Relevant bibliographies by topics / Carbon dioxide capture and storage

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  2. Dissertations / Theses
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Academic literature on the topic 'Carbon dioxide capture and storage'

Author: Grafiati
Published: 4 June 2021
Last updated: 21 February 2023

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Journal articles on the topic "Carbon dioxide capture and storage"

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Benson, Sally M., and Franklin M. Orr. "Carbon Dioxide Capture and Storage." MRS Bulletin 33, no. 4 (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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Shcherbyna, Yevhen, Oleksandr Novoseltsev, and Tatiana Evtukhova. "Overview of carbon capture, utilisation and storage technologies to ensure low-carbon development of energy systems." System Research in Energy 2022, no. 2 (2022): 4–12. http://dx.doi.org/10.15407/srenergy2022.02.004.

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Carbon dioxide CO2 is a component of air that is responsible for the growing global warning and greenhouse gases emissions. The energy sector is one of the main sources of CO2 emissions in the world and especially in Ukraine. Carbon capture, utilization and storage (CCUS) is a group of technologies that play a significant role along with renewable energy sources, bioenergy and hydrogen to reduce CO2 emissions and to achieve international climate goals. Nowadays there are thirty-five commercial CCUS facilities under operation around the world with a CO2 capture capacity up to 45 million tons annually. Tougher climate targets and increased investment provide new incentives for CCUS technologies to be applied more widely. CCUS are applications in which CO2 is captured from anthropogenic sources (power generation and industrial processes) and stored in deep geological formations without entering atmosphere or used in various products using technologies without chemical modification or with conversion. The article discusses the use of various technologies of CO2 capture (post-combustion capture, pre-combustion capture and oxy-combustion capture), CO2 separation methods and their application in the global energy transition to reduce the carbon capacity of energy systems. Technical and economic indicators of CO2 capture at different efficiencies for coal and gas power plants are given. Technologies of transportation and storage of captured carbon dioxide and their economic indicators are considered. The directions for the alternative uses of captured CO2, among which the main ones are the production of synthetic fuels, various chemicals and building materials, are also presented and described in the paper. The possibility of utilization captured СО2 in the production of synthetic fuel in combination with Power-to-Gas technologies was studied. Keywords: greenhouse gases emissions, fossil fuels, СО2 capture technologies, capture efficiency, synthetic fuel
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Holloway, Sam. "Carbon dioxide capture and geological storage." Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences 365, no. 1853 (2007): 1095–107. http://dx.doi.org/10.1098/rsta.2006.1953.

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Carbon dioxide capture and geological storage is a technology that could be used to reduce carbon dioxide emissions to the atmosphere from large industrial installations such as fossil fuel-fired power stations by 80–90%. It involves the capture of carbon dioxide at a large industrial plant, its transport to a geological storage site and its long-term isolation in a geological storage reservoir. The technology has aroused considerable interest because it can help reduce emissions from fossil fuels which are likely to remain the dominant source of primary energy for decades to come. The main issues for the technology are cost and its implications for financing new or retrofitted plants, and the security of underground storage.
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MURAI, Shigeo, and Shingo KAZAMA. "CCS (Carbon Dioxide Capture and Storage)." Journal of the Society of Mechanical Engineers 114, no. 1109 (2011): 248–50. http://dx.doi.org/10.1299/jsmemag.114.1109_248.

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Zhou, Peilin, and Haibin Wang. "Carbon capture and storage—Solidification and storage of carbon dioxide captured on ships." Ocean Engineering 91 (November 2014): 172–80. http://dx.doi.org/10.1016/j.oceaneng.2014.09.006.

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Pierre, Alain C. "Enzymatic Carbon Dioxide Capture." ISRN Chemical Engineering 2012 (December 16, 2012): 1–22. http://dx.doi.org/10.5402/2012/753687.

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In the past decade, the capture of anthropic carbonic dioxide and its storage or transformation have emerged as major tasks to achieve, in order to control the increasing atmospheric temperature of our planet. One possibility rests on the use of carbonic anhydrase enzymes, which have been long known to accelerate the hydration of neutral aqueous CO2 molecules to ionic bicarbonate species. In this paper, the principle underlying the use of these enzymes is summarized. Their main characteristics, including their structure and catalysis kinetics, are presented. A special section is next devoted to the main types of CO2 capture reactors under development, to possibly use these enzymes industrially. Finally, the possible application of carbonic anhydrases to directly store the captured CO2 as inert solid carbonates deserves a review presented in a final section.
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Smid, Karsten. "Carbon Dioxide Capture and Storage – eine Fata MorganaCarbon Dioxide Capture and Storage – a Mirage." GAIA - Ecological Perspectives for Science and Society 18, no. 3 (2009): 205–7. http://dx.doi.org/10.14512/gaia.18.3.5.

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Edwards, Ryan W. J., and Michael A. Celia. "Infrastructure to enable deployment of carbon capture, utilization, and storage in the United States." Proceedings of the National Academy of Sciences 115, no. 38 (2018): E8815—E8824. http://dx.doi.org/10.1073/pnas.1806504115.

