以环氧乙烷为活性基的多孔颗粒状固定化青霉素酰化酶的制备*

报道了用以环氧乙烷为活性基的多孔颗粒状载体 (Eupergit C)制备固定由巨大芽孢杆菌 (^{B .megaterium})产生的青霉素酰化酶的研究。用己二胺 ,赖氨酸对载体进行化学修饰后制备固定化酶 ,获得了较好的固定结果。用未修饰的载体制备固定化酶 ,经 2 4h固定反应 ,酶活力达 1 76.5IU/g (wet) ,酶活力总收率达 53.7%,酶蛋白的固定量为 197mg/g(dry) ,酶蛋白的固定效率达 87.5 %。游离酶的酶浓度对制备固定化酶的活力无显著影响。当加酶量从     

以聚丙烯腈纤维为载体制备固定化青霉素G酰化酶的研究

以酸部分水解聚丙烯腈纤维为载体 ,以戊二醛为交联剂 ,共价键结合制备了固定化胞外青霉素G酰化酶。当水解后的载体中 NH2 基含量为 690 μmol g和含水量为 64%时 ,对酶蛋白的固定量达 1 0 0mg g以上 ,固定化酶的活力达 2 30 0IU g ,酶活力总产率为 30 % ,固定化效率为 56%。酶活力的总产率和固定化率随加酶量的增加而降低。该酶可以将浓度为 2 5%～1 2 5%的青霉素G钾盐水解 98%以上。批投青霉素G钾盐为 1 0g,酶负荷为 1 50IU g(PGK) ,经2 0批水解反应后 ,剩余酶活力为 80 %。用二硫基苏醣醇处理固定化酶 ,对水解青霉素G钾盐的操作稳定性有促进作用。固定化酶的室温保存半衰期为 1 30d。用戊二醛和硼氢化钠溶液处理固定化酶后 ,酶活力的室温保存稳定性有所降低。     

固定化青霉素酰化酶的研究

将巨大芽孢杆菌胞外青霉素酰化酶通过共价键连接到醋酸纤维素载体上,制成的固定化青霉素酰化酶的表观活力达2000 u／g左右(PDAB法)。水解lO％(w／v)的青霉素G钾盐落液,使用30批,保留活力70％以上。6-氨基青毒烷酸(6-APA)总收率平均达88．37％。固定化青霉素酰化酶水解青霉素G的最适pH为9．95,最适温度为55℃,表观米氏常数为1.093×10-2mol／L,在pH 5．8-10．7,温度45℃以下酶的活力稳定。     

聚丙烯腈纤维固定化青霉素酰化酶性质的研究

将巨大芽孢杆菌（Bacillusmegaterium）青霉素酞化酶连接到聚丙烯腈纤维载体上,制成固定化青霉素酰化酶。其表现活力约为2000u／g。水解青霉素G的最适温度为50℃;最适PH为9．0;在PHS．5～10．3、温度50℃以下酶的活力稳定;表观米氏常数Ka为1．33×10-8mol／L;最大反应速度Vm为2．564mmol·min-1;苯乙酸为竞争性抑制剂,抑制常数为0．16mol／L。水解10％的青霉素G钾盐溶液,使用20批,保留酶活力80％。     

固定化青霉素V酰化酶的制备及性质

尖镰孢(Fusarium oxysporum)FP941青霉素V酰化酶经γ氧化铝吸附洗脱、硫酸铵沉淀和脱盐处理后,固定在环氧丙烯聚合物载体上,湿固定化酶表现活力为217 IU/g,固定化产率为53%。固定化酶作用最适温度为55℃,最适pH为80;在pH50～110及50℃以下稳定;37℃使用25次后,酶活力保留90%。     

