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| Content Provider | Springer Nature Link |
|---|---|
| Author | Gavrilescu, M. Roman, R. V. Tudose, R. Z. |
| Copyright Year | 1997 |
| Abstract | Liquid circulation superficial velocity and gas holdup behaviours were investigated in an external-loop airlift bioreactor of 0.170 m3 liquid volume in gas-induced and forced-circulation-loop operation modes, in the presence of static mixers made of corrugated stainless steel pieces, resulting in packets with the height-to-diameter ratio equal to unity and using non-Newtonian starch solutions as liquid phase. The static mixers were disposed in the riser in three blocks, each with three mixing packets, successively turned 90° to the adjacent mixing element. It was found that in the presence of static mixers and forced-loop operation mode, liquid circulation superficial velocity in the riser section was significantly diminished, while gas holdup increased in a great measure. It was considered that static mixers split the fluid into individual streams and break up the bubbles, resulting in small bubble sizes with a relative homogeneous bubble distribution over riser cross section. They act as supplementary resistances in liquid flow, reducing riser cross sectional area, equivalent with A D /A R area ratio diminishing. |
| Starting Page | 93 |
| Ending Page | 99 |
| Page Count | 7 |
| File Format | |
| ISSN | 0178515X |
| Journal | Bioprocess Engineering |
| Volume Number | 16 |
| Issue Number | 2 |
| e-ISSN | 16157605 |
| Language | English |
| Publisher | Springer-Verlag |
| Publisher Date | 1997-01-15 |
| Publisher Place | Berlin, Heidelberg |
| Access Restriction | One Nation One Subscription (ONOS) |
| Content Type | Text |
| Resource Type | Article |
| Subject | Applied Microbiology and Biotechnology Biotechnology |
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