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1.
The effects of dodecylamine (DDA), kerosene and pH on the recovery of combustible matter and ash content of a lignitic coal from Tuncbilek, Turkey have been studied using a three-variable and two-level (23) factorial experimental design. The coal sample responded favourably to batch flotation with high recoveries in excess of 95% using both kerosene and DDA respectively. The main effects of all three factors on the recovery are positive. Significance of DDA as a collector, is somewhat greater than that of kerosene, but its selectivity for ash reduction is not significant at the 95% confidence level. The pH-dependence of recovery by these collectors is opposite to each other. The DDA-induced flotation recovery is lowest at pH 9.4, an effect which has been related to precipitation of cationic species of this collector. The kerosene-induced recovery and grade of combustible matter increases with pH and this has been attributed to a better dispersion of coal and its associated clays. The two-way interaction effects are all negative at a smaller level. The main and interaction effects have been discussed on the basis of adsorption at most favourable surface sites, different modes of orientation of DDA species, competition with kerosene, and probable collecting properties of the frother used. The simultaneous effects of the two collectors on the recovery of combustible matter have been discussed at each pH value used.  相似文献   

2.
The effects of different heavy metals (copper and mercury), cationic surfactants cetylpyridinium chloride, anionic surfactant sodium dodecylbenzenesulfonate and the chemistry of the solution (pH value) on the adsorption of three selected phenolic compounds (2, 4-Dichlorophenol, 2, 4-Dinitro-phenol and 2, 4-Dimethyphenol) on sediment were studied. Results indicated that in the sediment-water system with phenolic compounds: (1) all of the data could be simulated by Freundlich equation; (2) the experiments studying pH effects showed that the adsorption capacity of 2, 4-Dichlorophenol and 2, 4-Dimethyphenol were quite potentia Hydrogenii dependent and increased with decrease in potentia Hydrogenii, while 2, 4-Dinitrophenol followed the different trend; (3) As the concentration increased from 0 to 0.2?mM for Cu2+, the Freundlich capacity coefficient constant varied from 62.84 to 325.1 for 2, 4-Dichlorophenol, from 13.1 to 82.179 for 2, 4-Dinitrophenol and from 29.433 to 7.976 for 2, 4-Dimethyphenol, respectively. The Freundlich capacity coefficient constant of 2, 4-Dichlorophenol, 2, 4-Dinitrophenol and 2, 4-Dimethyphenol varied from 62.84 and 421.43, 13.1 and 138.1, 29.433 and 1.381, respectively, with concentration of Hg2+ increased from 0 to 0.04?mM, respectively; (4) the adsorption of 2, 4-Dichlorophenol and 2, 4-Dimethyphenol were accentuated by cetylpyridinium chloride but suppressed by sodium dodecylbenzenesulfonate, whereas the adsorption of 2, 4-Dinitrophenol on sediment was enhanced by both cationic and anionic surfactants, effects that are consistent with electrostatic and hydrophobic interactions among ionic surfactants, phenolic compounds and sediment. The results are believed to provide a useful insight into describing the transport and fate of phenolic compounds in natural environments.  相似文献   

3.
Both froth flotation and centrifugal concentration were used to pre-concentrate the oil sands froth treatment tailings prior to the recovery of heavy minerals (titanium and zirconium minerals). Over 90% of the heavy minerals were recovered into a bulk flotation concentrate that was about 50% of the feed mass at 85 °C without any reagents. The same recoveries were obtained at 50 °C with the addition of NaOH and/or sodium oleate. However, the flotation concentrate also recovered over 90% of the residual bitumen and much of the clays/slimes. Subsequent treatment of the flotation concentrate such as dewatering and bitumen removal would be difficult due to these residual bitumen and clays. On the other hand, a SB40 centrifugal concentrator recovered over 85% of the heavy minerals but less than 30% of the residual bitumen. With improved liberation the recovery of the residual bitumen into the concentrate could be further reduced. The particle sizes of the SB40 concentrates were also larger than the flotation concentrates, making subsequent processing much easier.  相似文献   

