Encapsulation in LentiKats of Dextransucrase from Leuconostoc mesenteroides NRRL B-1299, and its Effect on Product Selectivity

Insoluble (cell-bound) dextransucrase from Leuconostoc mesenteroides B-1299 was encapsulated in highly elastic and stable hydrogels formed by polyvinyl alcohol. The gelation was carried out by controlled partial drying at room temperature, resulting in lens-shaped particles, called LentiKats. A similar recovery of activity (approximately 55%) was achieved when compared with entrapment in calcium alginate gels. Under reaction conditions, the protein leakage in LentiKats was reduced from 18% to 4% by pre-treatment of the dextransucrase with glutaraldehyde. The immobilized dextransucrases were tested in the acceptor reaction with methyl α-D-glucopyranoside. The conversion to oligosaccharides using Lentikat-dextransucrase was higher than that obtained for alginate-dextransucrase, probably due to the reduction of diffusional limitations derived from its lenticular shape. In addition, a shift of selectivity towards the synthesis of oligosaccharides containing α(1→2) bonds was observed for the Lentikat-biocatalysts. These non-digestible compounds are supposed to be specifically fermented by beneficial species of the human microflora (prebiotic effect). The Lentikat-entrapped dextransucrase can be efficiently reused in this process at least for five cycles of 24 h.     

Immobilization of oxalate decarboxylase to Eupergit and properties of the immobilized enzyme

Oxalate decarboxylase, an oxalate degradation enzyme used for medical diagnosis and decreasing the oxalate level in the food or paper industry, was covalently immobilized to Eupergit C. Different immobilization parameters, including ratio of enzyme to support, ammonia sulfate concentration, pH, and incubation time, were optimized. Under the condition of enzyme/support ratio at 1:20, pH 9, with 1.5?mol/L (NH(4))(2)SO(4), room temperature, and shaking at 30?rpm for 24?hr, activity recovery of immobilized Oxdc reached 90% with an apparent specific activity of 0.44?U/mg support. The enzymatic properties of immobilized Oxdc were investigated and compared with those of the soluble enzyme. Both shared a similar profile of optimum conditions; the optimum pH and temperature for soluble and immobilized Oxdc were 3.5 and 50°C, respectively. The immobilized enzyme was more stable at lower pH and higher temperatures. The kinetic parameters for soluble and immobilized enzyme were also determined.     

无载体固定化酵母细胞木薯淀粉质原料酒精连续发酵研究

以木薯粉糖化液为发酵底物,在总发酵体积(有效)为15L的悬浮床生物反应器中,对一株粟酒裂殖酵母变异株进行一级和二级连续发酵研究。结果表明,二级连续发酵系统可明显改善一级系统的不足,并取得了平均流加糖液浓度150g/L,发酵强度为97g/L.h,流出液酒精浓度727g/L,残糖浓度374g./L,总糖利用率达90%的较好结果;整个系统在连续一个月的运行中从未发现染菌现象,发酵操作稳定。     

Lipase catalyzed acetylation of 3,5,4′-trihydroxystilbene: optimization and kinetics study

The use of immobilized lipase from Candida antarctica (Novozym(?) 435) to catalyze acetylation of trans-3,5,4'-trihydroxystilbene was investigated in this study. Response surface methodology and 5-level-4-factor central composite rotatable design were adopted to evaluate the effects of synthesis variables, including reaction time (24-72 h), temperature (25-65 °C), substrate molar ratio (1:15-1:75), and enzyme amount (600-3,000 PLU) on the percentage molar conversion of trans-4'-O-acetyl-3,5-dihydroxystilbene. The results showed that reaction temperature and enzyme amount were the most important parameters on percentage molar conversion. Based on ridge max analysis, the optimum conditions for synthesis were: reaction time 60 h, reaction temperature 64 °C, substrate molar ratio 1:56 and enzyme amount 2,293 PLU. The molar conversion of actual experimental values was 95% under optimal conditions. The synthesis product was analyzed using HPLC, mass and NMR. The results revealed that the major product was trans-4'-O-acetyl-3,5-dihydroxystilbene. The reaction kinetics was found to follow the Ping-Pong mechanism; substrate inhibition was not found at high vinyl acetate concentration.     

