Flotation column design is an area of reactor engineering that has not
attracted much research interest in chemical engineering. As a result
, key design and scale-up parameters (e.g. column height) continue to
be based on such factors as building and crane rail heights, both of w
hich are not related to the particle collection process [M. Ounpuu and
R. Tremblay, Investigation into the effect of column height on the 12
00 mm diameter column at Matagami, Proc. Int. Conf. on Column Flotatio
n, Sudbury, Ont., Canada, June 2-6,1991, Vol. 1, pp 303-316, J. B. Rei
s, Jr. and A. E. C. Peres, Industrial application of flotation columns
in the concentration of a sulfide ore at Mineracao Manati Ltd. - Braz
il, Proc. Int. Conf. on Column Flotation, Sudbury, Ont., Canada, June
2-6, 1991, Vol. 2, pp 525-537]. It is shown that the use of analogy wi
th chemical kinetics in column design is also not correct. By using an
alogy with interface mass transfer, a new approach to flotation column
design was presented [M. T. Ityokumbul, A new modelling approach to f
lotation column design. Miner. Eng., 5 (1992) 585-593]. This paper des
cribes the application of this technique in the optimal selection of c
olumn height. Literature data from a variety of applications (coal and
mineral flotation in columns of different sizes) are used to validate
the procedure.