Necator H16 Research Articles

Metabolic engineering of Cupriavidus necator H16 for heterotrophic and autotrophic production of 3-hydroxypropionic acid

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 CO2 as sole carbon source. These results form the basis for establishing C. necator H16 as an efficient platform for the production of 3-HP and 3-HP-containing polymers.

Engineering a Rhodopsin-Based Photo-Electrosynthetic System in Bacteria for CO2 Fixation.

A key goal of synthetic biology is to engineer organisms that can use solar energy to convert CO2 to biomass, chemicals, and fuels. We engineered a light-dependent electron transfer chain by integrating rhodopsin and an electron donor to form a closed redox loop, which drives rhodopsin-dependent CO2 fixation. A light-driven proton pump comprising Gloeobacter rhodopsin (GR) and its cofactor retinal have been assembled in Ralstonia eutropha (Cupriavidus necator) H16. In the presence of light, this strain fixed inorganic carbon (or bicarbonate) leading to 20% growth enhancement, when formate was used as an electron donor. We found that an electrode from a solar panel can replace organic compounds to serve as the electron donor, mediated by the electron shuttle molecule riboflavin. In this new autotrophic and photo-electrosynthetic system, GR is augmented by an external photocell for reductive CO2 fixation. We demonstrated that this hybrid photo-electrosynthetic pathway can drive the engineered R. eutropha strain to grow using CO2 as the sole carbon source. In this system, a bioreactor with only two inputs, light and CO2, enables the R. eutropha strain to perform a rhodopsin-dependent autotrophic growth. Light energy alone, supplied by a solar panel, can drive the conversion of CO2 into biomass with a maximum electron transfer efficiency of 20%.

Crystal structure of multi-functional enzyme FadB from Cupriavidus necator: Non-formation of FadAB complex

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.

Thermodynamic limitations of PHB production from formate and fructose in Cupriavidus necator

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.

Microbial conversion of syngas to single cell protein: The role of carbon monoxide

Syngas has been widely utilized as substrate in microbial processes to produce various high-value products. Nevertheless, its applicability for single cell protein (SCP) production by hydrogen-oxidizing bacteria (HOB) has never been explored. Especially, the role of carbon monoxide in SCP synthesis is unknown. Thus, this study first investigated the effect of different CO and H2 ratios in syngas on Cupriavidus necator H16 growth and SCP production. The growth of C. necator H16 was significantly restrained with the increase of CO content, and it almost ceased once the CO:H2 ratios were above 1. In addition, the growth rate of C. necator H16 increased with the increase of shaking frequency and inoculum volume. Furthermore, larger gas–liquid interfacial areas and gas input amount resulted in a higher growth rate and OD value. The raw protein contents were around 50–60% regardless of CO concentration, and the amino acid profiles showed no apparent differences. The results showed that although the presence of CO led to the reduction of the growth rate of C. necator H16, it had a limited effect on the SCP quality. H2 and CO2 in syngas were the primary substrates for SCP production, while CO served more as a toxic inhibitor. The successful demonstration of SCP synthesis from syngas may provide a superior route for the valorization of waste biomass by turning it into food or feed.

Bioconversion Process of Polyethylene from Waste Tetra Pak® Packaging to Polyhydroxyalkanoates

Presented herein are the results of a novel recycling method for waste Tetra Pak® packaging materials. The polyethylene (PE-T) component of this packaging material, obtained via a separation process using a “solvents method”, was used as a carbon source for the biosynthesis of polyhydroxyalkanoates (PHAs) by the bacterial strain Cupriavidus necator H16. Bacteria were grown for 48–72 h, at 30 °C, in TSB (nitrogen-rich) or BSM (nitrogen-limited) media supplemented with PE-T. Growth was monitored by viable counting. It was demonstrated that C. necator utilised PE-T in both growth media, but was only able to accumulate 40% w/w PHA in TSB supplemented with PE-T. Only 1.5% w/w PHA was accumulated in the TSB control, and no PHA was detected in the BSM control. Extracted biopolymers were characterised by nuclear magnetic resonance (NMR), Fourier-transform infrared (FTIR) spectroscopy, electrospray tandem mass spectrometry (ESI-MS/MS), gel permeation chromatography (GPC), and accelerator mass spectrometry (AMS). The characterisation of PHA by ESI-MS/MS revealed that PHA produced by C. necator in TSB supplemented with PE-T contained 3-hydroxybutyrate, 3-hydroxyvalerate, and 3-hydroxyhexanoate co-monomeric units. AMS analysis also confirmed the presence of 96.73% modern carbon and 3.27% old carbon in PHA derived from Tetra Pak®. Thus, this study demonstrates the feasibility of our proposed recycling method for waste Tetra Pak® packaging materials, alongside its potential for producing value-added PHA, and the ability of 14C analysis in validating this bioconversion process.

