Academic literature on the topic 'Flue gas treatment'

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Journal articles on the topic "Flue gas treatment"

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Zhao, Junyou, Chongning Liu, Yafei Dong, Qingqiang He, Fawei Wan, Thibaud Friedrich, Xiaodong Bi, and Yamin Tian. "Flue gas fine treatment by ejecting technology." Proceedings of the Institution of Mechanical Engineers, Part C: Journal of Mechanical Engineering Science 233, no. 12 (November 25, 2018): 4311–18. http://dx.doi.org/10.1177/0954406218813395.

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PM2.5 refers to fine particles with a diameter of 2.5 µm or less in the air. With PM2.5 continuously impacting people's lives, researchers are starting to pay more attention on the treatment of flue gas emitted from coal-fired boilers. This paper introduces a treatment device for ejected fine flue gas. The device uses ejectors to effectively remove acid substances and large dust particles contained in flue gas, and uses air dynamic ultrasonic atomizer to eliminate micro dust particles effectively. The overall scheme of the flue gas processing device is designed, the principle and simulation results of the main components of the ejector are studied, and the optimal value of the ejector ratio is determined by experiments. Finally, the efficiency of processing dust and sulfur dioxide in the flue gas is tested during experiments on the industrial worksite. For the gas emissions from domestic small- and medium-sized coal-fired boilers, this device is more efficient and costs less energy.
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AOKI, Shinji. "Electron-beam flue gas treatment." Journal of the Fuel Society of Japan 69, no. 3 (1990): 165–71. http://dx.doi.org/10.3775/jie.69.165.

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Kano, Y., Y. Kawashima, and T. Hayasaka. "Catalyst for flue gas treatment." Zeolites 15, no. 8 (November 1995): 756. http://dx.doi.org/10.1016/0144-2449(95)96857-w.

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Yin, Mei Yao, Xiao Juan Zhao, Chen Guang Li, Hong Da Cui, and Juan Wang. "Treatment, Electricity Harvesting and Sulfur Recovery from Flue Gas Pre-Treatment Wastewater Using Microbial Fuel Cells with Sulfate Reduction Bacterial." Advanced Materials Research 1073-1076 (December 2014): 920–23. http://dx.doi.org/10.4028/www.scientific.net/amr.1073-1076.920.

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Aiming at the problem of the traditional flue gas desulfurization and effluent disposal, two identical dual-chambered Microbial fuel cells (MFCs) are designed to remove man-made flue gas pre-treatment wastewater (FGPW). Glucose is used as the carbon source of the Sulfate reducing bacteria (SRB). Carbon cloth is used as the material of anodic and cathode. The treatment performance of flue gas pre-treatment wastewater and the possibility of electricity harvesting and sulfur recovery were investigated. The results show that the output voltage is 0.68-0.72V and the maximum current density is 28.12mA/m2 at pH=7.520. The concentration of sulfate measured with ion chromatography is decreased gradually during the operation of MFC. The elemental sulfur is found in carbon cloth (taken from the MFC after working for 58 days) by analysis with XPS. The results suggest that treatment of flue gas pre-treatment wastewater and electricity harvesting and sulfur recovery by MFC is technical feasibility.
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Han, Jun Shu, Li Hua Wu, and Zheng Wang. "Research on Flue Gas Emission Control Technology of Vehicular Pyrolysis Treatment Equipment for Medical Waste." Advanced Materials Research 1010-1012 (August 2014): 973–78. http://dx.doi.org/10.4028/www.scientific.net/amr.1010-1012.973.

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This Thesis introduces the principle and structure of vehicular pyrolysis treatment furnace for medical waste and analyzes two flue gas purification structures of direct purification and coil purification and the effects, existing problems and forming reasons of flue gas emission of aftertreatment underwater aeration quenching structure; purification structure and quenching structure designed based on 3T control theory can control flue gas emission quality effectively and greatly reduce the influence on the environment due to the secondary synthesis of Dioxin and these structures have met national safety and emission standards; flue gas emission technology is a key technology for miniaturization and light-weight trend of pyrolysis treatment equipment for medical waste and a significant technological base for development of pyrolysis treatment car for medical waste.
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Kikuchi, Ryunosuke. "Factors Influencing SO2 Removal Efficiency by Electron Beam Processing of Coal-Fired Flue Gas Treatment." Energy & Environment 9, no. 5 (August 1998): 535–47. http://dx.doi.org/10.1177/0958305x9800900506.

