Abstract：
:A Tubular Liquid Film Reactor was designed as a model system to transfer a batch culture kinetic to a continuous cascade. Cell density, product formation and substrate consumption rates were followed during fermentation at two dilution rates. In spite of the high dilution rates effective in each segment by itself high cell densities of up to 10(7) cells/ml were achieved due to cell sedimentation. The model character of the reactor was taken to determine critical values of substrate concentrations that influence production rates and result in an adaptation of metabolism.
journal_name
Cytotechnologyjournal_title
Cytotechnologyauthors
Borth N,Steindl F,Weigang F,Reiter M,Katinger Hdoi
10.1007/BF00365489subject
Has Abstractpub_date
1990-05-01 00:00:00pages
253-8issue
3eissn
0920-9069issn
1573-0778journal_volume
3pub_type
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