Continuous production of l-phenylalanine from acetamidocinnamic acid using co-immobilized cells of Corynebacterium sp. and Paracoccus denitrificans

In order to produce l-phenylalanine efficiently from acetamidocinnamic acid with immobilized microbial cells, a two-step enzyme reaction using the acetamidocinnamate amidohydrolase activity of Corynebacterium sp. C-23 cells and the aminotransferase activity of Paracoccus denitrificans pFPr-1 cells was investigated. It was found that the useage of co-immobilized Corynebacterium sp. and P. denitrificans cells with κ-carrageenan was superior to that of the mixture of immobilized Corynebacterium sp. cells and immobilized P. denitrificans cells. When the space velocity was 0.06 h⁻¹ at 30°C, 147 mml-phenylalanine were produced with a 98% conversion ratio from acetamidocinnamic acid. The half-life of the l-phenylalanine-forming activity of the column was calculated to be ≈ 14 days at 30°C.     

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     

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     

l-phenylalanine production by double auxotrophic multianalogue-resistant mutant ofArthrobacter globiformis

Tryptophan-plus-tyrosine double auxotrophic mutants resistant to fluorophenylalanine (PFP) and β-2-thienylalanine (TA) were isolated from a biotin-requiring glutamate-producingArthrobacter globiformis. The mutants were found to producel-phenylalanine in mineral salts medium. Further improvement ofl-phenylalanine production was achieved by isolation of mutants resistant to 5-methyltryptophan (MT) and 3-nitrotyrosine (NT) from a double auxotrophic PFP^r and TA^r mutant. Under optimal cultural condition one mutant yielded 9.6g phenylalanine per L medium in flask culture. Enzymic activity of regulatory enzymes (deoxy-d-arabino-heptulosonate-7-phosphate synthase, chorismate mutase and prephenate dehydratase) were observed in the wild type, double auxotroph and double-auxotrophic multianalogue-resistant mutant.     

The fermentation process for l-phenylalanine production using an auxotrophic regulatory mutant of Escherichia coli

Summary A process for l-phenylalanine production was studied using a tyrosine auxotrophic regulatory mutant of Escherichia coli, resistant to both -2-thienyl-dl-alanine and p-fluoro-dl-phenylalanine. Fermentations were carried out in a 30-1 fermentor with intermittent feeding of glucose plus phosphate. The mutant accumulated l-phenylalanine in the fermentation broth up to 15 g/l at pH 7.0 and 33°C. Column chromatography on a strong cation exchanger was employed as the most effective step in the purification of l-phenyl-alanine from the broth. This step brought about 4-fold concentration of the product with 96% recovery.     

Pilot-scale production of l-phenylalanine from d-glucose

Effects of inoculum size and total sugar content on both l-phenylalanine productivity and titre have been investigated using a tyrosine auxotrophic regulatory mutant of Escherichia coli. Fermentations were carried out in a 500 litre pilot fermenter with intermittent feeding of d-glucose plus phosphate. It was found that the productivity was not greatly affected by inoculum size. However, the l-phenylalanine titre was significantly affected by total sugar content. Relatively high productivities of up to 0.35–0.40 g l-phenylalanine l^?1 h^?1 have been achieved at l-phenylalanine titres of 14–15 g l^?1.     

L-Phenylalanine formation from acetamidocinnamic acid by newly isolated bacteria

Summary Bacteria with the ability to form L-phenylalanine from acetamidocinnamic acid were isolated from several soils. Among them, strain no. S-7 and strain no. N-7 were identified as Alcaligenus faecalis S-7 and Bacillus sphaericus N-7, respectively. The L-phenylalanine-forming enzyme systems in both bacteria were found to be inducible and intracellular. With intact cells of both bacteria and 40 mg/ml as wet base, 10 mg/ml acetamidocinnamic acid was utilized, and 7.7 mg/ml L-phenylalanine in a molar yield of 94% was produced after 72h incubation. The pathway of L-phenylalanine formation is considered to take the following course: acetamidocinnamic acid is deacetylated to -amino cinnamic acid; this is spontaneously changed to phenylpyruvic acid, and L-phenylalanine is formed by transamination.     

Enzymatic production of the lignin precursor trans-[U-14C]cinnamic acid from l-[U-14C]phenylalanine using l-phenylalanine ammonia-lyase

An enzymatic method using phenylalanine ammonia-lyase (l-phenylalanine ammonia-lyase, EC 4.3.1.5) for the rapid conversion of l-[U-¹⁴C]phenylalanine to the deaminated lignin precursor trans-[U-¹⁴C]cinnamic acid is described. The method produces an experimentally useful ¹⁴C-labelled deaminated lignin precursor unavailable from radiochemical supply companies.     

