Mixing with helical ribbon agitators: Part II. Newtonian Fluids

✍ Scribed by W. Ian Patterson; P. J. Carreau; C. Y. Yap

• Publisher: American Institute of Chemical Engineers
• Year: 1979
• Tongue: English
• Weight: 939 KB
• Volume: 25
• Category: Article
• ISSN: 0001-1541
• DOI: 10.1002/aic.690250317

✦ Synopsis

Abstract

Of necessity, the mixing process is sometimes restricted to the laminar regime, although turbulent mixing is generally more desirable. Common examples of laminar mixing are found when the fluid has a very high viscosity, or when one of the mixture components is shear sensitive. It has been pointed out that the helical ribbon agitator (HRA) is admirably suited to the low Reynolds number mixing process. This work derives a model to predict the power consumption of the HRA. The model has been developed with the aid of experimental data and tested extensively using literature data. For a wide range of mixer geometries and sizes, it predicts power consumption with an average deviation of 13%.

The concept of relative efficiency of mixers is also described as an aid to comparing different HRA mixer geometries. Finally, the problem of scale‐up of different HRA configurations is discussed.