Extracting silica and alumina from low-grade bauxite
The unit shown schematically in Figure 4 is designed for the agitation leaching procedure. Finely ground (-2 mm) calcined bauxite was dosed from a bunker by feeder to a rod mill (L = 3 m, D = 1 m) revolving at 32 rpm. Initially, the heated alkali solution at 90-95[degrees]C was fed to the mill with...
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Veröffentlicht in: | JOM (1989) 2003-08, Vol.55 (8), p.47-50 |
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Hauptverfasser: | , , , |
Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | The unit shown schematically in Figure 4 is designed for the agitation leaching procedure. Finely ground (-2 mm) calcined bauxite was dosed from a bunker by feeder to a rod mill (L = 3 m, D = 1 m) revolving at 32 rpm. Initially, the heated alkali solution at 90-95[degrees]C was fed to the mill with pump and batcher. The alkali-bauxite slurry with a liquid-to-solid ratio of 5:1 was delivered into two in-line stirrers by pumps. |
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ISSN: | 1047-4838 1543-1851 |
DOI: | 10.1007/s11837-003-0105-z |