Porting the synthetic D‐glucaric acid pathway from Escherichia coli to Saccharomyces cerevisiae

D‐Glucaric acid can be produced as a value‐added chemical from biomass through a de novo pathway in Escherichia coli. However, previous studies have identified pH‐mediated toxicity at product concentrations of 5 g/L and have also found the eukaryotic myo‐inositol oxygenase (MIOX) enzyme to be rate‐limiting. We ported this pathway to Saccaromyces cerevisiae, which is naturally acid‐tolerant and evaluate a codon‐optimized MIOX homologue. We constructed two engineered yeast strains that were distinguished solely by their MIOX gene – either the previous version from Mus musculus or a homologue from Arabidopsis thaliana codon‐optimized for expression in S. cerevisiae – in order to identify the rate‐limiting steps for D‐glucaric acid production both from a fermentative and non‐fermentative carbon source. myo‐Inositol availability was found to be rate‐limiting from glucose in both strains and demonstrated to be dependent on growth rate, whereas the previously used M. musculus MIOX activity was found to be rate‐limiting from glycerol. Maximum titers were 0.56 g/L from glucose in batch mode, 0.98 g/L from glucose in fed‐batch mode, and 1.6 g/L from glucose supplemented with myo‐inositol. Future work focusing on the MIOX enzyme, the interplay between growth and production modes, and promoting aerobic respiration should further improve this pathway.     

Multi‐enzymatic one‐pot reduction of dehydrocholic acid to 12‐keto‐ursodeoxycholic acid with whole‐cell biocatalysts

Ursodeoxycholic acid (UDCA) is a bile acid of industrial interest as it is used as an agent for the treatment of primary sclerosing cholangitis and the medicamentous, non‐surgical dissolution of gallstones. Currently, it is prepared industrially from cholic acid following a seven‐step chemical procedure with an overall yield of <30%. In this study, we investigated the key enzymatic steps in the chemo‐enzymatic preparation of UDCA—the two‐step reduction of dehydrocholic acid (DHCA) to 12‐keto‐ursodeoxycholic acid using a mutant of 7β‐hydroxysteroid dehydrogenase (7β‐HSDH) from Collinsella aerofaciens and 3α‐hydroxysteroid dehydrogenase (3α‐HSDH) from Comamonas testosteroni. Three different one‐pot reaction approaches were investigated using whole‐cell biocatalysts in simple batch processes. We applied one‐biocatalyst systems, where 3α‐HSDH, 7β‐HSDH, and either a mutant of formate dehydrogenase (FDH) from Mycobacterium vaccae N10 or a glucose dehydrogenase (GDH) from Bacillus subtilis were expressed in a Escherichia coli BL21(DE3) based host strain. We also investigated two‐biocatalyst systems, where 3α‐HSDH and 7β‐HSDH were expressed separately together with FDH enzymes for cofactor regeneration in two distinct E. coli hosts that were simultaneously applied in the one‐pot reaction. The best result was achieved by the one‐biocatalyst system with GDH for cofactor regeneration, which was able to completely convert 100 mM DHCA to >99.5 mM 12‐keto‐UDCA within 4.5 h in a simple batch process on a liter scale. Biotechnol. Bioeng. 2013; 110: 68–77. © 2012 Wiley Periodicals, Inc.     

Metabolic self‐organization of bioluminescent Escherichia coli

A possible reason for the complexity of the signals produced by bioluminescent biosensors might be self‐organization of the cells. In order to verify this possibility, bioluminescence images of cultures of lux gene reporter Escherichia coli were recorded for several hours after being placed into 8–10 mm diameter cylindrical containers. It was found that luminous cells distribute near the three‐phase contact line, forming irregular azimuthal waves. As we show, space–time plots of quasi‐one‐dimensional bioluminescence measured along the contact line can be simulated by reaction–diffusion–chemotaxis equations, in which the reaction term for the cells is a logistic (autocatalytic) growth function. It was found that the growth rate of the luminous cells (~0.02 s^?1) is >100 times higher than the growth rate of E. coli. We provide an explanation for this result by assuming that E. coli exhibits considerable respiratory flexibility (the ability of oxygen‐induced switching from one metabolic pathway to another). According to the simple two‐state model presented here, the number of oxic (luminous) cells grows at the expense of anoxic (dark) cells, whereas the total number of (oxic and anoxic) cells remains unchanged. It is conjectured that the corresponding reaction–diffusion–chemotaxis model for bioluminescence pattern formation can be considered as a model for the energy‐taxis and metabolic self‐organization in the population of the metabolically flexible bacteria under hypoxic conditions. Copyright © 2011 John Wiley & Sons, Ltd.     

