Production of enantiopure styrene oxide by recombinant Escherichia coli synthesizing a two-component styrene monooxygenase

A whole cell biocatalytic process was developed to enable the efficient oxidation of styrene to chiral (S)-styrene oxide with an enantiomeric excess better than 99%. Recombinant Escherichia coli cells were employed to express the genes styAB encoding the styrene monooxygenase of Pseudomonas sp. strain VLB120 from an expression plasmid utilizing the alk regulatory system of P. oleovorans GPo1. The strains reached specific activities of up to 70 U* (g cell dry weight)(-1) in shake-flask experiments with glucose as the carbon source. An efficient two-liquid phase fed-batch process was established for the production of (S)-styrene oxide with hexadecane as an apolar carrier solvent and a nutrient feed consisting of glucose, magnesium sulfate, and yeast extract. Engineering of the phase fraction and the composition of organic phase and feed led to a 2-L scale process with maximal volumetric productivities of 2.2 g (S)-styrene oxide per liter liquid volume per hour. This optimized process was based completely on defined medium and used bis(2-ethylhexyl)phthalate as the apolar carrier solvent, which together with substrate and inducer consisted of 50% of the total liquid volume. Using this system, we were able to produce per liter liquid volume 11 g of enantiopure (S)-styrene oxide in 10 h.     

Medium chain length alkane solvent-cell transfer rates in two-liquid phase, pseudomonas oleovorans cultures

The oxidation of medium chain length alkanes and alkenes (C6 to C12) by Pseudomonas oleovorans and related, biocatalytically active recombinant organisms, in two-liquid phase cultures can be used for the biochemical production of several interesting fine chemicals. The volumetric productivities that can be attained in two-liquid phase systems can be, in contrast to aqueous fermentations, limited by the transport of substrates from an apolar phase to the cells residing in the aqueous phase and by toxic effects of apolar solvents on microbial cells. We have assessed the impact of these possible limitations on attainable productivities in two-liquid phase fermentations operated with mcl-alkanes. Pseudomonas oleovorans grows well in two-liquid phase media containing a bulk n-octane phase as the sole carbon source. However, cells are also damaged, typically resulting in a cell lysis rate of about 0.08 to 0. 10 h-1. These rates could be lowered by 50 to 70% to 0.03 h-1 and substrate yields increased from 0.55 to 0.85 g g-1 by diluting octane in non-metabolizable long-chain hydrocarbon solvents. Transfer rates of medium chain length (mcl) alkanes from the apolar phase to the cells were determined by following growth and the rate at which carbon-containing metabolites accumulated in the different phases of the cultures. mcl-Alkane solvent-cell transfer rates of at least 79, 64, and 18 mmol per liter of aqueous medium per hour were determined for n-heptane, n-octane, and n-decane, respectively. Rates of up to 30 mmol L-1 h-1 were observed under octane-limiting conditions in systems where the apolar substrate was dissolved to concentrations below 3% (v/v) in hexadecene. Based on low power input experiments, we estimated the maximum obtainable mass transfer rates in large scale processes to be in the range of 13 mmol L-1 h-1 for decane and higher than 45 mmol L-1 h-1 for octane and heptane. The results indicate that high solvent to cell mass transfer rates and minimized cell damage will enable high production rates in two-liquid phase bioprocesses, justifying ongoing efforts to attain high densities of catalytically, highly active cells in such systems. Copyright 1998 John Wiley & Sons, Inc.     

Production of (S)-styrene oxide by recombinant Pichia pastoris containing epoxide hydrolase from Rhodotorula glutinis

A recombinant yeast Pichia pastoris carrying the gene encoding epoxide hydrolase (EH) of Rhodotorula glutinis was constructed and used for producing (S)-styrene oxide by enantioselective hydrolysis of racemic mixtures of styrene oxides. The EH gene was obtained by PCR amplification of cDNA of R. glutinis and integrated into the chromosomal DNA of P. pastoris to express EH under the control of AOX promoter. The recombinant yeast has a high hydrolytic activity toward (R)-styrene oxide as 358 nmol min⁻¹ (mg cell)⁻¹, which is about 10-fold higher than that of wild type R. glutinis. When kinetic resolution was conducted by the recombinant yeast at a high initial epoxides concentration of 526 mM that constitutes an epoxide–water two-liquid phase, chiral (S)-styrene oxide with an enantiomeric excess (e.e.) higher than 98% was obtained as 36% yield (theoretical, 50%) at 16 h.     