4.
阴-阳离子表面活性剂复合柱撑蒙脱石的制备与表征   总被引：1，自引：0，他引：1  
利用阳离子表面活性剂--十六烷基三甲基溴化铵(HDTMAB)和阴离子表面活性剂--十二烷基磺酸钠(SDS)制备了一系列阴-阳离子表面活性剂复合柱撑蒙脱石.同时采用多种测试手段(碳、硫、硅含量分析、X射线衍射分析和热分析)对产物进行结构表征和性能分析.结果表明,SDS难以单独进入蒙脱石层间,但与HDTMAB作用后,SDS可以进入到蒙脱石结构层间.在复合物中有机碳量较低时,SDS对有机碳含量增加贡献明显,但其柱撑效率随着HDTMAB加入量增加而下降,至HDTMAB加入量大于3倍阳离子交换容量(CEC)时趋于平衡.在复合物中有机碳量较高时,HDTMAB负载量有下降的趋势,至HDTMAB加入量大于3倍阳离子交换容量时趋于平衡.SDS进入结构层内总体提高蒙脱石的有机碳含量,明显地增加产物的层间高度,并且改善其热稳定性.  相似文献   

5.
滇黔地区的"白泥塘层"与锰矿具有密切的成因联系,前人对其地球化学特征研究时关注的主要是硅质灰岩全岩,并非硅质成分本身,而硅质岩全岩能否真实地反映"白泥塘层"中硅质的来源有待研究。本文以滇黔地区"白泥塘层"硅质灰岩为研究对象,用盐酸去除硅质灰岩中的碳酸盐矿物,获得成分较为单一的硅质组分,采用ICP-MS和ICP-OES测定全岩与去除碳酸盐的硅质组分中的微量元素,通过对比两者的微量元素地球化学特征研究"白泥塘层"中硅质的来源问题。结果表明:去除碳酸盐的硅质组分的Th/U=0.02~0.05,低于全岩的Th/U值(0.08~0.2),Eu/Eu*=0.86~1.54(均值1.15),显示为正Eu异常,此特征不同于全岩(全岩的Eu/Eu*=0.87~0.93,均值0.90,显示为弱的负Eu异常);硅质组分及全岩的稀土含量均表现为轻稀土较重稀土富集,但硅质组分中的轻稀土所占比重大于全岩。以上特征确切地表明了"白泥塘层"硅质灰岩中的硅质成分来自于热水,对于解释二叠系时期锰矿的形成具有重要的指示意义。  相似文献   

6.
马生凤  温宏利  李冰  王蕾  朱云 《岩矿测试》2016,35(3):271-275
采用悬浮液进样进行原子光谱测定,可以减少样品前处理和不用酸碱化学试剂,是一种绿色化学的发展方向。本文采用表面张力仪对聚丙烯酸钠、聚氧化乙烯、六偏磷酸钠、柠檬酸三钠等表面活性剂与铅锌矿粉末组成悬浮液的表面张力进行测定,利用火焰原子吸收光谱法的雾化装置进行了雾化效率的考察和优化选择。随着表面活性剂浓度的增加,水溶液和悬浮液的雾化效率均增大,当达到一定浓度时,雾化效率增幅趋缓并达到最大值,不同表面活性剂具有不同变化趋势。对于聚氧化乙烯制备的悬浮液,在2 g/L浓度时具有最高的雾化效率;而聚丙烯酸钠在5 g/L浓度时具有更高的雾化效率,可达20%。表明表面活性剂能改善悬浮液的稳定性并提高雾化效率,可以应用于原子光谱的测定。  相似文献   

7.
石英与钠长石浮选分离的研究   总被引：3，自引：0，他引：3  
用十八胺(阳离子捕收剂)和十二烷基磺酸钠(阴离子捕收剂,SDS)作浮选为捕收剂分离石英与钠长石,研究了浮选条件对分离效果的影响以及捕收剂在矿物表面的吸附行为.结果表明,最佳浮选条件是浮选液的pH=2,阴、阳离子捕收剂的浓度分别为3.0×10-6 mol/L和4.0×10-6 mol/L;阴阳离子捕收剂在石英与钠长石两种矿物上表现出相同的吸附行为.在最佳浮选条件下,对不同配比的石英和钠长石混合物进行浮选,石英回收率为14%,钠长石回收率达80%,分离效果显著;对含微量长石的石英矿粉进行浮选,分离效果与石英与钠长石混合物相近.  相似文献   

