Continuous production of L-phenylalanine by Rhodotorula glutinis immobilized cells using a column reactor

Studies have been conducted on L-phenylalanine (L-Phe) production and phenylalanine ammonia lyase (PAL) stabilization in the presence of several optimum effectors and reducing agents under bioconversion of transcinnamic acid (t-CA) conditions during repeated batch operations. L-Phe production was maximized and reuseability of PAL catalyst was extended to eight consecutive cycles (repeated batches) in the presence of optimum effectors (glutamic acid, polyethylene glycol and glycerol), thioglycolic acid and sparging with nitrogen gas. These best optimum bioconversion conditions desensitize the PAL catalyst to substantially elevated higher substrate t-CA concentrations and inhibit inactivation of PAL enzyme over longer reaction periods compared to the control. The fed batch mode operation of bioconversion of total t-CA (300 mM) to L-Phe was superior (65.2%, conversion), comparing with conventional batch and repeated batch (58.4%, conversion) operations after 120 h. Gamma irradiation process was employed to polymerize and crosslink polyvinyl alcohol (PVA) with N,N'-methylene-bisacrylamide (BIS) agent. The use of immobilized PAL biocatalyst containing cells in PVA-BIS copolymer gel carrier produced by radiation polymerization is obviously advantageous with regards to the yield of L-Phe which was increased in average 1.2-fold when compare to those obtained with free cells during optimum bioconversion process. When comparing the magnitudes of gamma irradiation effects on immobilized entrapped yeast cells in PVA-BIS copolymer gel carrier using scanning electron microscopy it was show that yeast cells were protected and capable to overcome these conditions and had normal shape and other features as free (unirradiated) intact yeast cells. Optimum conditions for continuous production of L-Phe by PVA-BIS copolymer carrier entrapped yeast cells in a packed bed column reactor in recycle fed-batch mode were investigated. Under these optimum conditions L-Phe accumulated to concentration 240.1 mM represts a total conversion yield of 80% (w/w) from (300 mM) t-CA after 84 h of reaction process, which was higher than that obtained after 120 h of reaction, 65.2% (w/w) from (300 mM) t-CA with free cells in fed-batch mode. The results also demonstrated that during about 4 weeks of repeated continuous recycle fed batch mode experiments (using immobilized cells in packed bed reactor), the final production of L-Phe concentrations decreased gradually in eight consecutive runs with no sign of breakage or disintegration of the carrier gel beads.     

Selective production of L-aspartic acid and L-phenylalanine by coupling reactions of aspartase and aminotransferase in Escherichia coli

With L-aspartate (L-Asp) as the amino donor, L-phenylalanine (L-Phe) can be prepared from phenylpyruvate (PPA) via an amination reaction mediated by aminotransferase (encoded by aspC). On the other hand, L-Asp can be produced by an aspartase (encoded by aspA) -catalyzed reaction using fumaric acid as substrate. To overproduce aspartase in Escherichia coli, the aspA gene was cloned and overexpressed 180 times over the wild-type level. The use of AspA-overproducing E. coli strain for L-Asp production exhibited an 83% conversion, approaching to the theoretical yield, whereas the wild-type strain obtained scarcely L-Asp. Furthermore, the recombinant strain overproducing both AspA and AspC was able to produce L-Asp and L-Phe simultaneously by using fumaric acid and PPA as substrates. As a result, the conversion yields obtained for L-Asp and L-Phe were 78% and 85%, respectively. In sharp contrast, the wild-type strain attained a conversion of L-Phe less than 15% and an undetectable level of L-Asp. This result illustrates a potential and attractive process to yield both L-Asp and L-Phe by coupling AspA and AspC. A further study on the repeated use of the recombinant strain immobilized with calcium alginate showed that after eight batch runs L-Asp conversion maintained roughly constant (around 75%), whereas L-Phe conversion dropped to 65% from 81%. This result indicates the stability of AspA being superior to AspC.     

