Biological sulfate removal from acrylic fiber manufacturing wastewater using a two-stage UASB reactor
A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater.Mesophilic operation(35±0.5℃) was performed with hydraulic retention time(HRT) varied between 28 and 40 hr.Mixed liquor suspended solids(MLSS) in the reactor was maintained about 8000 mg/L.The results...
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Veröffentlicht in: | Journal of environmental sciences (China) 2012-02, Vol.24 (2), p.343-350 |
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Sprache: | eng |
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Zusammenfassung: | A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater.Mesophilic operation(35±0.5℃) was performed with hydraulic retention time(HRT) varied between 28 and 40 hr.Mixed liquor suspended solids(MLSS) in the reactor was maintained about 8000 mg/L.The results indicated that sulfate removal was enhanced with increasing the ratio of COD/SO24-.At low COD/SO42-,the growth of the sulfate-reducing bacteria(SRB) was carbon-limited.The optimal sulfate removal efficiencies were 75% when the HRT was no less than 38 hr.Sulfidogenesis mainly happened in the sulfate-reducing stage,while methanogenesis in the methane-producing stage.Microbes in sulfate-reducing stage performed granulation better than that in methaneproducing stage.Higher extracellular polymeric substances(EPS) content in sulfate-reducing stage helped to adhere and connect the flocculent sludge particles together.SRB accounted for about 31% both in sulfate-reducing stage and methane-producing stage at COD/SO42-ratio of 0.5,while it dropped dramatically from 34% in sulfate-reducing stage to 10% in methane-producing stage corresponding to the COD/SO42-ratio of 4.7.SRB and MPA were predominant in sulfate-reducing stage and methane-producing stage respectively. |
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ISSN: | 1001-0742 1878-7320 |
DOI: | 10.1016/S1001-0742(11)60772-9 |