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Polyhydroxybutyrate (PHB) is a bio-based, biodegradable and biocompatible plastic that has the potential to replace petroleum-based plastics. Lignocellulosic biomass is a promising feedstock for industrial fermentation to produce bioproducts such as polyhydroxybutyrate (PHB). However, the pretreatment processes of lignocellulosic biomass lead to the generation of toxic byproducts, such as furfural, 5-HMF, vanillin, and acetate, which affect microbial growth and productivity. In this study, to reduce furfural toxicity during PHB production from lignocellulosic hydrolysates, we genetically engineered Cupriavidus necator NCIMB 11599, by inserting the nicotine amide salvage pathway genes pncB and nadE to increase the NAD(P)H pool. We found that the expression of pncB was the most effective in improving tolerance to inhibitors, cell growth, PHB production and sugar consumption rate. In addition, the engineered strain harboring pncB showed higher PHB production using lignocellulosic hydrolysates than the wild-type strain. Therefore, the application of NAD salvage pathway genes improves the tolerance of Cupriavidus necator to lignocellulosic-derived inhibitors and should be used to optimize PHB production.

The chemolithotroph Cupriavidus necator H16 is known as a natural producer of the bioplastic-polymer PHB, as well as for its metabolic versatility to utilize different substrates, including formate as the sole carbon and energy source. Depending on the entry point of the substrate, this versatility requires adjustment of the thermodynamic landscape to maintain sufficiently high driving forces for biological processes. Here we employed a model of the core metabolism of C. necator H16 to analyze the thermodynamic driving forces and PHB yields from formate for different metabolic engineering strategies. For this, we enumerated elementary flux modes (EFMs) of the network and evaluated their PHB yields as well as thermodynamics via Max-min driving force (MDF) analysis and random sampling of driving forces. A heterologous ATP:citrate lyase reaction was predicted to increase driving force for producing acetyl-CoA. A heterologous phosphoketolase reaction was predicted to increase maximal PHB yields as well as driving forces. These enzymes were then verified experimentally to enhance PHB titers between 60 and 300% in select conditions. The EFM analysis also revealed that PHB production from formate may be limited by low driving forces through citrate lyase and aconitase, as well as cofactor balancing, and identified additional reactions associated with low and high PHB yield. Proteomics analysis of the engineered strains confirmed an increased abundance of aconitase and cofactor balancing. The findings of this study aid in understanding metabolic adaptation. Furthermore, the outlined approach will be useful in designing metabolic engineering strategies in other non-model bacteria.

The domination of high-cost organic acids over other 3-hydroxyvalerate (3HV) precursors due to the wide preference among polyhydroxyalkanoates (PHA)-producing bacteria has limited the development of diverse poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] production processes. 1-pentanol is a low-cost 3HV precursor but is rarely employed due to the relatively low tolerance among PHA-producing bacteria. This study demonstrated P(3HB-co-3HV) production with manipulable and reproducible 3HV composition and 3HV yield from palm olein and 1-pentanol. Cupriavidus malaysiensis USMAA2-4

Šio tyrimo metu siekta įvertinti įvairių anglies šaltinių įtaką polihidroksialkanoatų sintezei, išeigai ir savybėms. Polihidroksialkanoatų sintezė buvo vykdoma naudojant tris bakterijų kultūras – Bacillus subtilis, Cupriavidus necator ir Escherichia coli. Anglies šaltiniai, pasirinkti tyrimui buvo cukranendrių cukrus, gliukozė, melasa, apdorota melasa, sacharozė ir stevija. Įvykdžius polihidroksialkanoatų šių mikroorganizmų polihidroksialkanoatų biosintezę su kiekvienu anglies šaltiniu, buvo atliekami susintetintų junginių savybių tyrimai. Įvertinus visus polihidroksialkanoatų išeigos rezultatus, nustatyta, kad didžiausia polihidroksialkanoatų koncentracija gauta iš Bacillus subtilis kultūros po 48 valandų fermentacijos, kai anglies šaltinis fermentacijos terpėje buvo cukranendrių cukrus (8,03 g/l). Tyrimo metu pagamintų polihidroksialkanoatų struktūra buvo įvertinta atliekant FTIR spektroskopiją. Siekiant išsiaiškinti junginių antioksidacinį aktyvumą, buvo atlikti DPPH, FRAP, ABTS radikalų slopinimo tyrimai bei redukcinių savybių tyrimas. Nustatyta, kad didžiausiomis redukcinėmis savybėmis pasižymėjo iš Escherichia coli pagaminti polihidroksialkanoatai, kurių anglies šaltinis buvo stevija (0,17 o. v.). Stipriausiomis redukcinėmis savybėmis pagal FRAP metodą pasižymėjo iš Cupriavidus necator gauti biopolimerai, kai anglies šaltinis buvo cukranendrių cukrus (0,0023 µmol/l). ABTS radikalą efektyviausiai slopino polihidroksialkanoatai, gauti iš Bacillus subtilis kultūros, kai anglies šaltinis buvo gliukozė (99,5 %)., The aim of this study was to evaluate the influence of different carbon sources on the synthesis, yield and properties of polyhydroxyalkanoates. The synthesis of polyhydroxyalkanoates was carried out using three bacterial cultures, Bacillus subtilis, Cupriavidus necator and Escherichia coli. The carbon sources chosen for the study were cane sugar, glucose, molasses, treated molasses, sucrose and stevia. After evaluation of all the yields of polyhydroxyalkanoates, it was found that the highest concentration of polyhydroxyalkanoates was obtained from the culture of Bacillus subtilis after a 48-hour fermentation with cane sugar as the carbon source in the fermentation medium (8,03 g/l). After the biosynthesis of polyhydroxyalkanoates of these microorganisms with each carbon source, the properties of the synthesised compounds were investigated. The structure of the polyhydroxyalkanoates produced in the study was evaluated by FTIR spectroscopy. DPPH, FRAP, ABTS radical scavenging assays and reductive property assay were carried out in order to elucidate the antioxidant activity of the compounds. The polyhydroxyalkanoates produced from Escherichia coli with stevia as the carbon source (0.17 o.v.) were found to have the highest reductive properties. The biopolymers obtained from Cupriavidus necator with cane sugar as the carbon source had the highest reducing properties according to the FRAP method (0,0023 µmol/l). The most effective inhibitor of the ABTS radical was the polyhydroxyalkanoates obtained from Bacillus subtilis culture with glucose as the carbon source (99,5 %).

Here a multiple heavy metal and antibiotic resistant bacterium Cupriavidus necator C39 (C. necator C39) was isolated from a Gold-Copper mine in Zijin, Fujian, China. C. necator C39 was able to tolerate intermediate concentrations of heavy metal(loid)s in Tris Minimal (TMM) Medium (Cu(II) 2 mM, Zn(II) 2 mM, Ni(II) 0.2 mM, Au(III) 70 μM and As(III) 2.5 mM). In addition, high resistance to multiple antibiotics was experimentally observed. Moreover, strain C39 was able to grow on TMM medium containing aromatic compounds such as benzoate, phenol, indole, p-hydroxybenzoic acid or phloroglucinol anhydrous as the sole carbon sources. The complete genome of this strain revealed 2 circular chromosomes and 1 plasmid, and showed the closest type strain is C. necator N-1T based on Genome BLAST Distance Phylogeny. The arsenic-resistance (ars) cluster GST-arsR-arsICBR-yciI and a scattered gene encoding the putative arsenite efflux pump ArsB were identified on the genome of strain C39, which thereby may provide the bacterium a robust capability for arsenic resistance. Genes encoding multidrug resistance efflux pump may confer high antibiotic resistance to strain C39. Key genes encoding functions in degradation pathways of benzene compounds, including benzoate, phenol, benzamide, catechol, 3- or 4-fluorobenzoate, 3- or 4-hydroxybenzoate and 3,4-dihydroxybenzoate, indicated its potential for degrading those benzene compounds.

