Summary
Penicillin G was extracted from a model medium with a secondary amine (Amberlite LA-2) as carrier in n-butylacetate as solvent in a 7.6 m high pilot plant Karr-column at different stroke frequencies, throughput of the phases, concentrations of Penicillin G and carrier and ratios of the throughputs of the aqueous and organic phases. Up to penicillin concentrations of 30 gl−1, throughputs of the aqueous phase of 100 lh−1 and throughput ratios of the aqueous phase-to-organic phase of 3, very high degrees of extraction (99%) can be achieved with a penicillin loss below 1%.
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Abbreviations
- a:
-
specific interfacial area with regard to the volume of the continuous phase
- C:
-
partition coefficient
- cA, cA, i:
-
concentration of carrier (sec. amine) in the bulk at the interface
- cAHP, cAHP, i:
-
concentration of complex in the bulk at the interface
- cH:
-
proton concentration
- cHPa, cHPa,i :
-
concentration of free acid in the bulk of the aqueous phase at the interface
- cHPo, cHPo, i :
-
concentration of free acid in the bulk of the organic phase, at the interface
- cP, cP, i:
-
concentration of acid anions in the bulk of the aqueous phase, at the interface
- d32 :
-
Sauter droplet diameter
- E:
-
degree of extraction
- f:
-
stroke frequency
- KG:
-
reaction equilibrium constant
- Kphys :
-
distribution coefficient
- N:
-
number of stages in cascade
- t:
-
mean residence time of the aqueous phase
- \(\dot V\) aq :
-
throughput of the aqueous phase
- \(\dot V\) o :
-
throughput of the organic phase
- Z:
-
dimensionless longitudinal coordinate of the column with regard to its active length (4 m)
- ɛ:
-
holdup of the organic phase
References
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Reschke M, Schügerl K (1984c) Reactive Extraction of Penicillin. III. Kinetics. The Chem/Biochem Eng J 29: B25-B29
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Müller, B., Schlichting, E., Bischoff, L. et al. Reactive extraction of penicillin G in a pilot plant Karr-column. Appl Microbiol Biotechnol 26, 36–41 (1987). https://doi.org/10.1007/BF00282146
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DOI: https://doi.org/10.1007/BF00282146