Academic literature on the topic 'Wet flue gas desulfurization (WFGD)'

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Journal articles on the topic "Wet flue gas desulfurization (WFGD)"

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Xiao, Hai Ping, Lin Dong, Gao Yan Han, and Xiang Ning. "Influence of Gas-Gas Heater on Wet Flue Gas Desulfuration." Advanced Materials Research 986-987 (July 2014): 92–96. http://dx.doi.org/10.4028/www.scientific.net/amr.986-987.92.

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Material balance calculation was adopted to a wet flue gas desulfurization (WFGD) system for exploring impacts of gas-gas heater (GGH). Effects of GGH on flue and water consumption were analyzed. Results showed that inlet flue temperature of desulfurization tower reduced by 3.4 °C at 100% load after installation of GGH. Exhausted gas temperature of system increased by 34.9°C. The heat release of original flue in desulfurization tower reduced by 43.72%. Plume rise height was significantly improved. Water evaporation in desulfurization tower declined by 42.07%.Amount of addendum water reduced by
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Qu, Cheng Tun, Hong Guang Su, Jing Tian, Xue Yang, and Xin Wang. "The Main WFGD Technologies and their Development Trend." Advanced Materials Research 599 (November 2012): 510–15. http://dx.doi.org/10.4028/www.scientific.net/amr.599.510.

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Abstract: Four popular wet flue gas desulfurization processes were introduced in the paper, including their principles, advantages and disadvantages and application scale. Several process indexes were compared. Finally based on much analysis, the development trend of mainstream wet flue gas desulfurization is predicted.
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Song, Jing Hui, Yan Lin, Yan Fen Liao, Xiao Qian Ma, and Shu Mei Wu. "Economic Analysis of Wet Flue Gas Desulfurization System with the Application of Low Pressure Economizer for Waste Heat Recovery." Advanced Materials Research 1092-1093 (March 2015): 491–97. http://dx.doi.org/10.4028/www.scientific.net/amr.1092-1093.491.

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The data of wet flue gas desulfurization (WFGD) power and water consumption, from two different coal-fired power plants (100 MW and 1000 MW) under full load operation, are studied for the WFGD economic analysis of waste-heat-recovery transformation with the installation of low pressure economizer (LPE). The results of 100MW unit show that, WFGD inlet flue gas temperature drops from 155°C to 110°C, the benefits generated include power consumption of fans declines by 23.85% and water consumption of the smoke desulfurization absorption tower declines by 34.88%. In another case, the temperature of
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Chen, Chuanmin, Songtao Liu, Yang Gao, and Yongchao Liu. "Investigation on Mercury Reemission from Limestone-Gypsum Wet Flue Gas Desulfurization Slurry." Scientific World Journal 2014 (2014): 1–6. http://dx.doi.org/10.1155/2014/581724.

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Secondary atmospheric pollutions may result from wet flue gas desulfurization (WFGD) systems caused by the reduction of Hg2+to Hg0and lead to a damping of the cobenefit mercury removal efficiency by WFGD systems. The experiment on Hg0reemission from limestone-gypsum WFGD slurry was carried out by changing the operating conditions such as the pH, temperature, Cl−concentrations, and oxygen concentrations. The partitioning behavior of mercury in the solid and liquid byproducts was also discussed. The experimental results indicated that the Hg0reemission rate from WFGD slurry increased as the oper
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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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Jiang, Yu Ze, Chuan Min Chen, Li Xing Jiang, Song Tao Liu, and Bin Wang. "Study of Mercury Re-Emission from Simulated Wet Flue Gas Desulfurization Liquors." Advanced Materials Research 610-613 (December 2012): 2033–37. http://dx.doi.org/10.4028/www.scientific.net/amr.610-613.2033.

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Hg2+captured by wet flue gas desulfurization (WFGD) systems can easily be reduced by reducing substances such as S(IV) (SO32-or HSO3-) and results in emissions of elemental mercury (Hg0). The re-emission of Hg0would lead to a damping of the total mercury removal efficiency by WFGD systems. The effects of the operating conditions, which included the pH, temperature, Cl-concentrations and oxygen concentrations, on Hg0re-emission from WFGD liquors was carried out. The experimental results indicated that the Hg0re-emission rate from WFGD liquors increased as the operational temperatures and pH val
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Wypiór, Tomasz, and Renata Krzyżyńska. "Influence of ammonia on wet-limestone flue gas desulfurization process from coal-based power plant." E3S Web of Conferences 116 (2019): 00101. http://dx.doi.org/10.1051/e3sconf/201911600101.