Kinetic resolution of N‐acetyl‐DL‐alanine methyl ester using immobilized Escherichia coli cells bearing recombinant esterase from Bacillus cereus

D‐alanine is widely used in medicine, food, additives, cosmetics, and other consumer items. Esterase derived from Bacillus cereus WZZ001 exhibits high hydrolytic activity and stereoselectivity. In this study, we expressed the esterase gene in Escherichia coli BL21 (DE3). We analyzed the biocatalytic resolution of N‐acetyl‐DL‐alanine methyl ester by immobilized whole E. coli BL21 (DE3) cells, which were prepared through embedding and cross‐linking. We analyzed biocatalytic resolution under the optimal conditions of pH of 7.0, temperature of 40°C and substrate concentration of at 700 mM with an enantiomeric excess of 99.99% and e.e._p of 99.50%. The immobilized recombinant B. cereus esterase E. coli BL21 (DE3) cells exhibited excellent reusability and retained 86.04% of their initial activity after 15 cycles of repeated reactions. The immobilized cells are efficient and stable biocatalysts for the preparation of N‐acetyl‐D‐alanine methyl esters.     

Engineering of recombinant E. coli cells co‐expressing P450pyrTM monooxygenase and glucose dehydrogenase for highly regio‐ and stereoselective hydroxylation of alicycles with cofactor recycling

E. coli (P450pyrTM‐GDH) with dual plasmids, pETDuet containing P450pyr triple mutant I83H/M305Q/A77S (P450pyrTM) and ferredoxin reductase (FdR) genes and pRSFDuet containing glucose dehydrogenase (GDH) and ferredoxin (Fdx) genes, was engineered to show a high activity (12.7 U g^?1 cdw) for the biohydroxylation of N‐benzylpyrrolidine 1 and a GDH activity of 106 U g^?1 protein. The E. coli cells were used as efficient biocatalysts for highly regio‐ and stereoselective hydroxylation of alicyclic substrates at non‐activated carbon atom with enhanced productivity via intracellular recycling of NAD(P)H. Hydroxylation of N‐benzylpyrrolidine 1 with resting cells in the presence of glucose showed excellent regio‐ and stereoselectivity, giving (S)‐N‐benzyl‐3‐hydroxypyrrolidine 2 in 98% ee as the sole product in 9.8 mM. The productivity is much higher than that of the same biohydroxylation using E. coli (P450pyrTM)b without expressing GDH. E. coli (P450pyrTM‐GDH) was found to be highly regio‐ and stereoselective for the hydroxylation of N‐benzylpyrrolidin‐2‐one 3 , improving the regioselectivity from 90% of the wild‐type P450pyr to 100% and giving (S)‐N‐benzyl‐4‐hydroxylpyrrolidin‐2‐one 4 in 99% ee as the sole product. A high activity of 15.5 U g^?1 cdw was achieved and (S)‐ 4 was obtained in 19.4 mM. E. coli (P450pyrTM‐GDH) was also found to be highly regio‐ and stereoselective for the hydroxylation of N‐benzylpiperidin‐2‐one 5 , increasing the ee of the product (S)‐N‐benzyl‐4‐hydroxy‐piperidin‐2‐one 6 to 94% from 33% of the wild‐type P450pyr. A high activity of 15.8 U g^?1 cdw was obtained and (S)‐ 6 was produced in 3.3 mM as the sole product. E. coli (P450pyrTM‐GDH) represents the most productive system known thus far for P450‐catalyzed hydroxylations with cofactor recycling, and the hydroxylations with E. coli (P450pyrTM‐GDH) provide with simple and useful syntheses of (S)‐ 2 , (S)‐ 4 , and (S)‐ 6 that are valuable pharmaceutical intermediates and difficult to prepare. Biotechnol. Bioeng. 2013; 110: 363–373. © 2012 Wiley Periodicals, Inc.     

