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Relevant bibliographies by topics / Flue Gas Desulfurization Reactor

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Academic literature on the topic 'Flue Gas Desulfurization Reactor'

Author: Grafiati

Published: 4 June 2021

Last updated: 13 February 2022

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Journal articles on the topic "Flue Gas Desulfurization Reactor"

1

Yang, Yong, Hu Peng Yu, Jin Long Jiang, and Yun Hua Qian. "Flue Gas Desulfurization over Copper Oxide Loaded on Complex Carrier of Attapulgite and Activated Carbon." Advanced Materials Research 549 (July 2012): 387–90. http://dx.doi.org/10.4028/www.scientific.net/amr.549.387.

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Sorbent of CuO loaded on complex carrier of attapulgite and activated carbon was prepared by incipient impregnation method for flue gas desulfurization. The effects of CuO loading, reaction temperature and components in flue gas on the desulfurization performance were investigated in a fixed-bed quartz reactor. The experimental results indicate that the sorbents of 20 wt% CuO loading has a high desulfurization activity under conditions of reaction temperatures 200-250 oC and 21000 h-1, and O2 is necessary for the high desulfurization activity of the sorbents.

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Zhou, Jian An, Sheng Jun Zhong, Jun Xiang Dang, and Xu Li. "Experimental Investigation of Sintering Flue Gas Desulfurization with Steel Slag Using Dry CFB Method." Applied Mechanics and Materials 71-78 (July 2011): 2547–50. http://dx.doi.org/10.4028/www.scientific.net/amm.71-78.2547.

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SO2 Emission of sintering flue gas accounts for more than 70% of total SO2 emission of steel industry. The purpose of this paper was to use steel slag for desulfurization of sintering flue gas. Based on traditional circulating fluidized beds (CFB) for flue gas desulfurization (FGD), a new dry digestion CFB-FGD process was developed. The new process eliminated the traditional digestion procedure, and the functions of the reactor include preliminary dust collection, digestion and desulfurization. An pilot CFB installation with maximum flow rate of 8000 Nm3/h for flue gas desulfurization was esta

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3

Zhang, Yu Zhu, and Ying Xu. "Study of Dual-Alkali on Sintering Flue Gas Desulfurization." Advanced Materials Research 393-395 (November 2011): 304–7. http://dx.doi.org/10.4028/www.scientific.net/amr.393-395.304.

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Combining with the characteristics and control methods of sintering flue gas, several common methods for flue gas desulfurization(FGD) and development trend of desulfurization technology were described in this paper. According to characteristics of sintering flue gas and selection principles, dual-alkali method was used in the FGD. Desulfurization process, basic principle and characteristics of the process were studied in detail. By contrast test, the effect of concentration of the desulfurization, flue gas flow and surface active agent on the desulfurization efficiency was investigated in det

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4

Zhao, Jing Dong, Shi Jun Su, Xiao Fan Zhu, and Hong Lei Wang. "Experimental Study on Macro-Kinetics of Flue Gas Desulfurization Using Pyrolusite Pulp by a Double Magnetic Stirred Reactor." Materials Science Forum 610-613 (January 2009): 32–40. http://dx.doi.org/10.4028/www.scientific.net/msf.610-613.32.

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It’s a gas-liquid-solid three-phase reaction system in the reactor for flue gas desulfurization using pyrolusite pulp. Based on the two-film mass transfer theory and shrine core model, the macro-kinetics of flue gas desulfurization using pyrolusite pulp in a double magnetic stirred reactor were investigated. The effects of diffusion in solid film, surface chemical reaction, diffusion in liquid phase and gas phase of the process, have been carried out to distinguish the control step of the process. It was observed that SO2 absorption efficiency increased with the decreasing of pyrolusite partic

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Xiao, Hai Ping, Lin Dong, Gao Yan Han, and Xiang Ning. "Impacts on Water Consumption in Wet Flue Gas Desulfuration." Advanced Materials Research 986-987 (July 2014): 151–55. http://dx.doi.org/10.4028/www.scientific.net/amr.986-987.151.

