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A microwave plasma potential in producer gas cleaning — preliminary results with a gas derived from a sewage sludge

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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The paper presents an attempt to evaluate the impact of coal and coal mine methane cocombustion on the physics of the heat exchange in an 140 t/h pulverized-coal boiler through an analysis of 21 combinations of the boiler operating parameters – three different boiler loads (50, 75, and 100%) and seven values of the fired gas thermal contribution (0–60%). The obtained results are the temperature distribution of flue gas and steam in the boiler characteristic points, the heat transfer coefficient values for the boiler individual elements expressing the nature of changes in the heat transfer and the change in the boiler efficiency depending on how much gas is actually fired. An increase in the amount of co-fired gas involves a temperature increase along the flue gas path. This is the effect of the reduction in the amount of heat collected by the evaporator in the furnace. For these reason, the flue gas temperature at the furnace outlet rises by 9 K on average per a 0.1 increment in the fired gas thermal contribution. The temperature rise improves the heat transfer in the boiler heat exchangers – for the first- and the secondstage superheater the improvement totals 2.8% at a 10 pp. increase in the fired gas thermal contribution. However, the rise in the flue gas temperature at the boiler outlet involves a drop in the boiler efficiency (by 0.13 pp. for a rise in the fired gas thermal contribution by 0.1).
Słowa kluczowe
Rocznik
Tom
Strony
19--39
Opis fizyczny
Bibliogr. 41 poz., rys., tab.
Twórcy
  • Wrocław University of Technology, Department of Boilers, Combustion and Energy Processes, Wybrzeże Wyspiańskiego 27, 50-370 Wrocław, Poland
autor
  • REMIX S.A., Poznańska 36, 66-200 Świebodzin, Poland
autor
  • REMIX S.A., Poznańska 36, 66-200 Świebodzin, Poland
autor
  • Wrocław University of Technology, Department of Boilers, Combustion and Energy Processes, Wybrzeże Wyspiańskiego 27, 50-370 Wrocław, Poland
Bibliografia
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  • [3] Mun T-Y., Kim J-W., Kim J-S.: Air gasification of dried sewage sludge in a two-stage gasifier: Part 1. The effects and reusability of additives on the removal of tar and hydrogen production. Int. J. Hydrogen Energ. 38(2013), 13, 5226–5234.
  • [4] Chun Y.N., Kim S.C., Yoshikawa K.: Pyrolysis gasification of dried sewage sludge in a combined screw and rotary kiln gasifier. Appl. Energ. 88(2011), 1105–1112.
  • [5] Werle S.: Gasification of a dried sewage sludge in a laboratory scale fixed bed reactor. Energy Procedia 66(2015), 253–256.
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  • [7] Arjharn W., Hinsui T., Liplap P., Raghavan G.S.V.: Evaluation of an energy production system from sewage sludge using a pilot-scale downdraft gasifier. Energ. Fuel. 27(2013), 1, 229–236.
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  • [20] Uhm H.S., Kwak H.S., HongY.C.: Carbon dioxide elimination and regeneration of resources in a microwave plasma torch. Environ. Pollut. 211(2016), 191–197.
  • [21] Nunnally T., Gutsol K., Rabinovich A, Fridman A, Gutsol A., Kemoun A.: Dissociation of CO2 in a low current gliding arc plasmatron. J. Phys. D: Appl. Phys. 44(2011), 27, 1–7.
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  • [23] Pikoń K., Czekalska Z., Stelmach S., Ścierski W.: Plasma technologies for purification of product gases from biomass gasification. Archiwum Gospodarki Odpadami i Ochrony Środowiska 12(2010), 4, 61–72 (in Polish).
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  • [25] Tao K., Ohta N., Liu G., Yoneyama Y., Wang T., Tsubaki N.: Plasma enhanced catalytic reforming of biomass tar model compound to syngas. Fuel 104(2013), 53–57.
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  • [31] Chun Y.N., Kim S.C., Yoshikawa K.: Removal characteristics of tar benzene using the externally oscillated plasma reformer. Chem. Eng. Process. 57-58(2012), 65–74.
  • [32] Eliott R.M., Nogueira M.F.M., Sobrinho A.S.S., Couto B.A.P., Maciel H.S., Lacava P.T.: Tar reforming under a microwave plasma torch. Energ. Fuel. 27(2013), 2, 1174–1181.
  • [33] Jasiński M., Dors M., Mizeraczyk J.: Production of hydrogen via methane reforming using atmospheric pressure microwave plasma. J. Power Sources 181(2008), 1, 41–45.
  • [34] Mączka T.: The concept of organic wastes plasma treatment. Tworzywa Sztuczne w Przemyśle 3(2013), 41–44 (in Polish).
  • [35] Wnukowski M.: Microwave plasma application in decomposition of toluene as a tar model compound. In: Proc. 22nd Int. Symp. Combustion Processes, Polish Jurassci Highland, 22–25 Sept. 2015.
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  • [37] Gautier M., Cressault Y., Takali S., Rohani V., Fulcheri L.: Heat and mass transfer modelling in a three-phase AC hydrogen plasma torch: Influence of radiation and very high pressure. ISPC 22 – 22nd Int. Symp. Plasma Chemistry, Antwerp, July 2015.
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  • [39] Jankowski K., Reszke E.: Recent developments in instrumentation of microwave plasma sources for optical emission and mass spectrometry: Tutorial review. J. Anal. Atom. Spectrom. 28(2013), 1196–1212.
  • [40] Rönkkönen H., Simell P., Reinikainen M., Krause O, Niemelä M.V.: Catalytic clean-up of gasification gas with precious metal catalysts – A novel catalytic reformer development. Fuel 89(2010), 11, 3272–3277.
  • [41] Prabir B.: Biomass Gasification and Pyrolysis Practical Design. Elsevier, Oxford 2010.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-09117ce6-d8a1-4ea3-bf71-76e7b979276c
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