Complete conversion of D,L-5-monosubstituted hydantoins with a low velocity of chemical racemization into D-amino acids using whole cells of recombinant Escherichia coli

A reaction system was developed for the production of D-amino acids from D,L-5-monosubstituted hydantoins with a very slow rate of spontaneous racemization. For this purpose the D-hydantoinase and D-carbamoylase from Agrobacterium radiobacter NRRL B11291 were cloned in separate plasmids and expressed in Escherichia coli. The third enzyme, hydantoin racemase, was cloned from Agrobacterium tumefaciens C58. The hydantoin racemase amino acid sequence was significantly similar to those previously described. A reaction system consisting of recombinant Escherichia coli whole cell biocatalysts containing separately expressed D-hydantoinase, D-carbamoylase, and hydantoin recemase showed high substrate specificity and was effective toward both aliphatic and aromatic D,L-5-monosubstituted hydantoins. After optimizing reaction conditions (pH 8 and 50 degrees C), 100% conversion of D,L-5-(2-methylthioethyl)-hydantoin (15 mM) into D-methionine was obtained in 30 min.     

Production of D-p-hydroxyphenylglycine by N-carbamoyl-D-amino acid amidohydrolase-overproducing Escherichia coli strains.

The N-carbamoyl-D-amino acid amidohydrolase (D-carbamoylase) gene from Agrobacterium radiobacter NRRL B11291 has been successfully cloned and expressed in Escherichia coli. Subcloning of the D-carbamoylase gene into different types of vectors and backgrounds of E. coli strains showed that the optimal expression level of D-carbamoylase was achieved in a ColE1-derived plasmid with a 150-fold increase in specific enzyme activity compared to that in a pSC101-derived plasmid. In addition, the recombinant plasmids were very stable in the E. coli strain ATCC11303 but not in JCL1258 tested here. Employing the recombinant E. coli strain DH5alpha/pAH61 for D-p-hydroxyphenylglycine production showed that the cell was capable of transforming N-carbamoyl-D-hydroxylphenylglycine to D-p-hydroxyphenylglycine with a molar conversion yield of 100% and a production rate of 1.9 g/(L h). In comparison with A. radiobacter NRRL B11291, this productivity approximates a 55-fold increase in D-hydroxyphenylglycine production. This result suggests the potential application of recombinant E. coli strains for the transformation reaction.     

Construction and evaluation of a novel bifunctional N-carbamylase-D-hydantoinase fusion enzyme

A fully enzymatic process employing two sequential enzymes, D-hydantoinase and N-carbamylase, is a typical case requiring combined enzyme activity for the production of D-amino acids. To test the possibility of generating a bifunctional fusion enzyme, we constructed a fusion protein via end-to-end fusion of a whole gene that encodes an intact protein at the N terminus of the D-hydantoinase. Firstly, maltose-binding protein (MBP) gene of E. coli was fused with D-hydantoinase gene from Bacillus stearothermophilus SD1, and the properties of the resulting fusion protein (MBP-HYD) were compared with those of native D-hydantoinase. Gel filtration and kinetic analyses clearly demonstrated that the typical characteristics of D-hydantoinase are maintained even in a fusion state. Based on this result, we constructed an artificial fusion enzyme composed of the whole length of N-carbamylase (304 amino acids [aa]) from Agrobacterim radiobacter NRRL B11291 and D-hydantoinase (471 aa). The fusion enzyme (CAB-HYD) was functionally expressed with an expected molecular mass of 86 kDa and efficiently converted exogenous hydantoin derivatives to the D-amino acids. A related D-hydantoinase (HYD1) gene from Bacillus thermocatenulatus GH2 was also fused with the N-carbamylase gene at its N terminus. The resulting enzyme (CAB-HYD1) was bifunctional as expected and showed better performance than the CAB-HYD fusion enzyme. The conversion of hydantoin derivatives to corresponding amino acids by the fusion enzymes was much higher than that by the separately expressed enzymes, and comparable to that by the coexpressed enzymes. Thus, the fusion enzyme might be useful as a potential biocatalyst for the production of nonnatural amino acids.     

