Biosynthesis of platform chemical 3-hydroxypropionic acid (3-HP) directly from CO2 in cyanobacterium Synechocystis sp. PCC 6803

3-hydroxypropionic acid (3-HP) is an important platform chemical with a wide range of applications. So far large-scale production of 3-HP has been mainly through petroleum-based chemical processes, whose sustainability and environmental issues have attracted widespread attention. With the ability to fix CO₂ directly, cyanobacteria have been engineered as an autotrophic microbial cell factory to produce fuels and chemicals. In this study, we constructed the biosynthetic pathway of 3-HP in cyanobacterium Synechocystis sp. PCC 6803, and then optimized the system through the following approaches: i) increasing expression of malonyl-CoA reductase (MCR) gene using different promoters and cultivation conditions; ii) enhancing supply of the precursor malonyl-CoA by overexpressing acetyl-CoA carboxylase and biotinilase; iii) improving NADPH supply by overexpressing the NAD(P) transhydrogenase gene; iv) directing more carbon flux into 3-HP by inactivating the competing pathways of PHA and acetate biosynthesis. Together, the efforts led to a production of 837.18 mg L⁻¹ (348.8 mg/g dry cell weight) 3-HP directly from CO₂ in Synechocystis after 6 days cultivation, demonstrating the feasibility photosynthetic production of 3-HP directly from sunlight and CO₂ in cyanobacteria. In addition, the results showed that overexpression of the ribulose-1, 5-bisphosphate carboxylase/oxygenase (Rubisco) gene from Anabaena sp. PCC 7120 and Synechococcus sp. PCC 7942 led to no increase of 3-HP production, suggesting CO₂ fixation may not be a rate-limiting step for 3-HP biosynthesis in Synechocystis.     

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.     

Development of a deletion mutant of Pseudomonas denitrificans that does not degrade 3-hydroxypropionic acid

Pseudomonas denitrificans is a gram-negative bacterium that can produce vitamin B₁₂ under aerobic conditions. Recently, recombinant strains of P. denitrificans overexpressing a vitamin B₁₂-dependent glycerol dehydratase (DhaB) were developed to produce 3-hydroxypropionic acid (3-HP) from glycerol. The recombinant P. denitrificans could produce 3-HP successfully under aerobic conditions without an exogenous supply of vitamin B₁₂, but the 3-HP produced disappeared during extended cultivation due to the 3-HP degradation activity in this strain. This study developed mutant strains of P. denitrificans that do not degrade 3-HP. The following eight candidate enzymes, which might be responsible for 3-HP degradation, were selected, cloned, and studied for their activity in Escherichia coli: four (putative) 3-hydroxyisobutyrate dehydrogenases (3HIBDH), a putative 3-HP dehydrogenase (3HPDH), an alcohol dehydrogenase (ADH), and two choline dehydrogenases (CHDH). Among them, 3HIBDHI, 3HIBDHIV, and 3HPDH exhibited 3-HP degrading activity when expressed heterologously in E. coli. When 3hpdh alone or along with 3hibdhIV were disrupted from P. denitrificans, the mutant P. denitrificans exhibited greatly reduced 3-HP degradation activity that could not grow on 3-HP as the sole carbon and energy source. When the double mutant P. denitrificans Δ3hpdhΔ3hibdhIV was transformed with DhaB, an improved 3-HP yield (0.78 mol/mol) compared to that of the wild-type counterpart (0.45 mol/mol) was obtained from a 24-h flask culture. This study indicates that 3hpdh and 3hibdhIV (to a lesser extent) are mainly responsible for 3-HP degradation in P. denitrificans and their deletion can prevent 3-HP degradation during its production by recombinant P. denitrificans.     

Production of optically pure d-lactate from CO2 by blocking the PHB and acetate pathways and expressing d-lactate dehydrogenase in cyanobacterium Synechocystis sp. PCC 6803

Lactate is an important industrial material with numerous potential applications, and its production from carbon dioxide is very attractive. d-Lactate is an essential monomer for production of thermostable polylactide. The photoautotrophic prokaryote cyanobacterium Synechocystis sp. PCC 6803 represents a promising host for biosynthesis of d-lactate from CO₂ as it only contains d-lactate dehydrogenase. The production of d-lactate from CO₂ by an engineered strain of Synechocystis sp. PCC 6803 with overexpressing d-lactate dehydrogenase and a soluble transhydrogenase has been reported recently. Here, we report an alternative engineering strategy to produce d-lactate from CO₂. This strategy involves blocking two competitive pathways, the native poly-3-hydroxybutyrate and acetate pathways from the acetyl-CoA node, and introducing a more efficient d-lactate dehydrogenase into Synechocystis sp. PCC 6803. The engineered strain of Synechocystis sp. PCC 6803 was capable of producing 1.06 g/L of d-lactate from CO₂. This alternative strategy for the production of optically pure d-lactate could also be used to produce other acetyl-CoA-derived chemicals from CO₂ by using engineered cyanobacteria.     

