介孔分子筛在生物酶固定化中的应用

综述了MCM-48和SBA-15等新型介孔分子筛用生物酶固定化载体研究的新进展。介孔分子筛由于拥有巨大的比表面积(~1000m2/g)、纳米尺寸孔道(2~50m)和较大的孔容(~1.0 cm3/g),因此以分子筛为载体利用物理吸附制备的固定化酶呈现出高的催化活性,但固定化酶操作稳定性较低,在使用过程中部分酶分子发生了脱落,其原因是分子筛表面自由的硅羟基通过物理吸附或氢键作用固定酶分子。借助介孔分子筛自身的自由硅羟基在表面嫁接-COOH、-NH2、-CH=CH2等有机官能团来构筑酶固定化的微环境,改善酶分子和载体的亲和作用,提高固定化酶的活性。目前,利用有机官能团功能化介孔分子筛固定化酶是研究发展的趋势。     

PDA/SiO2大孔复合材料固定化荧光假单胞菌脂肪酶

以具有三维骨架结构的大孔聚合物为模板制备SiO_2大孔材料,通过多巴胺在SiO_2大孔材料孔道表面的原位聚合制得聚多巴胺表面功能化修饰的二氧化硅大孔材料(PDA/SiO_2)。应用SEM、EDX、MIP、BET、TG-DTA和FTIR等技术对修饰前后的材料进行表征。以PDA/SiO_2为载体固定荧光假单胞菌脂肪酶(PFL),优化固定化条件并对比游离脂肪酶和固定化脂肪酶的性质。结果表明SiO_2大孔材料具有三维连续贯通的孔道结构,孔径分布在300~500 nm,聚多巴胺修饰后形成聚多巴胺/二氧化硅复合纳米薄膜构筑的大孔材料。在固定化时间为14 h、p H值为8、初始脂肪酶浓度为0.4 mg·m L-1时,固定化效果最佳,酶活回收率达246%。与游离脂肪酶相比,固定化脂肪酶有更宽的温度和p H适用范围、热稳定性显著提高,并展现出良好的储存稳定性和操作稳定性,固定化脂肪酶的Km低于游离脂肪酶的,酶与底物的亲和性较好。     

介孔材料及其改性材料中酶的固定化研究进展

介孔材料具有高的比表面积、高的孔体积、均一可调的孔径、有序的孔道结构以及易于表面功能化等优点,可广泛用于酶的固定化.介孔材料中酶的固定化方法主要包括物理吸附、物理包埋和化学吸附.综述了介孔材料中不同固定化酶方法的优缺点、酶的固定化影响因素及固定化酶的应用,并对固定化酶的发展前景进行了展望.     

介孔SiO2的改性及对诺维信漆酶的交联固定化

采用十六烷基三甲基溴化铵(CTAB)为模板剂,四乙氧基硅烷(正硅酸乙酯,TEOS)为硅源,硝酸为催化剂来制备介孔SiO2,并采用后嫁接法对介孔SiO2进行氨基化改性。利用红外光谱(IR),X射线粉末衍射(XRD),差热-热重分析(DTA-TG),扫描电镜(SEM),元素分析,微电泳法及N2吸附-脱附方法对改性前后的产物进行表征。结果表明氨基已成功嫁接到介孔SiO2孔道中,改性后的介孔SiO2有序度有所下降,但仍为介孔材料;改性之后介孔材料的孔径、比表面积、孔体积均变小。等电点由原来的2.74变为4.75。本文还以氨基修饰的介孔SiO2为载体,通过交联剂戊二醛固定诺维信(Novozymes)工业级漆酶,并采用正交设计法对固定化条件进行了优化。研究表明漆酶经固定化后,其操作稳定性比游离酶高。     

介孔碳的快速水相合成及对辣根过氧化物酶的固定

以间苯三酚-甲醛为碳源前驱体, 嵌段聚合物F127 (PEO₁₀₆PPO₇₀PEO₁₀₆)为模板剂, 在水相中快速合成了介孔碳材料. 将其应用于辣根过氧化物酶的固定化, 并初步研究了固定化对酶稳定性的影响. 利用TEM和SEM观察该材料的微观结构, 通过N₂吸附-脱附技术对介孔碳材料的孔结构和孔容等进行了表征. 结果表明, 介孔碳材料具有蠕虫状介孔结构, 孔径可在5.6～7.6 nm之间调变, 相应的比表面积介于691.1～787.8 m²/g, 且随着反应体系中盐酸浓度的增加, 所得材料的孔径、比表面积和孔容等均呈现减小的趋势. 固定在介孔碳中的辣根过氧化物酶, 保持了其蛋白质二级结构, 且与游离酶相比, 固定化酶的热稳定性、pH稳定性和操作稳定性都有明显的提高. 经多次循环操作, 固定化酶依然保持较高的活性, 说明其具有良好的可重复利用价值.     

