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.     

Studies on the expression of recombinant fuculose-1-phosphate aldolase in E. coli

Fuculose-1-phosphate aldolase (Fuc-1-PA) is a dihydroxyacetone phosphate (DHAP) dependent aldolase with potential application in chiral synthesis. The influence of the growth medium on the expression of the enzyme in Escherichia coli has been studied. Complex LB medium, a defined medium (MD) and a semi-complex medium (MSC) have been compared in order to maximize aldolase production. The defined medium produced highest expression levels (700 activity units (AU)/g of dry cell weight (DCW)). The optimal induced isopropyl-β-thiogalactopyranoside (IPTG) concentration of 100 μM produces in the MD medium of 41 μmol/g dry cell weight of enzyme.     

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。     

Identification and Mutational Analysis of <Emphasis Type="Italic">Escherichia coli</Emphasis> Sorbitol-Enhanced Glucose-Repressed <Emphasis Type="Italic">srlA</Emphasis> Promoter Expressed in LB Medium by Using Homologous Recombination and One-Round PCR Products

Escherichia coli has been used for recombinant protein production for many years. However, no native E. coli promoters have been found for constitutive expression in LB medium. To obtain high-expression E. coli promoters active in LB medium, we inserted various promoter regions upstream of eEmRFP that encodes a red fluorescent protein. Among the selected promoters, only colonies of srlA promoter transformants turned red on LB plate. srlA is a gene that regulates sorbitol utilization. The addition of sorbitol enhanced eEmRFP expression but glucose and other sugars repressed, indicating that srlAp is a sorbitol-enhanced glucose-repressed promoter. To analyze the srlAp sequence, a novel site-directed mutagenesis method was developed. Since we demonstrated that homologous recombination in E. coli could occur between 12-bp sequences, 12-bp overlapping sequences were attached to the set of primers that were designed to produce a full-length plasmid, denoted “one-round PCR product.” Using this method, we identified that the srlA promoter region was 100 bp. Further, the sequence adjacent to the start codon was found to be essential for high expression, suggesting that the traditionally used restriction enzyme sites for cloning in the promoter region have hindered expression. The srlA-driven expression system and DNA manipulation with one-round PCR products are useful tools in E. coli genetic engineering.     

Regulated expression systems for the development of whole-cell biocatalysts expressing oxidative enzymes in a sequential manner

This work reports the preparation of two recombinant strains each containing two enzymatic activities mutually expressed through regulated systems for production of functionalized epoxides in one-pot reactions. One strain was Pseudomonas putida PaW340, containing the gene coding for styrene monooxygenase (SMO) from Pseudomonas fluorescens ST under the auto-inducing Ptou promoter and the TouR regulator of Pseudomonas sp. OX1 and the gene coding for naphthalene dihydrodiol dehydrogenase (NDDH) from P. fluorescens N3 under the Ptac promoter inducible by IPTG. The second strain was Escherichia coli JM109, in which the expression of SMO was under the control of the Pnah promoter and the NahR regulator of P. fluorescens N3 inducible by salicylate, while the gene expressing NDDH was under the control of the Plac promoter inducible by IPTG. SMO and NDDH activities were tested in bioconversion experiments using cinnamyl alcohol as reference substrate. The application that we selected is one example of the sequential use of the two enzymatic activities which require a temporal control of the expression of both genes.     

微生物转化连翘苷制备连翘脂素的研究

本文旨在开发一种微生物转化工艺,将连翘苷转化为活性更高的连翘脂素.结果从土壤中分离筛选到一株桔青霉(Penicillium citrinum)LB菌株,转化连翘苷为连翘脂素的专一性较高.经培养基主要组成和转化条件优化,得出较佳的产酶培养组成为:蔗糖7 g/L,(NH4)2 SO45 g/L,NaCl 5 g/L,KH2 PO45 g/L,MgSO41 g/L,MnSO40.5 g/L,pH 6.0.LB菌株经产酶培养后,过滤收集菌体悬浮于2倍发酵液体积的磷酸盐缓冲液中,加入2 g/L的底物连翘苷,于30℃、200 r/min转化20 h,连翘脂素的转化得率可达94.1%.利用微生物将连翘苷转化为连翘脂素,具有方法简单、转化得率高、产物容易纯化和副产物少等优点,有潜在的工业化应用价值.     

