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将温石棉尾矿煅烧活化产物酸浸获得硫酸镁溶液,以硫酸镁溶液与轻质氧化镁为反应物料,采用水热合成法制备碱式硫酸镁晶须,并对其进行了SEM、XRD、FT-IR以及TG-DTA分析.研究了MgSO4溶液的浓度、硫酸镁与氧化镁摩尔比、反应温度对产物的影响.实验结果表明,该法制备碱式硫酸镁晶须的较佳条件为:MgSO4浓度0.6 mol/L,硫酸镁与氧化镁的摩尔比1∶2,反应温度170℃.实验制备的碱式硫酸镁晶须样品长径比为10~50,其分子式为MgSO4·5Mg(OH)2· 3H2O. 相似文献
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盐酸浸取高岭土中氧化铝的研究 总被引:6,自引:0,他引:6
对盐酸浸取高岭土中氧化铝进行了研究。考察了煅烧温度、盐酸浓度、盐酸用量、酸浸时间及加入反应剂焙烧等因素对氧化铝浸出率的影响 ;研究发现在煅烧温度为 70 0℃ ,盐酸浓度为30 % ,盐酸与氧化铝 mol比为 6 ,酸浸时间为 2 h时 ,试样中的氧化铝浸出率达到 89% ,加入反应剂焙烧可减少酸浸时间 ;为利用高岭土生产铝盐制品 ,提高原料的利用率提供了依据 相似文献
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为有效提高黄陵煤泥的硅铝比,并降低铁含量,研究了用盐酸从煤泥中浸出铝和铁的最佳工艺条件。首先根据黄陵煤泥的化学与物相组成特点,确立了煅烧活化,利用盐酸脱出铝铁的基本技术路线。通过单因素实验确定了煅烧和酸浸反应的最佳工艺条件为:煅烧温度800℃,煅烧时间2 h,酸浸盐酸浓度6 mol/L,液固比10∶1(mL/g),酸浸温度100℃。经最佳条件反应后,铝和铁浸出率分别为83.06%和90.20%,泥渣中SiO2含量由52.58%提高到73.32%,Al2O3含量由19.67%降低到8.49%,Fe2O3含量由5.99%降低到1.06%,SiO2与Al2O3摩尔比由4.87提高到15.73。 相似文献
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氧化锌矿制备活性氧化锌的工艺研究 总被引:10,自引:0,他引:10
研究了以氧化锌矿为原料, 经酸浸、净化、沉淀转化、过滤、洗涤、打浆、喷雾干燥制得活性前驱体碱式碳酸锌, 前驱体经煅烧制备活性氧化锌的新工艺。重点考查了前驱体碱式碳酸锌制备工艺中反应温度、尿素的浓度、物料配比及干燥过程中添加的分散剂种类和用量对前驱体粒径的影响。 相似文献
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研究了以高硅氧化锌矿为原料, 经条件温和的两段循环酸浸、净化、碳铵沉锌、前驱体煅烧等工序制备活性氧化锌的工艺。重点考查了锌的两段循环浸出、碳铵沉锌中各因素的影响及煅烧过程中温度、时间对活性氧化锌粒径的影响。 相似文献
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以工业低铁级硫酸铝、工业硫酸铵为原料,先制备出高纯的硫酸铝铵,再用碳酸氢铵将它转化成碳酸铝铵,经高温煅烧后可制得纯度高,ω(Al_2O_3)>99.99%,分散性好的氧化铝粉体(D_(50)0.5μm),以该氧化铝为原料,制备的灯用稀土三基色荧光粉,其发光亮度和粉体性能均达到或超过了三基色粉的国家标准。 相似文献
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氢氧化镁晶须制备研究 总被引:11,自引:0,他引:11
本文以碱式硫酸镁晶须和氢氧化钠为原料,研究了水热合成法制备氢氧化镁晶须的合理工艺条件。结果表明:当碱式硫酸镁晶须料浆浓度(质量分数)为4.0%,搅拌强度为100r/min,反应温度为180℃,反应时间为4h时,可合成直径≤0.5μm、长径比≥15、表面光滑、纤细均匀、高纯度的氢氧化镁晶须。 相似文献
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鼓泡法制备文石型碳酸钙晶须的实验研究 总被引:6,自引:0,他引:6
本文利用鼓泡法在MgCl2—Ca(OH)2-CO2体系中合成了文石型碳酸钙晶须。用X-射线衍射分析(XRD)表明制备的碳酸钙晶须绝大部分是文石相含有少量的方解石相,显微镜和扫描电子显微镜(SEM)对晶须的进行了形貌分析,结果表明所制备的碳酸钙晶须表面光滑、均匀性好、长径比大。 相似文献
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以脱硫石膏为原料,利用水热法在硫酸-无机盐-水体系中成功制备出硫酸钙晶须。借助SEM、图像粒度分析等方法,考察反应温度、时间、硫酸浓度、晶型控制剂等条件对晶须形貌及长径比的影响,并初步讨论硫酸-无机盐-水体系对晶须成核和生长过程的影响。结果表明:在硫酸-无机盐-水体系中,反应温度、反应时间、硫酸浓度和晶型控制剂的类型,都会改变硫酸钙晶须的平均长径比。制备硫酸钙晶须的最优工艺条件为:脱硫石膏质量分数5%,反应温度135℃,反应时间150 min,硫酸浓度10-3 mol/L,使用的晶型控制剂为氯化铜(质量分数为0.17%)。在此条件下制备的半水硫酸钙晶须平均长径比可达到74.38。 相似文献
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温石棉尾矿煅烧活化产物经盐酸浸取后得到氯化镁溶液。以氯化镁溶液与碳酸氢铵为反应物料,采用碳化法制备碱式碳酸镁晶须。通过正交实验,研究了氯化镁与碳酸氢铵摩尔比、MgCl2溶液的浓度、碳化温度、碳化时间、陈化时间对产物的种类及其晶须形貌的影响,并对产物进行SEM、XRD和热分析。结果表明,该法制备碱式碳酸镁晶须最佳条件:氯化镁与碳酸氢铵的摩尔比为1∶2,MgCl2浓度为0.8mol/L,碳化时间2 h,碳化温度60℃,陈化时间为4h,在此条件下制备出碱式碳酸镁晶须样品长径比为10~40,其分子式为4MgCO3.Mg(OH)2.4H2O。 相似文献
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《Minerals Engineering》2007,20(3):252-258
