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Статті в журналах з теми "Post-combustion system"
Zhaofeng, Xu, He Xin, Xue Yali, and Li Zheng. "Dynamic Simulation of Post-Combustion Capture System." Energy Procedia 37 (2013): 2164–71. http://dx.doi.org/10.1016/j.egypro.2013.06.095.
Повний текст джерелаZhao, Li, Eko Primabudi, and Detlef Stolten. "Investigation of a Hybrid System for Post-Combustion Capture." Energy Procedia 63 (2014): 1756–72. http://dx.doi.org/10.1016/j.egypro.2014.11.183.
Повний текст джерелаBerger, Adam H., Yuqi Wang, Abhoyjit S. Bhown, Anthony Castrogiovanni, Robert Kielb, and Vladimir Balepin. "Thermodynamic Analysis of Post-combustion Inertial CO2 Extraction System." Energy Procedia 114 (July 2017): 7–16. http://dx.doi.org/10.1016/j.egypro.2017.03.1140.
Повний текст джерелаHussain, Arshad, Sarah Farrukh, and Fozia T. Minhas. "Two-Stage Membrane System for Post-combustion CO2 Capture Application." Energy & Fuels 29, no. 10 (September 29, 2015): 6664–69. http://dx.doi.org/10.1021/acs.energyfuels.5b01464.
Повний текст джерелаFernández, Javier, Maria Sotenko, Vladimir Derevschikov, Anton Lysikov, and Evgeny V. Rebrov. "A radiofrequency heated reactor system for post-combustion carbon capture." Chemical Engineering and Processing: Process Intensification 108 (October 2016): 17–26. http://dx.doi.org/10.1016/j.cep.2016.07.004.
Повний текст джерелаRaksajati, Anggit, Minh Ho, and Dianne Wiley. "Solvent Development for Post-Combustion CO2 Capture: Recent Development and Opportunities." MATEC Web of Conferences 156 (2018): 03015. http://dx.doi.org/10.1051/matecconf/201815603015.
Повний текст джерелаKawabata, Masako, Osamu Kurata, Norihiko Iki, Atsushi Tsutsumi, and Hirohide Furutani. "System modeling of exergy recuperated IGCC system with pre- and post-combustion CO2 capture." Applied Thermal Engineering 54, no. 1 (May 2013): 310–18. http://dx.doi.org/10.1016/j.applthermaleng.2013.01.029.
Повний текст джерелаMulukutla, Tripura, Gordana Obuskovic, and Kamalesh K. Sirkar. "Novel scrubbing system for post-combustion CO2 capture and recovery: Experimental studies." Journal of Membrane Science 471 (December 2014): 16–26. http://dx.doi.org/10.1016/j.memsci.2014.07.037.
Повний текст джерелаAkinola, Toluleke E., Eni Oko, Yuanlin Gu, Hua-Liang Wei, and Meihong Wang. "Non-linear system identification of solvent-based post-combustion CO2 capture process." Fuel 239 (March 2019): 1213–23. http://dx.doi.org/10.1016/j.fuel.2018.11.097.
Повний текст джерелаZhao, Li, Alexander Otto, Martin Robinius, and Detlef Stolten. "Investigation of the Cooling System of a Membrane-based Post-combustion Process." Energy Procedia 114 (July 2017): 666–85. http://dx.doi.org/10.1016/j.egypro.2017.03.1210.
Повний текст джерелаДисертації з теми "Post-combustion system"
Abdul, Manaf Norhuda. "MANAGEMENT DECISION SUPPORT SYSTEM OF SOLVENT-BASED POST-COMBUSTION CARBON CAPTURE." Thesis, The University of Sydney, 2016. http://hdl.handle.net/2123/16567.
Повний текст джерелаBrasington, Robert David S. M. Massachusetts Institute of Technology. "Integration and operation of post-combustion capture system on coal-fired power generation: load following and peak power." Thesis, Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/72878.
Повний текст джерелаCataloged from PDF version of thesis.
Includes bibliographical references (p. 85-87).
