Question
Scale-up of Pilot Plant Tests of a Reciprocating-Plate Extraction Column The pilot plant data in Table P6.9 are for the extraction of an antibiotic from
Scale-up of Pilot Plant Tests of a Reciprocating-Plate Extraction Column
The pilot plant data in Table P6.9 are for the extraction of an antibiotic from whole fermentation broth using the solvent chloroform in a reciprocating-plate extraction column. The concentration of the antibiotic was 1.4 g/liter in the broth. The column had a diameter of 2.54 cm, and the height of the plates was 3.05 m. The partition coefficient K for the antibiotic is known to be 2.68. For each pilot run, determine the diameter and height of the plates for the plant column that would be required for processing 50 000 liters of broth in 12 h to give an exit raffinate concentration of antibiotic of 10 mg/liter, assuming a concentration of antibiotic in the feed broth of 1.0 g/liter (a spreadsheet is convenient for these calculations). Without doing a complete economic analysis, in your judgment which scaled-up pilot run appears to be optimum? (Data from A. E. Karr, W. Gebert, and M. Wang, Can. J. Chem. Eng., vol. 58, p. 249, 1980.)
Run number | Flow rates (mL min1) | Antibiotic concentration in raffinate (mg L1) | |
Broth | Chloroform | ||
1 | 45 | 135 | 2 |
2 | 67.5 | 135 | 3 |
3 | 125 | 135 | 30 |
4 | 80 | 120 | 5 |
5 | 100 | 150 | 7 |
6 | 120 | 180 | 9 |
7 | 150 | 225 | 25 |
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