8.
In this research, effect of temperature, pressure, salinity, surfactant concentration, and surfactant type on interfacial tension (IFT) and critical micelle concentration of Saudi Arabian crude oil and various aqueous phases were investigated. The temperature ranged from ambient condition to 90°C, and the pressures were varied from atmospheric to 4,000 psi (27.58 MPa). Surfactant solutions were prepared using several aqueous phases, i.e., purified water, 10% brine consisting of 100% NaCl, 10% brine consisting of 95% NaCl and 5% CaCl2, and 10% brine consisting of 83% NaCl and 17% CaCl2. Out of 13 commercial surfactants, only three surfactants showed good solubility in pure water and brine. Those are Zonyl FSE Fluorosurfactant®, Triton X-100®, and Triton X-405®. Therefore, they were investigated thoroughly by measuring their efficiency in reducing the crude oil-aqueous phase IFT. Based on this screening process, laboratory surfactant flooding experiments for crude oil recovery were conducted using Triton X-405 and Triton X-100. The chemical flood was made at both original oil in place and at residual oil in place subsequent to conventional water flooding. Based on the obtained results, both surfactants were efficient, and more oil was recovered than that obtained through water flooding. Comparing both surfactant solutions, it was observed that Triton X-405 was more efficient than Triton X-100 at the same surfactant concentration and reservoir conditions.  相似文献   

9.
The conditions under which dilute CuS sols might be stable in natural waters have been explored. In single electrolyte solutions at room temperature, coagulation data adhere approximately to the classic theory for electrostatic stabilization. From this theory, the Hamaker constant is estimated to be 4 × 10?19J. In a simple, four-component, synthetic seawater, coagulation occurs at 0.14 g/kg salinity. The critical coagulation concentration for CaCl2 drops by a factor of six between 25 and 175°C. These measurements, which appear to be the first over so large a temperature range, confirm previous suppositions about the effect of temperature. The results suggest that electrostatic stabilization will be ineffective in nature for substances like CuS with large Hamaker constants, because divalent cation concentrations in most aquatic environments are sufficient for coagulation. Three alternate mechanisms by which organic compounds can stabilize sulfide sols are reported: chelation of counterions. surface hydrophillization through adsorption, and steric stabilization by polymers. Humic acid, which contributes stability when present at less than 1 mg C/1, may stabilize by all three mechanisms. However, theory indicates that even in the absence of chemical stabilization, extremely dilute sols such as would be encountered in anoxic marine basins might require many years to coagulate, thus appearing stable even if not.  相似文献   

10.
Anionic and cationic flotation of a Stillwater Complex chromite was studied as a function of pH and various pretreatments of the mineral. Aging the ground mineral in air markedly decreased anionic (sodium dodecylsulfate) flotation below pH3 and enhanced it above pH 4–5. Such aging increased cationic (dodecylammonium chloride) flotation in the basic pH region. Mildly preheating the mineral enhanced anionic flotation. Increased conditioning time in collector solution decreased anionic flotation. Strongly acid pretreating the mineral caused it to behave like a simple charged oxide toward both anionic and cationic flotation. These phenomena appear to be related to the effect of aging on the amounts of Fe(II) and Fe(III), of Cr(III) and Cr(VI) and of Mg(II) on the mineral's surface.  相似文献   

11.
王艳  傅俊醒  唐强  胡安详  刘佳鑫 《岩土力学》2016,37(Z1):329-333
表面活性剂随着工业、农业、日常生活等各种活动进入到土体及地下水中,不仅会带来环境污染的风险,还会改变土体的结构等从而影响土体的工程性质。为了合理评估表面活性剂污染土体的工程适宜性,采用阴离子表面活性剂十二烷基苯磺酸钠(SDBS)和阳离子表面活性剂三甲基十六烷基溴化铵(CTAB)对粉土进行改性,通过直剪试验研究其对粉土强度特性的影响。结果表明,表面活性剂改性后的粉土内摩擦角减小,随着表面活性剂浓度的增大,内摩擦角减小的幅值越大,当表面活性剂浓度达2%时,粉土内摩擦角减小23.9%;SDBS改性后的粉土黏聚力大大减小,SDBS浓度为2%时,黏聚力减小91.8%,CTAB改性后粉土黏聚力增大,最大增幅达41.8%;改性粉土中加入不同pH的表面活性剂时,内摩擦角变化很小,表明表面活性剂的酸碱程度对土样内摩擦角影响较小,随着表面活性剂溶液pH的增大,改性粉土的黏聚力呈现出下降的趋势,pH改变了土壤的电荷的分配,改变了土粒间的静电作用,从而引起土体黏聚力的变化。  相似文献   

