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脆硫锑铅矿

脆硫锑铅矿的相关文献在1989年到2022年内共计69篇,主要集中在矿业工程、冶金工业、化学 等领域,其中期刊论文57篇、会议论文2篇、专利文献53877篇;相关期刊30种,包括中南大学学报(自然科学版)、金属矿山、现代矿业等; 相关会议2种,包括第三届全国选矿专业学术年会、第三届全国化学工程与生物化工年会暨首届广西化学化工研究生学术论坛等;脆硫锑铅矿的相关文献由125位作者贡献,包括胡岳华、张芹、吴伯增等。

脆硫锑铅矿—发文量

期刊论文>

论文:57 占比:0.11%

会议论文>

论文:2 占比:0.00%

专利文献>

论文:53877 占比:99.89%

总计:53936篇

脆硫锑铅矿—发文趋势图

脆硫锑铅矿

-研究学者

  • 胡岳华
  • 张芹
  • 吴伯增
  • 覃文庆
  • 邱冠周
  • 魏宗武
  • 余润兰
  • 徐兢
  • 陈建华
  • 孙伟
  • 期刊论文
  • 会议论文
  • 专利文献

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    • 魏宗武; 张瀚; 侍兴君
    • 摘要: 广西某铅锌多金属矿石矿物种类较多,Pb、Sb、Zn、S、Ag品位分别为2.75%、2.33%、12.24%、28.27%、96.08g/t,属高品位复杂难选锡伴生多金属硫化矿.为给该矿石选矿工艺流程确定提供依据,对其进行了浮选工艺研究.试验确定采用先选铅、选铅尾矿选锌的工艺流程.铅浮选采用组合抑制剂硫酸锌+亚硫酸钠抑制铁闪锌矿、硫酸为活化剂、LW-01为捕收剂,经1粗2精2扫浮选脆硫锑铅矿,选铅尾矿以组合抑制剂石灰+y-As抑制硫铁矿和毒砂、硫酸铜为活化剂、丁基黄药为捕收剂,经1粗2精2扫选锌,闭路试验可获得铅品位26.93%、锑品位23.35%、锌品位5.45%、银品位960g/t、铅回收率87.91%、锑回收率87.82%、银回收率86.98%的铅锑精矿,锌精矿锌品位48.67%、锌回收率94.22%的指标.
    • 彭学天
    • 摘要: 为了提高广西大厂巴里选厂铅锑精矿质量及降低锌金属在铅锑精矿中的损失率,针对铅锑精矿中锌损失率较高的问题,采用新型有机抑制剂FY-15代替现场硫酸锌与亚硫酸钠作为铁闪锌矿抑制剂,参照现场优先浮选流程,闭路试验铅锑精矿铅、锑回收率分别提高了0. 74、2. 44个百分点,锌损失率降低了2. 87个百分点,技术指标较好.
    • 陈旭波; 朴永超; 周高云; 胡志强
    • 摘要: 某铅锌多金属硫化矿含铅1.18%、锌1.85%、锑0.79%、银30.62 g/t,铅、锑矿物以脆硫锑铅矿为主,锌矿物主要为铁闪锌矿.以BK338和丁基黄药为捕收剂,BK204为起泡剂,采用"铅锑混选-混选尾矿选锌"工艺流程,闭路试验可获得铅品位30.08%,锑品位20.16%,银含量583.46 g/t,铅、锑、银回收率分别为89.25%、88.76%、71.05%的铅锑精矿,获得锌品位45.18%,锌回收率88.69%的锌精矿,取得了较好的浮选指标,实现了资源的有效利用.%A lead-zinc polymetallic sulfide ore contains1 .18% Pb ,1 .85% Zn ,0 .79% Sb and 30 .62 g/t Ag .Lead and antimony are mainly occurs on jamesonite ,and marmatite is the main zinc mineral .Use BK338 and butyl xanthate as collecting agent ,via Pb-Sb bulk flotation and enrich Zn from flotation tailings ,finally Pb-Sb bulk concentrate grading 30 .08% Pb with recovery of 89 .25% ,grading 20 .16% Sb with recovery of 89 .25% ,and grading 583 .46 g/t Ag with recovery of 71 .05% ,zinc concentrate grading 45 .18% Zn with recovery of 88 .69% was obtained by the small-scale closed-circuit test .
    • 孙伟; 孙晨; 刘润清; 曹学锋; 陶红标
