Дисертації з теми "Carbon capture engineering (excl. sequestration)"
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Alexandrakis, Mary-Irene, and Bret S. (Bret Sanford) Smart. "Marine transportation for Carbon Capture and Sequestration (CCS)." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/60794.
Повний текст джерелаCataloged from PDF version of thesis.
Includes bibliographical references (p. 115-118).
The objective of this report is to determine whether opportunities to use liquefied carbon dioxide carriers as part of a carbon capture and storage system will exist over the next twenty years. Factors that encourage or discourage the use of vessels are discussed. This study concludes that liquefied carbon dioxide carriers can potentially be used in both the near and long term under different sets of circumstances.
by Mary-Irene Alexandrakis and Bret S. Smart.
S.M.in Transportation
Narain, Mudit. "Pathways to adoption of carbon capture and sequestration in India : technologies and policies." Thesis, Massachusetts Institute of Technology, 2007. http://hdl.handle.net/1721.1/39279.
Повний текст джерелаThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Includes bibliographical references (p. 83-85).
India is the world's second most populous country with a rapidly growing economy and increasing emissions. With the imminent threat of anthropogenic climate change in the coming decades, helping to control India's emissions will have to be a global priority. Carbon capture and sequestration (CCS) can play a pivotal role in reducing India's emissions in the future, given India's reliance on coal power and the large coal reserves. The motivation for this dissertation is the need to ascertain the current situation and conditions relevant to carbon capture in India so as to help guide the processes to prepare for large scale adoption if desired in the future. For carbon capture to be undertaken at a significant scale, various pieces will have to fall in to place in sync with each other. The technological capability would have to be complemented by adequate geological capacity under the umbrella of the right policies. Adoption of carbon capture would need a tailored approach for each country and for a diverse country the size of India, these approaches may need to be customized even locally to each region.
(cont.) The objective of this thesis is to increase the understanding of the opportunities, issues and challenges amongst the stakeholders regarding CCS in India regarding the capacity, political structures and policies. To address the objective, this dissertation analyzes the current power and coal sector situations, geological capacity for sequestration in India, the political decision making structures and the current views of the relevant civil servants in this field. At the end, there are some recommendations for the government of India and the international climate and CCS community to make conditions conducive for CCS in India.
by Mudit Narain.
S.M.
Ereira, Eleanor Charlotte. "Assessing early investments in low carbon technologies under uncertainty : the case of Carbon Capture and Storage." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/59674.
Повний текст джерелаCataloged from PDF version of thesis.
Includes bibliographical references (p. 100-106).
Climate change is a threat that could be mitigated by introducing new energy technologies into the electricity market that emit fewer greenhouse gas (GHG) emissions. We face many uncertainties that would affect the demand for each of these technologies in the future. The costs of these technologies decrease due to learning-by-doing as their capacity is built out. Given that we face uncertainties over future energy demands for particular technologies, and that costs reduce with experience, an important question that arises is whether policy makers should encourage early investments in technologies before they are economically competitive, so that they could be available in the future at lower cost should they be needed. If society benefits from early investments when future demands are uncertain, then there is an option value to investing today. This question of whether option values exist is investigated by focusing on Coal-fired Power Plants with Carbon Capture and Storage (CCS) as a case study of a new high-cost energy technology that has not yet been deployed at commercial scale. A decision analytic framework is applied to the MIT Emissions Prediction Policy Analysis (EPPA) model, a computable general equilibrium model that captures the feedback effects across different sectors of the economy, and measures the costs of meeting emissions targets. Three uncertainties are considered in constructing a decision framework: the future stringency of the US GHG emissions policy, the size of the US gas resource, and the cost of electricity from Coal with CCS. The decision modeled is whether to begin an annual investment schedule in Coal with CCS technology for 35 years. Each scenario in the decision framework is modeled in EPPA, and the output measure of welfare is used to compare the welfare loss to society of meeting the emissions target for each case. The decision framework is used to find which choice today, whether to invest in CCS or not, gives the smallest welfare cost and is therefore optimal for society. Sensitivity analysis on the probabilities of the three uncertainties is carried out to determine the conditions under which CCS investment is beneficial, and when it is not. The study finds that there are conditions, specified by ranges in probabilities for the uncertainties, where early investment in CCS does benefit society. The results of the decision analysis demonstrate that the benefits of CCS investment are realized in the latter part of the century, and so the resulting optimal decision depends on the choice of discount rate. The higher the rate, the smaller the benefit from investment until a threshold is reached where choosing to invest becomes the more costly decision. The decision of whether to invest is more sensitive to some uncertainties investigated than others. Specifically, the size of the US gas resource has the least impact, whereas the stringency of the future US GHG emissions policy has the greatest impact. This thesis presents a new framework for considering investments in energy technologies before they are economically competitive. If we can make educated assumptions as to the real probabilities we face, then extending this framework to technologies beyond CCS and expanding the decision analysis, would allow policymakers to induce investment in energy technologies that would enable us to meet our emissions targets at the lowest cost possible to society.
