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。     

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%。     

One-step production of D-p-hydroxyphenylglycine by recombinant Escherichia coli strains

The gene encoding D-hydantoinase from Agrobacterium radiobacter NRRL B11291 was successfully cloned by use of polymerase chain reaction. A positive clone was scored, and its nucleotide sequence was further analyzed. The analysis by deleting various lengths of nucleotides from the amino terminus of the open reading frame revealed the putative regions for promoter and RBS site. By highly expressing both D-hydantoinase and carbamoylase, recombinant Escherichia coli strains were able to convert DL-hydroxyphenyl hydantoin (DL-HPH) to D-p-hydroxyphenylglycine (D-HPG) with a conversion yield of 97%, accounting for productivity 5 times higher than that obtained by A. radiobacter NRRL B11291. Immobilizing the recombinant cells with kappa-carrageenan could also achieve a conversion of 93%, while A. radiobacter NRRL B11291 attained 20% within the same period of reaction time. These results illustrate the feasibility in employing recombinant E. coli to accomplish one-step conversion of DL-HPH to D-HPG. In the process of improving D-HPG production, D-hydantoinase activity was increased 2.57-fold but carbamoylase activity remained constant, which resulted in only a 30% increase in the reaction rate. It suggests that carbamoylase is the step setting the pace of the reaction. Since the reaction substrate is highly insoluble, achieving sufficient agitation appears to be an important issue in this heterogeneous system. This view is further supported by the study on repeated use of cells, which shows that to reach a conversion of more than 90% free cells can be recycled six times, whereas immobilized cells can be used only twice. In conclusion, the poor reusability of immobilized cells is due to the fouling on the gel surface.     

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.     

Membrane reactor coupled with electrophoresis for enzymatic production of aspartic acid

Aspartic acid production by aspartase reaction on ammonium fumarate was carried out in a membrane reactor coupled with electrophoresis. A pressurized, stirred vessel attached with an ultrafiltration membrane was used as a membrane reactor. An electric field was applied across the membrane to preferentially remove the product aspartate from the reactor into the permeate stream. The charged molecule, aspartate, is much smaller than the molecular-weight cutoff of the membrane (10(4)) so that the ions would move freely through pores of the membrane. The concentration of aspartate in the permeate stream is determined by the electromigration velocity of the ions and the permeation rate of solvent (water) through the membrane. The permeation rate of solvent could be controlled by the applied pressure, and the migration velocity of the ions could be controlled by the electric field strength applied. The equilibrium conversion of ammonium fumarate to the aspartate was 70%. In the presence of electric field, the aspartase activity was not disturbed. Also, it is shown that the aspartate concentration in the permeate stream was 20% higher than that in the reaction solution with the permeate flow rate of 0.7 mL/min. The steady-state conversion was 60%. Instead of aspartate, aspartic acid can be recovered directly from the permeate stream by controlling the circulation of buffer electrolyte in the anode compartment.     

构建重组枯草芽孢杆菌催化制备D-对羟基苯甘氨酸

目的: 在Bacillus subtilis中表达异源D-海因酶基因(hyd)和D-氨甲酰水解酶基因(adc),构建重组细胞作为催化剂,用于生产D-对羟基苯甘氨酸(D-HPG)。方法: 构建hyd表达质粒,考察培养基中二价金属离子对D-海因酶活性的影响。过表达acoR基因,考察AcoR蛋白胞内水平与P_acoA-hyd基因拷贝数的关系。筛选表达adc基因的启动子,构建hyd和adc基因共表达质粒,考察双酶活性菌株的催化特性。结果: 成功构建了海因酶表达质粒pHPS和pUBS,培养基中添加0.8mmol/L的MnCl₂·4H₂O,使168N/pUBS菌株的D-海因酶活性达到956U/gDCW。整合表达P_cdd-acoR基因,使LSL02/pUBS菌株的D-海因酶活性达到1 470U/gDCW。单拷贝P_AE-adc基因的表达水平相对最高。双酶共表达质粒pUBSC被成功构建,菌株LSL02/pUBSC的最适催化温度为40℃45℃,催化活性能够持续12h,当底物起始浓度为20g/L时,反应12h生成的D-HPG达到14.32g/L,转化率达到95%,收率超过80%。结论: 构建具有D-海因酶和D-氨甲酰水解酶双酶活性的重组Bacillus subtilis作为全细胞催化剂,用于海因酶法生产D-HPG,具有技术上的可行性和优势。     

