苯丙氨酸解氨酶在催化反式苯丙烯酸向L-苯丙氨酸转化中新的稳定作用

用分离株SPA1O从反式苯丙烯酸生产的L-辈丙氨酸产量减少到起初观测的26%,起初的实验是生产菌与新鲜底物二次作用而进行的。含苯丙氨酸解氨酶细胞的稳定性(再用可能性)明显地受反式苯丙烯酸盐的浓度和最初反应pH的影响。使用2%的反式苯丙烯酸盐,L-苯丙氨酸的产量在PH9.0连续培养3次后比在最适pH10.2时的产量大7倍。细胞在存在有5%的反式苯丙烯酸盐时的作用相当不稳定。渗透因子,如甲苯、二甲苯能促进L-本丙氨酸的合成量,但同时也会增加苯丙氨酸解氨酶的不稳定性。有几种效应物表明对苯丙氨酸解氨酶的起始转化速率起促进作用,但只有山梨醇,藻酸盐,戌二醛,聚乙二醇和甘油使其具一定程度的稳定性。用不同的气体对培养物和生物反应器进行通气搅动,表明氧气促进苯丙氨酸解氨酶失活,二氧化碳有少的影响,而氮气使苯丙氨酸解氨酶活性在培养基中几个星期都具明显的稳定性。氯离子的存在(来自HCl)以及底物的通气搅动降低酶的再用可能性,用硫酸取代盐酸,并用氮气进行通气搅动,在26℃时,导致极好的最初转化速率,并且酶活相当稳定,但在30℃时效果差些,反应物中含有1.5M山梨醇使苯丙氨酸解氨酶活性稳定连续维持几个培养周期。     

几种效应物对苯丙氨酸解氨酶稳定性的影响

为了对利用苯丙氨酸解氨酶（PAL）转化肉桂酸生成L-苯丙氨酸的生物转化反应条件进行优化,采用添加效应物的方法来提高苯丙氨酸解氨酶的稳定性,通过单因素实验研究了谷氨酸钠,海藻酸钠,聚乙二醇,甘油,锌粉,氮气等对PAL的稳定性影响,通过正交实验和方差分析,确定在转化液中添加1.0g/L锌粉和20g/L谷氨酸钠作为效应物,L-苯丙氨酸积累浓度提高55%,该两种效应物对PAL的稳定性增加显著。     

粘红酵母产L-苯丙氨酸解氨酶发酵培养基的优化

通过单因子和正交试验 ,对粘红酵母产 L -苯丙氨酸解氨酶 ( PAL )培养基进行优化 ,L-苯丙氨酸的积累浓度可以从 2 .0 g/1 0 0 ml提高到 3 .3 g/1 0 0 ml,最终得到了 L-苯丙氨酸解氨酶发酵的最适条件     

L-苯丙氨酸生产方法及新菌株

<正> L-苯丙氨酸(以下缩写成苯丙氨酸)是合成天门冬苯丙氨酸甲苯酯的重要前体物。天门冬苯丙氨酸是近年来最受人们重视的一种二肽甜味剂。这样就关系到了苯丙氨酸生产工艺问题。在这一工艺程序中最重要的是如何经微生物反应由肉桂酸与氨苯供体生产苯丙氨酸。     

头状轮生链霉菌芳香族氨基酸合成途径的调节

对头状轮生链霉菌(Streptoverticillium caespitosus)芳香氨基酸合成途径的研究表明,第一个酶即3—脱氧—α—阿拉伯庚酮糖-7-磷酸(DAHP)合成酶无同工酶,不被L-色氨酸阻遏,比活力可被硝酸盐促进。L-色氨酸强烈地反馈抑制此酶,L-酪氨酸和L-苯丙氨酸无作用。L-色氨酸的反馈抑制对磷酸烯醇式丙酮酸(PEP)是非竞争性的,K_I为373μmol/L。酶对PEP和4-磷酸亦藓糖(E4P)的K_m值分别为50和100μmol/L。PEP和C0²⁺对酶有稳定作用。邻氨基苯甲酸合成酶活力可被1mmol/L L-色氨酸完全抑制,此酶也受L-色氨酸的阻遏,但是色氨酸支路上其余4个酶不被阻遏。分支酸变位酶被L-酪氨酸抑制。L-苯丙氨酸抑制预苯酸脱水酶,并更强地抑制预苯酸脱氢酶。     