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In February 2018, the United States enacted significant financial incentives for carbon capture, utilization, and storage (CCUS) that will make capture from the lowest-capture-cost sources economically viable. The largest existing low-capture-cost opportunity is from ethanol fermentation at biorefineries in the Midwest. An impediment to deployment of carbon capture at ethanol biorefineries is that most are not close to enhanced oil recovery (EOR) fields or other suitable geological formations in which the carbon dioxide could be stored. Therefore, we analyze the viability of a pipeline network to transport carbon dioxide from Midwest ethanol biorefineries to the Permian Basin in Texas, which has the greatest current carbon dioxide demand for EOR and large potential for expansion. We estimate capture and transport costs and perform economic analysis for networks under three pipeline financing scenarios representing different combinations of commercial and government finance. Without government finance, we find that a network earning commercial rates of return would not be viable. With 50% government financing for pipelines, 19 million tons of carbon dioxide per year could be captured and transported profitably. Thirty million tons per year could be captured with full government pipeline financing, which would double global anthropogenic carbon capture and increase the United States’ carbon dioxide EOR industry by 50%. Such a development would face challenges, including coordination between governments and industries, pressing timelines, and policy uncertainties, but is not unprecedented. This represents an opportunity to considerably increase CCUS in the near-term and develop long-term transport infrastructure facilitating future growth.
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Anvita Abhijit Bhate and Elizabeth Biju Joseph. "Decarbonizing the future: Understanding carbon capture, utilization, and storage methods." World Journal of Advanced Engineering Technology and Sciences 8, no. 1 (2023): 247–50. http://dx.doi.org/10.30574/wjaets.2023.8.1.0020.

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Carbon capture refers to the removal of carbon dioxide from the atmosphere, or directly at the source of its emissions. The latter employs chemical engineering to design capture systems for industries. Aqueous amine scrubbing makes use of amine based solvents to capture carbon dioxide from flue gas streams. The carbon, once captured, is compressed and redirected for either reutilisation or storage. In enhanced oil recovery, the CO2 is injected into oil and gas reservoirs to increase their extraction. Carbon storage methods work to remove the carbon from the atmosphere, and aid mitigation against carbon emissions from industry, thereby reducing the contribution to global warming and ocean acidification. This paper aims to provide the readers with an understanding of the technologies involved in the above processes.
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Singleton, Scott. "President's Page: Leading the way to a carbon-neutral world." Leading Edge 40, no. 10 (2021): 712–13. http://dx.doi.org/10.1190/tle40100712.1.

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Carbon capture and storage (CCS) and carbon capture, utilization, and storage (CCUS) are expanding at lightning speed as the world increasingly embraces the need for a carbon-neutral future. As it is described on the U.S. Department of Energy (DOE) website, “CCUS is a process that captures carbon dioxide emissions from sources like coal-fired power plants and either reuses or stores it so it will not enter the atmosphere. Carbon dioxide storage in geologic formations includes oil and gas reservoirs, unmineable coal seams and deep saline reservoirs — structures that have stored crude oil, natural gas, brine and carbon dioxide over millions of years” ( https://www.energy.gov/carbon-capture-utilization-storage ). The International Energy Agency (IEA) states that “CCUS is the only group of technologies that contributes both to reducing emissions in key sectors directly and to removing CO2 to balance emissions that are challenging to avoid – a critical part of “net-zero” goals. After years of slow progress, new investment incentives and strengthened climate goals are building new momentum behind CCUS” ( https://www.iea.org/reports/ccus-in-clean-energy-transitions ).
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Dissertations / Theses on the topic "Carbon dioxide capture and storage"

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Cowton, Laurence Robert. "Monitoring sub-surface storage of carbon dioxide." Thesis, University of Cambridge, 2017. https://www.repository.cam.ac.uk/handle/1810/270308.

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Since 1996, super-critical CO$_2$ has been injected at a rate of $\sim$0.85~Mt~yr$^{-1}$ into a pristine, saline aquifer at the Sleipner carbon capture and storage project. A suite of time-lapse, three-dimensional seismic reflection surveys have been acquired over the injection site. This suite includes a pre-injection survey acquired in 1994 and seven post-injection surveys acquired between 1999 and 2010. Nine consistently bright reflections within the reservoir, mapped on all post-injection surveys, are interpreted to be thin layers of CO$_2$ trapped beneath mudstone horizons. The areal extents of these CO$_2$ layers are observed to either increase or remain constant with time. However, volume flux of CO$_2$ into these layers has proven difficult to measure accurately. In addition, the complex planform of the shallowest layer, Layer 9, has proven challenging to explain using reservoir simulations. In this dissertation, the spatial distribution of CO$_2$ in Layer~9 is measured in three dimensions using a combination of seismic reflection amplitudes and changes in two-way travel time between time-lapse seismic reflection surveys. The CO$_2$ volume in this layer is shown to be growing at an increasing rate through time. To investigate CO$_2$ flow within Layer~9, a numerical gravity current model that accounts for topographic gradients is developed. This vertically-integrated model is computationally efficient, allowing it to be inverted to find reservoir properties that minimise differences between measured and modelled CO$_2$ distributions. The best-fitting reservoir permeability agrees with measured values from nearby wells. Rapid northward migration of CO$_2$ in Layer~9 is explained by a high permeability channel, inferred from spectral decomposition of the seismic reflection surveys. This numerical model is found to be capable of forecasting CO$_2$ flow by comparing models calibrated on early seismic reflection surveys to observed CO$_2$ distributions from later surveys. Numerical and analytical models are then used to assess the effect of the proximity of an impermeable base on the flow of a buoyant fluid, motivated by the variable thickness of the uppermost reservoir. Spatial gradients in the confinement of the reservoir are found to direct the flow of CO$_2$ when the current is of comparable thickness to the reservoir. Finally, CO$_2$ volume in the second shallowest layer, Layer~8, is measured using structural analysis and numerical modelling. CO$_2$ in Layer~8 is estimated to have reached the spill point of its structural trap by 2010. CO$_2$ flux into the upper two layers is now $\sim$40\% of total CO$_2$ flux injected at the base of the reservoir, and is increasing with time. This estimate is supported by observations of decreasing areal growth rate of the lower layers. The uppermost layers are therefore expected to contribute significantly to the total reservoir storage capacity in the future. CO$_2$ flow within Layer~9 beyond 2010 is forecast to be predominantly directed towards a topographic dome located $\sim$3~km north of the injection point. This dissertation shows that advances in determining the spatial distribution and flow of CO$_2$ in the sub-surface can be made by a combination of careful seismic interpretation and numerical flow modelling.
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Lamb, Katie Joanna. "Investigating alternative green methods for carbon dioxide utilisation and carbon capture and storage." Thesis, University of York, 2017. http://etheses.whiterose.ac.uk/18394/.