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Material balance calculation was adopted to a bubbling desulfurization system of 600MW unit for water-saving measures. Analysis was made on main factors affecting water consumption. Results showed that heat release of desulfurization reaction and water evaporation went up with sulfur content increasing; Free water and bound water in gypsum increased rapidly with calcium improved; When sulfur content enhanced from 0.5% to 3.5%, water evaporation of reactor increased by 28.9% and waste water increased by 7.8%; With inlet flue temperature of WFGD raised from 120°C to 200°C, waste water increased

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6

Zhao, Jing Dong, Shi Jun Su, Nan Shan Ai, and Xiao Fan Zhu. "Modelling Flue Gas Desulfurization Using Pyrolusite Pulp in a Jet Bubbling Reactor." Materials Science Forum 610-613 (January 2009): 85–96. http://dx.doi.org/10.4028/www.scientific.net/msf.610-613.85.

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A mathematical model for flue gas desulfurization using pyrolusite pulp in jet bubbling reactor (JBR) was described. Firstly, based on the concept of two stages mass balance with chemical reaction, two models were set up, for jet bubbling zone and rising bubble zone, respectively, according to the construction of JBR. The models consist of two coupling differential equations and were solved simultaneously by integral and separation of the variables. Then the SO2 absorption efficiency expression was developed, considering the great discrepancy existing between the gas-side mass transfer coeffic

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7

Liao, Yong Jin, Ming Zhai, Fang Yong Li, Wei Qiang Shi, Yu Zhang, and Peng Dong. "Experimental Study on Desulfurization of Fly Ash Slurry." Applied Mechanics and Materials 148-149 (December 2011): 487–90. http://dx.doi.org/10.4028/www.scientific.net/amm.148-149.487.

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This paper designs a bubbling type of desulfurization reactor, which simulates flue gas nitrogen and sulfur dioxide according to a certain flow ratio, equipped with absorber through into the bubbling type desulfurization absorb and reactor by iodine volume method, measures import and export of SO2 concentration and pH value of absorber. The desulfurization rate of fly ash slurry is measured in the small drum bubble desulfurization reactor device. Results show that increasing the concentration of fly ash and entrance SO2 concentration, and decreasing particle size of fly ash will increase the d

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8

Guo, He, Nan Jiang, Jie Li, et al. "Study of oxidation of calcium sulfite in flue gas desulfurization by pore-type surface dielectric barrier discharge." RSC Advances 8, no. 8 (2018): 4464–71. http://dx.doi.org/10.1039/c7ra11503b.

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9

Yang, Liang, Yunkai Cai, and Lin Lu. "Experimental Study on Simultaneous Desulfurization and Denitrification by DBD Combined with Wet Scrubbing." Applied Sciences 11, no. 18 (2021): 8592. http://dx.doi.org/10.3390/app11188592.

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A dielectric barrier discharge (DBD) reactor combined with a wet scrubbing tower was used to carry out an experimental study on desulfurization and denitrification. The effects of the packing type, packing height, spray density, mass fraction of the NaOH solution, discharge power in the DBD reactor, and simulated flue gas flow rate on the desulfurization and denitrification efficiency were analyzed, along with the influence weight of each factor, using orthogonal testing. The experimental results showed that SO2 was easily absorbed by the scrubbing solution, while the desulfurization efficienc

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Shanshan, Zhang, Wang Renlei, Tang Guorui, and Dai YU. "Application and performance evaluation of desulfurization wastewater spray drying technology." E3S Web of Conferences 143 (2020): 02029. http://dx.doi.org/10.1051/e3sconf/202014302029.