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The paper presents data concerning the influence of ammonia on wet flue gas desulfurization (WFGD) absorber. Paper presents preliminary results of an industrial scale study on WFGD absorber, that collects flue gases from four boilers with total flue gas flow capacity of the WFGD equal to 1 500 000 Nm3/h. Each boiler is equipped with selective non-catalytic reduction (SNCR) with urea injection. It was shown, that ammonia present in the flue gas upstream the WFGD increases the pH of absorption slurry, impacting the desulphurization process. In addition, analysis of particulate matter upstream an
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Deng, Jia-jia, Liang-ming Pan, De-qi Chen, et al. "Numerical simulation and field test study of desulfurization wastewater evaporation treatment through flue gas." Water Science and Technology 70, no. 7 (2014): 1285–91. http://dx.doi.org/10.2166/wst.2014.359.

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Aimed at cost saving and pollution reduction, a novel desulfurization wastewater evaporation treatment system (DWETS) for handling wet flue gas desulfurization (WFGD) wastewater of a coal-fired power plant was studied. The system's advantages include simple process, and less investment and space. The feasibility of this system has been proven and the appropriate position and number of nozzles, the spray droplet size and flue gas temperature limitation have been obtained by computational fluid dynamics (CFD) simulation. The simulation results show that a longer duct, smaller diameter and higher
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Wang, Anyu, Shuran Li, Qinzhen Zheng, et al. "Study on the Effects of Wet Flue Gas Desulfurization on Particulate Matter Emission from Industrial Coal-Fired Power Plants." Separations 10, no. 6 (2023): 356. http://dx.doi.org/10.3390/separations10060356.

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This study aimed to investigate the effects of wet flue gas desulfurization (WFGD) on particulate matter (PM) emissions in coal-fired power plants (CFPPs) using an electrical low-pressure impactor (ELPI). The investigation was conducted on five industrial CFPPs of various loads in China to clarify the influence factors of WFGD on PM10 emissions. After WFGD, the proportion of PM2.5 to PM10 in the outlet flue gas increases, which showed that the WFGD system is selective in the capture of PM, with a significant effect on the capture of large particle sizes. The investigation found that four spray
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Liu, Hong Lei, Zhi Qi Wang, and Lei Zhang. "Test and Application of Desulfurization Catalyst." Advanced Materials Research 781-784 (September 2013): 2577–81. http://dx.doi.org/10.4028/www.scientific.net/amr.781-784.2577.

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Explains the principle and reaction mechanism of desulfurization catalyst. Introduces the test applying desulfurization catalyst in WFGD (wet flue gas desulfurization) system of 320MW generating units operating in thermal power plant. Desulfurization efficiency is improved significantly by using desulfurization catalyst of 100 μ g/g to 600 μ g/g concentrations. To save electricity, stopping the top level slurry pump is the priority.
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Dissertations / Theses on the topic "Wet flue gas desulfurization (WFGD)"

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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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Sanghavi, Urvi. "Novel Regenerable Adsorbents for Wastewater Treatment from Wet Flue Gas Scrubbers." University of Cincinnati / OhioLINK, 2016. http://rave.ohiolink.edu/etdc/view?acc_num=ucin147982088374556.

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Tseng, Chao-Heng. "Enhanced Pulsed Corona Method for the Removal of SO2 and NOx from Combustion Gas in a Wet Electrostatic Precipitator." University of Cincinnati / OhioLINK, 2000. http://rave.ohiolink.edu/etdc/view?acc_num=ucin962380157.

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Sklenářová, Dorothea. "Studium vlivů, které ovlivňují reaktivitu vápenců." Master's thesis, Vysoké učení technické v Brně. Fakulta stavební, 2018. http://www.nusl.cz/ntk/nusl-372112.

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This thesis is a part of grant assignment and focuses on the effect and properties of input material, limestone, on reactivity and speed of decarbonation. The aim of this thesis is to find the effect of chemical composition, petrography, genesis and diagenesis, porosity and microstructure of limestones on reactivity and speed and profile of decarbonation. The experimental part of thesis describes analysis of chosen limestone samples regarding porosity, reactivity by Bischof-Uhde method and process of decarbonation of calcite in term of crystallinity of product.
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Chu, Kuo-Wei, and 朱國偉. "Cost Function for Wet Desulfurization of Flue Gas." Thesis, 2008. http://ndltd.ncl.edu.tw/handle/09783822841858946097.

