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      KCI등재 SCIE SCOPUS

      Modeling of Poly(3-hydroxybutyrate)Production by High Cell Density Fed-batchCulture of Ralstonia eutropha

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      https://www.riss.kr/link?id=A104467514

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      다국어 초록 (Multilingual Abstract)

      High cell density culturing has been conducted for the production of poly(3-hydroxybutyrate) fed-batch cultures of Ralstonia eutropha with phosphate limitation. It was found that a high glucose concentration inhibited the synthesis of P(3HB) in the high cell density culture of R. eutropha. Although a low glucose concentration can trigger the synthesis of P(3HB) in a manner similar to that of phosphate limitation, it also limited both the P(3HB) synthesis and the cell growth, and led to a low P(3HB) productivity because glucose is the sole carbon source in this reaction. An unstructured model was proposed for predicting the cell growth and P(3HB) synthesis in high cell density cultures of R. eutropha, where the phosphate concentration played a key role in the accumulation of P(3HB) and in cell growth. Good agreements were found between the experimental data and model predictions. The results of simulation showed that the final P(3HB) concentration would decrease more than 25% when the glucose was concentration increased to 40 g/L, and indicated that the optimal glucose concentration for P(3HB) production by high cell density cultures of R. eutropha was around 9 g/L.
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      High cell density culturing has been conducted for the production of poly(3-hydroxybutyrate) fed-batch cultures of Ralstonia eutropha with phosphate limitation. It was found that a high glucose concentration inhibited the synthesis of P(3HB) in the hi...

      High cell density culturing has been conducted for the production of poly(3-hydroxybutyrate) fed-batch cultures of Ralstonia eutropha with phosphate limitation. It was found that a high glucose concentration inhibited the synthesis of P(3HB) in the high cell density culture of R. eutropha. Although a low glucose concentration can trigger the synthesis of P(3HB) in a manner similar to that of phosphate limitation, it also limited both the P(3HB) synthesis and the cell growth, and led to a low P(3HB) productivity because glucose is the sole carbon source in this reaction. An unstructured model was proposed for predicting the cell growth and P(3HB) synthesis in high cell density cultures of R. eutropha, where the phosphate concentration played a key role in the accumulation of P(3HB) and in cell growth. Good agreements were found between the experimental data and model predictions. The results of simulation showed that the final P(3HB) concentration would decrease more than 25% when the glucose was concentration increased to 40 g/L, and indicated that the optimal glucose concentration for P(3HB) production by high cell density cultures of R. eutropha was around 9 g/L.

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      참고문헌 (Reference)

      1 "Website of Superprodesigner"

      2 Wlaschin A. P, "The fractional contributions of elementary modesto the metabolism of Escherichia coli and their estimationfrom reaction entropies" 8 : 338-352, 2006

      3 A, "Substrate inhibiton kinetics for microbial growth andsynthesis of poly-β-hydroxybutyric acid by Alcaligeneseutrophus ATCC 17697" 11-17, 1989

      4 Shahhosseini, S, "Simulation and optimization ofPHB production in fed-batch culture of Ralstonia eutropha" 39 : 963-969, 2004

      5 Jiang, Q., "Predictive modeling ofwhole-cell bioactivity retention data in the presence oforganic compounds" 12 : 228-234, 2007

      6 Chu, K. H., "Predictive modeling ofcompetitive biosorption equilibrium data" 11 : 67-71, 2006

      7 Shang, L, "Poly(3-hydroxybutyrate) synthesis in fed-batch culture of Ralstoniaeutropha with phosphate limitation under differentglucose concentrations" 25 : 1415-1419, 2003

      8 Belfares L, "Multi-inhibition kineticmodel for the growth of Alcaligenes eutrophus" 41 : 249-256, 1995

      9 Aboudzadeh, M. R, "Modelingof protein adsorption to DEAE sepharose FF:Comparison of data with model simulation" 23 : 124-130, 2006

      10 Tohyama M, "Modeling of the mixed culture and periodic controlfor PHB production" 10 : 157-173, 2002

      1 "Website of Superprodesigner"

      2 Wlaschin A. P, "The fractional contributions of elementary modesto the metabolism of Escherichia coli and their estimationfrom reaction entropies" 8 : 338-352, 2006

      3 A, "Substrate inhibiton kinetics for microbial growth andsynthesis of poly-β-hydroxybutyric acid by Alcaligeneseutrophus ATCC 17697" 11-17, 1989

