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Biotechnology and Bioengineering, Vol.43, No.6, 439-445, 1994
Extraction of Cephalosporin-C from Whole Broth and Separation of Desacetyl Cephalosporin-C by Aqueous 2-Phase Partition
Cephalosporin C was extracted from diluted or whole broth by PEG/salt aqueous two-phase systems. Parameters such as PEG molecular weight, salt type, pH, and salt concentration were investigated for finding a suitable extraction system. In PEG 600/ammoninum sulfate or phosphate systems, K-c (partition coefficient of cephalosporin C) was observed to be larger than 1, with K-d (partition coefficient of desacetyl cephalosporin C) being smaller than 1. The particular values of these coefficients would imply that the difficult separation of cephalosporin C and desacetyl cephalosporin C could possibly be achieved via the aqueous two-phase extraction. The addition of surfactants, water-miscible solvents, and neutral salts for enhancement of the separation efficiency was also investigated. The addition of surfactants to the system did not affect the separation efficiency substantially. K-c would increase whereas K-d decreased as a result of the addition of acetone, MeOH, EtOH, IPA, and n-BuOH. Meanwhile both K-c and K-d would decrease whenever neutral salts, NaCl, KCI, Kl, or KSCN, were added. The partitioning behavior of cephalosporin C and desacetyl cephalosporin C in filtered, whole, and different batches of broth was notably quite similar to that of diluted broth. The recovery yield of cephalosporin C in whole broth extraction was observed to be a function of centrifugal force used in phase separation.
Keywords:2-PHASE SYSTEMS;REACTIVE EXTRACTION;ESCHERICHIA-COLI;FERMENTATION;PROTEINS;GALACTOSIDASE;VANCOMYCIN;RECOVERY;BIOMASS