Effect of puuC overexpression and nitrate addition on glycerol metabolism and anaerobic 3-hydroxypropionic acid production in recombinant Klebsiella pneumoniae ΔglpKΔdhaT

3-Hydroxypropionic acid (3-HP), an industrially important platform chemical, is used as a precursor during the production of many commercially important chemicals. Recently, recombinant strains of K. pneumoniae overexpressing an NAD⁺-dependent γ-glutamyl-γ-aminobutyraldehyde dehydrogenase (PuuC) enzyme of K. pneumoniae DSM 2026 were shown to produce 3-HP from glycerol without the addition coenzyme B₁₂, which is expensive. However, 3-HP production in K. pneumoniae is accompanied with NADH generation, and this always results in large accumulation of 1,3-propanediol (1,3-PDO) and lactic acid. In this study, we investigated the potential use of nitrate as an electron acceptor both to regenerate NAD⁺ and to prevent the formation of byproducts during anaerobic production of 3-HP from glycerol. Nitrate addition could improve NAD⁺ regeneration, but decreased glycerol flux towards 3-HP production. To divert more glycerol towards 3-HP, a novel recombinant strain K. pneumoniae ΔglpKΔdhaT (puuC) was developed by disrupting the glpK gene, which encodes glycerol kinase, and the dhaT gene, which encodes 1,3-propanediol oxidoreductase. This strain showed improved cellular NAD⁺ concentrations and a high carbon flux towards 3-HP production. Through anaerobic cultivation in the presence of nitrate, this recombinant strain produced more than 40±3 mM 3-HP with more than 50% yield on glycerol in shake flasks and 250±10 mM 3-HP with approximately 30% yield on glycerol in a fed-batch bioreactor.     

Metabolic engineering of Corynebacterium glutamicum for the production of 3-hydroxypropionic acid from glucose and xylose

3-Hydroxypropionic acid (3-HP) is a promising platform chemical which can be used for the production of various value-added chemicals. In this study,Corynebacterium glutamicum was metabolically engineered to efficiently produce 3-HP from glucose and xylose via the glycerol pathway. A functional 3-HP synthesis pathway was engineered through a combination of genes involved in glycerol synthesis (fusion of gpd and gpp from Saccharomyces cerevisiae) and 3-HP production (pduCDEGH from Klebsiella pneumoniae and aldehyde dehydrogenases from various resources). High 3-HP yield was achieved by screening of active aldehyde dehydrogenases and by minimizing byproduct synthesis (gapA^A1GΔldhAΔpta-ackAΔpoxBΔglpK). Substitution of phosphoenolpyruvate-dependent glucose uptake system (PTS) by inositol permeases (iolT1) and glucokinase (glk) further increased 3-HP production to 38.6 g/L, with the yield of 0.48 g/g glucose. To broaden its substrate spectrum, the engineered strain was modified to incorporate the pentose transport gene araE and xylose catabolic gene xylAB, allowing for the simultaneous utilization of glucose and xylose. Combination of these genetic manipulations resulted in an engineered C. glutamicum strain capable of producing 62.6 g/L 3-HP at a yield of 0.51 g/g glucose in fed-batch fermentation. To the best of our knowledge, this is the highest titer and yield of 3-HP from sugar. This is also the first report for the production of 3-HP from xylose, opening the way toward 3-HP production from abundant lignocellulosic feedstocks.     