以HPD-750大孔树脂为载体材料固定化果胶酶

HPD-750树脂是中极性大孔吸附树脂,生物相容性好,机械性能稳定,具有较大的比表面积,可用于固定化酶载体材料。本文以HPD-750大孔树脂为载体固定化果胶酶,研究各因素对固定化酶的影响,并采用正交试验对固定化条件进行优化。结果表明,当pH为4.0、固定化温度为45℃、固定化时间为4h、加酶量为0.16g/mL时,固定化酶活力可达5146U/mg。以HPD-750大孔树脂为载体材料制备的固定化酶相较于游离酶具有更好的酸碱稳定性和热稳定性。在循环使用10次后,酶活力依然保留80%以上;4℃储藏25d之后,其酶活力仍保留60%以上。与D311大孔树脂、聚丙烯酰胺和海藻酸钠微球制备的固定化酶相比,HPD-750大孔树脂固定化酶的活性、操作稳定性、机械稳定性和储存稳定性都较好。该结果说明,HPD-750大孔树脂可作为固定化酶较好的载体材料。     

CS-MCM-48复合载体固定化脂肪酶催化苯乙酮-锅法还原转酯化拆分反应

将天然聚合物壳聚糖(CS)涂覆在介孔分子筛MCM-48表面制得CS-MCM-48复合载体,控制CS与介孔分子筛MCM-48质量比为1∶10时,CS-MCM-48的比表面积、平均孔径和孔容分别为408 m2/g、2.14 nm和0.38 cm3/g.在磷酸盐缓冲溶液-异辛烷混合溶剂中制备了固定化假单胞菌脂肪酶(Pseudomonas CepaciaLipase,PSL)PSL/CS-MCM-48,并用于潜手性苯乙酮一锅法还原转酯化手性拆分反应.结果表明,PSL/CS-MCM-48的催化活性和对映选择性均明显优于纯介孔分子筛MCM-48和壳聚糖制备的固定化酶PSL/MCM-48和PSL/CS.甲苯作溶剂,反应温度为40℃时,底物1-苯乙醇转化率达15.3%,产物(R)-乙酸苯乙酯和(S)-1-苯乙醇的对映体过量值分别为99%和18.0%,对映选择性参数E值达237,固定化酶PSL/CS-MCM-48显示出良好的手性拆分性能.     

固定化脂肪酶催化麻疯树油与碳酸二甲酯制备生物柴油的研究

以介孔硅材料(MPS)为载体将脂肪酶固定化,以碳酸二甲酯为酰基受体,对固定化酶催化碳酸二甲酯进行了反应路径(原料油)、反应条件(反应温度、碳酸二甲酯的用量、加水量)的优化,在最佳的条件下对实验过程中所用的固定化酶进行重复使用性的考察。实验结果表明,不同种油与碳酸二甲酯反应在固定化酶的催化下制备生物柴油的产率以麻疯树油为最高,最佳反应条件是碳酸二甲酯的浓度为16m L/g、不加水,在50℃下反应24h,生物柴油得率达81.6%。     

CS-MCM-48复合载体固定化脂肪酶催化苯乙酮一锅法还原转酯化拆分反应

将天然聚合物壳聚糖(CS)涂覆在介孔分子筛MCM-48表面制得CS-MCM-48复合载体,控制CS与介孔分子筛MCM-48质量比为1∶10时,CS-MCM-48的比表面积、平均孔径和孔容分别为408m2/g、2.14nm和0.38cm3/g。在磷酸盐缓冲溶液-异辛烷混合溶剂中制备了固定化假单胞菌脂肪酶(Pseudomonas Cepacia Lipase,PSL)PSL/CS-MCM-48,并用于潜手性苯乙酮一锅法还原转酯化手性拆分反应。结果表明,PSL/CS-MCM-48的催化活性和对映选择性均明显优于纯介孔分子筛MCM-48和壳聚糖制备的固定化酶PSL/MCM-48和PSL/CS。甲苯作溶剂,反应温度为40℃时,底物1-苯乙醇转化率达15.3%,产物(R)-乙酸苯乙酯和(S)-1-苯乙醇的对映体过量值分别为99%和18.0%,对映选择性参数E值达237,固定化酶PSL/CS-MCM-48显示出良好的手性拆分性能。     