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Reducing carbon dioxide emissions is vital to reducing the effects of global warming. Numerous industrial methods exist, but developing alternative, greener and more energy-efficient methods is essential. Two pieces of work were investigated in this thesis towards developing alternative methods and are presented as two individual chapters, each with their own introduction, results, discussion, conclusion and future work sections. A general introduction to carbon dioxide and the vitality of decreasing carbon dioxide emissions acts as a preface to these chapters and is presented in Chapter 1. Chapter 2 examines promoting Carbon Dioxide Utilisation with new chromium(III) salophen complexes and Chapter 3 investigates a novel electrochemical carbon capture and mineralisation methodology. A range of chromium(III) salophen complexes were synthesised and were found to catalyse the synthesis of cyclic carbonates from carbon dioxide and terminal or internal epoxides at ambient conditions. The most active catalyst contained methoxy and tert-butyl groups on the salicylaldehyde and a bromide counterion, and is one of the most active catalysts in this field. Some of these catalysts were also used to catalyse the synthesis of the oxazolidinone diphenyloxazolidin-2-one from styrene oxide and phenyl isocyanate with successful results. A new electrochemical method was developed to perform carbon dioxide mineralisation, forming an amorphous aluminium hydroxycarbonate, at ambient conditions. The most energy efficient methods captured carbon with an energy requirement of 231-250 kJ mol-1 of carbon dioxide. This methodology worked with sustainable energy and materials, such as solar energy, seawater and “waste” aluminium. The carbon capture and energy efficiency of this methodology however could be improved to promote future developments and industrialisation, but nonetheless provides an interesting and alternative method to capture and mineralise carbon dioxide.
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Wang, Xiaolong. "Carbon dioxide capture and storage by mineralisation using recyclable ammonium salts." Thesis, University of Nottingham, 2011. http://eprints.nottingham.ac.uk/12982/.

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Carbon dioxide capture and storage by mineralisation (CCSM) is considered to be an alternative solution for reducing anthropogenic C0₂in some regions, where geological storage is not possible or considered uneconomically viable. However, low efficiency of mineral dissolution and use of unrecyclable additives are two key barriers for the development of CCSM. A novel CCSM process with recyclable ammonium salts is proposed to overcome these barriers in this study. This process integrates mineral carbonation with C0₂capture by employing NH₃, NH₄HSO₄and C0₂containing ammonium salts in the capture step, mineral dissolution and carbonation steps, respectively. The NH₄HSO₄ and NH₃can then be regenerated by thermal decomposition of (NH₄)₂SO₄, which is the by-product from the process. The use of C0₂ containing ammonium salts as the source of C0₂can avoid desorption and compression of C0₂, which account for 70 % of the total energy consumption in the whole CCS chain. In this work, a CCSM process route at low solid to liquid ratio (50 g/I) was experimentally investigated to validate the process concept. It was found that the dissolution efficiency of magnesium (Mg) can achieve 100 % by using NH₄HSO₄and the carbonation efficiency can reach 96.5 % by using CO₂containing ammonium salts from the capture step and addition of aqueous NH₃. Three products, including Si rich residue, Fe rich residue and pure hydromagnesite were obtained from the process. The TGA studies reported that the regeneration efficiency of NH₄HSO₄ and NH₃ in this process was 95 %. Both dissolution and carbonation efficiencies achieved in this work are higher than the values reported in previous work. In order to reduce the water usage, a CCSM process at high solid to liquid ratio (200-300 g/I) was developed. It was found that the dissolution efficiency of Mg was 64 and 72 % at 200 and 300 g/l, respectively. The increase of dissolution efficiency with a solid to liquid ratio could be explained by the removal of passive product layer caused by particle-particle interaction. At a solid to liquid ratio of 300 g/l, the highest carbonation efficiency achieved was 65.4 %. Magnesite instead of hydromagnesite was found after carbonation due to the CO₂ pressure caused by the decomposition of ammonium salts above 70 °C. Additionally, the carbonation efficiency was doubled by using (NH₄)₂CO₃compared to that using NH₄HCO₃. A preliminary evaluation was conducted to estimate the OPEX, including energy consumption, chemical costs and feedstock cost, based on the experimental results from the two process routes developed. In order to get low OPEX, the optimization process conditions, such as solid to liquid ratio and reaction time, were determined. Then, experiments at these optimized conditions were conducted. The dissolution efficiency of Mg from serpentine with particle size 75-150 pm using 2.8 M NH₄HSO₄at 100 g/l solid to liquid ratio for 1h was around 80 %. The carbonation efficiency was 96 % when the molar ratio of Mg: CO₂ containing NH⁴+ salts: NH₃was 1: 1.5: 2. Thus, the mass balance of the process showed that 3.0 t' of serpentine, 0.2 t of NH₄HSO₄and 0.1 t of NH₃ were required to sequester 1t of CO₂and produce 1.9 t of magnesite. Moreover, 1.7 t of high Si content (46.9 wt. %) and 0.3 t of high Fe content (60 wt. %) were produced. Finally, a cost evaluation study including CAPEX and OPEX was made using Aspen plus software to simulate the optimized CCSM process with recyclable ammonium salts for a 100 MW coal-fired power plant. For the input of 60 t/h CO₂, 93 % of them can be sequestered by the process with 29.5 % energy consumption and the total carbon capture and storage costs was 71.8 US$/t CO₂sequestered, excluding the product sale.
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Singh, Nisheeth 1973. "A systems perspective for assessing carbon dioxide capture and storage opportunities." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/34803.

