Gotowe bibliografie tematyczne / Flue gases

Gotowa bibliografia na temat „Flue gases”

Autor: Grafiati
Data publikacji: 4 czerwca 2021
Data aktualizacji: 28 lipca 2024

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Artykuły w czasopismach na temat "Flue gases"

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Gribkov, A. M., K. M. Mirsalikhov i N. D. Chichirova. "Selection of the configuration of the cross-section of a multi-flue stacks with four inner flues of different diameters". Power engineering: research, equipment, technology 25, nr 1 (23.04.2023): 3–13. http://dx.doi.org/10.30724/1998-9903-2023-25-1-3-13.

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Despite the widespread use of single-flue stacks, due to the possibility of increasing the rise of flue gases into the atmosphere due to the close location of individual flues in a common shell and ensuring the high reliability of this shell by isolating it from flue gases, multi-flue stacks are increasingly being used. To minimize their cost, it is necessary to determine such an arrangement of flues, in which the diameter of the stack shell will be minimal.THE PURPOSE. Consider the main types of multi-flue stacks used in world practice. Obtain an analytical solution for determining the minimum possible diameter of the reinforced concrete shell of a four-flue stack with flues of different diameter.METHODS. Graphical and analytical methods using computer modeling, as well as the use of computer-aided design systems.RESULTS. An analytical solution is obtained to determine the minimum possible diameter of the reinforced concrete shell of a four-flue stack with stems of different diameters at given distances between the flues and between the flues and the containment shell as a solution to a system of algebraic and trigonometric equations. The distances between the flues and between the flues and the containment can be set to any. In this paper, a new methodology and calculation program for four-flue stacks has been developed. It is shown that the shell diameter depends on the arrangement of flues of different diameters. In the absence of space restrictions for flues, flues with the largest diameters should be placed opposite each other. The obtained method for determining the shell diameter due to more accurate design and when all specified conditions are met, allows to reduce the cost of the shell by 4–9 % compared to the current method for determining the shell diameter.
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Glazyrin, Sergey A., Mikhail G. Zhumagulov, Zhanar A. Aydimbaeva i Abay M. Dostiyarov. "Universal Installation for the integrated utilization of flue gases and wastewater from thermal power plants". E3S Web of Conferences 178 (2020): 01062. http://dx.doi.org/10.1051/e3sconf/202017801062.

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For 30 years research has been carried out on the use of wastewater from thermal power plants and industrial boilers, as well as on the use and extraction of various components from flue gases such as carbon dioxide, sulfur and nitrogen. Technological solutions were developed and implemented in various productions at various times: use of acid-forming components of flue gases for the regeneration of cation exchangers; carbon dioxide from flue gases of 99.9% purity with “food” quality; technical nitrogen of 95-99 purity from flue gases; wastewater usage to increase the degree of sulfur oxides from flue gases. The article presents a technological solution for the integrated utilization of flue gases and wastewater from a thermal power plant with high-pressure boilers burning solid fuels.
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Mihelić-Bogdanić, Alka, i Ivana Špelić. "Energy Efficiency Optimization in Polyisoprene Footwear Production". Sustainability 14, nr 17 (30.08.2022): 10799. http://dx.doi.org/10.3390/su141710799.

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The evaluation of energy efficiency improvements in polyisoprene footwear production is shown. By installing air preheater, combustion air natural gas consumption is reduced by 7%. Simultaneously, the boiler outlet flue gases’ temperature is decreased from 204 °C to 66.93 °C, providing a sound basis for both economical savings and energy efficiency improvements, as well as ecological benefits to the environment. The application of condensate heat recovery resulted in flue gases’ volume decreasing by 11.85% and a thermal pollution decrease of 91.34%. Combining air preheating by exhaust flue gases and condensate heat recovery resulted in a decrease in the flue gases’ volume by 17.97%, and in the temperature lowering to 66.93 °C. The energy consumption for a combined system on location φ=45°49′) with a collector field of 12.936 × 103 m2 was investigated. The hybrid system was calculated for four variants: (1) solarized process without flue gases’ heat recovery, (2) solarized processes with heat contend in flue gases using an air preheater, (3) solarized processes with condensate heat recovery, and (4) solarized processes with heat contend in flue gases using air preheater and condensate heat recovery. The highest fuel savings were shown in solarized processes with heat contend in flue gases using air preheater and condensate heat recovery, resulting in savings of up to 78.92%, while the flue gases’ volume decreased from 5390.95 m3FG/h to 932.12 m3FG/h.
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Ibragimov, I. I., I. М. Indrupskyi, Сh А. Garifullina, Т. F. Haliullin, I. V. Valiullin, R. R. Afljatunov i I. H. Kashapov. "Study of Changes in Reservoir Oil Properties When Interacting with Flue Gases". Oil and Gas Technologies 146, nr 3 (2023): 33–38. http://dx.doi.org/10.32935/1815-2600-2023-146-3-33-38.