Exogenous application of L-phenylalanine and ferulic acid enhance phenylalanine ammonia lyase activity and accumulation of phenolic acids in pea (Pisum sativum) to offer protection against Erysiphe pisi

Phenylalanine ammonia lyase (PAL) activity was measured using HPLC in pea leaves following exogenous application of L-phenylalanine and ferulic acid. Treatment with different concentrations (50, 100, 150 ppm) of L-phenylalanine caused increased activity of PAL activity in comparison to control. In pea leaves treated with 50 ppm L-phenylalanine, maximum PAL activity was observed after 72 h of treatment. Application of ferulic acid first reduced PAL activity at lower concentration (50 ppm) but it further increased at higher concentrations of the compound (100 and 150 ppm) in pea leaves compared to control. Minimum PAL activity was 0.19 nM cinnamic acid/min/g fresh wt after 24 h at 50 ppm and then increased with time. Treatment with both compounds significantly increased the accumulation of phenolic acids and salicylic acid and reduced conidial germination of Erysiphe pisi on pea leaves. They were equally effective at 100 and 150 ppm in reducing conidial germination. Conidial germination on L-phenylalanine-treated leaves was 26% after 24 h and that on ferulic acid treated leaves 34% compared to control (46%). Foliar application of different concentrations of L-phenylalanine increased the level of ferulic acid in the leaves of pea plants. Maximum enzyme activity in terms of the accumulation of cinnamic acid (79.3 and 83.5 μg/g fresh wt) was observed following the application of L-phenylalanine after 24 and 48 h respectively. At 50 ppm, cinnamic acid accumulation in pea leaves was 35.6 and 39.4 μg/g fresh wt and 74.3 and 86.5 μg/g fresh wt at 100 ppm.     

A modern view of phenylalanine ammonia lyase.

Phenylalanine ammonia lyase (PAL; E.C.4.3.1.5), which catalyses the biotransformation of L-phenylalanine to trans-cinnamic acid and ammonia, was first described in 1961 by Koukol and Conn. Since its discovery, much knowledge has been gathered with reference to the enzyme's catabolic role in microorganisms and its importance in the phenyl propanoid pathway of plants. The 3-dimensional structure of the enzyme has been characterized using X-ray crystallography. This has led to a greater understanding of the mechanism of PAL-catalyzed reactions, including the discovery of a recently described cofactor, 3,5-dihydro-5-methyldiene-4H-imidazol-4-one. In the past 3 decades, PAL has gained considerable significance in several clinical, industrial, and biotechnological applications. The reversal of the normal physiological reaction can be effectively employed in the production of optically pure L-phenylalanine, which is a precursor of the noncalorific sweetener aspartame (L-phenylalanyl-L-aspartyl methyl ester). The enzyme's natural ability to break down L-phenylalanine makes PAL a reliable treatment for the genetic condition phenylketonuria. In this mini-review, we discuss prominent details relating to the physiological role of PAL, the mechanism of catalysis, methods of determination and purification, enzyme kinetics, and enzyme activity in nonaqueous media. Two topics of current study on PAL, molecular biology and crystal structure, are also discussed.     

Biochemical characterization of a prokaryotic phenylalanine ammonia lyase

The committed biosynthetic reaction to benzoyl-coenzyme A in the marine bacterium "Streptomyces maritimus" is carried out by the novel prokaryotic phenylalanine ammonia lyase (PAL) EncP, which converts the primary amino acid L-phenylalanine to trans-cinnamic acid. Recombinant EncP is specific for L-phenylalanine and shares many biochemical features with eukaryotic PALs, which are substantially larger proteins by approximately 200 amino acid residues.     

Enhanced conversion rate of L-phenylalanine by coupling reactions of aminotransferases and phosphoenolpyruvate carboxykinase in Escherichia coli K-12.