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A bench-scale test (800 Nm3/h) for electron beam treatment of flue gas was conducted. It was concluded that the method is favourable for treatment of flue gas with a high SO2 concentration (5,500 ppm) at low electron beam irradiation (5 kGy). Results are consistent with the claim that SOx is removed from flue gas by the reaction of SOx with ammonia, and the intermediate salts formed are oxidised by radicals to sulphate salts consisting mainly of ammonium sulphate (a N-fertiliser). A typical flue gas desulphurization (FGD) method such as the wet limestone process cannot remove NOx and SO3 effectively (Ando, 1990), but the electron beam process removes SO2, SO3 and NOx simultaneously without generating waste water and CO2.
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Aoki, Sinji, and Ryoji Szuki. "Electron-Beam Flue-Gas Treatment System." IEEJ Transactions on Fundamentals and Materials 114, no. 5 (1994): 349–55. http://dx.doi.org/10.1541/ieejfms1990.114.5_349.

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Selivanovs, Jevgenijs, Edgars Vigants, Vivita Priedniece, Ivars Veidenbergs, and Dagnija Blumberga. "Flue gas treatment multi-criteria analysis." Energy Procedia 128 (September 2017): 379–85. http://dx.doi.org/10.1016/j.egypro.2017.09.056.

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Sayari, Abdelhamid, Youssef Belmabkhout, and Rodrigo Serna-Guerrero. "Flue gas treatment via CO2 adsorption." Chemical Engineering Journal 171, no. 3 (July 2011): 760–74. http://dx.doi.org/10.1016/j.cej.2011.02.007.

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Liu, Xiaoyu, Bing Yang, and RuoZheng Li. "Flue Gas Treatment of Desulphurization Wastewater." IOP Conference Series: Earth and Environmental Science 634 (February 5, 2021): 012022. http://dx.doi.org/10.1088/1755-1315/634/1/012022.

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Dissertations / Theses on the topic "Flue gas treatment"

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Lindblom, Jonas, and Max Larsson. "Algal Flue Gas Sequestration and Wastewater Treatment : An Industrial Experiment." Thesis, KTH, Industriell ekologi, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-32146.

