1. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Schematic diagram of the experiment system: 1—compressed nitrogen cylinder; 2—manometer; 3—valves; 4—pressure maintaining valve; 5—rotameter; 6—Plexiglass square tank; 7—tripod; 8—lasers; 9—photodiodes; 10—sampling detector; 11— computer; and 12—CCD camera Figure Legend:

2. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Calibration curve of bubble terminal velocity in 93% Glycerin solution (uncertainty of data: ±2.1%) Figure Legend:

3. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Master curve of shifted CD based on 1.0% PAM (uncertainty of data: ±8.6%) Figure Legend:

4. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Master curve with shifted E based on 1.0% PAM (uncertainty of data:±6.9%) Figure Legend:

5. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Effect of bubble volume on bubble terminal velocity (uncertainty of data: ±7.8%) Figure Legend:

6. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Relationship between CD/Ar0.683 Eo−0.0931 and Re Figure Legend:

7. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Comparison between measured and predicted CD Figure Legend:

8. Date of download: 6/27/2016 Copyright © ASME. All rights reserved. From: An Experimental Investigation for Bubble Rising in Non-Newtonian Fluids and Empirical Correlation of Drag Coefficient J. Fluids Eng. 2010;132(2):021305-021305-7. doi:10.1115/1.4000739 Validity on present model in 93% glycerin solution Figure Legend: