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Treatment of highly polluted cosmetic wastewater

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Three samples of cosmetic wastewater from the production of soaps and shampoos were treated by the following processes: coagulation with sedimentation (C/S), coagulation with dissolved air flotation (C/DAF), and the Fenton process (FP). The COD values of raw wastewater samples were 13 160, 13 580 and 9410 mg O2/dm3. The anionic surfactants were 3000, 4500 and 4000 mg/dm3, for samples 1, 2, and 3, respectively. All three processes were effective in highly polluted cosmetic wastewater treatment. The most effective process was coagulation. In the case of sample 1, application of FeCl3 at pH 6.0 resulted in 88.2% of COD removal and the application of aluminum based coagulants allowed for 80.1–85.3% COD removal. In the case of samples 2 and 3, the usage of Al 1019 and Al 3010 coagulants brought about a 91.6% and 82.6% decrease in COD values, respectively. C/DAF was found to be less effective than C/S. The best results with C/DAF were obtained using Al 3010 coagulant with wastewater recirculation the COD removal efficiency amounted to 82.3, 87.3 and 78.8, respectively. The lowest COD removal efficiency was observed for FP and it was equal to 64.0 and 72.7% for samples 2 and 3, respectively.
Rocznik
Strony
25--40
Opis fizyczny
Bibliogr. 25 poz., tab., rys.
Twórcy
autor
  • Warsaw University of Technology, Faculty of Building Services, Hydro and Environmental Engineering, ul. Nowowiejska 20, 00-653 Warsaw, Poland
  • Warsaw University of Technology, Faculty of Building Services, Hydro and Environmental Engineering, ul. Nowowiejska 20, 00-653 Warsaw, Poland
autor
  • Warsaw University of Technology, Faculty of Building Services, Hydro and Environmental Engineering, ul. Nowowiejska 20, 00-653 Warsaw, Poland
Bibliografia
  • [1] BUREK M., Report on implemented solutions in the company’s wastewater treatment plant AVON Operations Polska, Sp. z o.o., Gaz, Woda, Techn. Sanit., 2008, 12, 31 (in Polish).
  • [2] REIF R., SUÁREZ S., OMIL F., LEMA J.M., Fate of pharmaceuticals and cosmetic ingredients during the operation of a MBR treating sewage, Desalination, 2008, 221, 511.
  • [3] ROSAL R., RODRIGUEZ A., PERDIGON-MELON J.A., PETRE A., GARCIA-CALVO E., GOMEZ J.M., Occurrence of emerging pollutants in urban wastewater and their removal through biological treatment followed by ozonation, Water Res., 2010, 44, 578.
  • [4] EL-GOHARY F., TAWFIK A., MAHMOUD U., Comparative study between chemical coagulation/precipitation (C/P) versus coagulation/dissolved air flotation (C/DAF) for pre-treatment of personal care products (PCPs) wastewater, Desalination, 2010, 252, 106.
  • [5] ALOUI F., KCHAOU S., SAYADI S., Physicochemical treatments of anionic surfactants wastewater. Effect on aerobic biodegradability, J. Hazard. Mater., 2009, 164, 353.
  • [6] PERDIGON-MELON J., CARBAJO J., PETRE A., ROSAL R., GARCIA-CALVO E., Coagulation-Fenton coupled treatment for ecotoxicity reduction in highly polluted industrial wastewater, J. Hazard. Mater., 2010, 181, 127.
  • [7] NAUMCZYK J., MARCINOWSKI P., BOGACKI J., WILIŃSKI P., Treatment of sewage from the cosmetic industry by means of a coagulation process, Rocz. Ochr. Śr., 2013, 15, 875 (in Polish).
  • [8] NAUMCZYK J., BOGACKI J., MARCINOWSKI P., KOWALIK P., Cosmetic wastewater treatment by coagulation and advanced oxidation processes, Environ. Technol., 2014, 35, 541.