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CJP Solutions och Waste Handling and Management (WHAM) är två företag i Melbourne, Australien, som utvecklar en process för återvinning av bioslam från Melbourne Waters reningsverk. Slammet är förorenat med metaller från industriellt avloppsvatten som har behandlats tillsammans med det kommunala avloppsvattnet. Företagen sökte en hållbar biologisk process inkluderande alger för att rena och fånga in rökgaser från pyrolisering och förbränning av det förorenade slammet. I det här examensarbetet har en teknisk lösning utformats, tillverkats och experimentellt prövats på plats under tjugo veckor i Melbourne, med mål att: mäta gas- och vattenreningsprestanda. Efter åtta veckors inledande litteraturstudie omfattande koldioxidinfångst samt algbiologi med industriell tillämpning fattades beslut om att i första hand använda mikroalgen Chlorella vulgaris, för dess robusta egenskaper samt potential för snabb tillväxt. Utöver Chlorella v. odlades en blandning lokala algkulturer tillsammans med Chlorella v. fram, och prövades parallellt vid de efterföljande experimenten. Experimenten utfördes under tre veckor vid energiföretaget AGLs biogasdrivna kraftvärmeverk, på Melbourne Waters Western Treatment Plant. I experimentet leddes orenade rökgaser genom ett system för kylning, filtrering och kompression, till algodlingarna. Algodlingarna var utformade i två separata system, det ena bestående av sju vertikala 25 liters plastkolonner, det andra av en 250 liters bassängodling. Systemen blandades genom luft- och rökgasinsprutning, samt genom mekaniserad omrörning. Algerna odlades i delvis renat avloppsvatten. Val av tekniska lösningar baserades på låga omkostnader, enkel konstruktion, komponenternas tillgänglighet, samt en tre veckors tidsfrist till att utforma och tillverka systemen.
CJP Solutions in collaboration with Waste Handling and Management (WHAM), two companies based in Melbourne, Australia, are currently developing a process to treat and recycle biosolids left over from the wastewater treatment process at Melbourne Water’s Western Treatment Plant. The biosolids are contaminated with heavy metals from industrial wastewater, being treated together with municipal wastewater. The companies are looking for a sustainable solution for sequestering flue gases from pyrolysis of the biosolids, into an algal biomass. In this Master Thesis project, a technical solution has been designed, constructed and tested on site over the course of twenty weeks in Melbourne, the goal being to determine gas and water cleanup performance. After eight weeks of initial literature review covering CO 2-sequestration and industrial applications of algae cultivation, the microalgae Chlorella vulgaris was chosen as the main strain to be used, due to it being robust and having a high growth rate. In addition to the Chlorella v. culture, a mix consisting of local algae cultures together with Chlorella v. was also cultivated throughout the experiments. The experiments were carried out during three weeks at AGL’s biogas power plant, at the Western Treatment Plant. Untreated exhaust gas was led through a system of cooling, filtration, and compression, into the two separate algal culture systems. One consisted of seven 25 litre plastic column reactors, the other of a 250 litre pond reactor. The systems were mixed through air bubbling, exhaust gas inlet, as well as by a mechanical stirrer in the pond reactor. The algae were grown in partially treated wastewater. Factors determining the system design included simplicity in construction, use of cheap, available materials, as well as a three week design and construction deadline.
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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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Potreck, J. "Membranes for flue gas treatment transport behavior of water and gas in hydrophilic polymer membranes /." Enschede : University of Twente [Host], 2009. http://doc.utwente.nl/60629.

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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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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
Department of Civil Engineering
Natalie Mladenov
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-Ayuso et al., 2006). Although FGD systems have proven to reduce atmospheric emissions they create wastewater containing harmful pollutants. Constructed wetlands are increasingly being employed for the removal of these toxic trace elements from FGD wastewater. In this study the effectiveness of using a constructed wetland treatment system was explored as a possible remediation technology to treat FGD wastewater from a coal-fired power plant in Kansas. To simulate constructed wetlands, a continuous flow-through column experiment was conducted with undiluted FGD wastewater and surface sediment from a power plant in Kansas. To optimize the performance of a CWTS the following hypotheses were tested: 1) decreasing the flow rate improves the performance of the treatment wetlands due to an increase in reaction time, 2) the introduction of microbial cultures (inoculum) will increase the retention capacity of the columns since constructed wetlands improve water quality through biological process, 3) the introduction of a labile carbon source will improve the retention capacity of the columns since microorganisms require an electron donor to perform life functions such as cell maintenance and synthesis. Although the FGD wastewater collected possessed a negligible concentration of arsenic, the mobilization of arsenic has been observed in reducing sediments of wetland environments. Therefore, constructed wetlands may also represent an environment where the mobilization of arsenic is possible. This led us to test the following hypothesis: 4) Reducing environments will cause arsenic desorption and dissolution causing the mobilization of arsenic. As far as removal of the constituents of concern (arsenic, selenium, nitrate, and sulfate) in the column experiments, only sulfate removal increased as a result of decreasing the flow rate by half (1/2Q). In addition, sulfate-S exhibited greater removal as a result of adding organic carbon to the FGD solution when compared to the control (at 1/2Q). Moderate selenium removal was observed; over 60% of selenium in the influent was found to accumulate in the soil. By contrast, arsenic concentrations increased in the effluent of the 1/2Q columns, most likely by dissolution and release of sorbed arsenic. When compared to the control (at 1/2Q), arsenic dissolution decreased as a result of adding inoculum to the columns. Dissolved arsenic concentrations in the effluent of columns with FGD solution amended with organic carbon reached 168 mg/L. These results suggest that native Kansas soils placed in a constructed wetland configuration and amended with labile carbon do possess an environment where the mobilization of arsenic is possible.
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Vasanthakumar, Adaikalamuthu Louis Savio. "Control of NO←x and SO←2 emission by plasma treatment." Thesis, Imperial College London, 1995. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.362946.