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The paper presents the results of experimental studies on the effect of flue gases on the properties of oil for a reservoir in Republic of Tatarstan. A methodology has been developed for studying the volumetric properties of reservoir oil using a recombination unit with additional equipment, with no need for expensive full-featured PVT complexes. Dependencies of oil properties on the content of flue gases in the recombined sample were obtained, characterizing the flue gases dissolution process in oil during injection into reservoir.The paper presents the results of experimental studies on the effect of flue gases on the properties of oil for a reservoir in Republic of Tatarstan. A methodology has been developed for studying the volumetric properties of reservoir oil using a recombination unit with additional equipment, with no need for expensive full-featured PVT complexes. Dependencies of oil properties on the content of flue gases in the recombined sample were obtained, characterizing the flue gases dissolution process in oil during injection into reservoir.
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Gorbyleva, Y. A. "Flue Gas-Simultaneous Water and Gas (Flue Gas-SWAG) Injection for Enhancing Oil Recovery". IOP Conference Series: Earth and Environmental Science 988, nr 3 (1.02.2022): 032072. http://dx.doi.org/10.1088/1755-1315/988/3/032072.

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Abstract This paper discusses the possibility of utilization of exhaust (flue) gases by injecting them into the reservoir. Currently, injection of flue gases into the reservoir is not a widely used method for increasing oil production compared to CO2 or N2 injection. Most of technologies for injecting water-gas mixture using flue gas as a gas provide for water-alternating-gas injection. Only a few studies discuss simultaneous water-alternating-gas injection using flue gases. Moreover, there are few studies on creating a mixture of water and exhaust gases for co-injection by means of pump-ejecting systems into the reservoir. Therefore, in this work we propose a new improved diagram of the laboratory bench using exhaust (flue) gases to create a water and gas mixture for flue gas-simultaneous water and gas injection by means of pump-ejecting system.
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Garifullina, Chulpan A., Timur F. Khaliullin, Ilya M. Indrupskiy, Ilsur V. Valiullin, Albert A. Zalyatdinov, Efim A. Burlutskiy, Rauza Kh Sadreeva, Rinat R. Aflyatunov i Ildar Kh Kashapov. "Experience in research and injection of flue gases into oil fields to increase oil recovery". Georesursy 24, nr 2 (30.09.2022): 149–63. http://dx.doi.org/10.18599/grs.2022.3.13.

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Decreasing negative impact of industrial emissions to the atmosphere and prolonging fossil fuel usage period are urgent issues of fuel and energy sector. In view of this problem, injection of flue gases into oil fields to increase oil recovery may be considered as environmentally safe and economically rational way for beneficial use of greenhouse gas emissions. To effectively displace oil with flue gases it is important to consider many factors: influence of composition of the flue gases and oil, miscibility conditions, injection regimes, etc. Flue gases, a product of fuel combustion in air, can be produced as a result of oil self-ignition when air is injected into a reservoir with light oil (thermal gas method). Flue gases from natural gas, fuel oil or coal combustion in power plants or other processes that burn fossil fuels can also be used for injection into the reservoir. This paper presents an analysis of the world laboratory and industrial experience in studying efficiency of oil displacement using flue gases. Conclusions are presented about optimal criteria for implementation of this process and directions for further research.
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Zhang, L., S. X. Wang, Q. R. Wu, F. Y. Wang, C. J. Lin, L. M. Zhang, M. L. Hui i J. M. Hao. "Mercury transformation and speciation in flue gases from anthropogenic emission sources: a critical review". Atmospheric Chemistry and Physics Discussions 15, nr 22 (24.11.2015): 32889–929. http://dx.doi.org/10.5194/acpd-15-32889-2015.

