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@ARTICLE{Habicher:874872,
author = {Habicher, Tobias and Rauls, Edward K. A. and Egidi,
Franziska and Keil, Timm and Klein, Tobias and Daub, Andreas
and Büchs, Jochen},
title = {{E}stablishing a {F}ed‐{B}atch {P}rocess for {P}rotease
{E}xpression with {B}acillus licheniformis in
{P}olymer‐{B}ased {C}ontrolled‐{R}elease {M}icrotiter
{P}lates},
journal = {Biotechnology journal},
volume = {15},
number = {2},
issn = {1860-7314},
address = {Weinheim},
publisher = {Wiley-VCH},
reportid = {FZJ-2020-01677},
pages = {1900088 -},
year = {2020},
abstract = {Introducing fed‐batch mode in early stages of development
projects is crucial for establishing comparable conditions
to industrial fed‐batch fermentation processes. Therefore,
cost efficient and easy to use small‐scale fed‐batch
systems that can be integrated into existing laboratory
equipment and workflows are required. Recently, a novel
polymer‐based controlled‐release fed‐batch microtiter
plate is described. In this work, the polymer‐based
controlled‐release fed‐batch microtiter plate is used to
investigate fed‐batch cultivations of a protease producing
Bacillus licheniformis culture. Therefore, the oxygen
transfer rate (OTR) is online‐monitored within each well
of the polymer‐based controlled‐release fed‐batch
microtiter plate using a µRAMOS device. Cultivations in
five individual polymer‐based controlled‐release
fed‐batch microtiter plates of two production lots show
good reproducibility with a mean coefficient of variation of
$9.2\%.$ Decreasing initial biomass concentrations prolongs
batch phase while simultaneously postponing the fed‐batch
phase. The initial liquid filling volume affects the
volumetric release rate, which is directly translated in
different OTR levels of the fed‐batch phase. An increasing
initial osmotic pressure within the mineral medium decreases
both glucose release and protease yield. With the volumetric
glucose release rate as scale‐up criterion, microtiter
plate‐ and shake flask‐based fed‐batch cultivations
are highly comparable. On basis of the small‐scale
fed‐batch cultivations, a mechanistic model is established
and validated. Model‐based simulations coincide well with
the experimentally acquired data.},
cin = {IEK-14},
ddc = {570},
cid = {I:(DE-Juel1)IEK-14-20191129},
pnm = {134 - Electrolysis and Hydrogen (POF3-134)},
pid = {G:(DE-HGF)POF3-134},
typ = {PUB:(DE-HGF)16},
pubmed = {pmid:31471944},
UT = {WOS:000511444500003},
doi = {10.1002/biot.201900088},
url = {https://juser.fz-juelich.de/record/874872},
}