Processing of aluminium dross is one of the most challenging tasks because of its toxic nature. The dross generated while melting at various facilities is generally remelted with salts to recover residual metal values. The remaining residue dross contains mostly aluminium oxide, alloying elements and salts such as NaCl or KCl. This residue dross while stock piling creates pollution of the adjoining area as salts leach out to water stream and also emits harmful gases. In the present study domestic aluminium dross was treated for developing a suitable process flow sheet to obtain η-alumina a high valued product. Initially H2SO4 leaching was carried out for both un-washed and washed dross. With un-washed dross the leaching efficiency achieved was ∼71% but washing of dross followed by leaching raised the recovery to ∼84%. Washing of dross is essential to have higher alumina recovery and also to recover salt for recycling. The liquor obtained after treatment of the dross with acid was further processed to obtain aluminium hydroxide of amorphous nature by hydrolyzing aluminium sulphate with aqueous ammonia. The aluminium hydroxide was then subjected to calcinations which resulted in the formation of η-alumina at 900 °C. 相似文献
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This article presents the results of a study conducted to investigate the recovery of rare earth metals and precipitated silicon dioxide from phosphorus slag. To determine the possibility and completeness of the studied processes, thermodynamic data was obtained through the determination of the Gibbs energy and equilibrium constant of the reactions of calcium metasilicate with different reagents, namely sodium hydroxide and carbonate as well as nitric, hydrochloric, and sulphuric acids. This article also presents the results of studies on the treatment of phosphorus slags via hydrometallurgical methods using alkaline agents (sodium hydroxide and sodium carbonate) and nitric acid. The recovery of silicon in solution by the autoclave leaching of phosphorus slag using solutions of sodium hydroxide and sodium carbonate resulted in recovery efficiencies of 1.1% and 16.6%, respectively. The nitric acid treatment of phosphorus slag was studied, and the recovery efficiencies of various elements were the following: rare earth metals, 98.3–98.6%; aluminium, 96.5–98.6%; iron, 94.9–96.5%; and calcium, 99.1–99.5%. Nitric acid (46.5%) was selected as the phosphorus slag recovery agent. The cake produced after the nitric acid treatment of phosphorus slag was leached using two processes based on the use of a sodium hydroxide solution: (1) in a temperature-controlled cell under normal conditions and (2) in an autoclave. The process of leaching under normal conditions was determined to be the most effective process, resulting in an efficiency of silicon recovery into solution of 97.7%. 相似文献
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离子型稀土矿无铵化浸取剂实验研究 总被引:4,自引:0,他引:4
为从源头控制离子型稀土矿原地浸矿工艺采用传统药剂造成的氨氮污染, 通过柱浸流程实验, 对比了氯化铁/铝、硫酸镁等无铵浸取剂的稀土浸出性能, 以及氢氧化钠、碳酸(氢)钠的除杂沉淀性能。结果表明, 氯化铁和氯化铝是较为理想的无铵浸取剂, 氢氧化钠和碳酸(氢)钠可分别作为无铵除杂剂和沉淀剂。与传统药剂相比, 无铵药剂用于原地浸矿具有浸取能力强、单耗用量少、浸取成本低、环境容量大等优势。 相似文献