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Tytuł artykułu

Removal of fine gangue minerals from Chador-malu iron concentrate using hydroseparator

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Phosphorus and silica are the main impurities of the Chador-malu iron ore which need to be reduced to the required values of 0.1 and 2%, respectively. The impurities in the final iron concentrate are mainly due to the presence of fine particles (less than 25 μm) of silica and apatite in the concentrates of magnetic separators and flotation circuits. In this study, the removal of very fine gangue minerals from iron concentrate of the Chador-malu processing plant was investigated using a laboratory hydroseparator. The laboratory-scale hydroseparator experiments were conducted under various operational conditions. The results showed that the silica and phosphorus contents of the flotation feed samples (less than 45 μm) decreased from 4.13% and 0.58% to 2.90 and 0.45%, respectively, while the iron grade increased from 59.5% to 63.5% by setting the effective parameters of the separator. The follow up flotation tests on the hydroseparator product resulted in an iron concentrate with silica and phosphorus contents of less than 2% and 0.04%, respectively. Moreover, its phosphorus content was reduced from 0.66% to 0.1% by desliming the final magnetic concentrate with hydroseparator. In this case, around 76% of phosphorus was removed.
Rocznik
Strony
250--263
Opis fizyczny
Bibliogr. 18 poz., rys., tab.
Twórcy
autor
  • Department of Mining and Metallurgical Engineering, Yazd University, Iran
autor
  • Department of Mining and Metallurgical Engineering, Yazd University, Iran
  • Mining Engineering Department, University of Sistan and Baluchestan, Iran
Bibliografia
  • AROL A. I., AYDOGAN A., 2004, Recovery enhancement of magnetite fines in magnetic separation, Colloids and Surfaces A: Physicochemical and Engineering Aspects, 232(2), 151-154.
  • BARRIOS G.F., 2009, Increasing the capacity of the grinding circuits without installing more mills, in The Fourth Southern African Conference on Base Metals, pp. 443-444 (The South African Institute of Mining and Metallurgy: South Africa).
  • BURT R., 1999, The role of gravity concentration in modern processing plants, Minerals Engineering, 12(11), 1291-1300.
  • DAS B., PRAKASH S., MOHAPATRA B.K., BHAUMIK S.K., NARASIMHAN K.S, 1992, Beneficiation of iron ore slimes using hydrocyclone, Mineral and Metallurgical Processing, 9, 101-103.
  • DAVID D., LARSON M., LI M. 2011, Optimizing Western Australia Magnetite Circuit Design, Metallurgical Plant Design and Operating Strategies, 552-562.
  • DRUMMOND R., NICOL S., SWANSON A., 2002, Teetered bed separators the Australian experience, Journal of the South African Institute of Mining and Metallurgy (South Africa), 102(7), 385-391.
  • LUTTRELL G.H., HONAKER R.Q., BRATTON R.C., WESTERFIELD T.C., KOHMUENCH J.N., 2006, In-plant testing of high-efficiency hydraulic separators, Virginia Polytech Inst St Univ. MARK M., 2012, Froth Flotation of Iron Ores, International Journal of Mining Engineering and Mineral Processing, 1(2), 56-61.
  • MCNAB B., JANKOVIC A., DAVID D., PAYNE P., 2009, Processing of magnetite iron ores–comparing grinding options, In Proceedings of Iron Ore 2009 Conference, Perth, Australia, pp. 27-29.
  • MURTHY N., BASAVARAJ K., 2012, Assessing the performance of a flotex density separator for the recovery of iron from low-grade Australian iron ore fines- A case study, XXVI International Mineral Processing Congress (IMPC).
  • RICHARDSON J.F., ZAKI W.N., 1954, Trans. Inst. Chem. Eng, 32, 35–53. ROCHA L., CANCADO R. Z.L., PERES A.E. C, 2010, Iron ore slimes flotation, Minerals Engineering, 23(11), 842-845.
  • SARKAR B., DAS A., MEHROTRA S.P., 2008, Study of separation features in floatex density separator for cleaning fine coal, International Journal of Mineral Processing, 86(1), 40-49.
  • SARKAR B, DAS A, ROY S.K, CHATTORAJ U.S, BHATTACHARYA N.K, BHATTACHARYA K.K, 2006, Optimization of teetered bed separator for alumina removal form iron ore fines, Proc. Workshop on Iron Ore Beneficiation, June 16–17, Jamshedpur, India, pp76–84.
  • SARKAR B., DAS A., ROY S., RAI S.K. 2008b, Characterization of and alumina removal from an iron ore fines of Indian origin using teetered bed separator, Miner. Proc. Ext. Met. (Trans IMMC), 117 (1), 48–55.
  • STAFEEV A.A. 2011, Iron-ore enrichment by magnetic hydroseparation, Steel in Translation, 41(10), 823-825. SUBRATA, R. 2009, Recovery improvement of fine iron ore particles by multi gravity separation, The Open Mineral Processing Journal 2, No. 14: 17-30.
  • SUNIL, K.T., MALLICH M.K., SINGH V., MURTHY M.R, 2013, Preliminary studies on teeter bed separator for separation of manganese fines, Powder Technology, 239, 284-289.
  • SURKOV A., SAMYKINA E., EPPELBAUM L., SEMENOV S., 2008, The main reason for mineral loss in gravity dressing, The Open Mineral Processing Journal, 1, 37-44.
  • THOMPSON P.D., GALVIN, K.P, 1997, An empirical description for the classification in an inclined counter-flow settler, Minerals Engineering, 10(1), 97-109.
  • TRIPATHY S.K., BHOJA S.K., KUMAR C.R., SURESH N, 2015, A short review on hydraulic classification and its development in mineral industry, Powder Technology, 270, 205-220. WILLS B.A., 2011, Wills' Mineral Processing Technology: An introduction to the practical aspects of ore treatment and mineral recovery, Butterworth-Heinemann.
Uwagi
Opracowanie ze środków MNiSW w ramach umowy 812/P-DUN/2016 na działalność upowszechniającą naukę (zadania 2017).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-f5595b03-b217-41a7-bf93-77db8b8dc9af
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