Evaluation of immobilized lipases on poly-hydroxybutyrate beads to catalyze biodiesel synthesis

Five microbial lipase preparations from several sources were immobilized by hydrophobic adsorption on small or large poly-hydroxybutyrate (PHB) beads and the effect of the support particle size on the biocatalyst activity was assessed in the hydrolysis of olive oil, esterification of butyric acid with butanol and transesterification of babassu oil (Orbignya sp.) with ethanol. The catalytic activity of the immobilized lipases in both olive oil hydrolysis and biodiesel synthesis was influenced by the particle size of PHB and lipase source. In the esterification reaction such influence was not observed. Geobacillus thermocatenulatus lipase (BTL2) was considered to be inadequate to catalyze biodiesel synthesis, but displayed high esterification activity. Butyl butyrate synthesis catalyzed by BTL2 immobilized on small PHB beads gave the highest yield (≈90 mmol L(-1)). In biodiesel synthesis, the catalytic activity of the immobilized lipases was significantly increased in comparison to the free lipases. Full conversion of babassu oil into ethyl esters was achieved at 72 h in the presence of Pseudozyma antarctica type B (CALB), Thermomyces lanuginosus lipase (Lipex(?) 100 L) immobilized on either small or large PHB beads and Pseudomonas fluorescens (PFL) immobilized on large PHB beads. The latter preparation presented the highest productivity (40.9 mg of ethyl esters mg(-1) immobilized protein h(-1)).     

Covalent immobilization of Kluyveromyces fragilis β-galactosidase on magnetic nanosized epoxy support for synthesis of galacto-oligosaccharide

The novel magnetic nanobeads with epoxy groups on the surface were prepared from glycidyl methacrylate (GMA), ethylene glycol dimethacrylate (EGDMA) and hydroxyethyl methacrylate (HEMA) via emulsifier-free emulsion polymerisation, and they were characterized by scanning electron microscopy and vibrating sample magnetometer. The magnetic poly(GMA-EDGMA-HEMA) nanobeads were used as support for covalent immobilization of Kluyveromyces fragilis β-galactosidase, the maximum amount enzyme attached onto the support was 145.6?mg/g with activity recovery of 72.6%. The loading capacity of this novel support for K. fragilis β-galactosidase was improved 2.6-folds compared with Eupergit(?) C (commercial epoxy support). The immobilized K. fragilis β-galactosidase exhibited high catalytic activity for the reaction of galacto-oligosaccharide (GOS) synthesis, and a total of 2,240?g GOS were produced per gram of immobilized enzyme during consecutive batch reaction of 10 times. The immobilized biocatalyst retained 81.5% of its original activity after 10 reaction cycles.     

非水体系中脂肪酶催化合成乳酸乙基糖苷酯的工艺研究

在非水体系中 ,通过固定化脂肪酶催化合成一种新型α 羟基酸衍生物 乳酸糖苷酯。考察了常压下有机溶剂、酰基供体、不同种固定化酶、乙基糖苷的浓度、酶量和反应温度对反应的影响。研究表明在无溶剂体系中以乳酸丁酯作为酰基供体可有效地合成乳酸糖苷酯 ,固定化酶Novozym435和来源于Candida sp .菌株的细胞固定化酶 ,化学修饰的干酶粉均是合适的催化剂。最佳反应条件为 :酶浓度 75g L ,乙基葡萄糖苷的浓度为 0.4mol L ,温度为 70℃ ,转速 200r min ,反应 50h ,转化率可达 71%。在真空度为 0.09MPa的压力下 ,反应温度 65℃ ,酶浓度 75g L ,乙基葡萄糖苷 0.35mol L时 ,反应初速率可达到 607(mmol·L^-1·h^-1 ) ,40h后转化率可达到 90%。反应产物经过萃取法和硅胶柱层析方法分离 ,纯度达到 95 % (W/W)。     

Thermophilic esterase from the archaeon Archaeoglobus fulgidus physically immobilized on hydrophobic macroporous resin: A novel biocatalyst for polyester synthesis

This paper reviews the immobilization of a thermophilic esterase, AFEST from the archaeon Archaeoglobus fulgidus, on a hydrophobic macroporous resin and its application in polyester synthesis using the ring-opening polymerization of ?-caprolactone as a model. Using the physical adsorption technique, the AFEST loading concentration after 24 h was 152 mg AFEST per g of support. Particle size and surface morphology of the immobilized enzyme were investigated using laser scattering analysis and scanning electron microscopy. The effects of enzyme concentration, temperature, reaction time and reaction medium on monomer conversion and product molecular weight were systematically investigated. Through the optimization of reaction parameters, poly(?-caprolactone) was obtained at an almost 100% monomer conversion rate and with a low average molecular weight (< 1,100 g/mol). Finally, the immobilized enzyme exhibited good operational stability, with a monomer conversion value of more than 55% after four batch reactions.     

