Biosynthesis of Polyhydroxyalkanoate Terpolymer from Methanol via the Reverse β-Oxidation Pathway in the Presence of Lanthanide

Methylorubrum extorquens AM1 is the attractive platform for the production of value-added products from methanol. We previously demonstrated that M. extorquens equipped with PHA synthase with broad substrate specificity synthesized polyhydroxyalkanoates (PHAs) composed of (R)-3-hydroxybutyrate and small fraction of (R)-3-hydroxyvalerate (3HV) and (R)-3-hydroxyhexanoate (3HHx) units on methanol. This study further engineered M. extorquens for biosynthesis of PHAs with higher 3HV and 3HHx composition focusing on the EMC pathway involved in C1 assimilation. The introduction of ethylmalonyl-CoA decarboxylase, catalyzing a backward reaction in the EMC pathway, aiming to increase intracellular propionyl/butyryl-CoA precursors did not affect PHA composition. Reverse b-oxidation pathway and subsequent (R)-specific hydration of 2-enoyl-CoA were then enhanced by heterologous expression of four genes derived from Ralstonia eutropha for the conversion of propionyl/butyryl-CoAs to the corresponding (R)-3-hydroxyacyl-CoA monomers. The resulting strains produced PHAs with higher 3HV and 3HHx compositions, while the methylotrophic growth was severely impaired. This growth impairment was interestingly restored by the addition of La3+ without a negative impact on PHA biosynthesis, suggesting the activation of the EMC pathway by La3+. The engineered M. extorquens synthesized PHA terpolymer composed of 5.4 mol% 3HV and 0.9% of 3HHx with 41% content from methanol as a sole carbon source in the presence of La3+.

Synthetic biology toolkit for engineering Cupriviadus necator H16 as a platform for CO2 valorization

Background CO2 valorization is one of the effective methods to solve current environmental and energy problems, in which microbial electrosynthesis (MES) system has proved feasible and efficient. Cupriviadus necator (Ralstonia eutropha) H16, a model chemolithoautotroph, is a microbe of choice for CO2 conversion, especially with the ability to be employed in MES due to the presence of genes encoding [NiFe]-hydrogenases and all the Calvin–Benson–Basham cycle enzymes. The CO2 valorization strategy will make sense because the required hydrogen can be produced from renewable electricity independently of fossil fuels. Main body In this review, synthetic biology toolkit for C. necator H16, including genetic engineering vectors, heterologous gene expression elements, platform strain and genome engineering, and transformation strategies, is firstly summarized. Then, the review discusses how to apply these tools to make C. necator H16 an efficient cell factory for converting CO2 to value-added products, with the examples of alcohols, fatty acids, and terpenoids. The review is concluded with the limitation of current genetic tools and perspectives on the development of more efficient and convenient methods as well as the extensive applications of C. necator H16. Conclusions Great progress has been made on genetic engineering toolkit and synthetic biology applications of C. necator H16. Nevertheless, more efforts are expected in the near future to engineer C. necator H16 as efficient cell factories for the conversion of CO2 to value-added products.

Analysis of bacterial growth parttern in bioprocessing of polyhydroxyalkanoates from waste oil by Pseudomonas oleovorans

Pseudomonas oleovorans NCIMB 6576 and Ralstonia eutropha NCIMB 10442 were used for the production of Polyhydroxyalkanoates (PHA) from industrial waste cooking oils, the bacteria were cultured on tryptone soya broth (TSB) and Tryptone soya agar (TSA). The growth pattern of the bacteria, serial dilution and viable counting was done using the Miles and Misra method, 0.5ml (500 µl) of the sample was transferred aseptically into test tubes filled with 4.5ml ringer solution (1/4 strength) resulting in a ten-fold dilution, the growth curve of the cultures of P. oleovorans NCIMB6576 grown on TSB with and without PS oil sample shows error bars in the graph for each point depicting the standard error of the mean. The initial viable count ranges between 6.37 log10 cfu/ml and 5.1 log10 cfu/ml. The viable count reached its peak after 30 hours giving approximately 9.7 log10 cfu/ml for P. oleovorans NCIMB6576 with PS oil and 9.24 log10 cfu/ml after 30 hours as well without the oil, showing that maximum cell count was attained at the same time. The growth curves of P. oleovorans NCIMB6576 grown on TSB with and without the oil sample TS, where the errors bars depicts the standard errors of the means on each point. The initial viable count at the start of the experiments shows that for P. oleovorans NCIMB6576 grown with the oil, there was an initial viable count of 6.1 log10 cfu/ml as compared to 5.1 log10 cfu/ml without the oil respectively. It was observe that the time at which maximum cell counts was attained is slightly longer when the oil was not used as a carbon source (30 hours) as compared to the oil control (27 hours). A decline in cell count is also noticeable after 30 hours until it reaches its minimum value of 9.4 log.10 cfu/ml after 48 hours in the experiment involving the oil sample TS.

