Hostname: page-component-78c5997874-ndw9j Total loading time: 0 Render date: 2024-11-05T15:43:48.480Z Has data issue: false hasContentIssue false

Thickening Flocculated Kaolinite Slurries in the Nozzle Discharge, Multidisc, Bowl Centrifuge

Published online by Cambridge University Press:  09 July 2018

R. E. Brociner
Affiliation:
Research Laboratories, English Clays Lovering Pochin & Co. Ltd, St Austell
E. C. Vollans
Affiliation:
Research Laboratories, English Clays Lovering Pochin & Co. Ltd, St Austell

Abstract

Three semi-empirical equations are derived to characterize the performance of the nozzle discharge centrifuge as a thickener for flocculated kaolinite slurries. The first equation relates mass throughput to machine size and speed, the number and size of nozzles and the product concentration. The second equation relates the maximum clear effluent rate to the settling characteristics of the slurry and to machine parameters. The third equation relates power consumption to product and effluent rates and to machine parameters. Finally a numerical example of the use of the equations is given.

Type
Research Article
Copyright
Copyright © The Mineralogical Society of Great Britain and Ireland 1973

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Ambler, C.M. (1952) Chem. Eng. Proc. 48, 150.Google Scholar
Coe, H.S. & Clevenger, G.H. (1970) Trans. Am. Inst. Min. Engrs. 55, 356.Google Scholar
Coulson, J.M. & Richardson, J.F. (1955) Chemical Engineering, Vol. 2, pp. 459 and 514. McGraw-Hill Book Company Inc., New York and London.Google Scholar
Gwilliam, R.D. (1971) Filtr. Separ. 8, No. 2, 181.Google Scholar
Murkes, J. (1966) Filtr. Separ. 3, No. 2, 112.Google Scholar