by Eleanor Charlotte Ereira.
S.M.in Technology and Policy
Chakroun, Nadim Walid. "Techno-economic analysis of sour gas oxy-fuel combustion power cycles for carbon capture and sequestration." Thesis, Massachusetts Institute of Technology, 2014. http://hdl.handle.net/1721.1/92148.
Повний текст джерелаCataloged from PDF version of thesis.
Includes bibliographical references (pages 217-222).
The world's growing energy demand coupled with the problem of global warming have led us to investigate new energy sources that can be utilized in a way to reduce carbon dioxide emissions than traditional fossil fuel power plants. One of these unconventional fuels is sour gas. Sour gas consists of mainly methane, containing large concentrations of hydrogen sulfide and carbon dioxide. Over 30% of the world's natural gas reserves are considered sour. However this unusual fuel poses many challenges due to the toxic and corrosive nature of the combustion products. One of the most promising technologies for carbon capture and sequestration is oxy-fuel combustion. This involves separating the nitrogen from air prior to the combustion itself. Then, after combustion, we separate the water and other substances and can use the resulting carbon dioxide stream for enhanced oil recovery representing an added economic benefit of this system. Firing temperatures for pure oxygen combustion can reach values up to 2500° C, which is well above what the combustor can handle. Therefore a diluent has to be added to reduce the temperature back to appropriate levels, but the key question is how this impacts the efficiency and performance of the entire cycle. Hence, if feasible, the use of sour gas in an oxy-fuel power plant could potentially allow us to harness the economic and environmental potential of this unconventional fuel. Depending on the cycle configuration, water or carbon dioxide can be used as diluents to control the flame temperature in the combustion process. All of these cycle types were modeled and the cycles' performances and emissions were studied. When the working fluid condenses in the cycle, sulfuric acid is formed due the presence of SO, compounds, which causes corrosion and can damage power plant components. Therefore, either expensive acid resistant materials should be used, or a redesign of the cycle is required to overcome this challenge. Different options were explored for each of the cycle types mentioned to help in the visualization and performance prediction of possible sour gas oxy-fuel power cycle configurations. A cost analysis of the proposed systems was also conducted in order to provide preliminary levelized cost of electricity estimates.
by Nadim Walid Chakroun.
S.M.
Kritzinger, Liaan Rudolf. "Establishing a pilot plant facility for post combustion carbon dioxide capture studies." Thesis, Stellenbosch : Stellenbosch University, 2013. http://hdl.handle.net/10019.1/80143.