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In order to realize zero discharge of desulfurization wastewater, spray drying technology of desulfurization wastewater was used in 2x330MW unit of a power plant. Its principle was to use a rotary atomizer for atomization,and a part of hot flue gas was drawn from the SCR denitrification reactor and air preheater into the drying tower, the heat was used to evaporate the desulfurization wastewater in a spray drying tower. The salt in the waste water was mixed with the dust, which was collected and removed by the electric dust remover. Then the water vapor was mixed with the flue gas and finally

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Dissertations / Theses on the topic "Flue Gas Desulfurization Reactor"

1

Duespohl, Dale W. "Modeling and optimization of a cross-flow, moving-bed, flue gas desulfurization reactor." Ohio : Ohio University, 1995. http://www.ohiolink.edu/etd/view.cgi?ohiou1179511746.

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2

Scott, Kevin David. "Electrochemical flue gas desulfurization." Diss., Georgia Institute of Technology, 1985. http://hdl.handle.net/1853/11145.

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Chiang, Ray-Kuang. "Calcium-based sorbents for flue gas desulfurization." Case Western Reserve University School of Graduate Studies / OhioLINK, 1995. http://rave.ohiolink.edu/etdc/view?acc_num=case1062008694.

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4

Carr, Kathryn E. "Evaluation of modified dry limestone process for flue gas desulfurization." Thesis, Virginia Tech, 1988. http://hdl.handle.net/10919/43382.

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Martin, Gregory Dean. "Microbial Community Composition and Activities in Wet Flue Gas Desulfurization Systems." University of Akron / OhioLINK, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=akron1493919370366314.

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Berry, David A. "Investigation of hot gas desulfurization utilizing a transport reactor." Morgantown, W. Va. : [West Virginia University Libraries], 1999. http://etd.wvu.edu/templates/showETD.cfm?recnum=500.

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Thesis (M.S.)--West Virginia University, 1999.<br>Title from document title page. Document formatted into pages; contains vi, 101 p. : ill. (some col.) Includes abstract. Includes bibliographical references (p. 82-85).

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Taerakul, Panuwat. "Characterization of trace elements in dry flue gas desulfurization (FGD) by-products." Connect to this title online, 2005. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1119038889.

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Thesis (Ph. D.)--Ohio State University, 2005.<br>Title from first page of PDF file. Document formatted into pages; contains xvii, 173 p.; also includes graphics Includes bibliographical references (p. 161-173). Available online via OhioLINK's ETD Center

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Iannacone, Meg M. "Evaluation of equalization basins as initial treatment for flue gas desulfurization waters." Connect to this title online, 2007. http://etd.lib.clemson.edu/documents/1202418446/.

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Pasini, Rachael A. "An Evaluation of Flue Gas Desulfurization Gypsum for Abandoned Mine Land Reclamation." The Ohio State University, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=osu1250605536.

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Paredez, Jose Miguel. "Coal-fired power plant flue gas desulfurization wastewater treatment using constructed wetlands." Thesis, Kansas State University, 2014. http://hdl.handle.net/2097/18255.

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Master of Science<br>Department of Civil Engineering<br>Natalie Mladenov<br>In the United States approximately 37% of the 4 trillion kWh of electricity is generated annually by combusting coal (USEPA, 2013). The abundance of coal, ease of storage, and transportation makes it affordable at a global scale (Ghose, 2009). However, the flue gas produced by combusting coal affects human health and the environment (USEPA, 2013). To comply with federal regulations coal-fired power plants have been implementing sulfur dioxide scrubbing systems such as flue gas desulfurization (FGD) systems (Alvarez-Ayu

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Books on the topic "Flue Gas Desulfurization Reactor"

1

Lunt, Richard R., and John D. Cunic. Profiles in Flue Gas Desulfurization. John Wiley & Sons, Inc., 2000. http://dx.doi.org/10.1002/9780470935446.

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2

Sudhoff, F. A. Shawnee flue gas desulfurization computer model users manual. U.S. Environmental Protection Agency, Industrial Environmental Research Laboratory, 1985.

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3

Miller, M. Michael. Flue gas desulfurization and industrial minerals: A bibliography. U.S. Bureau of Mines, 1993.

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4

Miller, M. Michael. Flue gas desulfurization and industrial minerals: A bibliography. U.S. Dept. of the Interior, Bureau of Mines, 1993.