High production of heterologous proteins in Escherichia coli using the thermo-regulated T7 expression system

The exclusive use of isopropyl beta-D-thiogalactopyranoside to activate the T7 promoter for protein production has limited the general use of the expression system. We have sought an alternative by constructing a recombinant Escherichia coli strain, BL21 (G2), to carry a chromosomal copy of T7 gene 1 fused to the lambdaPL and lambdaP(R) tandem promoter. As a result, the recombinant strain harboring the carbamoylase gene from Agrobacterium radiobacter NRRL B11291 was shown to display various levels of.protein production in response to different degrees of heat shock. In particular, the system remained inactive at 30 degrees C and exhibited high sensitivity to heat such that a detectable carbamoylase activity could be measured after exposure to 33 degrees C. Moreover, heating in two steps - elevating the temperature from 30 degrees C to 39 degrees C and holding for a brief period, followed by reducing to 37 degrees C--was found to be the most potent method for protein production in this case. Using this approach, the recombinant protein accounted for 20% of total protein content of the cell. These results reveal the advantages of this expression system: responsiveness to thermal modulation and high-level production capability. In an attempt to enhance the total protein yield, a fed-batch fermentation process was carried out to control the cell growth rate by adjusting the substrate inflow. By applying the two-step temperature change. a carbamoylase yield with enzyme activity corresponding to 14,256 units was obtained. This production yield is a 10-fold increase in comparison with that at the batch-fermentation scale and 2,000-fold higher than that achieved at the shake-flask scale. Overall, it illustrates the promise of the newly constructed T7 system based on heat inducibility for industrial scale production of recombinant proteins.     

利用基因工程菌HC01固定化细胞转化生产D-对羟基苯甘氨酸

对一菌两酶工程菌HC01转化底物DL-对羟基苯海因(DL-HPH)的最适条件及其细胞固定化进行了研究,HC01游离细胞转化DL-HPH的最适条件为40°C、pH7.5。通过对固定化细胞酶活力测定,确定细胞固定化的最优条件为海藻酸钠浓度2.5%、细胞浓度0.029g/mL、钙离子浓度3%。固定化HC01的热稳定性比游离细胞高5°C,二价金属离子Mn2+、Mg2+、Cu2+、Co2+和Ni2+在浓度为0.1mmol/L时对固定化细胞中D-海因酶(HYD)和N-氨甲酰-D-氨基酸酰胺水解酶(CAB)两酶的活力无显著影响,Mn2+和Mg2+可分别使游离细胞中CAB活力提高至原来的2.1和2.7倍。在氮气保护下,当初始pH为9.0、转化温度为40°C、转速为80r/min,利用固定化HC01转化30g/L的DL-HPH时,36h后转化率可达97%左右,产物D-HPG经纯化后光学纯度达到99.7%,得率可达85%。     

Purification of industrial hydantoinase in one chromatographic step without affinity tag

Hydantoinase is used in industry as a biocatalyst for the production of optically pure D- or L-amino acids. Previously, homogeneous hydantoinase was obtained by multi-chromatographic purification procedures. Here, we reported a process that contained only a single chromatographic step to purify a recombinant hydantoinase to homogeneity. Hydantoinase from Agrobacterium radiobacter NRRL B11291 was expressed in Escherichia coli. The recombinant enzyme was purified following heat treatments, high concentration alcohol precipitation, and chelating Sephacel chromatography. The recombinant hydantoinase did not contain any affinity tags from the plasmid. This simplified procedure provided a convenient way to obtain hydantoinase in high yield (71%) and high purity. It should be very useful for further industrial application and for the study of the structure-function of hydantoinase.     

Adsorptive removal of inhibitory by-product in the enzymatic production of optically active D-p-hydroxyphenylglycine from 5-substituted hydantoin

Summary One-step enzymatic production of D-p-hydroxyphenylglycine (D-HPG) from 5-substituted hydantoin was carried out using a bacterium Agrobacterium sp I-671 which possesses D-hydantoinase and N-carbamoylase. From the inhibition study, it was found that N-carbamoylase was severely inhibited by ammonium ions which is co-produced with D-HPG. In order to increase the conversion yield of D-HPG, simultanious removal of inhibitory by-product from reaction mixture was carried out using the specific adsorbents for ammonium ions. The conversion yield of D-HPG reached about 98% in the presence of adsorbents in 27 hours, while 50% conversion was observed in the absence of adsorbents.     