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Thesis (S.M.)--Massachusetts Institute of Technology, System Design & Management Program, 2004.
Includes bibliographical references (p. 86-89).
Even as the acceptance of the fossil fuel greenhouse effect theory continues to grow amongst academics, statesmen and plebeians alike, the early adopters have already engaged in pre-emptive research activities aimed at mitigating the effects of such greenhouse gases. The focus of one such effort is on the capture and storage of CO₂ (carbon dioxide) from anthropogenic fixed source emissions. This effort can be broken down into a few broad categories such as terrestrial, ocean and geologic sequestration. Geologic sequestration refers to all activities geared towards the capture and storage of CO₂ under the surface of the earth in diverse 'reservoirs' such as deep saline formations, depleted oil and gas wells and unmineable coal seams to name a few. This investigation develops a systems perspective for assessing carbon dioxide capture and storage (CCS) opportunities within the realm of geologic sequestration. While multiple concurrent research activities continue to explore CCS opportunities from various perspectives, efforts at a systems analysis of the overall picture are just beginning. A systems view describing methodologies to integrate a variety of CCS data to assess potential sequestration opportunities is at the heart of this study. It is based on research being conducted at the Massachusetts Institute of Technology (MIT) under sponsorship of the United States Department of Energy (DOE). Using a Geographic Information System (GIS) and publicly available data, a detailed characterization of CO₂ sources and reservoirs are being developed. A source-reservoir matching process will be implemented which begins with quantifying the 'capturability' of a CO₂ source, a function of the purity, volume and several site specific considerations. Next, the potential
(cont.) proximate reservoirs are identified and then ranked based on transport options, type, capacity, cost, regulatory considerations and political sensitivity. All the above criteria will be spatially represented in the GIS and can be overlaid to produce a composite picture identifying the potential areas which would represent the maximum probability of success in sequestration efforts. A rigorous systems engineering approach will be adopted throughout the investigation. Novel tools such as the Object-Process CASE (OPCAT) tool will be used to model the complex and interdisciplinary system. A comprehensive systems modeling and engineering tool, it allows the representation of function, structure and behavior in a single model. Ultimately, the methodologies developed will be integrated and utilized in a case study to illustrate the methodology of evaluating CCS options for a given set of sources. A region in Mississippi has been identified for this model case-study. The methodology will be applied at a later time to evaluate CCS potential in the South East Regional Carbon Sequestration Partnership (SERCSP) and the West Coast Regional Carbon Sequestration Partnership (WCRCSP).
by Nisheeth Singh.
S.M.
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Mutch, Greg Alexander. "Carbon capture and storage optimisation in solid oxides : understanding surface-fluid interactions." Thesis, University of Aberdeen, 2016. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?pid=231044.

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To decrease carbon dioxide emissions into the atmosphere for climate change mitigation it is necessary to modify existing practices in processes where greenhouse gases are emitted. Due to the extremely large volumes of carbon dioxide produced globally, it is generally accepted that although carbon dioxide conversion and utilisation will contribute in the long term, in the short to medium term it will be necessary to capture and store carbon dioxide emissions to progress towards a low carbon future. Current industrial capture processes incur large energy and thus economic penalties. Storage in geological formations requires robust confidence in storage security to be publically accepted. Therefore the objective of this work was to study carbon dioxide capture and storage in processes directly confronting these two major challenges. Carbon dioxide adsorption on oxide materials for advanced carbon capture processes with lower energetic and economic penalties was investigated. Water was shown to play a crucial role in determining the presence of reactive sites, the speciation of carbonates formed and increased sorbent utilisation. A high surface area oxide with specifically exposed facets was prepared and the impact of these facets on carbon dioxide uptake performance was assessed. Volumetric gas adsorption and isotherm modelling supported the presence of two distinct adsorption sites. To enhance confidence in storage security it is necessary to understand storage processes that result in stable products. An apparatus capable of obtaining geological storage conditions was developed and carbonate formation and surface hydration at high pressure was investigated. By locating individual reactive cations on the surface of silica, silicate mineral analogues were prepared. It was shown that carbonate speciation was dependent on the reactive cation and the presence or absence of water.
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Kumar, Sushant. "Clean Hydrogen Production and Carbon dioxide Capture Methods." FIU Digital Commons, 2013. http://digitalcommons.fiu.edu/etd/1039.

