessment of synthetic fuel production from CO2." Thesis, University of Sheffield, 2016. http://etheses.whiterose.ac.uk/14369/.

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Carbon Capture and Utilisation (CCU) is seen globally as one of the available technologies that can contribute to avoiding the effects of global warming while securing energy supply by utilising CO2 as a carbon source for chemical and fuel production. This thesis has measured the technical and economic performance of seven Carbon Capture and Utilisation (CCU) process designs (Base Case Models) based on best available technology. This was the first attempt to compare different routes of similar Technology Readiness Level to manufacture a liquid fuel from CO2. In addition, this thesis also examines the techno-economic feasibility of selective CO2 capture processes from biogas streams using ionic liquids as physical absorbents to assess the potential improvements that this developing technology could have on process performance. The selected Base Case Models were modelled using the process simulation software Aspen Plus to determine mass and energy balances. In addition, an economic assessment was developed using Aspen Plus Economic Analyzer (APEA) and MS Excel to determine capital, operating and production costs. The results revealed that the synthetic route based on CO2 capture and steam methane reforming was the most promising CO2-to-fuels route since it was able to achieve the highest overall plant energy efficiency (17.9%) and the lowest fuel production costs (£95.46 per GJ [LHV]); however this process cannot currently compete commercially with conventional fossil fuels. Further research in the specific areas suggested in this work is encouraged in order to bring fuel production costs down. It was also demonstrated that the evaluated ionic liquids cannot compete with MEA in terms of bio-methane production costs; however, the simulation methodology developed in this study can be used as a basis for further work in the area since it allows consideration of ionic liquids made of any combination of cation and anion as well as different gas streams.
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Zaragoza, Martín Francisco Javier. "Development and fluid dynamic evaluation of novel circulating fluidised bed elements for low-temperature adsorption based carbon capture processes." Thesis, University of Edinburgh, 2017. http://hdl.handle.net/1842/25482.

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A methodology for the thermodynamic-kinetic evaluation of circulating systems as TSA carbon capture processes is developed and used in the assessment of a novel CFB configuration against a benchmark (co-current riser). The novel CFB features a counter-current adsorber, a counter-current regenerator and a riser, the latter element playing a double role of solids conveyer and co-current adsorber. The advantages sought by using a counter-current adsorber are not only the more efficient gas-solid contact mode with respect co-current, but also a low pressure drop derived from operation at lower gas velocities and hydrostatic head partially supported on the contactor internals. Knowledge of the adsorption equilibrium alone is sufficient to realise the much higher sorbent circulation rates required by co-current configurations –compared to counter-current– to meet the stringent carbon capture specifications of 90% recovery and 95% purity. Higher solids circulation rates imply higher energy requirements for regeneration, and therefore research and development of co-current gas-solid contactors cannot be justified in terms of searching for energy-efficient post-combustion carbon capture processes. Parallel experimental investigation in the operation and fluid dynamics of cold model CFB rigs is carried out with the purposes of: 1) providing information that may impact the process performance and can be fed into the mathematical model used in the theoretical assessment for more realistic evaluation, and 2) determine gas and solids residence time distributions (RTDs), which are used for the estimation of axial dispersion and comparison with published results in similar systems. Gas RTD data is generated using a tracer pulse injection-detection technique, whereas RTD for the solid phase is studied using positron emission particle tracking (PEPT). The PEPT technique proved to be adequate for the identification of flow regimes in the novel design of the counter-current adsorber, featuring inclined orifice trays. At low gas velocities the particles flow straight down through the tray holes, whereas at higher velocities the particles flow down in zig-zag, increasing the residence time of the particles and reducing the particle axial dispersion, both beneficial in terms of separation efficiency.
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Ramirez, Santos Álvaro Andrés. "Application of membrane gas separation processes to CO2 and H2 recovery from steelmaking gases for carbon capture and use." Thesis, Université de Lorraine, 2017. http://www.theses.fr/2017LORR0272.