Engineering Hydrogen Gas Production from Formate in a Hyperthermophile by Heterologous Production of an 18-Subunit Membrane-bound Complex

Biohydrogen gas has enormous potential as a source of reductant for the microbial production of biofuels, but its low solubility and poor gas mass transfer rates are limiting factors. These limitations could be circumvented by engineering biofuel production in microorganisms that are also capable of generating H₂ from highly soluble chemicals such as formate, which can function as an electron donor. Herein, the model hyperthermophile, Pyrococcus furiosus, which grows optimally near 100 °C by fermenting sugars to produce H₂, has been engineered to also efficiently convert formate to H₂. Using a bacterial artificial chromosome vector, the 16.9-kb 18-gene cluster encoding the membrane-bound, respiratory formate hydrogen lyase complex of Thermococcus onnurineus was inserted into the P. furiosus chromosome and expressed as a functional unit. This enabled P. furiosus to utilize formate as well as sugars as an H₂ source and to do so at both 80° and 95 °C, near the optimum growth temperature of the donor (T. onnurineus) and engineered host (P. furiosus), respectively. This accomplishment also demonstrates the versatility of P. furiosus for metabolic engineering applications.     

Maltose fermentation to acetate,CO2 and H2 in the anaerobic hyperthermophilic archaeon Pyrococcus furiosus: evidence for the operation of a novel sugar fermentation pathway

The hyperthermophilic anaerobe Pyrococcus furiosus was grown on maltose as energy and carbon source. During growth 1 mol maltose was fermented to 3–4 mol acetate, 6–7 mol H₂ and 3–4 mol CO₂. The presence of the following enzyme activities in cell extracts of maltose-grown P. furiosus indicate that the sugar is degraded to pyruvate and H₂ by a modified non-phosphorylated Entner-Doudoroff-pathway (the values given in brackets are specific enzyme activities at 100 °C): Glucose: methyl viologen oxidoreductase (0.03 U/mg); 2-keto-3-deoxy-gluconate aldolase (0.03 U/mg); glyceraldehyde: benzyl viologen oxidoreductase (2.6 U/mg), glycerate kinase (2-phosphoglycerate forming) (0.48 U/mg), enolase (10.4 U/mg), pyruvate kinase (1.4 U/mg). Hexokinase, glucose-6-phosphate dehydrogenase, 2-keto-3-deoxy-6-phosphogluconate aldolase and phosphofructokinase could not be detected. Further conversion of pyruvate to acetate, CO₂ and H₂ involves pyruvate: ferredoxin oxidoreductase (0.4 U/mg; T=60°C with Clostridium pasteurianum ferredoxin as electron acceptor), hydrogen: methyl viologen ixodoreductase (3.4 U/mg) and ADP-dependent acetyl-CoA synthetase (1.9 U/mg). Phosphate acetyl transferase and acetate kinase could not be detected. The ADP-dependent acetyl-CoA synthetase catalyzes ATP synthesis via the mechanism of substrate level phosphorylation and apparently constitutes the only ATP conserving site during maltose catabolism in P. furiosus.This novel pathway of maltose fermentation to acetate, CO₂ and H₂ in the anaerobic archaeon P. furiosus may represent a phylogenetically ancient pathway of sugar fermentation.Non-standard abbreviations DTE dithioerythritol - MV methyl viologen - BV benzyl viologen - CHES cyclohexylamino-ethane sulfonic acid - ABTS 2,2-Azino-di-(3-ethylbenzthiazoliumsulfonate)     

Temperature-dependent acetoin production by Pyrococcus furiosus is catalyzed by a biosynthetic acetolactate synthase and its deletion improves ethanol production

The hyperthermophilic archaeon, Pyrococcus furiosus, grows optimally near 100 °C by fermenting sugars to acetate, carbon dioxide and molecular hydrogen as the major end products. The organism has recently been exploited to produce biofuels using a temperature-dependent metabolic switch using genes from microorganisms that grow near 70 °C. However, little is known about its metabolism at the lower temperatures. We show here that P. furiosus produces acetoin (3-hydroxybutanone) as a major product at temperatures below 80 °C. A novel type of acetolactate synthase (ALS), which is involved in branched-chain amino acid biosynthesis, is responsible and deletion of the als gene abolishes acetoin production. Accordingly, deletion of als in a strain of P. furiosus containing a novel pathway for ethanol production significantly improved the yield of ethanol. These results also demonstrate that P. furiosus is a potential platform for the biological production of acetoin at temperatures in the 70–80 °C range.     