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Eggert, Derek Anderson. "Constructed wetland treatment system an approach for mitigating risks of flue gas desulfurization waters /." Connect to this title online, 2009. http://etd.lib.clemson.edu/documents/1249066367/.

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Talley, Mary Katherine. "Analysis of a pilot-scale constructed wetland treatment system for flue gas desulfurization wastewater." Thesis, Kansas State University, 2012. http://hdl.handle.net/2097/15070.

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Master of Science
Department of Biological and Agricultural Engineering
Stacy L. Hutchinson
Coal-fired generation accounts for 45% of the United States electricity and generates harmful emissions, such as sulfur dioxide. With the implementation of Flue Gas Desulfurization (FGD) systems, sulfur dioxide is removed as an air pollutant and becomes a water pollutant. Basic physical/chemical wastewater treatment can be used to treat FGD wastewater, but increased regulations of effluent water quality have created a need for better, more economical wastewater treatment systems, such as constructed wetlands. At Jeffrey Energy Center, north of St. Mary’s, KS, a pilot-scale constructed wetland treatment system (CWTS) was implemented to treat FGD wastewater before releasing the effluent into the Kansas River. The objectives of this study were to 1.) determine if a portable water quality meter could be used to assess water quality and track pollutant concentrations, 2.) develop a water balance of the CTWS, 3.) generate a water use coefficient for the CWTS, and 4.) create a mass balance on the pollutants of concern. Water quality measurements were taken with a HORIBA U-50 Series Multi Water Quality Checker and compared to analytical water tests provided by Continental Analytic Services, Inc. (CAS) (Salina, KS). The water balance was created by comparing inflows and outflows of data determined through flow meters and a Vantage Pro2™ weather station. Information from the on-site weather station was also used to compute the system water use coefficient. Water sampling was conducted from date to date at 10 locations within the CWTS. In general, there was little to no relationship between the HORIBA water quality measurements and the analytical water tests. Therefore, it was recommended that JEC continue to send water samples on a regular basis to an analytical testing laboratory to assess the CWTS function and track pollutants of concern. Because the water balance was conducted during system initiation, there was a great deal of fluctuation due to problems with the pumping system, issues with the upstream FGD treatment system, extreme weather events, and immature vegetation. This fluctuation resulted in the system having a non-steady state operation, which weakened the ability to calculate a system water use coefficient. However, during periods of strong system function, the water use coefficient was similar to previous studies with maximum water use being approximately equal to the reference evapotranspiration. The results of the mass balance indicated high removals mercury, selenium, and fluoride, but low removals of boron, manganese, chloride, and sulfate were exported from the CWTS.
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Sundberg, Joacim. "Simulating MPC Controlled Lime Injection for the Flue-gas Treatment at Fortum's Thermal Power Plant." Thesis, KTH, Reglerteknik, 2015. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-168248.

