Isolation of l-phenylalanine dehydrogenase from Rhodococcus sp. M4 and its application for the production of l-phenylalanine

Summary l-Phenylalanine dehydrogenase [l-phenylalanine: NAD⁺-oxidoreductase (deaminating)] of Rhodococcus sp. strain M4 was studied emphasizing its application for the production of l-phenylalanine. A high enzyme level (30,000 U·l^-1, 25–30 U·mg^-1 in the crude extract) could be reached during aerob degradation of l-phenylalanine (10 g·l^-1) under optimized growth coditions. A partial purification of the intracellular enzyme by liquid-liquid extraction, and DEAE-cellulose led to a specific activity of more than 1300 U·mg^-1. The continuous production of l-phenylalanine in an enzyme-membrane-reactor for 350h resulted in a space-time yield of 456 g·l^-1·d^-1 with a mean substrate conversion of 95%. Consumption of phenylalanine dehydrogenase was 1,500 U·kg Phe^-1.Abbreviations BSA bovine serum albumine - pheDH l-phenylalanine dehydrogenase - phepyr phenylpyruvate - OD optical density - FDH formate dehydrogenase     

Enzymatic production of l-phenylalanine from the racemic mixture of d,l-phenyllactate

Summary The production of l-phenylalanine from the racemate d,l-phenyllactate in an enzyme membrane reactor has been examined. In a first step the racemate is dehydrogenated to the prochiral intermediate phenylpyruvate by the enzymes d-and l-hydroxyisocaproate dehydrogenase. In a second step phenylpyruvate is reductively aminated to l-phenylalanine by l-phenylalanine dehydrogenase. Both steps are dependent on coenzyme, the first one requires NAD, the second one NADH in stoichiometric amounts; in this way the coenzyme is regenerated and only required catalytically. The coenzyme is covalently bound to polyethylene glyco-20 000 and can thus be retained in the reactor analogously to the three enzymes. In order to optimize the continuous production of l-phenylalanine from d,l-phenyllactate, models of the reaction kinetics and of the reactor system have been set up. By means of the reactor model, we can calculate the optimum ratio of the three enzymes, the optimum coenzyme concentration and the optimum phenylpyruvate concentration in the feed.In this process, at a substrate concentration of 50 mM d,l-phenyllactate we reached a spacetime-yield of 28 g l-Phe/(l*d).Abbreviations PEG polyethylene glycol - d-HicDH d-hydroxyisocaproate dehydrogenase - l-HicDH l-hydroxyisocaproate dehydrogenase - PheDH l-phenylalanine dehydrogenase - V _max maximum velocity - K _M Michaelis-Menten constant - K _l inhibition constant - R₁ reaction rate of the d-HicDH forward reaction - R₂ reaction rate of the d-HicDH reverse reaction - R₃ reaction rate of the l-HicDH forward reaction - R₄ reaction rate of the l-HicDH reverse reaction - R₅ reaction rate of the PheDH forward reaction - R₆ reaction rate of the PheDH reverse reaction - d-PLac d-phenyllactate - l-PLac l-phenyllactate - PPy phenylpyruvate - l-Phe l-phenylalanine - NH₄ ammonium - residence time     

Production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans containing aminotransferase activity

Summary To establish an efficient production method for l-phenylalanine, the production of l-phenylalanine from phenylpyruvate by Paracoccus denitrificans pFPr-1 containing aminotransferase activity was investigated. By using intact cells, 0.74M l-phenylalanine was produced from 0.8M phenylpyruvate (conversion yield, 92.5%). Moreover, by using immobilized cells with -carrageenan, when the space velocity was 0.1 h^-1 at 30°C, 0.135 M l-phenylalanine was produced from 0.15 M phenylpyruvate (conversion yield, 90%). The half-life of the l-phenylalanine-forming activity of the column was estimated to be about 30 days at 30°C.     