Improving poly-3-hydroxybutyrate production in Escherichia coli by combining the increase in the NADPH pool and acetyl-CoA availability

The biosynthesis of poly-3-hydroxybutyrate (P3HB), a biodegradable bio-plastic, requires acetyl-CoA as precursor and NADPH as cofactor. Escherichia coli has been used as a heterologous production model for P3HB, but metabolic pathway analysis shows a deficiency in maintaining high levels of NADPH and that the acetyl-CoA is mainly converted to acetic acid by native pathways. In this work the pool of NADPH was increased 1.7-fold in E. coli MG1655 through plasmid overexpression of the NADP⁺-dependent glyceraldehyde 3-phosphate dehydrogenase gene (gapN) from Streptococcus mutans (pTrcgapN). Additionally, by deleting the main acetate production pathway (ackA-pta), the acetic acid production was abolished, thus increasing the acetyl-CoA pool. The P3HB biosynthetic pathway was heterologously expressed in strain MG1655 Δack-pta/pTrcgapN, using an IPTG inducible vector with the P3HB operon from Azotobacter vinelandii (pPHB _Av ). Cultures were performed in controlled fermentors using mineral medium with glucose as the carbon source. Accordingly, the mass yield of P3HB on glucose increased to 73 % of the maximum theoretical and was 30 % higher when compared to the progenitor strain (MG1655/pPHB _Av ). In comparison with the wild type strain expressing pPHB _Av , the specific accumulation of PHB (g_PHB/g_DCW) in MG1655 Δack-pta/pTrcgapN/pPHB _Av increased twofold, indicating that as the availability of NADPH is raised and the production of acetate abolished, a P3HB intracellular accumulation of up to 84 % of the E. coli dry weight is attainable.     

Introduction of a bacterial acetyl-CoA synthesis pathway improves lactic acid production in Saccharomyces cerevisiae

Acid-tolerant Saccharomyces cerevisiae was engineered to produce lactic acid by expressing heterologous lactate dehydrogenase (LDH) genes, while attenuating several key pathway genes, including glycerol-3-phosphate dehydrogenase1 (GPD1) and cytochrome-c oxidoreductase2 (CYB2). In order to increase the yield of lactic acid further, the ethanol production pathway was attenuated by disrupting the pyruvate decarboxylase1 (PDC1) and alcohol dehydrogenase1 (ADH1) genes. Despite an increase in lactic acid yield, severe reduction of the growth rate and glucose consumption rate owing to the absence of ADH1 caused a considerable decrease in the overall productivity. In Δadh1 cells, the levels of acetyl-CoA, a key precursor for biologically applicable components, could be insufficient for normal cell growth. To increase the cellular supply of acetyl-CoA, we introduced bacterial acetylating acetaldehyde dehydrogenase (A-ALD) enzyme (EC 1.2.1.10) genes into the lactic acid-producing S. cerevisiae. Escherichia coli-derived A-ALD genes, mhpF and eutE, were expressed and effectively complemented the attenuated acetaldehyde dehydrogenase (ALD)/acetyl-CoA synthetase (ACS) pathway in the yeast. The engineered strain, possessing a heterologous acetyl-CoA synthetic pathway, showed an increased glucose consumption rate and higher productivity of lactic acid fermentation. The production of lactic acid was reached at 142 g/L with production yield of 0.89 g/g and productivity of 3.55 g L⁻¹ h⁻¹ under fed-batch fermentation in bioreactor. This study demonstrates a novel approach that improves productivity of lactic acid by metabolic engineering of the acetyl-CoA biosynthetic pathway in yeast.     

Engineering of a modular and synthetic phosphoketolase pathway for photosynthetic production of acetone from CO2 in Synechococcus elongatus PCC 7942 under light and aerobic condition

Capture and conversion of CO₂ to valuable chemicals is intended to answer global challenges on environmental issues, climate change and energy security. Engineered cyanobacteria have been enabled to produce industry‐relevant chemicals from CO₂. However, the final products from cyanobacteria have often been mixed with fermented metabolites during dark fermentation. In this study, our engineering of Synechococcus elongatus PCC 7942 enabled continuous conversion of CO₂ to volatile acetone as sole product. This process occurred during lighted, aerobic culture via both ATP‐driven malonyl‐CoA synthesis pathway and heterologous phosphoketolase (PHK)‐phosphotransacetylase (Pta) pathway. Because of strong correlations between the metabolic pathways of acetate and acetone, supplying the acetyl‐CoA directly from CO₂ in the engineered strain, led to sole production of acetone (22.48 mg/L ± 1.00) without changing nutritional constraints, and without an anaerobic shift. Our engineered S. elongatus strains, designed for acetone production, could be modified to create biosolar cell factories for sustainable photosynthetic production of acetyl‐CoA‐derived biochemicals.     