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The aim of this thesis is to investigate the possibility to improve the separation of HCl and SO2 in the dry ue-gas treatment for boiler #3 at Fortum's thermal power plant in Hogdalen; by using a model predictive control instead of a PID controller to govern the slaked lime injection. To achieve this an ARMAX model was derived using MATLAB's System Identi cation Toolbox and measurements of the incoming and outgoing levels of HCl, SO2 and the speed of the injection motor. The ARMAX model was then converted to a state space model which will be used as the internal model for the MPC predictions. The cost function was a quadratic problem which included the error between the output and the set points, the change rate of the input and the inputs deviation from a default value. The MPC uses both a feedforward and a feedback loop to estimate the error over the prediction horizon. The controller also utilizes the ability to set constraints and tuning of the cost function weights. In conclusion, the thesis shows that a MPC controlled lime injection is possible and would o er some unique possibilities such as: natural constraints handling, more intuitive live tuning for the operator and prioritized input control. However the dry scrubber still struggles to suppress high amounts of incoming SO2 and since the project lacked a measuring unit for incoming HCl concentration the results showing an improvements in pollution separation was not conclusive.
Under 2011 utförde Fortum en ombyggnation av Panna 3 för att oka energiproduktionen vid Högdalens värmeverk. Detta ledde till ett okat rökgasflöde genom pannans rökgasrening och Fortum har sedan ombyggnationen noterat en försämrad separation av väteklorid (HCl) och svaveldioxid (SO2) i den torra rökgasreningen. I den torra rökgasreningen (torr skrubber) tillsatts släckt kalk till rökgaskanalen som sedan reagerar med HCl och SO2. Reaktionen mellan kalk och HCl/SO2 skapar ett fast ämne som kan filtreras med ett filter. Detta projekt har undersökt möjligheten att förbättra separationen av HCl och SO2 i den torr skrubbern genom att använda en prediktive regulator för att styra kalkinmatningen istället för en PID regulator. Projektet inleddes med att skapa en matematisk modell som beskriver sambandet mellan inkommande HCl, SO2 och kalk och utgående HCl och SO2. För att åstadkomma detta så mättes indata och utdata för att sedan användas i MATLAB's System Identification Toolbox som sedan skapade en ARMAX (Autoregressive Moving Average Extra signal) modell. Denna modell konverterades sedan till en tillståndsmodell för att bättre passa ändamålet som en intern modell i MPC regulatorn. Nästa steg var att sätta ihop själva regulatorn som styr hastigheten av de motorer som matar in kalk i rökgaskanalen i MATLAB Simulink. Denna regulator har till uppgift att hitta den optimala förändringen av motorhastigheten som gör så att utsignalen håller sig på en önskad referensnivå. Detta utförs genom att ställa upp en så kallad kostnadsfunktion som associerar en fiktiv kostnad till att avvika från referensnivån, att föreslå en stor ändring av motorhastigheten eller att avvika från en önskad motorhastighet. Kostnadsfunktionen ar formulerad som kvadratisk problem som MPC regulatorn försöker lösa för att hitta den optimala insignalen till systemet. Med andra ord så försöker regulatorn att hitta den minsta andringen av motorhastigheten som bidrar till den minsta avvikelsen från önskad motorhastighet och minsta avvikelsen mellan utsignal och referensnivå _a. Den framtagna regulatorn använder sig av både framkoppling och återkoppling för att estimera summan av de nuvarande och förväntade avvikelsen mellan utsignal och referensnivå. Regulatorn använder sig också av restriktioner som begränsar hastigheten på motorn och hur snabbt regulatorn kan andra den tidigare motorhastigheten. Detta betyder att regulatorn kommer endast att föreslå en förändring av hastigheten som ligger inom systemets restriktioner. Denna rapport kommer i jämförelsesyfte också att presentera en simulation av den existerande PID regulatorn. Resultaten från denna rapport kommer att innehålla den framtagna tillståndsmodellen, en skiss over den implementerade MPC regulatorn, den kod som utför själva optimeringen samt diagram från simuleringar av MPC och PID regulatorerna. I dessa resultat visade det sig att MPC regulatorn lyckas _åstadkomma marginellt bättre kontroll over utgående SO2 samt en mer exakt kontroll av utgående HCl. Det skall dock noteras att dessa resultat ar baserade på simuleringar och kan komma att andras i en verklig implementation. Aven med små förbättringar av utsläppsvärdena så erbjuder MPC regulatorn några intressanta möjligheter. En MPC regulator kan hantera restriktioner i processen mycket mer naturligt an PID regulatorn. Den kan också justeras under drift av operatören samt prioriterat val av kontrollsignal. Med prioriterat val av kontrollsignal menas att det ar möjligt att förknippa olika kostnader till era olika kontrollsignaler i kostnadsfunktionen. Detta skulle medföra att regulatorn prioriterar en andringar av den kontrollsignal som medför den minsta kostnaden under rådande omständigheter.
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Li, Ling. "Production of a new wastewater treatment coagulant from fly ash with concomitant SO₂ removal from flue gas." [Ames, Iowa : Iowa State University], 2008.

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Books on the topic "Flue gas treatment"

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Ltd, Canviro Consultants. An evaluation of flue gas desulphurization wastewater treatment by mechanical evaporation. Kitchener, Ontario: Canviro Consultants Ltd, 1985.

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Chmielewski, Andrzej G. Dose distribution effect on optimal geometry for industrial flue gas treatment system. Warszawa: Institute of Nuclear Chemistry and Technology, 1998.

