Immobilization of Papain on the Mesoporous Molecular Sieve MCM‐48

The immobilization of papain on the mesoporous molecular sieve MCM‐48 (with a pore size of 6.2 nm in diameter) with the aid of glutaraldehyde, and the characteristics of this immobilized papain are described. The optimum conditions for immobilization were as follows: 20 mg native free enzyme/g of the MCM‐48 and 0.75 % glutaraldehyde, 2 h at 10–20 °C and pH 7.0. Under these optimum conditions for immobilization, the activity yield [%] of the immobilized enzyme was around 70 %. The influence of the pH on the activity of the immobilized enzyme was much lower compared to the free enzyme. The thermostability of the immobilized enzyme, whose half‐life was more than 2500 min, was greatly improved and was found to be significantly higher than that of the free enzyme (about 80 min). The immobilized enzyme also showed good operational stability, and the activity of the immobilized enzyme continued to maintain 76.5 % of the initial activity even after a 12‐day continuous operation. Moreover, the immobilized enzyme still exhibited good storage stability. From these results, papain immobilized on the MCM‐48 with the aid of glutaraldehyde, can be used as a high‐performance biocatalyst in biotechnological processing, in particular in industrial and medical applications.     

Culture conditions for the production of amylolytic enzymes by a thermophilic Clostridium sp.

The growth of a thermophilic Clostridium sp. and the production of α-glucosidase, α-amylase and pullulanase were studied under anaerobic conditions using different carbon and nitrogen sources and varying pH values and temperatures. Growth and enzyme activities were highest with soybean meal as the nitrogen source. The optimum concentration was 2.5% [w/v] for the production of α-amylase as well as pullulanase and 2% [w/v] for α-glucosidase. The best carbon source proved to be soluble starch for α-amylase, and pullulanase and maltose for α-glucosidase. Growth and enzyme production reached their optimum at pH 6.5 to 7.0 and 70°C. Under these conditions, the enzyme activities followed exponential growth with maximum yields of α-glucosidase, α-amylase and pullulanase at 28, 36, and 44 h.     

Microbial production of conjugated γ‐linolenic acid from γ‐linolenic acid by Lactobacillus plantarum AKU 1009a

Aims: Optimal production conditions of conjugated γ‐linolenic acid (CGLA) from γ‐linolenic acid using washed cells of Lactobacillus plantarum AKU 1009a as catalysts were investigated. Methods and Results: Washed cells of Lact. plantarum AKU 1009a exhibiting a high level of CGLA productivity were obtained by cultivation in a nutrient medium supplemented with 0·03% (w/v) α‐linolenic acid as an inducer. Under the optimal reaction conditions with 13 mg ml^?1γ‐linolenic acid as a substrate in 5 ‐ml reaction volume, the washed cells [32% (wet cells, w/v) corresponding to 46 mg ml^?1 dry cells] as the catalysts produced 8·8 mg CGLA per millilitre reaction mixture (68% molar yield) in 27 h. The produced CGLA was a mixture of two isomers, i.e., cis‐6,cis‐9,trans‐11‐octadecatrienoic acid (CGLA1, 40% of total CGLA) and cis‐6,trans‐9,trans‐11‐octadecatrienoic acid (CGLA2, 60% of total CGLA), and accounted for 66% of total fatty acid obtained. The CGLA produced was obtained as free fatty acids adsorbed mostly on the surface of the cells of Lact. plantarum AKU1009a. Conclusion: The practical process of CGLA production from γ‐linolenic acid using washed cells of Lact. plantarum AKU 1009a was successfully established. Significance and Impact of the Study: We presented the first example of microbial production of CGLA. CGLA produced by the process is valuable for evaluating their physiological and nutritional effects, and chemical characteristics.     

Immobilization of permeabilized whole cell penicillin G acylase from Alcaligenes faecalis using pore matrix crosslinked with glutaraldehyde

The activity of penicillin G acylase from Alcaligenes faecalis increased 7.5-fold when cells were permeabilized with 0.3% (w/v) CTAB. The treated cells were entrapped by polyvinyl alcohol crosslinked with boric acid, and crosslinked with 2% (v/v) glutaraldehyde to increase the stability. The conversion yield of penicillin G to 6-aminopenicillanic acid was 75% by immobilized system in batch reaction. No activity was lost after 15 cycles and about 65% enzyme activity was retained at the end of the 31th cycle.     