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L’acier est produit aujourd’hui principalement en faisant appel à une technologie basée sur le procédé haut fourneau-convertisseur à l’oxygène, conduisant à trois types d’émissions principales: le gaz de haut fourneau (BFG), le gaz de cokerie (COG), et le gaz de convertisseur (BOFG). Dans le cadre du projet VALORCO, une analyse des possibilités de réduction des émissions carbonées, associée à une valorisation des émissions de la sidérurgie, a été réalisée. Une des voies étudiées est la production de composés d’intérêt industriel tel que méthanol, pouvant être produit par transformation chimique du CO et/ou CO2 contenus dans les émissions, associé à de l’hydrogène. L’objectif principal de ce travail de thèse consiste à évaluer les possibilités offertes par le procédé de perméation gazeuse, appliqué à la récupération sélective de ces composés dans les 3 types d’émissions. Dans un premier temps, un état de l’art des différents projets dédiés à la capture (CCS) et à la valorisation (CCU) des émissions dans l’industrie de l’acier est présenté, avec une attention particulière aux différentes technologies de séparation des gaz. Des mesures expérimentales de sélectivité et de perméance pour différentes conditions de température et de pression, réalisées sur banc dédié avec deux matériaux membranaires disponibles commercialement et sélectif à l’hydrogène (vitreux) et au CO2 (élastomère) ont permis une étude paramétrique systématique par simulation des performances de séparation du procédé appliqué au BFG, COG et BOFG. Une comparaison des procédés basés sur un seul ou plusieurs étages de perméation, y compris avec des boucles de recirculation, a ensuite été entreprise dans un environnement de type Process System Engineering (PSE, logiciel Aspen Plus). L’influence des paramètres opératoires (rapport de pression, température, taux de prélèvement) sur les performances de séparation a été réalisée, conduisant à une cartographie des compositions atteignables. La consommation énergétique et la surface membranaire nécessaires pour chaque configuration permettent au final une optimisation techno-économique du procédé, sur la base d’un modèle économique intégré aux conditions de simulation
Steel is produced today mainly in a blast furnace-oxygen converter process, leading to three main types of emissions: blast furnace gas (BFG), coke oven gas (COG), and converter gas (BOFG). In the framework of the VALORCO project, an analysis of the possibilities for reducing carbon emissions, combined with the valorization of emissions from the steel industry, was carried out. One of the routes studied is the production of compounds of industrial interest such as methanol, which can be produced by chemical transformation of the CO and / or CO2 contained in the emissions associated with hydrogen. The main objective of this thesis work is to evaluate the possibilities offered by the gas permeation process applied to the selective recovery of these compounds in the three types of emissions. Initially, a state of the art of the various projects dedicated to the capture (CCS) and the valorization (CCU) of the emissions in the steel industry is presented, with particular attention to the different gas separation technologies. Experimental measurements of selectivity and permeance for different temperature and pressure conditions, carried out on a dedicated bench with two commercially available membrane materials, one selective to hydrogen (glassy) and one to CO2 (rubbery), allowed a systematic parametric study by simulation of the separation performance of the process applied to the BFG, COG and BOFG. A comparison of the processes based on one or more permeation stages, including recirculation loops, was then undertaken in a Process System Engineering (PSE) environment (Aspen Plus software). The influence of the operating parameters (pressure ratio, temperature, stage cut) on the separation performance was evaluated, leading to a mapping of attainable compositions. The energy consumption and the membrane surface required for each configuration allow a techno-economic optimization of the process, on the basis of an economic model integrated to the simulation conditions
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Haider, Syed Kumail. "Oxygen carrier and reactor development for chemical looping processes and enhanced CO2 recovery." Thesis, Cranfield University, 2016. http://dspace.lib.cranfield.ac.uk/handle/1826/10014.

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This thesis’s main focus is a CO2 capture technology known as chemical looping combustion (CLC). The technology is a novel form of combustion and fuel processing that can be applied to gas, solid and liquid fuels. By using two interconnected fluidised-bed reactors, with a bed material capable of transferring oxygen from air to the fuel, a stream of almost pure CO2 can be produced. This stream is undiluted with nitrogen and is produced without any direct process efficiency loss from the overall combustion process. The heart of the process is the oxygen carrier bed material, which transfers oxygen from an air to fuel reactor for the conversion of the fuel. Oxygen carrier materials and their production should be of low relative cost for use in large-scale systems. The first part of this research centres on development and investigative studies conducted to assess the use of low-cost materials as oxygen carriers and as supports. Mixed-oxide oxygen carriers of modified manganese ore and iron ore were produced by impregnation. While copper (II) oxide supported on alumina cement and CaO have been produced by pelletisation. These oxygen carriers were investigated for their ability to convert gaseous fuels in a lab-scale fluidised bed, and characterised for their mechanical and chemical suitability in the CLC process. The modified ores and pelletised copper-based oxygen carriers’ mechanical properties were enhanced by their production methods and in the case of the modified iron ore, significant oxygen uncoupling was observed. The copper-based oxygen carriers particularly those containing alumina cement showed high conversion rates of gaseous fuels and improved mechanical stability. The second part of this research thesis focuses on the design philosophy, commissioning and operation of a dual-fast bed chemical looping pilot reactor. Based on the operational experience, recommendations for modifications to the CLC system are discussed. In support, a parallel hydrodynamic investigation has been conducted to validate control and operational strategies for the newlydesigned reactor system. It was determined that the two fast bed risers share similar density and pressure profiles. Stable global circulation rate is flexible and could be maintained despite being pneumatically controlled. Reactor-reactor leakage via the loop-seals is sensitive to loop seal bed-height, and inlet fluid velocity but can be maintained as such to ensure no leakage is encountered.
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Books on the topic "Carbon Capture Processes"