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Abstract. Mercury transformation mechanisms and speciation profiles are reviewed for mercury formed in and released from flue gases of coal-fired boilers, non-ferrous metal smelters, cement plants, iron and steel plants, municipal solid waste incinerators, and biomass burning. Mercury in coal, ores and other raw materials is released to flue gases in the form of Hg0 during combustion or smelting in boilers, kilns or furnaces. Decreasing temperature from over 800 °C to below 300 °C in flue gases leaving boilers, kilns or furnaces promotes homogeneous and heterogeneous oxidation of gaseous elemental mercury (Hg0) to gaseous divalent mercury (Hg2+), with a portion of Hg2+ adsorbed onto fly ash to form particulate-bound mercury (Hgp). Halogen is the primary oxidizer for Hg0 in flue gases, and active components (e.g.,TiO2, Fe2O3, etc.) on fly ash promote heterogeneous oxidation and adsorption processes. In addition to mercury removal, mercury transformation also occurs when passing through air pollution control devices (APCDs), affecting the mercury speciation in flue gases. In coal-fired power plants, selective catalytic reduction (SCR) system promotes mercury oxidation by 34–85 %, electrostatic precipitator (ESP) and fabric filter (FF) remove over 99 % of Hgp, and wet flue gas desulfurization system (WFGD) captures 60–95 % of Hg2+. In non-ferrous metal smelters, most Hg0 is converted to Hg2+ and removed in acid plants (APs). For cement clinker production, mercury cycling and operational conditions promote heterogeneous mercury oxidation and adsorption. The mercury speciation profiles in flue gases emitted to the atmosphere are determined by transformation mechanisms and mercury removal efficiencies by various APCDs. For all the sectors reviewed in this study, Hgp accounts for less than 5 % in flue gases. In China, mercury emission has a higher fraction (66–82 % of total mercury) in flue gases from coal combustion, in contrast to a greater Hg2+ fraction (29–90 %) from non-ferrous metal smelting, cement and iron/steel production. The higher Hg2+ fractions shown here than previous estimates may imply stronger local environmental impacts than previously thought, caused by mercury emissions in East Asia. Future research should focus on determining mercury speciation in flue gases from iron and steel plants, waste incineration and biomass burning, and on elucidating the mechanisms of mercury oxidation and adsorption in flue gases.
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Zhang, Lei, Shuxiao Wang, Qingru Wu, Fengyang Wang, Che-Jen Lin, Leiming Zhang, Mulin Hui, Mei Yang, Haitao Su i Jiming Hao. "Mercury transformation and speciation in flue gases from anthropogenic emission sources: a critical review". Atmospheric Chemistry and Physics 16, nr 4 (29.02.2016): 2417–33. http://dx.doi.org/10.5194/acp-16-2417-2016.

