The utilization of glycogen accumulating organisms for mixed culture production of polyhydroxyalkanoates

Production of polyhydroxyalkanoates (PHAs) by an open mixed culture enriched in glycogen accumulating organisms (GAOs) under alternating anaerobic–aerobic conditions with acetate as carbon source was investigated. The culture exhibited a stable enrichment performance over the 450‐day operating period with regards to phenotypic behavior and microbial community structure. Candidatus Competibacter phosphatis dominated the culture at between 54% and 70% of the bacterial biomass throughout the study, as determined by fluorescence in situ hybridization. In batch experiments under anaerobic conditions, PHA containing 3‐hydroxybutyrate (3HB) and 27 mol‐% 3‐hydroxyvalerate (3HV) was accumulated up to 49% of cell dry weight utilizing the glycogen pool stored in the SBR cycle. Under aerobic and ammonia limited conditions, PHA comprising only 3HB was accumulated to 60% of cell dry weight. Glycogen was consumed during aerobic PHA accumulation as well as under anaerobic conditions, but with different stoichiometry. Under aerobic conditions 0.31 C‐mol glycogen was consumed per consumed C‐mol acetate compared to 0.99 under anaerobic conditions. Both the PHA biomass content and the specific PHA production rate obtained were similar to what is typically obtained using the more commonly applied aerobic dynamic feeding strategy. Biotechnol. Bioeng. 2009; 104: 698–708 © 2009 Wiley Periodicals, Inc.     

Polyhydroxyalkanoate biosynthesis in Bacillus cereus SPV under varied limiting conditions and an insight into the biosynthetic genes involved

Aims:  A new strain of Bacillus, Bacillus cereus SPV, was found to be capable of using a wide range of carbon sources for the production of polyhydroxyalkanoates (PHAs) ( Valappil et al. 2007b ). Limiting nutrient in the culture conditions is crucial for PHA production. In this study, B.   cereus SPV was grown in different culture conditions with limitation of potassium, nitrogen, sulphur and phosphorous to establish the impact of nutritional limitation on PHA production.
Methods and Results:  The PHA yields obtained were found to be 13·4, 38, 13·15 and 33·33% dcw for potassium, nitrogen, sulphur and phosphorus limitations, respectively. Gas chromatography–mass spectrometry analysis of the isolated polymers showed the presence of P(3HB) under nitrogen, sulphur and phosphate-limiting conditions and P(3HB-3HV) copolymer under potassium limiting conditions. This ability of B. cereus SPV to accumulate different PHA monomers from structurally unrelated carbon sources led to an interest in the molecular analysis of PHA biosynthesis in this organism. To achieve this, PCR was used to identify the polyhydroxyalkanoate biosynthetic genes in B. cereus SPV.
Conclusion:  Sequence analysis of the PCR products from B. cereus SPV revealed the sequence of the putative biosynthetic genes, and possible regions involved in substrate binding.
The nucleotide sequence reported in this paper is in the GenBank nucleotide sequence database under accession number DQ486135 .
Significance and Impact of the Study:  This is the first report comparing the capability of B. cereus SPV to produce PHAs under different culture conditions of potassium, nitrogen, sulfur and phosphate limitations. The results in this study suggest the unique ability of B. cereus SPV to supply both 3HB and 3HV monomers from a structurally unrelated carbon source, glucose.     

Community Structure Evolution and Enrichment of Glycogen-Accumulating Organisms Producing Polyhydroxyalkanoates from Fermented Molasses