Enhanced expression of bovine growth hormone gene by different culture conditions in Escherichia coli

To optimize the production of bovine growth hormone (bGH) in E. coli, the cells harboring pUBJ10 plasmid, which contains the modified 59-coding region of bGH cDNA under the control of trc promoter, was induced to express under various culture conditions such as medium (LB or M9CA), temperature, induction stage, expression time, IPTG concentration, and hosts. Induction stage was effective at early logarithmic phase. The expression levels of bGH were not largely affected by IPTG concentrations, slightly greater in LB medium than in M9CA medium, and efficient in 4 to 6 h of expression time. The highest level of bGH production was obtained in E. coli BL21 strain.     

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.     

Whole-cell hydroxylation of n-octane by Escherichia coli strains expressing the CYP153A6 operon

CYP153A6 is a well-studied terminal alkane hydroxylase which has previously been expressed in Pseudomonas putida and Escherichia coli by using the pCom8 plasmid. In this study, CYP153A6 was successfully expressed in E. coli BL21(DE3) by cloning the complete operon from Mycobacterium sp. HXN-1500, also encoding the ferredoxin reductase and ferredoxin, into pET28b(+). LB medium with IPTG as well as auto-induction medium was used to express the proteins under the T7 promoter. A maximum concentration of 1.85?μM of active CYP153A6 was obtained when using auto-induction medium, while with IPTG induction of LB cultures, the P450 concentration peaked at 0.6–0.8?μM. Since more biomass was produced in auto-induction medium, the specific P450 content was often almost the same, 0.5–1.0?μmol P450 g _DCW ^?1 , for both methods. Analytical scale whole-cell biotransformations of n-octane were conducted with resting cells, and it was found that high P450 content in biomass did not necessarily result in high octanol production. Whole cells from LB cultures induced with IPTG gave higher specific and volumetric octanol formation rates than biomass from auto-induction medium. A maximum of 8.7?g octanol L _BRM ^?1 was obtained within 24?h (0.34?g L _BRM ^?1 ?h^?1) with IPTG-induced cells containing only 0.20?μmol P450 g _DCW ^?1 , when glucose (22?g L _BRM ^?1 ) was added for cofactor regeneration.     

Characterization and evaluation of corn steep liquid in acetone-butanol-ethanol production by Clostridium acetobutylicum

Corn steep liquor (CSL) obtained from a commercial starch manufacturing process was analyzed and tested as a complex nutrient source for ABE (acetone, butanol, and ethanol) production by Clostridium acetobutylicum PJC4BK_AdhE1. CSL contained a wealth of trace elements and nitrogenous components, proteins and amino acids. ABE production increased the content of CSL was raised up to 6% (v/v) in medium and then decreased at higher contents. In 6% CSL-containing medium, C. acetobutylicum PJC4BK_AdhE1 produced 21.4 g/L of ABE with a yield of 0.41 g/g in 18 h of fermentation. Although the final titer of ABE was similar in CSL containing media and Clostridial Growth Medium (CGM, containing yeast extract and asparagines as complex nutrients), the yield and productivity of ABE in 6% CSL-containing medium were found to be higher than 32 and 26%, respectively.     

Construction and co-expression of polycistronic plasmid encoding d-hydantoinase and d-carbamoylase for the production of d-amino acids

d-Hydantoinase and d-carbamoylase genes from Agrobacterium radiobacter TH572 were cloned by polymerase chain reaction (PCR). The plasmid pUCCH3 with a polycistronic structure that is controlled by the native hydantoinase promoter was constructed to co-express the two genes and transformed into Escherichia coli strain JM105. To obtain the highest level of expression of the d-carbamoylase and avoid intermediate accumulation, the d-carbamoylase gene was cloned closer to the promoter and the RBS region in the upstream of it was optimized. This resulted in high active expression of soluble d-hydantoinase and d-carbamoylase that is obtained without any inducer. Thus, by the constitutive recombinant JM105/pUCCH3, d-p-hydroxyphenylglycine (d-HPG) was obtained directly with 95.2% production yield and 96.3% conversion yield.     