Purification,characterization and regulation of a monomeric l-phenylalanine dehydrogenase from the facultative methylotroph Nocardia sp. 239

In Nocardia sp. 239 d-phenylalanine is converted into l-phenylalanine by an inducible amino acid racemase. The further catabolism of this amino acid involves an NAD-dependent l-phenylalanine dehydrogenase. This enzyme was detected only in cells grown on l- or d-phenylalanine and in batch cultures highest activities were obtained at relatively low amino acid concentrations in the medium. The presence of additional carbon- or nitrogen sources invariably resulted in decreased enzyme levels. From experiments with phenylalanine-limited continuous cultures it appeared that the rate of synthesis of the enzyme increased with increasing growth rates. The regulation of phenylalanine dehydrogenase synthesis was studied in more detail during growth of the organism on mixtures of methanol and l-phenylalanine. Highest rates of l-phenylalanine dehydrogenase production were observed with increasing ratios of l-phenylalanine/methanol in the feed of chemostat cultures. Characteristic properties of the enzyme were investigated following its (partial) purification from l- and d-phenylalanine-grown cells. This resulted in the isolation of enzymes with identical properties. The native enzyme had a molecular weight of 42 000 and consisted of a single subunit; it showed activity with l-phenylalanine, phenylpyruvate, 4-hydroxyphenyl-pyruvate, indole-3-pyruvate and -ketoisocaproate, but not with imidazolepyruvate, d-phenylalanine and other l-amino acids tested. Maximum activities with phenylpyruvate (310 mol min^-1 mg^-1 of purified protein) were observed at pH 10 and 53°C. Sorbitol and glycerol stabilized the enzyme.Abbreviations RuMP ribulose monophosphate - HPS hexulose-6-phosphate synthase - HPT hexulose-6-phosphate isomerase - FPLC fast protein liquid chromatography     

Isolation and characterization of acetamidocinnamate acylase,a new enzyme suitable for production of l-phenylalanine

Summary A new acylase catalyzing the deacetylation of acetamidocinnamic acid (ACA) was found in strains of Brevibacterium sp. Such strains could be isolated from soil samples by their ability to grow on ACA as well as on l-phenylalanine. A 110-fold enrichment of the enzyme with an over-all yield of 48% was obtained in 4 steps resulting in an electrophoretically pure preparation of 28.6 U·mg^-1. Important enzymological data concerning the application of the enzyme are: K _M (ACA) 0.45 mM, pH-optimum 7.5, heat stability up to 52°C, molecular weight of 50.000 Dalton, two subunits. Deacetylation of ACA resulted in phenylpyruvate via the unstable enamine-imine derivative. Coupling the acylase with l-phenylalanine dehydrogenase proved to be an alternative route for l-phenylalanine production avoiding substrate inhibition by phenylpyruvate and its instability. The substrate specifity of ACA-acylase revealed that the enzyme probably acts as a dipeptidase in its biological function.Abbreviations ACA acetamidocinnamate, acetamidocinnamic acid - FPLC fast protein liquid chromatography - pheDH l-Phenylalanine dehydrogenase - HicDH Hydroxyisocaproate dehydrogenase - OD optical density - BSA bovine serum albumin - FDH formate dehydrogenase Dedicated to Professor Dr. H. J. Rehm on the occasion of his 60th birthday     

Biotransformation of phenylpyruvic acid to l-phenylalanine using a strain of Pseudomonas fluorescens ATCC 11250 with high transaminase activity

The rate of l-phenylalanine production from phenylpyruvic acid by whole cells of Pseudomonas fluorescens strain ATCC 11250 was greater than 3 g·l^-1 h^-1. Synthesis of transaminase was constitutive but activity was greatest in medium containing d- or l- phenylalanine as sole nitrogen source. Maximum conversion was observed at 34–40° C and at alkaline pH, with over six times initial rate of conversion at pH 12 than at pH 5. The optimum catalyst (cell) concentration was between 10–20 mg ml^-1 dry weight. The initial rate of conversion was directly proportional to phenylpyruvate concentration, up to 4%, but the conversion yield steadily decreased between 2% and 4% substrate concentration. The rate of conversion, as expected, increased as the concentration of glutamate increased. Whole cells were still capable of over 63% conversion after 40 days providing reactions were supplemented with pyridoxal phosphate. Immobilisation of cells in calcium alginate and operation of a packed bed bioreactor enabled the continuous production of l-phenylalanine in concentrations greater than 15 g·l^-1 after 60 days operation.     

