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Dye removal efficiency of virgin activated carbon and activated carbon regenerated with Fenton's reagent

Wybrane pełne teksty z tego czasopisma
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The effectiveness of virgin and regenerated activated carbons was established for crystal violet removed from aqueous solutions. Granular activated carbon, WDex, saturated with the dye was regenerated using classic or modified Fenton's reagent, Fe2+/H2O2 and Fe2+/Ox, respectively. The application of modified Fenton's reagent resulted in the formation of hydrogen peroxide directly in the regeneration solution. The study was conducted under static and dynamic conditions. The sorptive capacities of virgin and regenerated WDex activated carbons for crystal violet were reported to be similar (approximately 42 mg/g). The results of the dynamic sorption show that under the predetermined conditions the regenerated activated carbons were better sorbents. The amount of dynamic sorption was approx. 17.6 g/dm3. The longest breakthrough time (3970 min) and the longest saturation time (11 600 min) were observed for the carbon bed regenerated with modified Fenton's reagent.
Rocznik
Strony
5--13
Opis fizyczny
Bibliogr. 18 poz., tab., rys.
Twórcy
autor
autor
  • Kielce University of Technology, Faculty of Civil and Environmental Engineering, Department of Environmental Engineering and Protection, Tysiąclecia Państwa Polskiego 7, 25-314 Kielce, ewa.ozimina@tu.kielce.pl
Bibliografia
  • [1] FUNG P.C., POON C.S., CHU C.W., TSUI S.M., Water Sci. Technol., 2001, 44, 67.
  • [2] The technological characteristics of the textile industry in the European Union, M. Mikułka (Ed.), Ministry of the Environment, Poland, Warsaw, September 2003.
  • [3] PERKOWSKI J., BULSKA A., JÓŹWIAK W.K., Environ. Prot. Eng., 2005, 31 (2), 61.
  • [4] DĘBOWSKI M., KRZEMIENIEWSKI M., Environ. Prot. Eng. 2007, 33(1), 65.
  • [5] KUCHARSKA M., NAUMCZYK J., Environ. Prot. Eng., 2009, 35 (2), 47.
  • [6] PERKOWSKI J., SIDOR M., Ochr. Środ., 2007, 29 (1), 19.
  • [7] LANGLEY L.A., FAIRBROTHER D.H., Carbon, 2007, 45, 47.
  • [8] SANTOS V.P., PEREIRA M.F.R., FARIA P.C.C., ÓRFÃO J.J.M., J. Hazard. Mater., 2009, 162, 736.
  • [9] MOORE B.C, CANNON F.S., WESTRICK J.A., METZ D.H., SHRIVE C.A., DEMARCO J., HARTMAN D.J., Carbon, 2001, 39, 789.
  • [10] RICHARD S. HORNG R.S., TSENG I.-CHIN, J. Hazard. Mat., 2008, 154, 366.
  • [11] MARCIOCHA D., FELIS E., SURMACZ-GÓRSKA J., Env. Prot. Eng., 2007, 33 (2), 165.
  • [12] NAUMCZYK J., KUCHARSKA M., Env. Prot. Eng., 2011, 37 (3), 47.
  • [13] Gryfskand Technical data sheets (unpublished).
  • [14] DĘBOWSKI Z., HOŁOWIECKI K., Koks–Smoła–Gaz, 1970, 15, 336.
  • [15] DĘBOWSKI Z., Criteria of selection of activated carbon for water treatment, Research Reports of the Central Mining Institute No 792, Katowice 1994.
  • [16] PADEREWSKI M.L., Adsorption processes in chemical engineering, WNT, Warsaw, 1999.
  • [17] Dangerous Substances Directive 67/548/EEC of 27 June 1967 on the approximation of laws, regulations and administrative provisions relating to the classification, packaging and labelling of dangerous substances (as amended).
  • [18] BINIAK S., TRYKOWSKI G., PAKUŁA M., ŚWIĄTKOWSKI A., MALINOWSKA Z., Adsorp. Sci. Technol., 2010, 28 (6), 521.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPW8-0022-0025
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