Enzymatic synthesis of γ-glutamylmethylamide from L-glutamylhydrazine and methylamine catalysed by immobilized recombinant γ-glutamyltranspeptidase

In many organisms, γ-glutamylmethylamide is a significant amino acid constituent. In this research, a novel method of γ-glutamylmethylamide synthesis is presented. The synthesis of γ-glutamylmethylamide was catalysed by immobilized recombinant γ-glutamyltranspeptidase and used L-glutamylhydrazine as an economical substrate. The optimal enzymes and γ-glutamyltranspeptidase reaction conditions for the production of γ-glutamylmethylamide were 200?mM L-glutamylhydrazine, 1?M methylamine, and 0.1?g/ml immobilized γ-glutamyltranspeptidase cells at pH 10 and 37?°C for 10?h. The immobilized γ-glutamyltranspeptidase cells were used for 10 reactions, and the average conversion ratio from L-glutamylhydrazine to γ-glutamylmethylamide reached 93.2%. The activity of immobilized recombinant γ-glutamyltransferase was not inhibited by 200?mM L-glutamylhydrazine. The immobilized γ-glutamyltranspeptidase cells exhibited favourable operational stability.     

Improvement of lipase activity by synergistic immobilization on polyurethane and its application for large-scale synthesizing vitamin A palmitate

Abstract

We have developed an improved and effective method to immobilize lipase on hydrophobic polyurethane foam (PUF) with different modifications. PUF was treated with hydrochloric acid to increase the active sites and then the active carboxyl groups and amino groups were exposed. Enzyme activity of lipase immobilized on PUF-HCL (8000?U/g) was 50% higher than that of lipase immobilized on PUF (5300?U/g). There is an increase in the activity of the immobilized lipase on AA/PEI-modified support (115,000?U/g), a 2.17-fold increase compared to lipase immobilized on the native support was observed. The activity of immobilized lipases was dependent on the PEI molecular weight, with best results from enzyme immobilized on PUF-HCL-AA/PEI (MW 70,000?Da, 12,800?U/g)), which was 2.41 times higher compared to that of the same enzyme immobilized on PUF. These results suggest that the activity of immobilized lipase is influenced by the support surface properties, and a moderate support surface micro-environment is crucial for improving enzyme activity. Finally, the immobilized lipase was used for the production of vitamin A palmitate. The immobilized lipase can be reused for up to 18 times with a conversion rate above 90% for 12?h in a 3?L bioreactor.

• Research highlights

• An efficient immobilization protocol on polyurethane foam was developed

• Polyethyleneimine and acetic acid were used to regulate the micro-environment concurrently

• The activity of lipase immobilized on PUF-HCL-AA/PEI was improved by 2.41 times

• Immobilized lipase exhibited excellent operational stability for vitamin A palmitate synthesis

     

Enhancing the biocatalytic potential of carbonyl reductase of Candida viswanathii using aqueous-organic solvent system

In the present work, the toxic effect of various solvents with different Log P values was studied on the whole cells of Candida viswanathii. Experiments showed that the lower concentrations of some solvent increased both the activity retention and enzyme activity as compared to the control while this was not the case with higher concentrations of the same solvents. The model compound taken in the present study was 1-acetophenone. The percentage conversion improved from 76 to 94%. Addition of 2-propanol increased the substrate tolerance, giving the conversion of 90% compared to 9% in control at a substrate concentration of 70 mM in 1h. The operational stability increased at higher temperatures with the addition of 2-propanol in the reaction mixture with good conversion (90%) and enantiomeric excess (>99%) at 45 degrees C and 50 degrees C. The effect was also found to be prominent in other tested substrates. In order to further stabilize the cells for long term use in higher concentration of organic solvents, the cells were further immobilized, and were found to have higher activity retention than that of free cells.     

Improved octyl glucoside synthesis using immobilized β-glucosidase on PA-M with reduced glucose surplus inhibition

A β-glucosidase extracted from bitter almond (Prunus dulcis var. amara) was immobilized on polyamine microspheres (PA-M) for catalytic octyl glucoside (OG) synthesis from glucose and octanol through reversed hydrolysis. The immobilization increased the activity of enzyme at pH 6.0–7.0, and the optimal reaction temperature for immobilized enzyme was identical to the free enzyme. The thermal stability and solvent tolerance of enzyme were increased by its immobilization. In the co-solvent system using 10% t-butyl alcohol and 10% (v/v) water, the yield of OG was increased by 1.7-fold compared to the yield from the system without co-solvent. Based on dynamic and Dixon plot analyses, the initial reaction velocity (V₀) increased approximately three-fold on immobilization and the OG synthesis was inhibited by surplus glucose. The inhibition dissociation constants for free and immobilized enzyme were 219?mM and 116?mM, respectively. A fed-batch mode was applied in the OG synthesis to minimize substrate inhibition. After 336?h of reaction, the OG yield and the conversion rate of glucose reached 134?mM and 59.6%, respectively. Compared to the batch operation, the fed-bath operation increased the OG yield and the conversion rate of glucose by 340% and 381%, respectively.     

