Production of acrylamide using immobilized cells of<Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> M33

The cellsof Rhodococcus rhodochrous M33, which produce a nitrile hydratase enzyme, were immobilized in acrylamide-based polymer gels. The optimum pH and temperature for the activity of nitrile hydratase in both the free and immobilized cells were 7.4 and 45°C, respectively, yet the optinum temperature for acrylamide production by the immobilized cells was 20°C. The nitrile hydratase of the immobilized cells was more stable with acrylamide than that of the free cells. Under optimal conditions, the final acrylamide concentration reached about 400 g/L with a conversion yield of almost 100% after 8 h of reaction when using 150 g/L of immobilized cells corresponding to a 1.91 g-dry cell weight/L. The enzyme activity of the immobilized cells rapidly decreased with repeated use. However, the quality of the acrylamide produced by the immobilized cells was much better than that produced by the free cells in terms of color, salt content, turbidity, and foam formation. The quality of the aqueous acrylamide solution obtained was found to be of commercial use without further purification.     

Rhodococcus pyridinovorans MW3, a bacterium producing a nitrile hydratase

Rhodococcus pyridinovorans MW3 was isolated from an arable land of manioc from the Congo for its ability to transform acrylonitrile to acrylamide. This strain contains a cobalt nitrile hydratase (NHase) showing high sequence homology with NHases so far described. The specific NHase activity was 97 U mg(-1) dry wt. NHase production by R. pyridinovorans MW3 was urea and Co-dependent. The NHase was active for acrylamide up to 60% (w/v) indicating its potential for acrylamide production.     

Purification of a hyperactive nitrile hydratase from resting cells of Rhodococcus rhodochrous PA-34

A propionitrile-induced nitrile hydratase (NHase), a promising biocatalyst for synthesis of organic amides has been purified from cell-free extract of Rhodococcus rhodochrous PA-34. About 11-fold purification of NHase was achieved with 52% yield. The SDS-PAGE of the purified enzyme revealed that it consisted of two subunits of 25.04 kD and 30.6 kD. However, the molecular weight of holoenzyme was speculated to be 86 kD by native-PAGE. This NHase exhibited maximum activity at pH 8.0 and temperature 40°C. Half-life was 2 h at 40°C and 0.5 h at 50°C. The Km and Vmax were 167 mM and 250 μmole/min/mg using 25 mM 3-cyanopyridine as substrate. AgNO₃, Pb(CH₃COO)₂ and HgCl₂ inhibited the NHase to extent of 89–100%.     

Cobalt-dependent transcription of the nitrile hydratase gene in Rhodococcus rhodochrous M8

Abstract The effects of cobalt ions on the activities of Rhodococcus rhodochrous M8 enzymes for nitrile utilization, nitrile hydratase and amidase, were investigated. In contrast to amidase, synthesis of nitrile hydratase and its activity required cobalt ions in the growth medium. Northern blot analysis showed that in the presence of cobalt ions, the level of mRNA for nitrile hydratase genes was several times higher than that under cobalt-limited conditions. It was assumed that the low nitrile hydratase activity in cells grown in the absence of cobalt ions is connected either with the weak expression of nitrile hydratase genes or with the rapid degradation of nitrile hydratase mRNA.     

Expression of nitrile hydratase gene of mutant 4D strain of Rhodococcus rhodochrous PA 34 in Pichia pastoris

The nitrile hydratase (NHase) gene of Rhodococcus rhodochrous PA-34 mutant 4D has been amplified by PCR, cloned and expressed in Pichia pastoris KM-71 using pHIL-D2 expression vector. The recombinant P. pastoris KM-71 exhibited active expression of the nitrile hydratase gene of the mutant 4D and has shown very good potential for the transformation of 3-cyanopyridine to nicotinamide. The recombinant P. pastoris KM-71 exhibited maximum NHase activity when cultivated in YPD medium was supplemented with 0.4?mM cobalt ions. The recombinant P. pastoris KM-71 showed maximum nitrile hydratase enzyme production, when incubated at 30?°C for 15?h.     

红球菌低分子量型腈水合酶的异源激活及激活子的结构域功能

腈水合酶激活子具有亚基自身交换伴随子或者金属离子伴随子的功能,能够辅助腈水合酶摄取金属离子,对于腈水合酶的活性表达必不可少。与腈水合酶自身相比,激活子的序列保守性低,研究其激活作用的特点,探索其结构与功能之间的关系,对于理解腈水合酶的成熟机制具有重要意义。将红球菌Rhodococcus rhodochrous J1低分子量型腈水合酶L-NHase分别与4种异源激活子组合共表达,测定异源激活子对L-NHase的激活作用,进一步对激活子进行序列分析和结构模拟,并研究关键结构域的功能。结果表明,4种异源激活子均能激活L-NHase,但激活后L-NHase的比酶活存在差异,激活子A对L-NHase的激活程度最高,激活后的L-NHase比酶活为出发酶的97.79%;激活子G对L-NHase的激活程度最低,激活后的L-NHase比酶活为出发酶的23.94%。激活子E和激活子G具有保守结构域TIGR03889,缺失其中部分序列会使两者的激活作用基本丧失。将激活子G的N端序列替换为激活子E的N端序列,并将激活子E的C端序列添加至激活子G的C端,能够使L-NHase的比酶活提高178.40%。激活子的激...     