Immobilized cyclomaltodextrin glucanotransferase of an alkalophilic Bacillus sp. No. 38-2

Cyclomaltodextrin glucanotransferase [1,4-alpha-D-glucan-4-alpha-D-(1,4-alpha-D-glucano)-transferase (cyclizing), E.C.-2.4.1.19] of an alkalophilic Bacillus sp. No. 38-2 (ATCC 21783), which contains three types of enzymes (acid, neutral, and alkaline enzymes), was immobilized on synthetic adsorption resin. No distinguishing changes in pH or thermal stabilities of enzyme were observed due to the immobilization. Since acid-enzyme activity had disappeared, the optimum pH of immobilized enzyme was 9.0. Optimum temperature for the enzyme activity changed from 50 to 55 degrees C. The enzyme converted starch to cyclodextrins without significant loss of activity under the conditions of continuous reaction for about two weeks by using the column system (60 degrees C at pH 8.0). About 63% of soluble starch solution [4% (w/v)] was changed to cyclodextrins, as tested so far.     

Stabilizing hyperactivated lecitase structures through physical treatment with ionic polymers

Lecitase Ultra has been covalently immobilized on cyanogen bromide cross-linked 4% agarose (CNBr) beads, maintaining 70% of the initial activity. The activity of the immobilized enzyme was improved in the presence of Triton X-100, sodium dodecyl sulfate (SDS), and cetyltrimethyl ammonium bromide (CTAB) (e.g., up to 800% when using CTAB). However, CTAB and Triton X-100 presented a negative effect on enzyme stability even at low concentrations, and SDS cannot be used for a long time at 1% concentration. To maintain the hyperactivated conformation of the enzyme in the absence of detergent, ionic polymers were added during incubation of the immobilized enzyme in the presence of detergents. Coating the immobilized enzyme with polyethylenimine in aqueous buffer (PEI) produced a 3-fold increase in enzyme activity. However, in the presence of 0.1% SDS (v/v), this coating produced a 50-fold increase in enzyme activity. Using PEI and 0.01% (v/v) CTAB, the Lecitase activity decreased to 10%. Using irreversible inhibitors, it could be shown that the PEI/SDS-CNBr-Lecitase preparation allowed its catalytic Ser to be more accessible to the reaction medium than the unmodified CNBr-Lecitase.     

Preparation and some properties of immobilized Penicillium funiculosum 258 dextranase

The production of dextranase was investigated in static cultures of Penicillium funiculosum 258. Maximal enzyme productivity was attained at pH 8.0, with 3.5% (w/v) dextran (MW, 260 000) as carbon source, NaNO₃ (1%, w/v) and yeast extract (0.2%, w/v) as nitrogen source, 0.4% (w/v) K₂HPO₄ and 0.06% (w/v) MgSO₄. It was possible to increase the productivity of dextranase to 41.8 units ml⁻¹ in the modified medium. The enzyme was immobilized on different carriers by different techniques of immobilization. The enzyme prepared by covalent binding on chitosan using glutaraldehyde had the highest activity, the immobilized enzyme retaining 63% of its original specific activity. Compared with the free dextranase, the immobilized enzyme exhibited: a higher pH optimum, a higher optimal reaction temperature and energy of activation, a higher Michaelis constant, improved thermal stability and higher values of deactivation rate constant. The immobilized enzyme retained about 80% of the initial catalytic activity even after being used for 12 cycles.     

Immobilization of fructosyltransferase by chitosan and alginate for efficient production of fructooligosaccharides

The effective system of reusing mycelial fructosyltransferase (FTase) immobilized with two polymers, chitosan and alginate were evaluated for continuous production of fructooligosaccharides (FOS). The alginate beads were successfully developed by maintaining spherical conformation of using 0.3% (w/v) sodium alginate with 0.1% (w/v) of CaCl₂ solution for highest transfructosylating activity. The characteristics of free and immobilized FTase were investigated and results showed that optimum pH and temperature of FTase activity were altered by immobilized materials. A successive production of FOS by FTase entrapped alginate beads was observed at an average of 62.96% (w/w) up to 7 days without much losing its activity. The data revealed by HPLC analysis culminate 67.75% (w/w) of FOS formation by FTase entrapped alginate beads and 42.79% (w/w) by chitosan beads in 36 h of enzyme substrate reaction.     