Background Intracellular biomacromolecules, such as industrial enzymes and biopolymers, represent an important class of bio-derived products obtained from bacterial hosts. A common key step in the downstream separation of these biomolecules is lysis of the bacterial cell wall to effect release of cytoplasmic contents. Cell lysis is typically achieved either through mechanical disruption or reagent-based methods, which introduce issues of energy demand, material needs, high costs, and scaling problems. Osmolysis, a cell lysis method that relies on hypoosmotic downshock upon resuspension of cells in distilled water, has been applied for bioseparation of intracellular products from extreme halophiles and mammalian cells. However, most industrial bacterial strains are non-halotolerant and relatively resistant to hypoosmotic cell lysis. Results To overcome this limitation, we developed two strategies to increase the susceptibility of non-halotolerant hosts to osmolysis using Cupriavidus necator, a strain often used in electromicrobial production, as a prototypical strain. In one strategy, C. necator was evolved to increase its halotolerance from 1.5% to 3.25% (w/v) NaCl through adaptive laboratory evolution, and genes potentially responsible for this phenotypic change were identified by whole genome sequencing. The evolved halotolerant strain experienced an osmolytic efficiency of 47% in distilled water following growth in 3% (w/v) NaCl. In a second strategy, the cells were made susceptible to osmolysis by knocking out the large-conductance mechanosensitive channel (mscL) gene in C. necator. When these strategies were combined by knocking out the mscL gene from the evolved halotolerant strain, greater than 90% osmolytic efficiency was observed upon osmotic downshock. A modified version of this strategy was applied to E. coli BL21 by deleting the mscL and mscS (small-conductance mechanosensitive channel) genes. When grown in medium with 4% NaCl and subsequently resuspended in distilled water, this engineered strain experienced 75% cell lysis, although decreases in cell growth rate due to higher salt concentrations were observed. Conclusions Our strategy is shown to be a simple and effective way to lyse cells for the purification of intracellular biomacromolecules and may be applicable in many bacteria used for bioproduction.

Poly[(R)-3-hydroxybutyrate-co-(R)-3-hydroxyhexanoate] (PHBHHx) is a type of biopolyester of the polyhydroxyalkanoate group (PHA). Due to a wide range of properties resulting from the alteration of the (R)-3-hydroxyhexanoate (3HHx) composition, PHBHHx is getting a lot of attention as a substitute to conventional plastic materials for various applications. Cupriavidus necator H16 is the most promising PHA producer and has been genetically engineered to produce PHBHHx efficiently for many years. Nevertheless, the role of individual genes involved in PHBHHx biosynthesis is not well elaborated. C. necator H16 possesses six potential physiologically active β-ketothiolase genes identified by transcriptome analysis, i.e., phaA, bktB, bktC (h16_A0170), h16_A0462, h16_A1528, and h16_B0759. In this study, we focused on the functionality of these genes in vivo in relation to 3HHx monomer supply. Gene deletion experiments identified BktB and H16_A1528 as important β-ketothiolases for C6 metabolism in β-oxidation. Furthermore, in the bktB/h16_A1528 double-deletion strain, the proportion of 3HHx composition of PHBHHx produced from sugar was very low, whereas that from plant oil was significantly higher. In fact, the proportion reached 36.2 mol% with overexpression of (R)-specifc enoyl-CoA hydratase (PhaJ) and PHA synthase. Furthermore, we demonstrated high-density production (196 g/L) of PHBHHx with high 3HHx (32.5 mol%) by fed-batch fermentation with palm kernel oil. The PHBHHx was amorphous according to the differential scanning calorimetry analysis. KEY POINTS: • Role of six β-ketothiolases in PHBHHx biosynthesis was investigated in vivo. • Double-deletion of bktB/h16_A1528 results in high 3HHx composition with plant oil. • Amorphous PHBHHx with 32.5 mol% 3HHx was produced in high density by jar fermenter.

Recombinant Cupriavidus necator H16/pMPJAS03, expressing a P. putida KT2440 enoyl-CoA hydratase (phaJ), was able to synthesize short-chain-length/ medium-chain-length (scl-mcl) PHA copolymers with a high content of mcl subunits using its native poly(3-hydroxyalkanoate) synthase. The cells were cultivated on fructose with canola oil or canola oil/decanoic acid (DA) mixtures in fed-batch fermentations. The recombinant C. necator H16 (without any synthase modification) produced a polymer composed of 3-hydroxybutyrate (3HB) with mcl-subunits, including 3-hydroxyhexanoate (3HHx), and about 300-fold more 3-hydroxyoctanoate (3HO) than the yields reported in previous studies, as well as a significant amount of 3-hydroxydecanoate (3HD). Increasing the DA content in the feed from 0% to 15% v/v increased the molar content of the 3HD subunits from 1.2 to 2.1 mol%. The presence of larger monomers, such as 3HO and 3HD, decreased the crystallinity and melting temperature and modified the mechanical properties of the polymers. Thus, replacing either of the two gene products (phaJ or phaC1) required to produce PHA from CoA-3-hydroxy fatty acids with broader spectrum enzymes, is suitable for the production of commercially useful scl-mcl-PHA.

International audience; Plasmid expression level heterogeneity in Cupriavidus necator was studied in response to stringent culture conditions, supposed to enhance plasmid instability, through plasmid curing strategies. Two plasmid curing strategies were compared based on their efficiency at generating heterogeneity in batch: rifampicin addition and temperature increase. A temperature increase from 30 degrees to 37 degrees C was the most efficient plasmid curing strategy. To generate a heterogeneous population in terms of plasmid expression levels, successive batches at supra optimal culture temperature (i.e. 37 degrees C) were initially conducted. Three distinct fluorescent subpopulations P-0 (not fluorescent), P-1 (low fluorescence intensity, median = 1 10(3)) and P-2 (high fluorescence intensity, median = 6 10(3)) were obtained. From there, the chemostat culture was implemented to study the long-term stress response under well-controlled environment at defined dilution rates. For dilution rates comprised between 0.05 and 0.10 h(-1), the subpopulation P-2 (62% vs 90%) was favored compared to P1 cells (54% vs 1%), especially when growth rate increased. Our biosensor was efficient at discriminating subpopulation presenting different expression levels under stringent culture conditions. Plus, we showed that controlling growth kinetics had a stabilizing impact on plasmid expression levels, even under heterogeneous expression conditions.

Polyhydroxyalkanoates (PHAs) are emerging as alternatives to plastics by replacing fossil fuels with renewable raw substrates. Herein, we present the construction of engineered Escherichia coli strains to produce short-chain-length PHAs (scl-PHAs), including the monomers 4-hydroxyvalerate (4HV) and 3-hydroxyvalerate (3HV) produced from levulinic acid (LA). First, an E. coli strain expressing genes (lvaEDABC) from the levulinic acid metabolic pathway of Pseudomonas putida KT2440 was constructed to generate 4HV-CoA and 3HV-CoA. Second, both PhaAB enzymes from Cupriavidus necator H16 were expressed to supply 3-hydroxybutyrate (3HB)-CoA from acetyl-CoA. Finally, PHA synthase (PhaCCv) from Chromobacterium violaceum was introduced for the subsequent polymerization of these three monomers. The resulting E. coli strains produced four PHAs (w/w% of dry cell weight): 9.1 wt% P(4HV), 1.7 wt% P(3HV-co-4HV), 24.2 wt% P(3HB-co-4HV), and 35.6 wt% P(3HB-co-3HV-co-4HV).