An open mixed culture was enriched with glycogen-accumulating organisms (GAOs) by using a sequencing batch reactor and treating an agroindustrial waste (sugar cane molasses) under cyclic anaerobic-aerobic conditions. Over a 1-year operating period, the culture exhibited a very stable GAO phenotype with an average polyhydroxyalkanoate (PHA) content of 17% total suspended solids. However, the GAO microbial community evolved over the course of operation to a culture exhibiting unusual characteristics in producing PHAs comprised of short-chain-length monomers, namely, 3-hydroxybutyrate, 3-hydroxy-2-methylbutyrate, 3-hydroxyvalerate, and 3-hydroxy-2-methylvalerate, and also, up to 31 mol% of the medium-chain-length (MCL) monomer 3-hydroxyhexanoate (3HHx). Microbial community analysis by fluorescence in situ hybridization revealed a concurrent long-term drift in the GAO community balance, from mainly “Candidatus Competibacter phosphatis” to mainly Defluviicoccus vanus-related organisms. The production of 3HHx was confirmed by ¹³C nuclear magnetic resonance (NMR) and appeared to be related to the increased presence of D. vanus-related GAOs. These results suggest a broadened spectrum of material, chemical, and mechanical properties that can be achieved for biopolymers produced by open mixed cultures from fermented waste. The increased spectrum of polymer properties brings a wider scope of potential applications.Polyhydroxyalkanoates (PHAs) are biopolymers synthesized by bacteria as intracellular reserves of carbon, energy, and reducing power, with physical properties that make them an attractive source of biobased thermoplastics. These polymers are completely biodegradable and biocompatible and show promise for a broad range of engineering applications, from commodity to high-value-added specialty niche products (27).The most common PHAs are homopolymers of 3-hydroxybutyrate [P(3HB)] and copolymers with, for example, 3-hydroxyvalerate (3HV) [P(3HB-co-3HV)]. The homopolymer P(3HB) is highly crystalline with low impact strength. The copolymer P(3HB-co-3HV) exhibits contrasting mechanical properties, such as lower crystallinity and an increased impact strength and flexibility due to the incorporation of 3HV units. The copolymers with P(3HB) thus exhibit properties that are strongly dependent on the type and content of additional monomer elements. The incorporation of monomers other than 3HV may further extend the scope for PHA applications by tailoring the polymer''s mechanical properties (8, 17).The industrial production of PHAs is currently conducted using bacterial cultures of pure or recombinant strains that require sterile production conditions and strict process control. This state of the art has a high energy demand and, consequently, high production costs relative to those of, for example, polypropylene. Furthermore, well-defined and expensive substrates, such as glucose or propionic acid, are used as feedstock, contributing even further to the relatively high costs of production (10). As a result and notwithstanding the potential environmental benefits of a biodegradable thermoplastic, PHA production economics represent a considerable obstacle to widespread commercial use of these polymers.In the search for more cost-effective PHA production, one promising cost-saving strategy is to use open mixed microbial cultures constrained by selection pressures of the process operating environment (17). With the right operating conditions, it is possible to select for a microbial culture with high PHA storage ability. The application of open mixed cultures avoids costs in sterilization and simplifies the process control, given that it is designed based on the ecological role of species survival with PHAs. Additionally, agroindustrial wastes and by-products, such as olive oil mill effluents (18), sugar cane molasses (1), or paper mill wastewater (7), may be used as the carbon source (42), rather than refined organic substrates.To date, the research on PHA production by mixed cultures has been conducted mostly with aerobic dynamic feeding (ADF) systems, also known as “feast and famine” enrichment, where the substrate is provided intermittently and microbial growth occurs under non-steady-state conditions (1, 7, 19, 32, 42). An alternative approach to ADF is an anaerobic-aerobic selection strategy, where electron donor and acceptor are separated (i.e., the carbon source is provided intermittently and under anaerobic conditions). For a bioreactor inoculated with activated sludge, such anaerobic-aerobic selection in the absence of excess phosphorus concentrations promotes enrichment of a specific group of bacteria, glycogen-accumulating organisms (GAOs) (14, 38). GAOs have been thoroughly investigated in the context of enhanced biological phosphate removal (38).The GAO phenotype occurs when an external source of soluble carbon (volatile fatty acids [VFAs]) is taken up anaerobically and stored as PHAs at the expense of intracellular glycogen. Glycogen is hydrolyzed in order to provide energy (ATP), reducing power (NADH), and PHA precursors. In the subsequent aerobic phase, PHAs are used as a source of carbon, energy, and reducing power for cell growth, maintenance, and glycogen replenishment (36).This GAO phenotype has been observed for a number of bacterial organisms: “Candidatus Competibacter phosphatis,” belonging to the Gammaproteobacteria phylum (11); Sphingomonadales-related organisms, belonging to the Alphaproteobacteria phylum (5); and cluster 1 (48) and cluster 2 (35) Defluviicoccus vanus-related organisms, also belonging to the Alphaproteobacteria phylum. The latter organisms belonging to the Alphaproteobacteria phylum typically appear in arrangements of four or more cells and are generally referred to as tetrad-forming organisms (47). To date, no pure cultures of these organisms have been isolated. They have all been identified in situ with techniques such as fluorescence in situ hybridization (FISH).In ADF mixed-culture systems fed with complex substrates, different bacterial groups may possibly develop, with different substrate affinities and metabolisms. The net result can be the production of different homopolymers rather than one copolymer. Although GAO mixed cultures may include several bacterial strains, all will have the same type of metabolism, involving glycogen turnover. GAOs use glycogen for polymer production in conjunction with the external substrates provided, making it more feasible to control for a true copolymer production (14). However, utilization of GAOs for PHA production has mainly been studied using synthetic substrates (13, 14). Only one previous study with a complex fermented waste, a paper mill wastewater, was reported (6).In the present investigation, enrichment of GAOs using fermented sugar cane molasses, a carbon source that has been studied previously for ADF enrichment (1), was studied. The enrichment of the GAO culture for PHA production was accomplished at laboratory scale with an anaerobic-aerobic sequencing batch reactor (SBR). The laboratory system was operated over a 1-year period, and the evolution of both phenotypic and genotypic characteristics of the microbial community was systematically evaluated.     

