Abstract

A coupled anaerobic-aerobic granular bio-film reactor was employed with two operation stages: Stage I, granular sludge was formed from digestion sludge using brewery wastewater, and Stage II, granular sludge was acclimatized using coking wastewater. Two oxygenation methods (i.e. A and B) were employed to acclimatize the granules. For method A, dissolved O 2 was supplied through a continuous oxygenation way of 800-15000ml-min-1 . And for method B, dissolved O2 was supplied of 800-15000ml-min-1 18-12 times at 20-60min intervals, 1h each time. The experimental results showed that granules could quickly form in 10d in the EGSB reactor seeded with digestion sludge and little loose granules lack of nutrition, and it was the key factor for granules forming to add little loose granules. It took only about 6 months for granules acclimation using coking wastewater. Both oxygenation methods could run well when acclimatizing the granules. However, method A could have comparatively high and stable operation effect. The actual coking wastewater had distinct inhibition effect on the granules, but the supplement of some oxygen could promote the recovery of SMA, and NaHCO3 supplement could also weaken the inhibition effect of the CWW. Method A had more strongly activity recovery ability than method B.

Highlights

  • The A2/O biological treatment system is frequently used in order to treat coking wastewater for the toxic organic compounds and NH3-N removal

  • The 2.3m height EGSB reactor was an acrylic column with a conical-shaped bottom, a working volume of 12L, an internal diameter of 10cm The wastewater used as influent to the reactor was obtained one from synthetic wastewater using sucrose, beer and sodium acetate as the carbon source and NH4Cl, KH2PO4, Na2S·9H2O, FeCl2·4H2O, CoCl2·6H2O, NiCl2·6H2O as nutrients, and the other from the actual coking wastewater collected from the buffer tank of the first coking plant of Taiyuan Coal Gas and Chemical Stock Co., LTD. located in Shan'xi Province, North China with 818-978mg.L-1 COD, 12.8-49.3mg.L-1 phenol, 1.8257.8mg.L-1 CN, 66.7-154.7mg.L-1 showed the variation of influent thiocyanate (SCN) and 6.5-8.1 pH

  • The ammonia removal efficiency variations for the reactor A (RA) and reactor B (RB) were presented in Fig.3 and Fig

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Summary

Introduction

The A2/O biological treatment system is frequently used in order to treat coking wastewater for the toxic organic compounds and NH3-N removal. There are problems which are inherent to an anaerobic/aerobic treatment sequence (such as the A2/O system) since the anaerobic transformation of toxic organic compounds is often incomplete[1,2,3,4]. Faculative bacteria have been shown to be predominant in the peripheral layer while the methanogens are preferentially biodegradation of the recalcitrant xenobiotic compounds and in the simultaneous removal of toxic organic compounds and NH3-N in the coking wastewater. Integration of EGSB for the toxic organic pollutants removal and NH3-N removal will be a powerful alternative for coking wastewater treatment

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