微生物法生产丙烯酰胺的研究（Ⅰ）—腈水合酶产生菌株的培养和高活力的表达

研究了丙烯酰胺生产菌株的培养条件。通过对培养过程pH值调控、培养基补料以及诱导剂加入量的研究,使发酵液的腈水合酶的活力达到了6567u/mL菌液。这一酶活是国内外所见报道中最高的。进一步进行了丙烯腈的酶催化水合实验,产物中并没有发现副产物丙烯酸,说明在提高腈水合酶的同时,酰胺酶的活力并没有明显体现这一试验结果为工厂化生产改造以及新工艺的研究打下了基础。     

Rhodococcus rhodochrous J1腈水合酶在大肠杆菌中的表达策略

针对红球菌低分子量腈水合酶（L—NHase）在重组茵中难以表达这一问题,通过对其d亚基及调控蛋白NhlE基因的核糖体结合位点和0c,口亚基间隔序列的长度进行改造,构建了重组表达载体,实现了L．NHase及其调控蛋白NhlE在E．coliB121（DE3）中过量表达。通过培养条件优化,得到最佳表达条件为：37℃培养茵体浓度（DD600）到1．0时,加入终浓度为0．1g／L的CoCl2·6H,0,0．6mmol／L的IPTG,然后在24℃下诱导表达24h。最终得到的重组蛋白粗酶液的活性为（109．9-I-5．5）U／rag。采用Strep．tag／Strep—Tactin亲和层析简化了L-NHase的纯化方法,本研究结果为一些难于异源重组表达的多亚基蛋白质的表达具有一定的借鉴意义。     

Optimum culture conditions for the production of benzonitrilase by Rhodococcus rhodochrous J1

We sought the optimum conditions for the production of benzonitrilase by Rhodococcus rhodochrous J1. The use of isovaleronitrile or isobutyronitrile as an inducer greatly enhanced benzonitrilase formation. When Rhodococcus rhodochrous J1 was cultivated at 28°C for 96 h in a medium consisting of 0.1 ml of isovaleronitrile, 0.5 g of polypeptone, 0.3 g of malt extract, 0.3 g of yeast extract and 1 g of glycerol per 100 ml of tap water (pH 7.2), and isovaleronitrile was fed twice at the concentrations of 0.1% (v/v) and 0.2% (v/v) at 55 h and 77 h, respectively, during the course of cultivation, the enzyme activity in the culture broth reached approximately 3,100-times higher than the initially obtained level.     

Isolation and purification of methyl mercaptan oxidase fromRhodococcus rhodochrous for mercaptan detection

Methyl mercaptan oxidase was successfully induced fromRhodococcus rhodochrous IGTS8 using methyl mercaptan gas and purified to homogeneity for the detection of mecrcaptans. The purification procedure involved DEAE-Sephacel and Superose 12 column chromatography with recovery yields of 85.8 and 83.3%, and a specific activity of 92.7 and 303.4 units/mg-protein, respectively. The molecular weight of purified methyl mercaptan, oxidase was determined to be 64.5 kDa by SDS-PAGE. The extract from gel filtration chromatography oxidizes methyl mercaptan to produce formaldehyde, which can be easily detected by the purpald-coloring method. Optimum temperature for activity was achieved at 60°C. This enzyme was inhibited by both K₂SO₄ and NaCl at concentration of less than 100 mM and recovered to original activity at concentration of 200 mM. In the presence of methanol, the activity decreased by 33%.     