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5

Miller, M. Michael. Flue gas desulfurization and industrial minerals: A bibliography. U.S. Bureau of Mines, 1993.

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6

Klingspor, Jonas S. FGD handbook: Flue gas desulphurisation systems. IEA Coal Research, 1987.

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7

Dacey, P. W. Flue gas desulphurisation: System performance. IEA Coal Research, 1986.

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8

Melia, M. Flue gas desulfurization information system (FGDIS): Data base user's manual. U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1985.

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9

Dotson, R. L. Lime spray dryer flue gas desulfurization computer model users manual. U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1987.

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10

Dotson, R. L. Lime spray dryer flue gas desulfurization computer model users manual. U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1987.

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Book chapters on the topic "Flue Gas Desulfurization Reactor"

1

Doğu, Gülşen, and Timur Doğu. "Kinetics of Capture of Sulfur Dioxide and Applications to Flue Gas Desulfurization." In Chemical Reactor Technology for Environmentally Safe Reactors and Products. Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2747-9_19.

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2

Devitt, Timothy W. "Flue Gas Desulfurization Systems." In Air Pollution Control Equipment. Springer Berlin Heidelberg, 1994. http://dx.doi.org/10.1007/978-3-642-85144-5_11.

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3

Punshon, T., A. S. Knox, D. C. Adriano, J. C. Seaman, and J. T. Weber. "Flue Gas Desulfurization (FGD) Residue." In Biogeochemistry of Trace Elements in Coal and Coal Combustion Byproducts. Springer US, 1999. http://dx.doi.org/10.1007/978-1-4615-4155-4_2.

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4

Kadambi, J. R., R. J. Adler, M. E. Prudich, et al. "Flue Gas Desulfurization for Acid Rain Control." In Dry Scrubbing Technologies for Flue Gas Desulfurization. Springer US, 1998. http://dx.doi.org/10.1007/978-1-4615-4951-2_1.

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5

Blythe, Gary. "Mercury Capture in Wet Flue Gas Desulfurization Systems." In Mercury Control. Wiley-VCH Verlag GmbH & Co. KGaA, 2014. http://dx.doi.org/10.1002/9783527658787.ch16.

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6

Chiang, Ray-Kuang, Gwanghoon Kwag, and Malcolm E. Kenney. "New Calcium-Based Sorbents for Flue Gas Desulfurization." In Dry Scrubbing Technologies for Flue Gas Desulfurization. Springer US, 1998. http://dx.doi.org/10.1007/978-1-4615-4951-2_2.

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7

Fueyo, N., A. Gomez, and J. F. Gonzalez. "A Comprehensive Mathematical Model of Flue-gas Desulfurization." In Progress in Industrial Mathematics at ECMI 2006. Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-71992-2_37.

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8

Duespohl, D. W., K. J. Sampson, S. Chattopadhyay, and M. E. Prudich. "Simulation and Optimization of a Granular Limestone Flue Gas Desulfurization Process." In Dry Scrubbing Technologies for Flue Gas Desulfurization. Springer US, 1998. http://dx.doi.org/10.1007/978-1-4615-4951-2_10.

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9

Mandal, D., R. Venkataramakrishnan, K. J. Sampson, and M. E. Prudich. "Fundamental Studies Concerning Calcium-Based Sorbents." In Dry Scrubbing Technologies for Flue Gas Desulfurization. Springer US, 1998. http://dx.doi.org/10.1007/978-1-4615-4951-2_3.

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Fan, L. S., E. Abou-Zeida, S. C. Liang, and X. Luo. "Sorbent Transport and Dispersion." In Dry Scrubbing Technologies for Flue Gas Desulfurization. Springer US, 1998. http://dx.doi.org/10.1007/978-1-4615-4951-2_4.