Characterisation of polyhydroxyalkanoate copolymers with controllable four-monomer composition

Polyhydroxyalkanoate (PHA) copolymers comprising the four monomers 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), 3-hydroxy-2-methylvalerate (3HMV) and 3-hydroxy-2-methylbutyrate (3HMB) were generated using the recently discovered Defluviicoccus vanus-related glycogen accumulating organisms (DvGAOs) under anaerobic conditions without applying any nutrient limitations. The composition could be manipulated in a defined range by modifying the ratio of propionate and acetate provided in the feed stream. The PHAs produced were characterised as random copolymers (from propionate alone) or a mixture of random copolymers (from mixture of propionate and acetate) through microstructure analysis using 13C NMR spectroscopy. The sequence distribution of all eight comonomer pairs in the carbonyl region of 3HB and 3HV was identified and assigned with confidence utilising two-dimensional heteronuclear multiple bond coherence (HMBC) spectroscopy. Weight average molecular weights were in the range 390-560 kg/mol. Differential scanning calorimetry (DSC) traces showed that the melting temperature (Tm) varied between 70 and 161 degrees C and glass transition temperature (Tg) ranged from -8 to 0 degrees C. The incorporation of considerable amounts of 3HMV and 3HMB monomer units introduced additional "defects" into the PHBV copolymer structure and hence greatly lowered the crystallinity. The data indicate the potential of these four-monomer PHAs to be employed for practical applications, considering their favourable properties and the cost-effective production process using a mixed culture and simple carbon sources.     

Model-based analysis of anaerobic acetate uptake by a mixed culture of polyphosphate-accumulating and glycogen-accumulating organisms