12.
The Ba2+ ion adsorption isotherms on β-MnO2 were of the Langmuir type. The endothermic heat of adsorption (40 kJ mol?1) is ascribed to entropy contributions associated with the Na+Ba2+ ion-exchange mechanism. The Ba2+ ion adsorption density was higher at pH 10 than that at pH 7, due to the more negative surface charge at the higher pH. Ba2+ ions were found to reverse the sign of the ζ potential of the MnO2 particles.More oleate was adsorbed by β-MnO2 in the presence of Ba2+ ions than in their absence. The oleate adsorption isotherms on Ba2+-activated MnO2 were of the Freundlich type and indicated an exothermic process. Hallimond flotation recovery of Ba2+-activated MnO2 was higher at pH 10 than at pH 7, although less oleate was adsorbed at the higher pH. At pH 7, Mn2+-activation led to higher recoveries than Ba2+-activation. It seems that the attraction between the surface and the activator plays an important rôle in determining the flotation recovery.  相似文献   

13.
Hallimond tube flotation experiments have been carried out on the two calcium minerals scheelite and calcite using dodecylammonium chloride as collector. The main variables studied were the calcium ion concentration and the pH.In the case of scheelite, addition of calcium chloride markedly lowered the flotation recovery. Recovery was also lowered when the pH was reduced below about 10. Since it is known that the zeta potential of scheelite is almost independent of pH this confirms that co-adsorption of un-ionized amine is necessary for good flotation. Other un-ionized long-chain molecules can replace the amine; thus it was shown that excellent flotation can be obtained event at about pH 7 by adding dodecanol together with dodecylammonium chloride. With the completely ionic trimethyldodecylammonium chloride recoveries were poor and were independent of pH.In the case of calcite, calcium chloride had no immediate effect on flotation recovery, but at low collector concentrations marked depression occurred after many hours standing in the presence of calcium ions. The effect of pH on flotation of calcite was anomalous and there appear to be two pH regions in which recoveries are high.The results are discussed and attention is drawn to the need for more thorough studies of the calcium carbonate/water interface.  相似文献   

14.
The adsorption of surfactants from aqueous solution is a phenomenon of major importance in applications ranging from ore flotation and paint technology to enhanced oil recovery. As this paper will illustrate, the process is very complex and of high scientific interest; its results can be extended to the retention of organic compounds (humic and fulvic acids, pollutants...) on solids in the biosphere. For a good understanding of the mechanisms involved in surfactants adsorption at the hydrophilic solid–aqueous solution interface, thermodynamic models have to take into account: (i) the physical chemistry of the surfactant in aqueous solution for choosing the appropriate reference phase, (ii) the surface heterogeneity of the adsorbing solid, (iii) the intensity of normal adsorbate–adsorbent bonds responsible for adsorption, (iv) the intensity of lateral bonds that favour the formation of surface aggregates through cooperative process and finally, (v) suitable theoretical models to describe adsorption phenomena. Once this has been achieved, two systems can be discussed: systems characterised by strong normal adsorbate–adsorbent bonds, currently used in ore flotation, which lead, in the case of heterogeneous surfaces, to the formation of lamellar aggregates at monolayer concentration and bilayer formation for higher concentrations. Systems characterised by weak normal adsorbate–adsorbent bonds, currently used in enhanced oil recovery and hydrocarbon (bio)remediation, which correspond to: (i) formation of globular micelles at the solid surface near the CMC when the temperature is higher than the Krafft point, (ii) formation of bilayered lamellar aggregates in the opposite case, (iii) three-dimensional condensation on substrate (T<TKrafft) if the ionic surfactant interacts with cations in the bulk. To cite this article: J.-M. Cases et al., C. R. Geoscience 334 (2002) 675–688.  相似文献   