Increased 3′‐Phosphoadenosine‐5′‐phosphosulfate Levels in Engineered Escherichia coli Cell Lysate Facilitate the In Vitro Synthesis of Chondroitin Sulfate A

Chondroitin sulfates (CSs) are linear glycosaminoglycans that have important applications in the medical and food industries. Engineering bacteria for the microbial production of CS will facilitate a one‐step, scalable production with good control over sulfation levels and positions in contrast to extraction from animal sources. To achieve this goal, Escherichia coli (E. coli) is engineered in this study using traditional metabolic engineering approaches to accumulate 3′‐phosphoadenosine‐5′‐phosphosulfate (PAPS), the universal sulfate donor. PAPS is one of the least‐explored components required for the biosynthesis of CS. The resulting engineered E. coli strain shows an ≈1000‐fold increase in intracellular PAPS concentrations. This study also reports, for the first time, in vitro biotransformation of CS using PAPS, chondroitin, and chondroitin‐4‐sulfotransferase (C4ST), all synthesized from different engineered E. coli strains. A 10.4‐fold increase is observed in the amount of CS produced by biotransformation by employing PAPS from the engineered PAPS‐accumulating strain. The data from the biotransformation experiments also help evaluate the reaction components that need improved production to achieve a one‐step microbial synthesis of CS. This will provide a new platform to produce CS.     

Application of solid–liquid TPPBs to the production of L‐phenylacetylcarbinol from benzaldehyde using Candida utilis

The biotransformation of benzaldehyde and glucose to L ‐phenylacetylcarbinol (PAC) using Candida utilis was demonstrated in a solid–liquid two‐phase partitioning bioreactor (TPPB) with the aim of reducing substrate, product, and by‐product toxicity via sequestration. Previous work in the field had used octanol as the sequestering phase of liquid–liquid TPPBs but was limited by the toxic effects of octanol on C. utilis. To improve solvent selection in any future studies, the critical log P of C. utilis was determined in the current study to be 4.8 and can be used to predict biocompatible solvents. Bioavailability tests showed alkanes and alkenes to be non‐bioavailable. As polymers are biocompatible and non‐bioavailable, a wide range of commercially available polymers was screened and it was demonstrated that polymer softness plays a key role in absorptive capability. The polymer Hytrel G3548L was selected as the second phase to sequester benzaldehyde, PAC, and benzyl alcohol, with partition coefficients of 35, 7.5, and 10, respectively. With a 9% by volume partitioning phase, 13.6 g/L biomass of C. utilis achieved an overall PAC concentration of 11 g/L, a 1.9‐fold improvement over the single‐phase case. Benzyl alcohol concentration was 4.5 g/L, a 1.6‐fold reduction. The volumetric productivity was 0.85 g/L h, a 1.2‐fold improvement over the single‐phase system. These results demonstrate a promising starting point for solid–liquid TPPBs for PAC production. Biotechnol. Bioeng. 2010;107:633–641. © 2010 Wiley Periodicals, Inc.     

Polymer characterization and optimization of conditions for the enhanced bioproduction of benzaldehyde by Pichia pastoris in a two‐ ;phase partitioning bioreactor

Benzaldehyde, with its apricot and almond‐like aroma, is the second most abundantly used molecule in the flavor industry, and is most commonly produced via chemical routes, such as by the oxidation of toluene. Biologically produced benzaldehyde, whether by extraction of plant material or via microbial biotransformation, commands a substantial price advantage, and greater consumer acceptance. Methylotrophic yeast, such as Pichia pastoris, contain the enzyme alcohol oxidase (AOX), which, in the presence of alcohols other than methanol, are able to yield aldehydes as dead‐end products, for example, benzaldehyde from benzyl alcohol. In this work, we have determined that benzaldehyde, and not benzyl alcohol, is inhibitory to the transformation reaction by P. pastoris, prompting the development of a selection strategy for identifying sequestering polymers for use in a partitioning bioreactor that was based on the ratio of partition coefficients (PCs) for the two target molecules. Additionally, we have now confirmed for the first time, that the mechanism of solute uptake by amorphous polymers is via absorption, not adsorption. Finally, we have adopted a common strategy used for the production of heterologous proteins by P. pastoris, namely the use of a mixed methanol/glycerol feed for inducing the required AOX enzyme, while reducing the time required for high density biomass generation. All of these components were combined in a final experiment in which 10% of the polymer Kraton D1102K, whose PC ratio of benzaldehyde to benzyl alcohol was 14.9, was used to detoxify the biotransformation in a 5 L partitioning bioreactor, resulting in a 3.4‐fold increase in benzaldehyde produced (14.4 g vs. 4.2 g) relative to single phase operation, at more than double the volumetric productivity (97 mg L^?1 h^?1 vs. 41 mg L^?1 h^?1). Biotechnol. Bioeng. 2013; 110: 1098–1105. © 2012 Wiley Periodicals, Inc.     