  • [9] CARPINTEYRO-URBAN S., VACA M., TORRES L.G., Can vegetal biopolymers work as coagulant–flocculant aids in the treatment of high-load cosmetic industrial wastewaters?, Water Air Soil Poll., 2012, 223, 4925.
  • [10] BOROSKI M., RODRIGUES A.C., GARCIA J.C., SAMPAIO L.C., NOZAKI J., HIOKA N., Combined electrocoagulation and TiO2 photoassisted treatment applied to wastewater effluents from pharmaceutical and cosmetic industries, J. Hazard. Mater., 2009, 162, 448.
  • [11] BAUTISTA P., MOHEDANO A.F., GILARRANZ M.A., CASAS J., RODRIGUEZ J., Application of Fenton oxidation to cosmetic wastewaters treatment, J. Hazard. Mater., 2007, 143, 128.
  • [12] BAUTISTA P., MOHEDANO A., MENENDEZ N., CASAS J., RODRIGUEZ J.J., Catalytic wet peroxide oxidation of cosmetic wastewaters with Fe-bearing catalysts, Catal. Today, 2010, 151, 148.
  • [13] BAUTISTA P., MOHEDANO A.F., CASAS J.A., ZAZO J.A., RODRIGUEZ J.J., Oxidation of cosmetic wastewaters with H2O2 using a Fe/g-Al2O3 catalyst, Water Sci. Technol., 2010, 61, 1631.
  • [14] CARBALLA M., MANTEROLA G., LARREA L., TERNES T., OMIL F., LEMA J., Influence of ozone pre-treatment on sludge anaerobic digestion. Removal of pharmaceutical and personal care products, Chemosphere, 2007, 67, 1444.
  • [15] MARCINOWSKI P., BOGACKI J., NAUMCZYK J., Cosmetic wastewater treatment using the Fenton, photo- -Fenton and H2O2/UV processes, J. Environ. Sci. Health A., 2014, 49, 1531.
  • [16] EBRAHIEM E.E., AL-MAGHRABI M.N., MOBARKI A.R., Removal of organic pollutants from industrial wastewater by applying photo-Fenton oxidation technology, Arabian J. Chem., 2013, doi:10.1016/j.arabjc.2013.06.012.
  • [17] FRIHA I., KARRAY F., FEKI F., JLAIELL., SAYADI S., Treatment of cosmetic industry wastewater by sub-merged membrane bioreactor with consideration of microbial community dynamics, Int. Biodeter. Biodegr., 2014, 88, 125.
  • [18] MONSALVO V.M., LOPEZ J., MOHEDANO A.F., RODRIGUEZ J.J., Treatment of cosmetic wastewater by a full-scale membrane bioreactor, Environ. Sci. Pollut., 2014, 21, 12662.
  • [19] ZHANG C., NING K., GUO Y., CHEN J., LIANG C., ZHANG X., WANG R., GUO L., Cosmetic wastewater treatment by a combined anaerobic/aerobic (ABR + UBAF) biological system, Desal. Water Treat., 2013, 1, 1.
  • [20] PUYOL D., MONSALVO V.M., MOHEDANO A.F., SANZ J.L., RODRIGUEZ J.J., Cosmetic wastewater treatment by upflow anaerobic sludge blanket reactor, J. Hazard. Mater., 2011, 185, 1059.
  • [21] Brenntag, www.brenntag.pl (last access on 03.09.2015).
  • [22] Kemipol, www.kemipol.com (last access on 03.09.2015).
  • [23] KANG Y.W., HWANG K.-Y., Effects of reaction conditions on the oxidation efficiency in the Fenton process, Water Res., 2000, 34, 2786.
  • [24] CARBALLA M., OMIL F., LEMA J.M., Removal of cosmetic ingredients and pharmaceuticals in sewage primary treatment, Water Res., 2005, 39, 4790.
  • [25] GUMIŃSKA J., KŁOS M., Analysis of post-coagulation properties of flocs in terms of coagulant choice, Environ. Prot. Eng., 2012, 38 (1), 103.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-fdaba185-e681-401c-934d-d1a4720c29f7
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