15.
Experimentation with cupric salts and aqueous sulphide solutions at room temperature and pressure resulted in the formation of normal and blaubleibender covellite. Blaubleibender covellite is formed at higher pH and lower Eh values than normal covellite. The experimental pH/Eh values for normal covellite formation fall within the theoretical CuS stability field. Blaubleibender was produced at pH/Eh values outside this area. Variations in pH and Eh during the course of the experimental runs showed that normal covellite formed by the simple reaction: Cu2++HS–=CuS+H+; blaubleibender covellite formation on the other hand involves solid state reduction of an initial normal covellite precipitate. Cell volume and formation pH show a straight line relationship in normal covellite which is not observed with blaubleibender. Blaubleibender covellite can be formed from aqueous solution at low temperatures and pressures. The experimental results indicate that it is a metastable intermediary in the reduction of normal covellite to more reduced, stable, copper sulphides. The copper sulphide formed from sedimentary processes in a normal marine environment should initially be normal covellite, or transitory blaubleibender covellite which may be reduced during diagenesis.
Zusammenfassung Synthetische Versuche mit Kupfersalzen und wässrigen Sulfidlösungen bei Zimmertemperatur und atmosphärischem Druck ergaben die Bildung von normalem und blaubleibendem Covellin. Blaubleibender Covellin wird bei höheren pH- und niedereren Eh-Werten gebildet als normaler Covellin. Die pH/Eh-Werte für normalen Covellin fallen in das theoretische Stabilitätsfeld von CuS. Die Bildung von blaubleibendem Covellin erfolgte bei pH/Eh-Werten außerhalb dieses Feldes. Systematische Veränderungen der pH- und Eh-Werte während der Syntheseversuche ließen erkennen, daß die Bildung von normalem Covellin nach folgender einfacher Reaktion verläuft: Cu2++HS–=CuS+H+; die Bildung von blaubleibendem Covellin dagegen erfolgt unter teilweiser Reduktion eines vorher gefällten Niederschlags von normalem Covellin. Im Gegensatz zum blaubleibenden Covellin zeigt der normale Covellin eine geradlinige Beziehung zwischen Zellvolumen und Formations-pH-Wert. Blaubleibender Covellin kann aus wässrigen Lösungen bei niederen Temperaturen und niederem Druck gebildet werden. Die Untersuchungsergebnisse zeigen, daß er eine metastabile Zwischenform zu normalem Covellin und stärker reduzierten stabilen Kupfersulfiden bildet. Die Kupfersulfide, die sich während eines Sedimentationsprozesses in einer normalen marinen Facies bilden, werden anfänglich aus normalem Covellin bestehen oder vorübergehend aus blaubleibendem Covellin, mit einer möglichen Reduktion während der Diagenese.
  相似文献   

16.
Alkyl xanthyl thiosulphates (R.OCSS.S2O3?) (RXT?) are formed in solution by mild oxidation (e.g. by I2) of solutions containing both xanthate and thiosulphate. They can also be formed by reaction of Cu2+ with xanthate and thiosulphate, reaction of dixanthogen with thiosulphate, and by reaction of xanthate with tetrathionate; these last three reactions can occur in flotation pulps in slightly acid or alkaline solutions (pH 5–10).Alkyl xanthyl thiosulphates are stable in acid and neutral solution; the solutions have a UV absorption maximum at 289 nm. In strongly alkaline solution (pH 12) RXT? decomposes within a few minutes to yield a xanthate (mostly) plus a little perxanthate. At pH 10 this decomposition to xanthate takes about 48 h. At pH 7–9 RXT? is relatively stable. RXT? is not extracted from aqueous solution with common solvents (chloroform, iso-octane, cyclohexane, or ether). It forms a water-insoluble adduct with cetyltrimethyl-ammonium bromide (CTAB); this adduct can be extracted into chloroform, and the extract has a UV absorption maximum at 296 nm.RXT? was found in solutions from the gangue-sulphide flotation section at Renison Ltd, the zinc flotation circuit and the copper flotation circuit at Mount Isa Mines Ltd, and the lead flotation section of The Zinc Corporation Ltd. The presence of RXT? in operating flotation plants has various practical and theoretical implications.  相似文献   