Metabolic rewiring of synthetic pyruvate dehydrogenase bypasses for acetone production in cyanobacteria

Designing synthetic pathways for efficient CO₂ fixation and conversion is essential for sustainable chemical production. Here we have designed a synthetic acetate‐acetyl‐CoA/malonyl‐CoA (AAM) bypass to overcome an enzymatic activity of pyruvate dehydrogenase complex. This synthetic pathway utilizes acetate assimilation and carbon rearrangements using a methyl malonyl‐CoA carboxyltransferase. We demonstrated direct conversion of CO₂ into acetyl‐CoA‐derived acetone as an example in photosynthetic Synechococcus elongatus PCC 7942 by increasing the acetyl‐CoA pools. The engineered cyanobacterial strain with the AAM‐bypass produced 0.41 g/L of acetone at 0.71 m/day of molar productivity. This work clearly shows that the synthetic pyruvate dehydrogenase bypass (AAM‐bypass) is a key factor for the high‐level production of an acetyl‐CoA‐derived chemical in photosynthetic organisms.     

Autocatalytic activation of acetyl-CoA synthase

Acetyl-CoA synthase (ACS ACS/CODH CODH/ACS) from Moorella thermoacetica catalyzes the synthesis of acetyl-CoA from CO, CoA, and a methyl group of a corrinoid-iron-sulfur protein (CoFeSP). A time lag prior to the onset of acetyl-CoA production, varying from 4 to 20 min, was observed in assay solutions lacking the low-potential electron-transfer agent methyl viologen (MV). No lag was observed when MV was included in the assay. The length of the lag depended on the concentrations of CO and ACS, with shorter lags found for higher [ACS] and sub-saturating [CO]. Lag length also depended on CoFeSP. Rate profiles of acetyl-CoA synthesis, including the lag phase, were numerically simulated assuming an autocatalytic mechanism. A similar reaction profile was monitored by UV-vis spectrophotometry, allowing the redox status of the CoFeSP to be evaluated during this process. At early stages in the lag phase, Co²⁺FeSP reduced to Co⁺FeSP, and this was rapidly methylated to afford CH₃-Co³⁺FeSP. During steady-state synthesis of acetyl-CoA, CoFeSP was predominately in the CH₃-Co³⁺FeSP state. As the synthesis rate declined and eventually ceased, the Co⁺FeSP state predominated. Three activation reductive reactions may be involved, including reduction of the A- and C-clusters within ACS and the reduction of the cobamide of CoFeSP. The B-, C-, and D-clusters in the subunit appear to be electronically isolated from the A-cluster in the connected subunit, consistent with the ~70 Å distance separating these clusters, suggesting the need for an in vivo reductant that activates ACS and/or CoFeSP.Abbreviations ACS acetyl-CoA synthase, also known as CODH (carbon monoxide dehydrogenase) or CODH/ACS or ACS/CODH - CH₃-Co³⁺FeSP, Co²⁺FeSP, and Co⁺FeSP corrinoid-iron-sulfur protein with the cobalamin in the methylated 3+, unmethylated 2+, and unmethylated 1+ states - CoA coenzyme A - DTT dithiothreitol - H-THF or THF tetrahydrofolic acid or tetrahydrofolate - MT methyl transferase - MV methyl viologen     

Strategies for reliable and improved large-scale production of Pyrococcus furiosus with integrated purification of hydrogenase I

The hyperthermophilic archaeon Pyrococcus furiosus is an interesting organism for research and application, especially owing to its unique NADPH-dependent hydrogenase I. However, mass production of P. furiosus through fermentation is susceptible to fault because of its sensitivity to oxygen, a short exponential and stationary phase and a rapid cell lysis in typical cultivation process. In this study, significant improvement for pilot plant scale production processes for P. furiosus biomass was made by investigations of the fermentation process with subsequent hydrogenase I enzyme purification. Scale-up in a 300-L stirred tank bioreactor was successfully achieved. A repeated-batch cultivation process with high reproducibility and productivity was realized. Furthermore, the enzyme hydrogenase I was purified, and its activity tested and verified. The improvements in this production process for the production of large amount of P. furiosus biomass and hydrogenase I have been achieved, especially by successfully implementing the following key measures and steps: unsterile cultivation setup, skipping typical intermediate preculture and inoculation steps, accelerating the cultivation process by defining an optimal state of the inoculation, optimal time point of biomass harvesting and finally by choosing a one-step purification procedure for enzyme recovery.     