An increasing number of studies shows that the glycogen-accumulating organisms (GAOs) can survive and may indeed proliferate under the alternating anaerobic/aerobic conditions found in EBPR systems, thus forming a strong competitor of the polyphosphate-accumulating organisms (PAOs). Understanding their behaviors in a mixed PAO and GAO culture under various operational conditions is essential for developing operating strategies that disadvantage the growth of this group of unwanted organisms. A model-based data analysis method is developed in this paper for the study of the anaerobic PAO and GAO activities in a mixed PAO and GAO culture. The method primarily makes use of the hydrogen ion production rate and the carbon dioxide transfer rate resulting from the acetate uptake processes by PAOs and GAOs, measured with a recently developed titration and off-gas analysis (TOGA) sensor. The method is demonstrated using the data from a laboratory-scale sequencing batch reactor (SBR) operated under alternating anaerobic and aerobic conditions. The data analysis using the proposed method strongly indicates a coexistence of PAOs and GAOs in the system, which was independently confirmed by fluorescent in situ hybridization (FISH) measurement. The model-based analysis also allowed the identification of the respective acetate uptake rates by PAOs and GAOs, along with a number of kinetic and stoichiometric parameters involved in the PAO and GAO models. The excellent fit between the model predictions and the experimental data not involved in parameter identification shows that the parameter values found are reliable and accurate. It also demonstrates that the current anaerobic PAO and GAO models are able to accurately characterize the PAO/GAO mixed culture obtained in this study. This is of major importance as no pure culture of either PAOs or GAOs has been reported to date, and hence the current PAO and GAO models were developed for the interpretation of experimental results of mixed cultures. The proposed method is readily applicable for detailed investigations of the competition between PAOs and GAOs in enriched cultures. However, the fermentation of organic substrates carried out by ordinary heterotrophs needs to be accounted for when the method is applied to the study of PAO and GAO competition in full-scale sludges.     

Polyhydroxyalkanoate (PHA) biosynthesis from structurally unrelated carbon sources by a newly characterized Bacillus spp

A newly acquired polyhydroxyalkanoate (PHA) producing Bacillus spp. was identified to be a strain of Bacillus cereus using a range of microbiological and molecular techniques. This strain, named B. cereus SPV, was found to be capable of using a wide range of carbon sources including glucose, fructose, sucrose, various fatty acids and gluconate for the production of PHAs, an advantage for the commercial production of the polymers. The media used for the polymer production was novel in the context of the genus Bacillus. The PHA, once produced, was found to remain at a constant maximal concentration, without any degradation, a great advantage for the commercial production of the PHAs. This particular strain of Bacillus spp. was able to synthesize various PHAs with 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV) and 4-hydroxybutyrate (4HB)-like monomer units from structurally unrelated carbon sources such as fructose, sucrose and gluconate. This is the first report of the incorporation of a 4HB related monomer containing PHA by the genus Bacillus and from structurally unrelated carbon sources. The PHAs isolated had molecular weights ranging between (0.4 and 0.8) x 10(6) and low polydispersity index values (M(W)/M(N)) ranging from 2.6 to 3.4.     

Biopolymers production from mixed cultures and pyrolysis by-products

Polyhydroxyalkanoates (PHAs) production from low value substrates and/or byproducts represents an economical and environmental promising alternative to established industrial manufacture methods. Bio-oil resulting from the fast-pyrolysis of chicken beds was used as substrate to select a mixed microbial culture (MMC) able to produce PHA under feast/famine conditions. In this study a maximum PHA content of 9.2% (g/g cell dry weight) was achieved in a sequencing batch reactor (SBR) operated for culture selection. The PHA obtained with bio-oil as a carbon source was a copolymer composed by 70% of hydroxybutyrate (HB) and 30% of hydroxyvalerate (HV) monomers. Similar results have been reported by other studies that use real complex substrates for culture selection indicating that bio-oil can be a promising feedstock to produce PHAs using MMC. To the best of our knowledge this is the first study that demonstrated the use of bio-oil resulting from fast pyrolysis as a possibly feedstock to produce short chain length polyhydroxyalkanoates.     

Biosynthesis of Polyhydroxyalkanaotes by a Novel Facultatively Anaerobic <Emphasis Type="Italic">Vibrio</Emphasis> sp. under Marine Conditions

