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某高砷高硫金精矿焙砂浸金特性的研究 被引量:6
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作者 杨永斌 刘晓亮 +2 位作者 李骞 姜涛 曾冠武 《矿冶工程》 CAS CSCD 北大核心 2014年第3期65-68,共4页
某高砷高硫金精矿焙砂含Au84.27 g/t,含As0.55%、S1.03%,生产现场金的氰化浸出率不足80%,迫切需要查明该焙砂的浸金特性。结合化学成分和物相分析,发现含铁物相包裹是浸金渣中残留金难以浸出的根本原因。浸金渣残留金(19.54 g/t)中包裹... 某高砷高硫金精矿焙砂含Au84.27 g/t,含As0.55%、S1.03%,生产现场金的氰化浸出率不足80%,迫切需要查明该焙砂的浸金特性。结合化学成分和物相分析,发现含铁物相包裹是浸金渣中残留金难以浸出的根本原因。浸金渣残留金(19.54 g/t)中包裹金占96.66%,主要包裹物相有氧化铁、毒砂和黄铁矿等含铁物相,92.68%的包裹金存在于这些含铁物相中。浸金试验中焙砂及浸金渣所达到的浸出率分别只有84.47%、16.70%,进一步验证了含铁物相中的包裹金极难浸出,焙砂的浸金率很难继续提高。 展开更多
关键词 金精矿焙砂 氰化浸出
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含砷锑金精矿焙砂预处理与提金工艺研究 被引量:4
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作者 李希山 《有色矿冶》 2020年第3期36-39,47,共5页
云南某低品位难处理金矿含有砷、硫、碳、锑等多种对氰化浸金有害的杂质成分,金矿中金以包裹金为主.两段焙烧后焙砂直接氰化浸出的浸金率较低.本研究针对含砷锑硫金精矿焙砂,对比了酸浸预处理、碱浸预处理、碱性硫化物预处理等方式,结... 云南某低品位难处理金矿含有砷、硫、碳、锑等多种对氰化浸金有害的杂质成分,金矿中金以包裹金为主.两段焙烧后焙砂直接氰化浸出的浸金率较低.本研究针对含砷锑硫金精矿焙砂,对比了酸浸预处理、碱浸预处理、碱性硫化物预处理等方式,结果显示,碱性硫化物预处理效果最好,金浸出率可以达到95.06%. 展开更多
关键词 金精矿焙砂 预处理 碱性硫化物 氰化浸出
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金精矿焙砂氯化挥发多元素综合提取新技术研究 被引量:3
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作者 潘贵 邵京明 +2 位作者 钱虎 陈学辉 朱万强 《世界有色金属》 2017年第23期230-230,232,共2页
为解决传统剧毒氰化浸出提金工艺对环境的危害,本文对金精矿焙砂直接氯化挥发提金进行了探索试验研究,试验考察了CaCl_2添加量、焙烧时间、球团粒径等主要因素对金挥发率影响情况。结果表明金精矿焙砂直接氯化提取技术可行,在条件CaCl_... 为解决传统剧毒氰化浸出提金工艺对环境的危害,本文对金精矿焙砂直接氯化挥发提金进行了探索试验研究,试验考察了CaCl_2添加量、焙烧时间、球团粒径等主要因素对金挥发率影响情况。结果表明金精矿焙砂直接氯化提取技术可行,在条件CaCl_2加入量11%、氯化焙烧时间2h、球团粒径10mm下,Au与Ag的挥发率达98%和80%以上,实现了焙砂中金、银的高效综合回收。 展开更多
关键词 金精矿焙砂 氯化挥发 多元素 综合回收
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Differences of cyanide leaching between calcine and dust from refractory gold concentrates 被引量:5
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作者 Pan CAO Shang-hua ZHANG +4 位作者 Ya-jie ZHENG Han-bing HE Shen-zhi LAI Xing-jun WANG Bing TAN 《Transactions of Nonferrous Metals Society of China》 SCIE EI CAS CSCD 2020年第7期1964-1979,共16页
Differences of cyanide leaching between the calcine and the dust from a refractory gold concentrate were investigated by comparative method. Results showed that gold leaching efficiencies of the calcine and the dust w... Differences of cyanide leaching between the calcine and the dust from a refractory gold concentrate were investigated by comparative method. Results showed that gold leaching efficiencies of the calcine and the dust were 85.31% and 54.30%, respectively, with direct cyanidation. Contents and existing forms of arsenic and carbon were the main reasons for those differences. The maximum gold leaching efficiencies of the calcine and the dust were 87.70% and 58.60%, respectively, with cyanidation after NaOH pre-leaching. Harmful elements removal, gold loss in NaOH pre-leaching and iron oxides hindrance codetermined gold leaching efficiencies of the calcine and the dust. After H2SO4 pre-leaching, the maximum gold leaching efficiencies of the calcine and the dust achieved 94.96% and 80.40%, respectively. The effect of carbonaceous matter was the main reason for differences for leaching efficiencies of the calcine and the dust. Based on those differences, two proper gold extraction processes were put forward, and gold leaching efficiencies for the calcine and the dust achieved 94.91% and 91.90%, respectively. 展开更多
关键词 refractory gold concentrate CALCINE DUST CYANIDATION carbonaceous matter
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