Use of residence-time distribution techniques to analyze industrial-scale froth-flotation circuits

Author:

Dowling E. C.,Arnold B. J.,Klimpel R. R.,Apian F. F.

Publisher

Springer Science and Business Media LLC

Subject

Materials Chemistry,Metals and Alloys,Mechanical Engineering,Geotechnical Engineering and Engineering Geology,General Chemistry,Control and Systems Engineering

Reference24 articles.

1. Arnold, B.J., 1989, “Flotation Rate and Residence Time Distribution in Continuous Coal Froth Flotation Circuits and an Evaluation of Reagents and Circuit Variations for Pyritic Removal,” Ph.D. Dissertation, The Pennsylvania State University, 361 pp.

2. Arnold, B.J., 1993, “The froth factor and what it tells you about your coal flotation circuit,” Flotation Plants: Are They Optimized, D. Malhotra, ed., Chapter 19, SME, Littleton, CO, pp. 123–134.

3. Bull, W.R., and Spottiswood, D.J., 1974, “A study of mixing flow patterns in a bank of flotation cells,” Colorado School of Mines Quarterly, Vol. 69, pp. 1–26.

4. Cholette, A., and Cloutier, L., 1959, “Mixing efficiency determinations for continuous flow systems,” Can. J. Chem. Eng., Vol. 37, pp. 105–112.

5. Dinsdale, J.D., and Berube, Y., 1972, “A characterization of hydrodynamics in a 700-cu ft Maxwell flotation cell,” Can. Met. Q., Vol. 11, pp. 507–513.

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