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Removal of hardness in wastewater effluent using membrane filtration

Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The effluents from urban wastewater treatment plant are characterized by high concentrations of both calcium and magnesium salts which contribute to the hardness of this particular water flux. It applies primarily to places where the distribution systems draw water from underground sources. Using hard water, for instance, in households causes the domestic wastewater to be hard as well. The hardness of wastewater is not a normative indicator. However, it is an important scientific aspect in the field of water reclamation. As part of this work, research of the reduction of the overall hardness of effluent from the selected urban wastewater treatment plant in the Upper Silesia (Poland) was commenced. After the preliminary tests it was determined that, according to the common water hardness classification, the hardness of effluent from the researched treatment plant equals the hardness of hard water (350-550 mg CaCO3/L). In order to reduce the hardness of wastewater effluent a membrane filtration, including nanofiltration and reverse osmosis, was proposed. The processes were performed comparatively with the use of composite pipe membranes of PCI Membrane System Inc. (USA). The membrane used for nanofiltration was AFC-30 and the one for reverse osmosis was AFC-80. In both cases the transmembrane pressure was 2.0 MPa, while temperature and feed linear velocity amounted to 20°C and 3.4 m/s, respectively. It was determined that after both the reverse osmosis and nanofiltration the treated wastewaters were very soft. Therefore, the use of these processes, for instance, for productive purposes, may be considered. It should also be borne in mind that the nanofiltration process was more favorable in terms of membrane effectiveness.
Rocznik
Strony
141--147
Opis fizyczny
Bibliogr. 21 poz.
Twórcy
  • Prof.; Faculty of Energy and Environmental Engineering, Institute of Water and Wastewater Engineering, Silesian University of Technology, Konarskiego 18, 44-100 Gliwice, Poland
autor
  • PhD; Faculty of Energy and Environmental Engineering, Institute of Water and Wastewater Engineering, Silesian University of Technology, Konarskiego 18, 44-100 Gliwice, Poland
Bibliografia
  • [1] Kowal, A. L., Świderska-Bróż, M. (2009). Oczyszczanie wody. Podstawy teoretyczne i technologiczne, procesy i urządzenia. (Water treatment. Theoretical and technological basics, processes and equipment). Warszawa. Wydawnictwo Naukowe PWN.
  • [2] Sahinkaya, E, Sahin, A, Yurtsever, A, Kitis, M. (2018). Concentrate minimization and water recovery enhancement using pellet precipitator in a reverse osmosis process treating textile wastewater. Journal of Environmental Management, 222, 420-427.
  • [3] Brastad, K.S., He, Z. (2013). Water softening using microbial desalination cell technology. Desalination, 309, 32-37.
  • [4] Gallup, D.L. (2007). Treatment of geothermal waters for production of industrial, agricultural or drinking water, Geothermics, 36, 473-483.
  • [5] Koo, Ch., Mohammad, A.W., Suja, F. (2011). Recycling of oleochemical wastewater for boiler feed water using reverse osmosis membranes - A case study, Desalination, 271, 178-186.
  • [6] Song, J.H., Yeon, K.H., Cho, J., Moon, S.H. (2005). Effects of the operating parameters on the reverse osmosis-electrodeionization performance in the production of high purity water, Korean Journal of Chemical Engineering, 22, 108-114.
  • [7] Zarga, Y., Ben Boubaker, H., Ghaffour, N., Elfil, H. (2013). Study of calcium carbonate and sulfate coprecipitation, Chemical Engineering Science, 96, 33-41.
  • [8] Katz, I., Dosoretz, C.G. (2008). Desalination of domestic wastewater effluents: phosphate removal as pretreatment, Desalination, 222, 230-242.
  • [9] Comstock, S.E.H., Boyer, T.H. (2014). Combined magnetic ion exchange and cation exchange for removal of DOC and hardness, Chemical Engineering Journal, 241, 366-375.
  • [10] Soleimani, M., Kaghazchi, T. (2008). Adsorption of gold ions from industrial wastewater using activated carbon derived from hard shell of apricot stones - an agricultural waste, Bioresource Technology, 99, 5374-5383.
  • [11] Baker, R.W. (2012). Membrane technology and applications, John Wiley and Sons, Hoboken, USA.
  • [12] Bergman, R. (2007). Reverse osmosis and nanofiltration, American Water Works Association, Denver, USA.
  • [13] Bodzek, M., Konieczny, K. (2005). Wykorzystanie procesów membranowych w uzdatnianiu wody. [The application of membrane processes in water treatment] Projprzem-EKO, Szubin, Polska.
  • [14] Hillis, P. (2000) Membrane technology in water and wastewater treatment, Royal Society of Chemistry, Cambridge, UK.
  • [15] Howe, K.J. (2007). Membrane treatment for drinking water and reuse applications: a compendium of peerreviewed papers, American Water Works Association, Denver, USA.
  • [16] Norman, N.L. (2008). Advanced Membrane Technology and Applications, John Wiley and Sons, Chichester, UK.
  • [17] PN-ISO 6059:1999. Jakość wody. Oznaczanie sumarycznej zawartości wapnia i magnezu. Metoda miareczkowa z EDTA. (Water quality. Determination of the total calcium and magnesium content. Titration method with EDTA).
  • [18] Dudziak, M., Kudlek, E. (2018). Obniżanie twardości odpływów z oczyszczalni ścieków komunalnych za pomocą filtracji membranowej. (Reducing the hardness of effluents from urban wastewater treatment plant by means of membrane filtration), Proceedings of ECOpole, 12, 149-156.
  • [19] Antony, A., Low, J.H., Gray, S., Childress, A.E., Le- Clech, P., Leslie, G. (2011). Scale formation and control in high pressure membrane water treatment systems: A review, Journal of Membrane Science, 383, 1-16.
  • [20] Shang, W., Sun, F., Chen, L. (2018). Nanofiltration fouling propensity caused by wastewater effluent organic matters and surface-water dissolved organic matters, Environmental Technology, 39, 1914-1925.
  • [21] Zhang, L., Wang, L., Zhang, G., Wang, X. (2009). Fouling of nanofiltration membrane by effluent organic matter: Characterization using different organic fractions in wastewater, Journal of Environmental Sciences, 21, 49-53.
Uwagi
PL
Opracowanie rekordu ze środków MNiSW, umowa Nr 461252 w ramach programu "Społeczna odpowiedzialność nauki" - moduł: Popularyzacja nauki i promocja sportu (2020).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-7cb7ce7b-bc65-4714-a604-bd64e2de49cb
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