工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2015年
8期
78-81
,共4页
范荣桂%张世强%姜清风%许倩
範榮桂%張世彊%薑清風%許倩
범영계%장세강%강청풍%허천
Ir-Ta-Sn掺杂电极%电催化氧化%垃圾渗滤液
Ir-Ta-Sn摻雜電極%電催化氧化%垃圾滲濾液
Ir-Ta-Sn참잡전겁%전최화양화%랄급삼려액
Ir-Ta-Sn doping electrode%electric catalytic oxidation%landfill leachate
电催化氧化技术是水处理领域的一门新兴技术,具有环境兼容性好的优势。采用Ir-Ta-Sn掺杂电极作阳极、不锈钢电极作阴极处理垃圾渗滤液,并考察极板间距、电催化氧化电压、起始pH和电催化氧化时间对电解效果的影响。实验结果表明,酸性条件下进行降解较有利;极板电压和极板间距对降解效果均有不同程度的影响;电解时间超过4 h时,对COD的降解没有显著影响。当pH为3、极板电压为24~36 V、极板间距为1.5~2.0 cm及反应时间为4 h时,对垃圾渗滤液的COD去除率可达50%左右。
電催化氧化技術是水處理領域的一門新興技術,具有環境兼容性好的優勢。採用Ir-Ta-Sn摻雜電極作暘極、不鏽鋼電極作陰極處理垃圾滲濾液,併攷察極闆間距、電催化氧化電壓、起始pH和電催化氧化時間對電解效果的影響。實驗結果錶明,痠性條件下進行降解較有利;極闆電壓和極闆間距對降解效果均有不同程度的影響;電解時間超過4 h時,對COD的降解沒有顯著影響。噹pH為3、極闆電壓為24~36 V、極闆間距為1.5~2.0 cm及反應時間為4 h時,對垃圾滲濾液的COD去除率可達50%左右。
전최화양화기술시수처리영역적일문신흥기술,구유배경겸용성호적우세。채용Ir-Ta-Sn참잡전겁작양겁、불수강전겁작음겁처리랄급삼려액,병고찰겁판간거、전최화양화전압、기시pH화전최화양화시간대전해효과적영향。실험결과표명,산성조건하진행강해교유리;겁판전압화겁판간거대강해효과균유불동정도적영향;전해시간초과4 h시,대COD적강해몰유현저영향。당pH위3、겁판전압위24~36 V、겁판간거위1.5~2.0 cm급반응시간위4 h시,대랄급삼려액적COD거제솔가체50%좌우。
Electric catalytic ox idat ion technology is an emerging technology in the field of water treatment ,which has good environmental compatibility. The Ir-Ta-Sn doping electrode as anode and stainless steel electrode as cath-ode have been used for treating landfill leachate. The effects of the plate distance ,electric catalysis oxidation volt-age,the initial pH and the electric catalytic oxidation time have been investigated. The experimental results show that acidic condition is more advantageous for the degradation of COD. The degradation effect is affected by both of the plate voltage and plate distance to different degrees. The degradation of COD is not significantly affected when the electrolysis time is longer than four hours. When the initial pH is 3 ,the plate voltage 24-36 V,plate spacing 1.5-2.0 cm,and reaction time 4 hr,the COD removing rate from landfill leachate can reach about 50%.