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碩士<br>國立臺灣大學<br>環境工程學研究所<br>96<br>Wet method is one of major treatment procedures for flue-gas desulphurization. In Taiwan, there are four kinds of treatment system are used frequently and the market share is over 95%. In order to assist users for better decision-making process, the purpose of this study is to build up a simple cost function and to compare four commonly used wet methods of flue-gas desulphurization as the subject of research. In additions, this study also defines the research scope and rules out the uncertain factors. Based on the simulation results of this cost model
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Koech, Lawrence. "The dissolution of limestone, coal fly ash and bottom ash in wet flue gas desulphurization." Thesis, 2015. http://hdl.handle.net/10352/356.

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M. Tech. (Department of Chemical Engineering, Faculty of Engineering and Technology): Vaal University of Technology<br>Strict environmental regulation on flue gas emission has led to the implementation of FGD technologies in power stations. Wet FGD technology is commonly used because it has high SO2 removal efficiency, high sorbent utilization and due to availability of the sorbent (limestone) used. SO2 is removed by passing flue gas through the absorber where it reacts with the slurry containing calcium ions which is obtained by dissolution. This study presents the findings of the dissolutio
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Books on the topic "Wet flue gas desulfurization (WFGD)"

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Krzyżyńska, Renata. Zintegrowane oczyszczanie spalin z SO₂, NOx i Hg w układach mokrego odsiarczania spalin: Integrated removal of SO₂, NOx and Hg in the wet flue gas desulphurization systems. Oficyna Wydawnicza Politechniki Wrocławskiej, 2012.

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Environmental review of the proposed wet flue gas desulfurization (FGD) system project at the Chalk Point Generating Station. Maryland Department of Natural Resources, Maryland Power Plant Research Program, 2008.

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Book chapters on the topic "Wet flue gas desulfurization (WFGD)"

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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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Kunkun, Han, Chi Guozhen, and Ni Jianjun. "Simulation Study on the Demercuration Performance of Wet Flue Gas Desulfurization System." In Clean Coal Technology and Sustainable Development. Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-2023-0_60.

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Chang, S. G. "Technical Analyses of a Wet Process for Flue Gas Simultaneous Desulfurization and Denitrification." In ACS Symposium Series. American Chemical Society, 1986. http://dx.doi.org/10.1021/bk-1986-0319.ch014.

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Brown, Shannon R., Richard F. DeVault, and Paul J. Williams. "Application of Test Methods for Use in Limestone Selection for Wet Flue Gas Desulfurization." In Lime: Building on the 100-Year Legacy of The ASTM Committee C07. ASTM International, 2012. http://dx.doi.org/10.1520/stp104324.

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Brown, Shannon R., Richard F. DeVault, and Paul J. Williams. "Application of Test Methods for Use in Limestone Selection for Wet Flue Gas Desulfurization." In Lime: Building on the 100-Year Legacy of The ASTM Committee C07. ASTM International, 2012. http://dx.doi.org/10.1520/stp104324t.

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Zhang, Lin, Bin Hu, Hao Wu, Xia Wang, Rui Liu, and Linjun Yang. "CO2 Capture Using Hollow Fiber Membrane Under Wet Ammonia-Based Desulfurization Flue Gas Conditions." In Clean Coal Technology and Sustainable Development. Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-2023-0_49.

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Huang, Yu, Peng-shuai Han, Xin Guo, and Chu-guang Zheng. "Experimental Study on the Stability of the Mercuric Complexes in Wet Flue Gas Desulfurization Wastewater." In Clean Coal Technology and Sustainable Development. Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-2023-0_63.

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Xu, Jialing, Jingjing Bao, Jiguo Tang, Min Du, Zhengyu Mo, and Licheng Sun. "Characteristics of Hg0 Re-emission Caused by Sulfite in a Wet Flue Gas Desulfurization System." In Clean Coal and Sustainable Energy. Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-1657-0_67.

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Hao, Wu, and Yang Linjun. "Removal of Fine Particles from Coal Combustion by Heterogeneous Condensational Enlargement in Wet Flue Gas Desulfurization." In Clean Coal Technology and Sustainable Development. Springer Singapore, 2016. http://dx.doi.org/10.1007/978-981-10-2023-0_54.

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del Valle-Zermeño, Ricardo, Josep Maria Chimenos, and Joan Formosa. "Flue Gas Desulfurization." In Applying Nanotechnology to the Desulfurization Process in Petroleum Engineering. IGI Global, 2016. http://dx.doi.org/10.4018/978-1-4666-9545-0.ch011.

