Multivariable control of alcohol concentrations in the production of polyhydroxyalkanoates (PHAs) by Paracoccus denitrificans

被引:18
作者
Chanprateep, S
Abe, N
Shimizu, H
Yamane, T
Shioya, S
机构
[1] Osaka Univ, Grad Sch Engn, Dept Biotechnol, Suita, Osaka 5650871, Japan
[2] Nagoya Univ, Grad Sch Agr Sci, Dept Appl Biol Mech & Funct, Chikusa Ku, Nagoya, Aichi 4648601, Japan
关键词
biodegradable polymer; P(3HB-co-3HV); mole fraction control; multivariable controller;
D O I
10.1002/bit.1101
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
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. (C) 2001 John Wiley & Sons, Inc.
引用
收藏
页码:116 / 124
页数:9
相关论文
共 27 条
[1]   PHYSICAL-PROPERTIES OF POLY(HYDROXYBUTYRATE) AND COPOLYMERS OF HYDROXYBUTYRATE AND HYDROXYVALERATE [J].
BARHAM, PJ ;
BARKER, P ;
ORGAN, SJ .
FEMS MICROBIOLOGY LETTERS, 1992, 103 (2-4) :289-298
[2]  
BLOEMNERGEN S, 1986, MACROMOLECULES, V23, P26
[3]   RAPID GAS-CHROMATOGRAPHIC METHOD FOR DETERMINATION OF POLY-BETA-HYDROXYBUTYRIC ACID IN MICROBIAL BIOMASS [J].
BRAUNEGG, G ;
SONNLEITNER, B ;
LAFFERTY, RM .
EUROPEAN JOURNAL OF APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1978, 6 (01) :29-37
[4]   Factors affecting the economics of polyhydroxyalkanoate production by bacterial fermentation [J].
Choi, J ;
Lee, SY .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1999, 51 (01) :13-21
[5]  
COX MK, 1994, STUD POLYM SCI, V12, P120
[6]   Metabolic Modeling as a Tool for Evaluating Polyhydroxyalkanoate Copolymer Production in Plants [J].
Daae, Elisabeth B. ;
Dunnill, Peter ;
Mitsky, Timothy A. ;
Padgette, Steven R. ;
Taylor, Nancy B. ;
Valentin, Henry E. ;
Gruys, Kenneth J. .
METABOLIC ENGINEERING, 1999, 1 (03) :243-254
[7]   A KINETIC-MODEL FOR GROWTH AND SYNTHESIS OF POLY-BETA-HYDROXYBUTYRIC ACID (PHB) IN ALCALIGENES-EUTROPHUS-H16 [J].
HEINZLE, E ;
LAFFERTY, RM .
EUROPEAN JOURNAL OF APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1980, 11 (01) :8-16
[8]   Mole fraction control of poly(3-hydroxybutyric-co-3-hydroxyvaleric) acid in fed-batch culture of Alcaligenes eutrophus [J].
Ishihara, Y ;
Shimizu, H ;
Shioya, S .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1996, 81 (05) :422-428
[9]  
Leaf TA, 1998, BIOTECHNOL BIOENG, V57, P557, DOI 10.1002/(SICI)1097-0290(19980305)57:5<557::AID-BIT8>3.0.CO
[10]  
2-F