毕赤酵母底盘芳香族氨基酸合成途径改造生产肉桂酸及对香豆酸*

目的:改造毕赤酵母使其异源合成类黄酮生物合成途径的重要中间体肉桂酸、对香豆酸,并优化前体芳香族氨基酸生物合成途径以提高毕赤酵母的生产能力。方法:在毕赤酵母GS115中利用乙醇诱导型人工转录系统表达Rhodotorula glutinis来源的苯丙氨酸解氨酶,并在该重组菌株中分别过表达胞内芳香族氨基酸生物合成途径中的关键酶或其突变体以进行优化。结果:异源表达苯丙氨酸解氨酶可使毕赤酵母将自身产生的L-苯丙氨酸、L-酪氨酸转化为肉桂酸(38.8 mg/L)、对香豆酸(34.2 mg/L),而通过过表达相关酶进行优化,最终肉桂酸和对香豆酸的产量分别达到124.1 mg/L和302.0 mg/L。结论:利用新的异源宿主毕赤酵母成功合成了肉桂酸、对香豆酸,并对胞内的芳香族氨基酸生物合成途径进行了优化,表明毕赤酵母具有生产黄酮类化合物的应用潜力,也为其他芳香族氨基酸衍生物或植物化合物在毕赤酵母中的异源合成奠定了基础。     

用木瓜蛋白酶及固定化木瓜蛋白酶拆分DL-苯丙氨酸

为了将手性化合物D-苯丙氨酸和L-苯丙氨酸进行分离,利用木瓜蛋白酶及固定化木瓜蛋白酶催化的方法对其拆分．试验结果表明,用DL-苯丙氨酸合成N-乙酰-DL-苯丙氨酸,得率为88.7％．木瓜蛋白酶、海藻酸钠 壳聚糖固定化木瓜蛋白酶(IPSAC)、尼龙布固定化木瓜蛋白酶(IPN)催化合成N-乙酰-L-苯丙氨酰苯胺时,对催化合成过程影响最大的因素分别是溶液中的离子强度、溶液中的离子强度、反应温度;溶液中的离子强度与pH对合成的影响较大．本试验得出分别用木瓜蛋白酶、IPSAC、IPN催化合成N-乙酰-L-苯丙氨酰苯胺的3个最佳方案;用此3个方案合成时,产率分别为61.2%、54.7%、36.3%．N-乙酰-L-苯丙氨酰苯胺水解生成L-苯丙氨酸,产率59.2%,光学纯度为96.6％．N-乙酰-D-苯丙氨酸水解生成D-苯丙氨酸,产率61.7%,光学纯度为95.7％．     

L-苯丙氨酸制备的研究进展

笔者对化学和生物合成L-苯丙氨酸的研究进展进行了综述。首先简述L-苯丙氨酸化学合成和酶促合成方法;然后综述微生物发酵法制备L-苯丙氨酸的研究进展,简单介绍大肠杆菌和谷氨酸棒杆菌发酵法生成L-苯丙氨酸的代谢机制,同时,对发酵法合成L-苯丙氨酸的各项应用研究展开重点介绍;最后,对L-苯丙氨酸在生物领域的发展进行了展望。     