Induction of Bacillus subtilis expression system using environmental stresses and glucose starvation

The application of safe and cheap inducers is important in the field of fermentation technology, which persuades employing new expression systems. In this study, a Bacillus subtilis expression system was induced by applying starvation and environmental stresses to produce xylanase. The expression plasmid harbors SigB-dependent ohrB promoter. The target gene was expressed by inoculating the recombinant strain into glucose-limited synthetic medium resulting in a sharp increase of xylanase activity at the end of logarithmic growth phase. The recombinant strain was able to express the xylanase enzyme 14-fold higher than that of the control one. The induction was also performed by exposing the recombinant strain to NaCl and ethanol stresses, and heat shock; the strain growing in LB showed 5-, 15- and 6-fold increases in xylanase activity, respectively. The best induction using environmental stresses was achieved by applying the salt stress in the synthetic medium. The maximum expression for NaCl and ethanol stresses occurred after 40 min of induction. All observed inductions were related to activation of SigB protein causing expression of the SigB-dependent xylanase gene. This SigB-dependent expression system can be considered as a biotechnology tool and an alternative to eliminate the cost of conventional inducers.     

Enhanced hydantoin-hydrolyzing enzyme activity in an Agrobacterium tumefaciens strain with two distinct N-carbamoylases

Hydantoin-hydrolyzing enzymes of Agrobacterium tumefaciens isolates such as strain RU-OR are used as biocatalysts in the commercial production of d-hydroxyphenylglycine via hydrolysis of d, l-p-hydroxyphenylhydantoin. Hydantoin-hydrolyzing enzyme activity in RU-OR cells is tightly regulated by nitrogen catabolite repression and is induced when hydantoin or a hydantoin-analogue is present in the growth medium. Previous studies have selected mutant strains which are inducer-independent and no longer subject to nitrogen catabolite expression. However, these mutants did not exhibit significantly higher levels of enzyme activity compared to the wild-type strain. In this study, we have focused on enhancing the levels of hydantoinase and N-carbamoylase activity in wild-type RU-OR cells by manipulating the growth medium or over-expressing the global nitrogen regulatory factors, NtrBC. We also show that this strain encodes two distinct d-selective N-carbamoylases. One enzyme is virtually identical to the other Agrobacterium N-carbamoylases while the second represents a new class of d-N-carbamoylases with potentially novel biocatalytic properties.     

Gene expression usingnar promoter under anaerobic condition with recombinantE. coli

Thenar promoter as an inducible promoter was characterized for the process development for the gene expression and the protein production under anaerobic condition. The LB medium was selected as a main culture medium showing the enzyme activity of 18,000 units/min/g cell in the flask cultivation. The optimum concentration of nitrate was 1%. Under anaerobic conditions, the gene expression was fully induced in the presence of nitrate.     

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。     

Engineering a repression-free catabolite-enhanced expression system for a thermophilic alpha-amylase from Bacillus licheniformis MSG

Most expression systems used for the over production of many enzymes employ carbon catabolite repressible promoters and hence must use sugar free, rich complex media. Use of expression systems to overcome carbon repression opens an avenue for exploiting cheap carbon sources for the production of recombinant enzymes. A self-inducible, catabolite repression free and above all a glucose-activated expression system has been developed using an industrially suitable thermophilic alpha-amylase as a model. The alpha-amylase gene of Bacillus licheniformis MSG without the 5' cre operator produced unimpeded glucose-enhanced expression when fused to the phosphate starvation-inducible strong pst promoter with optimum translation signals in a protease deficient Bacillus subtilis. A combination of high glucose with limited phosphate permitted sufficient biomass and fast transition to quiescent phase by phosphate starvation permitting 1250-fold induction for 70 h. A ~300-fold high productivity (9070 U mL^-1) and 131-fold increase in specific expression in 2% glucose and a 100-fold high yield in 4% molasses were obtained compared to the production by the parent strain. The yield was 18.5-fold higher than that from the native promoter in an isogenic clone. This strategy of catabolite enhanced enzyme expression uncoupled from biomass formation can be applied for cost effective high production of proteins using starch or molasses.     

