期刊
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY
卷 93, 期 11, 页码 3208-3218出版社
WILEY
DOI: 10.1002/jctb.5677
关键词
biochemical engineering; industrial biotechnology; mathematical modeling; process optimization; proteins; yeast
类别
资金
- MINECO/FEDER,UE [CTQ2016-74959-R]
- PIF grant of the Universitat Autonoma de Barcelona
BACKGROUNDTo improve the efficiency of a bioprocess, key parameters, such as yield, titer and productivity, must be considered. They are mainly dependent on the specific rates for product (q(P)) and cell growth (), and their correlation determines the most suitable feeding polices that should be applied. RESULTSThe mathematical description of the Pichia pastoris (Komagataella spp) P-AOX1-based system (Mut(+)) expressing recombinant Rhizopus oryzae lipase (ROL), which includes cell growth, substrate consumption and product formation kinetics, was used to define the optimal profiles regarding methanol feeding-rate (F), residual methanol concentration (S) and specific growth rate (). Optimal trajectories obtained using numerical optimization and algorithms based on S-profile determination were first applied to manage the multiplicity of S-states with both and q(P). Once the S-profile was determined, the F and profiles were obtained in a straightforward manner from mass balances and growth kinetics. From experimental results, the bioprocess efficiency improvement was confirmed in terms of a 2.2-fold higher final titer and 3.4-fold higher productivity compared with the best standard pre-programmed exponential substrate feeding strategy. Additionally, 1.2-fold higher productivity and 1.1-fold higher final titer relative to the most promising feedback control of the methanol concentration strategy were obtained. CONCLUSIONThe whole model-based approach was established as a versatile and simple platform, which would then be transferable to alternative modes of operation and even to produce other proteins of interest. (c) 2018 Society of Chemical Industry
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