工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2014年
11期
55-58
,共4页
宋震宇%杨伟%张景辉%杨永健%吴津%李少凡%陈冠益
宋震宇%楊偉%張景輝%楊永健%吳津%李少凡%陳冠益
송진우%양위%장경휘%양영건%오진%리소범%진관익
地下水污染%氯代烃%无泡曝气%中空纤维膜
地下水汙染%氯代烴%無泡曝氣%中空纖維膜
지하수오염%록대경%무포폭기%중공섬유막
groundwater contamination%chlorinated hydrocarbon%bubbleless-aeration%hollow fiber membrane
以无泡曝气膜组件为氢源和氧源的释放装置,分别建立厌氧还原修复区和好氧氧化分解区,并考察了氢气和氧气曝气压力对水相氧化还原电位的影响及曝气过程对厌氧还原脱氯反应、好氧氧化分解反应的影响。结果表明:厌氧还原脱氯区的氧化还原电位-水相停留时间曲线均呈现出上开口抛物线特征;好氧氧化分解区的氧化还原电位-水相停留时间曲线均呈现出下开口抛物线特征;两个修复区的最佳停留时间比例为4∶1。
以無泡曝氣膜組件為氫源和氧源的釋放裝置,分彆建立厭氧還原脩複區和好氧氧化分解區,併攷察瞭氫氣和氧氣曝氣壓力對水相氧化還原電位的影響及曝氣過程對厭氧還原脫氯反應、好氧氧化分解反應的影響。結果錶明:厭氧還原脫氯區的氧化還原電位-水相停留時間麯線均呈現齣上開口拋物線特徵;好氧氧化分解區的氧化還原電位-水相停留時間麯線均呈現齣下開口拋物線特徵;兩箇脩複區的最佳停留時間比例為4∶1。
이무포폭기막조건위경원화양원적석방장치,분별건립염양환원수복구화호양양화분해구,병고찰료경기화양기폭기압력대수상양화환원전위적영향급폭기과정대염양환원탈록반응、호양양화분해반응적영향。결과표명:염양환원탈록구적양화환원전위-수상정류시간곡선균정현출상개구포물선특정;호양양화분해구적양화환원전위-수상정류시간곡선균정현출하개구포물선특정;량개수복구적최가정류시간비례위4∶1。
Using the bubbleless-aeration membrane module as the releasing device of hydrogen and oxygen sources, the anaerobic reductive remediation area and the aerobic oxidative decomposition remediation area have been estab-lished. The effects of aeration pressure of hydrogen and oxygen on oxidation reduction potential (ORP) aqueous and the effect of aeration process on anaerobic reduction dechloridation reaction and aerobic oxidation decomposition reaction are investigation,respectively. The results show that the ORP-aqueous retention time curve in anaerobic reductive dechlorination remediation area presents an up-opening parabolic feature of growth ,while the ORP aque-ous retention time curve in aerobic oxidative decomposition remediation area presents a feature of down-opening parabola of growth. The optimal proportion of the retention time of the two remediation areas is 4∶1.