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Abstract. Mercury transformation mechanisms and speciation profiles are reviewed for mercury formed in and released from flue gases of coal-fired boilers, non-ferrous metal smelters, cement plants, iron and steel plants, waste incinerators, biomass burning and so on. Mercury in coal, ores, and other raw materials is released to flue gases in the form of Hg0 during combustion or smelting in boilers, kilns or furnaces. Decreasing temperature from over 800 °C to below 300 °C in flue gases leaving boilers, kilns or furnaces promotes homogeneous and heterogeneous oxidation of Hg0 to gaseous divalent mercury (Hg2+), with a portion of Hg2+ adsorbed onto fly ash to form particulate-bound mercury (Hgp). Halogen is the primary oxidizer for Hg0 in flue gases, and active components (e.g., TiO2, Fe2O3, etc.) on fly ash promote heterogeneous oxidation and adsorption processes. In addition to mercury removal, mercury transformation also occurs when passing through air pollution control devices (APCDs), affecting the mercury speciation in flue gases. In coal-fired power plants, selective catalytic reduction (SCR) system promotes mercury oxidation by 34–85 %, electrostatic precipitator (ESP) and fabric filter (FF) remove over 99 % of Hgp, and wet flue gas desulfurization system (WFGD) captures 60–95 % of Hg2+. In non-ferrous metal smelters, most Hg0 is converted to Hg2+ and removed in acid plants (APs). For cement clinker production, mercury cycling and operational conditions promote heterogeneous mercury oxidation and adsorption. The mercury speciation profiles in flue gases emitted to the atmosphere are determined by transformation mechanisms and mercury removal efficiencies by various APCDs. For all the sectors reviewed in this study, Hgp accounts for less than 5 % in flue gases. In China, mercury emission has a higher Hg0 fraction (66–82 % of total mercury) in flue gases from coal combustion, in contrast to a greater Hg2+ fraction (29–90 %) from non-ferrous metal smelting, cement and iron and/or steel production. The higher Hg2+ fractions shown here than previous estimates may imply stronger local environmental impacts than previously thought, caused by mercury emissions in East Asia. Future research should focus on determining mercury speciation in flue gases from iron and steel plants, waste incineration and biomass burning, and on elucidating the mechanisms of mercury oxidation and adsorption in flue gases.
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Zhuralev, Evgenii, Dmitry Chugunkov i Galina Seyfelmlyukova. "FEATURES OF NOISE REDUCTION IN GAS PATHS OF BOILERS DURING CONDENSATION OF WATER VAPOR FROM FLUE GASES". Akustika, VOLUME 41 (2021): 217–20. http://dx.doi.org/10.36336/akustika202141217.

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An important characteristic of noise silencers, which determines the effectiveness of their use, in addition to reducing the noise level and the pressure losses they create, is the operational resource. Short-term unfavorable operating modes of boilers are possible, in which condensation of water vapor on the walls of flues through which flue gases are evacuated to the environment is possible. Condensation in the gas path leads to corrosion of the metal of the flues, as well as noise silencers. The article lists recommendations for the design of noise silencers installed in the gas paths of boilers operating under conditions of possible condensation of water vapor from flue gases. The introduced silencers of noise of gas paths of boilers which not only reduce noise highly effectively, but also allow to work in difficult operational conditions are given.
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Kryvda, V., O. Brunetkin, K. Beglov, T. Markolenko i I. Lutsenko. "Method of controlling the volume of combustion products at different boiler loads". Naukovyi Visnyk Natsionalnoho Hirnychoho Universytetu, nr 1 (29.02.2024): 100–104. http://dx.doi.org/10.33271/nvngu/2024-1/100.

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Purpose. Development of a method for controlling the volume of combustion products at different load of boiler equipment. Achieving the objective may allow controlling the flue gas temperature and, consequently, the efficiency to increase it. Methodology. Control of the flue gas volume value on the basis of determining the appropriate composition of the fuel gas mixture. Findings. The effect of flue gas temperature increase at use of fuel gases of lower calorific value and increase in ballast gases quantity is revealed. The latter can be the air used as an oxidising agent at its considerable excess. The mechanism of such an effect due to the increase in the quantity and velocity of flue gases is suggested. A parameter determining the volume of flue gases produced per unit calorific value of various fuel gases is proposed. On the basis of this parameter the method for calculating the composition of the mixture of different gases to ensure the constancy of the flue gas volume at variable load is proposed Originality. On the example of the results of verification thermal calculation the change in flue gas temperature and efficiency value is considered. The non-standard character of their change is revealed. In contrast to the case of using fuel gas of constant composition with increasing load, the temperature of flue gases remained close to constant, and the value of efficiency increased. Practical value. The obtained results indicate the possibility of controlling the flue gas temperature and boiler efficiency at a given load. This allows one, unlike the case of using fuel gas of constant composition, to increase the efficiency exactly at maximum load avoiding getting into the condensate mode at minimum load. There is a possibility to save fossil gas and, consequently, to reduce the greenhouse share in CO2 emissions.
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Rozprawy doktorskie na temat "Flue gases"

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Arthur, Lia Frieda. "Silicate sorbents for flue gas cleaning /". Digital version accessible at:, 1998. http://wwwlib.umi.com/cr/utexas/main.