微生物法生产丙烯酰胺的研究（Ⅱ）—腈水合酶催化反应动力学与失活动力学

在以丙烯腈为原料 ,微生物转化生产丙烯酰胺的过程中 ,酶催化反应是过程的关键。为了了解酶催化的动力学 ,本研究以自由细胞的酶为催化剂 ,进行了腈水合酶的反应动力学和失活动力学的研究。首先研究了菌体浓度、温度、pH值、丙烯腈浓度、丙烯酰胺浓度等对腈水合酶催化反应速度的影响。结果表明 ,在这些因素中 ,温度和丙烯酰胺浓度是最主要的影响因素。 2 8℃时酶活为 5 6 5 9u mL(菌液 ) ,在 5℃时的反应速率仅为 2 8℃时的11 72 % ,相应的表观酶活为 6 6 3u mL(菌液 )。而在丙烯酰胺 45 %浓度条件下的酶活大约只有丙烯酰胺 5 %浓度下的酶活的 1 2。经过对不同温度下的反应速度的研究 ,得到腈水合酶水合反应的活化能为 6 5 5 7kJ·mol- 1 。本文进一步研究了自由细胞状态下 ,菌体浓度、pH值、温度、丙烯腈浓度、丙烯酰胺浓度对腈水合酶失活的影响 ,得到了失活动力学。结果表明 ,在这些因素中 ,对酶失活影响的最主要因素还是温度和丙烯酰胺浓度。尤其当丙烯酰胺浓度到达 35 %时 ,酶活下降得很快 ,在 5 5h后 ,酶活几乎为零。而在丙烯酰胺浓度为 10 %的情况下 ,5 5h的酶活仍然还存在约 5 0 %。试验结果还表明 ,丙烯腈对酶的稳定性的影响很小。经过数据处理 ,得到的 2 8℃的酶失活速率常数为 5℃下的 2 1 7     

Biochemical characterization of Rhodococcus erythropolis N′4 nitrile hydratase acting on 4-chloro-3-hydroxybutyronitrile

The Rhodococcus erythropolis strain (N′4) possesses the ability to convert 4-chloro-3-hydroxybutyronitrile into the corresponding acid. This conversion was determined to be performed by its nitrile hydratase and amidase. Ammonium sulfate fractionation, DEAE ion exchange chromatography, and phenyl chromatography were used to partially purify nitrile hydratase from cell-free extract. A SDS-PAGE showed that the partially purified enzyme had two subunits and gel filtration chromatography showed that it consisted of four subunits of α₂β₂. The purified enzyme had a high specific activity of 860 U mg⁻¹ toward methacrylonitrile. The enzyme was found to have high activity at low temperature range, with a maximum activity occurring at 25 °C and be stable in the presence of organic acids at higher temperatures. The enzyme exhibited a preference for aliphatic saturated nitrile substrates over aliphatic unsaturated or aromatic ones. It was inhibited by sulfhydryl, oxidizing, and serine protease inhibitors, thus indicating that essential cysteine and serine residues can be found in the active site.The purified nitrile hydratase was able to convert 4-chloro-3-hydroxybutyronitrile into the corresponding amide at 15 °C. GC analysis showed that the initial conversion rate of the reaction was 215 mg substrate consumed min⁻¹ mg⁻¹. This demonstrated that this enzyme could be used in conjunction with a stereoselective amidase to synthesize ethyl (S)-4-chloro-3-hydroxybutyrate, an intermediate for a hypercholesterolemia drug, Atorvastatin.     

Fluorene Cometabolism by Rhodococcus rhodochrous and Pseudomonas fluorescens Cultures

The transformation of fluorene by Rhodococcus rhodochrous strain 172 grown on sucrose and Pseudomonas fluorescens strain 26K grown on glycerol was studied as a function of the substrate concentration and the growth phase. Under certain cultivation conditions, fluorene was completely consumed from the medium. The specific transformation rate of fluorene was considerably higher when it was transformed in the presence of the cosubstrates than when it served as the sole carbon source. An approach to the evaluation of the specific transformation rate of fluorene during batch cultivations is proposed.     

Draft genome sequence of Rhodococcus rhodochrous strain ATCC 17895

Rhodococcus rhodochrous ATCC 17895 possesses an array of mono- and dioxygenases, as well as hydratases, which makes it an interesting organism for biocatalysis. R. rhodochrous is a Gram-positive aerobic bacterium with a rod-like morphology. Here we describe the features of this organism, together with the complete genome sequence and annotation. The 6,869,887 bp long genome contains 6,609 protein-coding genes and 53 RNA genes. Based on small subunit rRNA analysis, the strain is more likely to be a strain of Rhodococcus erythropolis rather than Rhodococcus rhodochrous.     

Biotransformation of benzonitrile to benzohydroxamic acid by Rhodococcus rhodochrous in the presence of hydroxylamine

Whole cells of the bacterium Rhodococcus rhodochrous LL100-21, which had been grown on benzonitrile to induce the nitrilase enzyme, converted benzonitrile to benzohydroxamic acid in the presence of hydroxylamine.     

Bench scale conversion of 3-cyanopyidine to nicotinamide using resting cells of <Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> PA-34

The nitrile hydratase (NHase, EC 3.5.5.1) activity of Rhodococcus rhodochrous PA-34 was explored for the conversion of 3-cyanopyridine to nicotinamide. The NHase activity (∼18 U/mg dry cell weight, dcw) was observed in 0.1 M phosphate buffer, pH 8.0 containing 1M 3-cyanopyridine as substrate, and 0.75 mg of resting cells (dry cell weight) per ml reaction mixture at 40°C. However, 25°C was more suitable for prolonged batch reaction at high substrate (3-cyanopyridine) concentration. In a batch reaction (1 liter), 7M 3-cyanopyridine (729 g) was completely converted to nicotinamide (855 g) in 12h at 25°C using 9.0 g resting cells (dry cell weight) of R. rhodochrous PA-34.     

