@misc{Leśniak_Władysław_Comparative_1993,
 author={Leśniak, Władysław and Pietkiewicz, Jerzy and Podgórski, Waldemar},
 volume={22},
 number={3},
 copyright={Creative Commons Attribution BY-SA 4.0 license},
 journal={Biotechnologia, vol.22, 3 (1993)-.},
 howpublished={online},
 year={1993},
 publisher={Committee on Biotechnology PAS},
 publisher={Institute of Bioorganic Chemistry PAS},
 language={pol},
 abstract={The mixing and mass transfer have been investigated in industrial bioreactors of capacity10, 30, 50 and 150 m^ used for citric acid fermentation. Hydrodynamic parameters were examined on water using mineral acid as a trace. Volumetric mass transfer coefficient (kLa) wasdetermined by balance method. It was found that the examined bioreactors have similarhydrodynamic parameters despite their different capacities. The differences were found in maximum values of kj^a (from 150 to 200 h~^) which coresponded to the citric acid yield and productivity.},
 title={Comparative characteristic of bioreactors used for citric acid biosynthesis in industrial scale},
 type={Text},
 URL={http://rcin.org.pl/Content/154156/PDF/POZN271_188397_biotechnologia-1993-no3-lesniak.pdf},
 keywords={biotechnology},
}