工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2015年
1期
44-47
,共4页
周安兴%方芳%杨吉祥%季新%陈猷鹏%郭劲松
週安興%方芳%楊吉祥%季新%陳猷鵬%郭勁鬆
주안흥%방방%양길상%계신%진유붕%곽경송
厌氧氨氧化%启动%SBBR%低基质
厭氧氨氧化%啟動%SBBR%低基質
염양안양화%계동%SBBR%저기질
anaerobic ammonium oxidation(anammox)%start-up%SBBR%low substrate
采用SBBR反应器,接种普通污水厂剩余污泥,以人工配制含NH4+-N和NO2--N的低氨氮废水为进水, NH4+-N、NO2--N分别为24.3~32.0 mg/L、31.9~37.5 mg/L, pH为7.60~7.75,水温为(32±1)℃,考察低基质条件下厌氧氨氧化反应器启动及稳定运行特征。结果表明:经100余天后,SBBR厌氧氨氧化反应器成功启动。进水TN为60.8~68.7 mg/L时,平均去除率为88.3%,NH4+-N和NO2--N的去除率均达到95%以上。稳定运行期间,NH4+-N去除量、NO2--N去除量和NO3--N生成量的质量浓度之比为1∶1.37∶0.27,出水pH略高于进水,稳定在7.95左右。
採用SBBR反應器,接種普通汙水廠剩餘汙泥,以人工配製含NH4+-N和NO2--N的低氨氮廢水為進水, NH4+-N、NO2--N分彆為24.3~32.0 mg/L、31.9~37.5 mg/L, pH為7.60~7.75,水溫為(32±1)℃,攷察低基質條件下厭氧氨氧化反應器啟動及穩定運行特徵。結果錶明:經100餘天後,SBBR厭氧氨氧化反應器成功啟動。進水TN為60.8~68.7 mg/L時,平均去除率為88.3%,NH4+-N和NO2--N的去除率均達到95%以上。穩定運行期間,NH4+-N去除量、NO2--N去除量和NO3--N生成量的質量濃度之比為1∶1.37∶0.27,齣水pH略高于進水,穩定在7.95左右。
채용SBBR반응기,접충보통오수엄잉여오니,이인공배제함NH4+-N화NO2--N적저안담폐수위진수, NH4+-N、NO2--N분별위24.3~32.0 mg/L、31.9~37.5 mg/L, pH위7.60~7.75,수온위(32±1)℃,고찰저기질조건하염양안양화반응기계동급은정운행특정。결과표명:경100여천후,SBBR염양안양화반응기성공계동。진수TN위60.8~68.7 mg/L시,평균거제솔위88.3%,NH4+-N화NO2--N적거제솔균체도95%이상。은정운행기간,NH4+-N거제량、NO2--N거제량화NO3--N생성량적질량농도지비위1∶1.37∶0.27,출수pH략고우진수,은정재7.95좌우。
The start-up and characteristics of stably running anaerobic ammonium oxidation (anammox) under low substrate conditions has been investigated,using SBBR and inoculated excess sludge from an ordinary sewage treatment plant,and artificially prepared low ammonia-nitrogen wastewater consisting of NH4+-N and NO2--N as influent,when the mass concentrations of NH4+-N and NO2--N are 24.3-32.0 mg/L and 31.9-37.5 mg/L,respectively, pH 7.60-7.75 and temperature of the influent (32 ±1) ℃. The results show that the SBBR can be started up successfully,after 100 days or more. And,when the mass concentration of influent TN is 60.8-68.7 mg/L,the ave-rage removing rate is 88.3%,and the removing rates of both NH4+-N and NO2--N can reach 95%above. The mass concentration of NH4+-N removing rate,NO2--N removing rate,and NO3--N production quantity is 1∶1.37∶0.27. The effluent pH is stable,at about 7.95,which is a little higher than that of influent.