聚苯乙烯微球吸附脂肪酶催化油酸环氧化的研究

南极假丝酵母脂肪酶B(Candida antarctica Lipase B,CALB)在H2O2的存在下可以有效地催化不饱和脂肪酸上双键的环氧化反应,制备出具有广泛用途的环氧植物油和环氧脂肪酸,但反应体系中的H2O2和反应生成的过氧酸对酶有严重的失活作用,需通过固定化提高酶稳定性。本文选用具有不同亲疏水性和孔径的聚苯乙烯微球,通过吸附法固定化CALB,并构建了非水相和油/水两相体系作为CALB催化油酸环氧化反应的介质。结果表明,固定化CALB在非水相体系中具有较高的活力,而在油/水两相体系中重复使用性能较好;CALB在疏水性介孔聚苯乙烯微球PST30上具有最高的酶负载量(100.7mg/g),在疏水性超大孔聚苯乙烯微球PST上表现出最高的催化活力和重复使用稳定性,其在非水相和两相反应体系中的催化活力分别是Novozym 435的1.8倍和7.3倍,重复使用次数与Novozym 435相当,在油/水两相体系中重复使用至第2次还出现独特的活力升高现象。     

Immobilization of Candida antarctica Lipase B by Adsorption to Green Coconut Fiber

An agroindustrial residue, green coconut fiber, was evaluated as support for immobilization of Candida antarctica type B (CALB) lipase by physical adsorption. The influence of several parameters, such as contact time, amount of enzyme offered to immobilization, and pH of lipase solution was analyzed to select a suitable immobilization protocol. Kinetic constants of soluble and immobilized lipases were assayed. Thermal and operational stability of the immobilized enzyme, obtained after 2 h of contact between coconut fiber and enzyme solution, containing 40 U/ml in 25 mM sodium phosphate buffer pH 7, were determined. CALB immobilization by adsorption on coconut fiber promoted an increase in thermal stability at 50 and 60 °C, as half-lives (t _1/2) of the immobilized enzyme were, respectively, 2- and 92-fold higher than the ones for soluble enzyme. Furthermore, operational stabilities of methyl butyrate hydrolysis and butyl butyrate synthesis were evaluated. After the third cycle of methyl butyrate hydrolysis, it retained less than 50% of the initial activity, while Novozyme 435 retained more than 70% after the tenth cycle. However, in the synthesis of butyl butyrate, CALB immobilized on coconut fiber showed a good operational stability when compared to Novozyme 435, retaining 80% of its initial activity after the sixth cycle of reaction.     

Man-tailored cellulose-based carriers for invertase immobilization

Cellulose-based carriers Granocel were specially prepared and optimised for covalent immobilization of enzymes. The effects of carrier characteristics such as pore size, chemistry of anchor groups and their density on invertase immobilization efficiency were evaluated. It was found that the preferential adsorption/binding of the enzyme to a carrier during coupling and its activity after immobilization depended on microenvironmental effects created by hydrophilic surface of the carrier, functional groups and their activators. The best preparations (activity approx. 300 U/mL, high storage stability) were obtained for NH₂-Granocel activated with glutaraldehyde. It is probably due to Granocel modification with pentaethylenehexamine that gave a 19-atom spacer arm. The enzyme concentration in coupling mixture was optimised as well. The kinetic parameters of sucrose hydrolysis for native and immobilized invertase were evaluated. Compared to the native invertase, K _m value of immobilized enzyme was only twice higher with about three times lower substrate inhibition. Reaction runs in a well mixed batch reactors with native and immobilized invertase showed slightly slower reaction rate in the case of the enzyme covalently bound to Granocel. Very good stability of cellulose-based carrier was proved experimentally by 20 successive reaction runs in a batch reactor.     

Feruloyl esterase immobilization in mesoporous silica particles and characterization in hydrolysis and transesterification

Background

Enzymes display high reactivity and selectivity under natural conditions, but may suffer from decreased efficiency in industrial applications. A strategy to address this limitation is to immobilize the enzyme. Mesoporous silica materials offer unique properties as an immobilization support, such as high surface area and tunable pore size.