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Desideri, Umberto, Giampaolo Manfrida, and Enrico Sciubba, eds. ECOS 2012. Florence: Firenze University Press, 2012. http://dx.doi.org/10.36253/978-88-6655-322-9.

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The 8-volume set contains the Proceedings of the 25th ECOS 2012 International Conference, Perugia, Italy, June 26th to June 29th, 2012. ECOS is an acronym for Efficiency, Cost, Optimization and Simulation (of energy conversion systems and processes), summarizing the topics covered in ECOS: Thermodynamics, Heat and Mass Transfer, Exergy and Second Law Analysis, Process Integration and Heat Exchanger Networks, Fluid Dynamics and Power Plant Components, Fuel Cells, Simulation of Energy Conversion Systems, Renewable Energies, Thermo-Economic Analysis and Optimisation, Combustion, Chemical Reactors, Carbon Capture and Sequestration, Building/Urban/Complex Energy Systems, Water Desalination and Use of Water Resources, Energy Systems- Environmental and Sustainability Issues, System Operation/ Control/Diagnosis and Prognosis, Industrial Ecology.
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Sánchez, Jonathan Albo. Carbon Dioxide Capture: Processes, Technology and Environmental Implications. Nova Science Publishers, Incorporated, 2016.

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Li, Lan, Kevin Huang, Winnie Wong-Ng, and Lawrence P. Cook. Materials and Processes for CO2 Capture, Conversion, and Sequestration. Wiley & Sons, Incorporated, John, 2018.

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Li, Lan, Kevin Huang, Winnie Wong-Ng, and Lawrence P. Cook. Materials and Processes for CO2 Capture, Conversion, and Sequestration. Wiley & Sons, Incorporated, John, 2018.

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Materials and Processes for CO2 Capture, Conversion, and Sequestration. Wiley-American Ceramic Society, 2018.

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Li, Lan, Kevin Huang, Winnie Wong-Ng, and Lawrence P. Cook. Materials and Processes for CO2 Capture, Conversion, and Sequestration. Wiley & Sons, Limited, John, 2018.

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Nguyen, Van Huy, Sonil Nanda, and Dai-Viet N. Vo. Carbon Dioxide Capture and Conversion: Advanced Materials and Processes. Elsevier, 2022.

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Nguyen, Van Huy, Sonil Nanda, and Dai-Viet N. Vo. Carbon Dioxide Capture and Conversion: Advanced Materials and Processes. Elsevier, 2022.

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Steane, Andrew. The Tree. Oxford University Press, 2018. http://dx.doi.org/10.1093/oso/9780198824589.003.0009.

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The life of an ordinary tree is described, in terms of the main physical and chemical processes: carbon capture by photosynthesis; entropy and energy; moisture. The information expressed in the tree comes partly from the DNA and partly from the sunlight. The tree does not push upwards from the ground, but solidifies the air.
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Trieloff, Mario. Noble Gases. Oxford University Press, 2017. http://dx.doi.org/10.1093/acrefore/9780190647926.013.30.