Sequence-regulating polyhydroxyalkanoate synthase PhaC

Abstract Fluorescence spectroscopy offers a cheap, simple, and fast approach to monitor poly(3-hydroxybutyrate) (PHB) formation, a biodegradable polymer belonging to the biodegradable polyester class polyhydroxyalkanoates. In the present study, a fluorescence and side scatter-based spectroscopic setup was developed to monitor in situ biomass, and PHB formation of biotechnological applied Cupriavidus necator strain. To establish PHB quantification of C. necator, the dyes 2,2-difluoro-4,6,8,10,12-pentamethyl-3-aza-1-azonia-2-boranuidatricyclo[7.3.0.03,7]dodeca-1(12),4,6,8,10-pentaene (BODIPY493/503), ethyl 5-methoxy-1,2-bis(3-methylbut-2-enyl)-3-oxoindole-2-carboxylate (LipidGreen2), and 9-(diethylamino)benzo[a]phenoxazin-5-one (Nile red) were compared with each other. Fluorescence staining efficacy was obtained through 3D-excitation-emission matrix and design of experiments. The coefficients of determination were ≥ 0.98 for all three dyes and linear to the high-pressure liquid chromatography obtained PHB content, and the side scatter to the biomass concentration. The fluorescence correlation models were further improved by the incorporation of the biomass-related side scatter. Afterward, the resulting regression fluorescence models were successfully applied to nitrogen-deficit, phosphor-deficit, and NaCl-stressed C. necator cultures. The highest transferability of the regression models was shown by using LipidGreen2. The novel approach opens a tailor-made way for a fast and simultaneous detection of the crucial biotechnological parameters biomass and PHB content during fermentation. Key points • Intracellular quantification of PHB and biomass using fluorescence spectroscopy. • Optimizing fluorescence staining conditions and 3D-excitation-emission matrix. • PHB was best obtained by LipidGreen2, followed by BODIPDY493/503 and Nile red. Graphical abstract

In this study, a phaCR gene encoding PHA synthase was identified in Rhodoligotrophos defluvii which was adjacent to β-ketothiolase encoded by phaAR gene and acetoacetyl-CoA reductase encoded by phaBR gene. Amino acid comparison of PhaCR showed the highest homology of 65.98% with PhaC of R. appendicifer, while its homology with typical class I PHA synthase in Cupriavidus necator was only 42.54%. PHA synthesis genes were then transformed into E. coli harboring phaCABR and phaCRABC which were cultured with 15 g/L glucose respectively, and 20.46 wt% and 16.95 wt% of CDW for poly(3-hydroxybutyrate) (PHB) were accumulated respectively. To further explore the effect of substrate specificity for PHA production, the ptsG gene was then deleted and 15 g/L glucose and 1.5 g/L propionate were co-employed as carbon sources, which enabled the synthesis of poly(3HB-co-3HV) copolymer. As a result, poly(3HB-co-3HV) was accumulated up to 24.74 wt% of CDW, and the highest content of 3-hydroxyvalerate (3HV) was 10.86 mol%. The Td5 was 260 °C, which implied that it possessed good thermal stability, and the Mw of GPC in recombinant strains were between 22 and 26 × 104 g/mol, and the highest PDI was 3.771. The structure of poly (3HB-co-3HV) copolymer was determined through 1H NMR analysis.

Polyhydroxyalkanoates are attractive alternatives to traditional plastics. However, although polyhydroxybutyrate (PHB) is produced in large quantities by Cupriavidus necator H16, its properties are far from ideal for the manufacture of plastic products. These properties may be improved through its coproduction with 3-hydroxypropionate (3HP), which leads to the formation of the copolymer poly(3-hydroxybutyrate-co-3-hydroxypropionate) (poly(3HB-co-3HP). To achieve this, a pathway was designed to enable C. necator H16 to convert β-alanine to 3HP. The initial low levels of incorporation of 3HP into the copolymer were overcome by the overproduction of the native propionyl-CoA transferase together with PHA synthase from Chromobacterium sp. USM2. Following optimization of 3HP incorporation into the copolymer, the molar fraction of 3HP could be controlled by cultivation in medium containing different concentrations of β-alanine. Between 0 and 80 mol % 3HP could be achieved. Further supplementation with 2 mM cysteine increased the maximum 3HP molar fraction to 89%. Additionally, the effect of deletions of the phaA and phaB1 genes of the phaCAB operon on 3HP molar fraction were investigated. A phaAB1 double knockout resulted in a copolymer containing 91 mol % 3HP without the need for cysteine supplementation.

Marine macroalgae are potential renewable feedstocks for valuable biomaterials. Among them, alginate is a primary component in brown algae that can be nonenzymatically converted and enzymatically degraded by alginate lyases to 4-deoxy- l -erythro-5-hexoseulose uronic acid (DEH). Here, we constructed alginolytic enzyme complexes comprising two different alginate lyases for synergistic alginate degradation. The complexes showed good thermostability with 60% of the residual activity at high temperature (60 °C). Furthermore, they produced 0.85 and 0.18 mg/mL DEH from alginate and natural brown algae as substrates, respectively. The enzyme complex successfully decomposed brown algal biomass, resulting in a 3.15-fold improvement in DEH when compared to free enzymes. The Ralstonia eutropha strain with alginolytic enzyme complexes on the cell surface showed higher Polyhydroxybutyrate (PHB) production and produced 2.58 g/L PHB from alginate. After the use of alginate, remaining biomass such as fucoidan and laminaran can also be used in the future for high value ingredients in nutritional, medical device, skincare and dermatological products. These results demonstrate that it is possible to create more efficient strategies for producing biodegradable PHB and functional polysaccharides from brown algal substrates.

Poly(ethylene terephthalate) (PET) is a widely used plastic in bottles and fibers; its waste products pollute the environment owing to its remarkable durability. Recently, Ideonella sakaiensis 201-F6 was isolated as a unique bacterium that can degrade and assimilate PET, thus paving the way for the bioremediation and bioconversion of PET waste. We found that this strain harbors a poly(hydroxyalkanoate) (PHA) synthesis gene cluster, which is highly homologous with that of Cupriavidus necator, an efficient PHA producer. Cells grown on PET accumulated intracellular PHA at high levels. Collectively, our findings in this study demonstrate that I. sakaiensis can mediate the direct conversion of non-biodegradable PET into environment-friendly plastic, providing a new approach for PET recycling.

Solid-state fermentation (SSF) is a type of fermentation process with potential to use agro-industrial by-products as a carbon source. Nonetheless, there are few studies evaluating SSF compared to submerged fermentation (SmF) to produce polyhydroxyalkanoates (PHAs). Different methodologies are available associating the two processes. In general, the studies employ a 1st step by SSF to hydrolyze the agro-industrial by-products used as a carbon source, and a 2nd step to produce PHA that can be carried out by SmF or SSF. This paper reviewed and compared the different methodologies described in the literature to assess their potential for use in PHA production. The studies evaluated showed that highest PHA yields (86.2% and 82.3%) were achieved by associating SSF and SmF by Cupriavidus necator. Meanwhile, in methodologies using only SSF, Bacillus produced the highest yields (62% and 56.8%). Since PHA (%) does not necessarily represent a higher production by biomass, the productivity parameter was also compared between studies. We observed that the highest productivity results did not necessarily represent the highest PHA (%). C. necator presented the highest PHA yields associating SSF and SmF, however, is not the most suitable microorganism for PHA production by SSF. Concomitant use of C. necator and Bacillus is suggested for future studies in SSF. Also, it discusses the lack of studies on the association of the two fermentation methodologies, and on the scaling of SSF process for PHA production. In addition to demonstrating the need for standardization of results, for comparison between different methodologies.