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Ozturk, Bahtiyar. "Removal of acidic gases from flue gases using membrane contactors". Thesis, University of Salford, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.265396.

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

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Dennis, J. S. "The desulphurisation of flue gases using calcareous materials". Thesis, University of Cambridge, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.372626.

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Norman, Christian G. "Design of a bench scale apparatus for the evaluation of the gamma alumina flue gas desulfurizaton process". Ohio : Ohio University, 1985. http://www.ohiolink.edu/etd/view.cgi?ohiou1184071211.

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Anderson, Desmond Carl. "Chemical reactions involved in the desulphurisation of flue gases". Thesis, Queen's University Belfast, 1993. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.286829.

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Bell, Robert M. "Mass flow and temperature measurements in the flue of a woodburning appliance". Thesis, This resource online, 1985. http://scholar.lib.vt.edu/theses/available/etd-07212009-040221/.

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Evans, Jeffrey Trevor. "Adsorption of heavy metals onto flyash in waste incineration flue gases". Thesis, University of Leeds, 2004. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.414286.

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Khunsupat, Ratayakorn. "Poly(allylamine) and derivatives for co2 capture from flue gas or ultra dilute gas streams such as ambient air". Thesis, Georgia Institute of Technology, 2011. http://hdl.handle.net/1853/44909.

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Polymers rich in primary amine groups are proposed to be effective adsorbents for the reversible adsorption of CO2 from moderately dilute gas streams (10% CO2) and ultra-dilute gas streams (e.g. ambient air, 400 ppm CO2), with their performance under ultra-dilute conditions being competitive with or exceeding the state-of-the-art adsorbents based on supported poly(ethyleneimine) (PEI). The CO2 adsorption capacity (mmol CO2/g sorbent) and amine efficiency (mmol CO2/mmol amine) of linear poly(allylamine) (PAA), cross-linked poly(allylamine) prepared by post-polymerization crosslinking with epichlorohydrin (PAAEPI), and branched poly(allylamine) prepared by branching of poly(allylamine) with divinylbenzene (PAADVB) are presented here and compared with state-of-the-art adsorbents based on supported PEI, specifically branched and linear, low molecular weight PEI. Silica mesocellular foam, MCF, serves as the support material for impregnation of the amine polymers. In general, branched polymers are found to yield more effective adsorbents materials. Overall, the results of this work show that linear PAA, cross-linked PAAEPI, and branched PAADVB are promising candidates for solid adsorbents with high capacity for CO2.
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Daoudi, M. "The removal of HCl from hot gases with calcined limestone". Thesis, University of Nottingham, 1987. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.381217.

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Książki na temat "Flue gases"

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B, Naylor Theodore, red. Flue gases: Research, technology, and economics. Hauppauge, N.Y: Nova Science Publishers, 2009.

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F, Sens P., Wilkinson J. K i Commission of the European Communities. Directorate-General for Science, Research, and Development., red. Flue gas and fly ash. London: Elsevier Applied Science, 1989.

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Gao, Xiang, Chenghang Zheng, Pen-Chi Chiang i Kefa Cen. Multi-Pollutant Control for Flue Gases. Singapore: Springer Singapore, 2021. http://dx.doi.org/10.1007/978-981-16-1518-4.

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Espinosa, John M. Assessment of instrumentation and analytical techniques for high temperature in situ waste stream characterization of industrial flue gases. Idaho Falls, Idaho: EG & G Idaho, Inc., 1986.

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Santhanam, Chakra J. An evaluation of the disposal of flue gas desulfurization wastes in coal mines and the ocean: Mine disposal demonstration tests. Research Triangle Park, NC: U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1985.

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Hydro, Ontario. Report to the Lieutenant Governor in Council: Options available to meet acid gas limits and selection of preferred options. Toronto, Ont: Ontario Hydro, 1989.

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

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Mobley, J. David. Proceedings: EPA's industry briefing on the organic-acid-enhanced limestone FGD process (July 1984). Research Triangle Park, NC: U.S. Environmental Protection Agency, Air and Energy Engineering Research Laboratory, 1985.

