TY - JOUR
T1 - An integrated process for mixed culture production of 3-hydroxyhexanoate-rich polyhydroxyalkanoates from fruit waste
AU - Silva, Fernando
AU - Matos, Mariana
AU - Pereira, Bruno
AU - Ralo, Cláudia
AU - Pequito, Daniela
AU - Marques, Nuno
AU - Carvalho, Gilda
AU - Reis, Maria A. M.
N1 - Funding Information:
info:eu-repo/grantAgreement/EC/H2020/730349/EU#
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F04378%2F2020/PT#
We are also thankful for the support of Fundação para a Ciência e Tecnologia (Portugal) for funding through PD/BD/126626/2016 and PD/BD/104767/2014 The authors acknowledge Sumol + Compal (Portugal) for kindly providing the fruit waste used in this study, Elsa Mora and Mónica Centeio (chemical analysis) and Prof. Mário Eusébio for developing the software used to control the SBR cycle.
Funding Information:
The research leading to these results has received funding by RESURBIS project (European Union's Horizon 2020 research and innovation programme under grant agreement No 730349). We are also thankful for the support of Funda??o para a Ci?ncia e Tecnologia (Portugal) for funding through PD/BD/126626/2016 and PD/BD/104767/2014
Publisher Copyright:
© 2021 Elsevier B.V.
PY - 2022/1/1
Y1 - 2022/1/1
N2 - Fermented wastes have been demonstrated to be adequate sources for polyhydroxyalkanoates (PHA) production using mixed microbial cultures (MMC). In general, MMC processes are focused on the production of co-polymers containing 3-hydroxybutyrate (HB) and 3-hydroxyvalerate (HV), which limits the range of polymer properties and aplications. This study aimed at demonstrating the feasibility of producing a ter-polymer enriched in 3-hydroxyhexanoate (HHx) from a waste using a mixed-culture 3-stage process. For this purpose, each of the stages (acidogenic reactor, selection of a PHA-accumulating culture and PHA accumulation) was fine-tuned to maximise the process's yield and productivity. In the acidogenic reactor, operating conditions were manipulated to ferment fruit waste into a caproate-rich effluent (69%) with a fermentation products’ concentration (FP) of 13.0 gCOD L−1. A culture enriched in a highly efficient PHA-accumulating culture capable of converting caproate into HHx was selected. This culture was used as inoculum and fed with caproate-rich effluent, achieving a maximum PHA content of 71.3%, a PHA productivity of 3.29 gCOD L−1h−1 and a terpolymer with a composition of 33/1/66 (HB/HV/HHx,% wt.). Batch assays were carried out to demonstrate that caproate was the precursor of HHx, and acclimatization of the biomass to caproate was an important factor in the selection step to foster HHx-containing polymer production. This paper reports unprecedented values of yield, productivity and HHx fraction for the production of a mcl-PHA using MC and a fermented waste. These results are a significant contribution towards upscaling the process to convert a waste into HHx-rich PHA.
AB - Fermented wastes have been demonstrated to be adequate sources for polyhydroxyalkanoates (PHA) production using mixed microbial cultures (MMC). In general, MMC processes are focused on the production of co-polymers containing 3-hydroxybutyrate (HB) and 3-hydroxyvalerate (HV), which limits the range of polymer properties and aplications. This study aimed at demonstrating the feasibility of producing a ter-polymer enriched in 3-hydroxyhexanoate (HHx) from a waste using a mixed-culture 3-stage process. For this purpose, each of the stages (acidogenic reactor, selection of a PHA-accumulating culture and PHA accumulation) was fine-tuned to maximise the process's yield and productivity. In the acidogenic reactor, operating conditions were manipulated to ferment fruit waste into a caproate-rich effluent (69%) with a fermentation products’ concentration (FP) of 13.0 gCOD L−1. A culture enriched in a highly efficient PHA-accumulating culture capable of converting caproate into HHx was selected. This culture was used as inoculum and fed with caproate-rich effluent, achieving a maximum PHA content of 71.3%, a PHA productivity of 3.29 gCOD L−1h−1 and a terpolymer with a composition of 33/1/66 (HB/HV/HHx,% wt.). Batch assays were carried out to demonstrate that caproate was the precursor of HHx, and acclimatization of the biomass to caproate was an important factor in the selection step to foster HHx-containing polymer production. This paper reports unprecedented values of yield, productivity and HHx fraction for the production of a mcl-PHA using MC and a fermented waste. These results are a significant contribution towards upscaling the process to convert a waste into HHx-rich PHA.
KW - 3-hydroxyhexanoate
KW - Caproate
KW - Medium chain length polyhydroxyalkanoates
KW - Mixed microbial cultures
KW - Pilot scale
KW - Terpolymer
UR - http://www.scopus.com/inward/record.url?scp=85113924325&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2021.131908
DO - 10.1016/j.cej.2021.131908
M3 - Article
AN - SCOPUS:85113924325
SN - 1385-8947
VL - 427
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 131908
ER -