Polyhydroxyalkanoate production from whey by Pseudomonas hydrogenovora

Whey permeate from dairy industry was hydrolyzed enzymatically to cleave its main carbon source, lactose, to glucose and galactose. The hydrolysis products were chosen as carbon sources for the production of poly-3-hydroxybutyric acid (PHB) by Pseudomonas hydrogenovora. In shaking flask experiments,...

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Veröffentlicht in:Bioresource technology 2008-07, Vol.99 (11), p.4854-4863
Hauptverfasser: Koller, Martin, Bona, Rodolfo, Chiellini, Emo, Fernandes, Elizabeth Grillo, Horvat, Predrag, Kutschera, Christoph, Hesse, Paula, Braunegg, Gerhart
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container_end_page 4863
container_issue 11
container_start_page 4854
container_title Bioresource technology
container_volume 99
creator Koller, Martin
Bona, Rodolfo
Chiellini, Emo
Fernandes, Elizabeth Grillo
Horvat, Predrag
Kutschera, Christoph
Hesse, Paula
Braunegg, Gerhart
description Whey permeate from dairy industry was hydrolyzed enzymatically to cleave its main carbon source, lactose, to glucose and galactose. The hydrolysis products were chosen as carbon sources for the production of poly-3-hydroxybutyric acid (PHB) by Pseudomonas hydrogenovora. In shaking flask experiments, the utilization of whey permeate as a cheap substrate was compared to the utilization of pure glucose and galactose for bacterial growth under balanced conditions as well as for the production of PHB under nitrogen limitation. After determination of the inhibition constant K i for sodium valerate on biomass production ( K i = 1.84 g/l), the biosynthesis of PHA co-polyesters containing 3-hydroxybutyrate (3HB) and 3-hydroxyvalerate (3HV) units from hydrolyzed whey permeate and valerate was investigated. The application of hydrolyzed whey permeate turned out to be advantageous compared with the utilization of pure sugars. Therefore, fermentation under controlled conditions in a bioreactor was performed with hydrolyzed whey permeate to obtain detailed kinetic data (maximum specific growth rate, μ max = 0.29 1/h, maximum polymer concentration, 1.27 g/l PHB), values for molecular mass distribution (weight average molecular weight M w = 353.5 kDa, polydispersity index PDI = 3.8) and thermo analytical data. The fermentation was repeated with co-feeding of valerate (maximum specific growth rate, μ max = 0.20 1/h, maximum polymer concentration, 1.44 g/l poly-(3HB- co-21%-3HV), weight average molecular weight M w = 299.2 kDa, polydispersity index PDI = 4.3).
doi_str_mv 10.1016/j.biortech.2007.09.049
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subjects 3-Hydroxybutyric Acid - metabolism
Biological and medical sciences
Bioreactors
Fermentation - drug effects
Fundamental and applied biological sciences. Psychology
Galactose - pharmacology
Glucose - pharmacology
Hydrolysis - drug effects
Industrial Waste
Ketoglutaric Acids - metabolism
Polyesters - isolation & purification
Polyesters - metabolism
Polyhydroxyalkanoates
Polyhydroxyalkanoates - metabolism
Polymer characterization
Pseudomonas
Pseudomonas - cytology
Pseudomonas - drug effects
Pseudomonas - growth & development
Pseudomonas - metabolism
Pseudomonas hydrogenovora
Valerates - metabolism
Valeric acid
Whey permeate
title Polyhydroxyalkanoate production from whey by Pseudomonas hydrogenovora
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