Lab-Scale Cultivation of Cupriavidus necator on Explosive Gas Mixtures: Carbon Dioxide Fixation into Polyhydroxybutyrate.

Aerobic, hydrogen oxidizing bacteria are capable of efficient, non-phototrophic CO2 assimilation, using H2 as a reducing agent. The presence of explosive gas mixtures requires strict safety measures for bioreactor and process design. Here, we report a simplified, reproducible, and safe cultivation method to produce Cupriavidus necator H16 on a gram scale. Conditions for long-term strain maintenance and mineral media composition were optimized. Cultivations on the gaseous substrates H2, O2, and CO2 were accomplished in an explosion-proof bioreactor situated in a strong, grounded fume hood. Cells grew under O2 control and H2 and CO2 excess. The starting gas mixture was H2:CO2:O2 in a ratio of 85:10:2 (partial pressure of O2 0.02 atm). Dissolved oxygen was measured online and was kept below 1.6 mg/L by a stepwise increase of the O2 supply. Use of gas compositions within the explosion limits of oxyhydrogen facilitated production of 13.1 ± 0.4 g/L total biomass (gram cell dry mass) with a content of 79 ± 2% poly-(R)-3-hydroxybutyrate in a simple cultivation set-up with dissolved oxygen as the single controlled parameter. Approximately 98% of the obtained PHB was formed from CO2.

A unique class I polyhydroxyalkanoate synthase (PhaC) from Brevundimonas sp. KH11J01 exists as a functional trimer: A comparative study with PhaC from Cupriavidus necator H16

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.

Impact of various β-ketothiolase genes on PHBHHx production in Cupriavidus necator H16 derivatives.

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 36.2mol% with overexpression of (R)-specifc enoyl-CoA hydratase (PhaJ) and PHA synthase. Furthermore, we demonstrated high-density production (196g/L) of PHBHHx with high 3HHx (32.5mol%) 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 32.5mol% 3HHx was produced in high density by jar fermenter.

The reliance of glycerol utilization by Cupriavidus necator on CO2 fixation and improved glycerol catabolism

While crude glycerol is a cheap carbon source for industrial-scale cultivation of microorganisms, its application relies on fast growth and conversion. The biopolymer producing Cupriavidus necator H16 (synonym: Ralstonia eutropha H16) grows poorly on glycerol. The heterologous expression of glycerol facilitator glpF, glycerol kinase glpK, and glycerol dehydrogenase glpD from E. coli accelerated the growth considerably. The naturally occurring glycerol utilization is inhibited by low glycerol kinase activity. A limited heterotrophic growth promotes the dependency on autotrophic growth by carbon dioxide (CO2) fixation and refixation. As mixotrophic growth occurs in the wildtype due to low consumption rates of glycerol, CO2 fixation by the Calvin-Benson-Bassham (CBB) cycle is essential. The deletion of both cbbX copies encoding putative RuBisCO-activases (AAA + ATPase) resulted in a sharp slowdown of growth and glycerol consumption. Activase activity is necessary for functioning carboxylation by RuBisCO. Each of the two copies compensates for the loss of the other, as suggested by observed expression levels. The strong tendency towards autotrophy supports previous investigations of glycerol growth and emphasizes the versatility of the metabolism of C. necator H16. Mixotrophy with glycerol-utilization and CO2 fixation with a high dependence on the CBB is automatically occurring unless transportation and degradation of glycerol are optimized. Parallel engineering of CO2 fixation and glycerol degradation is suggested towards application for value-added production from crude glycerol. KEY POINTS: • Growth on glycerol is highly dependent on efficient carbon fixation via CBB cycle. • CbbX is essential for the efficiency of RuBisCO in C. necator H16. • Expression of glycerol degradation pathway enzymes accelerates glycerol utilization.

High amounts of medium-chain-length polyhydroxyalkanoates subunits can be accumulated in recombinant Cupriavidus necator with wild-type synthase

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.

