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Krofta M, Wang LK (1999) Flotation and related adsorptive bubble separation processes, 4th edn. Technical Manual No. Lenox 7–25–1999/348. Lenox Institute of Water Technology, Lenox, MA 16. Ata S, Jameson GJ (2005) The formation of bubble clusters in flotation cells. Int J Miner Process 76:1–2 17. Gelinas S, Finch JA (2005) Colorimetric determination of common industrial frothers. Miner Eng 18:2 18. Yapijakis C, Wang LK (2004) Treatment of soap and detergent industry wastes. ) Handbook of industrial and hazardous wastes treatment.

7. 8). Hydraulic loading is also a common design parameter. If one looks carefully at the units used (gal/min/ft2) and converts them to a common basis (ft3/ft2/min), by canceling one obtains units of ft/min, which is equivalent to the velocity expression reported as the rise rate. 7). What has happened, of course, is the bubbles are markedly slowed by their inclusion in the floc and interference (collision) with each other in rising. K. F. Bennett Fig. 5. Rise rate of air bubbles in tap water. 27 Principles of Air Flotation Technology 13 Ramirez (42) noted that the actual rise rate of bubbles greater in size than 150 mm is considerably faster than predicted by Stoke’s Law (Fig.

Humana Press, Totowa, NJ, pp 347–362 15. Krofta M, Wang LK (1999) Flotation and related adsorptive bubble separation processes, 4th edn. Technical Manual No. Lenox 7–25–1999/348. Lenox Institute of Water Technology, Lenox, MA 16. Ata S, Jameson GJ (2005) The formation of bubble clusters in flotation cells. Int J Miner Process 76:1–2 17. Gelinas S, Finch JA (2005) Colorimetric determination of common industrial frothers. Miner Eng 18:2 18. Yapijakis C, Wang LK (2004) Treatment of soap and detergent industry wastes.

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