Isolation,identification and characterisation of a soil bacterium producing an enzyme with l-phenylalanine oxidase activity

A gram-positive, mesophilic bacterium which assimilated l-phenylalanine but which failed to utilise l-tyrosine was isolated from soil. The isolate, identified as a strain of Bacillus carotarum, converted l-phenylalanine to phenylpyruvate with the initial step catalysed by an inducible, intracellular enzyme which possessed l-phenylalanine oxidase activity. Phenylalanine oxidase has not been previously reported in Gram-positive bacteria, although there are a few examples of non-specific l-amino acid oxidases with activity towards l-phenylalanine. The isolate grew abundantly on complex media but failed to synthesise significant amounts of the enzyme in the absence of l-phenylalanine. The highest enzyme levels were achieved in a chemically defined minimal salts medium containing the amino acid at 10 g/l as the primary carbon and energy source.     

Phenylalanine and tyrosine metabolism in the facultative methylotroph Nocardia sp. 239

Nocardia sp. 239 is able to use l-tyrosine and both d- and l-phenylalanine as carbon-, energy- and nitrogen sources for growth. The catabolism of these compounds is by way of (4-hydroxy)phenylpyruvate and (4-hydroxy)-phenylacetate as intermediates and the pathways merge at the level of homogentisate. The conversion of the amino acids into (4-hydroxy)phenylpyruvate is catalyzed by an inducible NAD-dependent phenylalanine dehydrogenase and l-tyrosine aminotransferase, respectively. Incubation of the organism in media with l-phenylalanine plus phenyl-pyruvate resulted in diauxic growth, with phenylpyruvate used first. Phenylalanine dehydrogenase activity cold only be detected after depletion of phenylpyruvate, in the ensuing second growth phase on l-phenylalanine. During growth on phenylalanine plus methanol, low levels of phenylalanine dehydrogenase were detected and this resulted in simultaneous utilization of the two substrates. Following diepoxyoctane treatment, mutants of Nocardia sp. 239 affected in phenylalanine and phenylpyruvate degradation were isolated. Double mutants blocked in both phenylalanine dehydrogenase and phenylpyruvate decarboxylase completely failed to catabolize phenylalanine. The absence of these enzymes did not affect growth on tyrosine.Abbreviations RuMP ribulose monophosphate - EMS ethylmethanesulphonate - NTG N-methyl-N-nitro-N-nitrosoguanidine     

Biotransformation of alkyl and aryl carbonates: enantioselective hydrolysis

Summary N-(Benzyloxycarbonyl)-l-asparty-l-phenylalanine methyl ester, the precursor of the synthetic sweetener aspartame, was continuously synthesized in an immobilized thermolysin plug-flow type reactor at 25° C with the substrates (N-benzyloxycarbonyl-l-aspartic acid and l-phenylalanine methyl ester) dissolved in ethyl acetate. The immobilized enzyme was quite stable in ethyl acetate containing 2.5% 0.01 M 2-(N-morpholino)ethanesulphonic acid-NaOH buffer, pH 6.0, and 20 mM CaCl₂ with or without the substrate at 25° C. By periodically washing the column, we could conduct a continuous reaction for over 500 h with an average yield of 95% and a space velocity of 1.85 h ^–1.Offprint requests to: K. Nakanishi     

d-Ribulokinase from Klebsiella pneumoniae for continuous production of d-(−)-ribulose-5-phosphate

Summary The production of d-ribulose-5-phosphate in an enzyme membrane reactor was examined. Phosphoryl transfer from ATP to d-ribulose was catalysed by d-ribulokinase isolated from Klebsiella pneumoniae. For production of d-ribulose-5-phosphate the phosphoryl donor ATP was used either in stoichiometric or in catalytic amounts. Using catalytic amounts of ATP requires a second enzyme, e.g. pyruvate kinase, to regenerate ATP. The kinetic parameters for d-ribulokinase and pyruvate kinase were determined to calculate the performance of an enzyme membrane reactor for continuous production of d-ribulose-5-phosphate. Both processes operated for more than 200 h. Regardless of whether ATP was used in catalytic or stoichiometric amounts, about the same production parameters were determined. In continuous production space/time yields of 117 g (with ATP regeneration) and 103 g (without ATP regeneration) of d-ribulose-5-phosphate 1^–1 per day were reached.Offprint requests to: D. Gygax     

Clues from a halophilic methanogen about aromatic amino acid biosynthesis in archaebacteria