Production of functional bacteriorhodopsin by an Escherichia coli cell‐free protein synthesis system supplemented with steroid detergent and lipid

Cell‐free expression has become a highly promising tool for the efficient production of membrane proteins. In this study, we used a dialysis‐based Escherichia coli cell‐free system for the production of a membrane protein actively integrated into liposomes. The membrane protein was the light‐driven proton pump bacteriorhodopsin, consisting of seven transmembrane α‐helices. The cell‐free expression system in the dialysis mode was supplemented with a combination of a detergent and a natural lipid, phosphatidylcholine from egg yolk, in only the reaction mixture. By examining a variety of detergents, we found that the combination of a steroid detergent (digitonin, cholate, or CHAPS) and egg phosphatidylcholine yielded a large amount (0.3–0.7 mg/mL reaction mixture) of the fully functional bacteriorhodopsin. We also analyzed the process of functional expression in our system. The synthesized polypeptide was well protected from aggregation by the detergent‐lipid mixed micelles and/or lipid disks, and was integrated into liposomes upon detergent removal by dialysis. This approach might be useful for the high yield production of functional membrane proteins.     

Detection of the mcr‐1 gene in colistin‐resistant Escherichia coli from retail meat in Japan

In this study, the presence of the mcr‐1 gene in Escherichia coli from retail meat in Japan was investigated. Nine E. coli isolates (eight from chickens and one from pork) carried the mcr‐1 gene on the plasmid. In six isolates from domestic chickens, mcr‐1 was located on the IncI2 plasmid, which is approximately 60 kb in size. In the remaining three isolates from imported chicken and pork, mcr‐1 was located on the IncX4 plasmid (30 kb).

     

Protonation states of active‐site lysines of penicillin‐binding protein 6 from Escherichia coli and the mechanistic implications

The protonation states of the two active‐site lysines (Lys69 and Lys235) of PBP 6 of Escherichia coli were explored to understand the active site chemistry of this enzyme. Each lysine was individually mutated to cysteine, and the resultant two mutant proteins were purified to homogeneity. Each protein was denatured, and its cysteine was chemically modified to produce an S‐aminoethylated cysteine (γ‐thialysine) residue. Following renaturation, the evaluation of the kinetics of the dd ‐carboxypeptidase activity of PBP 6 as a function of pH was found consistent with one lysine in its free‐base (Lys69) and the other in the protonated state (Lys235) for optimal catalysis. The experimental estimates for their pK_a values were compared with the pK_a values calculated computationally, using molecular‐dynamics simulations and a thermodynamic cycle. Study of the γ‐thialysine69 showed that lysine at position 69 influenced the basic limb of catalysis, consistent with the fact that the two lysine side chains are in proximity to each other in the active site. Based on these observations, a reaction sequence for PBP 6 is proposed, wherein protonated Lys235 serves as the electrostatic substrate anchor and Lys69 as the conduit for protons in the course of the acylation and deacylation half‐reactions. Proteins 2014; 82:1348–1358. © 2013 Wiley Periodicals, Inc.     

