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Abstract Background Poly(4-hydroxybutyrate) [poly(4HB)] is a strong thermoplastic biomaterial with remarkable mechanical properties, biocompatibility and biodegradability. However, it is generally synthesized when 4-hydroxybutyrate (4HB) structurally related substrates such as γ-butyrolactone, 4-hydroxybutyrate or 1,4-butanediol (1,4-BD) are provided as precursor which are much more expensive than glucose. At present, high production cost is a big obstacle for large scale production of poly(4HB). Results Recombinant Escherichia coli strain was constructed to achieve hyperproduction of poly(4-hydroxybutyrate) [poly(4HB)] using glucose as a sole carbon source. An engineering pathway was established in E. coli containing genes encoding succinate degradation of Clostridium kluyveri and PHB synthase of Ralstonia eutropha. Native succinate semialdehyde dehydrogenase genes sad and gabD in E. coli were both inactivated to enhance the carbon flux to poly(4HB) biosynthesis. Four PHA binding proteins (PhaP or phasins) including PhaP1, PhaP2, PhaP3 and PhaP4 from R. eutropha were heterologously expressed in the recombinant E. coli, respectively, leading to different levels of improvement in poly(4HB) production. Among them PhaP1 exhibited the highest capability for enhanced polymer synthesis. The recombinant E. coli produced 5.5 g L-1 cell dry weight containing 35.4% poly(4HB) using glucose as a sole carbon source in a 48 h shake flask growth. In a 6-L fermentor study, 11.5 g L-1 cell dry weight containing 68.2% poly(4HB) was obtained after 52 h of cultivation. This was the highest poly(4HB) yield using glucose as a sole carbon source reported so far. Poly(4HB) was structurally confirmed by gas chromatographic (GC) as well as 1H and 13C NMR studies. Conclusions Significant level of poly(4HB) biosynthesis from glucose can be achieved in sad and gabD genes deficient strain of E. coli JM109 harboring an engineering pathway encoding succinate degradation genes and PHB synthase gene, together with expression of four PHA binding proteins PhaP or phasins, respectively. Over 68% poly(4HB) was produced in a fed-batch fermentation process, demonstrating the feasibility for enhanced poly(4HB) production using the recombinant strain for future cost effective commercial development.

PHA, a family of natural biopolymers aiming to replace non-degradable plastics for short-term usages, has been developed to include various structures such as short-chain-length (scl) and medium-chain-length (mcl) monomers as well as their copolymers. However, PHA market has been grown slowly since 1980s due to limited variety with good mechanical properties and the high production cost. Here, we review most updated strategies or approaches including metabolic engineering, synthetic biology and morphology engineering on expanding PHA diversity, reducing production cost and enhancing PHA production. The extremophilic Halomonas spp. are taken as examples to show the feasibility and challenges to develop next generation industrial biotechnology (NGIB) for producing PHA more competitively. • Engineering biosynthesis pathways and new PHA synthases for PHA diversity. • The uses of low-cost substrates and contamination resistant hosts for a low-cost production process. • Engineering cell morphology and growth behavior for enhanced PHA synthesis. • The development of next generation industrial biotechnology (NGIB) for a more competitive PHA production. [ABSTRACT FROM AUTHOR]

A couple of DNA ligation-independent cloning (LIC) methods have been reported to meet various requirements in metabolic engineering and synthetic biology. The principle of LIC is the assembly of multiple overlapping DNA fragments by single-stranded (ss) DNA overlaps annealing. Here we present a method to generate single-stranded DNA overlaps based on Nicking Endonucleases (NEases) for LIC, the method was termed NE-LIC. Factors related to cloning efficiency were optimized in this study. This NE-LIC allows generating 3′-end or 5′-end ss DNA overlaps of various lengths for fragments assembly. We demonstrated that the 10 bp/15 bp overlaps had the highest DNA fragments assembling efficiency, while 5 bp/10 bp overlaps showed the highest efficiency when T4 DNA ligase was added. Its advantage over Sequence and Ligation Independent Cloning (SLIC) and Uracil-Specific Excision Reagent (USER) was obvious. The mechanism can be applied to many other LIC strategies. Finally, the NEases based LIC (NE-LIC) was successfully applied to assemble a pathway of six gene fragments responsible for synthesizing microbial poly-3-hydroxybutyrate (PHB). [ABSTRACT FROM AUTHOR]