Повний текст джерелаENGLISH ABSTRACT: Carbon dioxide (CO2) is seen as one of the main contributors to global warming. The use of fossil fuels for power production leads to large quantities of carbon dioxide being released into the atmosphere. The released CO2 can, however, be captured by retrofitting capture units downstream from the power plant called Post Combustion Carbon Dioxide Capturing. Post combustion CO2 capture can involve the reactive absorption of CO2 from the power plant flue gas steam. Reactive solvents, such as monoethanolamine (MEA), are used for capturing the CO2 and the solvent is regenerated in a desorber unit where the addition of heat drives the reverse reaction, releasing the captured CO2. However, the large energy requirement for solvent regeneration reduces the viability of employing CO2 capture on an industrial scale. This study focused on establishing a facility for CO2 capture studies – the main aim being the construction and validation of the results produced by the pilot plant facility. A secondary aim of this study was developing an Aspen Plus® Simulation method that would simplify simulating the complex CO2 capture process. Results from the simulation were to be compared to that of the pilot plant experiments. A pilot plant facility with a closed gas system, allowing gas recycling from both the absorber and the stripping columns, was set up. The absorber column (internal diameter = 0.2 m) was set up to allow one to obtain information regarding gas- and liquid temperatures and compositions at various column heights. Online gas analysers are used for analysing the gas composition at various locations in the absorber column. The pilot plant was initially commissioned with 20 weight % MEA in aqueous solution; however the main validation experiments were conducted with 30 weight % MEA in aqueous solution. 30 weight % MEA (aq) is generally used as the reference solvent for pilot plant studies. Pilot plant results with regards to the carbon dioxide concentration profiles for the absorber column as well as the regeneration energy requirement and capture rates compared well to literature data. The Aspen Plus® simulation was also set up and validated using published pilot plant data. The comparison of the pilot plant results from this study, to the results from the Aspen Plus® Simulation, showed good agreement between the two. The Aspen Plus® Simulation could further be used to validate pilot plant data that has been gathered outside the range of reported CO2 capture efficiencies. The Aspen Plus®model was evaluated at liquid-to-gas ratios of 1.7 and regeneration energies matching the pilot plant results. It was found that the model under predicts the capture efficiency of CO2 with an average of 4.0%. The model was corrected for this error at liquid-to-gas ratios of 2 and the fit of the model to pilot plant results improved considerably (R2-value = 0.965). Pilot plant repeatability was investigated with both 20 weight %- and 30 weight % MEA in aqueous solution. Temperature- and gas concentration profiles from the absorber column showed good repeatability. The maximum deviation of the regeneration energy and the capture efficiency from the calculation means were ±0.72% and ±1.40% respectively. The aims of this study have been met by establishing, and validating the results of a pilot plant facility for carbon dioxide capture studies. It has been shown that the pilot plant produces repeatable results. Results from the Aspen Plus® Simulation were validated and also match results from the established pilot plant setup. The simulation may prove to provide valuable information regarding the optimal operating conditions for the pilot plant and may aid in performing a full parametric study on the CO2 capture process.
AFRIKAANSE OPSOMMING: Koolstofdioksied (CO2) word geklassifiseer as een van die bekendste kweekhuisgasse wat ʼn groot bydra lewer tot aardverwarming. Die gebruik van fossielbrandstowwe om na die energiebehoeftes van die mens om te sien lei daartoe dat groot hoeveelhede koolstofdioksied, hoofsaaklik vanaf kragstasies, vrygestel word in die atmosfeer. Daar is verskeie maniere hoe die CO2 uit die uitlaatgas van kragstasies verwyder kan word – die vernaamste hiervan is bekend as die Na-verbranding opvangs metode. Die opvangs van CO2 na verbranding van fossielbrandstowwe vir kragproduksie kan vermag word deur van reaktiewe absorpsie tegnieke gebruik te maak. Mono-etanol-amien (MEA) kan vir hierdie doeleindes aangewend word deur dit, in ʼn absorpsiekolom, in kontak te bring met die CO2. Die gereageerde oplosmiddel word geregenereer deur die oplosmiddel te verhit in ʼn stropingskolom. ʼn Bykans suiwer CO2 stroom word vrygestel. Die implementering van hierdie opvangtegniek op industriële skaal lei egter tot groot energieverliese vir die kragstasies. Die hoofrede hiervoor is die hoeveelheid energie wat benodig word om die oplosmiddel te regenereer vir hergebruik. Die hoofdoel van hierdie studie was gemik op die oprigting en inwerkstelling van 'n navorsingsfasiliteit vir studies aangaande die na-verbranding opvangs van CO2. Dit het behels die ontwerp, konstruksie en stawing van gelewerde resultate met resultate in die literatuur. 