蓖麻蚕中肠γ-谷氨酰转肽酶和底物的相互作用及其生理功能

蓖麻蚕Philosamta cynthia ?n,高度提纯的中肠γ-谷氨酰转肽酶(γ-GTP)体外转肽作用表明:L-苯丙氨酸、L-甲硫氨酸,L-半胱氨酸、L-色氨酸,L-精氨酸和L-赖氨酸是最好的γ-谷氨酰的受体,而L-谷氨酸和L-谷氨酰胺(L-Gln)系该酶良好的γ-谷氨酰供体。酶对γ-谷氨酰对硝基苯胺(γ-GNA)的K_m为0.13mmol/L(含L-苯丙氨酸)和0.29mmol/L(无L-苯丙氨酸)。谷胱甘肽(GSH)和L-Gln与γ-GNA竞争酶的γ-谷氨酰结合部位,其抑制常数K_1值分别为0.5mmol/L和1.1mmol/L。γ-GTP催化L-Gln的酰胺键水解和转肽,其催化速率相当于对γ-GNA的38％。     

转氨酶催化不对称合成芳香族L-氨基酸

芳香族L-氨基酸是合成许多药物、农药、精细化学品和食品添加剂的重要手性砌块(Chiral buildingblocks)。利用酶催化具有高活性和高立体选择性的特点合成手性砌块是目前不对称合成领域重要的研究方向。通过对不同来源转氨酶的进化分析,选择分别源自原核生物大肠杆菌Escherichia coli和真核生物酿酒酵母Saccharomyces cerevisia中的两种具有代表性Ⅰ型芳香族转氨酶TyrB和Aro8,比较研究了两种转氨酶通过平衡逆转不对称氨化催化合成芳香族L-氨基酸的反应过程和催化效率。重组转氨酶TyrB和Aro8都能有效地合成天然芳香族氨基酸苯丙氨酸和酪氨酸以及非天然氨基酸苯甘氨酸。手性HPLC分析表明,合成的氨基酸都是L-构型的,e.e值等于100%。L-丙氨酸是适宜的氨基供体,转氨酶TyrB和Aro8都不能利用D-型氨基酸作为氨基供体。反应体系中氨基供体L-丙氨酸和氨基受体芳香族α-酮酸的最适摩尔比为4∶1。底物芳香族α-酮酸分子结构中芳香环上的取代基以及脂肪酸碳链部分的长度都对酶催化的转氨效率有显著的影响。在制备规模试验中,TyrB催化不对称转氨反应合成L-苯甘氨酸、L-苯丙氨酸和L-酪氨酸的比生产速率为0.28 g/(g.h)、0.31 g/(g.h)和0.60 g/(g.h),Aro8催化上述反应的比生产速率分别为0.61 g/(g.h)、0.48 g/(g.h)和0.59 g/(g.h)。研究结果对利用转氨酶通过平衡逆转不对称催化合成芳香族L-氨基酸的工业化应用具有指导意义。     

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.     

Optimization of reaction conditions and stabilization of phenylalanine ammonia lyase-containing Rhodotorula glutinis cells during bioconversion of trans-cinnamic acid to L-phenylalanine

Studies were performed to elucidate the optimal reaction conditions (pH, temperature, ammonia concentration and biocatalyst loading) for bioconversion of trans-cinnamic acid (t-CA) to L-phenylalanine (L-Phe) by L-phenylalanine ammonia lyase (PAL) containing Rhodotorula glutinis cells. All treatments with permeabilizing agents stimulated L-Phe production and also enhanced instability of the catalyst, except Triton X-100 which gave a superior (56%) increase in conversion as compared to the control and a significant stabilization of PAL enzyme. Inclusion of several activity modifiers and stabilizer additives in reaction mixtures were shown to enhance the yield of L-Phe and maintained PAL stability over several successive incubations during the bioconversion process. Maximum stabilization of PAL and enhancement of L-Phe production was achieved with addition of 20% polyhydric alcohol (glycerol). The production of L-Phe continued to the fifth cycle and the total yield increased 2.3 times compared to the yield produced by the control (without glycerol addition) during the repeated batch process. Reducing agents such as 2-mercaptoethanol and thioglycolic acid were added to the bioconversion mixture in order to reduce the effects of oxygen on PAL catalyst life. Production of L-Phe by addition of 400 mgL(-1) of thioglycolic acid was maximized over the control by 55%. When both 20% glycerol and 400 mgL(-1) thioglycolic acid were simultaneously present in the reaction mixture, reuseability and stability of biocatalyst (PAL) were extended to eight consecutive cycles and conversion rate and overall productivity of L-Phe were higher than that of the control. These results may lead to improvements in the production of the essential amino acid L-Phe.     