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This is an advance summary of a forthcoming article in the Oxford Encyclopedia of Planetary Science. Please check back later for the full article.Although the second most abundant element in the cosmos is helium, noble gases are also called rare gases. The reason is that they are not abundant on terrestrial planets like our Earth, which is characterized by orders of magnitude depletion of—particularly light—noble gases when compared to the cosmic element abundance pattern. Indeed, such geochemical depletion and enrichment processes make noble gases so versatile concerning planetary formation and evolution: When our solar system formed, the first small grains started to adsorb small amounts of noble gases from the protosolar nebula, resulting in depletion of light He and Ne when compared to heavy noble gases Ar, Kr, and Xe: the so-called planetary type abundance pattern. Subsequent flash heating of the first small mm to cm-sized objects (chondrules and calcium, aluminum rich inclusions) resulted in further depletion, as well as heating—and occasionally differentiation—on small planetesimals, which were precursors of larger planets and which we still find in the asteroid belt today from where we get rocky fragments in form of meteorites. In most primitive meteorites, we even can find tiny rare grains that are older than our solar system and condensed billions of years ago in circumstellar atmospheres of, for example, red giant stars. These grains are characterized by nucleosynthetic anomalies and particularly identified by noble gases, for example, so-called s-process xenon.While planetesimals acquired a depleted noble gas component strongly fractionated in favor of heavy noble gases, the sun and also gas giants like Jupiter attracted a much larger amount of gas from the protosolar nebula by gravitational capture. This resulted in a cosmic or “solar type” abundance pattern, containing the full complement of light noble gases. Contrary to Jupiter or the sun, terrestrial planets accreted from planetesimals with only minor contributions from the protosolar nebula, which explains their high degree of depletion and basically “planetary” elemental abundance pattern. Indeed this depletion enables another tool to be applied in noble gas geo- and cosmochemistry: ingrowth of radiogenic nuclides. Due to heavy depletion of primordial nuclides like 36Ar and 130Xe, radiogenic ingrowth of 40Ar by 40K decay, 129Xe by 129I decay, or fission Xe from 238U or 244Pu decay are precisely measurable, and allow insight in the chronology of fractionation of lithophile parent nuclides and atmophile noble gas daughters, mainly caused by mantle degassing and formation of the atmosphere.Already the dominance of 40Ar in the terrestrial atmosphere allowed C. F v. Weizsäcker to conclude that most of the terrestrial atmosphere originated by degassing of the solid Earth, which is an ongoing process today at mid ocean ridges, where primordial helium leaves the lithosphere for the first time. Mantle degassing was much more massive in the past; in fact, most of the terrestrial atmosphere formed during the first 100 million years of Earth´s history, and was completed at about the same time when the terrestrial core formed and accretion was terminated by a giant impact that also formed our moon. However, before that time, somehow also tiny amounts of solar noble gases managed to find their way into the mantle, presumably by solar wind irradiation of small planetesimals or dust accreting to Earth. While the moon-forming impact likely dissipated the primordial atmosphere, today´s atmosphere originated by mantle degassing and a late veneer with asteroidal and possibly cometary contributions. As other atmophile elements behave similar to noble gases, they also trace the origin of major volatiles on Earth, for example, water, nitrogen, sulfur, and carbon.
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Book chapters on the topic "Carbon Capture Processes"

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Jin, Wenbiao, Guobin Shan, Tian C. Zhang, and Rao Y. Surampalli. "CO 2 Scrubbing Processes and Applications." In Carbon Capture and Storage, 239–80. Reston, VA: American Society of Civil Engineers, 2015. http://dx.doi.org/10.1061/9780784413678.ch09.

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Asgari, Mehrdad, and Wendy L. Queen. "Carbon Capture in Metal-Organic Frameworks." In Materials and Processes for CO2 Capture, Conversion, and Sequestration, 1–78. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119231059.ch1.

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Zhu, Xuancan, Yixiang Shi, Shuang Li, Ningsheng Cai, and Edward J. Anthony. "CHAPTER 5. System and Processes of Pre-combustion Carbon Dioxide Capture and Separation." In Pre-combustion Carbon Dioxide Capture Materials, 281–334. Cambridge: Royal Society of Chemistry, 2018. http://dx.doi.org/10.1039/9781788013390-00281.

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Shah, Yatish T. "Carbon Dioxide Conversion Using Solar Thermal and Photo Catalytic Processes." In CO2 Capture, Utilization, and Sequestration Strategies, 281–345. Boca Raton: CRC Press, 2021. http://dx.doi.org/10.1201/9781003229575-6.

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Coulier, Yohann, William Ravisy, J.-M. Andanson, Jean-Yves Coxam, and Karine Ballerat-Busserolles. "Experiments and Modeling for CO2 Capture Processes Understanding." In Cutting-Edge Technology for Carbon Capture, Utilization, and Storage, 235–54. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119363804.ch16.

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Cavaliere, Pasquale. "Carbon Capture and Storage: Most Efficient Technologies for Greenhouse Emissions Abatement." In Clean Ironmaking and Steelmaking Processes, 485–553. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-21209-4_9.

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Yin, Huayi, and Dihua Wang. "Electrochemical Valorization of Carbon Dioxide in Molten Salts." In Materials and Processes for CO2 Capture, Conversion, and Sequestration, 267–95. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119231059.ch6.