A key goal of synthetic biology is to engineer organisms that can use solar energy to convert CO

Bioconversion of sustainable feedstocks to commodity chemicals is considered as an effective solution for transforming the fossil-based economy into a carbon-neutral model. Here, the CO

Consensus design (CD) is a representative sequence-based protein design method that enables the design of highly functional proteins by analyzing vast amounts of protein sequence data. This study proposes a partial consensus design (PCD) of a protein as a derivative approach of CD. The method replaces the target protein sequence with a consensus sequence in a secondary-structure-dependent manner (i.e., regionally dependent and divided into α-helix, β-sheet, and loop regions). In this study, we generated several artificial partial consensus l-threonine 3-dehydrogenases (PcTDHs) by PCD using the TDH from Cupriavidus necator (CnTDH) as a target protein. Structural and functional analysis of PcTDHs suggested that thermostability would be independently improved when consensus mutations are introduced into the loop region of TDHs. On the other hand, enzyme kinetic parameters (kcat/Km) and average productivity would be synergistically enhanced by changing the combination of the mutations-replacement of one region of CnTDH with a consensus sequence provided only negative effects, but the negative effects were nullified when the two regions were replaced simultaneously. Taken together, we propose the hypothesis that there are protein regions that encode individual protein properties, such as thermostability and activity, and that the introduction of consensus mutations into these regions could additively or synergistically modify their functions.

Polyhydroxybutyrate (PHB) is a biodegradable plastic with physical properties similar to petrochemically derived plastics. Here, Shewanella marisflavi BBL25 was engineered by inserting the pLW487 vector containing polyhydroxyalkanoates synthesis genes from Ralstonia eutropha H16. Under optimal conditions, the engineered S. marisflavi BBL25 produced 1.99 ± 0.05 g/L PHB from galactose. The strain showed high tolerance to various inhibitors and could utilize lignocellulosic biomass for PHB production. When barley straw hydrolysates were used as a carbon source, PHB production was 3.27 ± 0.19 g/L. In addition, PHB production under the microbial fuel cell system was performed to confirm electricity coproduction. The maximum electricity current output density was 1.71 mA/cm2, and dry cell weight (DCW) and PHB production were 11.4 g/L and 6.31 g/L, respectively. Our results demonstrated PHB production using various lignocellulosic biomass and the feasibility of PHB and electricity production, simultaneously, and it is the first example of PHB production in engineered Shewanella.

Purpose To synthesize and investigate polyhydroxyalkanoates (PHAs) with different monomer composition and percentages and polymer films prepared from them. Results Various PHAs: homopolymer poly-3-hydroxybutyrate P(3HB) and 2-, 3-, and 4-component copolymers comprising various combinations of 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), 4-hydroxybutyrate (4HB), and 3-hydroxyhexanoate (3HHx) monomers were synthesized under specialized conditions. Relationships were found between the monomer composition of PHAs and their molecular-weight and thermal properties and degree of crystallinity. All copolymers had decreased weight average molecular weights, Mw (to 390–600 kDa), and increased values of polydispersity (3.2–4.6) compared to the P(3HB). PHA copolymers showed different thermal behavior: an insignificant decrease in Tmelt and the presence of the second peak in the melting region and changes in parameters of crystallization and glass transition. At the same time, they retained thermostability, and the difference between Tmelt and Tdegr was at least 100–120 °C. Incorporation of 4HB, 3HV, and 3HHx monomer units into the 3-hydroxybutyrate chain caused changes in the amorphous to crystalline ratio and decreased the degree of crystallinity (Cx) to 20–40%. According to the degree to which the monomers reduced crystallinity, they were ranked as follows: 4HB – 3HHx – 3HV. A unique set of films was produced; their surface properties and physical/mechanical properties were studied as dependent on PHA composition; monomers other than 3-hydroxybutyrate were found to enhance hydrophilicity, surface development, and elasticity of polymer films. Conclusion An innovative set of PHA copolymers was synthesized and solution-cast films were prepared from them; the copolymers and films were investigated as dependent on polymer chemical composition. Results obtained in the present study contribute to the solution of a critical issue of producing degradable polymer materials.

Polyhydroxyalkanoates (PHAs) are biodegradable polymers synthesized by certain bacteria and archaea with functions comparable to conventional plastics. Previously, our research group reported a newly PHA-producing bacterial strain, Rhodococcus pyridinivorans BSRT1-1, from the soil in Thailand. However, this strain’s PHA synthase (phaCRp) gene has not yet been characterized. Thus, this study aims to synthesize PHA using a newly engineered bacterial strain, Cupriavidus necator PHB−4/pBBR_CnPro-phaCRp, which harbors the phaCRp from strain BSRT1-1, and characterize the properties of PHA for skin tissue engineering application. To the best of our knowledge, this is the first study on the characterization of the PhaC from R. pyridinivorans species. The results demonstrated that the expression of the phaCRp in C. necator PHB−4 had developed in PHA production up to 3.1 ± 0.3 g/L when using 10 g/L of crude palm kernel oil (CPKO) as a sole carbon source. Interestingly, the engineered strain produced a 3-hydroxybutyrate (3HB) with 2 mol% of 3-hydroxyhexanoate (3HHx) monomer without adding precursor substrates. In addition, the 70 L stirrer bioreactor improved P(3HB-co-2 mol% 3HHx) yield 1.4-fold over the flask scale without altering monomer composition. Furthermore, the characterization of copolymer properties showed that this copolymer is promising for skin tissue engineering applications.

A representative hydrogen-oxidizing bacterium Cupriavidus necator H16 has attracted much attention as hosts to recycle carbon dioxide (COHere, we engineer the carbon fixation metabolism to improve COThe global transcriptional regulator RegA plays an important role in the regulation of carbon fixation and shows the possibility to improve autotrophic cell growth and PHB accumulation by increasing its expression level. This work represents another step forward in better understanding and improving the lithoautotrophic PHB production by C. necator H16.

3-Hydroxypropionate (3-HP) is a versatile compound for chemical synthesis and a potential building block for biodegradable polymers. Cupriavidus necator H16, a facultative chemolithoautotroph, is an attractive production chassis and has been extensively studied as a model organism for biopolymer production. Here, we engineered C. necator H16 for 3-HP biosynthesis from its central metabolism. Wild type C. necator H16 can use 3-HP as a carbon source, a highly undesirable trait for a 3-HP production chassis. However, deletion of its three (methyl-)malonate semialdehyde dehydrogenases (mmsA1, mmsA2 and mmsA3) resulted in a strain that cannot grow on 3-HP as the sole carbon source, and this strain was selected as our production host. A stepwise approach was used to construct pathways for 3-HP production via β-alanine. Two additional gene deletion targets were identified during the pathway construction process. Deletion of the 3-hydroxypropionate dehydrogenase, encoded by hpdH, prevented the re-consumption of the 3-HP produced by our engineered strains, while deletion of gdhA1, annotated as a glutamate dehydrogenase, prevented the utilization of aspartate as a carbon source, one of the key pathway intermediates. The final strain carrying these deletions was able to produce up to 8 mM 3-HP heterotrophically. Furthermore, an engineered strain was able to produce 0.5 mM 3-HP under autotrophic conditions, using CO

Polyhydroxybutyrate (PHB) is a biodegradable plastic that can be used as an alternative to petrochemical-based plastics. PHB is produced by various microorganisms such as Ralstonia, Halomonas, and Bacillus species. However, there are very few strains that produce PHB using xylose, an abundant and inexpensive carbon source. In this study, ten xylose-utilizing PHB producers isolated from South Korean marine environments were screened and characterized. Among these isolates, Bacillus sp. SM01, a newly identified strain, produced the highest amount of PHB using xylose. Under optimal conditions, the maximum dry cell weight (DCW) was 3.41 ± 0.09 g/L, with 62% PHB content, and Bacillus sp. SM01 showed Poly (3-hydroxybutyrate-co-3-hydroxyvalerate) copolymer production with propionate; however, the growth of Bacillus sp. SM01 was greatly inhibited by the presence of glucose. Co-culturing Bacillus sp. SM01 with Cupriavidus necator NCIMB 11599 resulted in increased DCW, PHB production, and utilization of glucose and xylose, the main sugar of lignocellulosic biomass, compared with the monoculture. Our results indicated that this co-culture system can be used to increase PHB production and overcome the limitation of sugar consumption associated with Bacillus sp. SM01 and C. necator.