Marine bacteria have recently attracted attention as potentially useful candidates for the production of practical materials from marine ecosystems, including the oceanic carbon dioxide cycle. The advantages of using marine bacteria for the biosynthesis of poly(hydroxyalkanoate) (PHA), one of the eco-friendly bioplastics, include avoiding contamination with bacteria that lack salt-water resistance, ability to use filtered seawater as a culture medium, and the potential for extracellular production of PHA, all of which would contribute to large-scale industrial production of PHA. A novel marine bacterium, Vibrio sp. strain KN01, was isolated and characterized in PHA productivity using various carbon sources under aerobic and aerobic–anaerobic marine conditions. The PHA contents of all the samples under the aerobic–anaerobic condition, especially when using soybean oil as the sole carbon source, were enhanced by limiting the amount of dissolved oxygen. The PHA accumulated using soybean oil as a sole carbon source under the aerobic–anaerobic condition contained 14% 3-hydroxypropionate (3HP) and 3% 5-hydroxyvalerate (5HV) units in addition to (R)-3-hydroxybutyrate (3HB) units and had a molecular weight of 42 × 10³ g/mol. The present result indicates that the activity of the beta-oxidation pathway under the aerobic–anaerobic condition is reduced due to a reduction in the amount of dissolved oxygen. These findings have potential for use in controlling the biosynthesis of long main-chain PHA by regulating the activity of the beta-oxidation pathway, which also could be regulated by varying the dissolved oxygen concentration.     

Metabolic model for acetate uptake by a mixed culture of phosphate- and glycogen-accumulating organisms under anaerobic conditions

This paper proposes a new metabolic model for acetate uptake by a mixed culture of phosphate- and glycogen-accumulating organisms (PAOs and GAOs) under anaerobic conditions. The model uses variable overall stoichiometry based on the assumption that PAOs may have the ability of using the glyoxylate pathway to produce the required reducing power for polyhydroxyalkonate (PHA) synthesis. The proposed model was tested and verified by experimental results. A sequencing batch reactor system was operated for enhanced biological phosphorus removal (EBPR) with acetate as the sole carbon source at different influent acetate/phosphate ratios. The resulting experimental data supported the validity of the proposed model, indicating the presence of GAOs for all tested HAc/P ratios, especially under P-limiting conditions. Strong agreement is observed between experimental values and model predictions for all model components, namely, PHB production, PHA composition, glycogen utilization, and P release.     

The effect of carbon source supplementation on the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by Cupriavidus necator

The objective of the present study was to investigate the ability of Cupriavidus necator to produce poly-(3-hydroxybutyrate-co-3-hydroxyvalerate) on various carbon sources in batch cultivation. These results show that C. necator produces poly-3-hydroxybutyrate from single carbon sources. The highest poly-3-hydroxybutyrate (P3HB) content was achieved at growth on fructose in the exponential growth phase. The maximum yield of the P3HV content was obtained when fructose was mixed with acetate. The highest content P3HB-co-3HV was also achieved by C. necator when we supplied C-excess and N- and P-normal conditions. These results indicate that C. necator accumulates high polyhydroxyalkanoates (PHA) content by depleting these elements in the culture medium. Nitrogen and phosphorus limitation has no significant effect on the PHA production, whereas C-excess leads to an increase in PHA formation of up to 92% PHAs of cell dry weight after growth on 5 g/L acetate and 40 g/L fructose.     

Metabolic model for glycogen-accumulating organisms in anaerobic/aerobic activated sludge systems

Glycogen-accumulating organisms (GAO) have the potential to directly compete with polyphosphate-accumulating organisms (PAO) in EBPR systems as both are able to take up VFA anaerobically and grow on the intracellular storage products aerobically. Under anaerobic conditions GAO hydrolyse glycogen to gain energy and reducing equivalents to take up VFA and to synthesise polyhydroxyalkanoate (PHA). In the subsequent aerobic stage, PHA is being oxidised to gain energy for glycogen replenishment (from PHA) and for cell growth. This article describes a complete anaerobic and aerobic model for GAO based on the understanding of their metabolic pathways. The anaerobic model has been developed and reported previously, while the aerobic metabolic model was developed in this study. It is based on the assumption that acetyl-CoA and propionyl-CoA go through the catabolic and anabolic processes independently. Experimental validation shows that the integrated model can predict the anaerobic and aerobic results very well. It was found in this study that at pH 7 the maximum acetate uptake rate of GAO was slower than that reported for PAO in the anaerobic stage. On the other hand, the net biomass production per C-mol acetate added is about 9% higher for GAO than for PAO. This would indicate that PAO and GAO each have certain competitive advantages during different parts of the anaerobic/aerobic process cycle.     

