黄金
黃金
황금
GOLD JOURNAL
2014年
2期
61-63
,共3页
刘强%李哲浩%降向正%朱军章
劉彊%李哲浩%降嚮正%硃軍章
류강%리철호%강향정%주군장
臭氧氧化%曝气生物滤池%含氰废水%处理工艺
臭氧氧化%曝氣生物濾池%含氰廢水%處理工藝
취양양화%폭기생물려지%함청폐수%처리공예
ozonation%biological aerated filter%cyanide wastewate%treatment process
针对黄金矿山尾矿库氰渣淋溶的低质量浓度含氰废水,采用OOT/OCT-BAF联合工艺进行处理。其试验结果表明,在进水总氰化合物为64.45 mg/L、硫氰酸盐为22.74 mg/L、COD为76.58 mg/L、铜为72.48 mg/L的条件下,当臭氧投加量为250 mg/L、臭氧投加量分流比为2∶1、BAF的废水停留时间为20 min、气水比为3∶1时,出水总氰化合物为0.02 mg/L、硫氰酸盐完全去除、COD为5.43 mg/L、铜为0.32 mg/L、氨氮为0.79 mg/L,出水达到《GB 3838-2002地表水环境质量标准》Ⅲ类水质。
針對黃金礦山尾礦庫氰渣淋溶的低質量濃度含氰廢水,採用OOT/OCT-BAF聯閤工藝進行處理。其試驗結果錶明,在進水總氰化閤物為64.45 mg/L、硫氰痠鹽為22.74 mg/L、COD為76.58 mg/L、銅為72.48 mg/L的條件下,噹臭氧投加量為250 mg/L、臭氧投加量分流比為2∶1、BAF的廢水停留時間為20 min、氣水比為3∶1時,齣水總氰化閤物為0.02 mg/L、硫氰痠鹽完全去除、COD為5.43 mg/L、銅為0.32 mg/L、氨氮為0.79 mg/L,齣水達到《GB 3838-2002地錶水環境質量標準》Ⅲ類水質。
침대황금광산미광고청사림용적저질량농도함청폐수,채용OOT/OCT-BAF연합공예진행처리。기시험결과표명,재진수총청화합물위64.45 mg/L、류청산염위22.74 mg/L、COD위76.58 mg/L、동위72.48 mg/L적조건하,당취양투가량위250 mg/L、취양투가량분류비위2∶1、BAF적폐수정류시간위20 min、기수비위3∶1시,출수총청화합물위0.02 mg/L、류청산염완전거제、COD위5.43 mg/L、동위0.32 mg/L、안담위0.79 mg/L,출수체도《GB 3838-2002지표수배경질량표준》Ⅲ류수질。
The combined process of OOT/OCT and biological aerated filter ( BAF) was used in the treatment of the low concentration cyanide wastewater in gold mines .The results show that under the conditions of the total influent cyanogen of 64.45 mg/L,thiocyanate of 22.74 mg/L,COD of 76.58 mg/L and copper of 72.47 mg/L,when the ozone dosage was 250 mg/L,the split ratio of ozone dosage was 2∶1 ,the hydraulic retention time of BAF was 20 min, and the ratio of gas to water was 3∶1 ,the total effluent cyanogen was 0 .02 mg/L,thiocyanate was degraded complete-ly,COD was 5.43 mg/L,copper was 0.32 mg/L and ammonia nitrogen was 0.79 mg/L.The effluent quality can reach standard Ⅲof GB 3838-2002 Surface Water Environment Quality Standard .