Abstract
The behavior of a liquid-pulsated, sieve-plate extraction column during start-up and following a disturbance was studied numerically using a mathematical model of such a column, and experimentally with the systems toluene-acetone-water and MIBK-acetic acid-water. The flooding-point curves, both with and without mass transfer, and the efficiency of mass transfer in both directions were determined.
| Original language | English |
|---|---|
| Pages (from-to) | 214-226 |
| Number of pages | 13 |
| Journal | International chemical engineering |
| Volume | 24 |
| Issue number | 2 |
| State | Published - 1984 |