Methane recovery from water hyacinth through whole-cell immobilization technology

The concepts of feed pretreatment, phase separation, and whole-cell immobilization technology have been incorporated in this investigation for the development of rational and cost-effective two- and three-stage methane recovery systems from water hyacinth (WH)Analyses of laboratory data reveal that a three-stage system could be designed with an alkali pretreatment stage [3.6% Na(2)CO(3) + 2.5% Ca(OH)(2) W/W, 24 h HRT] followed by an open acid reactor (2.1 days HRT) and closed immobilized methane reactor (12 h HRT), providing steady-state COD conversion of 62-65%, TVA conversion of 91-95%, and gas productivity of 4.08-5.36 L/L reactor volume/day with 82% methane. A gas yield of 50 L/kg WH/day (dry wt basis) at 35-37 degrees C is possible with this system. Insulation bricks, with particle size distribution of 500-3000 mum, were used as support material in the reactors at organic loading rate of 20 kg COD/m(3) day. The reactors matured in 15-18 weeksSubstantial reduction in retention time for the conversion of volatile acids in immobilized methane reactors prompted further research on the combined immobilized reactor to make possible an additional reduction in the cost of a WH-based biogas system. Evaluation of laboratory data reveals that a two-stage system could be designed with an open alkali pretreatment stage and a combined immobilized reactor (12 h HRT), providing steady-state COD conversion of 53% and gas productivity of 3.1 L/L reactor volume/day with 86% methane. A gas yield of 44 L/kg WH/day (dry wt basis) at 35-37 degrees C could be obtained from this system. Insulation bricks, with 500-1000 mum particle size distribution, was used as support material at an organic loading rate of 15 kg COD/m(3) day. Notwithstanding the fact that the technology in this study has been developed with water hyacinth as substrate, the implicit principles could be extended to any other organic substrate.     

Comparative study of thermostabilty and ester synthesis ability of free and immobilized lipases on cross linked silica gel

A novel support has been utilized for immobilization of lipase, which was prepared by amination of silica with ethanolamine followed by cross linking with glutaraldehyde. Lipases from Rhizopus oryzae 3562 and Enterobacter aerogenes were immobilized on activated silica gel, where they retained 60 and 50% of respective original activity. The thermal stability of the immobilized lipases was significantly improved in comparison to the free forms while the pH stability remained unchanged. E. aerogenes and R. oryzae 3562 lipases retained 75 and 97% of respective initial activity on incubation at 90 degrees C, whereas both the free forms became inactive at this temperature. The conversion yield of isoamyl acetate was found to be higher with the immobilized fungal (90 vs. 21%) and bacterial lipases (64 vs. 18%) than the respective free forms. Immobilized R. oryzae 3562 lipases retained 50% activity for isoamyl acetate synthesis up to ten cycles whereas it was eight cycles for E. aerogenes.     

疏水吸附固定化天冬氨酸酶及其性质的研究

本文论述了一种N-烷基琼脂珠衍生物的合成方法,研究了pH,离子强度、载体上疏水基团含量等因素对载体吸附天冬氨酸酶的影响以及固定化天冬酸酶的性质。结果表明邻甲苯胺基琼脂珠在pH5.5,0.1mol/L磷酸缓冲液(含有0.25mol/LKCL)中,每克湿载体可吸附15—25mg酶蛋白,酶活力回收达90％以上。固定化酶的性质有所改变,其热稳定性和操作稳定性明显增强。 固定化天冬氨酸酸柱可以用于连续化生产L-天冬氮酸,在pH8.0,1.0mol/L及丁烯二酸铵(含0.02mol/L MgCl_2),30℃条件下,以空间流速SV=3.5操作2个月,固定化酶活力仍保持79.5％。     

根瘤菌BK-20固定化细胞生产L(+)-酒石酸

顺式环氧琥珀酸水解酶(CESH)是根瘤菌BK-20生产L(+)-酒石酸的关键酶。为提高其生产效率和生产稳定性,首先优化根瘤菌BK-20的产酶条件,然后利用固定化细胞连续生产L(+)-酒石酸。结果显示,优化后游离细胞酶活达(3 498.0±142.6)U/g,较优化前提高643%。固定化细胞酶活达(2 817.2±226.7)U/g,其最适包埋剂、菌体浓度和凝胶浓度分别为海藻酸钠,10%(W/V)和1.5%(W/V)。固定化细胞连续反应10批后,其形状和酶活均无明显改变,单批次转化率达98%以上,具有良好的生产稳定性。     