Coal-fired power plants with post combustion capture and sequestration (CCS) systems have a variety of challenges to integrate the steam generation, air quality control, cooling water systems and steam turbine with the capture system. A variety of engineering studies have been completed that cover these aspects when a plant is operating at full load while operating at a 90 percent capture rate. These studies investigate the basic integration of the these systems, the energy penalty and the effect of capital costs; however, none of these studies comprehensively explore the ability of the capture plant and the balance of the integrated system to respond dynamically to changes in load or capture rate. These load changes occur due to a change in demand for electricity in the system, generation by variable, intermittent resources, or if the plant is equipped with the ability to store solvent to implement price arbitrage. The integrated carbon capture system can be broken down into three general modes: full capacity, load following and peak power generation. Each of these modes presents unique challenges to integration with the CCS system. The load following mode requires the ability to accommodate different ramp rates that are reflected in flue gas flow and composition. Operation at partial load will affect the quality of steam sent to the solvent regeneration unit. Depending on the setup of the steam turbine system, at lower loads multiple extractions points may be necessary or an increase of the amount of extraction steam will be required due to the reduction in steam quality. Using Aspen Dynamics, a CO₂ capture system using a monoethanolamine (MEA) absorption process is simulated at various plant loads to determine the overall effects on the efficiency of the CCS unit and the balance of the system. In addition, the dynamic behavior of the CCS unit on power output and emissions is shown to demonstrate that the capability of a coal-fired power plant to load follow is not hindered by the addition of a carbon capture unit. The solvent storage mode can be further broken to two operation modes. The first is peak power production, which occurs when the solvent is capturing CO₂ from the flue gas, but is minimizing or delaying regeneration to a future time through storage. This mode is used to take advantage of peak power prices by maximizing power output of the plant and maintaining a 90 percent capture rate. The regeneration mode entails the solvent being released from the storage tanks and sent to the reboiler column. Solvent storage has been shown in previous studies to have the ability to increase operating profits, but these studies have neglected to incorporate the capital costs associated with this type of operation mode and the operational issues and complexity associated with the large swings in quantities of steam required for the solvent regeneration. By including the capital costs, this study determines that a system with large duration solvent storage is not economically viable given the flexible demands of the system and current electricity price spreads. This thesis presents a framework for considering the flexible operations of a coal-fired power plant with an integrated carbon capture and sequestration system. By exploring the operational limitations of the integrated system and the economic costs, an evaluation is made of the viability of different CCS operational schemes. This study finds that the CCS unit can match the dynamics of the base coal plant and also increase the operational flexibility of the system. The increased capital expenditure to meet peak demand is viable for larger steam turbine configurations in electricity systems with high peak prices and plants with short duration solvent storage.
by Robert David Brasington.
S.M.in Technology and Policy
Samuelsson, Peter. "Management of technology in the process industries: Matching market and machine." Doctoral thesis, KTH, 2017. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-199705.
Повний текст джерелаQC 20170116
Glier, Justin C. "Assessment of Solid Sorbent Systems for Post - Combustion Carbon Dioxide Capture at Coal - Fired Power Plants." Research Showcase @ CMU, 2015. http://repository.cmu.edu/dissertations/741.
Повний текст джерелаTait, Paul. "Pilot-scale testing of dynamic operation and measurement of interfacial wave dynamics in post-combustion carbon dioxide capture." Thesis, University of Edinburgh, 2018. http://hdl.handle.net/1842/29544.
Повний текст джерелаWang, Yuan Verfasser], Detlef [Akademischer Betreuer] [Stolten, and Manfred [Akademischer Betreuer] Wirsum. "Techno-economic assessment of hybrid post-combustion carbon capture systems in coal-fired power plants and steel plants / Yuan Wang ; Detlef Stolten, Manfred Wirsum." Aachen : Universitätsbibliothek der RWTH Aachen, 2020. http://d-nb.info/1240838603/34.
Повний текст джерелаVillar, I. Comajoan Laia. "Simulation of stripper modifications for bioenergy carbon capture by absorption." Thesis, KTH, Kemiteknik, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-299891.