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Most of the total quantity of sulfur oxides (SOx) emitted to the atmosphere come from the combustion of fossil fuels, whose preponderance in the energy mix is expected to prevail in the years to come. In order to avoid the damaging consequences that this supposes, the improvement of the removal methods has been the topic of many researches. In this sense, the majority of abatement processes have always been based on wet Flue Gas Desulfurization (wFGD) technologies. In this chapter, the origin, development, deployment and enhancement of the wFGD processes is thoroughly revised. From the early s
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Conference papers on the topic "Wet flue gas desulfurization (WFGD)"

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Tossey, Brett M., John Shingledecker, and Barbara (Nikki) Padgett. "Technical Root Cause Analysis of Localized Corrosion in Wet Flue Gas Desulfurization Slurry at Coal-Fired Power Stations." In CORROSION 2014. NACE International, 2014. https://doi.org/10.5006/c2014-4442.

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Abstract Recent experience with stainless steels in wet flue gas desulfurization service has shown rapid localized attack. This paper discusses a brief historical perspective on the material performance in wet flue gas desulfurization (WFGD) and the findings of a technical root cause analysis (TRCA). Observations of attacked WFGD absorbers shows pitting and crevice corrosion near welds in the immersion zone and inside spray headers. All of the absorbers that were the subject of the TRCA were forced-oxidation limestone absorbers. Vertical spray towers and jet bubbling reactors were inspected an
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Tossey, Brett M., John Shingledecker, and Barbara (Nikki) Padgett. "Field Testing of Ten Corrosion Resistant Alloys in Wet Flue Gas Desulfurization Absorber Slurries." In CORROSION 2014. NACE International, 2014. https://doi.org/10.5006/c2014-4441.

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Abstract The Electric Power Research Institute (EPRI) and Det Norske Veritas USA, Inc. (DNV) performed a field-testing program that supported the “Corrosion in Wet Flue Gas Desulfurization Systems” study. This study was motivated by the fact that many alloy wet flue gas desulfurization (WFGD) absorbers of recent construction are experiencing premature failure from localized corrosion. The alloys of construction most affected by localized corrosion attack are: (1) UNS S32205 – a duplex stainless steel and (2) UNS S31703 – an austenitic stainless steel. The rate of attack on these alloys has exc
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Bochicchio, Victor A. "FRP Chimney Liners for Power Plant Flue Gas Desulfurization – a Chimney Supplier’s Perspective." In CORROSION 2011. NACE International, 2011. https://doi.org/10.5006/c2011-11366.

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Abstract The addition of Wet Flue Gas Desulphurization (WFGD) systems to existing coal fired power plants, and at several new plants, has resulted in the installation of over 90 FRP chimney liners in concrete chimneys during the past 6 years. The lower flue gas temperatures in power plants with WFGD increases corrosion concerns for chimney lining materials and often leads to the selection of FRP as the liner material of choice. Although the design and manufacture of the FRP liner is usually performed by a specialty FRP supplier, the integration of the liner into the overall chimney design and
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Tossey, Brett M., and John Shingledecker. "Corrosion Mitigation Strategies in Forced Oxidation Wet Flue Gas Desulfurization Absorbers Made of UNS S32205 Duplex Stainless Steel." In CORROSION 2015. NACE International, 2015. https://doi.org/10.5006/c2015-05947.

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Abstract Independent investigators documented corrosion mitigation strategies at power stations. The study was motivated by the fact that many alloy wet flue gas desulfurization (WFGD) absorbers of recent construction are experiencing premature failure from localized corrosion. The alloy of construction most affected by localized corrosion attack is UNS S32205 – a duplex stainless steel. The rate of attack has exceeded 500 mils per year (mpy) in forced oxidation WFGD service. A corrosion rate of this magnitude will lead to perforation of the absorber walls and floor in less than one year of se
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Gates, Emily, Barbara Padgett, Bill Harper, Brett Tossey, and John Shingledecker. "Corrosion Resistance of Alloys in Calcium Bromide and Calcium Chloride Solutions." In CORROSION 2017. NACE International, 2017. https://doi.org/10.5006/c2017-09749.

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Abstract Calcium bromide is used in the coal fire power plant industry to help control mercury emissions. Adding bromide ions to the flue gas can cause the total halide ion content of the downstream Wet Flue Gas Desulfurization (WFGD) slurry to increase. The objective of this study was to determine the effect of bromide additions in chloride-rich WFDG slurries on the crevice corrosion resistance of commercially-available corrosion resistant alloys. Cyclic potentiodynamic polarization (CPP) was used to collect voltage-current traces for each alloy. The traces were analyzed to estimate the perfo
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Kelley, Don H., and Bob Brady. "Cost Effective Materials for Flue Gas Desulfurization (FGD)." In CORROSION 1996. NACE International, 1996. https://doi.org/10.5006/c1996-96398.