Biocatalytic ammonolysis of (5S)-4,5-dihydro-1H-pyrrole-1,5-dicarboxylic acid, 1-(1,1-dimethylethyl)-5-ethyl ester: preparation of an intermediate to the dipeptidyl peptidase IV inhibitor Saxagliptin

An efficient biocatalytic method has been developed for the conversion of (5S)-4,5-dihydro-1H-pyrrole-1,5-dicarboxylic acid, 1-(1,1-dimethylethyl)-5-ethyl ester (1) into the corresponding amide (5S)-5-aminocarbonyl-4,5-dihydro-1H-pyrrole-1-carboxylic acid, 1-(1,1-dimethylethyl)ester (2), which is a critical intermediate in the synthesis of the dipeptidyl peptidase IV (DPP4) inhibitor Saxagliptin (3). Candida antartica lipase B mediates ammonolysis of the ester with ammonium carbamate as ammonia donor to yield up to 71% of the amide. The inclusion of Ascarite and calcium chloride as adsorbents for carbon dioxide and ethanol byproducts, respectively, increases the yield to 98%, thereby offering an efficient and practical alternative to chemical routes which yield 57-64%.     

二价阳离子对短梗霉多糖发酵的影响

就二价阳离子对短梗霉多糖和黑色素的影响进行了分析和研究。结果表明 ,二价阳离子对短梗霉多糖的合成和黑色素的形成均有较大的影响。通过对培养基中二价阳离子含量和种类的控制不仅可以抑制细胞黑色素的形成 ,而且还保持了很高的多糖发酵水平 ,在 30L生物反应器中短梗霉多糖的产量和转化率分别达到了 59 8g/L和 61 5%。     

Improvement of oxidative and thermostability of N-carbamyl-d-amino Acid amidohydrolase by directed evolution

N-Carbamyl-D-amino acid amidohydrolase (N-carbamoylase), which is currently employed in the industrial production of unnatural D-amino acid in conjunction with D-hydantoinase, has low oxidative and thermostability. We attempted the simultaneous improvement of the oxidative and thermostability of N-carbamoylase from Agrobacterium tumefaciens NRRL B11291 by directed evolution using DNA shuffling. In a second generation of evolution, the best mutant 2S3 with improved oxidative and thermostability was selected, purified and characterized. The temperature at which 50% of the initial activity remains after incubation for 30 min was 73 degrees C for 2S3, whereas it was 61 degrees C for wild-type enzyme. Treatment of wild-type enzyme with 0.2 mM hydrogen peroxide for 30 min at 25 degrees C resulted in a complete loss of activity, but 2S3 retained about 79% of the initial activity under the same conditions. The K(m) value of 2S3 was estimated to be similar to that of wild-type enzyme; however k(cat) was decreased, leading to a slightly reduced value of k(cat)/K(m), compared with wild-type enzyme. DNA sequence analysis revealed that six amino acid residues were changed in 2S3 and substitutions included Q23L, V40A, H58Y, G75S, M184L and T262A. The stabilizing effects of each amino acid residue were investigated by incorporating mutations individually into wild-type enzyme. Q23L, H58Y, M184L and T262A were found to enhance both oxidative and thermostability of the enzyme and of them, T262A showed the most significant effect. V40A and G75S gave rise to an increase only in oxidative stability. The positions of the mutated amino acid residues were identified in the structure of N-carbamoylase from Agrobacterium sp. KNK 712 and structural analysis of the stabilizing effects of each amino acid substitution was also carried out.     