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author, Zeng Guang, ed. Fang kong "jia liu": Zhongguo nei di jia xing H1N1 liu gan ying dui ping gu = China's crisis management on H1N1 flu in 2009 : an assessment. Beijing Shi: She hui ke xue wen xian chu ban she, 2014.

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Agency, International Atomic Energy, ed. Treatment of off-gas from radioactive waste incinerators. Vienna: International Atomic Energy Agency, 1989.

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Unit, Energy Technology Support, Fichtner Consulting Engineers Ltd, and Great Britain. Department of Trade and Industry., eds. Optimisation studies of a dry lime flue gas treatment process on a municipal waste incinerator. [London]: Department of Trade and Industry, 1998.

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A, Smith Tim J., Newman C. J, Minerals, Metals and Materials Society. Pyrometallurgical Committee., and Minerals, Metals and Materials Society. Meeting, eds. Smelter process gas handling and treatment: Proceedings of an international symposium sponsored by the Pyrometallurgy Committee, held at the Annual Meeting of the Minerals, Metals and Materials Society in San Diego, California, USA, March 1-5, 1992. Warrendale, Pa: Minerals, Metals & Materials Society, 1991.

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Prevention (Firm : Emmaus, Pa.), ed. Gan mao yu liu xing xing gan mao: Jia su fu yuan de zhuan jia jian yi = The doctors book of home remedies for colds and flu. Taibei Shi: Yuan liu chu ban shi ye gu fen you xian gong si, 2002.

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Book chapters on the topic "Flue gas treatment"

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Grohmann, A. N., L. Bauch, and H. P. Scheerer. "Chemical Treatment of Flue Gas Washing Liquids." In Pretreatment in Chemical Water and Wastewater Treatment, 227–36. Berlin, Heidelberg: Springer Berlin Heidelberg, 1988. http://dx.doi.org/10.1007/978-3-642-73819-7_18.

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Breault, Ronald W., Chris McLarnon, and V. K. Mathur. "Reaction Kinetics for Flue Gas Treatment of NOx." In Non-Thermal Plasma Techniques for Pollution Control, 239–56. Berlin, Heidelberg: Springer Berlin Heidelberg, 1993. http://dx.doi.org/10.1007/978-3-642-78476-7_19.

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Gupta, Satyam, Neeraj Koshta, Raghvendra Singh, and Goutam Deo. "Flue Gas Treatment via Dry Reforming of Methane." In Catalysis for Clean Energy and Environmental Sustainability, 319–51. Cham: Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-65021-6_9.

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Prabakaran, Pandian, Pradeepa Virumandi, Sundaram Ravikumar, Nagasundaram Rashiya, Nagarajan Padmini, and Gopal Selvakumar. "Use of Flue Gas as a Carbon Source for Algal Cultivation." In Emerging Treatment Technologies for Waste Management, 225–57. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-2015-7_11.

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Drummond, Charles J., and Douglas F. Gyorke. "Research Strategy for the Development of Flue Gas Treatment Technology." In ACS Symposium Series, 146–58. Washington, DC: American Chemical Society, 1986. http://dx.doi.org/10.1021/bk-1986-0319.ch013.

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Dineshbabu, Gnanasekaran, Durairaj Vijayan, Vaithiyalingam Shanmugasundaram Uma, Bidhu Bhusan Makut, and Debasish Das. "Microalgal Systems for Integrated Carbon Sequestration from Flue Gas and Wastewater Treatment." In Application of Microalgae in Wastewater Treatment, 339–70. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-13909-4_15.

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Le Gleau, F., S. Caillat, E. Perdrix, L. Gasnot, D. Gambier, and J.-F. Pauwels. "Comparative Study of Flue Gas Dry Desulphurization and SCR Systems in an Industrial Hazardous Waste Incinerator." In Thermochemical Waste Treatment, 3–14. Toronto; Waretown, New Jersey : Apple Academic Press, 2016. |: Apple Academic Press, 2017. http://dx.doi.org/10.1201/b19983-3.

