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Reactive extraction of penicillin G in a pilot plant Karr-column

I. Model media

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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

  • Inoue K, Tsubonoue K, Nakamori I (1980) Extraction equilibrium of aqueous Phenol-long-chain alkylamine solution system. Sep Sci Technol 15: 1243–1254

    Google Scholar 

  • Müller B (1985) Reaktivextraktion von Penicillin in einer Technikumsanlage. Dissertation, Universität Hannover, FRG

    Google Scholar 

  • Reschke M, Schügerl K (1984a) Reactive Extraction of Penicillin. I. Stability of Penicillin G in the presence of Carriers and Relationships for Distribution Coefficients and Degrees of Extraction. The Chem/Biochem Eng J 28: B1-B9

    Google Scholar 

  • Reschke M, Schügerl K (1984b) Reactive Extraction of Penicillin. II. Distribution Coefficients and Degrees of Extraction. The Chem/Biochem Eng J 28: B11-B20

    Google Scholar 

  • Reschke M, Schügerl K (1984c) Reactive Extraction of Penicillin. III. Kinetics. The Chem/Biochem Eng J 29: B25-B29

    Google Scholar 

  • Reschke M, Schügerl K (1985) Continuous Reactive Extraction of Penicillin G in a Karr-Column. The Chem/Biochem Eng J 31: B19-B26

    Google Scholar 

  • Reschke M, Schügerl K (1986) Simulation of the Continuous Reactive Extraction of Penicillin G in a Karr-Column. The Chem/Biochem Eng J 32: B1-B5

    Google Scholar 

  • Teh CL, Prochazka J (1983) Reciprocating-Plate-Extraction Column. In: Teh CL, Baird MHI, Hanson C (eds) Handbook of Solvent Extraction. Wiley Interscience, New York, pp 373–389

    Google Scholar 

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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

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