'n Sekondêre doel van hierdie studie was die metode-ontwikkeling vir die opstel van 'n Aspen Plus® Model wat die simulasie van die CO2 opvangsproses met ʼn reaktiewe oplosmiddel, MEA, vereenvoudig. Gesimuleerde resultate is vergelyk met resultate uit die literatuur. Die toetsaanleg, met 'n geslote gas stelsel, maak voorsiening vir die hersirkulering van gas wat vir eksperimentele doeleindes gebruik word. Die absorpsie kolom (interne diameter van 0,2 m) is opgestel sodat informasie aangaande die gas- en vloeistof temperature, sowel as gas- en vloeistof komposisies vanaf verskillende kolomhoogtes, bekom kan word. ʼn Aanlyn CO2 analiseerder word gebruik om vir CO2 in die prosesgas te analiseer. Die toetsaanleg is aanvanklik in bedryf gestel met ʼn 20 massa % MEA in waterige oplossing; die hoof eksperimente is egter uitgevoer deur van 30 massa % MEA in waterige oplossing gebruik te maak. Die laasgenoemde oplosmiddel word algemeen gebruik in die CO2 opvangs verwante navorsingsveld. Die resultate van die toetsaanleg, vergelyk goed met resultate in die literatuur. Die gesimuleerde Aspen Plus® resultate is ook vergelyk met resultate in die literatuur en die gevolgtrekking is gemaak dat die simulasie gebruik kan word om redelike akkurate voorspellings van die werklike prosesresultate te gee. Die simulasie is verder ook gebruik om resultate, verkry vanaf die opgerigte toetsaanleg, te verifieer en ʼn goeie ooreenstemming tussen die gesimuleerde en die eksperimentele resultate is waargeneem. ʼn Verder gevolgtrekking aangaan die Aspen Plus® simulasie metode was dat dit in die toekoms ʼn groot doel kan dien in die optimeringsproses van toetsaanlegte waar navorsing aangaande die na-verbranding opvang van CO2 gedoen word. Die Aspen Plus® model is geëvalueer by ‘n vloeistof-tot-gas-verhouding van 1,7 en ooreenstemmende toetsaanleg resultate, aangaande die hoeveelheid energie wat ingesit is vir die regenerasie van die oplosmiddel. Die onakkuraathede in die model, met betrekking tot die voorspelling van die hoeveelheid CO2 wat vasgevang sal word, is hierdeur bepaal en die model is daarvoor aangepas. Resultate van die verbeterde model vergelyk baie goed met die toetsaanleg resultate – ʼn R2-waarde van 0.965. Die herhaalbaarheid van die toetsaanleg resultate is ondersoek en ʼn goeie herhaalbaarheid van die temperatuur- en CO2 konsentrasieprofiele is verkry. Die toetsaanleg dui ook goeie herhaalbaarheid met betrekking tot die effektiwiteit waarmee die CO2 uit ʼn gasstroom verwyder word (± 1,40%), sowel as die hoeveelheid energie wat benodig word vir regenerering van die oplosmiddel (± 0,72%). Die doelwitte van hierdie studie is bereik deur die oprigting en verifiëring van resultate gelewer deur 'n toetsaanleg vir studies aangaande die na-verbrandingsopvang van CO2. Die herhaalbaarheid van toetaanleg resultate is bewys. Resultate van die Aspen Plus® simulasie stem ooreen met resultate in die literatuur sowel as resultate van die toetsaanleg wat opgerig is in hierdie studie.
Hamilton, Michael Roberts. "An analytical framework for long term policy for commercial deployment and innovation in carbon capture and sequestration technology in the United States." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/59685.
Повний текст джерелаCataloged from PDF version of thesis.
Includes bibliographical references (p. 138-140).
Carbon capture and sequestration (CCS) technology has the potential to be a key CO2 emissions mitigation technology for the United States. Several CCS technology options are ready for immediate commercial-scale demonstration, but three obstacles to commercial deployment remain: the lack of a clear legal and regulatory framework for sequestration, the lack of a demonstration phase, and most importantly, the lack of a market for CCS. A successful demonstration phase will achieve the goal of technology readiness. The demonstration phase should be organized so as to share costs and risks between public and private actors. Project selection responsibility should be assigned to a dedicated private board and project management responsibility to private companies. This analysis recommends a combination of the Boucher Bill proposal for a CCS demonstration phase, as incorporated in the American Clean Energy and Security Act (ACES Act) of 2009, and a continuation of the DOE Clean Coal Power Initiative program. This combined approach can provide productive competition between public and private demonstration programs. Achieving technology readiness will not on its own lead to commercial deployment of CCS. Two additional policy objectives for the commercial deployment phase are considered: market penetration and cost reduction. Market penetration can be ensured through strong market pull policies, but this may be a very expensive policy approach in the long run. A more prudent goal is long-term cost reduction of CCS. Unlike the market penetration goal, the cost reduction goal will not guarantee that CCS will become a major contributor to carbon emissions mitigation, but it will provide a more cost-effective path. Achieving the cost reduction goal will require strong market pull policies for the short and medium term, together with a focus on technology push policies over the entire period. In the long term, market pull policies for CCS should be eliminated; if CCS is not economically competitive with alternative technologies, it should not be deployed on a significant scale. The ACES Act provides a good policy framework to achieve technology readiness through a demonstration phase and to pursue the long-term goal of cost reduction for commercial deployment of CCS technology. This approach will provide a cost-effective strategy for ensuring that CCS, a major scalable option for carbon emissions mitigation, is given the best chance of success in the long term.
by Michael Roberts Hamilton.