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Baciocchi, Renato, Giulia Costa, and Daniela Zingaretti. "Accelerated Carbonation Processes for Carbon Dioxide Capture, Storage and Utilisation." In Green Chemistry and Sustainable Technology, 263–99. Berlin, Heidelberg: Springer Berlin Heidelberg, 2014. http://dx.doi.org/10.1007/978-3-642-44988-8_11.

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Cockayne, Eric. "Contribution of Density Functional Theory to Microporous Materials for Carbon Capture." In Materials and Processes for CO2 Capture, Conversion, and Sequestration, 319–43. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119231059.ch8.

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Williamson, I., M. Lawson, E. B. Nelson, and L. Li. "Computational Modeling Study of MnO2 Octahedral Molecular Sieves for Carbon Dioxide-Capture Applications." In Materials and Processes for CO2 Capture, Conversion, and Sequestration, 344–55. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119231059.ch9.

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Conference papers on the topic "Carbon Capture Processes"

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Dunia, Ricardo, Thomas F. Edgar, Gary Rochelle, and Mark Nixon. "Monitoring of carbon dioxide capture processes." In 2013 American Control Conference (ACC). IEEE, 2013. http://dx.doi.org/10.1109/acc.2013.6580406.

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Shaw, George, and Roger James Kuhns. "COST-EFFECTIVE CARBON CAPTURE WITH NATURAL PROCESSES." In Northeastern Section - 57th Annual Meeting - 2022. Geological Society of America, 2022. http://dx.doi.org/10.1130/abs/2022ne-373331.

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Pavel, Ioan, Radu Radoi, Gabriela Matache, and Ana-Maria Popescu. "CARBON CAPTURE AND STORAGE IN BIOMASS COMBUSTION PROCESS." In GEOLINKS International Conference. SAIMA Consult Ltd, 2020. http://dx.doi.org/10.32008/geolinks2020/b2/v2/27.

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Biomass stores solar energy that man can convert into electricity, fuel or heat, resulting in cheap, clean energy with a negative carbon balance. The use of biomass from agricultural secondary production as a potential energy source can improve soil quality and reduce greenhouse gas emissions in a complementary, non-competing way. The paper presents a piece of combustion equipment performing the burning process by biomass gasification on the TLUD (Top-Lit UpDraft) principle, from which hot air and biochar are obtained. The main function of this type of gas generator set on the TLUD principle is to generate a syngas flame which can be used as a heat source. The biochar obtained as a by-product is a sterile, active carbon with a large adsorption surface which is used as a soil amendment in environments with limited capacity for carbon sequestration and in soils depleted of resources. Gasification on the TLUD principle occurs when the biomass layer is introduced into the reactor and rests on a grate through which the air flow for gasification passes from bottom to top. Priming of the gasification process is done by igniting the upper layer of biomass in the reactor. The oxidation front continuously descends consuming the biomass in the reactor. Due to the heat radiated by the oxidation front the biomass is heated, dried, and then it enters a fast pyrolysis process from which volatiles emerge and unconverted carbon remains there. When the combustion front reached the grate, all the volatiles in the biomass were gasified and some of the carbon fixed was reduced; about 10 - 20% of the initial mass in the form of sterile charcoal, called biochar, remains on the grill. Compared to wood direct combustion or gasification combustion processes, the TLUD gasification process is characterized by very low values of the superficial velocity of gas passing through the pyrolysis front. The slow process maintains superficial velocity of the generator gas produced at very low values, which ensures reduced carrying away of free ash of approximate size below PM2.5 and maxim values of 5 mg/MJbm when leaving the burner; such values are well below the target imposed in the EU in 2015 for biomass combustion processes, which is below 25 mg/MJ. The result of monitoring the gasification process can be used to automate and optimize the TLUD process in order to achieve green energy, for carbon sequestration in the obtained biochar and to reduce greenhouse gas emissions, thus contributing to achieving efficient protection of the environment and to ensuring sustainable energy development
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Du, Wenli, and Khalil Abdulghani Mutahar Alkebsi. "Model predictive control and optimization of vacuum pressure swing adsorption for carbon dioxide capture." In 2017 6th International Symposium on Advanced Control of Industrial Processes (AdCONIP). IEEE, 2017. http://dx.doi.org/10.1109/adconip.2017.7983816.

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Poothia, Tejaswa, Gaurav Pandey, Dipti Mehra, and Prerna B. S. Rawat. "Techno-Economic Assesment for Carbon Capture Techniques." In Offshore Technology Conference. OTC, 2022. http://dx.doi.org/10.4043/31947-ms.