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Maezawa, A., and M. Izutsu. "Application of E-Beam Treatment to Flue Gas Cleanup in Japan." In Non-Thermal Plasma Techniques for Pollution Control, 47–54. Berlin, Heidelberg: Springer Berlin Heidelberg, 1993. http://dx.doi.org/10.1007/978-3-642-78476-7_4.

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Neumann, Ulrich. "Treatment of industrial emissions and waste “Flue gas treatment according to the BF/UHDE process”." In Environmental Technology, 182–93. Dordrecht: Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3663-8_23.

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Gambin, Amandine, and Xavier Pettiau. "Flue Gas Treatment in the Glass Industry: Dry Process and Calcium-Based Sorbents." In 71st Conference on Glass Problems, 225–33. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2011. http://dx.doi.org/10.1002/9781118095348.ch20.

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Conference papers on the topic "Flue gas treatment"

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Mesyats, Gennady A., Yuri N. Novoselov, and D. L. Kuznetsov. "Pulsed electron beams for flue-gas treatment." In Photonics West '95, edited by Randy D. Curry. SPIE, 1995. http://dx.doi.org/10.1117/12.205002.

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ZACH, BOLESLAV, MICHAEL POHOŘELÝ, MICHAL ŠYC, KAREL SVOBODA, ŠÁRKA VÁCLAVKOVÁ, JAROSLAV MOŠKO, JIŘÍ BRYNDA, and MIROSLAV PUNČOCHÁŘ. "LIMITATIONS OF DRY FLUE GAS TREATMENT BY SODIUM BICARBONATE: THE INFLUENCE OF FLUE GAS COMPOSITION." In AIR POLLUTION 2018. Southampton UK: WIT Press, 2018. http://dx.doi.org/10.2495/air180551.

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Pakzadeh, Behrang, Jay Wos, and Jay Renew. "Flue Gas Desulfurization Wastewater Treatment for Coal-Fired Power Industry." In ASME 2014 Power Conference. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/power2014-32278.

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The United States Environmental Protection Agency (USEPA)’s announcement that it will revise the effluent limitation guidelines for steam electric power generating units could affect not only how power plants use water, but also how they discharge it. The revised guidelines may lower discharge limits for various contaminants in flue gas desulfurization (FGD) wastewater including mercury, selenium, arsenic, and nitrate/nitrite. Although the specific details of the guidelines are unknown at present, the power industry is evaluating various technologies that may address the new effluent limitation guidelines and promote water conservation. Moreover, the power industry is looking for avenues to increase water usage efficiency, reuse and recycle throughout its plant processes. Final rule approval is expected by the middle of 2014 and new regulations are expected to be implemented between 2017 and 2022 through 5-year NPDES permit cycles. discharge limits for various contaminants including arsenic, mercury, selenium, and nitrate/nitrite [1]. These pollutant limits may be below the levels achievable today with conventional treatment [2]. A growing interest exists in zero liquid discharge (ZLD) facilities and processes in power plant operations. Potentially stringent discharge limits along with water conservation and reuse efforts are two of the major drivers to achieve ZLD. Potential pollutant levels are so low that ZLD may be the best option, if not an outright requirement [1]. Thermal ZLD systems have been the subject of increased interest and discussion lately. They employ evaporating processes such as ponds, evaporators and crystallizers, or spray dryers to produce a reusable water stream and a solid residue (i.e. waste). Evaporators and crystallizers have been employed in the power industry for a number of years. However, typical A growing interest exists in zero liquid discharge (ZLD) facilities and processes in power plant operations. Potentially stringent discharge limits along with water conservation and reuse efforts are two of the major drivers to achieve ZLD. Potential pollutant levels are so low that ZLD may be the best option, if not an outright requirement. A key disadvantage of thermal ZLD is its high capital cost. One way to reduce this cost is to pre-treat the liquid stream using innovative membrane technologies and reverse osmosis (RO).
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Chmielewski, Andrzej G. "Industrial Plant for Flue Gas Treatment with High Power Electron Accelerators." In APPLICATION OF ACCELERATORS IN RESEARCH AND INDUSTRY: 17TH International Conference on the Application of Accelerators in Research and Industry. AIP, 2003. http://dx.doi.org/10.1063/1.1619848.