Terpenoids have an impressive structural diversity and provide valuable substances for a variety of industrial applications. Among terpenes, the sesquiterpenes (C15 ) are the largest subclass with bioactivities ranging from aroma to health promotion. In this article, we show a gram-scale production of the sesquiterpene α-humulene in final aqueous concentrations of 2 g L-1 with the recombinant strain Cupriavidus necator pKR-hum in a fed-batch mode on fructose as carbon source and n-dodecane as an extracting organic phase for in situ product removal. Since C. necator is capable of both heterotrophic and autotrophic growth, we additionally modeled the theoretically possible yields of a heterotrophic versus an autotrophic process on CO2 in industrially relevant quantities. We compared the cost-effectiveness of both processes based on a production of 10 t α-humulene per year, with both processes performing equally with similar costs and gains. Furthermore, the expression and activity of 3-hydroxymethylglutaryl-CoA reductase (hmgR) from Myxococcus xanthus was identified as the main limitation of our constructed C. necator pKR-hum strain. Thus, we outlined possible solutions for further improvement of our production strain, for example, the replacement of the hmgR from M. xanthus by a plant-based variant to increase α-humulene production titers in the future.

Polyhydroxyalkanoates (PHAs) are polyesters of significant interest due to their biodegradability and properties similar to petroleum-derived plastics, as well as the fact that they can be produced from renewable sources such as by-product streams. In this study, brewer’s spent grain (BSG), the main by-product of the brewing industry, was subjected to a set of physicochemical pretreatments and their effect on the release of reducing sugars (RS) was evaluated. The RS obtained were used as a substrate for further PHA production in Burkholderia cepacia, Bacillus cereus, and Cupriavidus necator in liquid cultures. Although some pretreatments proved efficient in releasing RS (acidthermal pretreatment up to 42.1 gRS L-1 and 0.77 gRS g-1 dried BSG), the generation of inhibitors in such scenarios likely affected PHA production compared with the process run without pretreatment (direct enzymatic hydrolysis of BSG). Thus, the maximum PHA accumulation from BSG hydrolysates was found in the reference case with 0.31 ± 0.02 g PHA per g cell dried weight, corresponding to 1.13 ± 0.06 g L-1 and a PHA yield of 23 ± 1 mg g-1 BSG. It was also found that C. necator presented the highest PHA accumulation of the tested strains followed closely by B. cepacia, reaching their maxima at 48 h. Although BSG has been used as a source for other bioproducts, these results show the potential of this by-product as a no-cost raw material for producing PHAs in a waste valorization and circular economy scheme.

The present study focuses on sustainable production of biodegradable polymers by Cupriavidus necator DSMZ 545 using glycerol as substrate. The batch growth and biopolymer production kinetics were established in a 7-L bioreactor, which resulted in a total biomass of 8.88 g L–1 and poly(3-hydroxybutyrate) (PHB) accumulation of 6.76 g L–1. The batch kinetic and independently acquired substrate inhibition data were then used to develop a mathematical model for PHB production process. This was eventually used to design different nutrient feeding strategies under constant feed rate, decreasing feed rate, and pseudo steady state of substrate (glycerol) to optimize the PHB production during fed-batch cultivation. Among all the fed-batch cultivation strategies, the highest PHB accumulation and productivity of 13.12 g L–1 and 0.27 g L–1 h–1, respectively, was achieved in fed-batch bioreactor cultivation where a pseudo steady state with respect to glycerol was maintained. This work is licensed under a Creative Commons Attribution 4.0 International License.

Decelerating global warming is one of the predominant challenges of our time and will require conversion of CO2 to usable products and commodity chemicals. Of particular interest is the production of fuels, because the transportation sector is a major source of CO2 emissions. Here, we review recent technological advances in metabolic engineering of the hydrogen-oxidizing bacterium Cupriavidus necator H16, a chemolithotroph that naturally consumes CO2 to generate biomass. We discuss recent successes in biofuel production using this organism, and the implementation of electrolysis/artificial photosynthesis approaches that enable growth of C. necator using renewable electricity and CO2. Last, we discuss prospects of improving the nonoptimal growth of C. necator in ambient concentrations of CO2.

LysR-type transcription regulators (LTTRs) comprise one of the largest families of transcriptional regulators in bacteria. They are typically homo-tetrameric proteins and interact with promoter DNA of ~ 50-60 bp. Earlier biochemical studies have suggested that LTTR binding to promoter DNA bends the DNA and, upon inducer binding, the bend angle of the DNA is reduced through a quaternary structure change of the tetrameric LTTR, leading to the activation of transcription. To date, crystal structures of full-length LTTRs, DNA-binding domains (DBD) with their target DNAs, and the regulatory domains with and without inducer molecules have been reported. However, these crystal structures have not provided direct evidence of the quaternary structure changes of LTTRs or of the molecular mechanism underlying these changes. Here, we report the first crystal structure of a full-length LTTR, CbnR, in complex with its promoter DNA. The crystal structure showed that, in the absence of bound inducer molecules, the four DBDs of the tetrameric CbnR interact with the promoter DNA, bending the DNA by ~ 70°. Structural comparison between the DNA-free and DNA-bound forms demonstrates that the quaternary structure change of the tetrameric CbnR required for promoter region-binding arises from relative orientation changes of the three domains in each subunit. The mechanism of the quaternary structure change caused by inducer binding is also discussed based on the present crystal structure, affinity analysis between CbnR and the promoter DNA, and earlier mutational studies on CbnR. DATABASE: Atomic coordinates and structure factors for the full-length Cupriavidus necator NH9 CbnR in complex with promoter DNA are available in the Protein Data Bank under the accession code 7D98.

Poly (3-hydroxybutyrate) (PHB) is a good alternative to petroleum-based plastics due to its biodegradable and biocompatible properties. In the present work, Cupriavidus necator ATCC 25207 was used for the first time to produce PHB using fructose, glucose, and acid or enzyme hydrolyzed molasses, a cheap carbon source. The bacterium produced highest PHB with 4.99 g/L, 3.94 g/L, and 15.28 g/L using fructose, glucose, and acid hydrolyzed molasses, respectively. Sulfuric acid and invertase treated molasses yielded 1288% and 529% more PHB than untreated molasses. In addition, acid treated molasses resulted in 151% more PHB but 34.04% less cell growth than enzyme hydrolyzed molasses. This novel finding could have applications in fermentations using molasses in growth or production media. The utilization of glucose by the bacterium was increased by 67.03% through spontaneous mutagenesis. The characterizations of the produced polymers were carried out using FTIR, NMR, XRD, DSC, TGA, and GPC. The molecular weights of PHB samples from acid hydrolyzed molasses and fructose are 3.84 $$\times $$ 105 and 1.43 $$\times $$ 106 g/mol, respectively. This study shows that C. necator ATCC 25207 has a potential to be used in PHB production using acid hydrolyzed molasses.