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Fossil fuels constitute a significant fraction of the world’s energy demand. The burning of fossil fuels emits huge amounts of carbon dioxide into the atmosphere. Therefore, the limited availability of fossil fuel resources and the environmental impact of their use require a change to alternative energy sources or carriers (such as hydrogen) in the foreseeable future. The development of methods to mitigate carbon dioxide emission into the atmosphere is equally important. Hence, extensive research has been carried out on the development of cost-effective technologies for carbon dioxide capture and techniques to establish hydrogen economy. Hydrogen is a clean energy fuel with a very high specific energy content of about 120MJ/kg and an energy density of 10Wh/kg. However, its potential is limited by the lack of environment-friendly production methods and a suitable storage medium. Conventional hydrogen production methods such as Steam-methane-reformation and Coal-gasification were modified by the inclusion of NaOH. The modified methods are thermodynamically more favorable and can be regarded as near-zero emission production routes. Further, suitable catalysts were employed to accelerate the proposed NaOH-assisted reactions and a relation between reaction yield and catalyst size has been established. A 1:1:1 molar mixture of LiAlH4, NaNH2 and MgH2 were investigated as a potential hydrogen storage medium. The hydrogen desorption mechanism was explored using in-situ XRD and Raman Spectroscopy. Mesoporous metal oxides were assessed for CO2 capture at both power and non-power sectors. A 96.96% of mesoporous MgO (325 mesh size, surface area = 95.08 ± 1.5 m2/g) was converted to MgCO3 at 350°C and 10 bars CO2. But the absorption capacity of 1h ball milled zinc oxide was low, 0.198 gCO2 /gZnO at 75°C and 10 bars CO2. Interestingly, 57% mass conversion of Fe and Fe3O4 mixture to FeCO3 was observed at 200°C and 10 bars CO2. MgO, ZnO and Fe3O4 could be completely regenerated at 550°C, 250°C and 350°C respectively. Furthermore, the possible retrofit of MgO and a mixture of Fe and Fe3O4 to a 300 MWe coal-fired power plant and iron making industry were also evaluated.
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Hussain, Bilaal Yusef. "Dynamic simulations of carbon dioxide pipeline transportation for the purpose of carbon capture and storage." Thesis, University of Birmingham, 2018. http://etheses.bham.ac.uk//id/eprint/8575/.

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This Engineering Doctorate project aimed to study the effects of varying flowrates on the flow dynamics of carbon dioxide within a pipeline. The researched utilised the software gCCS to simulate three different transport system. The first system looked at the effects of transporting pure carbon dioxide in both the supercritical phase and the sub-cooled liquid phase. The outputs from the model showed that when the inlet flowrate is decreased, the outlet flowrate responds in three distinct phases. The second system compared the effects of three different impurities; hydrogen, nitrogen and oxygen, on the flow response when the inlet flowrate is decreased. It was found that all three impurities caused an increase in the offset between the inlet and outlet flowrate. The third system looked at how multiple sources of carbon dioxide effect the flowrate within the main trunk pipeline. It was found that multiple sources of carbon dioxide do not affect the flow of CO2 within the pipeline beyond that of the base case. The final part of the research compared data from the Shell QUEST pipeline to the model. This showed the model was able to predict the flowrate and pressure of the carbon dioxide with good accuracy.
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Bojö, Erik, and Vincent Edberg. "Koldioxidlagring i Sverige : En studie om CCS, Bio-CCS, DACCS och biokol ur ett 2045-perspektiv." Thesis, KTH, Hållbar utveckling, miljövetenskap och teknik, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-297570.

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Sverige har som ambition att uppnå nettonollutsläpp av fossilt CO2 till år 2045. För att lyckas med detta ska landet minska sina utsläpp med 85%, samtidigt som så kallade kompletterande åtgärder kommer vidtas för att kompensera för resterande 15%. Denna studie utreder Sveriges arbete med negativa utsläpp som kompletterande åtgärd med fokus på teknikerna bio-energy for carbon capture and storage (Bio-CCS på svenska), Direct air capture for carbon capture and storage (DACCS) och biokol. Även carbon capture and storage (CCS), som kan bidra till att göra anläggningar CO2-neutrala, har studerats. Under arbetets gång har en litteraturstudie samt intervjuer med forskare, politiker, bransch- och företagsrepresentanter samt myndigheter genomförts.  För CCS och Bio-CCS, som innefattar avskiljning av CO2 från punktutsläpp, finns fyra olika avskiljningsstrategier som kallas post-, pre-, och oxyfuel combustion samt chemical looping. I fallet med DACCS tillämpas antingen absorption eller adsorption för att avskilja koldioxiden från atmosfären. Biokol produceras genom förbränning av biomassa i en pyrolysanläggning och kan sedan användas som jordförbättringsmedel och kolsänka. Det finns idag en inhemsk biokolsproduktion på kommersiell skala vilket gör att biokol skiljer sig från de övriga tre teknikerna som inte kommit lika långt i sin utveckling. Däremot finns det ett flertal pilotprojekt inom CCS och Bio-CCS i Sverige.  Sveriges väletablerade bioekonomi gör att det finns goda förutsättningar för biokol och Bio- CCS att bidra till negativa utsläpp ur ett 2045-perspektiv. DACCS anses däremot inte aktuellt som kompletterande åtgärd till år 2045. Efter intervjuer framgår att det råder en god samstämmighet mellan olika aktörer kring vilka faktorer som behöver behandlas för att implementera teknikerna. Gemensamt för alla tekniker är att det krävs ekonomiska incitament för att möjliggöra storskalig implementering. För CCS-teknikerna krävs även regulatoriska förändringar för att underlätta transporten av CO2.
Sweden's ambition is to achieve net zero emissions of fossil CO2 by the year 2045. To reach this target, Sweden aims to reduce its emissions by 85%, while so-called supplementary measures will be taken to compensate for the remaining 15%. This study investigates Sweden's work with negative emissions as a complementary measure with a focus on the technologies bio-energy for carbon capture and storage (Bio-CCS in Swedish), Direct air capture for carbon capture and storage (DACCS) and biochar. Carbon capture and storage (CCS), which can help make industrial plants CO2-neutral, has also been studied. During the project, a literature study and interviews with researchers, politicians, industry and company representatives as well as authorities were carried out, which formed the basis of the report.  For CCS and Bio-CCS, which include separation of CO2 from point source emissions, there are four different separation strategies called post-, pre-, and oxyfuel combustion as well as chemical looping. Among these, post combustion is highlighted as the most developed. In the case of DACCS, either absorption or adsorption is applied to separate CO2 from the atmosphere. CCS, Bio-CCS and DACCS all have in common that the captured CO2 must be stored in deep geological formations once it has been separated. Biochar is produced by heating biomass in a pyrolysis plant and can be used as a soil improver and carbon sink. Today Sweden has a domestic biochar production on a commercial scale, which means that biochar differs from the other three technologies that have yet to reach that stage of development. However, there are several pilot projects within Bio-CCS and CCS in Sweden.  Sweden's well-established bioeconomy means that the conditions are good for biochar and Bio-CCS to contribute to negative emissions in relation to the 2045 target. DACCS, on the other hand, is not considered relevant as a supplementary measure to the year 2045 due to its technical immaturity and high cost. From interviews with researchers, authorities, companies, industry organizations and politicians, it is clear that there is a consensus between the different actors on which factors need to be addressed in order to enable large-scale implementation of the technologies. Common to all technologies is that financial incentives are required to enable large-scale implementation. The CCS technologies also require regulatory changes to facilitate the transport of CO2.
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Nie, Zhenggang. "Life Cycle Modelling of Carbon Dioxide Capture and Geological Storage in Energy Production." Thesis, Imperial College London, 2009. http://hdl.handle.net/10044/1/9016.

