金属矿山
金屬礦山
금속광산
METAL MINE
2015年
2期
160-165
,共6页
刘奕祯%莫伟%张旭源%马少健%吴伯增%陈锦全
劉奕禎%莫偉%張旭源%馬少健%吳伯增%陳錦全
류혁정%막위%장욱원%마소건%오백증%진금전
锡石硫化矿尾矿%柱式静态浸泡%浸泡液初始pH%液固比%尾矿堆积高度%重金属溶出行为
錫石硫化礦尾礦%柱式靜態浸泡%浸泡液初始pH%液固比%尾礦堆積高度%重金屬溶齣行為
석석류화광미광%주식정태침포%침포액초시pH%액고비%미광퇴적고도%중금속용출행위
Cassiterite sulfide ore tailings%Column static soaking%Initial pH of soaking solution%Liquid-solid ratio%Stack height of tailings%Heavy metals leaching behavior
广西大厂凤凰选矿厂处理锡石硫化矿。通过柱式静态浸泡试验研究了浸泡液初始pH值、液固比、尾矿堆积高度对该厂尾矿中Mn、Zn、As溶出行为的影响以及不同条件下浸泡液pH的变化情况。结果表明:①不同的初始pH、液固比以及尾矿堆积高度下,随着浸泡时间的延长,Mn和Zn的溶出浓度均先显著下降然后趋于稳定,累积溶出量均先快速增长然后缓慢增长,As则无论是溶出浓度还是累积溶出量均总体上呈近乎线性增长趋势,而浸泡液的pH值均被中和到7.2~8.0之间。②初始pH为3.5时Mn、Zn最易溶出,为5.5时次之,为4.5时相对最难,但初始pH对As的溶出无显著影响;液固比越大,Mn、Zn和As均越容易溶出;尾矿堆积高度总体上对Mn、Zn和As的溶出都无显著影响。③试验范围内,Mn、Zn、As的溶出量都很低,对应的累积溶出量最大值分别只有14.505、13.471、0.768 mg/kg。以上研究成果可为现场尾矿库重金属污染的防控提供参考。
廣西大廠鳳凰選礦廠處理錫石硫化礦。通過柱式靜態浸泡試驗研究瞭浸泡液初始pH值、液固比、尾礦堆積高度對該廠尾礦中Mn、Zn、As溶齣行為的影響以及不同條件下浸泡液pH的變化情況。結果錶明:①不同的初始pH、液固比以及尾礦堆積高度下,隨著浸泡時間的延長,Mn和Zn的溶齣濃度均先顯著下降然後趨于穩定,纍積溶齣量均先快速增長然後緩慢增長,As則無論是溶齣濃度還是纍積溶齣量均總體上呈近乎線性增長趨勢,而浸泡液的pH值均被中和到7.2~8.0之間。②初始pH為3.5時Mn、Zn最易溶齣,為5.5時次之,為4.5時相對最難,但初始pH對As的溶齣無顯著影響;液固比越大,Mn、Zn和As均越容易溶齣;尾礦堆積高度總體上對Mn、Zn和As的溶齣都無顯著影響。③試驗範圍內,Mn、Zn、As的溶齣量都很低,對應的纍積溶齣量最大值分彆隻有14.505、13.471、0.768 mg/kg。以上研究成果可為現場尾礦庫重金屬汙染的防控提供參攷。
엄서대엄봉황선광엄처리석석류화광。통과주식정태침포시험연구료침포액초시pH치、액고비、미광퇴적고도대해엄미광중Mn、Zn、As용출행위적영향이급불동조건하침포액pH적변화정황。결과표명:①불동적초시pH、액고비이급미광퇴적고도하,수착침포시간적연장,Mn화Zn적용출농도균선현저하강연후추우은정,루적용출량균선쾌속증장연후완만증장,As칙무론시용출농도환시루적용출량균총체상정근호선성증장추세,이침포액적pH치균피중화도7.2~8.0지간。②초시pH위3.5시Mn、Zn최역용출,위5.5시차지,위4.5시상대최난,단초시pH대As적용출무현저영향;액고비월대,Mn、Zn화As균월용역용출;미광퇴적고도총체상대Mn、Zn화As적용출도무현저영향。③시험범위내,Mn、Zn、As적용출량도흔저,대응적루적용출량최대치분별지유14.505、13.471、0.768 mg/kg。이상연구성과가위현장미광고중금속오염적방공제공삼고。
Fenghuang Dressing Plant of Dachang in Guangxi Province is planning to deal with the cassiterite sulfide ore. Effects of soaking solution pH,liquid-solid ratio,stack height on release behavior of Mn,Zn,As in tailings,as well as pH values at various conditions,are investigated through the column static soaking immersion tests. Results indicated that:①when the in-itial pH,liquid-solid ratio,and stack height are different,and as the leaching time extended,release concentration of Mn and Zn is dropped dramatically first and then went steady. The cumulative release was rapidly increased first and then grown slowly. Meanwhile,As leaching concentration as well as cumulative release are nearly linearly increased,and the pH value of the soa-king solution is neutralized from 7. 2 to 8. 0.②Mn and Zn releases are the easiest when the initial pH is 3. 5,a little hard with pH value of 5. 5,and the hardest when pH is 4. 5,but the initial pH value has no influence on As leaching behavior;The high-er of liquid-solid ratio,the more easily Mn,Zn and As is leached;Stack height of tailings has little influence on leaching be-havior of Mn,Zn and As.③Within the test range,the release of Mn is very low,as well as Zn and As,and the corresponding maximum leaching amount is 14. 505,13. 471,0. 768 mg/kg respectively. The research results above provide some references for heavy metal pollution prevention and control in the field of tailings dam.