广东化工
廣東化工
엄동화공
GUANGDONG CHEMICAL INDUSTRY
2012年
3期
145-146,137
,共3页
万俊杰%谢光健%吴艳%陈华英%林凡
萬俊傑%謝光健%吳豔%陳華英%林凡
만준걸%사광건%오염%진화영%림범
Fenton高级氧化%偶氮染料%降解
Fenton高級氧化%偶氮染料%降解
Fenton고급양화%우담염료%강해
fenton%advanced oxidation%Azodye: degradation
对三种不同初始浓度的罗丹明B废水进行Fenton氧化降解工艺条件及降解历程进行研究。结果显示:当[H2O2]:[Fe^2+](摩尔比)=3.26的时候,COD去除效果最好,随着[Fe^2+]的投加量增加,废水会变成铁红色,同时沉淀物增加:COD分别为200,300和800mg/L的3种不同浓度的废水,[H202]投加量分别为0.5,0.9,3.5mL,废水的初始pH=3的时候,COD的去除率最好。
對三種不同初始濃度的囉丹明B廢水進行Fenton氧化降解工藝條件及降解歷程進行研究。結果顯示:噹[H2O2]:[Fe^2+](摩爾比)=3.26的時候,COD去除效果最好,隨著[Fe^2+]的投加量增加,廢水會變成鐵紅色,同時沉澱物增加:COD分彆為200,300和800mg/L的3種不同濃度的廢水,[H202]投加量分彆為0.5,0.9,3.5mL,廢水的初始pH=3的時候,COD的去除率最好。
대삼충불동초시농도적라단명B폐수진행Fenton양화강해공예조건급강해역정진행연구。결과현시:당[H2O2]:[Fe^2+](마이비)=3.26적시후,COD거제효과최호,수착[Fe^2+]적투가량증가,폐수회변성철홍색,동시침정물증가:COD분별위200,300화800mg/L적3충불동농도적폐수,[H202]투가량분별위0.5,0.9,3.5mL,폐수적초시pH=3적시후,COD적거제솔최호。
Degradation conditions and processes of Rhodmine B using Fenton(Fe^2+/H2O2) reactions was investigated in three different conditions. The results showed that the COD removing rate was the largest at [H2O2] : [FeZ+](molar ratio)=3.26. With the dosage increasing, the wastewater became red and more deposits generated. The COD removing rate was the largest at pH=3, dosages of [H2O2]=0.5, 0.9 and 3.5 mL for three different concentrations(200, 300 and 800 mg/L)wastewater.