共查询到18条相似文献，搜索用时 234 毫秒
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为研究金川铜镍矿山酸性废水溶解尾矿砂实现综合治理废液与废固的可能性,进行了尾矿砂在硫酸中的溶解实验。结果表明,尾矿砂在硫酸浓度大于3mol/L、温度保持90℃以上并在液固比6.0下强力搅拌,能够较好地溶解于硫酸中,生成无定形二氧化硅;300℃的马弗炉焙烧4h有助于尾矿砂中绿泥石的溶解,对透闪石的溶解影响不大。尾矿砂中橄榄石、蛇纹石和透辉石较容易被硫酸溶解,透闪石、斜长石则比较难溶解,这与尾矿砂中矿物性质有密切关系。 相似文献
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随着高品位硫化镍资源的日益减少及社会发展对镍需求量的日益增加,低品位红土镍矿的开发利用受到人们的日益关注。本文在对某蛇纹石型红土镍矿详细的矿物学研究基础上,进行了常压硫酸溶解浸出实验研究,获得硫酸浓度1 mol/L、液固比10、浸出反应温度70℃以上、反应时间6 h左右、磨矿细度65%(76μm以下含量)左右的最佳硫酸溶解浸出实验条件;该实验条件下,红土镍矿中Ni、Fe、Mg的浸出率分别为94.4%、72.1%和88.64%。本研究可为该类型红土镍矿的经济回收利用提供科学依据。 相似文献
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《矿物岩石地球化学通报》2015,(5)
金川铜镍硫化矿尾矿砂富含Cu、Ni和Co等金属,为对其进行回收,对新尾矿库不同深度的尾矿砂分别进行了直接硫酸酸溶浸出与A.f.-硫酸酸溶联合浸出实验,利用ICP-AES分析了不同阶段浸出液中Cu2+、Ni2+、Co2+含量。实验结果表明,A.f.-硫酸酸溶联合浸出工艺对尾矿砂中有价金属Cu、Ni和Co的浸出效果优于单独酸溶浸出工艺。其中,A.f.-硫酸酸溶联合浸出法对1m深度的尾矿砂中Cu、Ni、Co的浸出率最高,分别达到95.78%、98.01%和75.13%,而单独硫酸酸溶作用的离子浸出率分别为75.69%、74.33%和42.33%。 相似文献
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直接酸溶法浸取硫铁矿烧渣中铁的实验研究 总被引：4，自引：0，他引：4
对常压下用盐酸直接酸溶提取硫铁矿烧渣中的铁进行了实验研究，探讨了影响硫铁矿烧渣酸溶的因素。结果表明，影响铁溶出率的主要因素为液固比、反应时间和温度；当液固比为4．0mL／g、反应温度100℃时，高速搅拌反应2h后，铁的溶出率可达72％，浸取液经进一步处理可生产氯化铁系列产品，有较好的应用前景。 相似文献
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为了粉煤灰的高附加值综合利用,采用酸浸法对准格尔地区循环流化床粉煤灰进行了镓的浸出实验研究,考察了多种因素对镓的浸出率的影响,包括粉煤灰粒度,酸的种类与浓度、酸浸温度与时间、固液比等。结果表明,提高镓的浸出率的适宜条件为:粉煤灰粒度200目,盐酸的浓度6 mol/L,酸浸温度应大于160℃,酸浸时间6 h,液固比在5∶1~6∶1之间为宜。在优选的工艺条件下,镓的浸出率可达80%以上。从粉煤灰中提取镓,使其作为一种资源加以利用,是提高粉煤灰综合利用价值的有效途径。 相似文献
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金属矿山生产产生大量的尾矿,不但危害周围生态环境,而且对资源造成极大浪费。金川镍矿尾矿砂Ni、Cu和Co的平均含量分别达到0.21%、0.19%和0.01%,是够得上二次开发利用的宝贵资源。文中对金川镍矿尾矿砂矿物组成特征及酸溶特性进行了详细的研究,目的是为工业化高效回收尾矿砂中Ni、Cu和Co等有价金属提供科学依据与技术支撑。矿物学研究表明,金川镍矿尾矿砂主要由蛇纹石、绿泥石、橄榄石、辉石、透闪石、磁铁矿、白云石及少量磁黄铁矿、镍黄铁矿和黄铜矿等组成。经多年露天堆存,金川镍矿老尾矿库尾矿砂已发生不同程度的氧化作用。尾矿库3 m以上为强烈氧化带,金属硫化物矿物颗粒边缘、裂缝处基本都有强烈的氧化作用发生。碳酸盐等易溶矿物被大量消耗。硫酸溶解实验表明,金川镍矿老尾矿库尾矿砂中有价金属Cu、Ni和Co的平均浸出率分别可达88.6%、75.3% 和70.8%。尾矿砂中Cu、Ni和Co有价金属的浸出效果不但清楚直观地反映了尾矿库中尾矿砂的氧化程度,而且表明金属硫化物尾矿砂的风化作用,极大地促进了硫化物矿物中有价金属的酸溶浸出。 相似文献
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为研究不同pH值酸碱溶液对尾矿砂压缩特性的影响,通过应用自行研发的固结渗透装置,对采自辽宁省铁岭市红印尾矿库尾矿砂进行试验研究,测得不同pH值酸碱溶液浸泡后的尾矿砂孔隙比,压缩系数及压缩模量等参数随pH值变化的规律,结果表明:酸碱溶液浸泡后的尾矿砂在固结压力的作用下,初期变化速度很快,然后逐渐趋于平稳;且酸溶液浸泡后的尾矿砂孔隙比最小,蒸馏水浸泡后的尾矿砂孔隙比最大;酸(碱)溶液pH值与尾矿砂压缩系数呈单调递增(减)关系;酸碱溶液浸泡过尾矿砂的压缩模量比原状土大.实验所得的这些参数随pH值变化规律为研究尾矿坝整体稳定提供了一定的理论依据. 相似文献
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地浸采铀产生的污染物通过渗透迁移作用威胁地下水资源,已成为制约地浸采铀技术发展的瓶颈,而微生物胶结技术能有效地降低砂岩铀矿的渗透性,是目前抑制污染物向采区周围地下水迁移的有效方法。因此,选用巴氏芽孢杆菌,分析其耐酸性;利用自行研制的砂岩型铀矿砂渗透系数试验装置,测得不同胶结液浓度、不同菌液与胶结液体积比以及不同注浆轮次条件下砂岩型铀矿砂的渗透系数,确定其最优的参数配比;采用扫描电镜（scanning election
microscopy,简称 SEM）和X射线衍射光谱（X-ray diffraction,简称 XRD）等设备,表征微生物胶结前后铀矿砂的矿物成分及其微观结构,研究其微生物胶结抗渗机制。研究结果表明：巴氏芽孢杆菌在 pH = 4 时仍具有较好的繁殖能力和脲酶活性,能适应铀矿砂的酸性环境;在一定范围内增大胶结液浓度、菌液与胶结液的体积比可以促进碳酸钙的生成,最佳的胶结液浓度为 1 mol/L、菌液与胶结液体积比为1:3、注浆轮次为7时,注浆后铀矿砂的减渗率达到 95.33%;胶结后铀矿砂的渗透系数随注浆轮次的增加而降低,经过11轮注浆后铀矿砂的减渗率高达99.75%,渗透系数下降到 2.8×10−5 cm/s;沉积的碳酸钙晶型主要为方解石,方解石堵塞铀矿砂粒间孔隙,并将矿砂颗粒胶结成整体,是铀矿砂渗透系数降低的主要原因。微生物诱导碳酸钙沉淀胶结铀矿砂的抗渗机制为控制和减少地下水污染提供重要的理论指导。 相似文献