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S, Noskov A., Chumachenko V. A i Parmon V. N, red. Kataliticheskoe obezvrezhivanie otkhodi͡ashchikh gazov promyshlennykh proizvodstv. Novosibirsk: "Nauka," Sibirskoe otd-nie, 1991.

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1957-, Gullett Brian Kent, i United States. Environmental Protection Agency, red. Sorbent/urea slurry injection for simultaneous SOb2s/NOx removal. [Washington, D.C: U.S. Environmental Protection Agency, 1992.

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Części książek na temat "Flue gases"

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Chmielewski, A. G., E. Iller, B. Tymiński, Z. Zimek i J. Licki. "Electron Flue Gases Treatment in Poland". W The Modern Problems of Electrostatics with Applications in Environment Protection, 181–97. Dordrecht: Springer Netherlands, 1999. http://dx.doi.org/10.1007/978-94-011-4447-6_15.

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Simon, J. "Boron Chemistry in Flue Gases from Borosilicate Glass Furnaces". W Ceramic Transactions Series, 387–95. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2012. http://dx.doi.org/10.1002/9781118405949.ch39.

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Klockow, D., R. D. Kaiser, J. Kossowski, K. Larjava, J. Reith i V. Siemens. "Metal Speciation in Flue Gases, Work Place Atmospheres and Precipitation". W Metal Speciation in the Environment, 409–33. Berlin, Heidelberg: Springer Berlin Heidelberg, 1990. http://dx.doi.org/10.1007/978-3-642-74206-4_22.

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Tandon, P. N., P. Ramalingam i A. Q. Malik. "Dispersion of Flue Gases from Power Plants in Brunei Darussalam". W Air Quality, 405–18. Basel: Birkhäuser Basel, 2003. http://dx.doi.org/10.1007/978-3-0348-7970-5_25.

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Gao, Hong-liang, Jijing Li, Jin-song Zhou, Zhong-yang Luo i Kefa Cen. "Experimental Study of Factors Affecting Mercury Speciation in Coal-fired Flue Gases". W Challenges of Power Engineering and Environment, 700–704. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-76694-0_131.

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Mittelbach, G. "Desulfurization of Flue Gases on the Basis of Lime or Limestone Scrubbing". W Sulphur Dioxide and Nitrogen Oxides in Industrial Waste Gases: Emission, Legislation and Abatement, 93–109. Dordrecht: Springer Netherlands, 1991. http://dx.doi.org/10.1007/978-94-011-3624-2_6.

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Fehrmann, Rasmus, K. M. Eriksen, S. B. Rasmussen i J. Winnick. "Ionic Liquids as Catalysts for Sulfuric Acid Production and Cleaning of Flue Gases". W Green Industrial Applications of Ionic Liquids, 253–62. Dordrecht: Springer Netherlands, 2003. http://dx.doi.org/10.1007/978-94-010-0127-4_14.

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Castillo, José L., i Pedro L. Garcia-Ybarra. "Transport of Particles and Vapors in Flue Gases and Deposition on Cold Surfaces". W Progress in Industrial Mathematics at ECMI 2006, 284–89. Berlin, Heidelberg: Springer Berlin Heidelberg, 2008. http://dx.doi.org/10.1007/978-3-540-71992-2_36.

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Lancia, A., D. Musmarra, F. Pepe i G. Volpicelli. "Adsorption of Mercuric Chloride Vapours from Incinerator Flue Gases on Calcium Hydroxide Particles". W Combustion Technologies for a Clean Environment, 619–31. London: CRC Press, 2022. http://dx.doi.org/10.1201/9780367810597-47.

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Oğuz, Öznur, Coşkun Yurteri i Gürdal Tuncel. "Modelling Plume Rise and Dispersion of Power Plant Flue Gases Discharged Through Cooling Towers". W Air Pollution Modeling and Its Application XVI, 583–85. Boston, MA: Springer US, 2004. http://dx.doi.org/10.1007/978-1-4419-8867-6_54.

