TY - JOUR
T1 - The influence of process parameters on the characteristics of polyhydroxyalkanoates produced by mixed cultures
AU - Lemos, Paulo Alexandre da Costa
AU - Reis, Maria D'ascensão Carvalho Fernandes Miranda
AU - Ramos, Ana Maria Martelo
PY - 2008/1/1
Y1 - 2008/1/1
N2 - The characterization of polyhydroxyalkanciates (PHA) produced by mixed cultures is fundamental for foreseeing the possible final applications of the polymer. In this study PHA produced under aerobic dynamic feeding (ADF) conditions are characterized. The PHA produced shows a stable average molecular weight ((M) over bar (w)), in the range (1.0-3.0) x 10(6), along three years of reactor operation. Attempts to improve the amount of PHA produced did not introduce significant variations on the values of (M) over barw. Along this period, the polydispersity indices (PDI) were between 1.3 and 2.2. The use of different carbon sources allowed the tailoring of polymer composition: homopolymers of poly(3-hydroxybutyrate), P(3HB), were obtained with acetate and butyrate, whereas a mixture of acetate and propionate, and propionate and valerate, gave terpolymers of 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), and 2-methyl-3-hydroxyvalerate (2M3HV). All of these PHA had (M) over bar (w) between 2.0 x 10(6) and 3.0 x 10(6) Thermal characterization of the produced polymers showed values of glass transition temperature, melting temperature, melting enthalpy, and crystallinity slightly lower than those obtained for PHA from pure cultures. The introduction of a purification step during the polymer extraction process allowed the elimination of possible contaminants but did not significantly improve the polymer quality.
AB - The characterization of polyhydroxyalkanciates (PHA) produced by mixed cultures is fundamental for foreseeing the possible final applications of the polymer. In this study PHA produced under aerobic dynamic feeding (ADF) conditions are characterized. The PHA produced shows a stable average molecular weight ((M) over bar (w)), in the range (1.0-3.0) x 10(6), along three years of reactor operation. Attempts to improve the amount of PHA produced did not introduce significant variations on the values of (M) over barw. Along this period, the polydispersity indices (PDI) were between 1.3 and 2.2. The use of different carbon sources allowed the tailoring of polymer composition: homopolymers of poly(3-hydroxybutyrate), P(3HB), were obtained with acetate and butyrate, whereas a mixture of acetate and propionate, and propionate and valerate, gave terpolymers of 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), and 2-methyl-3-hydroxyvalerate (2M3HV). All of these PHA had (M) over bar (w) between 2.0 x 10(6) and 3.0 x 10(6) Thermal characterization of the produced polymers showed values of glass transition temperature, melting temperature, melting enthalpy, and crystallinity slightly lower than those obtained for PHA from pure cultures. The introduction of a purification step during the polymer extraction process allowed the elimination of possible contaminants but did not significantly improve the polymer quality.
KW - mixed cultures
KW - crystallinity
KW - average molecular weight
KW - polyhydroxyalkanoates
KW - glass transition
KW - Aerobic dynamic feeding
KW - melting point
U2 - 10.1002/mabi.200700200
DO - 10.1002/mabi.200700200
M3 - Article
SN - 1616-5187
VL - 8
SP - 355
EP - 366
JO - Macromolecular Bioscience
JF - Macromolecular Bioscience
IS - 4
ER -