Biosynthesis of synthons in two-liquid-phase media

The Pseudomonas oleovorans alkane hydroxylase and xylene oxygenase from Pseudomonas putida are versatile mono-oxygenases for stereo- and regioselective oxidation of aliphatic and aromatic hydrocarbons. Pseudomonas oleovorans and alkanol dehydrogenase deficient mutants of Pseudomonas have previously been used to produce alkanols from various alkanes and optically active epoxides from alkenes. Similarly, P. putida strains have been used to produce aromatic alcohols, aromatic acids, and optically active styrene oxides. A limitation in the use of Pseudomonas strains for bioconversions is that these strains can degrade some of the products formed. To counter this problem, we have constructed Escherichia coli recombinants, which contain the alk genes from the OCT plasmid of P. oleovorans [E. coli HB101 (pGEc47)] and the xylMA genes from the TOL plasmid of P. putida mt-2 [E. coli HB101 (pGB63)], encoding alkane hydroxylase and xylene oxygenase, respectively. Escherichia coli HB101 (pGEc47) was used to produce octanoic acid from n-octane and E. coli HB101 (pBG63) was put to use for the oxidation of styrene to styrene oxide in two-liquid phase biocatalysis at high cell densities. The alk(+) recombinant strain E. coli HB101 (pGEc47) was grown to 40 g/L cell dry mass in the presence of n-octane, which was converted to octanoic acid by the alkane oxidation system, the product accumulating in the aqueous phase. The xyl(+) recombinant E. coli HB101 (pBG63) was grown to a cell density of 26 g/L cell dry mass in the presence of around 7% (v/v) n-dodecane, which contained 2% (v/v) styrene. The recombinant E. coli (xyl(+)) converted styrene to (S)-(+)-styrene oxide at high enantiomeric excess (94% ee) and this compound partitioned almost exclusively into the organic phase. Using these high-cell-density two-liquid-phase cultures, the products accumulated rapidly, yielding high concentrations of products (50 mM octanoic acid and 90 mM styrene oxide) in the respective phases. (c) 1996 John Wiley & Sons, Inc.     

Enantioconvergent production of (R)-1-phenyl-1,2-ethanediol from styrene oxide by combining the Solanum tuberosum and an evolved Agrobacterium radiobacter AD1 epoxide hydrolases

Soluble epoxide hydrolase (EH) from the potato Solanum tuberosum and an evolved EH of the bacterium Agrobacterium radiobacter AD1, EchA-I219F, were purified for the enantioconvergent hydrolysis of racemic styrene oxide into the single product (R)-1-phenyl-1,2-ethanediol, which is an important intermediate for pharmaceuticals. EchA-I219F has enhanced enantioselectivity (enantiomeric ratio of 91 based on products) for converting (R)-styrene oxide to (R)-1-phenyl-1,2-ethanediol (2.0 +/- 0.2 micromol/min/mg), and the potato EH converts (S)-styrene oxide primarily to the same enantiomer, (R)-1-phenyl-1,2-ethanediol (22 +/- 1 micromol/min/mg), with an enantiomeric ratio of 40 +/- 17 (based on substrates). By mixing these two purified enzymes, inexpensive racemic styrene oxide (5 mM) was converted at 100% yield to 98% enantiomeric excess (R)-1-phenyl-1,2-ethanediol at 4.7 +/- 0.7 micromol/min/mg. Hence, at least 99% of substrate is converted into a single stereospecific product at a rapid rate.     