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Streszczenia konferencji na temat "Flue gases"

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Teich, T. H. "Plasma destruction of flue gases". W IEE Colloquium Pulsed Power '97. IEE, 1997. http://dx.doi.org/10.1049/ic:19970393.

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Adámek, Karel, Jan Kolář i Pavel Peukert. "Natural outlet of flue gases". W THE APPLICATION OF EXPERIMENTAL AND NUMERICAL METHODS IN FLUID MECHANICS AND ENERGY 2016: XX. Anniversary of International Scientific Conference. AIP Publishing LLC, 2016. http://dx.doi.org/10.1063/1.4953695.

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Vytisk, T., i R. Janalik. "Experimental Determination of Flue Gases Parameters". W 2015 International Conference on Electrical, Automation and Mechanical Engineering. Paris, France: Atlantis Press, 2015. http://dx.doi.org/10.2991/eame-15.2015.69.

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Zagirov, A. "SEPARATION OF PYROLYSIS GASES". W Ecological and resource-saving technologies in science and technology. FSBE Institution of Higher Education Voronezh State University of Forestry and Technologies named after G.F. Morozov, 2022. http://dx.doi.org/10.34220/erstst2021_78-81.

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A method for separating pyrolysis gases is considered, which is carried out by separating gases into distillate and non-condensable gases. The next stage is the combustion of non-condensable gas in the furnace of a shaft-type pyrolysis apparatus, where it forms flue gas, which, moving along the jacket, transfers part of its heat to the pyrolysis process. After passing through the pyrolysis apparatus, the flue gas enters the drying chamber and participates in the wood drying process. The waste flue gas is then discharged into the atmosphere after cleaning with a liquid.
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Shikina, Nadezhda, Oleg Tailakov i Zinfer Ismagilov. "Catalysts for Nitrogen Oxides Removal from Flue Gases". W 8th Russian-Chinese Symposium "Coal in the 21st Century: Mining, Processing, Safety". Paris, France: Atlantis Press, 2016. http://dx.doi.org/10.2991/coal-16.2016.60.

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Veloso, Marco, Santi Phithakkitnukoon i Carlos Bento. "Exploring relationship between taxi volume and flue gases' concentrations". W UbiComp '13: The 2013 ACM International Joint Conference on Pervasive and Ubiquitous Computing. New York, NY, USA: ACM, 2013. http://dx.doi.org/10.1145/2494091.2497353.

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Jogekar, Dhirajkumar D., Shubham G. Mhamane i Shrikant D. Mangate. "Conversion of Electricity from Waste Heat of Flue Gases". W 2019 IEEE 5th International Conference for Convergence in Technology (I2CT). IEEE, 2019. http://dx.doi.org/10.1109/i2ct45611.2019.9033865.

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Melis, Albert, Augusto Ezequiel de Paz, Rafel González-Olmos, Jordi Pujol, Julià Sempere, Oriol Martínez i Rosa Nomen. "Development of an Economic VPSA CO2 Capture from Flue Gases". W 14th Mediterranean Congress of Chemical Engineering (MeCCE14). Grupo Pacífico, 2020. http://dx.doi.org/10.48158/mecce-14.dg.06.12.

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Zavorin, A. S., S. A. Khaustov i N. A. Zaharushkin. "Recirculation vortices of flue gases in fire-tube boiler furnace". W 2014 International Conference on Mechanical Engineering, Automation and Control Systems (MEACS). IEEE, 2014. http://dx.doi.org/10.1109/meacs.2014.6986908.

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Carapellucci, Roberto, Roberto Cipollone i Davide Di Battista. "MCFC-Based System for Active CO2 Capture From Flue Gases". W ASME 2018 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/imece2018-86881.

