工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2014年
6期
56-58
,共3页
范荣桂%董雪%李美%陈瑶%董双双
範榮桂%董雪%李美%陳瑤%董雙雙
범영계%동설%리미%진요%동쌍쌍
含砷废水%活性炭%催化氧化%酸化
含砷廢水%活性炭%催化氧化%痠化
함신폐수%활성탄%최화양화%산화
arsenic-containing wastewater%activated carbon%catalytic oxidation%acidification
磨矿工艺产生的废水中含有砷和COD等,不能直接进入氰化工艺阶段,需进行处理。分别采用活性炭静态吸附法和空气-活性炭催化氧化法对磨矿含砷废水进行了处理,研究了2种方法的处理效果及影响因素。结果表明,活性炭静态吸附法对水中总砷的吸附能力差,处理出水不能达标排放;而单一的空气-活性炭催化氧化法处理效果也不佳,但经酸化预处理后,处理出水中各污染物浓度均达到排放标准的要求。
磨礦工藝產生的廢水中含有砷和COD等,不能直接進入氰化工藝階段,需進行處理。分彆採用活性炭靜態吸附法和空氣-活性炭催化氧化法對磨礦含砷廢水進行瞭處理,研究瞭2種方法的處理效果及影響因素。結果錶明,活性炭靜態吸附法對水中總砷的吸附能力差,處理齣水不能達標排放;而單一的空氣-活性炭催化氧化法處理效果也不佳,但經痠化預處理後,處理齣水中各汙染物濃度均達到排放標準的要求。
마광공예산생적폐수중함유신화COD등,불능직접진입청화공예계단,수진행처리。분별채용활성탄정태흡부법화공기-활성탄최화양화법대마광함신폐수진행료처리,연구료2충방법적처리효과급영향인소。결과표명,활성탄정태흡부법대수중총신적흡부능력차,처리출수불능체표배방;이단일적공기-활성탄최화양화법처리효과야불가,단경산화예처리후,처리출수중각오염물농도균체도배방표준적요구。
The wastewater from ore grinding process containing arsenic and COD ,etc. cannot enter the cyanidation process stage directly and needs treatment. Therefore ,the wastewater containing arsenic from ore grinding process should be treated by active carbon static adsorption method and air-activated carbon catalytic oxidation method. The removing effect and influencing factors of the two method is investigated. The results show that the removing capacity of activated carbon static adsorption method for total arsenic in water is poor ,and the treated effluent cannot reach the discharge standard. In addition,the treatment effect of single air-activated carbon catalytic oxidation method is not good either. Nevertheless,after the wastewater has been treated by acidification pretreatment,all of the pollutant concentrations in the treated effluent can meet the requirements of discharge standard.