Comparison of acetate and propionate uptake by polyphosphate accumulating organisms and glycogen accumulating organisms

Enhanced biological phosphorus removal (EBPR) performance is directly affected by the competition between polyphosphate accumulating organisms (PAOs) and glycogen accumulating organisms (GAOs). This study investigates the effects of carbon source on PAO and GAO metabolism. Enriched PAO and GAO cultures were tested with the two most commonly found volatile fatty acids (VFAs) in wastewater systems, acetate and propionate. Four sequencing batch reactors (SBRs) were operated under similar conditions and influent compositions with either acetate or propionate as the sole carbon source. The stimulus for selection of the PAO and GAO phenotypes was provided only through variation of the phosphorus concentration in the feed. The abundance of PAOs and GAOs was quantified using fluorescence in situ hybridisation (FISH). In the acetate fed PAO and GAO reactors, "Candidatus Accumulibacter phosphatis" (a known PAO) and "Candidatus Competibacter phosphatis" (a known GAO) were present in abundance. A novel GAO, likely belonging to the group of Alphaproteobacteria, was found to dominate the propionate fed GAO reactor. The results clearly show that there are some very distinctive differences between PAOs and GAOs in their ability to take up acetate and propionate. PAOs enriched with acetate as the sole carbon source were immediately able to take up propionate, likely at a similar rate as acetate. However, an enrichment of GAOs with acetate as the sole carbon source took up propionate at a much slower rate (only about 5% of the rate of acetate uptake on a COD basis) during a short-term switch in carbon source. A GAO enrichment with propionate as the sole carbon source took up acetate at a rate that was less than half of the propionate uptake rate on a COD basis. These results, along with literature reports showing that PAOs fed with propionate (also dominated by Accumulibacter) can immediately switch to acetate, suggesting that PAOs are more adaptable to changes in carbon source as compared to GAOs. This study suggests that the PAO and GAO competition could be influenced in favour of PAOs through the provision of propionate in the feed or even by regularly switching the dominant VFA species in the wastewater. Further study is necessary in order to provide greater support for these hypotheses.     

A metabolic model for acetate uptake under anaerobic conditions by glycogen accumulating organisms: Stoichiometry, kinetics, and the effect of pH

A metabolic model for the stoichiometry of acetate uptake under anaerobic conditions by an enriched culture of glycogen accumulating organisms (GAOs) was developed and tested by experimental studies. Glycogen served as the source of both reducing power and energy to drive the process of acetate uptake. The amount of glycogen consumed and poly-beta-hydroxyvalerate (PHV) accumulated in the cells increased with increasing pH, indicating that the energy requirements for acetate uptake increased with pH. The composition of the accumulated poly-beta-hydroxyalkanoates (PHAs) was adequately predicted using the assumption that acetyl-CoA and propionyl-CoA condense randomly to produce PHA. In addition, the rate of acetate uptake was strongly affected by the pH. The rate decreased with increasing pH and this dependence could be described with a saturation type of expression. A comparison of the rate of acetate uptake at low pH with the rates observed in enriched cultures of phosphorus accumulating organisms (PAOs) indicated that GAOs are able to compete effectively with PAOs in nutrient removal systems under certain conditions.     

Biosynthetic polyesters consisting of 2-hydroxyalkanoic acids: current challenges and unresolved questions