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Carbon dioxide emissions reduction in the atmosphere is the major driver of technological innovations, in particular in energy and industrial sectors. Those sectors are dominated by the use of fossil fuels whose main concern on the combustion gases is the presence of CO2. Their emission in atmosphere accumulates Carbon, the main cause of global warming. The only way to continue to make reference to fossil fuel in the medium-long term and to avoid the carbon accumulation in the atmosphere is to use technologies capable to capture and sequester the carbon in the flue gases (CCS). In the sector of electricity production, several technologies have been proposed for the capture CO2, including absorption, adsorption, cryogenic distillation or membrane separation. All of them offer flexibility and easiness of application, but they need external energy to operate. On the other hand, particular interest is reversed to those technological options that are able to remove CO2 without energy consumption; even more attention is reserved to those technologies which, suitably integrated with other conversion systems, can produce electrical energy at the same time, so increasing the electricity production with respect to the original plant. They are defined active systems and one of these is represented by Molten Carbonate Fuel Cells (MCFCs). In fact, MCFCs are fuel cell capable to concentrate CO2 at anode exhaust, making easier its capture, separation and storage and in parallel to contribute to the electricity production. In this paper, a comprehensive model of the MCFC is used to assess the opportunity related to its use as a CO2 remover from a flue gas as a CCS active device, without energy penalties related to traditional carbon capture methods (MEA, pre and post-combustion, oxy-combustion, etc.). Hence, it has been integrated in a wider system with auxiliary components: compressors to overcome pressure drops, steam generator (also using heat recovered from MCFC exhausts) for fuel dilution, fresh air integration in cathode inlet section, heat exchangers for thermal management and recovery. A CO2 compression and drying section has been considered and represented as a multi-step intercooled compression. The so-defined system can be used as a plug-in device able to be coupled to flue gases with different compositions and thermodynamic operating parameters (temperature, pressure, flow rates). Finally, it has been applied to a case study (a Natural Gas Combined Cycle power plant - NGCC) and the performance of the MCFC in terms of CO2 removal capacity, electrical power generation and size have been evaluated as well the energetic and environmental impact on the reference NGCC power plant.
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Raporty organizacyjne na temat "Flue gases"

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Michael Grutzeck. SO2 REMOVAL FROM FLUE GASES USING UTILITY SYNTHESIZED ZEOLITES. Office of Scientific and Technical Information (OSTI), kwiecień 1999. http://dx.doi.org/10.2172/9040.

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MICHAEL GRUTZECK. SO2 REMOVAL FROM FLUE GASES USING UTILITY SYNTHESIZED ZEOLITES. Office of Scientific and Technical Information (OSTI), październik 1998. http://dx.doi.org/10.2172/7775.

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Grutzeck, M. SO(2) Removal from Flue Gases Using Uutility Synthesized Zeolites. Office of Scientific and Technical Information (OSTI), marzec 1997. http://dx.doi.org/10.2172/643294.

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Dennis Laudal. JV Task 125-Mercury Measurement in Combustion Flue Gases Short Course. Office of Scientific and Technical Information (OSTI), wrzesień 2008. http://dx.doi.org/10.2172/989405.

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Andrews, Rodney. SEPARATION OF CO2 FROM FLUE GASES BY CARBON-MULTIWALL CARBON NANOTUBE MEMBRANES. Office of Scientific and Technical Information (OSTI), marzec 2001. http://dx.doi.org/10.2172/788129.

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Andrews, Rodney. SEPARATION OF CO2 FROM FLUE GASES BY CARBON-MULTIWALL CARBON NANOTUBE MEMBRANES. Office of Scientific and Technical Information (OSTI), listopad 2001. http://dx.doi.org/10.2172/792162.

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Melson, G. Sulfur dioxide removal from flue gases by supported copper and iron absorbents. Office of Scientific and Technical Information (OSTI), styczeń 1988. http://dx.doi.org/10.2172/5501765.

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Smith, John H. Metallurgical evaluation of type 304 stainless steel exposed to woodburning stove flue gases. Gaithersburg, MD: National Bureau of Standards, 1985. http://dx.doi.org/10.6028/nbs.ir.85-3103.

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Morris D. Argyle. Supported, Alkali-Promoted Cobalt Oxide Catalysts for NOx Removal from Coal Combustion Flue Gases. Office of Scientific and Technical Information (OSTI), grudzień 2005. http://dx.doi.org/10.2172/913563.

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Wang, Dexin. Simultaneous Waste Heat and Water Recovery from Power Plant Flue Gases for Advanced Energy Systems. Office of Scientific and Technical Information (OSTI), grudzień 2016. http://dx.doi.org/10.2172/1347684.

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