کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
680507 | 1459971 | 2014 | 9 صفحه PDF | دانلود رایگان |
• In situ formation of hydrotalcite (HT) capable of removing 41% of nitrate.
• Biological denitrification removed >70% residual nitrate from HT-treated water.
• Sodium acetate as electron donor allowed better denitrification than methanol.
• Sewage sludge readily acclimatised to denitrify high-nitrate effluent.
A sequential process using hydrotalcite precipitation and biological denitrification was evaluated for the treatment of a magnesium nitrate (Mg(NO3)2)-rich effluent (17,000 mg NO3−-N/L, 13,100 mg Mg/L) generated from an industrial nickel-mining process. The hydrotalcite precipitation removed 41% of the nitrate (7000 mg NO3−-N/L) as an interlayer anion with an approximate formula of Mg5Al2(OH)14(NO3)2·6H2O. The resultant solute chemistry was a Na–NO3–Cl type with low trace element concentrations. The partially treated effluent was continuously fed (hydraulic retention time of 24 h) into a biological fluidised bed reactor (FBR) with sodium acetate as a carbon source for 33 days (1:1 v/v dilution). The FBR enabled >70% nitrate removal and a maximal NOx (nitrate + nitrite) removal rate of 97 mg NOx-N/L h under alkaline conditions (pH 9.3). Overall, this sequential process reduced the nitrate concentration of the industrial effluent by >90% and thus represents an efficient method to treat Mg(NO3)2-rich effluents on an industrial scale.
Flow sheet of the proposed two-step sequential hydrotalcite precipitation and biological denitrification treatment for Direct Nickel effluent.Figure optionsDownload as PowerPoint slide
Journal: Bioresource Technology - Volume 172, November 2014, Pages 373–381