2-Hydroxyalkanoates (2HAs) have become the new monomeric constituents of bacterial polyhydroxyalkanoates (PHAs). PHAs containing 2HA monomers, lactate (LA), glycolate (GL), and 2-hydroxybutyrate (2HB) can be synthesized by engineered microbes in which the broad substrate specificities of PHA synthase and propionyl-CoA transferase are critical factors for the incorporation of the monomers into the polymer chain. LA-based polymers, such as P[LA-co-3-hydroxybutyrate (3HB)], have the properties of pliability and stretchiness which are distinctly different from those of the rigid poly(lactic acid) (PLA) and P(3HB) homopolymers. This versatile platform is also applicable to the biosynthesis of GL- and 2HB-based polymers. In the case of the synthesis of 2HB-based polymers, the enantiospecificity of PHA synthase enabled the production of isotactic (R)-2HB-based polymers, including P[(R)-2HB], from racemic precursors of 2HB. P(2HB) is a pliable material, in contrast to PLA. Furthermore, to obtain a new 2HA-polymerizing PHA synthase, the class I PHA synthase from Ralstonia eutropha was engineered so as to achieve the first incorporation of LA units. The analysis of the polymer synthesized using this new LA-polymerizing PHA synthase unexpectedly focused a spotlight on the studies on block copolymer biosynthesis.     

Elucidation of metabolic pathways in glycogen-accumulating organisms with in vivo 13C nuclear magnetic resonance

Glycogen-accumulating organisms (GAOs) are found in enhanced biological phosphorus removal systems where they compete with polyphosphate-accumulating organisms for external carbon substrates. (13)C nuclear magnetic resonance ((13)C-NMR) was used to elucidate the metabolic pathways operating in an enriched GAO culture dominated by two known GAOs (81.2%). The experiments consisted of adding (13)C-acetate (labelled on position 1 or 2) to the culture under anaerobic conditions, and operating the culture through a cycle consisting of an anaerobic, an aerobic and a further anaerobic phase. The carbon transformations over the cycle were monitored using in vivo(13)C-NMR. The two-carbon moieties in hydroxybutyrate and hydroxyvalerate were derived from acetate, while the propionyl precursor of hydroxyvalerate was primarily derived from glycogen, with only a small fraction originating from acetate. Comparison of the labelling patterns in hydroxyvalerate at the end of the first and the second anaerobic periods in pulse experiments with 2-(13)C-acetate showed that the Entner-Doudoroff (ED) pathway was used for the breakdown of glycogen. This conclusion was further supported by the labelling pattern on glycogen observed in the pulse experiments with 1-(13)C-acetate, which can only be explained by the operation of ED with recycling of pyruvate and glyceraldehyde 3-phosphate via gluconeogenesis. The activity of the ED pathway for glycogen degradation by GAOs is demonstrated here for the first time. In addition, the decarboxylating part of the tricarboxylic acid cycle was confirmed to operate also under anaerobic conditions.     

Poly(3-hydroxybutyrate) production by Bacillus cereus SPV using sugarcane molasses as the main carbon source

The main hindrance in the use of polyhydroxyalkanoates (PHAs) as a replacement for existing petroleum-based plastics is their high production cost. The carbon source accounts for 50% of the cost for PHA production. Thus, increasing the yield and productivity of PHAs on cheap substrates is an important challenge for biotechnologists to support the commercialization and further applications of these polymers. In this study, we have investigated the use of an agricultural raw material, sugarcane molasses, as the main carbon source for poly(3-hydroxybutyrate) (P(3HB)) production by Bacillus cereus SPV. These studies were carried out in both shaken flasks and 2 L bioreactors. Various conditions were evaluated for their effects on biomass and P(3HB) accumulation. A high polymer yield was obtained, 61.07% dry cell weight (DCW) in a 1 L shaken flask study and 51.37% DCW in a 2 L fermenter study. These yields are 50% higher than previously observed with Bacillus cereus SPV. Hence, the results are encouraging and show that sugarcane molasses are a promising carbon source for an economical and commercially viable production of P(3HB).     

Formation of poly(3-hydroxyalkanoates) by phototrophic and chemolithotrophic bacteria