Production host selection for asymmetric styrene epoxidation: Escherichia coli vs. solvent-tolerant Pseudomonas

Selection of the ideal microbe is crucial for whole-cell biotransformations, especially if the target reaction intensively interacts with host cell functions. Asymmetric styrene epoxidation is an example of a reaction which is strongly dependent on the host cell owing to its requirement for efficient cofactor regeneration and stable expression of the styrene monooxygenase genes styAB. On the other hand, styrene epoxidation affects the whole-cell biocatalyst, because it involves toxic substrate and products besides the burden of additional (recombinant) enzyme synthesis. With the aim to compare two fundamentally different strain engineering strategies, asymmetric styrene epoxidation by StyAB was investigated using the engineered wild-type strain Pseudomonas sp. strain VLB120ΔC, a styrene oxide isomerase (StyC) knockout strain able to accumulate (S)-styrene oxide, and recombinant E. coli JM101 carrying styAB on the plasmid pSPZ10. Their performance was analyzed during fed-batch cultivation in two-liquid phase biotransformations with respect to specific activity, volumetric productivity, product titer, tolerance of toxic substrate and products, by-product formation, and product yield on glucose. Thereby, Pseudomonas sp. strain VLB120ΔC proved its great potential by tolerating high styrene oxide concentrations and by the absence of by-product formation. The E. coli-based catalyst, however, showed higher specific activities and better yields on glucose. The results not only show the importance but also the complexity of host cell selection and engineering. Finding the optimal strain engineering strategy requires profound understanding of bioprocess and biocatalyst operation. In this respect, a possible negative influence of solvent tolerance on yield and activity is discussed.     

Production of styrene oxide from styrene by a recombinant Escherichia coli with enhanced AcrAB-TolC efflux pump level in an aqueous-organic solvent two-phase system

ABSTRACT

The AcrAB-TolC efflux pump is involved in the organic solvent tolerance of Escherichia coli. Most E. coli strains are highly sensitive to organic solvents such as n-hexane and cyclohexane. Here, a recombinant E. coli transformed with an expression plasmid containing acrAB and tolC became tolerant to n-hexane and cyclohexane. The levels of AcrA, AcrB, and TolC in the recombinant increased by 3- to 5-fold compared to those in the control strain without the plasmid for acrAB or tolC. To investigate the usability of the recombinant as a biocatalyst in an aqueous-organic solvent two-phase system, we further introduced xylMA xylene monooxygenase genes from Pseudomonas putida mt-2 into the recombinant and examined the production of styrene oxide from styrene. The resulting recombinant produced 1.8 mg and 1.0 mg styrene oxide mL^?1 of medium in a medium overlaid with a 25% volume of n-hexane and cyclohexane containing 10% (wt vol^?1) styrene, respectively.     

Biocatalysis of nitro substituted styrene oxides by non-conventional yeasts

Yeast strains (410) from more than 45 different genera were screened for the enantioselective hydrolysis of nitro substituted styrene oxides. These strains included 262 yeasts with known epoxides hydrolase activity for various other epoxides. Epoxide hydrolase activity for p-nitrostyrene oxide (pNSO) (177 strains) and m-nitrostyrene oxide (mNSO) (148 strains) was widespread in the yeasts, while activity for o-nitrostyrene oxide (oNSO) was less ubiquitous (22 strains). The strains that displayed enantioselectivity in the hydrolysis of one or more of the nitro substituted styrene oxides (35 strains) were also screened against styrene oxide (SO). Rhodosporidium toruloides UOFS Y-0471 displayed the highest enantioselectivity for pNSO (ee 55%, yield 35%) while Rhodotorula glutinis UOFS Y-0653 displayed the highest enantioselectivity for mNSO (ee >98%, yield 29%), oNSO (ee 39%, yield 19%) and SO (ee >98%, yield 19%). (R)-Styrene oxide was preferentially hydrolysed to the corresponding (R)-diol with retention of configuration at the stereogenic centre. In the case of the nitro substituted styrene oxides the absolute configurations of the remaining epoxides and the formed diols were not established.     

Bacterial influence on partitioning rate during the biodegradation of styrene in a biphasic aqueous-organic system

The degradation by a consortium of slightly-halophile marine bacteria of styrene initially dissolved in silicone oil was monitored in batch reactors stirred at 75, 125 and 500 rpm, respectively. In the 75 and 125 rpm cases, the styrene biodegradation rate was higher than the rate of spontaneous partitioning of styrene from the oil to the water, determined under abiotic conditions. Abiotic transfer tests carried out after biodegradation runs revealed that bacterial activity had resulted in a significant increase in the rate of styrene partitioning between the two liquid phases. Even though bacterial adsorption was noticeable at the oil-water interface, this effect appeared to be due to the release by the bacteria of chemicals in the aqueous phase. Similarity with observations made with Triton X-100 suggested that the chemicals released may have been biosurfactants or solubilizing agents.     