Production of D-amino acid using whole cells of recombinant Escherichia coli with separately and coexpressed D-hydantoinase and N-carbamoylase

We developed a fully enzymatic process employing D-hydantoinase and N-carbamoylase for the production of D-amino acid from 5'-monosubstituted hydantoin. For the comparison of the reaction systems using two sequential enzymes, D-hydantoinase of Bacillus stearothermophilus SD1 and N-carbamoyl-D-amino acid amidohydrolase (N-carbamoylase) of Agrobacterium tumefaciens NRRL B11291 were separately expressed in each host cell and coexpressed in the same host cell. A high level and constitutive expression of both enzymes in Escherichia coli in a soluble form was achieved using a promoter derived from B. stearothermophilus SD1. The expression levels of both enzymes ranged from 17% to 23% of the total soluble protein, depending on the expression system. In the case of employing separately expressed enzymes, the product yield of D-hydroxyphenylglycine from D,L-p-hydroxyphenylhydantoin and productivity were 71% and 2.57 mM/g-cell/h in 15 h, respectively. The accumulation of N-carbamoyl-D-hydroxyphenylglycine was significant over the reaction time. On the other hand, use of coexpressed enzymes resulted in 98% product yield of D-hydroxyphenylglycine in 15 h, minimizing the level of intermediates in the reaction mixture. The productivity of coexpressed whole cell reaction was estimated to be 6.47 mM/g-cell/h in 15 h. The coexpressed system was tested for an elevated concentration of D,L-p-hydroxyphenylhydantoin, and efficient production can be achieved.     

Burkholderia piCkettii中D-乙内酰脲酶基因(dha)的克隆、测序及表达

对一株能转化D,L－对羟基苯乙内酰脲为D－对羟基苯甘氨酸的菌株MMR003进行了细菌分类学鉴定,该菌为皮氏伯克霍尔德氏菌（Burkholderia pickettii)。实验通过Southern杂交,部分文库构建和筛选,并经一系列亚克隆分析,获得一长度为1374bp的完整开放阅读框,编码458个氨基酸的D－乙内酰脲酶基因。用该基因序列构建的高表达质粒xXZPH2转化E.coliBL21(DE3),经IPTG诱导后,检测到D－乙内酰脲酶活性。该基因编码的氨基酸序列经Blast同源比较分析与放射形土壤杆菌NRRL B11291所产相应酶有85％的同源性。以D,L－对羟基苯乙内酰脲为底物测得的表达酶的活力为0.66u/mL,比相同条件下所测出发菌株MMR003的酶活提高了2倍。     

One-step purification of insoluble hydantoinase overproduced in Escherichia coli

Over-expression of hydantoinase from Agrobacterium radiobacter NRRL B11291 (HDTar) results in the formation of insoluble aggregates in Escherichia coli. As previously reported, recombinant HDTar could be obtained in a homogeneous form using one chromatographic step. However, soluble proteins are required for the pre-treatment in several steps before proceeding to the chromatographic purification step. In this study, we reported a method based on artificial oil bodies (AOBs) to obtain homologous HDTar from its insoluble form in one step. By linkage of HDTar to intein-oleosin gene fusion, the tripartite fusion protein was over-expressed as aggregates in E. coli. Upon sonication, the mixture comprising plant oil and the insoluble fusion protein was readily assembled into AOBs. Further induction for peptide cleavage mediated by intein, the bound HDTar was liberated from AOBs, and the protein free of fusion tags was then recovered. As a result, refolded HDTar was amplified by over 300-fold. Obviously, this simplified method provides an efficient way to obtain HDTar with high yield and high purity.     