Results

The performance of a commercially available feruloyl esterase, E-FAERU, immobilized on mesoporous silica by physical adsorption was evaluated for its transesterification ability. We optimized the immobilization conditions by varying the support pore size, the immobilization buffer and its pH. Maximum loading and maximum activity were achieved at different pHs (4.0 and 6.0 respectively). Selectivity, shown by the transesterification/hydrolysis products molar ratio, varied more than 3-fold depending on the reaction buffer used and its pH. Under all conditions studied, hydrolysis was the dominant activity of the enzyme. pH and water content had the greatest influence on the enzyme selectivity and activity. Determined kinetic parameters of the enzyme were obtained and showed that K_m was not affected by the immobilization but k_cat was reduced 10-fold when comparing the free and immobilized enzymes. Thermal and pH stabilities as well as the reusability were investigated. The immobilized biocatalyst retained more than 20% of its activity after ten cycles of transesterification reaction.

Conclusions

These results indicate that this enzyme is more suited for hydrolysis reactions than transesterification despite good reusability. Furthermore, it was found that the immobilization conditions are crucial for optimal enzyme activity as they can alter the enzyme performance.

     

Effects of porous polystyrene resin parameters on Candida antarctica lipase B adsorption, distribution, and polyester synthesis activity

Polystyrene resins with varied particle sizes (35 to 350-600 microm) and pore diameters (300-1000 A) were employed to study the effects of immobilization resin particle size and pore diameter on Candida antarctica Lipase B (CALB) loading, distribution within resins, fraction of active sites, and catalytic properties for polyester synthesis. CALB adsorbed rapidly (saturation time 相似文献   

Effects of macroporous resin size on Candida antarctica lipase B adsorption, fraction of active molecules, and catalytic activity for polyester synthesis

Methyl methacrylate resins with identical average pore diameter (250 A) and surface area (500 m2/g) but with varied particle size (35 to 560-710 microm) were employed to study how immobilization resin particle size influences Candida antarctica Lipase B (CALB) loading, fraction of active sites, and catalytic properties for polyester synthesis. CALB adsorbed more rapidly on smaller beads. Saturation occurred in less than 30 s and 48 h for beads with diameters 35 and 560-710 microm, respectively. Linearization of adsorption isotherm data by the Scatchard analysis showed for the 35 microm resin that: (i) CALB loading at saturation was well below that required to form a monolayer and fully cover the support surface and (ii) CALB has a high affinity for this resin surface. Infrared microspectroscopy showed that CALB forms protein loading fronts for resins with particle sizes 560-710 and 120 microm. In contrast, CALB appears evenly distributed throughout 35 microm resins. By titration with p-nitrophenyl n-hexyl phosphate (MNPHP), the fraction of active CALB molecules adsorbed onto resins was <50% which was not influenced by particle size. The fraction of active CALB molecules on the 35 microm support increased from 30 to 43% as enzyme loading was increased from 0.9 to 5.7% (w/w) leading to increased activity for epsilon-caprolactone (epsilon-CL) ring-opening polymerization. At about 5% w/w CALB loading, by decreasing the immobilization support diameter from 560-710 to 120, 75, and 35 microm, conversion of epsilon-CL % to polyester increased (20 to 36, 42, and 61%, respectively, at 80 min). Similar trends were observed for condensation polymerizations between 1,8-octanediol and adipic acid.     

Improved Covalent Immobilization of Horseradish Peroxidase on Macroporous Glycidyl Methacrylate-Based Copolymers

A macroporous copolymer of glycidyl methacrylate and ethylene glycol dimethacrylate, poly(GMA-co-EGDMA), with various surface characteristics and mean pore size diameters ranging from 44 to 200 nm was synthesized, modified with 1,2-diaminoethane, and tested as a carrier for immobilization of horseradish peroxidase (HRP) by two covalent methods, glutaraldehyde and periodate. The highest specific activity of around 35 U g^?1 dry weight of carrier was achieved on poly(GMA-co-EGDMA) copolymers with mean pore diameters of 200 and 120 nm by the periodate method. A study of deactivation kinetics at 65 °C and in 80 % dioxane revealed that periodate immobilization also produced an appreciable stabilization of the biocatalyst, while stabilization factor depended strongly on the surface characteristics of the copolymers. HRP immobilized on copolymer with a mean pore diameter of 120 nm by periodate method showing not only the highest specific activity but also good stability was further characterized. It appeared that the immobilization resulted in the stabilization of enzyme over a broader pH range while the Michaelis constant value (K _m) of the immobilized HRP was 10.8 mM, approximately 5.6 times higher than that of the free enzyme. After 6 cycles of repeated use in a batch reactor for pyrogallol oxidation, the immobilized HRP retained 45 % of its original activity.     