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Conference papers on the topic "Flue Gas Desulfurization Reactor"

1

Wang, Lidong, Yongliang Ma, Gang Yuan, and Jiming Hao. "Study on the Reaction Characteristics of Flue Gas Desulfurization by Magnesia." In 2009 3rd International Conference on Bioinformatics and Biomedical Engineering (iCBBE). IEEE, 2009. http://dx.doi.org/10.1109/icbbe.2009.5163522.

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2

Sun, Bao-Ming, Shui-E. Yin, and Zhong-Li Wang. "Study on the Experiments of Flue Gas Denitrification and Desulfurization Using Nitric Acid Solution." In ASME 2008 2nd International Conference on Energy Sustainability collocated with the Heat Transfer, Fluids Engineering, and 3rd Energy Nanotechnology Conferences. ASMEDC, 2008. http://dx.doi.org/10.1115/es2008-54073.

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The present study attempts to take nitric acid as absorbent to clean up SO2 and NO gases simultaneously from the simulated flue gas in the lab-scale bubbling reactor, this study was divide into the individual DeNOx experiments and the combined DeSOx/DeNOx experiments: the individual DeNOx experiments were carried out to examine the effect of various operating parameters such as input NO concentration, nitric acid concentration, oxygen concentration input SO2 concentration, adding KMnO4 as additive and taking NaOH as the secondary absorption processes on the SO2 and NOx removal efficiencies at

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3

Guo, Rui-tang, Wei-guo Pan, Xiao-bo Zhang, Jiang Wu, and Jian-xing Ren. "Dissolution Rate of Limestone for Wet Flue Gas Desulfurization in the Presence of Citric Acid." In ASME 2011 Power Conference collocated with JSME ICOPE 2011. ASMEDC, 2011. http://dx.doi.org/10.1115/power2011-55403.

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Dissolution rate of limestone for wet flue gas desulfurization in the presence of citric acid was measured by pH-stat method. It was found that limestone dissolution rate in the presence of citric acid was controlled by mass transfer. As can be seen from the experimental results, in the presence of citric acid, limestone dissolution rate increased with increasing stirring speed and reaction temperature. When pH value was greater than or equal to 5.5, due to the formation of calcium citrate, citric acid would inhibit the dissolution process of limestone. And the inhibition effect was more obvio

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Silaen, Armin, Bin Wu, Chenn Q. Zhou, and William Breen. "Numerical Model of FGD Unit in Power Plant." In ASME 2014 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/imece2014-37720.

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Numerical model technique was employed to model the reactive multiphase flow inside a flue gas desulfurization (FGD) unit. The model was divided into two parts: (a) the absorption tower model and (b) the reaction tank model. Eulerian-Lagrangian approach was employed in the absorption tower model. Discrete phase model was used to model the limestone slurry droplets and the SO2 absorption by the limestone slurry was included in the model. Eulerian-Eulerian approach was employed in the reaction tank model where the oxidation of the slurry to form gypsum was modeled. The absorption tower model and

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5

Zhong, Zhaoping, Basheng Jin, Jixiang Lan, Changqing Dong, and Hongchang Zhou. "Experimental Study of Municipal Solid Waste (MSW) Incineration and Its Flue Gas Purification." In 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-011.

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This paper presents experimental study of fluidized absorption process for flue gas purification of co-combustion of municipal solid waste (MSW) and coal in a circulating fluidized bed Combustor (CFBC) test rig. The test rig is composed of a CFBC, coal/MSW feeding subsystem, ash cycle subsystem and flue gas purification subsystem. In the circulating fluidized bed, section area of fluidized bed is 230mm × 230mm and the freeboard is 460mm × 395mm. The total height of the test facility is 8m; height of bed and freeboard are 1.5m and 6m respectively. The preheated air enters the bed as primary air

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Buecker, Brad. "Important Concepts of Wet-Limestone Flue Gas Desulfurization." In ASME 2008 Power Conference. ASMEDC, 2008. http://dx.doi.org/10.1115/power2008-60064.

