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阴阳极协同作用电催化深度处理焦化废水
李海涛; 李鑫钢; 李玉平; 曹宏斌
2009
Source Publication化工进展
IssueS2Pages:98-102
Abstract在质子交换隔膜电解槽中采用石墨毡填充电极对焦化废水降解进行研究。以生化出水为研究对象,阴极电芬顿的最佳处理条件为:pH=2~3,Fe2+=0.5~1mmol/L,I=100mA,2h。阴极电芬顿和阳极氧化对COD去除率分别为66.9%和71.2%,电流效率分别为90%和92%。在连续式反应器中,最佳条件下,阳极氧化后COD=180~200mg/L、pH=2~3,再经过阴极电芬顿后COD小于100mg/L,pH=6~9,达到国家一级排放标准。阳极氧化和阴极电芬顿均能够有效去除酚类、苯类、含氮杂环、苯腈、苯并杂环类、多环芳烃等多种有机污染物。
Keyword电芬顿 阳极氧化 隔膜 石墨毡电极 焦化废水
Indexed By其他
Document Type期刊论文
Identifierhttp://ir.ipe.ac.cn/handle/122111/10046
Collection研究所(批量导入)
Recommended Citation
GB/T 7714
李海涛,李鑫钢,李玉平,等. 阴阳极协同作用电催化深度处理焦化废水[J]. 化工进展,2009(S2):98-102.
APA 李海涛,李鑫钢,李玉平,&曹宏斌.(2009).阴阳极协同作用电催化深度处理焦化废水.化工进展(S2),98-102.
MLA 李海涛,et al."阴阳极协同作用电催化深度处理焦化废水".化工进展 .S2(2009):98-102.
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