Establishing Mixotrophic Growth of Cupriavidus necator H16 on CO2 and Volatile Fatty Acids

The facultative chemolithoautotroph Cupriavidus necator H16 is able to grow aerobically either with organic substrates or H2 and CO2 s and it can accumulate large amounts of (up to 90%) poly (3-hydroxybutyrate), a polyhydroxyalkanoate (PHA) biopolymer. The ability of this organism to co-utilize volatile fatty acids (VFAs) and CO2 as sources of carbon under mixotrophic growth conditions was investigated and PHA production was monitored. PHA accumulation was assessed under aerobic conditions, with either individual VFAs or in mixtures, under three different conditions—with CO2 as additional carbon source, without CO2 and with CO2 and H2 as additional sources of carbon and energy. VFAs utilisation rates were slower in the presence of CO2. PHA production was significantly higher when cultures were grown mixotrophically and with H2 as an additional energy source compared to heterotrophic or mixotrophic growth conditions, without H2. Furthermore, a two-step VFA feeding regime was found to be the most effective method for PHA accumulation. It was used for PHA production mixotrophically using CO2, H2 and VFA mixture derived from an anaerobic digestor (AD). The data obtained demonstrated that process parameters need to be carefully monitored to avoid VFA toxicity and low product accumulation.

Biosensor-informed engineering of Cupriavidus necator H16 for autotrophic D-mannitol production

Cupriavidus necator H16 is one of the most researched carbon dioxide (CO2)-fixing bacteria. It can store carbon in form of the polymer polyhydroxybutyrate and generate energy by aerobic hydrogen oxidation under lithoautotrophic conditions, making C. necator an ideal chassis for the biological production of value-added compounds from waste gases. Despite its immense potential, however, the experimental evidence of C. necator utilisation for autotrophic biosynthesis of chemicals is limited. Here, we genetically engineered C. necator for the high-level de novo biosynthesis of the industrially relevant sugar alcohol mannitol directly from Calvin-Benson-Bassham (CBB) cycle intermediates. To identify optimal mannitol production conditions in C. necator, a mannitol-responsive biosensor was applied for screening of mono- and bifunctional mannitol 1-phosphate dehydrogenases (MtlDs) and mannitol 1-phosphate phosphatases (M1Ps). We found that MtlD/M1P from brown alga Ectocarpus siliculosus performed overall the best under heterotrophic growth conditions and was selected to be chromosomally integrated. Consequently, autotrophic fermentation of recombinant C. necator yielded up to 3.9 g/L mannitol, representing a substantial improvement over mannitol biosynthesis using recombinant cyanobacteria. Importantly, we demonstrate that at the onset of stationary growth phase nearly 100% of carbon can be directed from the CBB cycle into mannitol through the glyceraldehyde 3-phosphate and fructose 6-phosphate intermediates. This study highlights for the first time the potential of C. necator to generate sugar alcohols from CO2 utilising precursors derived from the CBB cycle.

Identification and characterization of L- and D-lactate-inducible systems from Escherichia coli MG1655, Cupriavidus necator H16 and Pseudomonas species

Lactic acid is an important platform chemical used for the production of various compounds including polylactic acid (PLA). Optically pure L- and D-lactic acids are required to obtain high quality PLA. To advance the development and selection of microbial strains for improved production of lactic acid enantiomers, a high-throughput screening, dynamic pathway control, or real-time monitoring are often applied. Inducible gene expression systems and their application in the genetically encoded biosensors contribute to the development of these techniques and are important devices for the advancement of lactic acid biotechnology. Here, we identify and characterize eleven lactate-inducible systems from Escherichia coli, Cupriavidus necator, and Pseudomonas spp. The specificity and dynamics of these systems in response to L- and D-lactate, or structurally similar compounds are investigated. We demonstrate that the inducible systems EcLldR/PlldP and CnGntR/PH16_RS19190 respond only to the L-lactate, exhibiting approximately 19- and 24-fold induction, respectively. Despite neither of the examined bacteria possess the D-lactate-specific inducible system, the PaPdhR/PlldP and PfPdhR/PlldP are induced approximately 37- and 366-fold, respectively, by D-lactate and can be used for developing biosensor with improved specificity. The findings of this study provide an insight into understanding of L- and D-lactate-inducible systems that can be employed as sensing and tuneable devices in synthetic biology.

Heterologous phasin expression in Rhodopseudomonas palustris CGA009 for bioplastic production from lignocellulosic biomass

Rhodopseudomonas palustris CGA009 is a metabolically robust microbe that can utilize lignin breakdown products to produce polyhydroxyalkanoates (PHAs), biopolymers with the potential to replace conventional plastics. Our recent efforts suggest PHA granule formation is a limiting factor for maximum production of the bioplastic poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) by R. palustris. The Phap1 phasin (phaP1) from the PHB-producing model bacterium Cupriavidus necator H16 was expressed in R. palustris with the aim of overproducing PHBV from the lignin breakdown product p-coumarate by fostering smaller and more abundant granules. Expression of phaP1 yielded PHBV production from R. palustris aerobically (0.7 g/L), which does not occur in the wild-type strain, and led to a significantly higher PHBV titer than wild-type anaerobic production (0.41 g/L). The 3HV fractions were also significantly increased under both anaerobic and aerobic conditions, which boosts thermomechanical properties and potential for application. Thus, heterologous phasin expression in R. palustris provides flexibility for industrial processing and could foster compositional changes in copolymers with better thermomechanical properties compared to PHB alone.