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Carbon dioxide (CO2) capture and geological storage (CCS) is recognised as one of themain options in the portfolio of greenhouse gas (GHG) mitigation technologies beingdeveloped worldwide. The CO2 capture and storage technologies require significantamounts of energy during their implementation and also change the environmentalprofile of power generation. The holistic perspective offered by Life Cycle Assessment(LCA) enables decision makers to quantify the trade-offs inherent in any change to thepower production systems and helps to ensure that a reduction in GHG emissions doesnot result in significant increases in other environmental impacts. Early LCA studies ofpower generation with CCS report a wide range of results, as they focus on specific CO2capture cases only. Furthermore, previous work and commercial LCA software have arigid approach to system boundaries and do not recognise the importance of the level ofdetail that should be included in the Life Cycle Inventory (LCI) data. This research developed a complete LCA framework for the ?cradle-to-grave?assessment of alternative CCS technologies in carbon-containing fuel power generation. A comprehensive and quantitative Life Cycle Inventory (LCI) database, which modelsinputs/outputs of processes at high level of detail, accounts for technical and geographicdifferences, generates LCI data in a consistent and transparent manner was developedand arranged and flexible structure. The developed LCI models were successfully applied to power plants with alternativepost-combustion chemical absorption capture and oxy-fuel combustion capture. Theresults demonstrate that most environmental impacts come from power generation withCCS and the upstream process of coal production at a life-cycle perspective. LCAresults are sensitive to the type of coal used and the CO2 capture options chosen. Moreover, the models developed successfully trace the fate of elements (including tracemetals) of concern throughout the power generation, CO2 capture, transport andinjection chain. Monte Carlo simulation method combined with the LCI models wasapplied to quantify the uncertainty of emissions of concern. A novel analytical framework for the LCA of CO2 storage was also developed andapplied to a saline aquifer storage field case. The potential CO2 leakage rates werequantified and the operational and geological parameters that determine the ratio of CO2leakage total volume of CO2 injected were identified.
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Cherezov, Ilia. "Modelling convective dissolution and reaction of carbon dioxide in saline aquifers." Thesis, University of Cambridge, 2017. https://www.repository.cam.ac.uk/handle/1810/268170.

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In an effort to reduce atmospheric carbon dioxide (CO2) emissions and mitigate climate change, it has been proposed to sequester supercritical CO2 in underground saline aquifers. Geological storage of CO2 involves different trapping mechanisms which are not yet fully understood. In order to improve the understanding of the effect of chemical reaction on the flow and transport of CO2, these storage mechanisms are modelled experimentally and numerically in this work. In particular, the destabilising interaction between the fluid hydrodynamics and a density-increasing second-order chemical reaction is considered. It is shown that after nondimensional scaling, the flow in a given physicochemical system is governed by two dimensionless groups, Da/Ra2, which measures the timescale for convection compared to those for reaction and diffusion, and CBo', which reflects the excess of the environmental reactant species relative to the diffusing solute. The destabilising reactive scenario is modelled experimentally under standard laboratory conditions using an immiscible two-layer system with acetic acid acting as the solute. A novel colorimetric technique is developed to infer the concentrations of chemical species from the pH of the solution making it possible to measure the flux of solute into the aqueous domain. The validity of this experimental system as a suitable analogue for the dissolution of CO2 is tested against previous work and the destabilising effect of reaction is investigated by adding ammonia to the lower aqueous layer. The system is also modelled numerically and it is shown that the aqueous phase reaction between acetic acid and ammonia can be considered to be instantaneous, meaning that Da/Ra2 tends to infinity and the flow is therefore governed only by the initial dimensionless concentration of reactant in the aqueous phase. The results from the experiments and numerical simulations are in good agreement, showing that an increase in the initial concentration of reactant increases the destabilising effect of reaction, accelerates the onset of convection and enhances the rate of dissolution of solute. The numerical model is then applied to a real world aquifer in the Sleipner gas field and it is demonstrated how the storage capacity of a potential CO2 reservoir could be enhanced by chemical reaction.
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Books on the topic "Carbon dioxide capture and storage"

1

Royal Society of Chemistry (Great Britain), ed. Carbon capture: Sequestration and storage. RSC Pub., 2010.