Enantioselective synthesis of (S)‐naproxen using immobilized lipase on chitosan beads

S‐naproxen by enantioselective hydrolysis of racemic naproxen methyl ester was produced using immobilized lipase. The lipase enzyme was immobilized on chitosan beads, activated chitosan beads by glutaraldehyde, and Amberlite XAD7. In order to find an appropriate support for the hydrolysis reaction of racemic naproxen methyl ester, the conversion and enantioselectivity for all carriers were compared. In addition, effects of the volumetric ratio of two phases in different organic solvents, addition of cosolvent and surfactant, optimum pH and temperature, reusability, and inhibitory effect of methanol were investigated. The optimum volumetric ratio of two phases was defined as 3:2 of aqueous phase to organic phase. Various water miscible and water immiscible solvents were examined. Finally, isooctane was chosen as an organic solvent, while 2‐ethoxyethanol was added as a cosolvent in the organic phase of the reaction mixture. The optimum reaction conditions were determined to be 35 °C, pH 7, and 24 h. Addition of Tween‐80 in the organic phase increased the accessibility of immobilized enzyme to the reactant. The optimum organic phase compositions using a volumetric ratio of 2‐ethoxyethanol, isooctane and Tween‐80 were 3:7 and 0.1% (v /v/v), respectively. The best conversion and enantioselectivity of immobilized enzyme using chitosan beads activated by glutaraldehyde were 0.45 and 185, respectively.     

In vivo photochemical skin micronucleus test using a sunlight simulator: detection of 8-methoxypsoralen and benzo[a]pyrene in hairless mice

Evaluating in vivo photochemical genotoxicity (photogenotoxicity) or photochemical carcinogenicity (photocarcinogenicity) in the skin that is actually exposed to light is important for estimating the risk of human exposure to chemicals under sunlight. With regard to the skin micronucleus test, Nishikawa et al. developed a reliable technique that is simple and in which the negative control has a stable background. In the present study, we applied 8-methoxypsoralen (8-MOP) and benzo[a]pyrene (B[a]P) to the backs of hairless mice and subjected the mice to irradiation by a sunlight simulator in order to investigate whether this test can detect photogenotoxicity of these chemicals. In the treatment with 8-MOP [0.00075% and 0.0015% (w/v)], a significant increase was observed in the frequency of micronucleated cells only under light irradiation using the sunlight simulator. At a high chemical dose, the frequency of micronucleated cells increased from 48h after the treatment, peaked at 96h, and then decreased at 168h. Furthermore, at 96h with the high dose under light irradiation, we frequently observed cells with nuclear buds. In the treatment with B[a]P [first experiment: 0.025% and 0.05% (w/v); second experiment: 0.005%, 0.01%, and 0.02% (w/v)], a significant increase was observed in the frequency of micronucleated cells at skin-irritating doses [0.01%, 0.02%, 0.025%, and 0.05% (w/v)] at 72 or 96h after the treatment only under light irradiation using the sunlight simulator. In conclusion, photogenotoxicity of 8-MOP and B[a]P was detected in the in vivo photochemical skin micronucleus study.     

铜金属螯合载体固定糖化酶

[目的]制备出含Cu2+的琼脂糖-IDA螯合载体及对其固定糖化酶工艺条件进行优化.[方法]利用金属螯合配体(IDA-Cu2+)与蛋白质表面供电子氨基酸相互作用的原理制备载体,采用紫外分光光度法测定不同影响因素下固定化糖化酶的酶活.[结果]Cu2+的加入量和固定化过程的酸度比给酶量对固定化糖化酶的活性影响还要大,在给酶量80 mg/g载体、1.0× 10-2 mol Cu2+/g载体、pH 4.6和固定化4h的固定化条件下,固定化酶活为252.1 U/g,重复使用5次后酶活为首次固定化酶活的65.1％.[结论]该Cu2+-IDA-金属螯合琼脂糖可用于淀粉水解糖化酶的优良固定化载体材料.     

α-Amylase immobilization on gelatin: Optimization of process variables

α-Amylase was extracted and purified from soybean seeds to apparent homogeneity by affinity precipitation. The homogeneous enzyme preparation was immobilized on gelatin matrix using glutaraldehyde as an organic hardener. Response surface methodology (RSM) and 3-level-3-factor Box–Behnken design was employed to evaluate the effects of immobilization parameters, such as gelatin concentration, glutaraldehyde concentration and hardening time on the activity of immobilized α-amylase. The results showed that 20% gelatin (w/v), 10% glutaraldehyde (v/v) and 1 h hardening time yielded an optimum immobilization of 82.5%.     