Use of the two-liquid phase concept to exploit kinetically controlled multistep biocatalysis

The two-liquid phase concept was used to develop a whole cell biocatalytic system for the efficient multistep oxidation of pseudocumene to 3,4-dimethylbenzaldehyde. Recombinant Escherichia coli cells were employed to express the Pseudomonas putida genes encoding xylene monooxygenase, which catalyzes the multistep oxygenation of one methyl group of toluene and xylenes to corresponding alcohols, aldehydes, and acids. A fed-batch based two-liquid phase bioconversion was established with bis(2-ethylhexyl)- phthalate as organic carrier solvent and a phase ratio of 0.5; the product formation pattern, the impact of the nutrient feeding strategy, and the partitioning behavior of the reactants were studied. On the basis of the favorable conditions provided by the two-liquid phase system, engineering of the initial pseudocumene concentration allowed exploiting the complex kinetics of the multistep reaction for the exclusive production of 3,4-dimethyl- benzaldehyde. Further oxidation of the product to 3,4-dimethylbenzoic acid could be inhibited by suitable concentrations of pseudocumene or 3,4-dimethylbenzyl alcohol. The optimized biotransformation setup includes a completely defined medium with high iron content and a nutrient feeding strategy that avoids severe glucose limitation as well as high inhibitory glucose levels. Using such a system on a 2-liter scale, we were able to produce, within 14.5 h, 30 g of 3,4-dimethylbenzaldehyde as predominant reactant in the organic phase and reached a maximal productivity of 1.6 g per liter liquid volume per hour. The present study implicates that the two-liquid phase concept is an efficient tool to exploit the kinetics of multistep biotransformations in general.     

Enantioselective hydrolysis of racemic styrene oxide by epoxide hydrolase of<Emphasis Type="Italic">Rhodosporidium kratochvilovae</Emphasis> SYU-08

Enantioselective hydrolysis for the production of chiral styrene oxide was investigated using the epoxide hydrolase activity of a newly isolatedRhodosporidium kratochvilovae SYU-08. The effects of reaction prameters—buffer type, pH, temperature, initial substrate concentrations, phenyl-1,2-ethanediol concentrations on hydrolysis rate, and enantioselectivity—were analyzed. Optically active (S)-styrene oxide with an enantiomeric excess higher than 99 % was obtained from its racemate with a yield of 38 % (theoretically 50% maximum yield) from an initial concentration of 80 mM.     

High-performance liquid chromatographic assay of cytosolic glutathione S-transferase activity with styrene oxide

A high-performance liquid chromatographic (HPLC) assay for measuring cytosolic glutathione S-transferase activity with styrene oxide is described. After incubating lung or liver cytosol with reduced glutathione and styrene oxide, unreacted styrene oxide is extracted into ethyl acetate. An aliquot of the aqueous phase is evaporated to dryness and reconstituted in the mobile phase for HPLC analysis. The two glutathione conjugates of styrene oxide [S-(1-phenyl-2-hydroxyethyl)glutathione and S-(2-phenyl-2-hydroxyethyl)glutathione] are separated in less than 10 min; quantitation of transferase activity is based on the comparison of the UV absorbance of the two conjugates at 254 nm with synthetic conjugate standards. As little as 1 nmole of either conjugate can be quantitated with good precision. This assay has advantages over previously published methods for measuring styrene oxide glutathione S-transferase activity as it does not depend on the use of relatively unstable and expensive radiolabelled substrates.     