Polyhydroxyalkanoates (PHAs), bioprocessing using waste oil

Pseudomonas oleovorans NCIMB 6576 and Ralstonia eutropha NCIMB 10442 were used for the production of Polyhydroxyalkanoates (PHA) from industrial waste cooking oils, the bacteria were cultured on tryptone soya broth (TSB) and Tryptone soya agar (TSA). P. oleovorans NCIMB6576 gave a better percentage PHB yield (8.2%) with PS oil as carbon source as compared to 6.45% with TS oil. However, a very low yield (0.64%) was recorded when P. oleovorans NCIMB6576 was grown on TSB without the oils as carbon source. Ralstonia eutropha NCIMB 10442 gave an appreciable yield of 13.63% and 14.80% with PS and TS oil samples respectively as carbon source with negligible variation in the yields. The results obtained across all experiments were compared with one another. The SEM images from the PHB samples generated from the experiments shows that there is a slight difference in the surface morphologies of the PHB with respect to the oil samples as well as the different bacteria used in the experiment.

Upcycling Biodegradable PVA/Starch Film to a Bacterial Biopigment and Biopolymer

Meeting the challenge of circularity for plastics requires amenability to repurposing post-use, as equivalent or upcycled products. In a compelling advancement, complete circularity for a biodegradable polyvinyl alcohol/thermoplastic starch (PVA/TPS) food packaging film was demonstrated by bioconversion to high-market-value biopigments and polyhydroxybutyrate (PHB) polyesters. The PVA/TPS film mechanical properties (tensile strength (σu), 22.2 ± 4.3 MPa; strain at break (εu), 325 ± 73%; and Young’s modulus (E), 53–250 MPa) compared closely with low-density polyethylene (LDPE) grades used for food packaging. Strong solubility of the PVA/TPS film in water was a pertinent feature, facilitating suitability as a carbon source for bioprocessing and microbial degradation. Biodegradability of the film with greater than 50% weight loss occurred within 30 days of incubation at 37 °C in a model compost. Up to 22% of the PVA/TPS film substrate conversion to biomass was achieved using three bacterial strains, Ralstonia eutropha H16 (Cupriavidus necator ATCC 17699), Streptomyces sp. JS520, and Bacillus subtilis ATCC6633. For the first time, production of the valuable biopigment (undecylprodigiosin) by Streptomyces sp. JS520 of 5.3 mg/mL and the production of PHB biopolymer at 7.8% of cell dry weight by Ralstonia eutropha H16 from this substrate were reported. This low-energy, low-carbon post-use PVA/TPS film upcycling model approach to plastic circularity demonstrates marked progress in the quest for sustainable and circular plastic solutions.

Production of soluble regulatory hydrogenase from Ralstonia eutropha in Escherichia coli using a fed-batch-based autoinduction system

Background Autoinduction systems can regulate protein production in Escherichia coli without the need to monitor cell growth or add inducer at the proper time following culture growth. Compared to classical IPTG induction, autoinduction provides a simple and fast way to obtain high protein yields. In the present study, we report on the optimization process for the enhanced heterologous production of the Ralstonia eutropha regulatory hydrogenase (RH) in E. coli using autoinduction. These autoinduction methods were combined with the EnPresso B fed-batch like growth system, which applies slow in situ enzymatic glucose release from a polymer to control cell growth and protein synthesis rate. Results We were able to produce 125 mg L−1 RH corresponding to a productivity averaged over the whole process time of 3 mg (L h)−1 in shake flasks using classic single-shot IPTG induction. IPTG autoinduction resulted in a comparable volumetric RH yield of 112 mg L−1 and due to the shorter overall process time in a 1.6-fold higher productivity of 5 mg (L h)−1. In contrast, lactose autoinduction increased the volumetric yield more than 2.5-fold and the space time yield fourfold reaching 280 mg L−1 and 11.5 mg (L h)−1, respectively. Furthermore, repeated addition of booster increased RH production to 370 mg L−1, which to our knowledge is the highest RH concentration produced in E. coli to date. Conclusions The findings of this study confirm the general feasibility of the developed fed-batch based autoinduction system and provide an alternative to conventional induction systems for efficient recombinant protein production. We believe that the fed-batch based autoinduction system developed herein will favor the heterologous production of larger quantities of difficult-to-express complex enzymes to enable economical production of these kinds of proteins.