Overproduction of d-hydantoinase and carbamoylase in a soluble form in Escherichia coli

The production of d-hydantoinase and carbamoylase from Agrobacterium radiobacter NRRL B11291 using T7 and trc promoters, respectively, was found to cause protein aggregates in Escherichia coli. We initiated a systematic study aimed at overproducting these two proteins in a soluble form. As a result, the protein aggregate from carbamoylase overproduction could be alleviated with the aid of GroEL/GroES. In contrast, the production of a high level of d-hydantoinase in an active form can be achieved at low temperature (25 °C) or by the coproduction of DnaJ/DnaK. Overall, with such approaches both recombinant proteins gain more than a four-fold increase in enzyme activity. In addition, by fusion with thioredoxin, d-hydantoinase activity can be increased 25% more than the unfused counterpart in the presence of DnaJ/DnaK. These results indicate the success of our approaches to overproducing d-hydantoinase and carbamoylase in a soluble form in E. coli. Received: 26 November 1999 / Received revision: 28 February 2000 / Accepted: 10 March 2000     

Chitin-binding domain based immobilization of D-hydantoinase

Chitin-binding domain (ChBD) of chitinase A1 from Bacillus circulans WL-12 comprises 45 amino acids and exhibits remarkably high specificity to chitin (Hashimoto, M., Ikegami, T., Seino, S., Ohuchi, N., Fukada, H., Sugiyama, J., Shirakawa, M., Watanabe, T., 2000. Expression and characterization of the chitin-binding domain of chintinase A1 from B. circulans WL-12. J. Bacteriol. 182, 3045-3054.). To investigate the feasibility of exploiting ChBD as affinity tags to confine enzymes of interest on chitin, ChBD fused to the C-terminus of the gene encoding D-hydantoinase was constructed. Subsequent expression of the hybrid protein in Escherichia coli gave a soluble fraction accounting for 8% of total cell protein content. Direct adsorption of the ChBD-fused D-hydantoinase on chitin beads was carried out, and SDS-PAGE analysis showed that the linkage between the fusion protein and the affinity matrix was highly specific, substantially stable, and reversible. As compared to its free counterpart, the immobilized D-hydantoinase exhibited higher tolerance to heat and gained a half life of 270 h at 45 degrees C. In addition, the shelf life (defined as 50% of initial activity remained) of the immobilized enzyme stored at 4 degrees C was found to reach 65 days. Furthermore, D-hydantoinase immobilized on chitin could be reused for 15 times to achieve the conversion yield exceeding 90%. Overall, it illustrates the great usefulness of ChBD for enzyme immobilization.     

假单胞菌海因酶基因在大肠杆菌中的高效表达(英文)

为实现利用生物酶转化法进行D 对羟基苯甘氨酸的工业化生产 ,构建了 3株海因酶基因工程菌 .利用PCR技术从恶臭假单胞菌 (Pseudomonasputida)CPU 980 1染色体DNA中扩增得到长约1.8kb的含编码区和自身启动子的海因酶全基因 .通过将海因酶全基因插入pMD18 T质粒、海因酶基因的编码区与pET 17 b质粒重组、海因酶基因编码区和T7强启动子一起插入pMD18 T质粒分别得到重组质粒pMD dht、pET dht和pMD T7 dht.将上述重组质粒分别转化大肠杆菌 (Escherichiacoli) ,通过地高辛标记菌落原位杂交和海因酶活力测定两种方法 ,筛选出具有海因酶活力的阳性转化子 .结果表明 ,大肠杆菌的RNA聚合酶能够识别和结合来自恶臭假单胞菌海因酶基因的自身启动子 ,该启动子在大肠杆菌中能够工作 .基因工程菌E .coliBL2 1 pMD dht、E .coliBL2 1 pET dht和E .coliBL2 1 pMD T7 dht的海因酶活力分别为 170 0U L、190 0U L和 2 5 0 0U L ,比野生菌P .putidaCPU 980 1的海因酶活力分别提高了 8倍、9倍和 12倍 .薄层扫描结果显示 ,这些工程菌的海因酶表达量分别约占菌体总可溶性蛋白质的 2 0 %、31%和 5 7%.SDS PAGE显示 ,海因酶的单体分子量约为 5 0kD .经工程菌E .coliBL2 1 pMD T7 dht催化 ,底物对羟基苯海因的转化率在 13h内可达到 9     