An astonishing variety of functions has been attributed to polyphosphate (polyP) in prokaryotes. Besides being a reservoir of phosphorus, functions in exopolysaccharide formation, motility, virulence and in surviving various forms of stresses such as exposure to heat, extreme pH, oxidative agents, high osmolarity, heavy metals and others have been ascribed to polyP. In this contribution, we will provide a historical overview on polyP, will then describe the key proteins of polyP synthesis, the polyP kinases, before we will critically assess of the underlying data on the multiple functions of polyP and provide evidence that – with the exception of a P-storage-function – most other functions of polyP are not relevant for survival of Ralstonia eutropha, a biotechnologically important beta-proteobacterial species.

Oil extracted from spent coffee grounds (SCG) [yield 16.8 % (w/w)] was discovered to be a highly suitable carbon substrate for the biosynthesis of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3 HV)] copolymers by Cupriavidus necator DSM 545 in the absence of any traditional 3 HV precursors. Cells cultivated in a 3 L bioreactor (batch) reached a total biomass concentration of 8.9 g L−1 with a P(3HB-co-3 HV) (6.8 mol% 3 HV) content of 89.6 % (w/w). In contrast, cells grown on sunflower oil reached a total biomass concentration of 9.4 gL−1 with a P(3HB-co-3 HV) (0.2 mol% 3 HV) content of 88.1 % (w/w). It is proposed that the organism could synthesize 3 HV monomers from succinyl CoA, an intermediate of the tricarboxylic acid (TCA) cycle, via the succinate-propionate metabolic pathway.

Chemolithoautotrophic bacterium Ralstonia eutropha is a versatile host for production of various useful compounds including polyhydroxyalkanoates (PHAs) under both heterotrophic and autotrophic conditions. In this bacterium, Calvin–Benson–Bassham (CBB) cycle is functional even under heterotrophic conditions on sugars and reutilizes CO2 emitted through sugar metabolisms into PHA, leading to increase in yield of the storage polyester. This study focused on isopropanol production from glucose by engineered strains of R. eutropha. The isopropanol-producing strains were constructed by introduction of codon-optimized genes of acetoacetate decarboxylase (adc) and primary-secondary alcohol dehydrogenase (adh) from clostridia into glucose-utilizing and PHA-negative (ΔphaC1) strain of R. eutropha. Several genetic modifications showed that high expression of the isopropanol synthesis genes by using a strong synthetic promoter and deletion of NAD+-dependent (S)-3-hydroxybutyryl-CoA dehydrogenase genes (paaH1 and had) in addition to NADPH-dependent acetoacetyl-CoA reductase genes (phaB1 and phaB3) were effective for improving isopropanol production with low by-production of acetone. Isopropanol titer of 4.13 g/L was achieved by two-stage cultivation of the strain IP-007/pBj5c2-adh-adc, corresponding to overall yield of 0.6 mol mol-glucose−1. The fixation of sugar-derived CO2 during isopropanol synthesis was evaluated by 13C-labelling of the isopropanol produced from [1–13C]-glucose. The 13C-abundance in isopropanol synthesized by the engineered strain was significantly increased up to 4.8%, demonstrating actual reassimilation of CO2 emitted from glucose moiety by decarboxylation and potential contribution towards increase in the carbon yield of isopropanol on glucose.

The nature of air-inactivation of the formate dehydrogenase FdsDABG from Cupriavidus necator has been investigated. It is found that superoxide, generated in the reaction of reduced enzyme with oxygen, is responsible for the loss of activity and that superoxide dismutase protects the enzyme from air-inactivation. Inhibition appears to be due to the reaction of superoxide with the catalytically essential MoS group of the enzyme's molybdenum center in such a way that generates sulfite. SYNOPSIS: Superoxide generated in the reaction of reduced formate dehydrogenase FdsDABG from Cupriavidus necator with O2 is found to be responsible for the loss of activity. Catalytic amounts of superoxide dismutase are found to protect FdsDABG just as well as more generally used stabilizing inhibitors such as nitrate.

Cupriavidus necator H16 is a gram-negative chemolithoautotrophic bacterium that has been extensively studied for biosynthesis and biodegradation of polyhydroxyalkanoate (PHA) plastics. To improve our understanding of fatty acid metabolism for PHA production, we determined the crystal structure of multi-functional enoyl-CoA hydratase from Cupriavidus necator H16 (CnFadB). The predicted model of CnFadB created by AlphaFold was used to solve the phase problem during determination of the crystal structure of the protein. The CnFadB structure consists of two distinctive domains, an N-terminal enol-CoA hydratase (ECH) domain and a C-terminal 3-hydroxyacyl-CoA dehydrogenase (HAD) domain, and the substrate- and cofactor-binding modes of these two functional domains were identified. Unlike other known FadB enzymes that exist as dimers complexed with FadA, CnFadB functions as a monomer without forming a complex with CnFadA. Small angle X-ray scattering (SAXS) measurement further proved that CnFadB exists as a monomer in solution. The non-sequential action of FadA and FadB in C. necator appears to affect β-oxidation and PHA synthesis/degradation.

Polyhydroxyalkanoates (PHAs) are natural biodegradable polyesters that are produced by numerous prokaryotic microorganisms primarily as a carbon- and energy reserve. The PhaC enzyme catalyzes the last step in the PHA biosynthesis pathway and synthesizes PHA polymers from hydroxyalkanoic acids. A type I PhaC from a PHA-producing marine bacterium Brevundimonas sp. KH11J01 (BrPhaC) was identified, produced recombinantly and characterized. Its properties were compared with its homolog from C. necator H16 (RePhaC). Unlike other PhaCs, it was found that BrPhaC is a lag-phase free enzyme organized as a trimer, even without the presence of a substrate. The enzymatic reaction is initiated instantly irrespective of temperature, in contrast to RePhaC in which the duration of the lag-phase was highly affected by temperature. At 10 °C BrPhaC was 40% active whereas RePhaC was barely active. The significance of using marine microorganisms, harboring cold-active PHA biosynthesis enzymes, for energy efficient PHA production, is also discussed briefly. The unique trimeric organization of BrPhaC challenges our understanding of the PhaC reaction mechanisms, which is mainly based on the crystal structures of the inactive forms of the enzyme.

Exploiting biological processes to recycle renewable carbon into high value platform chemicals provides a sustainable and greener alternative to current reliance on petrochemicals. In this regardCupriavidus necatorH16 represents a particularly promising microbial chassis due to its ability to grow on a wide range of low-cost feedstocks, including the waste gas carbon dioxide, whilst also naturally producing large quantities of polyhydroxybutyrate (PHB) during nutrient-limited conditions. Understanding the complex metabolic behaviour of this bacterium is a prerequisite for the design of successful engineering strategies for optimising product yields. We present a genome-scale metabolic model (GSM) ofC.necatorH16 (denotediCN1361), which is directly constructed from the BioCyc database to improve the readability and reusability of the model. After the initial automated construction, we have performed extensive curation and both theoretical and experimental validation. By carrying out a genome-wide essentiality screening using a Transposon-directed Insertion site Sequencing (TraDIS) approach, we showed that the model could predict gene knockout phenotypes with a high level of accuracy. Importantly, we indicate how experimental and computational predictions can be used to improve model structure and, thus, model accuracy as well as to evaluate potential false positives identified in the experiments. Finally, by integrating transcriptomics data withiCN1361 we create a condition-specific model, which, importantly, better reflects PHB production inC.necatorH16. Observed changes in the omics data andin-silico-estimated alterations in fluxes were then used to predict the regulatory control of key cellular processes. The results presented demonstrate thatiCN1361 is a valuable tool for unravelling the system-level metabolic behaviour ofC.necatorH16 and can provide useful insights for designing metabolic engineering strategies.