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Abstract This paper focuses on a techno-economic analysis for carbon capture technologies with a study of processes that apprise different grades of products purity. The cost evaluation of carbon capture and storage techniques has been discussed. It describes about the cost metrics, carbon storage and transport, aspects of energy supply, maturity, retrofitting cost of these techniques. Therefore, the three leading carbon capture techniques namely: pre-combustion, oxyfuel-combustion and post combustion carbon techniques are enlightened to review the development of carbon capture techniques and their techno economical aspects which can be beneficial for sustainable development. Carbon products streams that are generated by Carbon Capture and Storage (CCS) techniques, are observed to contain the impurities at some level. The effect of these impurities for the efficient and safe storage and transportation of carbon is fundamentally major issue. Acceptability and economic viability in terms of health risks and surrounding environment are also very critical factors. The paper aims to review the various technoeconomical aspects for carbon capturing technologies in industries and different power plants in order to increase the feasibility/efficiency of CO2 storage and transport for promising future.
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Poothia, Tejaswa, Gaurav Pandey, Dipti Mehra, and Prerna B. S. Rawat. "Techno-Economic Assesment for Carbon Capture Techniques." In Offshore Technology Conference. OTC, 2022. http://dx.doi.org/10.4043/31947-ms.

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Abstract This paper focuses on a techno-economic analysis for carbon capture technologies with a study of processes that apprise different grades of products purity. The cost evaluation of carbon capture and storage techniques has been discussed. It describes about the cost metrics, carbon storage and transport, aspects of energy supply, maturity, retrofitting cost of these techniques. Therefore, the three leading carbon capture techniques namely: pre-combustion, oxyfuel-combustion and post combustion carbon techniques are enlightened to review the development of carbon capture techniques and their techno economical aspects which can be beneficial for sustainable development. Carbon products streams that are generated by Carbon Capture and Storage (CCS) techniques, are observed to contain the impurities at some level. The effect of these impurities for the efficient and safe storage and transportation of carbon is fundamentally major issue. Acceptability and economic viability in terms of health risks and surrounding environment are also very critical factors. The paper aims to review the various technoeconomical aspects for carbon capturing technologies in industries and different power plants in order to increase the feasibility/efficiency of CO2 storage and transport for promising future.
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Ganapathy, Harish, Sascha Steinmayer, Amir Shooshtari, Serguei Dessiatoun, Mohamed Alshehhi, and Michael M. Ohadi. "Enhanced Carbon Capture in a Multiport Microscale Absorber." In ASME 2013 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/imece2013-66345.

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Increasing concerns on the effects of global warming leading to climate change has necessitated the development of efficient technologies to separate acid gas components, such as carbon dioxide and hydrogen sulfide, from gaseous mixtures. Microscale technologies have the potential to substantially enhance gas-liquid absorption processes on account of their inherent high surface area to volume ratio. The present work reports the mass transfer characteristics during gas-liquid absorption in a multiport microscale absorber. The reactor was designed to comprise of 15 straight, parallel channels having a hydraulic diameter of 456 micrometer and square cross-sectional geometry. The absorption of CO2 mixed with N2 into aqueous diethanolamine was investigated. The performance of the absorber was characterized with respect to the absorption efficiency and mass transfer coefficient. Parametric studies investigating the effects of the gas and liquid phase superficial velocity were performed and discussed. Additionally, the effect of varying the liquid reactant concentration was investigated and discussed.
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Pei, Peng, and Manohar Kulkarni. "A Model for Analysis of Integrated Gasification Combined Cycle Power Plant With Carbon Dioxide Capture." In ASME 2008 Power Conference. ASMEDC, 2008. http://dx.doi.org/10.1115/power2008-60124.