Stringent regulation and high-level expression of heterologous genes in Escherichia coli using T7 system controllable by the araBAD promoter

The recombinant Eschreichia coli strain BL21 (BAD) was constructed to carry a chromosomal copy of T7 gene 1 fused to the araBAD promoter. To further characterize this expression system, strain BL21 (BAD) was transformed with the plasmid containing the carbamoylase gene from Agrobacterium radiobacter driven by the T7 promoter. Upon induction with L-arabinose, recombinant cells produced 100-fold increase in carbamoylase activity in comparison with uninduced cells on M9 semidefined medium plus glycerol. This protein yield accounts for 30% of total cell protein content. In addition, it was found that after 100 generations the plasmid harboring the carbamoylase gene remained firmly stable in strain BL21 (BAD), but its stability dropped to only 20-30% in strain BL21 (DE3), a commercial strain bearing T7 gene 1 regulated by the lacUV5 promoter in its chromosome. In an attempt to enhance the total protein yield, fed-batch fermentation process was carried out using a two-stage feeding strategy to compartmentalize cell growth and protein synthesis. In the batch fermentation stage, the culture was grown on glucose to reach the stationary growth phase. Subsequently, glycerol was fed to the culture broth and L-arabinose was augmented to induce protein production when cells entered the late log growth phase. As a result, a carbamoylase yield corresponding to 5525 units was obtained, which amounts to a 337-fold increase over that achieved on a shake-flask scale. Taken together, these results illustrate the practical usefulness of T7 system under control of the araBAD promoter for heterologous protein production.     

Modeling and kinetic analysis of the reaction system using whole cells with separately and co-expressed D-hydantoinase and N-carbamoylase

We developed a kinetic model that describes a heterogeneous reaction system for the production of D-p-hydroxyphenylglycine from D,L-p-hydroxyphenyl-hydantoin using D-hydantoinase of Bacillus stearothermophilus SD1 and N-carbamoylase of Agrobacterium tumefaciens NRRL B11291. As a biocatalyst, whole cells with separately or co-expressed enzymes were used. The reaction system involves dissolution of substrate particles, enzymatic conversion, racemization of the L-form substrate, and transfer of the dissolved substrate, intermediate, and product through the cell membrane. Because the two enzymes have different pH optimum, kinetic parameters were evaluated at different pH for the reaction systems. The model was simulated using the kinetic parameters and compared with experimental data, and it was found that the kinetic model well describes the behavior of the reaction systems using whole cells with separately and co-expressed enzymes. Factors affecting the kinetics of the reaction systems were analyzed on the basis of the kinetic model. In the reaction system with separately expressed enzymes, racemization rate and transport of the reaction intermediate (N-carbamoyl-D-p-hydroxyphenylglycine) were revealed to be the limiting factors at neutral pH, resulting in accumulation of intermediate in the reaction medium. At alkaline condition, on the other hand, inhibition of N-carbamoylase by ammonia was severe, and thereby the reaction rate significantly reduced. In the co-expressed enzyme system, accumulation of intermediate was negligible in the reaction medium, and the improved performance was observed compared to that with separately expressed enzymes. The present model might be applied for the optimization and development of the reaction system using two sequential enzymes.     

节杆菌BT801 N-氨甲酰氨基酸水解酶基因的克隆与表达

通过PCR从质粒pUC18 16 9中扩增得到N 氨甲酰氨基酸水解酶基因 (hyuC) ,置于原核表达载体pQE6 0的T5启动子下游构成表达质粒pQE6 0 hyuC ,并在大肠杆菌M15中实现了该基因的高表达。SDS PAGE检测表达产物 ,在相对分子量 44kD处有一表达带 ,经薄层扫描分析目的蛋白占全菌蛋白的 40 % ,主要以可溶性形式存在。酶活性分析结果表明 ,工程菌M15 pQE6 0 hyuC的N 氨甲酰氨基酸水解酶的比活分别比原始菌株ArthrobacterBT80 1和亚克隆DH5α pUC18 16 9提高了 5 2倍和 72倍。在节杆菌BT80 1和大肠杆菌DH5α pUC18 16 9的反应体系中加入等量菌体的工程菌M15 pQE6 0 hyuC ,可使乙内酰脲酶总比活分别提高 8 1倍和 3 0倍。     

