Segregated flux balance analysis constrained by population structure/function data: the case of PHA production by mixed microbial cultures.

In this study we developed a segregated flux balance analysis (FBA) method to calculate metabolic flux distributions of the individual populations present in a mixed microbial culture (MMC). Population specific flux data constraints were derived from the raw data typically obtained by the fluorescence in situ hybridization (FISH) and microautoradiography (MAR)-FISH techniques. This method was applied to study the metabolic heterogeneity of a MMC that produces polyhydroxyalkanoates (PHA) from fermented sugar cane molasses. Three populations were identified by FISH, namely Paracoccus sp., Thauera sp., and Azoarcus sp. The segregated FBA method predicts a flux distribution for each of the identified populations. The method is shown to predict with high accuracy the average PHA storage flux and the respective monomeric composition for 16 independent experiments. Moreover, flux predictions by segregated FBA were slightly better than those obtained by nonsegregated FBA, and also highly concordant with metabolic flux analysis (MFA) estimated fluxes. The segregated FBA method can be of high value to assess metabolic heterogeneity in MMC systems and to derive more efficient eco-engineering strategies. For the case of PHA-producing MMC considered in this work, it becomes apparent that the PHA average monomeric composition might be controlled not only by the volatile fatty acids (VFA) feeding profile but also by the population composition present in the MMC.

Mixed culture polyhydroxyalkanoate (PHA) production from volatile fatty acid (VFA)-rich streams: effect of substrate composition and feeding regime on PHA productivity, composition and properties.

In this study, the possibility of manipulating biopolymer composition in mixed culture polyhydroxyalkanoate (PHA) production from fermented molasses was assessed by studying the effects of substrate volatile fatty acid (VFA) composition and feeding regime (pulse wise versus continuous). It was found that the use of a continuous feeding strategy rather than a pulse feeding strategy can not only help mitigate the process constraints of the pulse-feeding strategy (resulting in higher specific and volumetric productivities) but also be used as means to broaden the range of polymer structures. Continuous feeding increased the hydroxyvalerate content by 8% relatively to that obtained from the same feedstock using pulse wise feeding. Therefore, the feeding strategy can be used to manipulate polymer composition. Furthermore, the range of PHA compositions, copolymers of P(HB-co-HV) with HV fraction ranging from 15 to 39%, obtained subsequently resulted in different polymer properties. Increasing HV content resulted in a decrease of the average molecular weight, the glass transition and melting temperatures and also in a reduction in the crystallinity degree from a semi-crystalline material to an amorphous matrix.

Mixed culture polyhydroxyalkanoates production from sugar molasses: the use of a 2-stage CSTR system for culture selection.

Polyhydroxyalkanoates (PHAs) are promising biodegradable polymers. The use of mixed microbial cultures (MMC) and low cost feedstocks have a positive impact on the cost-effectiveness of the process. It has typically been carried out in Sequencing Batch Reactors (SBR). In this study, a 2-stage CSTR system (under Feast and Famine conditions) was used to effectively select for PHA-storing organisms using fermented molasses as feedstock. The effect of influent substrate concentration (60-120 Cmmol VFA/L) and HRT ratio between the reactors (0.2-0.5h/h) on the system's selection efficiency was assessed. It was shown that Feast reactor residual substrate concentration impacted on the selective pressure for PHA storage (due to substrate-dependent kinetic limitation). Moreover, a residual substrate concentration coming from the Feast to the Famine reactor did not jeopardize the physiological adaptation required for enhanced PHA storage. The culture reached a maximum PHA content of 61%. This success opens new perspectives to the use of wastewater treatment infrastructure for PHA production, thus valorizing either excess sludge or wastewaters.

Polyhydroxyalkanoate (PHA) production by a mixed microbial culture using sugar molasses: effect of the influent substrate concentration on culture selection.

In Polyhydroxyalkanoate (PHA) production processes using Mixed Microbial Culture (MMC), the success of the culture selection step determines, to a great extent, the PHA accumulation performance obtained in the final PHA production stage. In this study, the effect of the influent substrate concentration (30-60Cmmol VFA/L) on the selection of a PHA-storing culture using a complex feedstock, fermented sugar molasses, was assessed. At 30 and 45Cmmol VFA/L, substrate concentration impacted on the process kinetics through a substrate dependent kinetic limitation effect. However, further increasing the carbon substrate concentration to 60Cmmol VFA/L, resulted in an unforeseen growth limitation effect associated with a micronutrient deficiency of the fermented feedstock (magnesium) and high operating pH. Struvite precipitation caused a nutrient limitation which prevented biomass concentration increase, thus causing the feast to famine length ratio to vary in the selection reactor, with subsequent impact on the selective pressure for PHA-storing organisms. A highly dynamic response of the selected population to transient conditions of feast to famine ratio, in the range of 0.21-1.1, was observed. Kinetic (limiting concentration of carbon source) and physiological (loss of internal growth limitation due to the shorter length of famine phase) effects, resulting from variation of the influent substrate concentration, were subsequently demonstrated in batch studies. The culture selected at an influent substrate concentration of 45Cmmol VFA/L showed the best PHA-storing capacity since neither substrate concentration nor feast to famine ratio were limiting factors. This culture, highly enriched in PHA-storing organisms (88%), reached a maximum PHA content of 74.6%.

Strategies for the development of a side stream process for polyhydroxyalkanoate (PHA) production from sugar cane molasses.

A three-stage process was developed to produce polyhydroxyalkanoates (PHAs) from sugar cane molasses. The process includes (1) molasses acidogenic fermentation, (2) selection of PHA-accumulating cultures, (3) PHA batch accumulation using the enriched sludge and fermented molasses. In the fermentation step, the effect of pH (5-7) on the organic acids profile and productivity was evaluated. At higher pH, acetic and propionic acids were the main products, while lower pH favoured the production of butyric and valeric acids. PHA accumulation using fermented molasses was evaluated with two cultures selected either with acetate or fermented molasses. The effect of organic acids distribution on polymer composition and yield was evaluated with the acetate selected culture. Storage yields varied from 0.37 to 0.50Cmmol HA/Cmmol VFA. A direct relationship between the type of organic acids used and the polymers composition was observed. Low ammonia concentration (0.1Nmmol/l) in the fermented molasses stimulated PHA storage (0.62Cmmol HA/Cmmol VFA). In addition, strategies of reactor operation to select a PHA-accumulating culture on fermented molasses were developed. The combination of low organic loading with high ammonia concentration selected a culture with a stable storage capacity and with a storage yield (0.59Cmmol HA/Cmmol VFA) similar to that of the acetate-selected culture.