Clustered regularly interspaced short palindromic repeats interference (CRISPRi) is used to edit eukaryotic genomes. Here, we show that CRISPRi can also be used for fine-tuning prokaryotic gene expression while simultaneously regulating multiple essential gene expression with less labor and time consumption. As a case study, CRISPRi was used to control polyhydroxyalkanoate (PHA) biosynthesis pathway flux and to adjust PHA composition. A pathway was constructed in Escherichia coli for the production of poly(3-hydroxybutyrate- co -4-hydroxybutyrate) [P(3HB- co -4HB)] from glucose. The native gene sad encoding E. coli succinate semi-aldehyde dehydrogenase was expressed under the control of CRISPRi using five specially designed single guide RNAs (sgRNAs) for regulating carbon flux to 4-hydroxybutyrate (4HB) biosynthesis. The system allowed formation of P(3HB- co -4HB) consisting of 1–9 mol% 4HB. Additionally, succinate, generated by succinyl-coA synthetase and succinate dehydrogenase (respectively encoded by genes sucC , sucD and sdhA , sdhB ) was channeled preferentially to the 4HB precursor by using selected sgRNAs such as sucC2, sucD2, sdhB2 and sdhA1 via CRISPRi. The resulting 4HB content in P(3HB- co -4HB) was found to range from 1.4 to 18.4 mol% depending on the expression levels of down-regulated genes. The results show that CRISPRi is a feasible method to simultaneously manipulate multiple genes in E. coli . [ABSTRACT FROM AUTHOR]

Abstract: Recombinant Escherichia coli was constructed for co-production of hydrogen and polyhydroxybutyrate (PHB) due to its rapid growth and convenience of genetic manipulation. In particular, anaerobic metabolic pathways dedicated to co-production of hydrogen and PHB were established due to the advantages of directing fluxes away from toxic compounds such as formate and acetate to useful products. Here, recombinant E. coli expressing hydrogenase 3 and/or acetyl-CoA synthetase showed improved PHB and hydrogen production when grown with or without acetate as a carbon source. When hydrogenase 3 was over-expressed, hydrogen yield was increased from 14 to 153mmol H2/mol glucose in a mineral salt (MS) medium with glucose as carbon source, accompanied by an increased PHB yield from 0.55 to 5.34mg PHB/g glucose in MS medium with glucose and acetate as carbon source. [Copyright &y& Elsevier]

Bacterial polyhydroxyalkanoates (PHA) are a family of intracellular polyester granules with sizes ranging from 100 to 500 nm. Due to their small sizes, it has been very difficult to separate the PHA granules from the bacterial broths. This study aims to engineer the PHA size control mechanism to obtain large PHA granular sizes beneficial for the separation. It has been reported that phasin (PhaP) is an amphiphilic protein located on the surface of PHA granules functioning to regulate sizes and numbers of PHA granules in bacterial cells, deletions on PhaPs result in reduced PHA granule number and enhanced granule sizes. Three genes phaP1 , phaP2 and phaP3 encoding three PhaP proteins were deleted in various combinations in halophilic bacterium Halomonas bluephagenesis TD01. The phaP1 -knockout strain generated much larger PHA granules with almost the same size as their producing cells without significantly affecting the PHA accumulation yet with a reduced PHA molecular weights. In contrast, the phaP2- and phaP3 -knockout strains produced slightly larger sizes of PHA granules with increased PHA molecular weights. While PHA accumulation by phaP3 -knockout strains showed a significant reduction. All of the PhaP deletion efforts could not form PHA granules larger than a normal size of H. bluephagenesis TD01. It appears that the PHA granular sizes could be limited by bacterial cell sizes. Therefore, genes minC and minD encoding proteins that block formation of cell fission rings (Z-rings) were over-expressed in various phaP deleted H. bluephagenesis TD01, resulting in large cell sizes of H. bluephagenesis TD01 containing PHA granules with sizes of up to 10 μm that has never been observed previously. It can be concluded that PHA granule sizes are limited by the cell sizes. By engineering a large cell morphology large PHA granules can be produced by PhaP deleted mutants. • The phaP1 -deleted H. bluephagenesis generated larger PHA granules with reduced number. • PHA granular sizes are limited by the cell sizes in PhaP deleted mutants of H. bluephagenesis. • Enlarged H. bluephagenesis (ΔphaP1) accumulates PHB granules with sizes of up to 10 μm. • Cells of H. bluephagenesis (ΔphaP1) were precipitated by weak centrifugation. [ABSTRACT FROM AUTHOR]

