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作 者:李广柱[1,2] 刘淼[1] 刘南[1] 陈嵩岳[1] 万政钰[1] 王禹[1]
机构地区:[1]吉林大学环境与资源学院,长春130012 [2]吉林省环境监测中心站,长春130011
出 处:《环境科学》2010年第10期2344-2348,共5页Environmental Science
基 金:吉林省科技发展项目(20060406-1)
摘 要:通过连续动态试验,对新型微压流化式复合生物反应器(MP-FHBR)处理模拟苯酚废水的效能进行研究.结果表明,MP-FHBR的COD容积负荷可达4.86kg/(m3·d)、苯酚容积负荷可达1.96kg/(m3·d),出水COD低于200mg/L、出水苯酚浓度低于1mg/L,COD和苯酚去除率分别达到90%和99%以上.当苯酚容积负荷达到2.04kg/(m3·d),苯酚在反应器中逐渐累积,反应器内微生物的TTC-比脱氢酶活性下降.当MP-FHBR进水苯酚浓度为800mg/L时,最佳水力停留时间为9~10h.水力负荷对反应器沉淀池的泥水分离效果影响较大,限制了反应器的进水量,所以MP-FHBR主要适用于处理较高浓度的含酚废水.A dynamic experiment was conducted continuously to study the efficiency of the new micro-pressurized fluidized hybrid biological reactor(MP-FHBR) for treating artificial phenolic wastewater.The experimental results showed that the COD volumetric loading and phenolic volumetric loading of MP-FHBR could reach 4.86 kg /(m^3·d) and 1.96 kg/(m^3·d) respectively;effluent COD was lower than 200 mg /L;phenol concentrations of effluent were lower than 1 mg /L;removal rates of COD and phenol reached 90% and 99% above respectively.When volumetric loading of phenol in MP-FHBR reached 2.04 kg /(m^3·d),phenol will accumulate gradually in the reactor along with the reactor running,and specific TTC-dehydrogenase activity of microbe in the reactor declines.When phenol concentration of influent was 800 mg /L,the optimum HRT was 9-10 h.Because of the influence of hydraulic loading on the settling performance of sedimentation tank of the reactor,MP-FHBR was superior to treating higher-concentration phenolic wastewater.
分 类 号:X703.1[环境科学与工程—环境工程]
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