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Usuwanie bromków i bromianów z wody w procesie wymiany anionów przez membranę jonowymienną

Treść / Zawartość
Identyfikatory
Warianty tytułu
EN
Removal of Bromides and Bromates from Water in the Anion-Exchange Process with Ion-Exchange Membrane
Języki publikacji
PL
Abstrakty
EN
Bromide ions are present both in surface and ground water and their concentration ranges from several to 800 µg/L. Bromides are not reported to be detrimental to human health but their presence in the water being disinfected is a contributing factor in the formation of harmful disinfection by-products (DBP). During water disinfection with chlorine, bromides are oxidized to hypobromous acid (HOBr), which reacts with natural organic matter (NOM) to form carcinogenic brominated trihalomethanes (BrTHM). When ozone is used in water disinfection, bromides are oxidized to hypobromite ions (OBr-/) and thereafter to bromates (BrO3-). Bromates are ions exerting a carcinogenic effect on human organisms. According to the data published by the US Environmental Protection Agency, the lifetime risk of cancer disease amounts to 10-4, for a man consuming daily 2 L of water containing 5 μg BrO3-/L. The above data prove that bromides or bromates should be removed from drinking water. Among the methods used for this purpose, coagulation (for bromide removal) and granular activated carbon adsorption or reverse osmosis (for bromate removal) provide the highest removal efficiency. We proposed Donnan dialysis with anion-exchange membrane for removal of bromides or bromates from water. In this process, an anion-exchange membrane separates two solutions: the feeding solution (with harmful anions) and the receiver (with a simple salt of a relatively high concentration). Transport of the driving anions (e.g. chlorides) from the receiver to the feeding solution induces an equivalent, oppositely directed anion flow to the receiver. In this way the harmful anions that occur in the solution being treated (bromides or bromates) are replaced with neutral ions from the receiver (i.e. chlorides). Donnan dialysis was performed in a laboratory dialytic set-up containing 20 cell pairs with anion-exchange membranes, Selemion AMV (Asahi Glass) or Neosepta ACS (Tokuyama Corp.). The working area of the membranes amounted to 0.140 m2. The feed was natural water enriched with bromide salt (500 µg Br-/L) or with bromate salt (50 µg BrO3-/L). The receiver was NaCl solution with concentration ranging from 50 to 300 mM. It was found that Donnan dialysis with the anion-exchange membrane Selemion AMV enables high removal efficiency of bromides from natural water containing 500 µg Br-/L. The efficiency of bromide removal amounts to 86% at a relatively low NaCl concentration in the receiver (100 mM). The exchange of bromide ions for chloride ions is paralleled by the exchange of associated anions: sulphates (with 76% efficiency) and bicarbonates (with 70% efficiency). Compared to the anion-exchange process with Selemion AMV, the process involving Neosepta ACS (an anion-exchange membrane of a compact surface structure) provides a higher efficiency of bromide removal that amounts to 90%. In this process, retention of the associated anions is relatively high: sulphates are exchanged for chlorides with the efficiency of 3% and bicarbonates – with the efficiency of 43%. The anion-exchange process with the membrane Selemion AMV offers complete removal of bromates from natural water (containing 50 µg BrO3-/L), when salt concentration in the receiver is low (100 mM NaCl). There is aconcomitant exchange of other anions for chloride ions: sulphates are exchanged for chlorides with the efficiency of 93% and bicarbonates – with the efficiency of 73%. The anion-exchange process also provides complete removal of bromates from natural water, when use is made of the Neosepta ACS membrane. However, the exchange of sulphate ions and bicarbonate ions for chloride ions is poor (3% efficiency and 47% efficiency, respectively). Such treatment approach may be recommended for implementation, when the concentration of anions (especially that of bicarbonates) in the water to be treated is low.
Rocznik
Strony
1260--1273
Opis fizyczny
Bibliogr. 21 poz., tab., rys.
Twórcy
  • Politechnika Wrocławska
  • Politechnika Wrocławska
autor
  • Politechnika Wrocławska
Bibliografia
  • 1. Asahi Glass Company: Selemion ion – exchange membranes. Katalog firmowy.