Extensive diversity in features of aromatic amino acid biosynthesis and regulation has become recognized in eubacteria, but almost nothing is known about the extent to which such diversity exists within the archaebacteria. Methanohalophilus mahii, a methylotrophic halophilic methanogen, was found to synthesize l-phenylalanine and l-tyrosine via phenylpyruvate and 4-hydroxyphenylpyruvate, respectively. Enzymes capable of using l-arogenate as substrate were not found. Prephenate dehydrogenase was highly sensitive to feedback inhibition by l-tyrosine and could utilize either NADP⁺ (preferred) or NAD⁺ as cosubstrate. Tyrosine-pathway dehydrogenases having the combination of narrow specificity for a cyclohexadienyl substrate but broad specificity for pyridine nucleotide cofactor have not been described before. The chorismate mutase enzyme found is a member of a class which is insensitive to allosteric control. The most noteworthy character state was prephenate dehydratase which proved to be subject to multimetabolite control by feedback inhibitor (l-phenylalanine) and allosteric activators (l-tyrosine, l-tryptophan, l-leucine, l-methionine and l-isoleucine). This interlock type of prephenate dehydratase, also known to be broadly distributed among the gram-positive lineage of the eubacteria, was previously shown to exist in the extreme halophile, Halobacterium vallismortis. The results are consistent with the conclusion based upon 16S rRNA analyses that Methanomicrobiales and the extreme halophiles cluster together.Abbreviation DAHP 3-deoxy-d-arabino-heptulosonate-7-phosphate     

Optimization of the solvent-tolerant <Emphasis Type="Italic">Pseudomonas putida</Emphasis> S12 as host for the production of <Emphasis Type="Italic">p</Emphasis>-coumarate from glucose

A Pseudomonas putida S12 strain was constructed that is able to convert glucose to p-coumarate via the central metabolite l-tyrosine. Efficient production was hampered by product degradation, limited cellular l-tyrosine availability, and formation of the by-product cinnamate via l-phenylalanine. The production host was optimized by inactivation of fcs, the gene encoding the first enzyme in the p-coumarate degradation pathway in P. putida, followed by construction of a phenylalanine-auxotrophic mutant. These steps resulted in a P. putida S12 strain that showed dramatically enhanced production characteristics with controlled l-phenylalanine feeding. During fed-batch cultivation, 10 mM (1.7 g l⁻¹) of p-coumarate was produced from glucose with a yield of 3.8 Cmol% and a molar ratio of p-coumarate to cinnamate of 85:1.     

Repeated batch and continuous syntheses of N-(benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester with immobilized thermolysin

Summary N-(Benzyloxycarbonyl)-l-phenylalanyl-l-phenylalanine methyl ester was synthesized from N-(benzyloxycarbonyl)-l-phenylalanine and l-phenylalanine methyl ester in an aqueous solution (aqueous phasic reaction), in an aqueous/organic biphasic system (biphasic reaction), and in an organic solvent (organic phasic reaction) with immobilized thermolysin. In the aqueous phasic reaction with thermolysin immobilized on Amberlite XAD-7, the whole product was trapped inside the support; extraction with ethyl acetate was needed to recover the product, and the equilibrium yield was low (about 65%). With the biphasic and organic phasic reactions with ethyl acetate as an organic solvent, the yield was around 95%. Because of the high yield and feasibility of operation, repeated batch and continuous reactions were done in the biphasic and organic phasic systems, respectively. The half-lives of the activity for the immobilized enzyme used in the biphasic system at 40°C by repeated batch operation and in a plug flow reactor fed with substrate dissolved in ethyl acetate at 40°C and 30°C were estimated to be about 200 h (67 batches), 420 h, and 1100 h, respectively.     