青霉素酰化酶在新型复合载体上的固定化研究

通过γ-氯丙基三甲氧基硅烷的媒介,将聚乙烯亚胺(PEI)化学偶联在硅胶微粒表面,制备了新型复合载体PEI/silica gel,然后通过双官能团试剂戊二醛的作用,将青霉素酰化酶固定在复合载体上;考察了戊二醛用量、pH值、固定化温度、固定化时间及给酶量等条件对固定化青霉素酰化酶表观活力、活性回收率等性能的影响;并通过测定复合载体在固定化前的ζ电位,探索了复合载体PEI/silica gel固定化酶的作用机理。研究结果表明,由于PEI分子链中含有大量胺基,共价键联与物理吸附相结合,使青霉素酰化酶被快速稳定地固定化,并具有高的催化活性与活力回收率。复合载体PEI/silica gel(0.5 g)固定青霉素酰化酶的适宜固定化条件为:固定化温度为30℃;固定化时间为14~15 h;戊二醛用量为1.2 mmol/g;pH=7.92;给酶量为0.1 mL/g。     

巨大芽孢杆菌青霉素G酰化酶在新型环氧载体ZH-HA上的固定化

巨大芽孢杆菌青霉素G酰化酶共价结合在新型环氧-氨基型载体ZH-HA 上,通过对酶浓度、固定化时间、pH以及缓冲液浓度等条件的考察,确定了最优固定化条件:50 mg比活力6000 U/g的巨大芽孢杆菌青霉素G酰化酶蛋白和1g ZH-HA悬浮于pH 9.01 mol/L磷酸缓冲液,室温搅拌6 h,制得固定化巨大芽孢杆菌青霉素G酰化酶,活力2126 U/g湿载体,活力回收率7.67%.比较研究了固定化酶与原酶性质,原酶最适温度45℃,最适pH为8.0.固定化酶则分别是50℃和9.0,分别比溶液酶偏移5℃、1.0个pH单位.经过40批连续水解青霉素G钾盐,固定化巨大芽孢杆菌青霉素酰化酶仍保持80%的活力,显示出良好的工作稳定性.     

几种纤维素及无机吸附载体对青霉素酰化酶的吸附作用及其固定化

本文就几种纤维素和无机吸附载体对青霉素酰化酶的吸附作用及其固定化进行了研究,结果表明:DEAE-纤维素、EYI-纤维素、微晶纤维素、CM-纤维素、羟基磷灰石、中性氧化铝、硅藻土及粉末状膨润土对青霉素酰化酶都有很强的吸附能力,其固定化青霉素酰化酶的比活分别在1.47～19.43u/g之间,活力回收率为16.3％至84％,几种固定化酶的最适pH均较游离酶低,且其操作稳定性较好。     

壳聚糖固定化木聚糖酶的研究

从青霉菌m8提取出木聚糖酶,将其固定在用戊二醛交联的壳聚糖载体上。1．0g壳聚糖与4％的二醛结合固定3．5mg蛋白,酶活回收率为46．6％。在酶的最适pH为4．6,固定化酶为pH3．8。原酶的最适温度为55℃,固定化酶在60－75℃都具有较高活性。固定化酶的耐热性优于原酶,固定化酶的表现Km值略低于原酶,前者为5．0×10－2g／L,后者为3．58×10－2g／L。     

活性炭吸附固定化粪产碱杆菌青霉素G酰化酶

目的：以活性炭为载体固定化粪产碱杆菌来源的青霉素G酰化酶,考察固定化酶的性质。方法：对影响酶固定化的因素优化筛选,确定有显著影响的因素：pH、离子强度、酶量、固定化时间进行L934的正交实验,获得最佳固定化条件,并对固定化酶的最适反应温度、pH及批次稳定性进行研究。结果：最佳固定化条件为：载体0.3g,酶量5mL,总反应体系为12mL,离子强度1mol/L,温度4℃,pH 7.0,固定化40h;最高固定化酶活性为135.9U/g湿载体。固定化酶性最适反应温度为55℃,最适pH为10,重复使用12次后没有活性损失。结论：活性炭吸附固定化青霉素G酰化酶的活性高,批次反应稳定,具有工业应用潜力。     