Crystal structures of ligand‐bound octaprenyl pyrophosphate synthase from Escherichia coli reveal the catalytic and chain‐length determining mechanisms

Octaprenyl pyrophosphate synthase (OPPs) catalyzes consecutive condensation reactions of one allylic substrate farnesyl pyrophosphate (FPP) and five homoallylic substrate isopentenyl pyrophosphate (IPP) molecules to form a C₄₀ long‐chain product OPP, which serves as a side chain of ubiquinone and menaquinone. OPPs belongs to the trans‐prenyltransferase class of proteins. The structures of OPPs from Escherichia coli were solved in the apo‐form as well as in complexes with IPP and a FPP thio‐analog, FsPP, at resolutions of 2.2–2.6 Å, and revealed the detailed interactions between the ligands and enzyme. At the bottom of the active‐site tunnel, M123 and M135 act in concert to form a wall which determines the final chain length. These results represent the first ligand‐bound crystal structures of a long‐chain trans‐prenyltransferase and provide new information on the mechanisms of catalysis and product chain elongation. Proteins 2015; 83:37–45. © 2014 Wiley Periodicals, Inc.     

Synthesis of Optically Active Diols by Escherichia coli Transformant Cells that Express the Glycerol Dehydrogenase Gene of Hansenula polymorphaDL‐1

Chiral alcohols are useful as intermediates for the synthesis of drugs. In the production of chiral alcohols, microbial enzymes are promising since high optical purity is required. Under these conditions, the reaction by resting cells is more convenient and inexpensive than by an enzyme reaction. Chiral 1,2‐propanediol and 2,3‐butanediol were obtained using cells expressing the enzyme which demonstrated high stereospecificity. By means of recombinant cells expressing the glycerol dehydrogenase of Hansenula polymorpha DL‐1, the medium was enriched with (S)‐1,2‐propanediol (98 % enantiometric excess, e.e.) during a 24‐h incubation, whereas the (R)‐form was removed from 100 mM of the racemate (R:S = 1:1). For an asymmetric reduction, a recombinant was constructed which also expressed the glucose dehydrogenase gene of Bacillus subtilis origin as an NADH reproducer. In the resting cell reaction, the pH control at 7.5 promoted the conversion from ketone to alcohol. (2R,3R)‐2,3‐butanediol (e.e. > 99.9 %; 308 mM) was produced from 800 mM acetoin (R:S = 3:4); (R)‐1,2‐propanediol (e.e. > 99.9 %; 550 mM) from 800 mM acetol in a 33‐h incubation by the addition of glucose and ketone with pH control. In this reaction, (S)‐forms of both 2,3‐butanediol and 1,2‐propanediol were not produced. The pH control and feeding of the substrates were uncomplicated. The production process of the chiral alcohol by the recombinants which expresses glycerol dehydrogenase proved convenient.     

Development and evaluation of efficient recombinant Escherichia coli strains for the production of 3‐hydroxypropionic acid from glycerol

3‐Hydroxypropionic acid (3‐HP) is a commercially valuable chemical with the potential to be a key building block for deriving many industrially important chemicals. However, its biological production has not been well documented. Our previous study demonstrated the feasibility of producing 3‐HP from glycerol using the recombinant Escherichia coli SH254 expressing glycerol dehydratase (DhaB) and aldehyde dehydrogenase (AldH), and reported that an “imbalance between the two enzymes” and the “instability of the first enzyme DhaB” were the major factors limiting 3‐HP production. In this study, the efficiency of the recombinant strain(s) was improved by expressing DhaB and AldH in two compatible isopropyl‐thio‐β‐galactoside (IPTG) inducible plasmids along with glycerol dehydratase reactivase (GDR). The expression levels of the two proteins were measured. It was found that the changes in protein expression were associated with their enzymatic activity and balance. While cloning an alternate aldehyde dehydrogenase (ALDH), α‐ketoglutaric semialdehyde dehydrogenase (KGSADH), instead of AldH, the recombinant E. coli SH‐BGK1 showed the highest level of 3‐HP production (2.8 g/L) under shake‐flask conditions. When an aerobic fed‐batch process was carried out under bioreactor conditions at pH 7.0, the recombinant SH‐BGK1 produced 38.7 g 3‐HP/L with an average yield of 35%. This article reports the highest level of 3‐HP production from glycerol thus far. Biotechnol. Bioeng. 2009; 104: 729–739 © 2009 Wiley Periodicals, Inc.