      4 Shahhosseini, S, "Simulation and optimization ofPHB production in fed-batch culture of Ralstonia eutropha" 39 : 963-969, 2004

      5 Jiang, Q., "Predictive modeling ofwhole-cell bioactivity retention data in the presence oforganic compounds" 12 : 228-234, 2007

      6 Chu, K. H., "Predictive modeling ofcompetitive biosorption equilibrium data" 11 : 67-71, 2006

      7 Shang, L, "Poly(3-hydroxybutyrate) synthesis in fed-batch culture of Ralstoniaeutropha with phosphate limitation under differentglucose concentrations" 25 : 1415-1419, 2003

      8 Belfares L, "Multi-inhibition kineticmodel for the growth of Alcaligenes eutrophus" 41 : 249-256, 1995

      9 Aboudzadeh, M. R, "Modelingof protein adsorption to DEAE sepharose FF:Comparison of data with model simulation" 23 : 124-130, 2006

      10 Tohyama M, "Modeling of the mixed culture and periodic controlfor PHB production" 10 : 157-173, 2002

      11 Patwardhan, P. R., "Modelbasedfed-batch cultivation of R. eutropha for enhancedbiopolymer production" 20 : 21-28, 2004

      12 Leaf, T. A., "Metabolic modeling ofpolyhydroxybutyrate biosynthesis" 57 : 557-570, 1998

      13 Dias J. M, "Mathematical modelling of a mixedculture cultivation process for the production of polyhydroxybutyrate" 92 : 209-222, 2005

      14 Prakorn, R, "Mass transfermodeling of membrane carrier system for extractionof Ce(IV) from sulfate media using hollow fiber supportedliquid membrane" 23 : 85-92, 2006

      15 Ryu H. W, "Mass production ofpoly(3-hydroxybutyrate) by fed-batch cultures of Ralstoniaeutropha with nitrogen and phosphate limitation" 9 : 751-756, 1999

      16 Omar R, "Kinetics and modelling of cellgrowth and substrate uptake in Centella asiatica cellculture" 11 : 223-229, 2006

      17 Kwon, Y. J., "Kinetic models forgrowth and product formation on multiple substrates" 10 : 587-592, 2005

      18 Chen Y, "Kinetic modeling for chromatographic separation of cytosinemonophosphate and uracil monophosphate" 23 : 784-788, 2006

      19 Shang L, "Inhibitory effect of carbon dioxideon the fed-batch culture of Ralstonia eutropha: EvaluaBiotechnol.Bioprocess Eng" 83 : 312-320, 2003

      20 Song B. D, "Hydrolysisof olive oil catalyzed by surfactant-coated Candidarugosa lipase in a hollow fiber membrane reactor" 12 : 121-124, 2007

      21 Lee, Y. M, "Generalapplications of modified Stokes expression for modelingand scale-up of expanded beds" 24 : 261-264, 2007

      22 Katoh T, "Dynamics and modeling on fermentativeproduction of poly(β-hydroxybutyric acid) from sugarsvia lactate by a mixed culture of Lactobacillu delbrueckiiand Alcaligenes eutrophus" 67 : 113-134, 1999

      23 Yoo, "Cybernetic model forsynthesis of poly-β-hydroxybutyric acid in Alcaligeneseutrophus" 1043-1051, 1994

      24 Khanna, S., "Computer simulatedfed-batch cultivation for over production of PHB:A comparison of simultaneous and alternate feeding ofcarbon and nitrogen" 27 : 197-203, 2006

      25 Song, J. Y., "Characteristics ofpoly(3-hydroxybutyrate-co-4-hydroxybutyrate) productionby Ralstonia eutropha NCIMB 11599 and ATCC17699" 10 : 603-606, 2005

      26 Mahadevan R, "Applications of metabolic modelingto drive bioprocess development for the productionof value-added chemicals" 10 : 408-417, 2005

      27 Lee J. H, "Application ofnonsingular transformation to on-line optimal control ofpoly-β-hydroxybutyrate fermentation" 55 : 135-150, 1997

      28 Sin G, "A new approachfor modelling simultaneous storage and growthprocesses for activated sludge systems under aerobicconditions" 92 : 600-613, 2005

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      기준연도 WOS-KCI 통합IF(2년) KCIF(2년) KCIF(3년)
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