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Multivariable control of alcohol concentrations in the production of polyhydroxyalkanoates (PHAs) by Paracoccus denitrificans
Author(s) -
Chanprateep Suchada,
Abe Naoya,
Shimizu Hiroshi,
Yamane Tsuneo,
Shioya Suteaki
Publication year - 2001
Publication title -
biotechnology and bioengineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.136
H-Index - 189
eISSN - 1097-0290
pISSN - 0006-3592
DOI - 10.1002/bit.1101
Subject(s) - mole fraction , chemistry , polyhydroxyalkanoates , mole , fraction (chemistry) , ethanol , fermentation , alcohol , organic chemistry , biology , bacteria , genetics
A novel multivariable control strategy is developed for alcohol (ethanol and n ‐pentanol) concentrations in the production of poly(3‐hydroxybutyrate‐co‐3‐hydroxyvalerate), P(HB‐co‐HV), a biodegradable polymer by Paracoccus denitrificans ATCC 1774. This controller, which is developed to control the mole fraction of P(HB‐co‐HV), consists of two parts: one is for ethanol concentration control and the other is for mole fraction control, based on the concept of metabolic flux distribution control. A simple metabolic reaction (MR) model is constructed for flux distribution analysis. The relationship between mole ratio of specific consumption rate of the two alcohols (ethanol and n ‐pentanol) and the mole fraction of 3HV units in the polymer is linear. This result suggests that the split ratio at a branched point of 3‐ketovaleryl‐CoA in the P(HB‐co‐HV) synthetic pathway is constant for several fermentation conditions. When the mole fraction of 3HV units has a target value, the feed rate of n ‐pentanol becomes a function of the feed rate of ethanol and the set value of 3HV, based on the MR model. The mole fraction of 3HV units successfully reached the target value using this strategy. The mole fraction control strategy is combined with an optimal production strategy based on the optimal profile of the specific growth rate. The combined strategy is realized using multivariable controllers and P(3HB‐co‐3HV) production is maximized with a given value of mole fraction of 3HV units at the final step of fermentation. © 2001 John Wiley & Sons, Inc. Biotechnol Bioeng 74: 116–124, 2001.