    • 摘要: 为有效分离方铅矿和脆硫锑铅矿并提高其在混合浮选中的回收率,研究两者与乙硫氮捕收剂(DDTC)的作用机理。通过单矿物浮选实验研究矿浆pH值对两者浮选行为的影响。通过循环伏安法和塔菲尔曲线测试研究两者与乙硫氮作用的电化学性质。浮选实验结果表明,在高碱体系中脆硫锑铅矿被石灰强烈抑制。循环伏安曲线和塔菲尔曲线表明,乙硫氮与方铅矿和脆硫锑铅矿的作用是电化学过程。高碱体系对方铅矿与乙硫氮的作用影响不大,但是对脆硫锑铅矿影响很大,这是其自身氧化以及OH−和CaOH+等离子的特性吸附,导致非电活性的羟基化合物和低导电性的钙系化合物附着在其表面,阻碍电子在电极表面的传递,从而使脆硫锑铅矿的可浮性降低。%In order to effectively separate galena and jamesonite and improve the recovery during the mixing flotation, the interaction mechanisms between the minerals and the collector of diethyl dithiocarbamate (DDTC) were investigated. Single mineral flotation test was organized to research the effect of pulp pH value on the flotation behavior of galena and jamesonite. Electrochemistry property of the interaction of these two minerals with DDTC was investigated by cyclic voltammetry and Tafel tests. Flotation test shows that the recovery of jamesonite in high alkaline pulp is strongly depressed by lime (Ca(OH)2). The cyclic voltammetry and Tafel tests results show that the interaction between galena and DDTC is an electrochemical process. High pH value has little influence on the interaction between galena and DDTC, while it has great effect on jamesonite due to self-oxidation and specific adsorption of OH− and CaOH+ on jamesonite surface. Non-electroactive hydroxyl compound and low-electroconductive calcium compounds cover the surface of jamesonite, which impedes electron transfer and DDTC adsorption, thus leads to very low floatability of jamesonite.
    • 胡明振; 曾纪术; 陈锦全; 魏宗武
    • 摘要: 针对广西大厂贫铟锡多金属硫化矿石因磁黄铁矿含量上升,铅锑品位下降,铅锑混浮捕收剂效果差,造成铅锑精矿指标不理想的问题,进行了磁黄铁矿弱磁选—铅锑混浮工艺条件研究.结果表明,磨矿细度为-0.074 mm占46.88%的矿石,经1次磁黄铁矿弱磁选(磁场强度为120 kA/m)后,以丁铵黑药+苯胺黑药+DY为组合捕收剂进行1粗2精2扫铅锑混合浮选,获得了Pb+Sb品位为55.08%,铅、锑回收率分别为93.22%、90.94%,锌含量为4.61%的铅锑混合精矿,与生产现场相比,铅锑混合精矿Pb+Sb的品位提高了2.91个百分点,铅、锑回收率分别提高了7.06、5.13个百分点,锌含量下降了0.58个百分点.因此,组合捕收剂丁铵黑药+苯胺黑药+DY可显著改善铅锑混浮精矿指标.
    • 曹攀; 王军; 胡喆; 赵红波; 程宏伟; 陶浪
    • 摘要: 对大厂铅锌多金属硫化矿混合精矿的浮选分离工艺进行了研究,探索了混合精矿经加温预处理后再进行浮选分离的工艺,并得到了较好的浮选试验指标。并探索了在加温基础上,加入亚硫酸钠与硫酸锌作为抑制剂预处理混合精矿,然后再进行浮选,通过一次铅粗选和两次铅精选,铅回收率达到69.95%,铅品位达到了39.97%,锌含量降到了1.17%;铅回收率较加温不加入抑制剂时提高了7.61个百分点,较好地解决了铅锌多金属硫化矿混合精矿难分离的问题。%Flotation separation of Pb⁃Zn bulk concentrate of a polymetallic sulfide ore from Dachang, Guangxi was investigated. Good flotation indexes were achieved when pulp heating had been introduced as a pretreatment process before flotation. Furthermore, with sodium sulfite and zinc sulfate as depressants, flotation of pre⁃heated bulk concentrate pulp, including one stage of Pb roughing and two stages of Pb cleaning, was conducted, resulted in 69.95%Pb recovery to the lead concentrate grading 39.97%Pb, with the zinc content therein decreased to 1.17%. Compared to the approach with pre⁃heating yet without dispersant, the Pb recovery by the new technique was increased by 7.61 percentage points, which solved effectively the puzzle for Pb⁃Zn bulk concentrate separation of such polymetallic sulfide ore.