  • 2. Asami M., Aizawa T., Morioka T., Nishijima W., Tabata A., Magara Y.: Bromate removal during transition from new granular activated carbon (GAC) to biological activated carbon (BAC). Wat. Res., 33, 2797–2804 (1999).
  • 3. Bonacquisti T.: A drinking water utility’s perspective on bromide, bromate, and ozonation. Toxicology, 221, 145–148 (2006).
  • 4. Boyer T., Singer P.: Bench-scale testing of a magnetic ion exchange resin for removal of disinfection by-product precursors. Wat. Res., 39, 1265–1276 (2005).
  • 5. Chellam S.: Effects of nanofiltration on trihalomethane and haloacetic acid precursor removal and speciation in waters containing low concentrations of bromide ion. Environ. Sci. Technol., 34, 1813–1820 (2000).
  • 6. De Borba B., Rohrer J., Pohl Ch., Saini Ch.: Determination of trace concentrations of bromate in municipal and bottled drinking waters using a hydroxide-selective column with ion chromatography. J. Chromatogr. A, 1085, 23–32 (2005).
  • 7. Ge F., Shu H., Dai Y.: Removal of bromide by aluminium chloride coagulant in the presence of humic acid. J. Hazard. Mater., 147, 457–462 (2007).
  • 8. Huang W., Cheng Y.: Effect of characteristics of activated carbon on removal of bromate. Sep. Purif. Technol., 59, 101–107 (2008).
  • 9. Kirists M., Snoeyink V., Kruithof J.: The reduction of bromate by granular activated carbon. Wat. Res., 34, 4250–4260 (2000).
  • 10. Magazinovic R., Nicholson B., Mulcahy D., Davey D.: Bromide levels in natural waters: its relationship to levels of both chloride and total dissolved solids and the implications for water treatment. Chemosphere, 57, 329–335 (2004).
  • 11. Marhaba T., Bengraine K.: Review of strategies for minimizing bromate formation resulting from drinking water ozonation. Clean Techn. Environ. Policy, 5, 101–112 (2003).
  • 12. Merck applications: Bromate in water and drinking water. Photometric determination with 3,3’-Dimethylnaftidin and iodine.
  • 13. Myllykangas T., Nissinen T., Hirvonen A., Rantakokko P., Vartiainen T.: The evaluation of ozonation and chlorination on disinfection by-product formation for a high-bromide water. Ozone: Sci. Eng., 27, 19–26 (2005).
  • 14. Nighitingale E.: Phenomenological theory of ion solvation. Effective radii of hydrated ions. J. Phys. Chem., 63, 1381–1387 (1959).
  • 15. Peldszus S., Andrews S., Souza R., Smith F., Douglas I., Bolton J., Huck P.: Effect of medium-pressure UV irradiation on bromate concentrations in drinking water, a pilot-scale study. Wat. Res., 38, 211–217 (2004).
  • 16. Selcuk H., Vitosoglu Y., Ozaydin S., Bekbolet M.: Optimization of ozone on coagulation processes for bromate control in Istanbul drinking waters. Desalination, 176, 211–217 (2005).
  • 17. Strathmann H.: Ion-exchange membrane separation processes. Elsevier, Amsterdam, 2004.
  • 18. Tokuyama Corporation: Neosepta® – grades and properties ion-exchange membrane. Katalog firmowy.
  • 19. van der Hoek J., Rijnbende D., Lokin C., Bonne P., Loonen M., Hofman J.: Electrodialysis as an alternative for reverse osmosis in an integrated membrane system. Desalination, 117, 159–172 (1998).
  • 20. Winid B.: Możliwości zastosowania wskaźnika chlorkowo-bromkowego w badaniach genezy zasolenia i jakości wód. Rocznik Ochrona Środowiska (Annual Set the Environment Protection), 14, 898–908 (2012).
  • 21. World Health Organization: Draft Guideline for Drinking Water Quality (third ed.). Geneva, Switzerland, 2003.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-5f5d53df-5ce6-4cf3-94b6-0e923ca4359f
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