Biosynthesis of aromatic amino acids in Nocardia sp. 239: effects of amino acid analogues on growth and regulatory enzymes

Summary Further steps required for overproduction of aromatic amino acids by a mutant strain of Nocardia sp. 239 (Noc 87-13), unable to grow on l-phenylalanine as a sole carbon and energy source, were investigated. A number of analogues of the aromatic amino acids displayed severe inhibitory effects on the activities of regulatory enzymes in the biosynthetic pathway and growth of the organism in glucose mineral medium. l-Tryptophane analogues strongly inhibited 3-deoxy-d-arabino-heptulosonate 7-phosphate (DAHP) synthase activity. l-Tyrosine analogues especially inhibited DAHP synthase and chorismate mutase, whereas l-phenylalanine analogues strongly inhibited chorismate mutase and prephenate dehydratase activity. Addition of the aromatic amino acids and their precursors chorismate, 4-hydroxyphenylpyruvate, phenylpyruvate and anthranilate, to the medium counteracted the growth inhibitory effect of specific analogues. The data indicate that ortho- (OFP) and para-fluoro-d,l-phenylalanine (PFP), and l-phenylalanine amide, are the most suitable analogues for the isolation of feedback-inhibition-insensitive prephenate dehydratase mutants. Attempts to isolate l-tyrosine and l-trytophane auxotrophic mutants were only successful in the latter case, resulting in the selection of a stable anthranilate synthase-negative mutant (Noc 87-13-14). Uptake of aromatic amino acids in Nocardia sp. 239 most likely involves a common transport system. This necessitates the use of anthranilate, rather than l-trytophane, as a supplement during the isolation of l-tyrosine auxotrophic and OFP- and/or PFP-resistant mutant derivative strains of Noc 87-13-14. Offprint requests to: L. Dijkhuizen     

Liver-specific Induction of Ribosomal Protein Gene Expression by Amino Acid Starvation in Rats

An aminoacylase, inducibly formed in Bacillus thermoglucosidius grown with a synthetic compound, acetamidocinnamate, was used for enzymatic synthesis of l-phenylalanine from chloroacetamido-cinnamate. The reaction system consisted of the hydrolysis of chloroacetamidocinnamate to phenylpyruvate by aminoacylase and the reductive amination of phenylpyruvate to l-phenylalanine by phenylalanine dehydrogenase. The coenzyme NADH consumed was regenerated by a coupled reaction with formate dehydrogenase. Under optimum conditions for l-phenylalanine production, more than 98% of the initially added chloroacetamidocinnamate was converted effectively to l-phenylalanine without appreciable decomposition or racemization.     

Isobutene production by Rhodotorula minuta

Summary Isobutene production by Rhodotorula minuta IFO 1102 was studied. It was confirmed that the gas species produced by this yeast was isobutene from the result of analysis with a gas chromatograph mass spectrometer. Oxygen supply was essential to the microbial production of isobutene. The optimum pH was found to be approximately pH 6.0 and optimum temperature 25°–27° C. Isobutene production rate was maximal when l-leucine and l-phenylalanine in the medium were being uptaken by the yeast.The results from an investigation of the role of l-leucine and l-phenylalanine suggested that l-leucine was the precursor of isobutene and l-phenylalanine the inducer for the enzyme concerned with isobutene production.     

Introduction of a stress-responsive gene, yggG, enhances the yield of l-phenylalanine with decreased acetic acid production in a recombinant Escherichia coli

A stress-responsive gene, yggG, was introduced into an l-phenylalanine producer, Escherichia coli AJ12741. In shake-flask culture, the yggG-containing recombinant strain (named AJ12741/pHYGG) produced 6.4 g l-phenylalanine l⁻¹ at the end of culture and its yield on glucose was 0.16 g l-phenylalanine g glucose⁻¹. These values are much higher than those of the original AJ12741 strain (3.7 g l-phenylalanine l⁻¹ and 0.09 g l-phenylalanine g glucose⁻¹, respectively). On the other hand, AJ12741/pHYGG strain produced only 4.5 g acetic acid l⁻¹ and its yield on glucose was about a half of that of the AJ12741 culture. Analysis of gene expression revealed that in late growth phase, the expression levels of genes involved in acetic acid production (pta, ackA, and poxB) were relatively low in AJ12741/pHYGG cells. In particular, the level of poxB expression in AJ12741/pHYGG strains was one-seventh of that of the original strain. These results suggest that the formation of a bottleneck for acetic acid production brings about a metabolic flow favorable to l-phenylalanine synthesis in the recombinant strain over-expressing the yggG gene. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.     

