TY - JOUR
T1 - Principles for stimulating concurrent selective microbial growth and polyhydroxyalkanoate (PHA) storage responses for enhanced PHA productivity
AU - Xing, Yizhou
AU - Pei, Ruizhe
AU - Cardoso, Marta F.S.
AU - van Veelen, H. Pieter J.
AU - van Loosdrecht, Mark C.M.
AU - Kleerebezem, Robbert
AU - Werker, Alan
PY - 2025
Y1 - 2025
N2 - Municipal wastewater treatment plants are a ubiquitous source of microbial biomass for PHA production. Technological feasibility of directly using municipal activated sludge (WAS) for a PHA accumulation bioprocess is demonstrated in the literature. However, PHA contents and yields may be lower due to a coexistence of PHA-storing and non-PHA-storing microorganisms in WAS. This work focused on metabolic principles for stimulating selective growth of PHA-storing microorganisms during a PHA accumulation bioprocess to enhance PHA productivity. Two model substrates, butyrate and acetate, were used to evaluate conditions and principles that may regulate this selective growth response. Conditions promoting selective growth of the PHA storers were consistently observed in the fed-batch PHA production process fed with butyrate. Productivity was increased to 4 times more PHA produced over 48 h, wherein PHA contents and average yields were improved from 0.39 gPHA/gVSS and 0.25 gCODPHA/gCOD to 0.61 gPHA/gVSS and 0.47 gCODPHA/gCOD, respectively. Respiration monitoring and mass balances, with metabolic modelling, suggest that expected underlying differences in ATP yields between two tested substrates are the main mechanistic drivers of the observed selective growth. This study proposed that if conditions are created such that ATP is produced in sufficient excess of the demands for PHA storage and cell maintenance, then those PHA storers will further grow concurrently. The selective microbial growth allows extra conversion of substrates into PHA. These principles, concerning the metabolic basis of the PHA production pathway, provide a foundation that can be applied to a range of substrates or substrate mixtures for enhanced PHA accumulation.
AB - Municipal wastewater treatment plants are a ubiquitous source of microbial biomass for PHA production. Technological feasibility of directly using municipal activated sludge (WAS) for a PHA accumulation bioprocess is demonstrated in the literature. However, PHA contents and yields may be lower due to a coexistence of PHA-storing and non-PHA-storing microorganisms in WAS. This work focused on metabolic principles for stimulating selective growth of PHA-storing microorganisms during a PHA accumulation bioprocess to enhance PHA productivity. Two model substrates, butyrate and acetate, were used to evaluate conditions and principles that may regulate this selective growth response. Conditions promoting selective growth of the PHA storers were consistently observed in the fed-batch PHA production process fed with butyrate. Productivity was increased to 4 times more PHA produced over 48 h, wherein PHA contents and average yields were improved from 0.39 gPHA/gVSS and 0.25 gCODPHA/gCOD to 0.61 gPHA/gVSS and 0.47 gCODPHA/gCOD, respectively. Respiration monitoring and mass balances, with metabolic modelling, suggest that expected underlying differences in ATP yields between two tested substrates are the main mechanistic drivers of the observed selective growth. This study proposed that if conditions are created such that ATP is produced in sufficient excess of the demands for PHA storage and cell maintenance, then those PHA storers will further grow concurrently. The selective microbial growth allows extra conversion of substrates into PHA. These principles, concerning the metabolic basis of the PHA production pathway, provide a foundation that can be applied to a range of substrates or substrate mixtures for enhanced PHA accumulation.
KW - ATP overflow
KW - Butyrate
KW - Polyhydroxyalkanoate (PHA) storage
KW - Selective growth
KW - Volumetric productivity
KW - Waste activated sludge
UR - http://www.scopus.com/inward/record.url?scp=105010922769&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2025.165907
DO - 10.1016/j.cej.2025.165907
M3 - Article
AN - SCOPUS:105010922769
SN - 1385-8947
VL - 520
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 165907
ER -