Properties of immobilized pepsin on Modified PMMA microspheres

In this work we use micro-size poly(methyl methacrylate)/acrylaldehyde microspheres as a support for pepsin immobilization. The aldehyde groups on the microspheres offer a very simple, mild and firm combination for enzyme immobilization. The amount of enzyme we can bind to this support reaches 82 mg/g, which is much higher than for other supports (mostly less than 10 mg/g). Compared to free enzyme, the Km of immobilized enzyme is increased, whereas the Vmax is decreased. Further, the Vmax/Km value for immobilized pepsin is about 50% of the value for free enzyme. This is better than values reported previously, generally lower than 35%. The optimum temperature shifts from 43 degrees C for free pepsin to 47 degrees C. However, the optimum pH does not change between free and immobilized enzyme. This improved resistance of the immobilized enzyme towards changes in temperature and pH also shows that the aldehyde modified poly(methyl methacrylate)/acrylaldehyde microspheres can be a valuable support for pepsin immobilization.     

Immobilization of invertase onto poly(3-methylthienyl methacrylate)/poly(3-thiopheneacetic acid) matrix

A novel immobilization matrix, poly(3-methylthienyl methacrylate)–poly(3-thiopheneacetic acid) (PMTM–PTAA), was synthesized and used for the covalent immobilization of Saccharomyces cerevisiae invertase to produce invert sugar. The immobilization resulted in 87% immobilization efficiency. Optimum conditions for activity were not affected by immobilization and the optimum pH and temperature for both free and immobilized enzyme were found to be 4.5 and 55 °C, respectively. However, immobilized invertase was more stable at high pH and temperatures. The kinetic parameters for free and immobilized invertase were also determined using the Lineweaver–Burk plot. The K_m values were 35 and 38 mM for free and immobilized enzyme, respectively. The V_max values were 29 and 24 mg glucose/mg enzyme min for free and immobilized enzyme, respectively. Immobilized enzyme could be used for the production of glucose and fructose from sucrose since it retained almost all the initial activity for a month in storage and retained the whole activity in repeated 50 batch reactions.     

Use of chemically modified PMMA microspheres for enzyme immobilization

Modified poly(methyl methacrylate) (PMMA) microspheres, about 7microm in diameter, carrying aldehyde groups on their surfaces were synthesized and used as the support for enzyme immobilization. The immobilizing behavior as well as the properties of immobilized enzyme was studied. The amount of bound enzyme can be extended to 76.8mg g(-1) support, which is relatively much higher than other supports. The kinetic investigation derived from three typical models shows that the practical process is more complicated than the ideal condition, with one or more interactions being involved in the immobilization process. The K(m) value is actually larger and V(max) is smaller in the immobilized form than those in the free form. The increased resistance of the immobilized enzyme against the changes of temperature indicates that immobilizing enzyme onto the modified microspheres is useful for enzyme immobilization.     

Immobilization of xylan-degrading enzymes from<Emphasis Type="Italic"> Melanocarpus albomyces</Emphasis> IIS 68 on the smart polymer Eudragit L-100

Xylanase of Melanocarpus albomyces IIS 68 was immobilized on Eudragit L-100. The latter is a copolymer of methacrylic acid and methyl methacrylate and is a pH-sensitive smart polymer. The immobilization was carried out by gentle adsorption and an immobilization efficiency of 0.82 was obtained. The enzyme did not leach off the polymer even in the presence of 1 M NaCl and 50% ethylene glycol. The K(m) of the enzyme changed from 5.9 mg ml(-1) to 9.1 mg ml(-1) upon immobilization. The V(max) of the immobilized enzyme showed an increase from 90.9 micro mol ml(-1) min(-1) (for the free enzyme) to 111.1 micro mol ml(-1) min(-1). The immobilized enzyme could be reused up to ten times without impairment of the xylanolytic activity. The immobilized enzyme was also evaluated for its application in pre-bleaching of eucalyptus kraft pulp.     