General Aspects of Biodegradable Biopolymers and the Polyhydroxyalkanoates’ Family

Background: Plastic polymers are ubiquitous and life without them is practically impossible. Despite the advantages provided by the material, conventional plastics are also harmful to the environment and human health. Therefore, the search for alternatives, such as polyhydroxyalkanoates (PHAs), a family of biodegradable thermoplastic polyesters naturally produced by PHA-accumulating bacteria, such as Pseudomonas spp. and Ralstonia eutropha, through fermentative processes, is of paramount importance. Objectives: In the present work, the objective of the researchers was to develop a revisional study regarding biodegradable biopolymers and the PHAs’ importance and benefits for society and the environment. Methods: In this review, articles published since the year 2000, related to the different aspects of biodegradable plastics and PHAs, were accurately analyzed and reviewed. The subjects covered ranged from conventional plastics and the problems related to their large-scale production and the importance of biodegradable plastics, as well as PHAs, their positive aspects, and the feasibility of their use as an alternative to replace conventional plastics. Those subjects were extensively reviewed and concisely discussed. Results and Conclusions: The present study demonstrated the importance of biodegradable plastics and the PHAs’ family, its different application possibilities, and its viability as an alternative to replace conventional plastics, since it can mimic their characteristics efficiently, with the advantage of being biodegradable and produced from renewable sources.

Technical-Economical Approach for PHB Production by Ralstonia Eutropha Strain Using Concentrated Vinasse as Carbon Source and Other Biotechnological Applications

The Brazilian ethanol industry is one of the most important in the global market, however these important industrial activities have been generating significant amounts of vinasse and its management has become costly for distilleries. In this study, the aim was to evaluate concentrated and in natura vinasse as basal culture media for biotechnological processes. Different bacteria and processes were assessed: L-threonine production by E. coli THR14, with glucose as carbon source; PHB production by halophilic strain Halomonas sp. HG03, with sucrose as carbon source; and PHB biosynthesis by R. eutropha L359PCJ, which used glycerol from vinasse as carbon source. Strains were evaluated firstly in shake flasks cultivations using vinasse-based media. E. coli THR14 had no statistical difference for biomass and L-threonine concentrations among control and vinasse-based treatments (up to 50% v v-1 of in natura vinasse). Halomonas sp. HG03 and R. eutropha L359PCJ were cultivated in mineral media diluted by in natura (50% and 75% v v-1) and concentrated (50% and 75% v v-1) vinasses. Higher vinasse concentrations resulted in higher cellular growth rather than PHB accumulation for both bacteria. In vinasse-based treatments, Halomonas sp. HG03 had PHB content between 19.6 – 75.2% and R. eutropha L359PCJ, 48.4 – 68.5%. 50% (v v-1) of concentrated vinasse was the most attractive condition for PHB production by both bacteria. Further experiments in CSTR bioreactors used this nutritional condition and R. eutropha L359PCJ had PHB content of 66.3%, concentrations of residual cell dry weight (rCDW) = 9.4 g L-1 and PHB = 18.6 g L-1, with YX/S = 0.16 g gGLYCEROL-1, YP/S = 0.32 g gGLYCEROL-1 and 0.25 gPHB Lh-1. Halomonas sp. HG03 had PHB content of 45.7%, rCDW = 9.8 g L-1, PHB = 8.3 g L-1 and YX/S = 0.18 g gSUCROSE-1, YP/S = 0.16 g gSUCROSE-1 and 0.12 gPHB Lh-1. Finally, cost reductions of PHB production by R. eutropha L359PCJ with concentrated vinasse-based medium were evaluated in silico by using SuperPro Designer. As a partial source of glycerol and other nutrients for PHB production by R. eutropha L359PCJ, vinasse reduced overall production costs by 13%. Simulated processes that used concentrated vinasse-based media combined with improvements of PHB productivity and higher cellular densities had production costs between US$ 3.9 – 7.5/kgPHB and 2.6 – 7.3 years of payback time.