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ENVIRONMENTAL SCIENCE AND TECHNOLOGY
2014年
5期
44-48
,共5页
陈婕%汤晓峰%汤波%杨宝明%沈怡韵
陳婕%湯曉峰%湯波%楊寶明%瀋怡韻
진첩%탕효봉%탕파%양보명%침이운
中烟废水%UASB%SBR%Fenton
中煙廢水%UASB%SBR%Fenton
중연폐수%UASB%SBR%Fenton
Tobacco wastewater%UASB%SBR%Fenton
采用UASB-SBR-Fenton法处理中烟废水,最终出水可以达到GB 8978-1996《污水综合排放标准》的二级排放标准,出水色度大大降低。结果表明:UASB反应器稳定运行时,进水COD质量浓度为8500 mg/L,出水COD质量浓度为1500 mg/L,去除率为82%;SBR反应器处理UASB的厌氧出水,进水COD质量浓度为1500 mg/L,出水COD质量浓度为255 mg/L,去除率为83%;取1 LSBR好氧出水,将出水pH值调节至3,投加2.0 g FeSO4催化剂以及10 mL质量分数为30%的双氧水(H2O2),出水COD的质量浓度由255 mg/L变为143 mg/L,去除率为44%。
採用UASB-SBR-Fenton法處理中煙廢水,最終齣水可以達到GB 8978-1996《汙水綜閤排放標準》的二級排放標準,齣水色度大大降低。結果錶明:UASB反應器穩定運行時,進水COD質量濃度為8500 mg/L,齣水COD質量濃度為1500 mg/L,去除率為82%;SBR反應器處理UASB的厭氧齣水,進水COD質量濃度為1500 mg/L,齣水COD質量濃度為255 mg/L,去除率為83%;取1 LSBR好氧齣水,將齣水pH值調節至3,投加2.0 g FeSO4催化劑以及10 mL質量分數為30%的雙氧水(H2O2),齣水COD的質量濃度由255 mg/L變為143 mg/L,去除率為44%。
채용UASB-SBR-Fenton법처리중연폐수,최종출수가이체도GB 8978-1996《오수종합배방표준》적이급배방표준,출수색도대대강저。결과표명:UASB반응기은정운행시,진수COD질량농도위8500 mg/L,출수COD질량농도위1500 mg/L,거제솔위82%;SBR반응기처리UASB적염양출수,진수COD질량농도위1500 mg/L,출수COD질량농도위255 mg/L,거제솔위83%;취1 LSBR호양출수,장출수pH치조절지3,투가2.0 g FeSO4최화제이급10 mL질량분수위30%적쌍양수(H2O2),출수COD적질량농도유255 mg/L변위143 mg/L,거제솔위44%。
Tobacco wastewater was tr eated by UASB-SBR-Fenton Method. The final effluent could reach the secondary emission standard of"sewage comprehensive discharge"(GB 8978-1996) and the color of effluent was greatly reduced. The results showed that: when the UASB reactor was in stable operation and the inlet COD concentration was 8 500 mg/L, the COD concentration of effluent was reduced to 1 500 mg/L with a removal rate of 82%; when the UASB anaerobic effluent was treated by SBR reactor with an inlet COD concentration of 1 500 mg/L, the effluent COD concentration was 255 mg/L with a removal rate of 83%; 1 L SBR aerobic effluent was taken, then the effluent pH was adjusted to 3, 2.0 g of ferrous sulfate catalyst and 10 ml (mass fraction of 30%) hydrogen peroxide were added, the effluent COD concentration could be reduced from 255 mg/L to 143 mg/L with a removal rate of 44%.