17.
The effect of amine collector type, pH, and ionic strength on the flotation behaviour of kaolinite was investigated in a series of laboratory batch flotation tests. In distilled water, ether diamine, a strong collector for silica, does not induce any flotation or only very weak flotation of kaolinite over a wide pH range from pH 3 to pH 10.5. Ether monoamine causes strong flotation of kaolinite in distilled water, especially in acidic solutions, but high dosages of the collector are required. Such observations are in contrast to the flotation behaviour of oxide minerals such as silica for which ether diamine shows stronger collecting power than ether monoamine. The pH dependence of kaolinite flotation is also opposite to that of oxides, with lower flotation recovery obtained at higher pH. In contrast to oxides, the flotation recovery of kaolinite increases with ionic strength. It was demonstrated that the enhanced flotation of kaolinite in NaCl solutions cannot be attributed to the frothing ability of NaCl or the intercalation of kaolinite by alkylamines. It is proposed that the screened zeta potential of kaolinite particles in a high ionic strength environment causes random aggregation of kaolinite particles exposing hydrophobic (001) silica plane in the presence of ether amines.  相似文献   

18.
A promising technique for the removal of heavy metal ions from wastewater streams involved firstly the ions adsorption on a colloidal precipitate (carrier) and then the separation of the loaded flocs (coagula) by a modified column flotation. Here, the effluent feed and the carrier (ferric hydroxide) enter smoothly by the top of the column through a special diffuser, in counter current with rising bubbles (100–600 μm diameter) generated by using recycled water, surfactant and air suction through a venturi. High separation values of the column flotation of the carrier precipitates were achieved, despite the high superficial flow rate and the high Fe+ 3 concentration utilized (> 60 mg L− 1 Fe). No rupture of colloidal carrier aggregates was observed and a low split was ensured by monitoring the concentrate (floated product) flow rate. Results indicated that best separation was attained by controlling the medium pH (for best heavy metal ion adsorption onto the carrier), followed by sodium oleate, used as “collector” and optimizing operating parameters (conditioning, flow rates, etc.). The column throughput reached 43 m h− 1 (m3 m− 2 h− 1), which is about 4 times the normal capacity of DAF-dissolved air flotation unit, the most used floater in wastewater treatment. Various metals (Cu, Ni, Pb, etc.) and molybdate ions present in synthetic and real effluent were successfully removed based on this colloidal adsorbing flotation principle. The process was also applied in a pilot scale to treat an industrial electroplating wastewater. Most of toxic metals (Cu, Ni and Zn) were reduced from initial concentrations of about of 2 to 10 mg L− 1, to below 0.5 to 1.0 mg L− 1, meeting local municipal discharge limits (but Cd ions). It is believed that flotation separation using medium-sized bubbles has great potential as a clean water and wastewater treatment technology.  相似文献   

19.
This study presents the results of chromate adsorption upon organically modified clinoptilolite obtained by the treatment of Bigadic clinoptilolite with surfactants in primary amine structure, namely 1-dodecylamine, 1-hexadecylamine and oleylamine. Natural and organo-clinoptilolites were characterized by X-ray diffraction, thermal gravimetry and Fourier transform infrared spectrometry which proved the integration of amine groups followed by the order oleylamine > 1-hexadecylamine > 1-dodecylamine. Organo-clinoptilolites were tested for their efficacy in chromate removal under base case conditions which implied 100 ppm initial concentration, pH 4.0, 10 g l?1 adsorbent dose and at 298 K. Results showed that amine loading induced chromate removal reaching up to 90 % for oleylamine-modified clinoptilolite. Experimentation was continued to determine the effects of pH, adsorbent dosage and initial concentration on chromate adsorption. Accordingly, maximum removal of 94.0 % was attained with 14 g l?1 of oleylamine-modified clinoptilolite, from Cr(VI) solution of 100 ppm initially at pH 3.0. Langmuir isotherm described the adsorption of chromate on oleylamine-modified clinoptilolite with 96.4 % consistency. Maximum theoretical uptake capacity was calculated as 6.72 mg g?1. Kinetic data were consistent with pseudo-second-order model with the controlling steps being film and pore diffusions.  相似文献   

20.
A fully automated semi-commercial flotation column incorporating state of the art instruments was designed to study the amenability of flotation column for the beneficiation of different minerals. In the present study, beneficiation of sillimanite was investigated by installing the flotation column in the flotation circuit of Orissa Sands Complex, Indian Rare Earths Limited, Chatrapur, Orissa. The effect of process parameters on sillimanite grade and recovery was investigated. At optimum conditions, the flotation column was operated continuously with a feed rate of one ton per hour and demonstrated the efficiency of the technology for the beneficiation of sillimanite. The results show that a concentrate assaying 96% sillimanite at 90% recovery can be obtained in a single column flotation stage.  相似文献   

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