The formation of adsorption properties of nanoporous materials by thermochemical activation

Results of the studies on the use of hydrolytic lignin as a raw material for the production of carbon adsorbents are given. A thermochemical method using sodium hydroxide as an activating agent was chosen as a method of activation of hydrolytic lignin. The experiment was aimed at finding out the influence of operating conditions on the yield and properties of the active carbon obtained. Synthesis of adsorbents was carried out using a uniform second order rotatable central composite design for three variables at five levels. Temperatures of prepyrolysis and pyrolysis, and a dosage of the activating agent represented changing parameters. For samples of active carbon obtained, the adsorption activity was investigated with respect to three adsorbates: methylene blue (MB), iodine, and hexane. Based on the output parameters, the coefficients of equations of regression were calculated and the assessment of their significance was carried out. The conclusion on the degree of the effect of factors and curvature of space studied could be made using absolute values and signs of the coefficients. The effect of operating parameters on the yield and sorption activity of the coal obtained was studied by constructing graphic dependencies and response surfaces. As a result of the analysis of the data obtained, a conclusion was made on the effectiveness of the method used for the synthesis of adsorbents, since the active carbon obtained had a developed porous structure.     

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     

Effect of mass transfer limitations on the enzymatic kinetic resolution of epoxides in a two-liquid-phase system

Optically active epoxides can be obtained by kinetic resolution of racemic mixtures using enantioselective epoxide hydrolases. To increase the productivity of the conversion of sparingly aqueous soluble epoxides, we investigated the use of a two-phase aqueous/organic system. A kinetic model which takes into account interphase mass transfer, enzymatic reaction, and enzyme inactivation was developed to describe epoxide conversion in the system by the epoxide hydrolase from Agrobacterium radiobacter. A Lewis cell was used to determine model parameters and results from resolutions carried out in the Lewis cell were compared to model predictions to validate the model. It was found that n-octane is a biocompatible immiscible solvent suitable for use as the organic phase. Good agreement between the model predictions and experimental data was found when the enzyme inactivation rate was fitted. Simulations showed that mass transfer limitations have to be avoided in order to maximize the yield of enantiomerically pure epoxide. Resolution of a 39 g/L solution of racemic styrene oxide in octane was successfully carried out in an emulsion batch reactor to obtain (S)-styrene oxide in high enantiomeric excess (>95% e.e.) with a yield of 30%.     

Anaerobic oxidation of ammonium is a biologically mediated process.

A newly discovered process by which ammonium is converted to dinitrogen gas under anaerobic conditions (the Anammox process) has now been examined in detail. In order to confirm the biological nature of this process, anaerobic batch culture experiments were used. All of the ammonium provided in the medium was oxidized within 9 days. In control experiments with autoclaved or raw wastewater, without added sludge or with added sterilized (either autoclaved or gamma irradiated) sludge, no changes in the ammonium and nitrate concentrations were observed. Chemical reactions could therefore not be responsible for the ammonium conversion. The addition of chloramphenicol, ampicillin, 2,4-dinitrophenol, carbonyl cyanide m-chlorophenyl-hydrazone (CCCP), and mercuric chloride (HgIICl2) completely inhibited the activity of the ammonium-oxidizing sludge. Furthermore, the rate of ammonium oxidation was proportional to the initial amount of sludge used. It was therefore concluded that anaerobic ammonium oxidation was a microbiological process. As the experiments were carried out in an oxygen-free atmosphere, the conversion of ammonium to dinitrogen gas did not even require a trace of O2. That the end product of the reaction was nitrogen gas has been confirmed by using 15NH4+ and 14NO3-. The dominant product was 14-15N2. Only 1.7% of the total labelled nitrogen gas produced was 15-15N2. It is therefore proposed that the N2 produced by the Anammox process is formed from equimolar amounts of NH4+ and NO3-.     

In situ removal of ammonium ions from hybridoma cell culture media: Selection of adsorbent

Various ion-exchange resins and zeolite Phillipsite-Gismondine were tested for their potential application as adsorbents for thein situ removal of ammonium ions from animal cell culture media in attempting to increase hybridoma cell density and MAb productivity. A zeolite, Phillipsite-Gismondine demonstrated the best performance in terms of NH₄ ⁺ adsorption capacity, selectivity and autoclavability among the various adsorbents tested. The biocompatibility of Phillipsite-Gismondine was also tested and the result showed improvement in cell density, viability, and antibody productivity.     