Poly(3-hydroxybutyrate- co -3-hydroxyvalerate) (PHBV) is a promising biopolyester with good mechanical properties and biodegradability. Large-scale production of PHBV is still hindered by the high production cost. CRISPR/Cas9 method was used to engineer the TCA cycle in Halomonas bluephagenesis on its chromosome for production of PHBV from glucose as a sole carbon source. Two TCA cycle related genes sdhE and icl encoding succinate dehydrogenase assembly factor 2 and isocitrate lysase were deleted, respectively, in H. bluephagenesis TD08AB containing PHBV synthesis genes on the chromosome, to channel more flux to increase the 3-hydroxyvalerate (3HV) ratio of PHBV. Due to a poor growth behavior of the mutant strains, H. bluephagenesis TY194 equipped with a medium strength P porin -194 promoter was selected for further studies. The sdhE and/or icl mutant strains of H. bluephagenesis TY194 were constructed to show enhanced cell growth, PHBV synthesis and 3HV molar ratio. Gluconate was used to activate ED pathway and thus TCA cycle to increase 3HV content. H. bluephagenesis TY194 (Δ sdhE Δ icl) was found to synthesize 17mol% 3HV in PHBV. Supported by the synergetic function of phosphoenolpyruvate carboxylase and Vitreoscilla hemoglobin encoded by genes ppc and vgb inserted into the chromosome of H. bluephagenesis TY194 (Δ sdhE) serving to enhance TCA cycle activity, a series of strains were generated that could produce PHBV containing 3–18mol% 3HV using glucose as a sole carbon source. Shake flask studies showed that H. bluephagenesis TY194 (Δ sdhE , G7::P porin - ppc) produced 6.3 g/L cell dry weight (CDW), 65% PHBV in CDW and 25mol% 3HV in PHBV when grown in glucose and gluconate. 25mol% 3HV was the highest reported via chromosomal expression system. PHBV copolymers with different 3HV molar ratios were extracted and characterized. Next-generation industrial biotechnology (NGIB) based on recombinant H. bluephagenesis grown under unsterile and continuous conditions, allows production of P(3HB-0∼25mol% 3HV) in a convenient way with reduced production complexity and cost. • Deletion on two TCA cycle related genes sdhE and icl of H. bluephagenesis channels flux to 3HV synthesis. • Promoter engineering was conducted to control 3HV synthesis operon to construct a better performance strain. • Gluconate was used to regulate NADH/NAD+ to improve TCA cycle activity for enhanced 3HV synthesis. • Chromosomal expression of ppc and vgb in recombinant strain grown on glucose led to formation of PHBV with 0–24 mol% 3HV. [ABSTRACT FROM AUTHOR]

