TY - JOUR
T1 - Feeding strategies for tuning poly (3-hydroxybutyrate-co-4-hydroxybutyrate) monomeric composition and productivity using Burkholderia sacchari
AU - Raposo, Rodrigo S.
AU - de Almeida, M. Catarina M.D.
AU - da Fonseca, M. M.R.
AU - Cesário, M. Teresa
N1 - Publisher Copyright:
© 2017 Elsevier B.V.
PY - 2017/12
Y1 - 2017/12
N2 - Poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P(3HB-4HB)) co-polymers were produced at bench-scale in fed-batch cultivations by Burkholderia sacchari from glucose (main carbon-source) and gamma-butyrolactone (GBL) as co-substrate. As P(3HB-4HB) properties highly depend on the 4-hydroxybutyrate (4HB) molar fraction, it is advantageous to have a thorough knowledge of the process in order to promote the production of the targeted final product. In this work, polymers with a 4HB molar percentage ranging from 1.5 to 8.4% (mol/mol) were obtained as consequence of a fine tuning of the fed-batch operation conditions, namely regarding the co-substrate feeding rate and its addition time, as GBL is toxic to B. sacchari cells. The best results regarding both the 4HB incorporation (molar%) and the co-polymer productivity (7.1% and 1.1 g/(L.h) respectively) were reached when a pulse of GBL (<10 g/L) was added early in the accumulation phase followed by a constant GBL addition at a rate similar to that of consumption so that a steady co-substrate concentration in the medium was maintained.
AB - Poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P(3HB-4HB)) co-polymers were produced at bench-scale in fed-batch cultivations by Burkholderia sacchari from glucose (main carbon-source) and gamma-butyrolactone (GBL) as co-substrate. As P(3HB-4HB) properties highly depend on the 4-hydroxybutyrate (4HB) molar fraction, it is advantageous to have a thorough knowledge of the process in order to promote the production of the targeted final product. In this work, polymers with a 4HB molar percentage ranging from 1.5 to 8.4% (mol/mol) were obtained as consequence of a fine tuning of the fed-batch operation conditions, namely regarding the co-substrate feeding rate and its addition time, as GBL is toxic to B. sacchari cells. The best results regarding both the 4HB incorporation (molar%) and the co-polymer productivity (7.1% and 1.1 g/(L.h) respectively) were reached when a pulse of GBL (<10 g/L) was added early in the accumulation phase followed by a constant GBL addition at a rate similar to that of consumption so that a steady co-substrate concentration in the medium was maintained.
KW - Bioreactor feeding strategy
KW - Burkholderia sacchari
KW - Gamma-butyrolactone
KW - P(3HB-4HB)
KW - Poly (3-hydroxybutyrate-co-4-hydroxybutyrate)
UR - http://www.scopus.com/inward/record.url?scp=85026781596&partnerID=8YFLogxK
U2 - 10.1016/j.ijbiomac.2017.07.111
DO - 10.1016/j.ijbiomac.2017.07.111
M3 - Article
C2 - 28735003
AN - SCOPUS:85026781596
SN - 0141-8130
VL - 105
SP - 825
EP - 833
JO - International Journal of Biological Macromolecules
JF - International Journal of Biological Macromolecules
ER -