Influence of varying nitrogen sources on polysaccharide production by Aureobasidium pullulans in batch culture

Summary Polysaccharide formation by Aureobasidium pullulans was affected by the nitrogen source in the medium, and its yield fell when excess ammonium ions were present, even under conditions which otherwise supported its synthesis. Experiments carried out with pH control gave results which question some of the earlier published data, so it is possible to obtain high polysaccharide yields at low pH (2.5), and mycelial growth at high pH (6.5) with certain nitrogen sources. There appeared to be no causal relationship between morphology and polysaccharide-producing capacity of the cultures.Offprint requests to: R. J. Seviour     

异源D-海因酶和N-氨甲酰水解酶共表达重组枯草芽孢杆菌的构建

【目的】构建异源D-海因酶和N-氨甲酰水解酶共表达的重组枯草芽孢杆菌,探讨其作为全细胞催化剂合成D-对羟基苯甘氨酸的可行性。【方法】采用P_(aco)表达盒表达D-海因酶基因hyd或sd1,采用P_(AE)表达盒表达N-氨甲酰水解酶基因adc。分别以质粒pHP13和pUB110为载体,构建D-海因酶和N-氨甲酰水解酶共表达质粒pHCS、pHCY和pUCS。在受体菌中整合表达了acoR和sigL基因,敲除了skf和sdp基因。将共表达质粒分别转化不同的受体菌,通过测定全细胞催化活性,表征D-海因酶和N-氨甲酰水解酶共表达的效果。【结果】带有质粒pHCY和pHCS的重组菌,全细胞催化活性分别为0.21 U/mL和0.31 U/mL。整合表达acoR和sigL基因以及高拷贝质粒pUCS,使全细胞催化活性达到1.0 U/mL。【结论】异源D-海因酶和N-氨甲酰水解酶在枯草芽孢杆菌中能够正确表达。基因拷贝数、acoR和sigL基因表达水平,及skf和sdp基因缺失对重组菌的催化活性具有显著影响。     

Removal of cesium ions from aqueous solutions using various separation technologies

Cesium is the major fission product of uranium, which widely exists in radioactive wastewater. Radiocesium has potential adverse effects on human health and ecological environment. Different methods such as chemical precipitation, coagulation/co-precipitation, solvent extraction, membrane process, chemical reduction, and adsorption have been used to remove radioactive cesium from aqueous solution. However, the development of innovative technologies capable of selectively removing radioactive cesium is still imperative yet challenging. This review focused on cesium removal using various separation technologies, including chemical precipitation, solvent extraction, membrane separation, and adsorption. The key restraints for cesium removal, as well as the recent progress of these methods have also been discussed. Particular attention has been paid to the adsorption methods, which has been highlighted by introducing the latest advances in inorganic adsorbents (such as metal hexacyanoferrates, clay minerals, carbon-based-adsorbents, and ammonium molybdophosphate), organic adsorbents (such as ion exchange resin, metal–organic frameworks and supramolecular/indicator grafting adsorbents), and biosorbents (such as agroforestry wastes and microbial biomass). Adsorption-based methods are high efficient in separation of cesium ions from aqueous streams, and adsorption of cesium ions has been investigated intensively and even used in practical applications, there is still considerable scope for improvement in terms of adsorption capacity and selectivity.

     

Separation of inulinase from Kluyveromyces marxianus using reversed micellar extraction

Inulinase from K. marxianus was extracted into a reversed micelle phase of the cationic surfactant BDBAC (n-benzyl-n-dodecyl-n-bis(2-hydroxyethyl)ammonium chloride) in isooctane/hexanol. The extractions carried out with cells (5.9 g/l) presented a recovery yield of 87% and a purification factor 2.8. Similar values were found for inulinase recovered from the clarified medium (91% recovery yield and 2.8 purification factor). For scaled-up (400-fold) extractions, the recovery of the initial activity reached 77% and the enrichment factor was 2.8.     

Hydantoinases and related enzymes as biocatalysts for the synthesis of unnatural chiral amino acids

A cascade of hydantoinase, N-carbamoylase and hydantoinracemase can be used for the production of natural and unnatural chiral D- and L-amino acids from chemically synthesized hydantoin derivatives. Potentially, 100% conversion and 100% optically pure amino acids can be obtained at the same time if racemic substrates are used. Recent research activities concentrate on newly isolated or improved enzymes and include directed evolution techniques, structure elucidation, studies of fusion proteins and the use of specially designed whole cell biocatalysts.