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Many utilities are installing wet flue gas desulfurization (FGD) systems to comply with tighter sulfur dioxide regulations. These installations will introduce many utility engineers and other technical personnel to a sometimes complex air pollution control technology. This paper outlines fundamental concepts of wet limestone FGD, particularly in the most common design, spray towers. Topics will include liquid-to-gas ratio, chemistry operating parameters, limestone grinding and classification, materials selection for a rugged environment, byproduct disposal, and scrubber performance monitoring.

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Guo, Bin, Zhe Zhu, Ailing Ren, and Yuanming Guo. "Leaching characteristics of semidry flue gas desulfurization products." In 2009 International Conference on Energy and Environment Technology (ICEET 2009). IEEE, 2009. http://dx.doi.org/10.1109/iceet.2009.387.

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Werncke Vieira, Lara, Tiago Haubert Andriotty, Paulo Smith Schneider, Augusto Delavald Marques, Jakeline Osowski Tomazi, and GUILHERME LACERDA DE OLIVEIRA. "ENERGY PENALTY MODEL FOR FLUE GAS DESULFURIZATION SYSTEMS." In Brazilian Congress of Thermal Sciences and Engineering. ABCM, 2018. http://dx.doi.org/10.26678/abcm.encit2018.cit18-0832.

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Wang, Xiaoliang, and Junping Deng. "Advances in Utilization of Flue Gas Desulfurization Gypsum." In 5th International Conference on Advanced Design and Manufacturing Engineering. Atlantis Press, 2015. http://dx.doi.org/10.2991/icadme-15.2015.222.

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Zhentao, Wang, and Luo Tiqian. "Experimental Investigation on Flue Gas Desulfurization by Electrostatic Spray." In 2009 International Conference on Energy and Environment Technology. IEEE, 2009. http://dx.doi.org/10.1109/iceet.2009.477.

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Reports on the topic "Flue Gas Desulfurization Reactor"

1

Gardner, N., M. Keyvani, and A. Coskundeniz. Flue gas desulfurization by rotating beds. Office of Scientific and Technical Information (OSTI), 1992. http://dx.doi.org/10.2172/7170260.

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2

Author, Not Given. Confined zone dispersion flue gas desulfurization demonstration. Office of Scientific and Technical Information (OSTI), 1992. http://dx.doi.org/10.2172/7296798.

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Author, Not Given. Confined zone dispersion flue gas desulfurization demonstration. Office of Scientific and Technical Information (OSTI), 1992. http://dx.doi.org/10.2172/6634187.

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4

Moore, Joe, Preom Sarkar, and Djuna Gulliver. Biological Treatment of Flue Gas Desulfurization Wastewater. Office of Scientific and Technical Information (OSTI), 2021. http://dx.doi.org/10.2172/1766571.

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Gardner, N., M. Keyvani, and A. Coskundeniz. Flue gas desulfurization by rotating beds. Final technical report. Office of Scientific and Technical Information (OSTI), 1992. http://dx.doi.org/10.2172/10103400.

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Michael W. Grutzeck, Maria DiCola, and Paul Brenner. BUILDING MATERIALS MADE FROM FLUE GAS DESULFURIZATION BY-PRODUCTS. Office of Scientific and Technical Information (OSTI), 2006. http://dx.doi.org/10.2172/881574.

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Wu, M. M., D. C. McCoy, R. O. Scandrol, M. L. Fenger, J. A. Withum, and R. M. Statnick. PRODUCTION OF CONSTRUCTION AGGREGATES FROM FLUE GAS DESULFURIZATION SLUDGE. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/794137.

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National Energy Technology Laboratory. Advanced Flue Gas Desulfurization (AFGD) Demonstration Project, A DOE Assessment. Office of Scientific and Technical Information (OSTI), 2001. http://dx.doi.org/10.2172/787341.

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G. Blythe, B. Marsh, S. Miller, C. Richardson, and M. Richardson. ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS. Office of Scientific and Technical Information (OSTI), 2001. http://dx.doi.org/10.2172/828035.

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Unknown. ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS. Office of Scientific and Technical Information (OSTI), 2001. http://dx.doi.org/10.2172/794238.

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