Effect of agitation and aeration on the production of nitrile hydratase by Rhodococcus erythropolis MTCC 1526 in a stirred tank reactor

Aims: To evaluate the effect of different physicochemical parameters such as agitation, aeration and pH on the growth and nitrile hydratase production by Rhodococcus erythropolis MTCC 1526 in a stirred tank reactor. Methods and Results: Rhodococcus erythropolis MTCC 1526 was grown in 7‐l reactor at different agitation, aeration and controlled pH. The optimum conditions for batch cultivation in the reactor were an agitation rate of 200 rev min^?1, aeration 0·5 v/v/m at controlled pH 8. In this condition, the increase in nitrile hydratase activity was almost threefold compared to that in the shake flask. Conclusion: Agitation and aeration rate affected the dissolved‐oxygen concentration in the reactor which in turn affected the growth and enzyme production. Significance and Impact of the Study: Cultivation of R. erythropolis MTCC 1526 in the reactor was found to have significant effect on the growth and nitrile hydratase production when compared to the shake flask.     

Hydration of 3-cyanopyridine to nicotinamide by crude extract nitrile hydratase

Summary The kinetic and stability characteristics of crude extract nitrile hydratase fromBrevibacterium R-312 were studied for the hydration of 3-cyanopyridine to nicotinamide. The enzyme was substrate and product inhibited and had the following kinetic constants:K _m =28 mM;K _p =36 mM;K _s =155 mM;V _m =5.8 mol/min/mg protein (25°C). Itsmaximum temperature and pH (phosphate buffer) were 35°C and 8.0, respectively and it had half-lives of 50 days, 10 days and 1 day at 4°C, 10°C and 25°C, respectively. The crude extract also exhibited amidase activity on nicotinamide, but it became significant only at nicotinamide concentrations greater than 300 mM. Mathematical models for batch and fed-batch hydrations were developed to account for substrate and product inhibitions and for enzyme decay. They predicted to within 10% experimental results for initial substrate and final product concentrations up to 300 mM; the accuracies decreased at higher concentrations primarily because of the relatively rapid hydrolysis of nicotinamide.     

Asymmetric hydrolysis of R-(−),S(+)-2-methylbutyronitrile by Rhodococcus rhodochrous NCIMB 11216

Whole cells and cell-free extracts derived from Rhodococcus rhodochrous NCIMB 11216 were shown to hydrolyse both aliphatic and aromatic nitriles, when the organism had been grown on either propionitrile or benzonitrile as the source of carbon and nitrogen. Whole cell suspensions and cell-free extracts derived from bacteria grown on either substrate were able to biotransform R-(-),S-(+)-2-methylbutyronitrile. The S-(+) enantiomer was biotransformed more rapidly than the the R-(-) enantiomer. For whole cell biotransformations at 30°C, the maximum enantiomeric excess (ee) of the remaining R-(-)-2-methylbutyronitrile was 93% when 70% of the R-(-) enantiomer had been converted to the product, 2-methylbutyric acid. For the corresponding biotransformation at 4°C, there was an ee of 93% for the residual R-(-) enantiomer of the substrate when only 60% of it had been converted to product. For biotransformations by cell-free extracts at 30°C the 2-methylbutyric acid product had an ee of 17% for the S-(+) enantiomer at the time of optimal ee for the remaining R-(-) enantiomer of the substrate. In contrast, when the reaction was carried out by whole cells, the ee for the product acid was 0.36%. This was probably due to further, non-selective metabolism of the acid, which was especially significant at the beginning of the reaction. At both temperatures, the ee for the S-(+) enantiomer of 2-methylbutyric acid was at a maximum in the early stage of the biotransformation; for example, at 4°C the maximum detectable ee was 100% when the yield was 11%.Abbreviations EDTA Ethylenediaminetetraacetic acid - ee enantiomeric excess - FID flame ionisation detector - GC gas chromatography - ¹HNMR H nuclear magnetic resonance - K _m Michaelis constant - NCIMB National Collection of Industrial and Marine Bacteria - td doubling time - V _max Maximum velocity     

Fed-batch fermentation of Lactobacillus lactis for hyper-production of l-lactic acid

A fed-batch fermentation of Lactobacillus lactis to produce l-lactic acid was developed in which the residual glucose concentration in the culture was used to control a continuous feeding strategy. Up to 210 g l-lactic acid l^–1 (97% yield) was obtained. The maximal dry cell was 2.7 g l^–1 and the average l-lactic acid productivity was 2.2 g l^–1 h^–1.