The formation of poly(3-hydroxyalkanoic acid), PHA, by various strains of chemolithotrophic and phototrophic bacteria has been examined. Chemolithotrophic bacteria were grown aerobically under nitrogen-limiting conditions on various aliphatic organic acids. Phototrophic bacteria were grown anaerobically in the light on a nitrogen-rich medium and were subsequently transferred to a nitrogen-free medium containing acetate, propionate, valerate, heptanoate or octanoate as carbon source. All 41 strains investigated in this study were able to synthesize and accumulate PHA. All 11 strains of chemolithotrophic bacteria and all 15 strains belonging to the non-sulfur purple bacteria synthesized a polymer, which contained 3-hydroxy-valerate (3HV) beside 3-hydroxybutyrate (3HB), if the cells were cultivated in the presence of propionate, valerate or heptanoate. Many non-sulfur purple bacteria synthesized copolyesters of 3HB and 3HV even with acetate as carbon source. In contrast, most sulfur purple bacteria did not incorporate 3HV at all. Among 15 strains tested, only Chromatium vinosum strain 1611, C. purpuratum strain BN5500 and Lamprocystis roseopersicina strain 3112 were able to synthesize polyesters containing 3HV with propionate, valerate or heptanoate as carbon source.     

Effect of carbon source on the formation of polyhydroxyalkanoates (PHA) by a phosphate-accumulating mixed culture

In the present work, attention was devoted to understand how different carbon substrates and their concentration can influence the production of PHA by polyphosphate-accumulating bacteria. Acetate, propionate, and butyrate were tested independently. The composition of the polymers formed was found to vary with the substrate used. Acetate leads to the production of a copolymer of hydroxybutyrate (HB) and hydroxyvalerate (HV) with the HB units being dominant. With propionate, HV units are mainly produced and only a small amount of HB is synthesized. When butyrate is used, the amount of polymer formed is much lower with the HB units being produced to a higher extent. The yield of polymer produced per carbon consumed (Y_P/S) was found to diminish from acetate (0.97) to propionate (0.61) to butyrate (0.21). Using a mixture of acetate, propionate, and butyrate and increasing the carbon concentration, although maintaining the relative concentration of each substrate, propionate is primarily consumed and consequently, PHA synthesized was enriched in HV units. The polymers obtained in all experiments were copolymers with the average molecular weight of the most representative fraction higher when hydroxybutyrate units were present in considerable amounts. All the polymers synthesized were found to be quite homogeneous and their average molecular weight is of the same order of magnitude as the ones commercially available.     

Recent advances in polyhydroxyalkanoate production by bacterial fermentation: mini-review.

Poly(3-hydroxybutyrate) [P(3HB)] and other polyhydroxyalkanoates (PHAs) have been drawing much attention as biodegradable substitutes for conventional nondegradable plastics. For the economical production of P(3HB), various bacterial strains, either wild-type or recombinant, and new fermentation strategies were developed for the production of P(3HB) with high concentration and productivity. To reduce the cost of carbon substrate, several processes for P(3HB) production from cheap carbon sources were also developed. P(3HB) can now be produced to a content of 80% of cell dry weight with the productivity greater than 4 g/l per h. Fermentation strategy was also developed for the efficient production of medium chain length PHA by high cell density culture. With all these advances, P(3HB) and PHAs can be produced by bacterial fermentation at a cost (ca. $2/kg) similar to that of other biodegradable polymers under development.     

Role of glycogen in acetate uptake and polyhydroxyalkanoate synthesis in anaerobic-aerobic activated sludge with a minimized polyphosphate content

The role of glycogen in the uptake of acetate in anaerobic-aerobic activated sludge without enhanced biological phosphorus removal were investigated. Although the polyphosphate content of the sludge was minimized by lowering the phosphorus feeding concentration, significant acetate uptake and accumulation of polyhydroxyalkanoates (PHAs) were observed in proportion to glycogen consumption under anaerobic conditions. The results of anaerobic inhibition studies, which showed suppressive effects on acetate uptake by a glycolysis inhibitor (iodoacetate) but not by a membrane ATPase inhibitor (N,N′-dicyclohexyl carbodiimide), supported an assumption that glycogen degradation through glycolysis supplies the required ATP and reducing power for PHA synthesis from acetate and consumed glycogen. Under subsequent aerobic conditions, the accumulated PHAs were depleted and the consumed glycogen recovered to the same level as that at the start of the anaerobic phase. Iodoacetate also inhibited the recovery of glycogen under aerobic conditions, suggesting that nearly 50% of the PHAs depleted was used for glycogen synthesis through reversed glycolysis.