In Escherichia coli, aspartate aminotransferase (encoded by aspC) and aromatic amino acid aminotransferase (encoded by tyrB) share overlapping substrate specificity in the syntheses of aromatic amino acids. Through the transamination reactions catalyzed by AspC or TyrB, L-phenylalanine (L-Phe) can be produced from phenylpyruvate with aspartic acid as the amino donor. To modulate and enhance the production levels of proteins, both aspC and tyrB were subcloned into a runaway-replication vector. As a result, the specific activities of AspC and TyrB obtained showed 65-fold and 50-fold increases, respectively, compared with the wild-type level. Employing resting cells of AspC- and TyrB-overproducing E. coli K-12 strains for L-Phe productions resulted in molar conversion yields of 70% and 55%, respectively. With an additional introduction of phosphoenolpyruvate carboxykinase (encoded by pck) into the transamination reactions, the conversion yields were improved to 93% from 70% and to 75% from 55% in a relatively short time. These results account for more than an 8-fold increase in productivity, as compared to the previous report (Calton et al., 1985). In addition, a four-run reuse of the recombinant cells for L-Phe production gave a total yield of 91 g/L with a 93% conversion.     

Nitrogen recycling during phenylpropanoid metabolism in sweet potato tubers.

In the first step of the phenylpropanoid metabolic pathway, L-phenylalanine (L-Phe) is deaminated to form E-cinnamate, in a conversion catalyzed by phenylalanine ammonia-lyase (PAL; EC 4.3.1.5). The metabolic fate of the ammonium ion (NH4+) produced in this reaction was investigated in sweet potato (Ipomoea batatas) tuber discs. [15N]-Labeled substrates including L-Phe, in the presence or absence of specific enzyme inhibitors, were administered to sweet potato discs in light under aseptic conditions. 15N-Nuclear magnetic resonance spectroscopic analyses revealed that the 15NH4+ liberated during the PAL reaction is first incorporated into the amide nitrogen of L-glutamine (L-Gln) and then into L-glutamate (L-Glu). These results extend our previous observations in pine and potato that PAL-generated NH4+ is assimilated by the glutamine synthetase (GS; EC 6.3.1.2)/glutamate synthase (GOGAT; EC 1.4.1.13) pathway, with the NH4+ so formed ultimately being recycled back to L-Phe via L-Glu as aminoreceptor and donor.     

Integrated L-phenylalanine separation in an E. coli fed-batch process: from laboratory to pilot scale

Pilot-scale reactive-extraction technology for fully integrated L-phenylalanine (L-Phe) separation in Escherichia coli fed-batch fermentations was investigated in order to prevent an inhibition of microbial L-Phe production by-product accumulation. An optimal reactive-extraction system, consisting of an organic kerosene phase with the cation-selective carrier DEHPA (di-2-ethylhexyl phosphonic acid) and an aqueous stripping phase including sulphuric acid, was found particularly efficient. Using this system with two membrane contactors, mass-transfer coefficients of up to 288 x 10(-7) cm s(-1) for the aqueous/organic and 77 x 10(-7) cm s(-1) for the organic/stripping phase were derived from experimental data using a simple modelling approach. Concentration factors higher than 4 were achieved in the stripping phase as compared to the aqueous donor phase. Reactive extraction enabled a 98% cation portion of L-Phe in the stripping phase, leading to final product purity higher than 99% after L-Phe precipitation. A doubling of L-Phe/glucose yield was observed when kerosene/DEHPA was added to the fermentation solution in the bioreactor to experimentally simulate a fully integrated L-Phe separation process.     

Enhanced pilot-scale fed-batch L-phenylalanine production with recombinant <Emphasis Type="Italic">Escherichia</Emphasis><Emphasis Type="Italic"> coli</Emphasis> by fully integrated reactive extraction

A fully integrated process for the microbial production and recovery of the aromatic amino acid L-phenylalanine is presented. Using a recombinant L-tyrosine (L-Tyr) auxotrophic Escherichia coli production strain, a fed-batch fermentation process was developed in a 20-l-scale bioreactor. Concentrations of glucose and L-Tyr were closed-loop-controlled in a fed-batch process. After achieving final L-phenylalanine (L-Phe) titres >30 g/l the process strategy was scaled up to 300-l pilot scale. In technical scale fermentation L-phenylalanine was continuously recovered via a fully integrated reactive extraction system achieving a maximum extraction rate of 110 g/h (final purity >99%). It was thus possible to increase L-Phe/glucose selectivity from 15 mol% without to 20.3 mol% with integrated product separation.     