酶法转化L-谷氨酸生产a-酮戊二酸

利用L-谷氨酸氧化酶(LGOX),对酶法转化L-谷氨酸生产α-酮戊二酸(α-KG)的工艺条件进行了研究。首先对野生菌链霉菌Streptomyces sp.FMME066进行亚硝基胍诱变,获得一株遗传性状稳定的突变株Streptomyces sp.FMME067;突变株在最优培养基(g/L):果糖10,蛋白胨7.5,KH2PO4 1,CaCl2 0.05条件下,LGOX酶活为0.14 U/mL。LGOX的生化特征为最适pH 8.5、温度35℃,Mn2+是激活剂。对LGOX转化L-谷氨酸生产α-KG的条件进行优化,在最优条件下转化24 h,α-KG产量为38.1 g/L,转化率为81.4%。研究结果为开发LGOX酶法转化生产α-KG的工业化奠定了坚实的基础。     

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 caffeic acid by koji from plant resources containing caffeoylquinic acid derivatives

The effect of a koji (Aspergillus awamori mut.) extract on the caffeoylquinic acid derivatives purified from sweetpotato (Ipomoea batatas L.) leaves was examined to develop the mass production of caffeic acid. A koji extract hydrolyzed the caffeoylquinic acid derivatives, chlorogenic acid, 3,4-di-O-caffeoylquinic acid, 3,5-di-O-caffeoylquinic acid, 4,5-di-O-caffeoylquinic acid and 3,4,5-tri-O-caffeoylquinic acid, to caffeic acid. Furthermore, the koji extract also converted the major polyphenolic components from sweetpotato, burdock (Arctium lappa L.), and mugwort (Artemisia indica var. maximowiczii) leaves to caffeic acid. These results suggest that the production of caffeic acid from plant resources containing caffeoylquinic acid derivatives is possible.     

Enzymatic synthesis of formic acid from H2 and CO2 and production of hydrogen from formic acid

Whole cells of Alcaligenes eutrophus (as well as isolated P. oxalaticus formate dehydrogenase and A. eutrophus hydrogenase coupled via NAD(+) or methyl viologen) have been shown to produce H(2) from formic acid. Immobilization of the cells in kappacarrageenan gel greatly enhances their stability at room temperature. The rate of hydrogen production catalyzed by immobilized A. eutrophus has been studied as a function of the concentrations of the cells and formate and also pH. An inhibition by high concentrations of formate has been found. Immobilized cells were also capable of synthesizingformate from H(2) and bicarbonate. Yields of formate up to 30% have been obtained. The catalytic efficiency of immobilized A. eutrophus cells was compared with that of palladium adsorbed on activated carbon.     

Enzymatic synthesis of an orlistat intermediate using a mutant short-chain dehydrogenase from Novosphingobium aromaticivorans

Methyl (R)-3-hydroxytetradeconoate ((R)-MHOT) is a crucial chiral intermediate for the chemical synthesis of the anti-obesity drug, orlistat. Here, (R)-MHOT was prepared from methyl 3-oxotetradecanoate (MOT) using a mutant of the short-chain dehydrogenase/reductase (SDR) from Novosphingobium aromaticivorans (NaSDR). Mutant NaSDR-G145A/I199L had a 3.23 times greater k_cat value than that of wild type toward MOT. The conditions for the expression of recombinant NaSDR-G145A/I199L were further investigated and obtained cells were used for gram-scale preparation of (R)-MHOT with 50 g/L of MOT. The target product was extracted and confirmed by gas chromatography; the enantiomeric excess value of (R)-MHOT was 99.0 %. Molecular docking analysis was used to reveal the molecular basis of the enhanced catalytic activity of NaSDR-G145A/I199L; NaSDR-G145A/I199L presented a more effective docking posture than NaSDR. This is the first reported use of SDR for preparing (R)-MHOT via the reduction of MOT. Our study provides a foundation for greener preparation of (R)-MHOT.     

Enzymatic production of ceramide from sphingomyelin

Due to its major role in maintaining the water-retaining properties of the epidermis, ceramide is of great commercial potentials in cosmetic and pharmaceutical industries such as in hair and skin care products. Chemical synthesis of ceramide is a costly process, and developments of alternative cost-efficient production methods are of great interest. Present study was the first attempt to perform a systematic study on the production of ceramide through enzymatic hydrolysis of sphingomyelin. Sphingomyelin hydrolysis proved to be more efficient in two-phase (water:organic solvent) system than in one-phase (water-saturated organic solvent) system. Among the screened phospholipase C, the Clostridium perfringens enzyme had the highest sphingomyelin conversion rate, with very small temperature dependence. Addition of ethanol to the system markedly enhanced the rate of ceramide formation, and a mixture of ethylacetate:hexane (50:50) was the best organic solvent tested. Other factors such as (NH(4))(2)SO(4), NaCl and CaCl(2) were also tested but excluded for further consideration. On the basis of the initial experiments, the reaction system was optimized using response surface methodology including five factors (enzyme amount, water amount, ethanol amount, reaction time and the hexane ratio of organic solvent). Water content and enzyme amount was shown to have the most significant influence on the hydrolysis reaction in the fitted quadratic model. The efficiency of sphingomyelin hydrolysis was dramatically improved through system evaluation and optimization, with the optimal conditions at 75 min reaction time, 3 Uml(-1) enzyme amount, 6% water amount, 1.8% ethanol amount and 46% hexane in ethylacetate.     

Enhanced biosynthesis of chiral phenyllactic acid from l-phenylalanine through a new whole-cell biocatalyst

Bioprocess and Biosystems Engineering - Phenyllactic acid (PLA) is a high-value compound, which was usually produced by lactic acid bacteria (LAB) as biocatalysts and glucose or phenylpyruvic acid...     

l-Ribulose production from l-arabinose by an l-arabinose isomerase mutant from Geobacillus thermodenitrificans

Geobacillus thermodenitrificans, with a double-site mutation in L: -arabinose isomerase, produced 95 g L-: ribulose l(-1 ) from 500 g L: -arabinose l(-1) under optimum conditions of pH 8, 70 degrees C, and 10 units enzyme ml(-1) with a conversion yield of 19% over 2 h. The half-lives of the mutated enzyme at 70 and 75 degrees C were 35 and 4.5 h, respectively.