The Overexpression of Phasin and Regulator Genes Promoting the Synthesis of Polyhydroxybutyrate in Cupriavidus necator H16 under Nonstress Conditions.

Cupriavidus necator H16 is an ideal strain for polyhydroxybutyrate (PHB) production from CO2. Low-oxygen stress can induce PHB synthesis in C. necator H16 while reducing bacterial growth under chemoautotrophic culture. The optimum growth and PHB synthesis of C. necator H16 cannot be achieved simultaneously, which restricts PHB production. The present study was initiated to address the issue through comparative transcriptome and gene function analysis. First, the comparative transcriptome of C. necator H16 chemoautotrophically cultured under low-oxygen stress and nonstress conditions was studied. Three types of genes were discovered to have differential levels of transcription: those involving PHB enzymatic synthesis, PHB granulation, and regulators. Under low-oxygen stress conditions, acetoacetyl-coenzyme A (CoA) reductase gene phaB2, PHB synthase gene phaC2, phasins genes phaP1 and phaP2, and regulator genes uspA and rpoN were upregulated 3.0-, 2.5-, 1.8-, 2.7-, 3.5-, and 1.6-fold, respectively. Second, the functions of upregulated genes and their applications in PHB synthesis were further studied. It was found that the overexpression of phaP1, phaP2, uspA, and rpoN can induce PHB synthesis under nonstress conditions, while phaB2 and phaC2 have no significant effect. Under the optimum conditions, the PHB percentage content in C. necator H16 was increased by 37.2%, 28.4%, 15.8%, and 41.0%, respectively, with overexpression of phaP1, phaP2, uspA, and rpoN, and the corresponding PHB production increased by 49.8%, 42.9%, 47.0%, and 77.5%, respectively, under nonstress chemoautotrophic conditions. Similar promotion by phaP1, phaP2, uspA, and rpoN was observed in heterotrophically cultured C. necator H16. The PHB percentage content and PHB production were increased by 54.4% and 103.1%, respectively, with the overexpression of rpoN under nonstress heterotrophic conditions. IMPORTANCE Microbial fixation of CO2 is an effective way to reduce greenhouse gases. Some microbes, such as C. necator H16, usually accumulate PHB when they grow under stress. Low-oxygen stress can induce PHB synthesis when C. necator H16 is autotrophically cultured with CO2, H2, and O2, while under stress, growth is restricted, and total PHB yield is reduced. Achieving the optimal bacterial growth and PHB synthesis at the same time is an ideal condition for transforming CO2 into PHB by C. necator H16. The present study was initiated to clarify the molecular basis of low-oxygen stress promoting PHB accumulation and to realize the optimal PHB production by C. necator H16. Genes upregulated under nonstress conditions were identified through comparative transcriptome analysis and overexpression of phasin, and regulator genes were demonstrated to promote PHB synthesis in C. necator H16.

Insights into the Degradation of Medium-Chain-Length Dicarboxylic Acids in Cupriavidus necator H16 Reveal β-Oxidation Differences between Dicarboxylic Acids and Fatty Acids.