金属螯合载体固定重组腈水解酶

以琼脂粉为基质制备金属螯合载体,并用于固定重组腈水解酶。研究发现:制备金属螯合载体最合适的金属离子为Zn2+。当Zn2+离子浓度0.3 mol/L、给酶量15.6 mg/g、固定化pH 8.0、固定化温度40℃时,制得的固定化酶活性最高。固定化酶最适反应温度为50℃、最适反应pH为7.0。当扁桃腈浓度为10 mmol/L、反应1 h时,固定化酶最大产率为0.041 mmol/(g·h);在反应12 h时,产物e.e.值可达到99%以上。固定化酶重复使用8次以后,酶活力仍保持在45%。     

Preparative-scale kinetic resolution of racemic styrene oxide by immobilized epoxide hydrolase

Epoxide hydrolase from Aspergillus niger was immobilized onto the modified Eupergit C 250 L through a Schiff base formation. Eupergit C 250 L was treated with ethylenediamine to introduce primary amine groups which were subsequently activated with glutaraldehyde. The amount of introduced primary amine groups was 220 μmol/g of the support after ethylenediamine treatment, and 90% of these groups were activated with glutaraldehyde. Maximum immobilization of 80% was obtained with modified Eupergit C 250 L under the optimized conditions. The optimum pH was 7.0 for the free epoxide hydrolase and 6.5 for the immobilized epoxide hydrolase. The optimum temperature for both free and immobilized epoxide hydrolase was 40 °C. The free epoxide hydrolase retained 52 and 33% of its maximum activity at 40 and 60 °C, respectively after 24h preincubation time whereas the retained activities of immobilized epoxide hydrolase at the same conditions were 90 and 75%, respectively. Immobilized epoxide hydrolase showed about 2.5-fold higher enantioselectivity than that of free epoxide hydrolase. A preparative-scale (120 g/L) kinetic resolution of racemic styrene oxide using immobilized preparation was performed in a batch reactor and (S)-styrene oxide and (R)-1-phenyl-1,2-ethanediol were both obtained with about 50% yield and 99% enantiomeric excess. The immobilized epoxide hydrolase was retained 90% of its initial activity after 5 reuses.     

Enzymatic resolution of (S)-(+)-naproxen in a trapped aqueous-organic solvent biphase continuous reactor

A trapped aqueous-organic biphase system for the continuous production of (S)-(+)-2-(6-methoxy-2-naphthyl) propionic acid (Naproxen) has been developed. The process consists of a stereoselective hydrolysis of the racemic Naproxen methyl ester by Candida rugosa lipase in a trapped aqueous-organic biphase system. The reaction has been carried out in a laboratory-scale continuous-flow stirred tank reactor (CSTR). The staring material has been supplied in and remaining substrate recovered by organic phase. YWG-C(6)H(5), a poorly polar synthetic support, has been employed to immobilize the lipase and to restrict the aqueous phase. Lipase immobilized on YWG-C(6)H(5) containing aqueous phase has been added into the CSTR to catalyze the hydrolysis. A dialysis membrane tube containing a continuous flow closed-loop buffer has been applied in the CSTR for the extraction of product and recruiting of the aqueous part consumed. Various reaction conditions have been studied. The activity of immobilized enzyme was effected by the polarity of support, the substrate concentration, logP value of organic phase and the product inhibition. At steady-state operating conditions, an initial conversion of 35% has been obtained. The CSTR was allowed to operate continuously for 60 days at 30 degrees C with a 30% loss of activity. The hydrolysis reaction yielded (S)-(+)-Naproxen with >90% enantiomeric excess and overall conversion of 30%.     

固定化嗜热脂肪芽孢杆菌连续合成半乳糖寡糖的研究

利用固定了产β-半乳糖苷酶的嗜热脂肪芽孢杆菌,以乳糖为底物,在纤维床反应器中连续合成半乳糖寡糖(GOS),最高得率为50.7%。在连续反应体系中,研究了底物浓度、pH、反应温度和停留时间对半乳糖寡糖合成的影响,确定最佳反应条件为底物浓度450 g/L、反应温度55℃、pH7.0、停留时间100 min。在连续反应24h后,流加1.5%的D-半乳糖能提高合成GOS的能力,固定化细胞反应体系中连续稳定操作120 h。