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(Firm), Knovel, ed. Carbon capture and storage. Butterworth-Heinemann/Elsevier, 2010.

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Gielen, Dolf. Prospects for CO₂ capture and storage. OECD/IEA, 2004.

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Bert, Metz, and Intergovernmental Panel on Climate Change. Working Group III, eds. IPCC special report on carbon dioxide capture and storage. Cambridge University Press for the Intergovernmental Panel on Climate Change, 2005.

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Developments and innovation in carbon dioxide (CO2) capture and storage technology. CRC Press, 2010.

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Meadowcroft, James R. Caching the carbon: The politics and policy of carbon capture and storage. Edward Elgar, 2009.

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Forbes, Sarah M. CCS guidelines: Guidelines for carbon dioxide capture, transport, and storage. Edited by World Resources Institute. World Resources Institute, 2008.

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Institute, World Resources, ed. CCS guidelines: Guidelines for carbon dioxide capture, transport, and storage. World Resources Institute, 2008.

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Carbon capture and storage: CO2 management technologies. Apple Academic Press, 2014.

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R, Meadowcroft James, and Langhelle Oluf 1964-, eds. Caching the carbon: The politics and policy of carbon capture and storage. Edward Elgar, 2009.

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Book chapters on the topic "Carbon dioxide capture and storage"

1

Zhang, Xiaolei, Song Yan, R. D. Tyagi, Rao Y. Surampalli, and Tian C. Zhang. "Enzymatic Sequestration of Carbon Dioxide." In Carbon Capture and Storage. American Society of Civil Engineers, 2015. http://dx.doi.org/10.1061/9780784413678.ch14.

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Kao, C. M., Z. H. Yang, R. Y. Surampalli, and Tian C. Zhang. "Carbon Dioxide Capture Technology for the Coal-Powered Electricity Industry." In Carbon Capture and Storage. American Society of Civil Engineers, 2015. http://dx.doi.org/10.1061/9780784413678.ch08.

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Chiang, Pen-Chi, and Shu-Yuan Pan. "Post-combustion Carbon Capture, Storage, and Utilization." In Carbon Dioxide Mineralization and Utilization. Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-3268-4_2.

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Jochem, Eberhard. "Carbon Dioxide-Free Power Stations/Carbon Dioxide Capture and Storage." In Improving the Efficiency of R&D and the Market Diffusion of Energy Technologies. Physica-Verlag HD, 2009. http://dx.doi.org/10.1007/978-3-7908-2154-3_6.

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Raza, Arshad, and Raoof Gholami. "Introduction to Carbon Dioxide Capture and Storage." In Sustainable Agriculture Reviews. Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-29298-0_1.

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Aresta, Michele, and Angela Dibenedetto. "Reduction of Carbon Dioxide Emission into the Atmosphere: The Capture and Storage (CCS) Option." In The Carbon Dioxide Revolution. Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-59061-1_6.

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Shaikh, Huma, Shahnila Shah, Syed Shujaat Karim, et al. "Carbon Dioxide (CO2) Gas Storage and Utilization." In Facilitated Transport Membranes (FTMs) for CO2 Capture: Overview and Future Trends. Springer International Publishing, 2023. http://dx.doi.org/10.1007/978-3-031-21444-8_8.

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Das, Anita, Deanna M. D’Alessandro, and Vanessa K. Peterson. "Carbon Dioxide Separation, Capture, and Storage in Porous Materials." In Neutron Scattering Applications and Techniques. Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-06656-1_3.

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Leonenko, Yuri. "Feasibility of Ex-Situ Dissolution for Carbon Dioxide Sequestration." In Cutting-Edge Technology for Carbon Capture, Utilization, and Storage. John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119363804.ch4.

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Shah, Yatish T. "Methods for Carbon Dioxide Capture/Concentrate, Transport/Storage, and Direct Utilization." In CO2 Capture, Utilization, and Sequestration Strategies. CRC Press, 2021. http://dx.doi.org/10.1201/9781003229575-2.

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Conference papers on the topic "Carbon dioxide capture and storage"

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Li, He-nan, Fang-qin Li, Jian-xing Ren, and Zhi-wu Hao. "Carbon Dioxide Capture, Transport and Storage." In 2010 4th International Conference on Bioinformatics and Biomedical Engineering (iCBBE 2010). IEEE, 2010. http://dx.doi.org/10.1109/icbbe.2010.5516122.

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2

Harsh, A. H., and V. A. Anne. "Carbon Dioxide Capture, Utilization and Storage (CCUS)." In 76th EAGE Conference and Exhibition 2014. EAGE Publications BV, 2014. http://dx.doi.org/10.3997/2214-4609.20141330.

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Pun, Betty Kong Ling, Armen Abazajian, Maria Vlachopoulou, and Tarik Ihab Kamel. "Technoeconomic Considerations for Carbon Dioxide Capture and Storage Projects." In ADIPEC. SPE, 2022. http://dx.doi.org/10.2118/210846-ms.