Carbon metabolism and product inhibition determine the epoxidation efficiency of solvent-tolerant Pseudomonas sp. strain VLB120DeltaC

Utilization of solvent tolerant bacteria as biocatalysts has been suggested to enable or improve bioprocesses for the production of toxic compounds. Here, we studied the relevance of solvent (product) tolerance and inhibition, carbon metabolism, and the stability of biocatalytic activity in such a bioprocess. Styrene degrading Pseudomonas sp. strain VLB120 is shown to be solvent tolerant and was engineered to produce enantiopure (S)-styrene oxide from styrene. Whereas glucose as sole source for carbon and energy allowed efficient styrene epoxidation at rates up to 97 micromol/min/(g cell dry weight), citrate was found to repress epoxidation by the engineered Pseudomonas sp. strain VLB120DeltaC emphasizing that carbon source selection and control is critical. In comparison to recombinant Escherichia coli, the VLB120DeltaC-strain tolerated higher toxic product levels but showed less stable activities during fed-batch cultivation in a two-liquid phase system. Epoxidation activities of the VLB120DeltaC-strain decreased at product concentrations above 130 mM in the organic phase. During continuous two-liquid phase cultivations at organic-phase product concentrations of up to 85 mM, the VLB120DeltaC-strain showed stable activities and, as compared to recombinant E. coli, a more efficient glucose metabolism resulting in a 22% higher volumetric productivity. Kinetic analyses indicated that activities were limited by the styrene concentration and not by other factors such as NADH availability or catabolite repression. In conclusion, the stability of activity of the solvent tolerant VLB120DeltaC-strain can be considered critical at elevated toxic product levels, whereas the efficient carbon and energy metabolism of this Pseudomonas strain augurs well for productive continuous processing.     

Biodegradability and toxicity of styrene in the anaerobic digestion process

Start-up and operation of an Upflow Anaerobic Sludge Blanket (UASB) reactor fed with an industrial effluent from a polymer synthesis plant containing 6 mg styrene l^–1 was unstable. In batch assays with 200 mg styrene l^–1, 74% of styrene was degraded at a rate of 7 ml methane g^–1 volatile suspended solids.day, without a lag phase. The toxicity limit (IC₅₀) of styrene was 1.4 mM for the acetoclastic activity, 0.45 and 1.6 mM for the methanogenic activity in the presence of 30 mM of propionate and ethanol respectively. Instability of UASB operation was attributed to other compounds such as acrylates or detergents present in the industrial effluent.     

The interaction of an epoxide with yeast alcohol dehydrogenase: evidence for binding and the modification of two active site cysteines by styrene oxide.

Yeast alcohol dehydrogenase is inactivated and alkylated by styrene oxide in a single exponential kinetic process. The concentration dependence of half-times for inactivation indicates the formation of an enzyme inhibitor complex, KI = 2.5 times 10(-2) M at pH 8.0. Reduced nicotinamide adenine dinucleotide (NADH), at a concentration of 3 times 10(-4) M where Kd congruent to 1 times 10(-5) M, has a small effect on kinetic parameters for inactivation. Although benzyl alcohol and acetamide-NADH increase the KI for styrene oxide in a manner consistent with their dissociation constants, substrate also increases the rate of inactivation at high styrene oxide concentrations. The reciprocal of half-times for inactivation, extrapolated to infinite styrene oxide concentration, increases with pH between 7.6 and 9.0, pK congruent to 8.5. The stoichiometry of alkylation by [3H]styrene oxide is 2.2 mol of reagent incorporated/mol of subunit, and is accompanied by the loss of 1.9 mol of sulfhydryl/mol of subunit; prior alkylation with iodoacetamide reduces the stoichiometry to 0.88:1, and increases the rate of labeling. Tryptic digests of enzyme modified with [14C]iodoacetamide or [3H]styrene oxide produce two major peptides which cochromatograph, indicating that styrene oxide and iodoacetamide modify the same cysteine residues. Previous investigators have reported that iodoacetate, iodoacetamide, and butyl isocyanate alkylate either of two reactive cysteines of yeast alcohol dehydrogenase; both cysteines cannot be modified simultaneously [Belke et al. (1974), Biochemistry 13, 3418]. The inactivation of enzyme by p-chloromercuribenzoate (PCMB) is reported here to be accompanied by the incorporation of 2.3 mol of PCMB/mol of enzyme subunits, in analogy with styrene oxide; the planarity of the alkylating agent appears to be an important factor in determining the stoichiometry of labeling.     