Hydrogenases are biotechnologically relevant metalloenzymes that catalyze the reversible conversion of molecular hydrogen into protons and electrons. The O2-tolerant [NiFe]-hydrogenases from Cupriavidus necator (formerly Ralstonia eutropha) are of particular interest as they maintain catalysis even in the presence of molecular oxygen. However, to meet the demands of biotechnological applications and scientific research, a heterologous production strategy is required to overcome the low production yields in their native host. We have previously used the regulatory hydrogenase (RH) from C. necator as a model for the development of such a heterologous hydrogenase production process in E. coli. Although high protein yields were obtained, the purified enzyme was inactive due to the lack of the catalytic center, which contains an inorganic nickel-iron cofactor. In the present study, we significantly improved the production process to obtain catalytically active RH. We optimized important factors such as O2 content, metal availability, production temperature and time as well as the co-expression of RH-specific maturase genes. The RH was successfully matured during aerobic cultivation of E. coli by co-production of seven hydrogenase-specific maturases and a nickel permease, which was confirmed by activity measurements and spectroscopic investigations of the purified enzyme. The improved production conditions resulted in a high yield of about 80 mg L–1 of catalytically active RH and an up to 160-fold space-time yield in E. coli compared to that in the native host C. necator [

This Doctoral Thesis has been carried out in the context of the European project "AFTERLIFE" (Advanced Filtration Technologies for the Recovery and Later conversion of relevant Fractions from wastEwater) where the development of a flexible and efficient process is proposed for the recovery and revalorization of different fractions from wastewater of agro-industrial origin. In this context, and the first chapter of this report, the bacteriumCupriavidus necatorH16 was selected for the transformation of volatile fatty acids (VFAs), derived from the anaerobic digestion (AD) of wastewater, into bioplastics from microbial origin or polyhydroxyalkanoates (PHA). Through the characterization of the raw materials and the study of the tolerance limits to the major components of the waste, the production of PHA was maximized in a bioreactor at a scale of 2 L. Applying a strategy of feeding coupled to biomass production and specific uptake rate of the carbon sources available in the wastewater, a PHA accumulation of 80 % (w/w) was achieved with respect to the biomass dry weight, as well as a 0.8 g-1L-1h-1yield.

Due to the fast increase in world population, many developing countries are facing malnutrition problems (famine, food insecurity, etc.). Particularly, the deficiency of protein sources is becoming a serious problem for both human and animals’ nutrition. Thus, the demand for protein sources has increased. In this context, Single Cell Proteins (SCP) produced by microorganisms could be exploited as an alternative and non-conventional protein source. The aim of this work was to study growth dynamics and SCP production and composition by Cupriavidus necator, under various environmental conditions stress and using different carbon (glucose, formic acid and oleic acid) and nitrogen (ammonium sulfate and urea) sources types. A mono-factorial approach under well-controlled conditions was used in order to investigate the impact of temperature, pH, carbon and nitrogen sources in bioreactor cultures. Results were compared in terms of bacterial growth, biomass composition (proteins and nucleic acids) and via the elemental biomass composition. Complementary analyses were also done using flow cytometry in order to study cell morphology, membrane permeability and presence of PHB production, a biopolymer naturally produced by C. necator. The temperature evaluation results showed that this parameter had an impact on growth and SCP production and composition. At 40°C, the growth was lower and low amounts of proteins, and nucleic acids were obtained. The same conclusion was obtained at pH5. Regarding the nitrogen source, the ammonium sulfate provided better results than urea as a nitrogen source. Added to that, the formic acid was found as a promising carbon source for protein production compared to glucose and oleic acid with a high total protein percentage of 90%DW (obtained with the Dumas’s method).; En raison de l'augmentation rapide de la population mondiale, de nombreux pays en cours de développement sont concernés par des problèmes de malnutrition (famine, insécurité alimentaire, etc.). En particulier, l’insuffisance en sources de protéines devient un problème majeur pour la nutrition humaine et animale et leur demande augmente de plus en plus. Dans ce contexte, les Protéines d’Organismes Unicellulaires (POU) produites par des micro-organismes peuvent exploitées comme une source de protéines alternative et non conventionnelle. L'objectif de ces travaux était d'étudier les dynamiques de croissance et de production de POU ainsi que leur composition par Cupriavidus necator, en réponse à des conditions environnementales différentes et en utilisant différents types de sources de carbone (glucose, acide formique et acide oléique) et d'azote (sulfate d’ammonium et urée). Une approche mono-factorielle en condition d’environnement contrôlé a été utilisée afin d'étudier l'impact de la température, du pH, des sources de carbone et d'azote dans des cultures en bioréacteurs. Les résultats ont été comparés en termes de croissance bactérienne, de composition de la biomasse (en protéines et en acides nucléiques) et via la composition élémentaire de la biomasse. Des analyses complémentaires ont également été effectuées par cytomètrie en flux afin de suivre la morphologie cellulaire, la perméabilité membranaire, et la présence potentielle de PHB, bio polymère naturellement produit par C. necator. Les résultats concernant la température ont montré que ce paramètre avait un impact sur la croissance ainsi que sur la production et la composition des POU. A 40°C, la croissance était plus faible et de faibles quantités de protéines et d'acides nucléiques ont été obtenues. La même conclusion a été obtenue à pH5. Concernant la nature de la source d’azote, le sulfate d'ammonium a donné les meilleurs résultats, comparé à l'urée, comme source d'azote. De plus, l'acide formique s'est avéré être une source de carbone prometteuse pour la production de protéines comparé au glucose et à l'acide oléique avec un pourcentage en protéines totales élevé autour de 90%DW (mesuré par la méthode de Dumas).

To increase the availability and expand the raw material base, the production of polyhydroxyalkanoates (PHA) by the wild strain Cupriavidus necator B-10646 on hydrolysates of sugar beet molasses was studied. The hydrolysis of molasses was carried out using β-fructofuranosidase, which provides a high conversion of sucrose (88.9%) to hexoses. We showed the necessity to adjust the chemical composition of molasses hydrolysate to balance with the physiological needs of C. necator B-10646 and reduce excess sugars and nitrogen and eliminate phosphorus deficiency. The modes of cultivation of bacteria on diluted hydrolyzed molasses with the controlled feeding of phosphorus and glucose were implemented. Depending on the ratio of sugars introduced into the bacterial culture due to the molasses hydrolysate and glucose additions, the bacterial biomass concentration was obtained from 20–25 to 80–85 g/L with a polymer content up to 80%. The hydrolysates of molasses containing trace amounts of propionate and valerate were used to synthesize a P(3HB-co-3HV) copolymer with minor inclusions of 3-hydroxyvlaerate monomers. The introduction of precursors into the medium ensured the synthesis of copolymers with reduced values of the degree of crystallinity, containing, in addition to 3HB, monomers 3HB, 4HB, or 3HHx in an amount of 12–16 mol.%.