Efficient production of Thermus protease aqualysin I in Escherichia coli: effects of cloned gene structure and two-stage culture

 The DNA sequence encoding Thermus protease aqualysin I was inserted downstream from a bacteriophage T7 promoter in an expression vector. In the T7 expression system, using a strain lacking an F′ episome, aqualysin I was produced in soluble form without chemical induction. The deletions of part (30 amino acid residues) or all (105 residues) of the C-terminal pro-sequence from the C terminus significantly affected both cellular growth and the production of the enzyme. Complete deletion adversely affected both. In contrast, the 30-residue deletion markedly improved productivity by approximately four times compared to non-deletion, and shortened the time needed for the activation of a precursor to active enzyme. The concentration of inducer isopropyl β-D-thiogalactopyrano-side (IPTG) was varied to examine its effects, and it was found that a low concentration of IPTG improved aqualysin I production. To avoid the inhibitory effects of acetic acid accumulation in the culture medium, the use of other carbon sources besides glucose was examined. When cells were cultivated with glycerol, the acetic acid level remained relatively low, and both good cellular growth and a high level of production were attained. The aqualysin I productivity for a fed-batch culture using two carbon sources, glucose and glycerol, reached more than 150 kU/ml enzymatically active aqualysin I. Received: 19 May 1995/Received revision: 28 July 1995/Accepted: 22 August 1995     

Statistical evaluation and modeling of cheap substrate-based cultivation medium of Chlorella vulgaris to enhance microalgae lipid as new potential feedstock for biolubricant

Chlorella vulgaris (C. vulgaris) microalga was investigated as a new potential feedstock for the production of biodegradable lubricant. In order to enhance microalgae lipid for biolubricant production, mixotrophic growth of C. vulgaris was optimized using statistical analysis of Plackett–Burman (P-B) and response surface methodology (RSM). A cheap substrate-based medium of molasses and corn steep liquor (CSL) was used instead of expensive mineral salts to reduce the total cost of microalgae production. The effects of molasses and CSL concentration (cheap substrates) and light intensity on the growth of microalgae and their lipid content were analyzed and modeled. Designed models by RSM showed good compatibility with a 95% confidence level when compared to the cultivation system. According to the models, optimal cultivation conditions were obtained with biomass productivity of 0.123 g L^?1 day^?1 and lipid dry weight of 0.64 g L^?1 as 35% of dry weight of C. vulgaris. The extracted microalgae lipid presented useful fatty acid for biolubricant production with viscosities of 42.00 cSt at 40°C and 8.500 cSt at 100°C, viscosity index of 185, flash point of 185°C, and pour point of ?6°C. These properties showed that microalgae lipid could be used as potential feedstock for biolubricant production.     

Addition of Co2+ to culture medium decides the functional expression of a recombinant nitrile hydratase in Escherichia coli

A nitrile hydratase (NHase) gene from Aurantimonas manganoxydans, cloned and expressed in Escherichia coli, gave an enzyme that efficiently hydrated 3-cyanopyridine to nicotinamide with high thermal stability. We have now found that adding Co²⁺ at 0.1 mM to LB medium was essential for production of an active enzyme. However, ≥0.3 mM Co²⁺ inhibited the growth of host cells in LB medium and decreased the production of the recombinant NHase. Furthermore, β-mercaptoethanol promoted regeneration of the Co²⁺-defective apoenzyme in vitro possibly by breaking a key disulfide bond thereby promoting the incorporation of Co²⁺ into the apoenzyme.