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Mixing characteristics of external-loop airlifts: non-Newtonian systems

✍ Scribed by Milan K. Popović; Campbell W. Robinson


Publisher
Elsevier Science
Year
1993
Tongue
English
Weight
932 KB
Volume
48
Category
Article
ISSN
0009-2509

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✦ Synopsis


Mixing time (0) was measured in a 45 or 60 1 working liquid volume external-circulation-loop airlift (ECL-AL) fermentor, and in a geometrically similar 6 1 prototype, both equipped with perforatedplate spargers (1 mm dia. holes). Carboxymethyleellulose solutions were used to simulate the rheological behaviour of non-Newtonian fermentation broths. The specific mixing time (f?/V) is shown to be highly dependent on the dispersion height and gas superficial velocity in the riser section, as well as on the riser diameter and the effective viscosity of the liquid phase. In the range studied (0.111 Q AD/AI, G 0.46). the downcomer-to-riser cross-sectional-area ratio has a relatively minor effect on 0/V. The superficial velocity of the circulating liquid in the riser (I+~) was also measured. The results have been combined with those of a previous investigation, by PopoviC and Robinson, to better elucidate the effect of dispersion height on the rate of liquid circulation. A modified correlation of uLn is presented and discussed.


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Effect of scale-up on average shear rate
✍ Waheed A. Al-Masry 📂 Article 📅 1999 🏛 John Wiley and Sons 🌐 English ⚖ 236 KB 👁 2 views

Average shear rates have been estimated experimentally in a 700-dm 3 external loop airlift reactor. Aqueous pseudoplastic carboxymethylcellulose and xanthan gum solutions were used to simulate non-Newtonian behavior of biological media. Average shear rates of non-Newtonian solutions were found by an