Abstract
A feedback-controlled fed-batch process for the recombinant production of a soluble human β-1,4-galactosyltransferase (NdrGal-T) with Saccharomyces cerevisiae was developed and scaled up to the pilot scale. A 5000 U NdrGal-T fermentation run was performed on a 300 l scale. Indirect feedback control of the glucose feeding with RQ data at a set-point of RQ = 1.1 resulted in higher NdrGal-T activities (30 U/l) than direct feedback control of glucose with on-line flow-injection analysis (9 U/l). This increase in final activity of NdrGal-T by a factor of 42 compared to published data makes the fed-batch production of glycosyltransferases with a Saccharomyces cerevisiae expression system competitive with cell-culture systems.
Published Version
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