Get a fix on high-shear mixing

Chemical Engineering Progress

Volumn 95, Issue 11, 1999, Pages 33-42

  Myers, Kevin J ^a,b,c,d,e   Reeder, Mark F ^b,f,g,h,i   Ryan, David ^a,b,j,k,l   Daly, Geoff ^b,j,m,n,o,p  

^a UNIVERSITY OF DAYTON   (United States)

^b Chemineer Inc   (United States)

^c University of Dayton   (United States)

^d WASHINGTON UNIVERSITY   (United States)

^e AMERICAN SOCIETY FOR ENGINEERING EDUCATION   (United States)

^f R and D Laboratory

^g WEST VIRGINIA UNIVERSITY   (United States)

^h OHIO STATE UNIVERSITY   (United States)

ⁱ NASA Glenn   (United States)

^j Chemineer Inc   (United States)

^k PURDUE UNIVERSITY   (United States)

^l AIChE   (United States)

^m Jaygo Inc

ⁿ London Borough Polytech ^*  (United Kingdom)

^o LONDON SOUTH BANK UNIVERSITY   (United Kingdom)

^p Institute of Industrial Engineers

more..

Author keywords

[No Author keywords available]

Indexed keywords

EID: 0003265342     PISSN: 03607275     EISSN: None     Source Type: Trade Journal    
DOI: None     Document Type: Article

References (16)

1. Meili, M., "Use of High Shear Equipment in Industry," paper presented at Mixing XV, The 15th Biennial North American Mixing Conference, (sponsored by AlChE, New York), Banff, Alberta, Canada (June 18-23, 1995).
2. Etchells, A. W., "Preliminary Theories of High Shear Mixing," paper presented at Mixing XV, The 15th Biennial North American Mixing Conference, (sponsored by AlChE, New York), Banff, Alberta, Canada (June 18-23, 1995).
3. Myers, K., et al., "Agitating for Success," The Chem. Eng., No. 620, pp. 39-42 (Oct. 10, 1996).
4. Fondy, P. L., and R. L. Bates, "Agitation of Liquid Systems Requiring a High Shear Characteristic," AIChE J., 9 (3), pp. 338-342 (Mar. 1963).
5. Myers, K. J., et al., "Avoid Agitation by Selecting Static Mixers," Chem. Eng. Progress, 93 (6), pp. 28-38 (June 1997).
6. Fasano, J. B., et al., "Advanced Impeller Geometry Boosts Liquid Agitation," Chem. Eng., 101 (8), pp. 110-116 (Aug. 1994).
7. Bakker, A., and L. E. Gates, "Properly Choose Mechanical Agitators for Viscous Liquids." Chem. Eng. Progress, 91 (12), pp. 25-34 (Dec. 1995).
8. Zhou, G., and S. M. Kresta, "Distribution of Energy Between Convective and Turbulent Flow for Three Frequently Used Impellers," Trans. Instit. Chem. Engineers, 74, Part A, pp. 379-389 (1996).
9. Edwards, M. F., et al, "Mixing of Liquids in Stirred Tanks," Chapter 8 in "Mixing in the Process Industries," 2nd ed., N. Harnby, M. F. Edwards, and A. W. Nienow, eds., Butterworth-Heinemann, Oxford, U.K. (1992).
10. Fasano, J. B., and W. R. Penney, "Avoid Blending Mix-Ups," Chem. Eng. Progress, 87 (10), pp. 56-63 (Oct. 1991).
11. Myers, K., et al., "Power Draw Characteristics of a High Shear Homogenizer," paper presented at Mixing XVII, The 17th Biennial North American Mixing Conference, (sponsored by AIChE, New York), Banff, Alberta, Canada (Aug. 15-20, 1999).
12. Parfitt, G. D., and H. A. Barnes, "The Dispersion of Fine Particles in Liquid Media," Chapter 6 in "Mixing in the Process Industries," 2nd ed., N. Harnby, M. F. Edwards, and A. W. Nienow, eds., Butterworth-Heinemann, Oxford, U.K. (1992).
13. Ayazi Shamlou, P., and N. Titchener-Hooker, "Turbulent Aggregation and Breakup of Particles in Stirred Vessels," Chapter 1 in "Processing of Solid-Liquid Suspensions," P. Ayazi Shamlou, ed., Butterworth-Heinemann, Oxford, U.K. (1993).
14. Calabrese, R. V., et al., "Drop Breakup in Turbulent Stirred-Tank Contactors, Part III: Correlations for Mean Size and Drop Size Distributions," AIChE J., 32 (4), pp. 677-681 (Apr. 1986).
15. Grace, H. P., "Dispersion Phenomena in High Viscosity Immiscible Fluid Systems and Application of Static Mixers as Dispersion Devices in Such Systems," Chem. Eng. Communications, 14, pp. 225-277 (1982).
16. Beck, K., "Drop Break-Up Using a Sawtooth Impeller," paper presented at Mising XVI. The 16th Biennial North American Mixing Conference, (sponsored by AIChE, New York), Williamsburg, VA (June 22-27, 1997).