Повний текст джерелаBio-energy with carbon capture and storage (BECCS) is a technology that can generate negative emissions. Hence it is recognized as a solution for becoming carbon neutral, which is essential for climate change mitigation. The main obstacle for its large scale implementation is the high energy requirements of the process. This thesis aims at quantifying the energy penalties for lean solvent flash and multi-pressure stripper layout modifications to improve the performance of carbon capture (CC) by means of absorption with a liquid solvent in a biomass-fired CHP plant. The work focuses on K2CO3 based solvents operated in a mixed temperature swing/pressure swing cycle witch is deemed advantageous for heat recovery. An equilibrium model was developed and validated to simulate a full-scale CC by chemical absorption in Aspen Plus using potassium carbonate as solvent. Both layout modifications result in energy penalties of 18-21 % for a CHP plant, while the energy penalty for the baseline process is 28 %. For a power plant, the penalties go from 32 % to 62 % for the lean solvent flash and the multi-pressure stripper respectively. This shows how improving the process can reduce the costs of CCS, especially if heat is considered a valuable product. CCS in CHP plants has a much lower energy impact than in power plants where heat is not recovered.
Jian-Syun-Li and 李建勳. "Post-combustion CO2 capture in a dry sorbent injection system." Thesis, 2015. http://ndltd.ncl.edu.tw/handle/24235645898048680655.
Повний текст джерела國立中興大學
環境工程學系所
103
Powder 13X zeolite was employed as the adsorbent for CO2 capture from flue gas by the dry sorbent injection and the feasibility of this process was evaluated. Research results were divided into the following two phases.The first phase was the comparison of the efficiency of capturing carbon dioxide between concurrent and countercurrent dry sorbent injection with powder 13X zeolite. The results indicate that the best of adsorption capacity was obtained under 30°C with 15 vol% CO2 inlet using powder 13X zeolite by the countercurrent dry sorbent injection. The adsorption capacity (q) of powder 13X zeolite reached 11.8 mg/g under 0.33 m/s of superficial velocity with gas-solid feed ratio of 20 g/L.The second phase was the comparison of CO2 adsorption/desorption with powder 13X zeolite between dry and wet flue gas inflow by countercurrent dry sorbent injection . The results indicated that after 50 cycles, the average q ,the AI (adsorption index) and the CO2 removal efficiency(RE) respectively reached 11.49 mg/g, 99.12% and 82.2% with dry flue gas and 11.1 mg/g, 99.12% and 81.5% with wet flue gas. Above results reveal that the powder 13X zeolite with countercurrent dry sorbent injection system has feasibility on CO2 capture from both dry and wet flue gas.
Chen, Jia-Xian, and 陳嘉賢. "Post-combustion CO2 capture in a Dry Sorbent Injection system." Thesis, 2016. http://ndltd.ncl.edu.tw/handle/85586514884678742723.
Повний текст джерела國立中興大學
環境工程學系所
104
The aim of this research is to obtain a technique of carbon capture which has economical development, refering to air pollution equipment in existence, we aim to change DSI into a technique of carbon capture. We use commercial material, zeolite 13X, to capture carbon for CO2 capture from flue gas. We intend to reduce carbon release and condense concentration of CO2 efficiently to promote capture and reuse of carbon. Then, we evaluate the possibility of this method according to the result of the resarch. Research results were divided into the following: The first part was found the best operating condition of granular 13X zeolite to capture carbon dioxide. We focus on the factors of the inlet like moisture content, CO2 concertration, temperature. The results showed that the best of adsorption capacity was obtained under 30 °C with 24lpm,15 % CO2 inlet. The working capacity (qw) reached 82.1 mg-CO2/g-13X. The second part desorbed CO2 from sorbents by using temperature programmed desorption process with low pressure condition or not. We operate the experiment under different desorption temperature, desorption time and five-cycles regeneration test to prove it. The results showed that 95% of CO2 was concentrated with Granular 13X under desorption conditions of 180°C in 10 minutes. In this desorption condition, the AI of 13X is 97.8, CO2 removel effferency is 99.1% and without the pressure swing process. Finally, DSI system is better way to capture CO2 in this research , compare with fixed bed and fluidized bed. These three method can capture 3.94、1.3、0.78 kgCO2 per day per kilogram 13X under the same conditions. The results indicate DSI system has feasibility on CO2 capture in a flue gas application.
Частини книг з теми "Post-combustion system"
Fosbøl, Philip, Nicolas von Solms, Arne Gladis, Kaj Thomsen, and Georgios M. Kontogeorgis. "Methods and Modelling for Post-combustion CO2Capture." In Process Systems and Materials for CO2Capture, 43–78. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch2.
Повний текст джерелаDinca, Cristian, Adrian Badea, Vladimir Tanasiev, and Horia Necula. "Life Cycle Assessment of Circulating Fluidized Bed Combustion with CO2 Post-Combustion Capture." In Progress in Systems Engineering, 113–20. Cham: Springer International Publishing, 2015. http://dx.doi.org/10.1007/978-3-319-08422-0_17.
Повний текст джерелаNeveux, Thibaut, Yann Le Moullec, and Éric Favre. "Post-combustion CO2Capture by Chemical Gas-Liquid Absorption." In Process Systems and Materials for CO2Capture, 283–310. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch11.
Повний текст джерелаDamartzis, Theodoros, Athanasios I. Papadopoulos, and Panos Seferlis. "Operability Analysis in Solvent-based Post-combustion CO2Capture Plants." In Process Systems and Materials for CO2Capture, 545–70. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch21.
Повний текст джерелаKakaras, Emmanouil K., Antonios K. Koumanakos, and Aggelos F. Doukelis. "Optimized Lignite-fired Power Plants with Post-combustion CO2Capture." In Process Systems and Materials for CO2Capture, 629–47. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch25.
Повний текст джерелаLawal, Adekola, Javier Rodriguez, Alfredo Ramos, Gerardo Sanchis, Mario Calado, Nouri Samsatli, Eni Oko, and Meihong Wang. "Improved Design and Operation of Post-combustion CO2Capture Processes with Process Modelling." In Process Systems and Materials for CO2Capture, 463–99. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch18.
Повний текст джерелаLiu, Helei, Raphael Idem, and Paitoon Tontiwachwuthikul. "Design, Modeling and Simulation of Post Combustion CO2 Capture Systems Using Reactive Solvents." In SpringerBriefs in Petroleum Geoscience & Engineering, 23–27. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-030-00922-9_3.
Повний текст джерелаNikolaidis, George N., Eustathios S. Kikkinides, and Michael C. Georgiadis. "Modelling and Optimization of Pressure Swing Adsorption (PSA) Processes for Post-combustion CO2Capture from Flue Gas." In Process Systems and Materials for CO2Capture, 343–69. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch13.
Повний текст джерелаBadr, Sara, Stavros Papadokonstantakis, Robert Bennett, Graeme Puxty, and Konrad Hungerbuehler. "Uncertainties in Modelling the Environmental Impact of Solvent Loss through Degradation for Amine Screening Purposes in Post-combustion CO2Capture." In Process Systems and Materials for CO2Capture, 153–72. Chichester, UK: John Wiley & Sons, Ltd, 2017. http://dx.doi.org/10.1002/9781119106418.ch6.
Повний текст джерелаAkula, Paul, John Eslick, Debangsu Bhattacharyya, and David C. Miller. "Modelling and Parameter Estimation of a Plate Heat Exchanger as Part of a Solvent-Based Post-Combustion CO2 Capture System." In Computer Aided Chemical Engineering, 47–52. Elsevier, 2019. http://dx.doi.org/10.1016/b978-0-12-818597-1.50008-4.
Повний текст джерелаТези доповідей конференцій з теми "Post-combustion system"
Cohen, Stuart M., Michael E. Webber, and Gary T. Rochelle. "Utilizing Solar Thermal Energy for Post-Combustion CO2 Capture." In ASME 2010 4th International Conference on Energy Sustainability. ASMEDC, 2010. http://dx.doi.org/10.1115/es2010-90147.
Повний текст джерелаManfredi Gasparovic, Claudia Luiza, Sandro Froehner, George Stanescu, and Marcelo Risso Errera. "CONSTRUCTAL DESIGN OF A MINERAL CARBONATION SYSTEM FOR POST-COMBUSTION CARBON CAPTURE." In 18th Brazilian Congress of Thermal Sciences and Engineering. ABCM, 2020. http://dx.doi.org/10.26678/abcm.encit2020.cit20-0468.