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Integrated Gasification Combined Cycle (IGCC) is believed to be one of the most promising technologies to offer electricity and other de-carbon fuels with carbon capture requirement at a relatively low cost. With the process of carbon dioxide capture, it can also actually meet strict regulations for other pollutants emission. However, the performances can vary depending on what kinds of technologies or processes are used. This paper has developed a model and calculated by using Engineering Equation Solver (EES) program to determine and compare different available technologies and processes. There are four main components in the model: Gasification Island; Gas Cleanup Island; Carbon Dioxide Capture Island and Power Island. Among them, the different options of Gasification Island; and Carbon Dioxide Capture Island are expected to be the most effective factors to influence the performance of the plant. Therefore, different gasification processes are examined in this paper, including Shell, GE (Texaco) and Lurgi. The carbon dioxide capture processes are based on SELEXOL, a physical absorption process, because of the high partial pressure of carbon dioxide in the syngas. A process called “double-absorption” is used for capturing sulfur compounds and carbon dioxide. This paper calculated and compared the net outputs, efficiency penalties for CO2 capture part, and net plant efficiencies for different technologies and processes by using EES program. This model tries to treat the IGCC with carbon dioxide capture part as a whole thermal system, instead of just looking at the capture system alone. Different gasification technologies mentioned above will result in various paths and efficiencies of using steam and waste energy in the system. It will make reasonable use of various waste energies and steams for both mechanical and chemical processes to improve the performance of the plant, and incorporate a CO2 capture system into the design concept of the power plant.
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Font-Palma, Carolina, George Lychnos, Homam Nikpey Somehsaraei, Paul Willson, and Mohsen Assadi. "Comparison of Performance of Alternative Post Combustion Carbon Capture Processes for a Biogas Fueled Micro Gas Turbine." In ASME Turbo Expo 2020: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2020. http://dx.doi.org/10.1115/gt2020-15558.

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Abstract The urgent need to decrease greenhouse gases (GHG) has prompted countries such as the UK and Norway to commit to net zero emissions by 2050 and 2030, respectively. One of the sectors contributing to GHG emissions is agriculture, by approximately 10% in the EU in 2017. GHG reductions in the production side should involve avoidance at source, reduction of emissions and/or removal of those emissions, with the potential for negative emissions by carbon capture. This paper focuses on the utilisation of agricultural waste that can be converted into biogas, such as livestock and crops residues which represent around 37% of GHG emissions by agriculture in the EU. The biogas can be used to produce electricity and heat in a micro gas turbine (MGT). Then, the exhaust gases can be sent to a carbon capture plant. This offers the potential for integration of waste into energy for in-house use in farms and fosters a circular-bioeconomy, where the captured CO2 could be used in greenhouses to grow vegetables. This could even allow the integration of other renewable technologies, since the MGT offers flexible operation for rapid start-up and shut down or intermittency of other technologies such as solar or wind. Current carbon capture processes are very costly at the smaller scales typical of remote communities. The alternative A3C (advanced cryogenic carbon capture) process is much more economical at smaller scales. The A3C separates CO2 from process gas that flows counter-currently with a cold moving bed, where the CO2 desublimes on the surface of bed material as a thin layer of frost. This allows enhanced heat transfer and avoids heavy build-up of frost that reduces severely the heat transfer. The phase change separation process employed by A3C and the large thermal inertia of the separation medium gives good flexibility of capture for load changes and on-off despatch. This study integrates a combined heat and power MGT, Turbec T100, of 100 kWe output. This include developed models for the MGT using characteristics maps for the compressor and turbine and for the cryogenic carbon capture plant, using two software tools, IPSEpro and Aspen Plus, respectively.
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Tewari, Raj Deo, Chee Phuat Tan, and M. Faizal Sedaralit. "A Toolkit for Offshore Carbon Capture and Storage CCS." In International Petroleum Technology Conference. IPTC, 2022. http://dx.doi.org/10.2523/iptc-22307-ms.

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Abstract Carbon dioxide (CO2) capture, utilization, and storage is the best option for mitigating atmospheric emissions of CO2 and thereby controlling the greenhouse gas concentrations in the atmosphere. Despite the benefits, there have been a limited number of projects solely for CO2 sequestration being implemented. The industry is well-versed in gas injection in reservoir formation for pressure maintenance and improving oil recovery. However, there are striking differences between the injection of CO2 into depleted hydrocarbon reservoirs and the engineered storage of CO2. The differences and challenges are compounded when the storage site is karstified carbonate in offshore and bulk storage volume. It is paramount to know upfront that CO2 can be stored at a potential storage site and demonstrate that the site can meet required storage performance safety criteria. Comprehensive screening for site selection has been carried out for suitable CO2 storage sites in offshore Sarawak, Malaysia using geographical, geological, geophysical, geomechanical and reservoir engineering data and techniques for evaluating storage volume, container architecture, pressure, and temperature conditions. The site-specific input data are integrated into static and dynamic models for characterization and generating performance scenarios of the site. In addition, the geochemical interaction of CO2 with reservoir rock has been studied to understand possible changes that may occur during/after injection and their impact on injection processes/mechanisms. Novel 3-way coupled modelling of dynamic-geochemistry-geomechanics processes were carried out to study long-term dynamic behaviour and fate of CO2 in the formation. The 3-way coupled modelling helped to understand the likely state of injectant in future and the storage mechanism, i.e., structural, solubility, residual, and mineralized trapping. It also provided realistic storage capacity estimation, incorporating reservoir compaction and porosity/permeability changes. The study indicates deficient localized plastic shear strain in overburden flank fault whilst all the other flaws remained stable. The potential threat of leakage is minimal as target injection pressure is set at initial reservoir pressure, which is much lower than caprock breaching pressure during injection. Furthermore, it was found that the geochemical reaction impact is shallow and localized at the top of the reservoir, making the storage safe in the long term. The integrity of existing wells was evaluated for potential leakage and planned for a proper mitigation plan. Comprehensive measurement, monitoring, and verification (MMV) were also designed using state-of-art tools and dynamic simulation results. The understanding gaps are closed with additional technical work to improve technologies application and decrease the uncertainties. A comprehensive study for offshore CO2 storage projects identifying critical impacting elements is crucial for estimation, injection, containment, and monitoring CO2 plume. The information and workflow may be adopted to evaluate other CO2 projects in both carbonate and clastic reservoirs for long-term problem-free storage of greenhouse gas worldwide.
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Reports on the topic "Carbon Capture Processes"

