About

Log in?

DTU users get better search results including licensed content and discounts on order fees.

Anyone can log in and get personalized features such as favorites, tags and feeds.

Log in as DTU user Log in as non-DTU user No thanks

DTU Findit

Conference paper · Book chapter

Model-based process development for a continuous lactic acid bacteria fermentation

From

Department of Chemical and Biochemical Engineering, Technical University of Denmark1

PROSYS - Process and Systems Engineering Centre, Department of Chemical and Biochemical Engineering, Technical University of Denmark2

PILOT PLANT, Department of Chemical and Biochemical Engineering, Technical University of Denmark3

Chr. Hansen AS4

A mechanistic process model describing a lactic acid bacteria (LAB) fermentation was applied to develop a continuous fermentation process. Producing LAB for the dairy industry in a continuous cultivation, which would allow harvesting the cells during the cultivation, would reduce production costs compared to traditional batch processes.

To this end, a validated mechanistic model of a Streptococcus thermophilus fermentation was used for a model-based continuous process evaluation. The fermentation model consists of biological and chemical mechanisms including a description of the growth rate as a function of pH and inhibition effects of metabolites.

The optimal dilution rate and substrate concentration in the feed were estimated in order to maximize the cell yield (biomass concentration) and to minimize the waste of substrate during the continuous fermentation in a 50 m3 bioreactor for two scenarios: downstream capabilities are i) flexible, and ii) fixed.

The biomass concentration is restricted by the growth-inhibiting lactic acid concentration, which is produced by the growing bacteria. Furthermore, the substrate, which is supplied by the feed, should be consumed completely in the fermentation and not wasted in the bioreactor effluent owing to raw material costs.

The resulting non-linear optimization problem was formulated and solved in MATLAB®. A Monte Carlo simulation showed the robustness of the results, where a biomass concentration of 5 g L-1 could be achieved in the continuous fermentation with a substrate wastage of less than 3 % in the bioreactor effluent.

The productivity of the continuous process was similar to a traditional batch process, but frequent cleaning and sterilization are no longer necessary in a continuous process resulting in a shorter unproductive downtime of the bioreactors. This promising potential of a continuous process for LAB cultivations encourages pilot-scale studies for a comprehensive techno-economic evaluation.

Language: English
Publisher: Elsevier
Year: 2018
Pages: 1601-1606
Proceedings: 28th European Symposium on Computer Aided Process Engineering (Escape 28)
Series: Computer Aided Chemical Engineering
ISBN: 0444642358 , 0444642366 , 9780444642356 and 9780444642363
ISSN: 15707946
Types: Conference paper and Book chapter
DOI: 10.1016/B978-0-444-64235-6.50279-5
ORCIDs: Spann, Robert , Eliasson Lantz, Anna , Gernaey, Krist V. and Sin, Gürkan

DTU users get better search results including licensed content and discounts on order fees.

Log in as DTU user

Access

Analysis