漆酶在纳米多孔金上的固定化及其酶学性质研究

利用纳米材料为载体对酶等生物大分子进行固定化近年来引起人们的浓厚兴趣. 以Au/Ag合金为原料, 通过控制浓硝酸的腐蚀时间再辅以退火处理得到了不同孔径的纳米多孔金(NPG), 利用扫描电镜(SEM)和N2气体吸附仪对孔性质进行了表征. 以NPG为载体, 用α-硫辛酸和N-乙基-N’-(3-二甲基氨基丙基)碳酰二亚胺/N-羟基琥珀酰亚胺(EDC/NHS)对金表面进行活化, 通过化学共价偶联的方法对产自Trametes versicolor的漆酶进行了固定化. 比较了孔径大小对酶固定化量及比活力的影响. 发现小孔径更有利于对该漆酶的固定化. 与游离酶相比, 固定化酶的最适pH没有改变, 但最适温度却从原来的40 ℃升到了60 ℃. 固定化后, 漆酶的pH和热稳定性都明显提高了. 重复使用8次仍能保持初始活力的65%, 且在4 ℃下保存1个月几乎观察不到酶活力的下降. 此外, 失活的固定化酶经浓硝酸处理后, NPG载体可重复利用. 本结果初步显示出了NPG在生物技术领域中的应用潜力.     

Di-functional magnetic nanoflowers: A highly efficient support for immobilizing penicillin G acylase

The novel di-functional magnetic nanoflowers (DMNF) which had both epoxy groups and hydrophilic catechol as well as phthaloquinone groups capable of covalently coupling of penicillin G acylase (PGA) were characterized by scanning electron microscopy, transmission electron microscope (TEM), vibrating sample magnetometer, N₂ adsorption, and so on. The studies showed that DMNF possessed “hierarchical petal” structure of nanosheets had specific saturation magnetization of 39.7 emu/g and average pore diameter of 25.4 nm as well as specific surface area of 17.28 m²/g. For hydrolysis of penicillin G potassium catalyzed by the PGA immobilized on DMNF with enzyme loading of 106 mg/g-support, its apparent activity reached 2,667 U/g, which benefited from the “hierarchical petal” and large pore structure of the magnetic DMNF leading to high enzyme loading and fast diffusion of substrate molecules to the immobilized PGA to reaction. The apparent activity of the immobilized PGA could keep 2,408 U/g (above 90% of its initial activity) after repeating use for 10 cycles. The magnetic immobilized PGA exhibited excellent operational stability due to covalently coupling of the enzyme molecules between the support by covalent interaction of the amino groups of PGA and the reactive groups of epoxy, catechol, and phthaloquinone groups on DMNF. Furthermore, the PGA displayed good acid and alkaline resistance as well as thermal stability by immobilization using DMNF.     

Multi-walled carbon nanotubes used as support for lipase from <Emphasis Type="Italic">Burkholderia cepacia</Emphasis>

Commercial lipase from Burkholderia cepacia is immobilized on functionalized multi-walled carbon nanotubes (MWNT-COOH and MWNT-OH) provided by a physical adsorption. The immobilization processes for the carbon nanotubes are defined using immobilization time (0–30 min) and distinct adsorbent:adsorbate ratios (1:4, 1:7, and 1:10) with lipase loading of 100, 175, and 250 mg, respectively. The characterization of the immobilized preparations, the free lipase, and the pure nanotubes (MWNT-COOH and MWNT-OH) indicate that the lipase adsorption is increased. Thermogravimetric analysis, differential scanning calorimetry, and scanning electron microscopy are used. The specific surface area, pore volumes, and average pore diameters are determined by nitrogen adsorption–desorption isotherms. For the pure lipase, in the range between 40 and 300 °C, the micrograph is acquired. Experimental results clearly show an effective lipase adsorption in a lower period of time (5 min) in MWNT-COOH and MWNT-OH as well as a decrease in the surface area (98.30–45.9(86)?±?2.5 and 97.61–37.71?±?3.3(7) m² g^?1) and the pore volume (0.48–0.25?±?0.01 and 0.39–0.24?±?0.05 cm³ g^?1), indicating that functionalized multi-walled carbon nanotubes can be successfully used as enzyme support.