TY - JOUR
T1 - Production and recovery of poly-3-hydroxybutyrate [P(3HB)] of ultra-high molecular weight using fed-batch cultures of Azotobacter vinelandii OPNA strain
AU - García, Andrés
AU - Pérez, Diana
AU - Castro, Manuel
AU - Urtuvia, Viviana
AU - Castillo, Tania
AU - Díaz-Barrera, Alvaro
AU - Espín, Guadalupe
AU - Peña, Carlos
N1 - Publisher Copyright:
© 2019 Society of Chemical Industry
PY - 2019/6
Y1 - 2019/6
N2 - BACKGROUND: Poly-3-hydroxybutyrate P(3HB) is a bioplastic that is characterized for its biodegradability and biocompatibility and can be used in the biomedical field. The aim of this study was to evaluate the scaling-up process at pilot level, for the production and recovery of P(3HB) synthesized by Azotobacter vinelandii OPNA strain, based on the use of fed-batch fermentation coupled to a recovery method using nonhalogenated solvents (ethanol and acetone). RESULTS: In fed-batch cultivations at the 3-L scale, using yeast extract and sucrose of industrial grade with a carbon:nitrogen ratio of 14 and manipulating the agitation rate from 500 to 700 rpm to give a maximal biomass concentration of 33.8 ± 1.5 g L−1, P(3HB) concentrations of 29 ± 4.5 g L−1 were reached. By simulating the gassed volumetric power input observed in the 3-L bioreactors at the different agitation rates (500 and 700 rpm), a scaling-up to 30-L bioreactors was performed. At this scale, the P(3HB) concentration, and productivity were similar or even better than those values obtained at the smaller scale. The production process was coupled to a P(3HB) separation process, in which the polymer was precipitated with ethanol and washed with acetone, reaching a purity close to 95% and a yield of 85%. The P(3HB) obtained was of ultra-high molecular mass, with values of 5693 ± 615 kDa. CONCLUSION: In this study a successful scaling-up process for the production of P(3HB) of ultra-high molecular weight at pilot scale was developed.
AB - BACKGROUND: Poly-3-hydroxybutyrate P(3HB) is a bioplastic that is characterized for its biodegradability and biocompatibility and can be used in the biomedical field. The aim of this study was to evaluate the scaling-up process at pilot level, for the production and recovery of P(3HB) synthesized by Azotobacter vinelandii OPNA strain, based on the use of fed-batch fermentation coupled to a recovery method using nonhalogenated solvents (ethanol and acetone). RESULTS: In fed-batch cultivations at the 3-L scale, using yeast extract and sucrose of industrial grade with a carbon:nitrogen ratio of 14 and manipulating the agitation rate from 500 to 700 rpm to give a maximal biomass concentration of 33.8 ± 1.5 g L−1, P(3HB) concentrations of 29 ± 4.5 g L−1 were reached. By simulating the gassed volumetric power input observed in the 3-L bioreactors at the different agitation rates (500 and 700 rpm), a scaling-up to 30-L bioreactors was performed. At this scale, the P(3HB) concentration, and productivity were similar or even better than those values obtained at the smaller scale. The production process was coupled to a P(3HB) separation process, in which the polymer was precipitated with ethanol and washed with acetone, reaching a purity close to 95% and a yield of 85%. The P(3HB) obtained was of ultra-high molecular mass, with values of 5693 ± 615 kDa. CONCLUSION: In this study a successful scaling-up process for the production of P(3HB) of ultra-high molecular weight at pilot scale was developed.
KW - Azotobacter vinelandii
KW - molecular mass
KW - poly-3-hydroxybutyrate
KW - scaling-up
UR - http://www.scopus.com/inward/record.url?scp=85063284198&partnerID=8YFLogxK
U2 - 10.1002/jctb.5959
DO - 10.1002/jctb.5959
M3 - Article
AN - SCOPUS:85063284198
SN - 0268-2575
VL - 94
SP - 1853
EP - 1860
JO - Journal of Chemical Technology and Biotechnology
JF - Journal of Chemical Technology and Biotechnology
IS - 6
ER -