TY - JOUR
T1 - Combined Strategies to Boost Polyhydroxyalkanoate Production from Fruit Waste in a Three-Stage Pilot Plant
AU - Matos, Mariana
AU - Cruz, Rafaela A. P.
AU - Cardoso, Pedro
AU - Silva, Fernando
AU - Freitas, Elisabete B.
AU - Carvalho, Gilda
AU - Reis, Maria A. M.
N1 - Funding Information:
info:eu-repo/grantAgreement/FCT/OE/SFRH%2FBD%2F104767%2F2014/PT#
info:eu-repo/grantAgreement/EC/H2020/730349/EU#
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F04378%2F2020/PT#
Publisher Copyright:
© 2021 American Chemical Society.
PY - 2021/6/21
Y1 - 2021/6/21
N2 - The full-scale implementation of polyhydroxyalkanoate (PHA) production using mixed microbial cultures (MMCs) has been limited by the low PHA global productivity and overall process yield. This work aimed to demonstrate, at a pilot scale, that by combining different effective operating conditions, it is possible to boost the PHA production performance when using fruit waste as a substrate. The organic loading rate (OLR) and pH of the acidogenic reactor were successfully used as tuning parameters to obtain a high fermentation yield (0.74 gCOD·gCOD-1) and a fermentate rich in butyrate, resulting in enhanced PHA production steps. A biomass highly enriched in PHA-storing microorganisms was selected as a result of uncoupling the carbon to the nitrogen feeding. The biomass concentration attained a notable value (7.83 g·L-1) as a response to the high OLR (8.7 gCOD·L-1·d-1) imposed. In the PHA accumulation assays, the culture selected at the optimal OLR in the selection reactor achieved a high storage yield (0.98 gCOD·gCOD-1), and the continuous feeding strategy led to a maximum PHA content of 80.5% (g-basis). The high global productivity (8.1 g-PHA·L-1·d-1) and overall process yield (0.45 gCOD·gCOD-1) are, to the best of the authors' knowledge, the highest values reported for MMC using a real feedstock at pilot scale. These results demonstrate the importance of combining different effective strategies to maximize the process performance, a promising result toward the full-scale implementation of PHA production from wastes and MMC.
AB - The full-scale implementation of polyhydroxyalkanoate (PHA) production using mixed microbial cultures (MMCs) has been limited by the low PHA global productivity and overall process yield. This work aimed to demonstrate, at a pilot scale, that by combining different effective operating conditions, it is possible to boost the PHA production performance when using fruit waste as a substrate. The organic loading rate (OLR) and pH of the acidogenic reactor were successfully used as tuning parameters to obtain a high fermentation yield (0.74 gCOD·gCOD-1) and a fermentate rich in butyrate, resulting in enhanced PHA production steps. A biomass highly enriched in PHA-storing microorganisms was selected as a result of uncoupling the carbon to the nitrogen feeding. The biomass concentration attained a notable value (7.83 g·L-1) as a response to the high OLR (8.7 gCOD·L-1·d-1) imposed. In the PHA accumulation assays, the culture selected at the optimal OLR in the selection reactor achieved a high storage yield (0.98 gCOD·gCOD-1), and the continuous feeding strategy led to a maximum PHA content of 80.5% (g-basis). The high global productivity (8.1 g-PHA·L-1·d-1) and overall process yield (0.45 gCOD·gCOD-1) are, to the best of the authors' knowledge, the highest values reported for MMC using a real feedstock at pilot scale. These results demonstrate the importance of combining different effective strategies to maximize the process performance, a promising result toward the full-scale implementation of PHA production from wastes and MMC.
KW - acidogenic fermentation
KW - butyrate
KW - fruit waste (FW)
KW - mixed microbial cultures (MMCs)
KW - pilot plant
KW - polyhydroxyalkanoate (PHA)
UR - http://www.scopus.com/inward/record.url?scp=85109047252&partnerID=8YFLogxK
U2 - 10.1021/acssuschemeng.1c02432
DO - 10.1021/acssuschemeng.1c02432
M3 - Article
AN - SCOPUS:85109047252
SN - 2168-0485
VL - 9
SP - 8270
EP - 8279
JO - ACS Sustainable Chemistry & Engineering
JF - ACS Sustainable Chemistry & Engineering
IS - 24
ER -