The study addresses the growth of the wild-type strain Cupriavidus necator B-10646 and synthesis of polyhydroxyalkanoates by this strain on media containing plant oils with different compositions of fatty acids: palm, Siberian oilseed, and refined and unrefined sunflower seed oils. The study showed that the best carbon substrate was palm oil. Comparison of fatty acid compositions of the starting oils and unutilized residual substrates showed that C. necator B-10646 cells consumed the fatty acids from palm oil evenly while in experiments with other oils, they utilized polyenoic fatty acids first. Higher production parameters of the culture were obtained by preparation of emulsified oil medium using Tween 80 and sodium cocoyl glutamate as emulsifiers. All polyhydroxyalkanoate specimens were terpolymers that contained 3-hydroxybutyrate as the major component and minor amounts of 3-hydroxyvalerate (0.9–1.9 mol%) and 3-hydroxyhexanoate (0.5–1.1 mol%). Molecular weight of polyhydroxyalkanoate specimens depended on the type of plant oil and emulsifier.

The acyl-CoA dehydrogenase (FadE) and (R)-specific enoyl-CoA hydratase (PhaJ) are functionally related to the degradation of fatty acids and the synthesis of polyhydroxyalkanoates (PHAs). To verify this, a recombinant Cupriavidus necator H16 harboring the plasmid -pMPJAS03- with fadE from Escherichia coli strain K12 and phaJ1 from Pseudomonas putida strain KT2440 under the arabinose promoter (araC-PBAD) was constructed. The impact of co-expressing fadE and phaJ genes on C. necator H16/pMPJAS03 maintaining the wild-type synthase on short-chain-length/medium-chain-length PHA formation from canola or avocado oil at different arabinose concentrations was investigated. The functional activity of fadEE.c led to obtaining higher biomass and PHA concentrations compared to the cultures without expressing the gene. While high transcriptional levels of phaJ1P.p, at 0.1% of arabinose, aid the wild-type synthase to polymerize larger-side chain monomers, such as 3-Hydroxyoctanoate (3HO) and 3-Hydroxydecanoate (3HD). The presence of even small amounts of 3HO and 3HD in the co-polymers significantly depresses the melting temperature of the polymers, compared to those composed of pure 3-hydroxybutyrate (3HB). Our data presents supporting evidence that the synthesis of larger-side chain monomers by the recombinant strain relies not only upon the affinity of the wild-type synthase but also on the functionality of the intermediate supplying enzymes.

Objective The rapid accumulation of crude-oil based plastics in the environment is posing a fundamental threat to the future of mankind. The biodegradable and bio-based polyhydroxyalkanoates (PHAs) can replace conventional plastics, however, their current production costs are not competitive and therefore prohibiting PHAs from fulfilling their potential. Results Different low-quality animal by-products, which were separated by thermal hydrolysis into a fat-, fat/protein-emulsion- and mineral-fat-mixture- (material with high ash content) phase, were successfully screened as carbon sources for the production of PHA. Thereby, Ralstonia eutropha Re2058/pCB113 accumulated the short- and medium-chain-length copolymer poly(hydroxybutyrate-co-hydroxyhexanoate) [P(HB-co-HHx)]. Up to 90 wt% PHA per cell dry weight with HHx-contents of 12–26 mol% were produced in shake flask cultivations. Conclusion In future, the PHA production cost could be lowered by using the described animal by-product streams as feedstock. Graphical abstract

Coupling recent advancements in genetic engineering of diverse microbes and gas-driven fermentation provides a path towards sustainable commodity chemical production. Cupriavidus necator H16 is a suitable species for this task because it effectively utilizes H2 and CO2 and is genetically tractable. Here, we demonstrate the versatility of C. necator for chemical production by engineering it to produce three products from CO2 under lithotrophic conditions: sucrose, polyhydroxyalkanoates (PHAs), and lipochitooligosaccharides (LCOs). We engineered sucrose production in a co-culture system with heterotrophic growth 30 times that of WT C. necator. We engineered PHA production (20-60% DCW) and selectively altered product composition by combining different thioesterases and phaCs to produce copolymers directly from CO2. And, we engineered C. necator to convert CO2 into the LCO, a plant growth enhancer, with titers of ~1.4 mg/L-equivalent to yields in its native source, Bradyrhizobium. We applied the LCOs to germinating seeds as well as corn plants and observed increases in a variety of growth parameters. Taken together, these results expand our understanding of how a gas-utilizing bacteria can promote sustainable production.

The valorization of agricultural waste is a sustainable way of how to utilize renewable resources wisely. Grape pomace is a by-product of the manufacturing of the must. The potential of Cupriavidus necator, Halomonas halophila and Halomonas organivorans to produce poly(3-hydroxybutyrate) (PHB) by using oil and fermentable sugars derived from grape pomace has been studied. C. necator proved to be the best producer of PHB when utilizing grape pomace extract as a carbon source. After 29.5 h of fermentation of C. necator in 2-L bioreactor, PHB titers reached 8.3 g l−1 and 63 % PHB content in bacteria cell dry mass. The average molecular weight and the polydispersity of accumulated polymer was 512.2 kDa and 1.2, respectively. In addition to fermentable sugars, this work indicates that oil, pigments, phenolics, lignin and cellulose can be isolated from seeds and the rest of the grape pomace to support the cascading utilization of agricultural waste and natural valuable resources recovery.

Films were prepared from 2% solutions of biodegradable poly-3-hydroxybutyrate [P(3HB)] and investigated. The polymer was synthesized by the Cupriavidus necator B-10646 bacterium cultivated using various carbon sources (glucose and glycerol of different degrees of purity, containing 0.3 to 17.93% impurities). Glycerol as the substrate influenced molecular-weight properties and crystallinity of the polymer without affecting its temperature characteristics. The P(3HB) specimens synthesized from glycerol had reduced Mw (300–400 kDa) and degree of crystallinity (50–55%) compared to the specimens synthesized from glucose (860 kDa and 76%, respectively). The low-crystallinity P(3HB) specimens, regardless of the degree of purity of glycerol, produced a beneficial effect on the properties of polymer films, which had a better developed folded surface and increased hydrophilicity. The values of the highest roughness (Ra) of the films synthesized from glycerol were 1.8 to 4.0 times lower and the water angles 1.4–1.6 times smaller compared to the films synthesized from glucose (71.75 nm and 87.4°, respectively). Those films performed better as cell scaffolds: the number of viable NIH fibroblasts was 1.7–1.9 times higher than on polystyrene (control) or films of P(3HB) synthesized from glucose.

Waste paper as a resource for polyhydroxyalkanoate (PHA) production through anaerobic digestion is a low-cost strategy to produce bioplastic. In this study, volatile fatty acids (VFAs) produced from waste paper, one of the significant constituents of municipal solid waste, was utilized as a feedstock for polyhydroxyalkanoate (PHA) production. PHA production from synthetic VFAs by Cupriavidus necator was initially optimized under different VFAs concentrations, VFAs ratios, and nitrogen sources. VFAs concentration of 10 g/L, 5:1:4 ratio of acetic, propionic, and butyric acids (HAc:HPr:HBu) and NaNO3 as nitrogen source were considered the optimum conditions with 56.98% PHA and 0.31 g/g yield. Anaerobic digestion of shredded office paper (OP/S) produced the maximum VFAs (521.50 mg/L) after 15 days of incubation and were utilized for PHA synthesis. Almost 2.24-fold increase in the yield of PHA was achieved with limited nutrient medium compared to nutrient contained medium with a PHA content of 53.50 and 23.88%, respectively. PHA production using anaerobic effluent of waste paper is a promising approach where a series of pretreatment processes, the expensive enzymatic hydrolysis, and detoxification were no longer required, suggesting an environmentally friendly way of biopolymer production.