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Tang, Chunli, Jianbo Li, Qingwen Qi, Chang’an Wang, and Defu Che. "Optimization Design and Thermal Economy Analysis of the Flue Gas Treatment System in Power Plant." In ASME 2015 Power Conference collocated with the ASME 2015 9th International Conference on Energy Sustainability, 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/power2015-49302.

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A novel flue gas treatment system was proposed in this paper. The system integrates the low pressure economizer (LPE) with the desulphurized flue gas heater (DFGH) for both waste heat recovery of the exhaust gas and the desulphurized flue gas heating. A model for the system was established based on the equivalent enthalpy drop theory. The thermal economic comparisons among 5 feasible connection schemes for the flue gas treatment system of a 300 MW unit were executed. The parametric analyses were also performed to evaluate the effects of the outlet flue gas temperature and the condensate temperature of the DFGH. Results indicate that the optimized flue gas treatment system can improve the thermal economy and heat the desulphurized flue gas. Better thermal economy is achieved when the LPE is connected with the high energy level feed water heater, and the low pressure extraction steam is extracted for heating desulphurized flue gas. The thermal economy decreases with the increase of the outlet flue gas temperature of the DFGH while it increases slightly with the decrease of the condensate temperature of the DFGH.
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Gao, Xudong, Baomin Sun, Shuie Yin, Yun Liu, Peishuo Bai, and Lei Wang. "Effect of NO Concentration on Effectiveness of Barrier Discharge Treatment Flue Gas Pollutants." In 2010 Asia-Pacific Power and Energy Engineering Conference. IEEE, 2010. http://dx.doi.org/10.1109/appeec.2010.5448820.

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YOSHIKAWA, MASA-AKI, AKINORI YASUTAKE, and ISAO MOCHIDA. "ADVANCED FLUE GAS TREATMENT BY NOVEL DE-SOX TECHNOLOGY OVER ACTIVE CARBON FIBERS." In Proceedings of the Third Pacific Basin Conference. WORLD SCIENTIFIC, 2003. http://dx.doi.org/10.1142/9789812704320_0085.

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Zheng, Bowen, Xiaohai Li, Haoran Chu, Chengming Jia, Wei Xu, Lili Yang, Peiyi Wang, et al. "Improvement of the Flue Gas Cleaning System in Radioactive Waste Incineration Facilities." In 2013 21st International Conference on Nuclear Engineering. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/icone21-15773.

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Three radioactive waste incineration facilities have been built in China. The first one has been in operation for more than ten years. Some problems, such as corrosion and waste water treatment in the flue gas cleaning system, have been found in the long time operation of the first facility. According to the origin of the problems, technical process and equipment material of the flue gas cleaning system have been improved in design and been adopted by the second facilities in China. The results showed that most of the problems were resolved, and the improvement is successful.
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Qian, Huiguo, Xionghui Luo, and Jingson Chen. "Study on Heat Treatment Procedure of Aluminum Alloy Castings and Flue Gas Waste Heat Recovery Technology." In 2017 6th International Conference on Energy, Environment and Sustainable Development (ICEESD 2017). Paris, France: Atlantis Press, 2017. http://dx.doi.org/10.2991/iceesd-17.2017.163.

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Peng Xiaoqiang, Han Xiaoqiang, Zhang Jizhou, Yang Yang, Wu Junxue, and An Bin. "Study on flue gas detection and treatment technology in in-situ combustion process of heavy oil." In 2016 International Field Exploration and Development Conference (IFEDC). Institution of Engineering and Technology, 2016. http://dx.doi.org/10.1049/cp.2016.1393.

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Reports on the topic "Flue gas treatment"

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

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Author, Not Given. Design of a low-cost, compact SRF accelerator for flue gas and wastewater treatment. Office of Scientific and Technical Information (OSTI), December 2017. http://dx.doi.org/10.2172/1414583.

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Ciovati, Gianluigi, jiquan guo, Robert Rimmer, Fay Hannon, Frank Marhauser, Vashek Vylet, John Rathke, et al. Design of a low-cost, compact SRF accelerator for flue gas and wastewater treatment. Office of Scientific and Technical Information (OSTI), December 2017. http://dx.doi.org/10.2172/1414584.

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