工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2015年
7期
81-84
,共4页
电镀废水尾水%生化性%倒置A2/O
電鍍廢水尾水%生化性%倒置A2/O
전도폐수미수%생화성%도치A2/O
tail water of electroplating wastewater%biodegradabability%inverted A2/O process
以电镀废水尾水为目标废水，联合生活污水处理，以提升目标废水的可生化性，并经过增设填料的改良型倒置A2/O工艺处理，研究了工艺对电镀废水尾水的脱氮处理效能。结果表明：在电镀废水尾水所占的体积百分数为30%时，工艺运行效益较好；在DO为1.90~2.10 mg/L，回流比在150%左右，系统对NH4+-N、TN、COD的去除率分别达到93%、80%、85%；当有足够的易降解有机碳源，即提高COD/TN时可使TN去除率≥84%。
以電鍍廢水尾水為目標廢水，聯閤生活汙水處理，以提升目標廢水的可生化性，併經過增設填料的改良型倒置A2/O工藝處理，研究瞭工藝對電鍍廢水尾水的脫氮處理效能。結果錶明：在電鍍廢水尾水所佔的體積百分數為30%時，工藝運行效益較好；在DO為1.90~2.10 mg/L，迴流比在150%左右，繫統對NH4+-N、TN、COD的去除率分彆達到93%、80%、85%；噹有足夠的易降解有機碳源，即提高COD/TN時可使TN去除率≥84%。
이전도폐수미수위목표폐수，연합생활오수처리，이제승목표폐수적가생화성，병경과증설전료적개량형도치A2/O공예처리，연구료공예대전도폐수미수적탈담처리효능。결과표명：재전도폐수미수소점적체적백분수위30%시，공예운행효익교호；재DO위1.90~2.10 mg/L，회류비재150%좌우，계통대NH4+-N、TN、COD적거제솔분별체도93%、80%、85%；당유족구적역강해유궤탄원，즉제고COD/TN시가사TN거제솔≥84%。
Taking the tail water of electroplating wastewater as the target ,and combining with the treatment of do-mestic sewage,the biodegradability of the target wastewater can be up-graded. The nitrogen removing treatment capa-city of the tail water of electroplating wastewater has been studied by establishing in addition the improved inverted A2/O process for fillers. The results show that when the volume percentage of tail water of electroplating wastewater is 30%,the running efficiency of this process is better. When DO is 1.90-2.10 mg/L and the ratio of reflux ratio is about 150%,the removing rates of NH4+-N,COD,and TN are 93%,80%,and 85%,respectively. When the degrad-able organic carbon source is enough,≥84%of TN removing rate can be up-graded by the up-grading of COD/TN.