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Baxter, Larry, Nathan Passey, Austin Walters, Kyler Stitt, Eric Mansfield, Stephanie Burt, Christopher Hoeger, and Aaron Sayre. Energy-Storing Cryogenic Carbon Capture™ for Utility- and Industrial-scale Processes Final Report. Office of Scientific and Technical Information (OSTI), April 2022. http://dx.doi.org/10.2172/1867496.

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Levy, Edward. Thermal Integration of CO{sub 2} Compression Processes with Coal-Fired Power Plants Equipped with Carbon Capture. Office of Scientific and Technical Information (OSTI), June 2012. http://dx.doi.org/10.2172/1064410.

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Alptekin, Gokhan, Ambalavanan Jayaraman, Michael Bonnema, and David Gribble. Integrated Water-Gas-Shift Pre-combustion Carbon Capture Process. Office of Scientific and Technical Information (OSTI), January 2022. http://dx.doi.org/10.2172/1838103.

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Singh, Surinder, Irina Spiry, Benjamin Wood, Dan Hancu, and Wei Chen. Pilot-Scale Silicone Process for Low-Cost Carbon Dioxide Capture. Office of Scientific and Technical Information (OSTI), July 2014. http://dx.doi.org/10.2172/1149479.

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William Tuminello, Maciej Radosz, and Youqing Shen. Novel Sorption/Desorption Process for Carbon Dioxide Capture (Feasibility Study). Office of Scientific and Technical Information (OSTI), November 2008. http://dx.doi.org/10.2172/993828.

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Meyer, Howard, S. James Zhou, Yong Ding, and Ben Bikson. Pre-Combustion Carbon Capture by a Nanoporous, Superhydrophobic Membrane Contactor Process. Office of Scientific and Technical Information (OSTI), March 2012. http://dx.doi.org/10.2172/1064408.

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Hornbostel, Marc. Pilot-Scale Evaluation of an Advanced Carbon Sorbent-Based Process for Post-Combustion Carbon Capture. Office of Scientific and Technical Information (OSTI), March 2018. http://dx.doi.org/10.2172/1337051.

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Li, Shiguang, Miao Yu, Yong Ding, Andrew Sexton, Darshan Sachde, Brad Piggott, Weiwei Xu, Shenxiang Zhang, Fanglei Zhou, and Howard Meyer. Energy Efficient GO-PEEK Hybrid Membrane Process for Post-combustion Carbon Dioxide Capture. Office of Scientific and Technical Information (OSTI), December 2020. http://dx.doi.org/10.2172/1750959.

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Singh, Surinder, Irina Spiry, Benjamin Wood, Dan Hance, Wei Chen, Mark Kehmna, and Dwayne McDuffie. Pilot-Scale Silicone Process for Low-Cost Carbon Dioxide Capture Preliminary Techno-Economic Analysis. Office of Scientific and Technical Information (OSTI), March 2014. http://dx.doi.org/10.2172/1134751.

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Hancu, Dan, Benjamin Wood, Sarah Genovese, Tiffany Westendorf, Robert Perry, Irina Spiry, Rachael Farnum, et al. Pilot-Scale Silicone Process for Low-Cost Carbon Dioxide Capture. Final Scientific/Technical Report. Office of Scientific and Technical Information (OSTI), August 2017. http://dx.doi.org/10.2172/1373652.

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