Alterations in Taxol production in plant cell culture via manipulation of the phenylalanine ammonia lyase pathway

One approach to increasing secondary metabolite production in plant cell culture is to manipulate metabolic pathways to utilize more resources toward production of one desired compound or class of compounds, such as diverting carbon flux from competing secondary pathways. Since phenylalanine provides both the phenylisoserine side chain and the benzoyl moiety at C-2 of Taxol, we speculated that blockage of the phenylpropanoid pathway might divert phenylalanine into Taxol biosynthesis. We used specific enzyme inhibitors to target the first enzyme in the phenylpropanoid pathway, phenylalanine ammonia lyase (PAL), the critical control point for conversion of L-phenylalanine to trans-cinnamic acid. Cinnamic acid acted quickly in reducing PAL activity by 40-50%, without affecting total protein levels, but it generally inhibited the taxane pathway, reducing Taxol by 90% of control levels. Of the taxanes produced, 13-acetyl-9-dihydro-baccatin III and 9-dihydrobaccatin III doubled as a percentage of total taxanes in C93AD and CO93P cells treated with 0.20 and 0.25 mM cinnamic acid, when all other taxanes were lowered. The PAL inhibitor alpha-aminooxyacetic acid (AOA) almost entirely shut down Taxol production at both 0.5 and 1.5 mM, whereas L-alpha-aminooxy-beta-phenylpropionic acid (AOPP) had the opposite effect, slightly enhancing Taxol production at 1 microM but having no effect at 10 microM. The discrepancy in the effectiveness of AOA and AOPP and the lack of effect with addition of phenylalanine or benzoic acid derivatives further indicates that the impact of cinnamic acid on Taxol is related not to its effect on PAL but rather to a specific effect on the taxane pathway. On the basis of these results, a less direct route for inhibiting the phenylpropanoid pathway may be required to avoid unwanted side effects and potentially enhance Taxol production.     

Purification and stabilization of phenylalanine ammonia lyase fromSporidiobolus pararoseus

The purification of phenylalanine ammonia-lyase (PAL) from S. pararoseus is described: PAL is recovered from cellular extracts by acid precipitation of contaminating proteins, nucleic acids and carotenoids; concentrated by ultrafiltration and purified by ion exchange chromatography in DEAE-Sephacel, with 80% yield and 32.6 fold purification. Elimination of carotenoids and stabilization with glycerol are introduced in the methodology to increase stability and purification yield.     

Ammonia lyases and aminomutases as biocatalysts for the synthesis of α-amino and β-amino acids

Ammonia lyases catalyse the reversible addition of ammonia to cinnamic acid (1: R=H) and p-hydroxycinnamic (1: R=OH) to generate L-phenylalanine (2: R=H) and L-tyrosine (2: R=OH) respectively (Figure 1a). Both phenylalanine ammonia lyase (PAL) and tyrosine ammonia lyase (TAL) are widely distributed in plants, fungi and prokaryotes. Recently there has been interest in the use of these enzymes for the synthesis of a broader range of L-arylalanines. Aminomutases catalyse a related reaction, namely the interconversion of α-amino acids to β-amino acids (Figure 1b). In the case of L-phenylalanine, this reaction is catalysed by phenylalanine aminomutase (PAM) and proceeds stereospecifically via the intermediate cinnamic acid to generate β-Phe 3. Ammonia lyases and aminomutases are related in sequence and structure and share the same active site cofactor 4-methylideneimidazole-5-one (MIO). There is currently interest in the possibility of using these biocatalysts to prepare a wide range of enantiomerically pure l-configured α-amino and β-amino acids. Recent reviews have focused on the mechanism of these MIO containing enzymes. The aim of this review is to review recent progress in the application of ammonia lyase and aminomutase enzymes to prepare enantiomerically pure α-amino and β-amino acids.     