Choline-O-Sulfate Biosynthesis in Plants (Identification and Partial Characterization of a Salinity-Inducible Choline Sulfotransferase from Species of Limonium (Plumbaginaceae)

Choline-O-sulfate is a compatible osmolyte accumulated under saline conditions by members of the halophytic genus Limonium and other Plumbaginaceae. A choline sulfotransferase (EC 2.8.2.6) responsible for the formation of choline-O-sulfate was characterized in Limonium species. A simple radiometric assay was developed in which [14C]choline was used as substrate, and the h [14C]choline-O-sulfate product was isolated by ion-exchange chromatography. The choline sulfotransferase activity was soluble, required 3[prime]-phosphoadenosine-5[prime]-phosphosulfate as the sulfate donor, and showed a pH optimum at 9.0. Apparent Km values were 25 [mu]M for choline and 5.5 [mu]M for 3[prime]-phosphoadenosine-5[prime]-phosphosulfate. Choline sulfotransferase activity was detected in various Limonium species but was very low or absent from species that do not accumulate choline-O-sulfate. In roots and leaves of Limonium perezii, the activity was increased at least 4-fold by salinization with 40% (v/v) artificial sea water. Choline sulfotransferase activity was also induced in cell cultures of L. perezii following salt shock with 20% (v/v) artificial sea water or osmotic shock with 19% (w/v) polyethylene glycol 6000. Labeling experiments with [14C]choline confirmed that the enzyme induced in cell cultures was active in vivo.     

Enzymatic hydrolysis of inulin to fructose by glutaraldehyde fixed yeast cells

Inulin, a polyfruction, is found as the reserve carbohydrate in the roots and tubers of various plants (i.e. Jerusalem artichoke, chicory, and dahlia tubers). The beta-fructofuranosidase (inulase) from the yeast Kluyveromyces fragilis is of interest because of its industrial potential in fructose syrup and alcohol production from inulin containing plants. We have found that the inulase of K. fragilis can be immobilized in the yeast cells by glutaraldehyde treatment. These cells are resistant to physical and enzymatic destruction. Although the exact nature of the immobilization is not fully understood, the kinetic parameters of the immobilized enzyme are similar to those of the soluble enzyme. No reduction of enzyme activity was observed after glutaraldehyde treatment and glutaraldehyde concentration did not affect enzyme activity. A 96% hydrolysis of dahlia inulin was achieved in 10.5 h with a 9.5% (w/v) fixed enzyme suspension. A Jerusalem artichoke extract containing 16.8%polyfructan was completely hydrolyzed in 3.5 h with a 0.24% (w/v)fixed enzyme suspension. This is a time frame feasible for industrial consideration.     

羊源丁酸梭菌HDRyYB1发酵工艺的优化

【目的】目前,国内外鲜有关于羊源丁酸梭菌的报道。本课题选用羊源丁酸梭菌HDRy YB1为研究对象,对其发酵工艺进行优化,为该菌株作为饲料添加剂应用于畜牧业生产奠定基础。【方法】采用Plackett-Burman(PB)试验设计法和响应面法分析并优化显著影响HDRy YB1菌株发酵液中芽胞数的培养基成分。【结果】发酵培养基中的面粉浓度、鱼粉浓度和米粉浓度显著影响发酵液中的芽胞数,优化后的发酵培养基组分(质量体积比)为:面粉3.72%、鱼粉0.90%、米粉3.96%、酵母粉0.60%、Na Cl 0.19%、Mg SO4·7H2O 0.19%、KH2PO4 0.01%、Na HCO3 0.01%、Ca CO3 0.48%;培养参数为:37°C,初始p H为7.2-7.4,瓶装量100/250,接种量3%。在此条件下,HDRy YB1菌株发酵完全(18 h)的芽胞数为1.478×108 CFU/m L,是优化前的2.7倍。【结论】HDRy YB1菌株发酵培养基得到了优化,优化后的培养基可用于后期的扩大发酵试验,验证其在实践生产中的应用价值。     

Immobilization of cyclodextrin glucanotransferase on amberlite IRA-900 for biosynthesis of transglycosylated xylitol

Cyclodextrin glucanotransferase (CGTase) fromThermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH 6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of the amount ratio of the adsorbed enzyme to the initial amount in the solution. Immobilization of CGTase shifted the optimum temperature for the enzyme to produce transglycosylated xylitol from 70°C to 90°C and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuously produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10% (w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10% (w/v) xylitol as the glycosyl acceptor, 20 mL/h of medium flow rate, and 60°C. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g·L⁻¹·h⁻¹, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.     