Production of l-Phenylalanine from trans-Cinnamic Acid with Rhodotorula glutinis Containing l-Phenylalanine Ammonia-Lyase Activity

An enzymatic method using l-phenylalanine ammonia-lyase (EC 4.3.1.5) for the rapid conversion of trans-cinnamic acid to l-phenylalanine has been investigated. With Rhodotorula glutinis, enzyme activity as high as 0.3 U/ml of culture broth was obtained. The enzyme activity was kept stable for a relatively long time during cultivation by the addition of l-isoleucine. Optimization of the parameters of the conversion reaction resulted in accumulation of 18 mg of l-phenylalanine per ml of reaction mixture. The conversion yield from trans-cinnamic acid was about 70%. The method may provide a rapid and practical way to produce l-phenylalanine useful as an essential amino acid.     

Transgene-mediated and elicitor-induced perturbation of metabolic channeling at the entry point into the phenylpropanoid pathway

3H-l-Phenylalanine is incorporated into a range of phenylpropanoid compounds when fed to tobacco cell cultures. A significant proportion of (3)H-trans-cinnamic acid formed from (3)H-l-phenylalanine did not equilibrate with exogenous trans-cinnamic acid and therefore may be rapidly channeled through the cinnamate 4-hydroxylase (C4H) reaction to 4-coumaric acid. Such compartmentalization of trans-cinnamic acid was not observed after elicitation or in cell cultures constitutively expressing a bean phenylalanine ammonia-lyase (PAL) transgene. Channeling between PAL and C4H was confirmed in vitro in isolated microsomes from tobacco stems or cell suspension cultures. This channeling was strongly reduced in microsomes from stems or cell cultures of transgenic PAL-overexpressing plants or after elicitation of wild-type cell cultures. Protein gel blot analysis showed that tobacco PAL1 and bean PAL were localized in both soluble and microsomal fractions, whereas tobacco PAL2 was found only in the soluble fraction. We propose that metabolic channeling of trans-cinnamic acid requires the close association of specific forms of PAL with C4H on microsomal membranes.     

Strain Improvement of Rhodotorula graminis for Production of a Novel l-Phenylalanine Ammonia-Lyase

l-Phenylalanine ammonia-lyase (PAL; EC 4.3.1.5) from Rhodotorula rubra has been used in the commercial manufacture of l-phenylalanine from trans-cinnamic acid. In this study, R. graminis PAL was investigated. Mutant strain GX6000 was isolated after ethyl methanesulfonate mutagenesis of wild-type R. graminis GX5007 by selecting for resistance to phenylpropiolic acid, an analog of trans-cinnamic acid. Mutant strain GX6000 produced inducible PAL at levels four- to fivefold higher than had wild-type R. graminis. Furthermore, this strain had several other physiological traits that make it more commercially useful than R. rubra. For example, during fermentation, the PAL half-life was three- to fivefold longer, PAL specific activity was six to seven times higher, and PAL synthesis was significantly less inhibited by temperatures above 30 degrees C. Induction of PAL in strain GX6000 appeared to be less tightly regulated; l-leucine acted synergistically with l-phenylalanine, the physiological inducer, to increase the PAL specific activity and titer to 165 U/g (dry weight) and 3,000 U/liter, respectively, a 40% increase over the effect of l-phenylalanine alone. Strain GX6000 PAL showed significantly greater stability in bioreactors for the synthesis of l-phenylalanine, a finding that is consistent with the stability properties observed during fermentation.     