    • 孙伟; 孙晨; 刘润清; 曹学锋; 陶红标
    • 摘要: 为有效分离方铅矿和脆硫锑铅矿并提高其在混合浮选中的回收率,研究两者与乙硫氮捕收剂(DDTC)的作用机理。通过单矿物浮选实验研究矿浆pH值对两者浮选行为的影响。通过循环伏安法和塔菲尔曲线测试研究两者与乙硫氮作用的电化学性质。浮选实验结果表明,在高碱体系中脆硫锑铅矿被石灰强烈抑制。循环伏安曲线和塔菲尔曲线表明,乙硫氮与方铅矿和脆硫锑铅矿的作用是电化学过程。高碱体系对方铅矿与乙硫氮的作用影响不大,但是对脆硫锑铅矿影响很大,这是其自身氧化以及OH-和CaOH+等离子的特性吸附,导致非电活性的羟基化合物和低导电性的钙系化合物附着在其表面,阻碍电子在电极表面的传递,从而使脆硫锑铅矿的可浮性降低。
    • 赵翠华; 陈建华; 李玉琼; 何茜; 吴伯增
    • 摘要: 采用密度泛函理论研究复杂矿物脆硫锑铅矿的电子结构及其浮选行为.脆硫锑铅矿的浮选行为与辉锑矿相似,pH值小于6时具有较好的可浮性,并且容易被NaOH抑制,尤其是在有石灰存在时.在弱碱性条件下,脆硫锑铅矿的浮选行为接近于方铅矿的浮选行为.脆硫锑铅矿中Pb的配位结构比方铅矿中Pb的配位结构复杂.脆硫锑铅矿中的Sb存在2种配位模式,而辉锑矿中的Sb仅存在3-配位.方铅矿中的Pb比脆硫锑铅矿中的Pb活跃.与辉锑矿中的Sb相比,脆硫锑铅矿中的Sb(3-配位)不活跃,但是4-配位的Sb比3-配位的Sb活跃得多.脆硫锑铅矿和辉锑矿的HOMO轨道含有金属原子,石灰的存在有助于CaOH+吸附构型的形成.因此石灰对脆硫锑铅矿和辉锑矿都具有抑制作用.
    • 谢兆凤; 李波; 刘万里; 李环; 蒋朝金; 黄海飞
    • 摘要: In the process, sodium sulfide is used to leach jamesonite. The resulted leaching solution is precipitated by feeding sulfur dioxide gas to generate antimony sulfide intermediates. After that, the antimony sulfide precipitate is oxidized in a stove to produce antimony white up to national standards. The optimal conditions, including being leached at 90°C for 3 h, stirring speed at 250 r/min, liquid-solid ratio of 2:1, with sodium sulfide to antimony in the mass ratio of 2.8 and sodium hydroxide to antimony in the mass ratio of 0.3, resulted in the antimony leaching rate up to 92.5%. The sulfur dioxide gas is fed into the leaching solution with the final pH controlled at 5~6, resulted in the obtained antimony sulfide containing 65% Sb, 30% S or less and 0.02% As or less, with antimony precipitation rate higher than 99%. Then, the antimony sulfide is melted at 980~1 000°C with air blown in from two directions for oxidation, leading to the obtained antimony white up to the national primary standard.%采用硫化钠浸出脆硫铅锑矿,浸出液通入二氧化硫气体沉淀出硫化锑中间体,再将硫化锑沉淀在炉中氧化,产出符合国家标准的合格锑白. 最佳工艺条件为:温度90 °C,时间3 h,搅拌速度250 r/min,液固比2:1,硫化钠与锑质量比为2.8,氢氧化钠与锑质量比为0.3,该条件下锑浸出率达92.5%. 将二氧化硫气体通入浸出液并控制终点pH值为5~6,锑沉淀率不低于99%,产出的硫化锑含Sb 65%、S含量不高于30%、As含量不高于0.02%. 硫化锑在980~1 000 °C下熔化,鼓入两路风氧化,产出的锑白产品达到国家一级标准.
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