Entrapment of β-galactosidase in polyvinylalcohol hydrogel

β-Galactosidase isolated from Aspergillus oryzae was immobilized in lens-shaped polyvinylalcohol capsules (with activity 25 U g⁻¹) giving 32% of its original activity. Immobilization did not change the pH optimum (4.5) of lactose hydrolysis. The relative enzyme activity during product inhibition testing was, in average, 10% higher for immobilized enzyme. No decrease of activity was observed after 35 repeated batch runs and during 530 h of continuous hydrolysis of lactose (10%, w/v) at 45°C. The immobilized enzyme was stable for 14 months without any change of activity during the storage at 4°C and pH 4.5.     

Measurement of in situ halophilic glyceraldehyde-3-phosphate dehydrogenase activity from the permeabilized cells of archaebacterium Haloarcula vallismortis

The cells of Haloarcula vallismortis, an extreme halophilic archaebacterium, were permeabilized by various chemical, physical, and biological treatments. Biological permeabilization by lysozyme and papain showed effective results as observed by studying the in situ activity of halophilic glyceraldehyde-3-phosphate dehydrogenase (hGAPDH) as the model enzyme. Detergents N-cetyl-N, N, N-trimethyl ammonium bromide (CTAB) and digitonin also showed significant results. Other strains of halobacteria could also be permeabilized by lysozyme. The cell morphology did not show any significant change after permeabilization as observed by phase contrast microscopy. The enzyme characteristics of hGAPDH were studied in situ using permeabilized H. vallismortis cells. The properties, like optimum pH, Km for GAP and NAD(+), inhibition by heavy metals, sulphydryl reagents, and other compounds, showed remarkable similarity with those studied in vitro.     

Optimization of pH,Temperature and Inoculum Ratio for the Production of β‐D‐Galactosidase by Kluyveromyces marxianus Using a Lactose‐free Medium

The pH, temperature and inoculum ratio for the production of β‐galactosidase by Kluyveromyces marxianus CDB 002 were optimized using sugar‐cane molasses (100 g/l) in a lactose‐free medium. The temperature optimum was evaluated in the range from 28–37 °C. Lactase production was initiated after substrate consumption indicating a reversible enzyme inhibition or catabolic repression. The specific enzyme activity after 45 h was between 456.3 U/g cell mass (37 °C) and 733.3 U/g (34 °C), whereas the highest volumetric activity was obtained at 30 °C: 21.8 U/ml. This is generally consistent with results from other authors that used whey as a carbon source. Ethanol as a by‐product reached its maximum concentration after 10–14 h (31.1–40.5 g/l), but was completely consumed afterwards. A pH of 5.5 without further control gave the best production rate for lactase (484.4 U/l × h). In this process, the pH was stable during cell growth at 5.5 and then went up to pH 7.2 after 45 h. At a fixed pH of 5.5 or 6.5, the production rates achieved 313.3 U/l × h and 233.3 U/ l × h, respectively. These results differed from those of other authors, who suggested a fixed pH at 7.0 using whey as a carbon source. There were no significant differences between inoculum ratios of 1% [v/v] and 10% [v/v] so that 1% is the preferable ratio as it is cheaper. Yeast extract (10 g/l) and peptone (20 g/l) were used as the vitamin and nitrogen source, respectively, for the studies of temperature and pH. These were substituted by corn steep liquor (100 g/l) for inoculum ratio experiments. Production of lactase using sugar cane molasses in a lactose‐free medium gave better enzyme productivity rates than obtained by other authors using whey. The optimum conditions for β‐galactosidase synthesis were a temperature of 30–34 °C and an inoculum ratio of 1% [v/v], an initial pH of 5.5 without any further control or a control of 5.5 during cell growth. Then the pH was raised up to 7.     

Optimization of Xylanase Production by Sporotrichum thermophile Using Corn Cobs and Response Surface Methodology

A 3² central composite experimental design was performed with the aim of optimizing the production of xylanase by Sporotrichum thermophile grown on corn cobs in submerged cultures. Various carbon and nitrogen sources were consecutively optimized, and corn cobs and ammonium phosphate concentrations were selected as substrates to test the effect of two variables, i.e., both substrate concentrations, on xylanase production. A second‐order quadratic model and a response surface method showed that the optimum conditions for xylanase production were 2.7 % [w/v] corn cobs and 0.7 % [w/v] ammonium phosphate. These optimum conditions were transferred to 7 L bioreactors, where activities as high as 56 U/mL were obtained.