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

被引:1
作者
Ask, Magnus [1 ]
Stocks, Stuart M. [2 ]
机构
[1] Novo Nordisk AS, Malov, Denmark
[2] LEO Pharma AS, Ballerup, Denmark
关键词
Bioreactors; Cell-culture; Evaporation; Fermentation; Scale-down; Scale-up; FED-BATCH FERMENTATION; MECHANISTIC MODEL; PENICILLIN; TOOL;
D O I
10.1007/s10529-022-03258-7
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
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 gH(2)O/Nm(3) 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 degrees C), fill (2.5 to 5 kg), broth temperature (25 to 40 degrees 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.
引用
收藏
页码:813 / 822
页数:10
相关论文
共 14 条
  • [1] BAJPAI RK, 1980, J CHEM TECHNOL BIOT, V30, P332
  • [2] A modular simulation package for fed-batch fermentation:: penicillin production
    Birol, G
    Ündey, C
    Çinar, A
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (11) : 1553 - 1565
  • [3] Flow-following sensor devices: A tool for bridging data and model predictions in large-scale fermentations
    Bisgaard, Jonas
    Muldbak, Monica
    Cornelissen, Sjef
    Tajsoleiman, Tannaz
    Huusom, Jakob K.
    Rasmussen, Tue
    Gernaey, Krist, V
    [J]. COMPUTATIONAL AND STRUCTURAL BIOTECHNOLOGY JOURNAL, 2020, 18 : 2908 - 2919
  • [4] BOLTON D, 1980, MON WEATHER REV, V108, P1046, DOI 10.1175/1520-0493(1980)108<1046:TCOEPT>2.0.CO
  • [5] 2
  • [6] The development of an industrial-scale fed-batch fermentation simulation
    Goldrick, Stephen
    Stefan, Andrei
    Lovett, David
    Montague, Gary
    Lennox, Barry
    [J]. JOURNAL OF BIOTECHNOLOGY, 2015, 193 : 70 - 82
  • [7] Euler-Lagrange computational fluid dynamics for (bio)reactor scale down: An analysis of organism lifelines
    Haringa, Cees
    Tang, Wenjun
    Deshmukh, Amit T.
    Xia, Jianye
    Reuss, Matthias
    Heijnen, Joseph J.
    Mudde, Robert F.
    Noorman, Henk J.
    [J]. ENGINEERING IN LIFE SCIENCES, 2016, 16 (07): : 652 - 663
  • [8] Application of a mechanistic model as a tool for on-line monitoring of pilot scale filamentous fungal fermentation processesThe importance of evaporation effects
    Mears, Lisa
    Stocks, Stuart M.
    Albaek, Mads O.
    Sin, Gurkan
    Gernaey, Krist V.
    [J]. BIOTECHNOLOGY AND BIOENGINEERING, 2017, 114 (03) : 589 - 599
  • [9] MATHEMATICAL-MODELING OF INDUSTRIAL PILOT-PLANT PENICILLIN-G FED-BATCH FERMENTATIONS
    MENEZES, JC
    ALVES, SS
    LEMOS, JM
    DEAZEVEDO, SF
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 1994, 61 (02) : 123 - 138
  • [10] EFFECT OF GROWTH RATE ON SYNTHESIS OF PENICILLIN BY PENICILLIUM CHRYSOGENUM IN BATCH AND CHEMOSTAT CULTURES
    PIRT, SJ
    RIGHELATO, RC
    [J]. APPLIED MICROBIOLOGY, 1967, 15 (06) : 1284 - +