Literature DB >> 35650455

Aerobic bioreactors: condensers, evaporation rates, scale-up and scale-down.

Magnus Ask1, Stuart M Stocks2.   

Abstract

OBJECTIVES: Hydrodynamics, mixing and shear are terms often used when explaining or modelling scale differences, but other scale differences, such as evaporation, can arise from non-hydrodynamic factors that can be managed with some awareness and effort.
RESULTS: We present an engineering approach to the prediction of evaporation rates in bioreactors based on gH2O/Nm3 of air entering and leaving the bioreactor and confirm its usefulness in a 28-run design of experiments investigating the effects of aeration rate (0.02 to 2.0 VVM), condenser temperature (10 to 20 °C), fill (2.5 to 5 kg), broth temperature (25 to 40 °C) and agitator speed (25 to 800 rpm). Aeration rate and condenser temperature used in the engineering prediction provided a practically useful estimate of evaporation; the other factors, while statistically identified as having some influence, were of negligible practical usefulness. Evaporation rates were never found to be zero, and could be at least 10% different to those expected at scale.
CONCLUSIONS: An assessment of evaporation rates for any project is encouraged, and it is recommended that the effects are accounted for by measurements, modelling or by tuning the exhaust cooling device temperature to minimize scale differences.
© 2022. The Author(s), under exclusive licence to Springer Nature B.V.

Entities:  

Keywords:  Bioreactors; Cell-culture; Evaporation; Fermentation; Scale-down; Scale-up

Mesh:

Year:  2022        PMID: 35650455     DOI: 10.1007/s10529-022-03258-7

Source DB:  PubMed          Journal:  Biotechnol Lett        ISSN: 0141-5492            Impact factor:   2.461


  8 in total

1.  Effect of Growth Rate on the Synthesis of Penicillin by Penicillium chrysogenum in Batch and Chemostat Cultures.

Authors:  S J Pirt; R C Righelato
Journal:  Appl Microbiol       Date:  1967-11

2.  The development of an industrial-scale fed-batch fermentation simulation.

Authors:  Stephen Goldrick; Andrei Ştefan; David Lovett; Gary Montague; Barry Lennox
Journal:  J Biotechnol       Date:  2014-11-01       Impact factor: 3.307

Review 3.  An Industrial Perspective on Scale-Down Challenges Using Miniaturized Bioreactors.

Authors:  Tannaz Tajsoleiman; Lisa Mears; Ulrich Krühne; Krist V Gernaey; Sjef Cornelissen
Journal:  Trends Biotechnol       Date:  2019-02-05       Impact factor: 19.536

4.  Application of a mechanistic model as a tool for on-line monitoring of pilot scale filamentous fungal fermentation processes-The importance of evaporation effects.

Authors:  Lisa Mears; Stuart M Stocks; Mads O Albaek; Gürkan Sin; Krist V Gernaey
Journal:  Biotechnol Bioeng       Date:  2016-09-26       Impact factor: 4.530

5.  Mathematical modelling of industrial pilot-plant penicillin-G fed-batch fermentations.

Authors:  J C Menezes; S S Alves; J M Lemos; S F de Azevedo
Journal:  J Chem Technol Biotechnol       Date:  1994-10       Impact factor: 3.174

6.  Euler-Lagrange computational fluid dynamics for (bio)reactor scale down: An analysis of organism lifelines.

Authors:  Cees Haringa; Wenjun Tang; Amit T Deshmukh; Jianye Xia; Matthias Reuss; Joseph J Heijnen; Robert F Mudde; Henk J Noorman
Journal:  Eng Life Sci       Date:  2016-09-14       Impact factor: 2.678

7.  A simple method to determine evaporation and compensate for liquid losses in small-scale cell culture systems.

Authors:  Vincent Wiegmann; Cristina Bernal Martinez; Frank Baganz
Journal:  Biotechnol Lett       Date:  2018-04-24       Impact factor: 2.461

  8 in total

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