有色金属科学与工程
有色金屬科學與工程
유색금속과학여공정
JIANGXI NONFERROUS METALS
2014年
3期
9-15
,共7页
Na2SO3%化学沉淀%晶种MnO2%曝气%电解锰废水
Na2SO3%化學沉澱%晶種MnO2%曝氣%電解錳廢水
Na2SO3%화학침정%정충MnO2%폭기%전해맹폐수
Na2SO3%chemical precipitation%crystal seed MnO2%aeration%electrolytic manganese wastewater
通过实验研究了还原沉淀-晶种曝气组合工艺去除电解锰废水中Cr6+和Mn2+,并探索了最佳工艺条件.首先以Na2SO3做还原剂将Cr6+转化为Cr3+后再通过化学沉淀法除去,然后采用加入MnO2做晶种曝气氧化去除废水中的Mn2+.结果表明:当Na2SO3投加量为0.5 g/L,还原反应pH值为4,还原反应时间6 min,Cr6+可完全转化为Cr3+.Cr3+在pH值为8时沉淀最完全,出水总铬浓度可从100 mg/L降到0.5 mg/L以下.除铬后,当MnO2投加量为25 g/L,废水pH值为9,曝气10 min,出水Mn2+浓度可从1000 mg/L 降到0.4 mg/L 以下.通过以上处理出水总铬和总锰均达到我国《污水综合排放标准(GB8978-1996)》一级要求.
通過實驗研究瞭還原沉澱-晶種曝氣組閤工藝去除電解錳廢水中Cr6+和Mn2+,併探索瞭最佳工藝條件.首先以Na2SO3做還原劑將Cr6+轉化為Cr3+後再通過化學沉澱法除去,然後採用加入MnO2做晶種曝氣氧化去除廢水中的Mn2+.結果錶明:噹Na2SO3投加量為0.5 g/L,還原反應pH值為4,還原反應時間6 min,Cr6+可完全轉化為Cr3+.Cr3+在pH值為8時沉澱最完全,齣水總鉻濃度可從100 mg/L降到0.5 mg/L以下.除鉻後,噹MnO2投加量為25 g/L,廢水pH值為9,曝氣10 min,齣水Mn2+濃度可從1000 mg/L 降到0.4 mg/L 以下.通過以上處理齣水總鉻和總錳均達到我國《汙水綜閤排放標準(GB8978-1996)》一級要求.
통과실험연구료환원침정-정충폭기조합공예거제전해맹폐수중Cr6+화Mn2+,병탐색료최가공예조건.수선이Na2SO3주환원제장Cr6+전화위Cr3+후재통과화학침정법제거,연후채용가입MnO2주정충폭기양화거제폐수중적Mn2+.결과표명:당Na2SO3투가량위0.5 g/L,환원반응pH치위4,환원반응시간6 min,Cr6+가완전전화위Cr3+.Cr3+재pH치위8시침정최완전,출수총락농도가종100 mg/L강도0.5 mg/L이하.제락후,당MnO2투가량위25 g/L,폐수pH치위9,폭기10 min,출수Mn2+농도가종1000 mg/L 강도0.4 mg/L 이하.통과이상처리출수총락화총맹균체도아국《오수종합배방표준(GB8978-1996)》일급요구.
A new technology of reduction precipitation combined with crystal seed aeration is proposed for completely removing Cr6+and Mn2+from electrolytic manganese wastewater by studying the optimum treatment conditions. In the first step, Cr6+ was removed by chemical precipitation by transforming into Cr3+ using Na2SO3 as reductant. Then Mn2+is removed by aeration using MnO2 as crystal seed. The results are as follows:Cr6+ can be transformed into Cr3+ completely with Na2SO3 dosage of 0.5 g/L, reduction pH value of 4, reduction time of 6 min. Precipitation of Cr3+ is the most complete when pH value is 8 and the effluent concentration of total chromium is less than 0.5 mg/L from 100 mg/L. After chromium removal, the effluent concentration of Mn2+ is less than 0.4 mg/L from 1 000 mg/L when MnO2 dosage is 25 g/L, wastewater pH value is 9 and aeration time is 10 min which meets the first grade national sewage effluent discharge standard (GB8978-1996).