Molecular breeding of a Brevibacterium lactofermentum l-phenylalanine producer using a cloned prephenate dehydratase gene

Summary The prephenate dehydratase gene was cloned from a mutant of Brevibacterium lactofermentum, AJ11957 that produced enzyme free from feedback inhibition. The recombinant plasmids pPH11 and pPH14 complemented a phenylalanine auxotroph of B. lactofermentum, A-15, provided the transformant with the desensitized enzyme and caused an increased level of the enzyme compared to that of a wild strain. Plasmid pPH14 was introduced into l-phenylalanine producers genetically induced from B. lactofermentum; MF358 and FP-1 excreting l-tyrosine and anthranilate, respectively, as by-products. Both transformants predominantly accumulated l-phenylalanine at the expense of by-product formation. Co-existence of pPH14 and pTAR16, a recombinant plasmid expressing desensitized 3-deoxy-d-arabino-hepturosonate-7-phosphate synthase had a marked effect on further improvement in l-phenylalanine productivity, accompanied by an increase in the corresponding enzyme activity. The parent, MF358, accumulating 5.5 g/l l-phenylalanine, 6.8 g/l l-tyrosine and 0.3 g/l anthranilate turned into a potent l-phenylalanine producer producing 18.2 g/l l-phenylalanine and 1.0 g/l l-tyrosine by-product. Offprint requests to: Hisao Ito     

From scratch to value: engineering <Emphasis Type="Italic">Escherichia coli</Emphasis> wild type cells to the production of <Emphasis Type="SmallCaps">l</Emphasis>-phenylalanine and other fine chemicals derived from chorismate

Recombinant strains of Escherichia coli K-12 for the production of the three aromatic amino acids (l-phenylalanine, l-tryptophan, l-tyrosine) have been constructed. The largest demand is for l-phenylalanine (l-Phe), as it can be used as a building block for the low-calorie sweetener, aspartame. Besides l-Phe, an increasing number of shikimic acid pathway intermediates can be produced from appropriate E. coli mutants with blocks in this pathway. The last common intermediate, chorismate, in E. coli not only serves for production of aromatic amino acids but can also be used for high-titer production of non-aromatic compounds, e.g., cyclohexadiene-transdiols. In an approach to diversity-oriented metabolic engineering (metabolic grafting), platform strains with increased flux through the general aromatic pathway were created by suitable gene deletions, additions, or rearrangements. Examples for rational strain constructions for l-phenylalanine and chorismate derivatives are given with emphasis on genetic engineering. As a result, l-phenylalanine producers are available, which were derived through several defined steps from E. coli K-12 wild type. These mutant strains showed l-phenylalanine titers of up to 38 g/l of l-phenylalanine (and up to 45.5 g/l using in situ product recovery). Likewise, two cyclohexadiene-transdiols could be recovered.     

Enzymic arrangement and allosteric regulation of the aromatic amino acid pathway in Neisseria gonorrhoeae

The pathway construction and allosteric regulation of phenylalanine and tyrosine biosynthesis was examined in Neisseria gonorrhoeae. A single 3-deoxy-d-arabino-heptulosonate 7-phosphate (DAHP) synthase enzyme sensitive to feedback inhibition by l-phenylalanine was found. Chorismate mutase and prephenate dehydratase appear to co-exist as catalytic components of a bifunctional enzyme, known to be present in related genera. The latter enzyme activities were both feedback inhibited by l-phenylalanine. Prephenate dehydratase was strongly activated by l-tyrosine. NAD⁺-linked prephenate dehydrogenase and arogenate dehydrogenase activities coeluted following ion-exchange chromatography, suggesting their identity as catalytic properties of a single broad-specificity cyclohexadienyl dehydrogenase. Each dehydrogenase activity was inhibited by 4-hydroxyphenylpyruvate, but not by l-tyrosine. Two aromatic aminotransferases were resolved, one preferring the l-phenylalanine:2-ketoglutarate substrate combination and the other preferring the l-tyrosine: 2-ketoglutarate substrate combination. Each aminotransferase was also able to transaminate prephenate. The overall picture of regulation is one in which l-tyrosine modulates l-phenylalanine synthesis via activation of prephenate dehydratase. l-Phenylalanine in turn regulates early-pathway flow through inhibition of DAHP synthase. The recent phylogenetic positioning of N. gonorrhoeae makes it a key reference organism for emerging interpretations about aromatic-pathway evolution.