Poly(3-hydroxypropionate) (P3HP) is the strongest family member of microbial polyhydroxyalkanoates (PHA) synthesized by bacteria grown on 1,3-propandiol or glycerol. In this study synthesis pathways of P3HP and its copolymer P3HB3HP of 3-hydroxybutyrate (3HB) and 3-hydroxypropionate (3HP) were assembled respectively to allow their synthesis from glucose, a more abundant carbon source. Recombinant Escherichia coli was constructed harboring the P3HP synthetic pathway consisting of heterologous genes encoding glycerol-3-phosphate dehydrogenase ( gpd1 ), glycerol-3-P phosphatase ( gpp2 ) from Saccharomyces cerevisiae that catalyzes formation of glycerol from glucose, and genes coding glycerol dehydratase ( dhaB123 ) with its reactivating factors ( gdrAB ) from Klebsiella pneumoniae that transfer glycerol to 3-hydroxypropionaldehyde, as well as gene encoding propionaldehyde dehydrogenase ( pdup ) from Salmonella typhimurium which converts 3-hydroxypropionaldehyde to 3-hydroxypropionyl-CoA, together with the gene of PHA synthase ( phaC ) from Ralstonia eutropha which polymerizes 3-hydroxypropionyl-CoA into P3HP. When phaA and phaB from Ralstonia eutropha respectively encoding β-ketothiolase and acetoacetate reductase, were introduced into the above P3HP producing recombinant E. coli , copolymers poly(3-hydroxybutyrate- co -3-hydroxypropionate) (P3HB3HP) were synthesized from glucose as a sole carbon source. The above E. coli recombinants grown on glucose LB medium successfully produced 5 g/L cell dry weight containing 18% P3HP and 42% P(3HB- co -84 mol% 3HP), respectively, in 48 h shake flask studies. [ABSTRACT FROM AUTHOR]

Abstract: Copolyesters of 3-hydroxypropionate (3HP) and 4-hydroxybutyrate (4HB), abbreviated as P(3HP-co-4HB), was synthesized by Escherichia coli harboring a synthetic pathway consisting of five heterologous genes including orfZ encoding 4-hydroxybutyrate-coenzyme A transferase from Clostridium kluyveri, pcs’ encoding the ACS domain of tri-functional propionyl-CoA ligase (PCS) from Chloroflexus aurantiacus, dhaT and aldD encoding dehydratase and aldehyde dehydrogenase from Pseudomonas putida KT2442, and phaC1 encoding PHA synthase from Ralstonia eutropha. When grown on mixtures of 1,3-propanediol (PDO) and 1,4-butanediol (BDO), compositions of 4HB in microbial P(3HP-co-4HB) were controllable ranging from 12mol% to 82mol% depending on PDO/BDO ratios. Nuclear magnetic resonance (NMR) spectra clearly indicated the polymers were random copolymers of 3HP and 4HB. Their mechanical and thermal properties showed obvious changes depending on the monomer ratios. Morphologically, P(3HP-co-4HB) films only became fully transparent when monomer 4HB content was around 67mol%. For the first time, P(3HP-co-4HB) with adjustable monomer ratios were produced and characterized. [Copyright &y& Elsevier]

Abstract: Folate derivatives are crucial growth factors for Ketogulonigenium vulgare which is used in mixed culture with Bacillus megaterium for the industrial production of 2-keto-l-gulonic acid (2-KGA), the precursor of l-ascorbic acid (l-AA) or vitamin C (Vc). To improve the growth and 2-KGA production, five genes involved in folate biosynthesis identified in a folate gene cluster from Lactococcus lactis MG1363, including folB, folKE, folP, folQ and folC, were over-expressed in K. vulgare. Intracellular folate concentration in the recombinant strain harboring folate biosynthesis genes cluster under the control of P sdh (sorbose dehydrogenase gene sdh promoter from K. vulgare) was 8 times higher than that of the wildtype K. vulgare DSM 4025 (P <0.001). In shake flask studies, the cell density and 2-KGA production of the recombinant K. vulgare Rif (pMCS2PsdhfolBC) were increased by 18% (P <0.001) and 14% (P <0.001), respectively, under a relatively stable pH 7 condition. In fermentor studies, enhancements around 25% cell density (P <0.001) and approximately 35% 2-KGA productivity (P <0.001) were observed in comparison with the controls without over-expressing the folate biosynthesis genes. This was the first successful study of metabolic engineering on K. vulgare for enhanced 2-KGA production. [Copyright &y& Elsevier]