Many homologous genes encoding β-oxidation enzymes have been found in the genome of Cupriavidus necator H16 (synonym Ralstonia eutropha H16). By proteome analysis, the degradation of adipic acid was investigated and showed differences from the degradation of hexanoic acid. During β-oxidation of adipic acid, activation with coenzyme A (CoA) is catalyzed by the two-subunit acyl-CoA ligase encoded by B0198 and B0199. The operon is completed by B0200 encoding a thiolase catalyzing the cleavage of acetyl-CoA at the end of the β-oxidation cycle. C. necator ΔB0198-B0200 strain showed improved growth on adipic acid. Potential substitutes are B1239 for B0198-B0199 and A0170 as well as A1445 for B0200. A deletion mutant without all three thiolases showed diminished growth. The deletion of detected acyl-CoA dehydrogenase encoded by B2555 has an altered phenotype grown with sebacic acid but not adipic acid. With hexanoic acid, acyl-CoA dehydrogenase encoded by B0087 was detected on two-dimensional (2D) gels. Both enzymes are active with adipoyl-CoA and hexanoyl-CoA as substrates, but specific activity indicates a higher activity of B2555 with adipoyl-CoA. 2D gels, growth experiments, and enzyme assays suggest the specific expression of B2555 for the degradation of dicarboxylic acids. In C. necator H16, the degradation of carboxylic acids potentially changes with an increasing chain length. Two operons involved in growth with long-chain fatty acids seem to be replaced during growth on medium-chain carboxylic acids. Only two deletion mutants showed diminished growth. Replacement of deleted genes with one of the numerous homologous is likely. IMPORTANCE The biotechnologically interesting bacterium Cupriavidus necator H16 has been thoroughly investigated. Fifteen years ago, it was sequenced entirely and annotated (A. Pohlmann, W. F. Fricke, F. Reinecke, B. Kusian, et al., Nat Biotechnol 24:1257-1262, 2006, https://doi.org/10.1038/nbt1244). Nevertheless, the degradation of monocarboxylic fatty acids and dicarboxylic acids has not been elucidated completely. C. necator is used to produce value-added products from affordable substrates. One of our investigations' primary targets is the biotechnological production of organic acids with different and specific chain lengths. The versatile metabolism of carboxylic acids recommends C. necator H16 as a candidate for producing value-added organic products. Therefore, the metabolism of these compounds is of interest, and, for different applications in industry, understanding such central metabolic pathways is crucial.

The pMTL70000 modular, plasmid vector series for strain engineering in Cupriavidus necator H16

Cupriavidus necator H16 can convert CO2 into industrial chemicals and fuels. To facilitate its engineering, we designed, built and tested the pMTL70000 modular plasmids comprising standardised Cupriavidus and E. coli replicons, selectable markers and application specific modules. Plasmids were characterised in terms of transmissibility, stability, copy number and compatibility.

PCAT vectors overcome inefficient electroporation of Cupriavidus necator H16

Cupriavidus necator H16 is a chemolithoautotroph with a range of industrial biotechnological applications. Advanced metabolic engineering in the bacterium, however, is impeded by low transformation efficiency, making it difficult to introduce and screen new genetic functions rapidly. This study systematically characterized the broad host range plasmids pBHR1, pBBR1MCS-2 and pKT230 used frequently for C. necator engineering. Kanamycin resistance cassette (KanR) and a truncated sequence of the replication origin (Rep) are contributing factors to C. necator low electroporation transformation efficiency. Consequently, a series of modular minimal plasmids, named pCAT, were constructed. pCAT vectors transform C. necator H16 with a > 3000-fold higher efficiency (up to 107 CFU/μg DNA) compared to control plasmids. Further, pCAT vectors are highly stable, expressing reporter proteins over several days of serial cultivation in the absence of selection pressure. Finally, they can be assembled rapidly from PCR or synthesized DNA fragments, and restriction-ligation reactions can be efficiently electroporated directly into C. necator, circumventing the requirement to use Escherichia coli for plasmid maintenance or propagation. This study demonstrates that an understanding of the behaviour of the constituent parts of plasmids in a host is key to efficient propagation of genetic information, while offering new methods for engineering a bacterium with desirable industrial biotechnological features.

Genetic incorporation of oil-utilizing ability in Cupriavidus malaysiensis USMAA2-4 for sustainable polyhydroxyalkanoates production from palm olein and 1-pentanol

The sustainability in polyhydroxyalkanoates (PHA) production is drawing increasing attention as the effort to increase the economic feasibility for commercialization pursues. Oleic acid is widely preferred by bacteria but its employment for PHA production makes sustainability rather dubious. This study showed promising poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] content of 68 wt % by lipase genes-harbouring Cupriavidus malaysiensis USMAA2-4 transformant from palm olein and 1-pentanol. High oleic acid content and low oil saturation caused palm olein to outperform crude palm oil, crude palm kernel oil and soybean oil due to its preference for oleic acid shown by previous screening. The transformant showed 8-fold and 40-fold higher lipase activity compared to C. necator H16 and its wild-type respectively. The transformant was unaffected by Co2+ but the growth of C. necator H16 was inversely proportional to Co2+ concentration and the employment of 1-pentanol also ceased its growth and PHA accumulation. Although the inhibitory effect of Fe2+, Cu2+ and Zn2+ at high molarity on LipA decreased PHA content of C. malaysiensis USMAA2-4 transformant by 23–24 wt %, the lipase activity was restorable with high molarity of Ca2+, thus resulted in higher PHA content. The transformant enabled the employment of low-cost 1-pentanol as the precursor for cost-effective PHA production and its preference for palm olein contributed to higher sustainability.