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Manganese was extracted from leaching low-grade manganese ore in sulfuric acid medium. The effects of granule diameter, leaching time, liquid/solid ratio (V/W) and the concentration of sulfuric acid were investigated through orthogonal and single factor experiments. The experimental results showed that the optimal leaching conditions are, size of 0.054mm, 120 minutes of reaction time, 3(V/W) of liquid/solid ratio and 30% of the concentration of sulfuric acid (g/g). Under those conditions, the leaching efficiency is 96.73%. The kinetics of the leaching process is in accordance with the characteristics of fractal reaction. 相似文献
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较低的矿物溶解率和反应剂的不可循环利用是CO2矿物封存发展的两大难题。针对这些问题,本文提出了一种新的以可循环的NH4Cl溶液作为中间媒介的CO2矿物封存工艺,并系统地研究了蛇纹石在氯化铵溶液中的液-固两相的反应动力学。实验研究发现:(1)纤蛇纹石的浸取符合Elovich模型,浸取过程基本在1h左右完成,在100℃、5mol/L氯化铵溶液中,纤蛇纹石的浸取率达到12.67%;(2)温度对纤蛇纹石初始反应速率的影响显著,温度越高,反应速率越快;(3)当氯化铵浓度在1~5mol/L范围内变化时,它对镁离子浸取率的影响不明显,反应速率随着浓度的升高而有所增加;(4)本实验反应表现出来的活化能大小为129.56kJ/mol。 相似文献
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The low-grade vanadium-containing stone coal used in this experiment was collected from Wuxi Coun- try, Chongqing City, China. The experiment focused on the vanadium recovery from roasted residue through opti- mizing the process conditions of an effective and environmentally-friendly technology, named calcified roast- ing-sulfuric acid leaching technology. By single-factor experiments and orthogonal experiments, the effects of roast- ing temperature, roasting time, sulfuric acid concentration and leaching time on the leaching ratio of vanadium were analyzed. The results showed that the leaching ratio of vanadium reached 85.5% under the proper technological con- ditions of roasting temperature=950℃, roasting time=4 h, 40% concentration of sulfuric acid and leaching time=6 h. 相似文献
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Leaching of three high-phosphorus manganese ore samples from central India with dilute hydrochloric acid (0.1–0.6 M) has been found to reduce their phosphorus contents below the specified limit of 0.12%. Various process parameters, such as concentration of acid, liquid/solid ratio, temperature and period of leaching, particle size of ore etc., have been investigated in detail and optimum values have been worked out on the laboratory scale. Both liquid/solid ratio (slurry concentration) and temperature of leaching appear to be critical process parameters. While the increase in liquid/solid ratio above 3–4 has no beneficial effect, leaching temperature above 50°C has an adverse effect on the extent of dephosphorization. Grain size of ore finer than 100 mesh (B.S.) in general gives satisfactory dephosphorization. Laboratory-scale results have been, in general, supported by bench-scale work which shows that phosphorus can be effectively removed from high-phosphorus manganese ores of central India by leaching in dilute hydrochloric acid at ambient temperature. Comparative performance of the dilute solutions of all the three mineral acids as leaching agents has been discussed. 相似文献
