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. 2022 Mar 4;7(10):9061–9070. doi: 10.1021/acsomega.2c00313

Table 1. Comparison of Gas Dispersion Parameters in Different Flotation Devices.

flotation devices experimental reagents methods maximum gas holdup (%) D32 (mm)
flotation column9 MIBC = 0.11 mmol/L; F150 = 0.05 mmol/L McGill bubble viewer; differential-pressure method 9.8; 13.4 1.1; 0.7
continuous bubble column47 hexanol/PO molar mixing ratio = 1/0.1, 60 ppm McGill bubble size analyzer; conductivity method 11.9 1.0
cyclone-static microbubble flotation column48 P = 0.34 MPa; Qg = 2.50 m3/h; pine oil = 10, 15, 20 mg/L; D = 6 mm differential-pressure method 12.14; 12.54; 12.8  
column flotation cell49 Jg = 1.47 cm/s; MIBC = 10, 20, 30 ppm differential-pressure method 9; 13; 18 2.06–1.04;
downflow column13 MIBC = 8.1 mg/L; Jg = 1.32 cm/s viewing system; drainage method 21 0.65
industrial flotation cell50 freon 13B1 as gas tracer local gas holdup measurement 8.8  
laboratory Denver flotation cell44 MIBC = 22.4 ppm; Jg = 0.9 cm/s; impeller peripheral speed = 4, 5, 6 m/s McGill bubble viewer; drainage method 8; 13; 24 0.43–0.11