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Abstract Wet Flue Gas Desulfurization (FGD) is an effective way to remove sulfur dioxide from coal combustion processes and reduce the potential for acid rain. However, wet FGD processes often require highly corrosion resistant construction materials such as high alloys for adequate service life. An excellent material for wet FGD applications at about one half the cost of high alloys is fiberglass-reinforced plastic (FRP) based on epoxy vinyl ester resin. This paper will discuss the background and improvements that have led to the use of some of the world's largest composite structures in FGD
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Ellis, Peter F. "Unusual Failures of Corrosion-Resistant Alloys in Flue Gas Desulfurization (FGD) Service." In CORROSION 1993. NACE International, 1993. https://doi.org/10.5006/c1993-93415.

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Abstract Corrosion resistant alloys have been used for many years to withstand the severely corrosive environments created by wet lime/limestone flue gas desulfurization (FGD) systems. While the limitations of the frequently used alloys are generally understood from experience, unusual failures continue to occur. Results of investigations of unusual failures of corrosion resistant alloys in four FGD systems are reported. These include a very unusual "pitting” and wastage of Alloy C-22 in a direct-bypass mixing zone, side-by-side severe corrosion of Alloys C-22 and C-276 in a direct-bypass mixi
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Kelley, Don H. "Pollution Control of Wet Flue Gas Desulfurization (FGD) Environments with Fiberglass-Reinforced Plastic (FRP) Equipment." In CORROSION 1994. NACE International, 1994. https://doi.org/10.5006/c1994-94417.

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Abstract Due to its corrosion resistance to wet FGD environments, high nickel alloy clad/wallpaper steel was the structural material of choice for Phase I wet FGD systems. Electric companies were willing to pay a premium for high nickel alloy clad/wallpaper steel because they believed it would last the life of the plant with minimal maintenance. An excellent material for wet FGD service at approximately half the cost of high nickel clad/wallpaper steel, is fiberglass-reinforced plastic (FRP) based on epoxy vinyl ester resin. With case histories dating back to 1972, FRP has become the material
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Tossey, Brett M., John Shingledecker, and Arun Agrawal. "Effect of Post-weld Cleanup Method on the Localized Corrosion Resistance of Duplex Stainless Steels." In CORROSION 2014. NACE International, 2014. https://doi.org/10.5006/c2014-4384.

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Abstract Recent experience with duplex stainless steels in wet flue gas desulfurization service has shown rapid localized attack in some cases. This paper discusses field observations, laboratory results, and a brief historical perspective on the corrosion phenomena. Early observations of attacked wet flue gas desulfurization absorbers showed pitting and crevice corrosion near welds in the immersion zone and inside spray headers. The post weld cleanup methods that were used were not consistent from plant to plant, offering a variety of data to analyze. Some of the common methods were wire brus
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Caudill, Dan L., and Gerhardus H. Koch. "Corrosion of Carbon Steel Substrate under Alloy C-276 Wallpaper." In CORROSION 1996. NACE International, 1996. https://doi.org/10.5006/c1996-96450.

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Abstract Flue gas desulfurization (FGD) systems or wet scrubbers are essentially chemical plants, which are used to reduce sulfur dioxide (SO2) emissions from coal fired power plants. The most common process involves wet limestone scrubbing. The scrubbed flue gas is discharged from the scrubber modules into an outlet duct that leads into the stack. The scrubbed flue gas enters the outlet duct at its adiabatic saturation temperature and, as a result, a considerable amount of condensation occurs on the duct walls. The condensate usually contains various mineral acids and many dissolved ions, whi
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Reports on the topic "Wet flue gas desulfurization (WFGD)"

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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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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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G. Blythe, S. Miller, C. Richardson, and K. Searcy. ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS--SITE 2 RESULTS. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/829670.

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G. Blythe, S. Miller, C. Richardson, and K. Searcy. ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS--SITE 2 RESULTS. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/829671.

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Unknown. ENHANCED CONTROL OF MERCURY BY WET FLUE GAS DESULFURIZATION SYSTEMS - SITE 1 RESULTS. Office of Scientific and Technical Information (OSTI), 1999. http://dx.doi.org/10.2172/761130.

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Kost, D. A., J. P. Vimmerstedt, and R. C. Stehouwer. Reclamation of acid, toxic coal spoils using wet flue gas desulfurization by-product, fly ash and sewage sludge. Final report. Office of Scientific and Technical Information (OSTI), 1997. http://dx.doi.org/10.2172/663438.

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