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Leaching of manganese residue for the preparation of trimanganese tetroxide with a high surface area
The accumulation of electrolytic manganese residue (EMR) has become a serious problem and its recycling will be of great benefit to protect the environment and assist sustainable development. The reusing method was conducted by leaching EMR with sulfuric acid and the optimal leaching condition was 1:3 (g/g) as the ratio of solid to liquid with 20% (g/g) H2SO4 , heating at 90 ℃ for 3 hours, which aims at extracting Mn in a sulfuric acid medium. The produced MnSO4 solution was precipitated by adding alkali and oxidized in aqueous phase. The oxidized products were characterized by various techniques, including X-ray powder diffraction (XRD), Fourier transform infrared (IR) spectrometry, vibrating sample magnetometry (VSM), with Brunauer-Emmett-Teller (BET) specific surface area instrument and laser particle size analyzer. The final products were confirmed to be a single-phase Mn3O4 . 相似文献
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《矿物学报》2013,(Z1)
Fly ash was used to prepare alumina and silica white, The 3 stages of the process are as follows: ammonium sulfate calcining, acid leaching and alkali dissolution. The optimum conditions for the experiments to determine are as follows: molar ratio of (NH4)2SO4/Al2O3 is 6, the calcining time is 2h, he H2SO4 concentration is 20%, the leaching temperature is 80℃ and dissolution duration is 2h, the ratio of solution and solid reaction material is 6 for ammonium sulfate calcining and acid leaching stage, reaction time 30min, ratio of liquid to ore 5∶1, alkali concentration 45% and reaction temperature 95 ℃for the alkali dissolution stage. Under these conditions, the total leaching efficiencies of Al2O3 and SiO2 are 78.86% and 95%, respectively. The quality of the main products alumina and silica white can meet the national standards of GB/T24487-2009 and GB10517-89, respectively. 相似文献
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金川铜镍硫化矿尾矿砂数量巨大,其中Ni、Cu和Co等有价金属种类较多,含量较为丰富,蕴含着巨大的经济价值。本文研究了氧化亚铁硫杆菌对金川铜镍尾矿砂提取有价金属效果的影响,在选取金川新尾矿库中心钻孔尾矿砂样品与氧化亚铁硫杆菌作用不同时间的基础上进行化学酸溶,利用电感耦合等离子体发射光谱仪(ICP-AES)分析了溶液中Cu2+、Ni2+、Co2+含量,并通过离子浸出率来表征微生物对尾矿中有价金属提取的影响效果。结果表明,尾矿砂直接化学酸溶后Cu2+、Ni2+浸出率分别为73.78%和69.87%,Co2+浸出率仅为39.57%;而氧化亚铁硫杆菌先与尾矿砂作用后再进行硫酸酸溶,其Cu2+、Ni2+总浸出率均可达到90%以上,Co2+总浸出率也可达到70%以上。实验结果证明氧化亚铁硫杆菌的参与促进了尾矿砂中Cu2+、Ni2+、Co2+的浸出。 相似文献