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Abstract OGCI Climate Investments is an investment organization that specializes in methane, efficiency, and carbon capture, utilization, and storage (CCUS). The team has evaluated many carbon capture and storage (CCS) development stage projects involving elements of the capture, compression, transport, and storage value chain. A set of tools has been formulated for high-level cost estimates that can be used to sense-check developer proposals. The cost tools use publicly available CapEx and OpEx information and engineering best practices for cost-scaling methodologies. Cost models are constructed in a modular approach, with solvent-based CO2 capture, compression/dehydration, transport, and storage elements, and associated fixed and variable OpEx. The CO2 capture scope is further disaggregated into inside boundary limits (ISBL) and outside boundary limits (OSBL) estimates. This cost tool has proven to be useful in due diligence exercises for evaluating the merits of proposed projects for investment. Different configurations evaluated include post-combustion carbon capture projects from a variety of flue gas sources with different CO2 concentrations and at different scales, number of parallel trains of equipment, strategies for waste heat, steam or cooling utility supply, configurations to aggregate capture equipment from various sources or to gather CO2 from facilities, disaggregation of equipment in the value chain, etc. This paper provides hypothetical case studies to illustrate how such cost estimating provides useful insights into the economic viability of different types of projects at various levels of incentives. It also discusses limitations and development trends, such as commodity cycles and related engineering, procurement, and construction costs.
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4

Koperna, George Jonathan, and David Edward Riestenberg. "Carbon Dioxide Enhanced Coalbed Methane and Storage: Is There Promise?" In SPE International Conference on CO2 Capture, Storage, and Utilization. Society of Petroleum Engineers, 2009. http://dx.doi.org/10.2118/126627-ms.

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Pentland, Christopher Holst, Rehab El-Maghraby, Stefan Iglauer, Yoshihiro Tsuchiya, Hiroshi Okabe, and Martin Julian Blunt. "Measurement of Supercritical Carbon Dioxide Capillary Trapping in Core Analysis." In SPE International Conference on CO2 Capture, Storage, and Utilization. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/138476-ms.

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Hill, Gerald. "SECARB Phase III Anthropogenic Test and Plant Barry Carbon Dioxide Capture and Storage Demonstration." In Carbon Sequestration Leadership Forum PIRT. US DOE, 2013. http://dx.doi.org/10.2172/1765688.

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Hill, Gerald. "SECARB Phase III Anthropogenic Test and Plant Barry Carbon Dioxide Capture and Storage Demonstration." In Carbon Sequestration Leadership Forum Technical Group. US DOE, 2013. http://dx.doi.org/10.2172/1765689.

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Movagharnejad, Kamyar, Azadeh Emamgholivand, and Hamed Mousavi. "Capture and Storage of Carbon Dioxide in Iranian Geological Formations." In 2009 Second International Conference on Environmental and Computer Science. IEEE, 2009. http://dx.doi.org/10.1109/icecs.2009.30.

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Yang, Fulin, and Yun Xue. "Jiangsu Oil Field Carbon Dioxide Cyclic Stimulation Operations: Lessons Learned and Experiences Gained." In SPE International Conference on CO2 Capture, Storage, and Utilization. Society of Petroleum Engineers, 2010. http://dx.doi.org/10.2118/139599-ms.

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Ozaki, Masahiko, Naoki Nakazawa, Akira Omata, Masao Komatsu, and Hiroki Manabe. "Ship-Based Carbon Dioxide Capture and Storage for Enhanced Oil Recovery." In Offshore Technology Conference. Offshore Technology Conference, 2015. http://dx.doi.org/10.4043/25861-ms.

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Reports on the topic "Carbon dioxide capture and storage"

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Dahowski, Robert T., Xiaochun Li, Casie L. Davidson, Ning Wei, and James J. Dooley. Regional Opportunities for Carbon Dioxide Capture and Storage in China: A Comprehensive CO2 Storage Cost Curve and Analysis of the Potential for Large Scale Carbon Dioxide Capture and Storage in the People?s Republic of China. Office of Scientific and Technical Information (OSTI), 2009. http://dx.doi.org/10.2172/990594.

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Dooley, James J. A Framework for viewing theoretical, technological, economic and market potential of carbon dioxide capture and storage. Office of Scientific and Technical Information (OSTI), 2004. http://dx.doi.org/10.2172/939054.

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Dooley, James J., Casie L. Davidson, and Robert T. Dahowski. An Assessment of the Commercial Availability of Carbon Dioxide Capture and Storage Technologies as of June 2009. Office of Scientific and Technical Information (OSTI), 2009. http://dx.doi.org/10.2172/967229.

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4

Oldenburg, Curtis M., and Jens T. Birkholzer. Review of Quantitative Monitoring Methodologies for Emissions Verification and Accounting for Carbon Dioxide Capture and Storage for California’s Greenhouse Gas Cap-and-Trade and Low-Carbon Fuel Standard Programs. Office of Scientific and Technical Information (OSTI), 2014. http://dx.doi.org/10.2172/1339969.

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White, D. Carbon capture and storage. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 2016. http://dx.doi.org/10.4095/311151.

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Nealon, Teresa. Wyoming Carbon Capture and Storage Institute. Office of Scientific and Technical Information (OSTI), 2014. http://dx.doi.org/10.2172/1158899.

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Berchtold, Kathryn A. Fact Sheet: Polymer-Based Carbon Dioxide Capture Membrane Systems. Office of Scientific and Technical Information (OSTI), 2013. http://dx.doi.org/10.2172/1090637.

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Ghezel-Ayagh, Hossein. Electrochemical Membrane for Carbon Dioxide Capture and Power Generation. Office of Scientific and Technical Information (OSTI), 2017. http://dx.doi.org/10.2172/1414833.

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Lin, Jerry Y. S. Zeolite Membrane Reactor for Pre-Combustion Carbon Dioxide Capture. Office of Scientific and Technical Information (OSTI), 2020. http://dx.doi.org/10.2172/1618128.

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James Ritter, Armin Ebner, Steven Reynolds Hai Du, and Amal Mehrotra. New Adsorption Cycles for Carbon Dioxide Capture and Concentration. Office of Scientific and Technical Information (OSTI), 2008. http://dx.doi.org/10.2172/958277.

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