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Kinetic Modeling of Fermentative Production of 1, 3-Propanediol by Klebsiella pneumoniae HR526 with Consideration of Multiple Product Inhibitions

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Abstract

During the fermentative production of 1, 3-propanediol (1,3-PD), the multiple product inhibitions cannot be negligible to accurately describe the kinetics of fermentation process. A kinetic model for fermentative production of 1,3-PD by Klebsiella pneumoniae HR526 with glycerol as carbon source under aerobic condition was proposed. The inhibitions of multiple products including 1,3-PD, 2, 3-butanediol (2,3-BD), acetate, and succinate were considered in the model. It was found that 1,3-PD, 2,3-BD, and acetate showed strong inhibitions to cell growth depending on their concentrations. The kinetic model was relatively accurate to predict the experimental data of batch, fed-batch, and continuous fermentations. The model thus can serve as a tool for further controlling and optimizing the fermentation process.

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Abbreviations

X :

Cell biomass concentration (g⋅L−1)

P :

1,3-PD concentration (g⋅L−1)

P B :

2,3-BD concentration (g⋅L−1)

P A :

Acetate concentration (g⋅L−1)

P S :

Succinate concentration (g⋅L−1)

S :

Glycerol concentration (g⋅L−1)

μ m :

Maximum specific growth rate (h−1)

K S :

Saturation constant for cell growth rate (g⋅L−1)

α :

Kinetic constant for 1,3-PD formation from cell growth (g⋅g−1)

β :

Kinetic constant for 1,3-PD formation from biomass (h−1)

α B :

Kinetic constant for 2,3-BD formation from cell growth (g⋅g−1)

β B :

Kinetic constant for 2,3-BD formation from biomass (h−1)

α A :

Kinetic constant for acetate formation from cell growth (g⋅g−1)

β A :

Kinetic constant for acetate formation from biomass (h−1)

α S :

Kinetic constant for succinate formation from cell growth (g⋅g−1)

β S :

Kinetic constant for succinate formation from biomass (h−1)

Y X/S :

Yield coefficient of biomass on glycerol (g⋅g−1)

Y P/S :

Yield coefficient of 1,3-PD on glycerol (g⋅g−1)

Y PB/S :

Yield coefficient of 2,3-BD on glycerol (g⋅g−1)

Y PA/S :

Yield coefficient of acetate on glycerol (g⋅g−1)

Y PS/S :

Yield coefficient of succinate on glycerol (g⋅g−1)

n :

Kinetic constant for glycerol consumption on cell metabolism (h−1)

\( C_P^{*} \) :

Critical inhibition concentration for 1,3-PD of maximum specific growth rate (g⋅L−1)

\( C_B^{*} \) :

Critical inhibition concentration for 2,3-BD of maximum specific growth rate (g⋅L−1)

\( C_A^{*} \) :

Critical inhibition concentration for acetate of maximum specific growth rate (g⋅L−1)

P*:

Critical feedback inhibition concentration of 1,3-PD for 1,3-PD formation (g⋅L−1)

\( P_B^{*} \) :

Critical feedback inhibition concentration of 2,3-BD for 2,3-BD formation (g⋅L−1)

\( P_A^{*} \) :

Critical feedback inhibition concentration of acetate for acetate formation (g⋅L−1)

\( P_S^{*} \) :

Critical feedback inhibition concentration of succinate for succinate formation (g⋅L−1)

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Acknowledgments

The authors are thankful to the International Collaboration Project of the Ministry of Science and Technology of China (no. 2010DFB40170) for supporting this work.

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Correspondence to Xuebing Zhao or Dehua Liu.

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He, L., Zhao, X., Cheng, K. et al. Kinetic Modeling of Fermentative Production of 1, 3-Propanediol by Klebsiella pneumoniae HR526 with Consideration of Multiple Product Inhibitions. Appl Biochem Biotechnol 169, 312–326 (2013). https://doi.org/10.1007/s12010-012-9984-1

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  • DOI: https://doi.org/10.1007/s12010-012-9984-1

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