Response of Winter Wheat to Cold: Production of Phenolic Compounds and L-Phenylalanine Ammonia Lyase Activity

The formation of soluble and polymeric (lignin) phenolic compounds, activity of L-phenylalanine ammonia lyase (PAL, EC 4.3.1.5), and content of free L-phenylalanine during cold hardening of winter wheat plants (Triticum aestivum L.) were studied. Cold treatment increased accumulation of soluble phenolic compounds in leaves while not affecting the content of lignin. The opposite was observed in tillering nodes. The activity of PAL was lower than in control plants in both tissues, and the content of free L-phenylalanine in tissues increased.     

甘油对粒毛盘菌DP5胞外多酚积累的影响

【目的】探明以甘油为碳源促进粒毛盘菌DP5积累多酚的可能原因。【方法】对碳源种类、甘油浓度、曲酸、抑制剂和前体等对多酚产量和生物量的影响进行分析。【结果】以甘油为碳源,能显著提高粒毛盘菌胞外多酚产量。甘油浓度为20 g/L时,胞外多酚产量最高,达到0.664 g GAE/L,并在发酵液中检测到曲酸,其含量为0.25 g/L。向以蔗糖为碳源的发酵液添加曲酸,胞外多酚含量从0.209 g GAE/L提高至0.376 g GAE/L。以甘油为碳源的发酵液中,酚氧化酶活性较低。粒毛盘菌DP5通过莽草酸途径和聚酮途径合成多酚,甘油有利于莽草酸途径和聚酮途径前体物质的合成。【结论】粒毛盘菌以甘油为碳源合成出曲酸,曲酸抑制多酚向黑色素的转化;甘油促进多酚前体的合成,从而提高了粒毛盘菌胞外多酚的积累量。     

Response of winter wheat to cold: production of phenolic compounds and L-phenylalanine ammonia-lyase activity

The formation of soluble and polymeric (lignin) phenolic compounds, activity of L-phenylalanine ammonia lyase (PAL, EC 4.3.1.5), and content of free L-phenylalanine during cold hardening of winter wheat plants (Triticum aestivum L.) were studied. Cold treatment increased accumulation of soluble phenolic compounds in leaves while not affecting the content of lignin. The opposite was observed in tillering nodes. The activity of PAL was lower than in control plants in both tissues, and the content of free L-phenylalanine in tissues increased.     

Effect of glycerol,polyethylene glycol and glutaraldehyde on stability of phenylalanine ammonia-lyase activity in yeast

Summary The polyhydric alcohols, glycerol and sorbitol, significantly increased the rate ofl-phenylalanine production from trans-cinnamic acid using whole cells ofRhodotorula rubra. Chloride ions and oxygen prevented the stimulatory effect of the polyhydric alcohols. Furthermore, the severe inhibition, of the biotransformation by high trans-cinnamic acid concentrations was alleviated in the presence of glycerol, and sorbitol. The rate of conversion could be manipulated still further, even with high trnas-cinnamic acid concentrations, by elevating the reaction pH to, 12 in the presence of polyhydric alcohol. When cells were also treated first with glutaradehyde (0.1% v/v) and then polyethylene glycol (15% v/v), although neither compound stimulated the actual rate of bioconversion, the reaction was markedly stabilised and gave a 73% yield after 28 days of continuous operation.     

Phenylalanine ammonia lyase production by gamma irradiated and analog-resistant mutants of Rhodotorula glutinis

Mutants resistant to phenylalanine analogs (L-tyrosine, p-fluoro-D, L-phenylalanine (PFP) and trans-cinnamic acid) were isolated from a wild type strain of Rhodotorula glutinis A-97 by mutagenic treatment with gamma radiation and screened for phenylalanine ammonia lyase (PAL) production. One such mutant, gammaT11 (resistant to L-tyrosine), exhibited four times the PAL activity of the parent wild strain A-97. Mutant isolate gammaTFP5.6 which was selected as L-tyrosine and PFP resistant isolate, produced inducible PAL activity at levels 5.94-fold higher than the wild-type A-97 and 2.66-fold higher than its parent mutant isolate gammaT5 which was resistant to L-tyrosine. The mutant isolate gammaTC5d which was resistant to L-tyrosine and trans-cinnamic acid, exhibited 3.48 and 1.56-fold increase in PAL activity compared to the parent wild strain A-97 and its parent mutant isolate gammaT5, respectively. Different media have been examined for the induction of PAL.     