Production of phenylalanine ammonia-lyase (PAL): isolation and evaluation of yeast strains suitable for commercial production of l-phenylalanine

Summary Phenylalanine Ammonia-Lyase (PAL) containing microorganisms were isolated from a wide variety of natural habitats. The best 21 strains to emerge from the primary screen were screened for PAL activities in both directions using l-phenylalanine and t-cinnamate substrates. Twelve of the latter strains were compared for total cell production and PAL activity and 7 isolates were chosen for examination of the extent of PAL induction in various media. On the basis of these screens, isolate SPA 10 (identified as Rhodotorula rubra) was selected for further optimization. Growth was optimal at 28° C and pH 5.0, although cellular PAL activity was shown to be higher at sub-optimal temperatures (36° C) and pH (8.0) for growth. Synthesis of PAL was repressed when grown in the presence of various sugars and NH ₄ ⁺ ions. Manipulation of fermentation conditions enabled PAL synthesis to occur at maximum biomass levels, upon glucose exhaustion. PAL was rapidly inactivated within cells shortly after maximum synthesis was attained: feeding of d,l-isoleucine and low concentrations of d,l-phenylalanine, and shifting of fermentation temperature conferred catalyst stability for fermentations over 100 h. These results demonstrate the suitability and superiority of isolate SPA 10 for the commercial production of l-phenylalanine from trans-cinnamic acid.     

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.     

Production of p-hydroxycinnamic acid from glucose in Saccharomyces cerevisiae and Escherichia coli by expression of heterologous genes from plants and fungi

Biological production of p-hydroxycinnamic acid (pHCA) from glucose can be achieved via deamination of the aromatic amino acids l-tyrosine or l-phenylalanine. Deamination of l-phenylalanine produces trans-cinnamic acid (CA) which is further hydroxylated in the para position to produce pHCA. However, when tyrosine is used as the substrate, trans-pHCA is produced in one step. This reaction is accomplished by phenylalanine ammonia-lyase (PAL)/tyrosine ammonia-lyase (TAL). Various bacteria and eukaryotic microorganisms were screened for their ability to produce a PAL/TAL enzyme with high TAL activity. Cell-free extracts of the yeast Rhodotorula glutinis possessed the highest level of TAL activity (0.0143U/mg protein) and the lowest PAL/TAL ratio (1.68) amongst species examined. The gene for this enzyme was cloned and expressed in Escherichia coli and the kinetics of the purified PAL/TAL determined. The recombinant PAL/TAL possessed characteristics similar to those of the wild-type enzyme. Functional expression of R. glutinis PAL/TAL enzyme in Saccharomyces cerevisiae cells containing the plant C4H P-450 and P-450 reductase enzymes from Helianthus tuberosus allowed conversion of glucose to pHCA. Addition of l-phenylalanine to these cultures increased pHCA production confirming its production via the PAL route. When R. glutinis PAL/TAL was synthesized in an E. colil-phenylalanine producing strain (ATCC 31882) and grown on glucose, pHCA was formed in the absence of the Cytochrome P-450 and the P-450 reductase enzymes underlining its production via the TAL route without CA intermediacy.     

酵母全细胞苯丙氨酸鲜氨酶（PAL）活性的紫外分光光度测定法

本文报告以L-苯丙氨酸 (L-phe) 为底物,酵母全细胞作酶源,酶促生成产物反式-肉桂酸 (t-Ca)测定苯丙氨解氨酸 (PAP,EC_(4.3.1.5) 活性的紫外分光光度法。测定程序包括标准物质t-Ca的加样试验,绝对回收率试验,线性回归分析的整套定量分析研宄步骤,建立了一套经过修改的Kalghatgi和Subba Rao(1975) PAL 活性测定法。此法具有良好的准确度和精密度,已经用于评价具有PAL活性的酵母菌株在液体培养物中细胞生长和PAL活性形成的时间过程研究。