Induction of sister chromatid exchanges by styrene and its presumed metabolite styrene oxide in the presence of rat liver homogenate

Styrene and its metabolite styrene oxide were tested for their ability to induce sister chromatid exchanges (SCE) in CHO cells. Styrene oxide appeared to be a potent inducer of SCE. Styrene itself did not increase the number of SCE per metaphase, even in the presence of a metabolic activation system. The metabolic activation system decreased the SCE induction caused by styrene oxide. Induction of SCE by styrene in the presence of metabolic activation occurred when cyclohexene oxide was used as an inhibitor of the enzyme epoxide hydrase.     

Mass transfer limitation as a tool to enhance the enantiomeric excess in the enzymatic synthesis of chiral cyanohydrins

The enantioselective synthesis of cyanohydrins catalyzed by R-hydroxynitrile lyase in an aqueous-organic liquid two-phase system using, mass transfer limitation to enhance enantiomeric excess at 5°C and pH 5.5 is described. Benzaldehyde, a good substrate, and cinnamaldehyde, a notoriously difficult substrate, were used as model substrates and compared in order to establish the mass transfer limitation concept in a two-liquid phase system, where the non-enzymatic-racemic reaction competes. Enzyme concentration and phase volume ratio between organic and buffer phase were geared to one another to enhance the enantiomeric excess for each substrate. In both cases, after optimization, excellent chemical conversion (>99% on a 60 mmol scale), high throughput and high enantiomeric excess (benzaldehyde >99% and cinnamaldehyde >96%) were achieved.     

Solid support membrane‐aerated catalytic biofilm reactor for the continuous synthesis of (S)‐styrene oxide at gram scale

Catalytic biofilms minimize reactant toxicity and maximize biocatalyst stability in selective transformations of chemicals to value‐added products in continuous processes. The scaling up of such catalytic biofilm processes is challenging, due to fluidic and biological parameters affording a special reactor design affecting process performance. A solid support membrane‐aerated biofilm reactor was optimized and scaled‐up to yield gram amounts of (S)‐styrene oxide, a toxic and instable high value chemical synthon. A sintered stainless steel membrane unit was identified as an optimal choice as biofilm substratum and for high oxygen mass transfer. A stable expanded polytetrafluoroethylene (ePTFE) membrane was best suited for in situ substrate delivery and product extraction. For the verification of scalability, catalytic biofilms of Pseudomonas sp. strain VLB120ΔC produced (S)‐styrene oxide to an average concentration of 390 mM in the organic phase per day (equivalent to 24.4 g L_aq^–1 day^–1). This productivity was gained by efficiently using the catalyst with an excellent product yield on biomass of 13.6 g_product g_biomass^–1. This product yield on biomass is in the order of magnitude reported for other continuous systems based on artificially immobilized biocatalysts and is fulfilling the minimum requirements for industrial biocatalytic processes. Overall, 46 g of (S)‐styrene oxide were produced and isolated (purity: 99%; enantiomeric excess [ee]: >99.8%. yield: 30%). The productivity is in a similar range as in comparable small‐scale biofilm reactors highlighting the large potential of this methodology for continuous bioprocessing of bulk chemicals and biofuels.     

Epoxidation of styrene by hemoglobin and myoglobin. Transfer of oxidizing equivalents to the protein surface

Methemoglobin and metmyoglobin catalyze the H2O2-dependent oxidation of styrene to styrene oxide and benzaldehyde. The formation of styrene oxide requires molecular oxygen as well as H2O2 but does not, as shown by inhibitor studies, involve the superoxide or hydroxyl radicals. Approximately 38, 67, and 78% of the oxygen in styrene oxide derives from 18O2 in the reactions catalyzed, respectively, by bovine hemoglobin, sperm whale myoglobin, and equine heart myoglobin, whereas 70, 55, and 35% of the oxygen can be shown to be derived from [18O]H2O2. However, a larger fraction of the epoxide oxygen than suggested by the labeling data (perhaps all) derives from molecular oxygen rather than H2O2 because the hemoproteins produce molecular oxygen from the peroxide. The epoxidation of styrene by methemoglobin gives equal amounts of the R and S enantiomers and, as shown by studies with trans-[1-2H]styrene, proceeds with partial (33%) loss of the olefin stereochemistry. The results are rationalized by H2O2-dependent formation of a protein radical that combines with molecular oxygen to give a protein-peroxy radical that oxidizes styrene.