Extractive bioconversion of 2-phenylethanol from L-phenylalanine by Saccharomyces cerevisiae

The bioconversion of L-phenylalanine (L-Phe) to 2-phenylethanol (PEA) by the yeast Saccharomyces cerevisiae is limited by the toxicity of the product. PEA extraction by a separate organic phase in the fermenter is the ideal in situ product recovery (ISPR) technique to enhance productivity. Oleic acid was chosen as organic phase for two-phase fed-batch cultures, although it interfered to some extent with yeast viability. There was a synergistic inhibitory impact toward S. cerevisiae in the presence of PEA, and therefore a maximal PEA concentration in the aqueous phase of only 2.1 g/L was achieved, compared to 3.8 g/L for a normal fed-batch culture. However, the overall PEA concentration in the fermenter was increased to 12.6 g/L, because the PEA concentration in the oleic phase attained a value of 24 g/L. Thus, an average volumetric PEA production rate of 0.26 g L(-1) h(-1) and a maximal volumetric PEA production rate of 0.47 g L(-1) h(-1) were achieved in the two-phase fed-batch culture. As ethanol inhibition had to be avoided, the production rates were limited by the intrinsic oxidative capacity of S. cerevisiae. In addition, the high viscosity of the two-phase system lowered the k(l)a, and therefore also the productivity. Thus, if a specific ISPR technique is planned, it consequently has to be remembered that the productivity of this bioconversion process is also quickly limited by the k(l)a of the fermenter at high cell densities.     

反应条件下苯丙氨酸解氨酶的活力稳定性

在苯丙氨酸解氨酶(PAL)的作用下由肉桂酸和氨合成L-苯丙氨酸(L-Phe)是酶法合成该氨基酸的重要途径,国外已利用该途径进行L-苯丙氨酸的工业生产,但是该过程仍存在着转化率低和酶活力稳定性差的问题。为解决这些问题,有必要在现有基础上开展提高酶活力稳定性的研究。     

Novel stabilization of phenylalanine ammonia-lyase catalyst during bioconversion of trans-cinnamic acid to l-phenylalanine

Summary Production of l-phenylalanine from trans-cinnamic acid using isolate SPA10 cells was reduced to 26% of that observed initially when cells were reacted a second time with fresh substrate mixture. The stability (reuseability) of Phenylalanine Ammonia-Lyase (PAL) containing cells was significantly influenced by both the trans-cinnamate concentration and initial reaction pH. Using 2% t-cinnamate, l-phenylalanine production was 7-fold greater after 3 successive runs at pH 9.0 than at the optimum of pH 10.2. Cells reacted in the presence of 5% t-cinnamate were relatively unstable. Permeabilising agents, such as toluene and xylene, stimulated l-phenylalanine production but also enhanced instability of the catalyst. Several effectors were shown to stimulate the initial rate of the PAL bioconversion, but only sorbitol, alginate, glutaraldehyde, polyethylene glycol and glycerol conferred any significant degree of stability. Sparging of cultures and bioreactors with various gases revealed that oxygen enhanced PAL inactivation, CO₂ had little effect and nitrogen conferred remarkable stability on PAL activity for several weeks in culture medium. The presence of chloride ions (from HCl) and aeration of substrate mixtures resulted in poor reuseability of catalyst. A combination of H₂SO₄ substitution for HCl and N₂-sparging resulted in excellent initial conversions and good catalyst stability at 26°C but less at 30°C. The inclusion of 1.5 M sorbitol in reaction mixtures maintained PAL stability over several successive incubations.