S.M.in Technology and Policy
Ebune, Guilbert Ebune. "Carbon Dioxide Capture from Power Plant Flue Gas using Regenerable Activated Carbon Powder Impregnated with Potassium Carbonate." Connect to resource online, 2008. http://rave.ohiolink.edu/etdc/view?acc_num=ysu1221227267.
Повний текст джерелаShu, Gary. "Economics and policies for carbon capture and sequestration in the western United States : a marginal cost analysis of potential power plant deployment." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/62874.
Повний текст джерелаThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.
Cataloged from student submitted PDF version of thesis.
Includes bibliographical references (p. 91-94).
Carbon capture and sequestration (CCS) is a technology that can significantly reduce power sector greenhouse gas (GHG) emissions from coal-fired power plants. CCS technology is currently in development and requires higher construction and operating costs than is currently competitive in the private market. A question that policymakers and investors have is whether a CCS plant will operate economically and be able to sell their power output once built. One way of measuring this utilization rate is to calculate capacity factors of possible CCS power plants. To investigate the economics of CCS generation, a marginal cost dispatch model was developed to simulate the power grid in the Western Interconnection. Hypothetical generic advanced coal power plants with CCS were inserted into the power grid and annual capacity factor values were calculated for a variety of scenarios, including a carbon emission pricing policy. I demonstrate that CCS power plants, despite higher marginal costs due to the operating costs of the additional capture equipment, are competitive on a marginal cost basis with other generation on the power grid at modest carbon emissions prices. CCS power plants were able to achieve baseload level capacity factors with $10 to $30 per ton-CO2 prices. However, for investment in CCS power plants to be economically competitive requires that the higher capital costs be recovered over the plant lifetime, which only occurs at much higher carbon prices. To cover the capital costs of first-of-the-kind CCS power plants in the Western Interconnection, carbon emissions prices have been calculated to be much higher, in the range of $130 to $145 per ton-CO2 for most sites in the initial scenario. Two sites require carbon prices of $65 per ton-CO2 or less to cover capital costs. Capacity factors and the impact of carbon prices vary considerably by plant location because of differences in spare transmission capacity and local generation mix.
by Gary Shu.
M.C.P.
S.M.in Technology and Policy
Dalton, Terra Ann. "Heterogeneity of Ohio’s Saline Reservoirs: Feldspar Abundance and its Effects on Carbon Sequestration." The Ohio State University, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=osu1313433616.
Повний текст джерелаOsman, Khalid. "Carbon dioxide capture methods for industrial sources." Thesis, 2010. http://hdl.handle.net/10413/3698.
Повний текст джерелаThesis (M.Sc.Eng.)-University of KwaZulu-Natal, Durban, 2010.
Gao, Ming. "Novel Liquid-Like Nanoscale Hybrid Materials with Tunable Chemical and Physical Properties as Dual-Purpose Reactive Media for Combined Carbon Capture and Conversion." Thesis, 2018. https://doi.org/10.7916/D8BK2VDG.
Повний текст джерелаSwanson, Edward J. "Catalytic Enhancement of Silicate Mineral Weathering for Direct Carbon Capture and Storage." Thesis, 2014. https://doi.org/10.7916/D8FQ9TK8.
Повний текст джерелаStonor, Maxim Richard Alphonse. "Bio-Energy with Carbon Capture and Storage (BECCS)- Production of H2 with Suppressed CO2 Formation via Alkaline Thermal Treatment." Thesis, 2017. https://doi.org/10.7916/D87M0DNW.
Повний текст джерела"Is Carbon Sequestration "Good" for the Environment? An Evaluation Based on Current Technology and Methods." Master's thesis, 2012. http://hdl.handle.net/2286/R.I.15119.
Повний текст джерелаDissertation/Thesis
sima pro
excel sheets
M.S. Civil and Environmental Engineering 2012
Ahmed, Sajjad. "Integration of New Technologies into Existing Mature Process to Improve Efficiency and Reduce Energy Consumption." Thesis, 2009. http://hdl.handle.net/10012/4502.
Повний текст джерела