Abstract

Abstract A novel method for the integrated gravity separation of sophorolipid from a fermentation broth has been developed, enabling removal of a sophorolipid phase of either higher or lower density than the bulk fermentation broth, while cells and other media components are recirculated and returned to the bioreactor. The capability of the separation system to recover an enriched sophorolipid product phase was demonstrated on three sophorolipid producing fed batch fermentations using Candida bombicola, giving an 11% reduction in fermenter volume required whilst maintaining sophorolipid production. Sophorolipid recoveries of up to 86% (280 g) of the total produced over a whole fermentation were achieved at an enrichment of up to 9. Furthermore, the broth viscosity reduction achieved by removal of the sophorolipid phase enabled a 34% reduction in mixing power to maintain the same dissolved oxygen level by the end of the fermentation, with a 9% average reduction over the course of the fermentation. Fermentation duration could be extended to 1023 h, allowing production of 623 g sophorolipid from 1 l initial batch volume. These benefits could lead to a substantial decrease in the cost of sophorolipid production, making high volume applications such as enhanced oil recovery economically feasible.

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