Aldehyde dehydrogenase activity is important to the production of 3-hydroxypropionic acid from glycerol by recombinant Klebsiella pneumoniae

3-Hydroxypropionic acid (3-HP) can be produced from glycerol via two enzymatic reactions catalyzed by a coenzyme B₁₂-dependent glycerol dehydratase (GDHt) and aldehyde dehydrogenase (ALDH) in Klebsiella pneumoniae. As the intracellular GDHt activity in K. pneumoniae is high, the overall rate of 3-HP production is controlled by the ALDH activity. To examine the effect of different ALDH activity on 3-HP production, three different ALDHs, AldH from Escherichia coli (EaldH), PuuC from K. pneumoniae (PuuC) and KGSADH from Azospirillum brasilense (KGSADH), were overexpressed and compared in various recombinant K. pneumoniae strains. In addition, the genes encoding DhaT and YqhD, which are responsible for the conversion of 3-hydroxypropionaldehyde (3-HPA) to 1,3-propanediol (1,3-PDO), were disrupted individually from K. pneumoniae to enhance the carbon flux from 3-HPA to 3-HP. When the ALDH activity was measured in various recombinant K. pneumoniae, KGSADH showed the highest crude cell activity of 8.0 U/mg protein, which was 2 and 4 times higher than that of PuuC and EaldH, respectively. The different ALDH activities had a significant effect on 3-HP production in a flask culture containing 100 mM glycerol, and K. pneumoniae ΔdhaT (KGSADH) resulted in the highest titer (64 mM) among the nine recombinant strains (three ALDH × three host strains; one wild type and two mutants). In glycerol fed-batch bioreactor cultivation, K. pneumoniae ΔdhaT (KGSADH) exhibited 3-HP production at >16 g/L in 48 h with a glycerol carbon yield of >40%. In comparison, K. pneumoniae ΔdhaT (PuuC) produced only 11 g/L 3-HP in 48 h with a yield of >23%. This study demonstrates that a high ALDH activity is essential for the effective production of 3-HP from glycerol with recombinant K. pneumoniae.     

Characterization of propionate CoA-transferase from Ralstonia eutropha H16

In this study, a propionate CoA-transferase (H16_A2718; EC 2.8.3.1) from Ralstonia eutropha H16 (Pct _Re ) was characterized in detail. Glu342 was identified as catalytically active amino acid residue via site-directed mutagenesis. Activity of Pct _Re was irreversibly lost after the treatment with NaBH₄ in the presence of acetyl-CoA as it is shown for all CoA-transferases from class I, thereby confirming the formation of the covalent enzyme-CoA intermediate by Pct _Re . In addition to already known CoA acceptors for Pct _Re such as 3-hydroxypropionate, 3-hydroxybutyrate, acrylate, succinate, lactate, butyrate, crotonate and 4-hydroxybutyrate, it was found that glycolate, chloropropionate, acetoacetate, valerate, trans-2,3-pentenoate, isovalerate, hexanoate, octanoate and trans-2,3-octenoate formed also corresponding CoA-thioesters after incubation with acetyl-CoA and Pct _Re . Isobutyrate was found to be preferentially used as CoA acceptor amongst other carboxylates tested in this study. In contrast, no products were detected with acetyl-CoA and formiate, bromopropionate, glycine, pyruvate, 2-hydroxybutyrate, malonate, fumarate, itaconate, β-alanine, γ-aminobutyrate, levulate, glutarate or adipate as potential CoA acceptor. Amongst CoA donors, butyryl-CoA, crotonyl-CoA, 3-hydroxybutyryl-CoA, isobutyryl-CoA, succinyl-CoA and valeryl-CoA apart from already known propionyl-CoA and acetyl-CoA could also donate CoA to acetate. The highest rate of the reaction was observed with 3-hydroxybutyryl-CoA (2.5 μmol mg^?1 min^?1). K _m values for propionyl-CoA, acetyl-CoA, acetate and 3-hydroxybutyrate were 0.3, 0.6, 4.5 and 4.3 mM, respectively. The rather broad substrate range might be a good starting point for enzyme engineering approaches and for the application of Pct _Re in biotechnological polyester production.