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Beneficiation of a low grade limestone sample 被引量:1

Beneficiation of a low grade limestone sample
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摘要 Pilot scale column flotation studies were conducted on a low grade siliceous limestone ore. Silica content was reduced to less than 1% in the concentrate so that it became satisfactory for use in the paper or rub- ber industries. The limestone sample was crystalline and constituted primarily of calcite that contained quartz, feldspar, pyroxene, and biotite as gangue minerals. Quartz is the major silicate gangue whereas feldspar, pyroxene, and biotite exist in minor to trace quantities. Traces of pyrite were also observed within the sample. A reverse flotation process was adopted where the silicate gangue minerals were floated using two different commercial cationic collectors: Chem-750 F or Floatamine-D. The studies clearly suggest it is possible to produce a limestone concentrate assaying around 96-97% CaCO3 contain- ing less than 1% SiO2. The effect of feed flow rate, percent solids, froth depth, and wash water on the grade and recovery of the CaCO3 concentrate is discussed. Pilot scale column flotation studies were conducted on a low grade siliceous limestone ore. Silica content was reduced to less than 13g in the concentrate so that it became satisfactory for use in the paper or rubber industries. The limestone sample was crystalline and constituted primarily of calcite that contained quartz, feldspar, pyroxene, and biotite as gangue minerals. Quartz is the major silicate gangue whereas feldspar, pyroxene, and biotite exist in minor to trace quantities. Traces of pyrite were also observed within the sample. A reverse flotation process was adopted where the silicate gangue minerals were floated using two different commercial cationic collectors: Chem-750 F or Floatamine-D. The studies clearly suggest it is possible to produce a limestone concentrate assaying around 96-97% CaCO3 containing less than 1 % Si02. The effect of feed flow rate, percent solids, froth depth, and wash water on the grade and recovery of the CaC03 concentrate is discussed.
出处 《Mining Science and Technology》 EI CAS 2011年第5期631-636,共6页 矿业科学技术(英文版)
关键词 低品位石灰石 样品 选矿 二氧化硅含量 精矿品位 脉石矿物 反浮选工艺 CAC03 Low grade limestoneReverse flotationColumn flotationCationic collector
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  • 1TAO Daniel,HONAKER Rick.Nanobubble generation and its applications in froth flotation(part Ⅱ):fundamental study and theoretical analysis[J].Mining Science and Technology,2010,20(2):159-177. 被引量:29
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同被引文献48

  • 1Luttrell G H;Yoon R H.A hydrodynamic model for bubble-particle attachment,1992(154).
  • 2Weber M E;Paddock D.lnterceptional and gravitational collision efficiencies for single collectors at intermediate Reynolds numbers,1983(94).
  • 3Weber M E.Collision efficiencies for small particles with a spherical collector at intermediate Reynolds numbers,1981(02).
  • 4Gaudin A M.Flotation:2nd Edition,1957.
  • 5Sutherland K L.Physical chemistry of flotation:XI kinetics of the flotation process,1949(52).
  • 6Kitchener J A.Colloid Chemistry in Mineral Processing,1992.
  • 7Crawford R;Ralston J.The influence of particle size and contact angle in mineral flotation,1988(23).
  • 8Finch J A;Dobby G S.Column Flotation,1990.
  • 9Arbiter N;Steinenger J.Hydronamics of Flotation Machine:Mineral Processing,1965.
  • 10Sun S;Zimmerman R E.The mechanism of coarse coal and mineral froth flotation,1950(05).

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