用基因工程菌酶法和化学法制备-D-对羟基苯甘氨酸(英文)

D 对羟基苯甘氨酸 (D p HPG)是制备羟氨苄青霉素、羟氨苄头孢菌素和羟氨唑头孢菌素等β 内酰胺类抗生素的重要中间体 ,同时它也用于多种多肽类激素及农药的合成 .在D 对羟基苯甘氨酸的多种制备方法中 ,生物酶转化法具有原料易得、工艺简单、耗能少、产率高、成本低、光学纯度好、三废污染少等优势 .为利用生物酶转化法制备D 对羟基苯甘氨酸 ,首先用尿素、乙醛酸和苯酚合成底物D ,L 对羟基苯海因 ,然后利用D 海因酶基因工程菌E .coliBL2 1 pMD T7 dht细胞作酶源 ,进行底物D ,L 对羟基苯海因到中间体N 氨基甲酰 D 对羟基苯甘氨酸的酶法转化 ,最后用化学法将N 氨基甲酰 D 对羟基苯甘氨酸进一步转化为D 对羟基苯甘氨酸 .结果表明 ,底物D ,L 对羟基苯海因的收率为 60 % .8L体积的发酵小试实验表明 ,发酵 12h ,工程菌E .coliBL2 1 pMD T7 dht的海因酶活力为 30 0 0U L ,SDS 聚丙烯酰胺凝胶电泳薄层扫描结果显示海因酶表达量约占菌体总可溶性蛋白质的 60 % ,菌体收率为 6% .8L体积的海因酶转化实验表明 ,在 4 %底物D ,L 对羟基苯海因和 1%菌体 (湿重 )pH 9 0情况下 ,反应 5h ,D ,L 对羟基苯海因的转化率可达 96% .在酸性条件下 ,用NaNO2 将N 氨基甲酰 D 对羟基苯甘氨酸转化为D 对羟基苯甘氨酸 ,反应 2h ,转     

海因酶法制备D-对羟基苯甘氨酸的研究进展

D-对羟基苯甘氨酸(D-HPG)主要用于合成β-内酰胺类半合成抗生素,是国内最紧缺的医药中间体之一。微生物酶法是目前获得光学纯D-HPG的重要途径,微生物中起催化作用的主要是D-海因酶和N-氨甲酰水解酶。文章综述了产酶微生物的来源,酶的理化性质,以及培养条件的优化、基因工程、酶的固定化技术生产D-HPG的研究进展。     

Optimization of a heterogeneous reaction system for the production of optically active D-amino acids using thermostable D-hydantoinase

A thermostable D-hydantoinase from Bacillus stearothermophilus SD-1 was previously mass-produced by batch cultivation of the recombinant E. coli harboring the gene encoding the enzyme (Lee et al., 1997). In this work, we attempted to optimize the process for the production of N-carbamoyl-D-p-hydroxyphenylglycine, which is readily hydrolyzed to D-p-hydroxyphenylglycine under acidic conditions, from 5-(4-hydroxyphenyl)hydantoin using the mass-produced D-hydantoinase. In an effort to overcome the low solubility of the substrate, enzyme reaction was carried out in a heterogeneous system consisting of a high substrate concentration up to 300 g/L. In this reaction system, most of substrate is present in suspended particles. Optimal temperature and pH were determined to be 45 degrees C and 8.5, respectively, by taking into account the reaction rate and conversion yield. When the free enzyme was employed as a biocatalyst, enzyme loading higher than 300 unit/g-substrate was required to achieve maximum conversion. Use of whole cell enzyme resulted in maximum conversion even at lower enzyme loadings than the free enzyme, showing 96% conversion yield at 300 g/L substrate. The heterogeneous reaction system used in this work might be applied to the enzymatic production of other valuable compounds from a rarely water-soluble substrate.