Abstract
The helical flow promoter (HFP), inserted in the downcomer of an airlift reactor (ALR), generates a helical flow pattern in the circulating gas-liquid (solid) mixture. Data on the fluidization capacity, gas holdup, liquid velocity and mass transfer rate for two- and three-phase systems with two different carboxymethylcellulose solutions collected in a 58 L ALR-HFP are presented and compared with those of common pneumatic reactors. Generally, an increasing solid concentration led to a slight decrease in gas holdup and liquid velocity but to a considerable decrease in mass transfer rates. Insertion of HFPs produced a significantly enhanced fluidization capacity of solid particles compared to the common systems.
| Original language | English |
|---|---|
| Pages (from-to) | 804-810 |
| Number of pages | 7 |
| Journal | Canadian Journal of Chemical Engineering |
| Volume | 77 |
| Issue number | 5 |
| DOIs | |
| State | Published - 1 Jan 1999 |
Keywords
- Airlift reactor
- Gas holdup
- Liquid velocity
- Mass transfer
- Three-phase
ASJC Scopus subject areas
- General Chemical Engineering