Повний текст джерелаChen, Xianhao, Shiyu Shen, Chonghui Zhang, Peizhi Liao, and Xiao Wu. "Feed-forward decoupling control of solvent-based post-combustion CO2 capture system." In 2019 Chinese Automation Congress (CAC). IEEE, 2019. http://dx.doi.org/10.1109/cac48633.2019.8997279.
Повний текст джерелаManfredi Gasparovic, Claudia Luiza, George Stanescu, and Marcelo Risso Errera. "FIRST-ORDER CONSTRUCT OF A MINERAL CARBONATION SYSTEM FOR POST-COMBUSTION CARBON CAPTURE." In 26th International Congress of Mechanical Engineering. ABCM, 2021. http://dx.doi.org/10.26678/abcm.cobem2021.cob2021-2004.
Повний текст джерелаLu, Xijia, Scott Martin, Mike McGroddy, Mike Swanson, Josh Stanislowski, and Jason D. Laumb. "Testing of a Novel Post Combustion Acid Removal Process for the Direct-Fired, Oxy-Combustion Allam Cycle Power Generation System." In ASME Turbo Expo 2017: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/gt2017-65217.
Повний текст джерелаDai, Baoxin, Xiao Wu, Xiufan Liang, and Jiong Shen. "Model predictive control of post-combustion CO2 capture system for coal-fired power plants." In 2017 36th Chinese Control Conference (CCC). IEEE, 2017. http://dx.doi.org/10.23919/chicc.2017.8028841.
Повний текст джерелаGülen, S. Can, and Chris Hall. "Gas Turbine Combined Cycle Optimized for Post-Combustion Carbon Capture." In ASME Turbo Expo 2017: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/gt2017-65261.
Повний текст джерелаAhn, Ji Ho, Ji Hun Jeong, and Tong Seop Kim. "Performance Enhancement of a Molten Carbonate Fuel Cell/Micro Gas Turbine Hybrid System With Carbon Capture by Off-Gas Recirculation." In ASME Turbo Expo 2018: Turbomachinery Technical Conference and Exposition. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/gt2018-76014.
Повний текст джерелаMontañé, Rubén, and Lars Olof Nord. "Dynamic Simulations of the Post-combustion CO2 Capture System of a Combined Cycle Power Plant." In The 12th International Modelica Conference, Prague, Czech Republic, May 15-17, 2017. Linköping University Electronic Press, 2017. http://dx.doi.org/10.3384/ecp17132111.
Повний текст джерелаChen, Qin, Ashok Rao, and Scott Samuelsen. "Solid Sorbent Post-Combustion CO2 Capture in Subcritical PC Power Plant." In ASME 2015 9th International Conference on Energy Sustainability collocated with the ASME 2015 Power Conference, the ASME 2015 13th International Conference on Fuel Cell Science, Engineering and Technology, and the ASME 2015 Nuclear Forum. American Society of Mechanical Engineers, 2015. http://dx.doi.org/10.1115/es2015-49483.
Повний текст джерелаЗвіти організацій з теми "Post-combustion system"
Brown, Alfred, and Nathan Brown. Novel Solvent System for Post Combustion CO{sub 2} Capture. Office of Scientific and Technical Information (OSTI), September 2013. http://dx.doi.org/10.2172/1155036.
Повний текст джерелаBalepin, Vladimir. Supersonic Post-Combustion Inertial CO2 Extraction System Final Report. Office of Scientific and Technical Information (OSTI), April 2017. http://dx.doi.org/10.2172/1394653.
Повний текст джерелаLiu, Kunlei, Heather Nikolic, Jesse Thompson, Reynolds Frimpong, Lisa Richburg, Keemia Abad, Saloni Bhatnagar, et al. Application of a Heat Integrated Post-combustion CO2 Capture System with Hitachi Advanced Solvent into Existing Coal-Fired Power Plant. Office of Scientific and Technical Information (OSTI), June 2020. http://dx.doi.org/10.2172/1635102.
Повний текст джерелаDillon, Des, Robert Chu, Haoren Lu, Brice Freeman, William Elliot, and Raymond McKaskle. Initial Engineering Design of a Post-Combustion CO2 Capture (PCC) System for Duke Energy’s East Bend Station Using Membrane-Based Technology. Office of Scientific and Technical Information (OSTI), October 2020. http://dx.doi.org/10.2172/1686164.
Повний текст джерела