Immobilization of endo-polygalacturonase from Aspergillus niger on various types of macromolecular supports

Endo-polygalacturonase (endo-PG) was immobilized on a wide range of natural and synthetic macromolecular supports and their modified derivatives representing many chemical classes, including esters, amides, phenols, alkyl- and arylamines, and carboxyl derivatives. The immobilization entailed methods of adsorption alone as well as covalent bond formation using glutaraldehyde or carbodiimide or via the diazo-coupling reaction. The most promising system proved to be immobilization on trimalehylchitosan (TMC) via adsorption followed by treatment with glutaraldehyde (GA). The binding capacity of the support is on the order of 13,000 IU/g, half of which is active. Various properties of immobilized endo-PG were evaluated. The optimum pH of the enzyme shifted to the alkaline side. The relative catalytic activity was considerably high even at room temperature and remained so above 70 degrees C. The thermal stability at pH 3-4 was notably improved by immobilization, the half-time doubling. Finally, the apparent K(m) was greater for immobilized endo-PG than for native enzyme, while the V(max) was smaller for the immobilized enzyme.     

Enzymatic modification of vegetable protein: Immobilization of Penicillium duponti enzyme on reconstituted collagen and the use of the immobilized-enzyme complex for solubilizing vegetable protein in a recycle reactor

Penicillium duponti enzyme was immobilized on reconstituted collagen by macromolecular complication, impregnation, and covalent crosslinking techniques. The immobilization of the enzyme on collagen has a twofold purpose: (1) providing a protein microenvironment for the proteolytic enzyme; and (2) extending the useful life the enzyme once immobilized on the collagen matrix. Two types of collagen were used, one produced by the United States Department of Agriculture and the other produced by FMC. The USDA collagen contained unhydrolyzed telepeptide linkages and required pretreatment to reduce collagenaselike activity of the enzyme. Activity analysis of the immobilized enzyme complex showed that membranes with enzyme loading less than 10 mg enzyme/g of wet membrane in the reactor were dimensionally stable. The degree of crosslinking was an important parameter. Membranes with structural opening up to three times the initial dry thickness were found to be the maximum limit for controlled release of enzyme from the collagen membrane during enzymatic reaction. Higher activities and better stability of the enzyme in collagen membrane were found for covalent crosslinking of the enzyme to treated collagen films. The hydrolysis of soybean vegetable protein with the immobilized enzyme in a recycle reactor at enzyme loading of mg/g of wet membrane at 40°C, pH 3.4, produced 56.5% of soluble protein in 10h. The production is equivalent to 1.84 h total contact time between the substrate and the immobilized enzyme. The average productivity based on a stable enzyme activity and 20g of dry membrane was 329 mg of protein/g/mg of active enzyme immobilized. The productivity of the free enzyme in a batch reactor was 62.5 mg protein/h/mg enzyme.     

Arthrobacter sp. lipase immobilization for preparation of enantiopure masked β-amino alcohols

Recent reports on immobilization of lipase from Arthrobacter sp. (ABL, MTCC 5125; IIIM isolate) on insoluble polymers have shown altered properties including stability and enantioselectivity. Present work demonstrates a facile method for the preparation of enantiopure β-amino alcohols by modulation of ABL enzyme properties via immobilization on insoluble as well as soluble supports using entrapment/covalent binding techniques. Efficacies of immobilized ABL on insoluble supports prepared from tetraethylorthosilicate/aminopropyltriethoxy silane and soluble supports derived from copolymerization of N-vinyl pyrrolidone-allylglycidyl ether (ANP type)/N-vinyl pyrrolidone-glycidyl methacrylate (GNP type) for kinetic resolution of masked β-amino alcohols have been studied vis-à-vis free ABL enzyme/wet cell biomass. The immobilized lipase on different insoluble/soluble supports has shown 21–110 mg/g protein binding and 30–700 U/g activity for hydrolyzing tributyrin substrate. The findings have shown a significant enhancement in enantioselectivity (ee 99%) vis-à-vis wet cell biomass providing ee 70–90% for resolution of β-amino alcohols.     

Immobilization of porcine pancreatic lipase on glycidyl methacrylate grafted poly vinyl alcohol

Graft copolymerization of glycidyl methacrylate (GMA) on to polyvinyl alcohol (PVA) using benzophenone (BP) as initiator was carried out. Grafted PVA was used as carrier for pancreatic lipase immobilization. The effects of GMA and BP concentrations as well as grafting reaction times on grafting yields and activities of the immobilized lipase were determined. The influence of enzyme concentrations was also studied. The optimal conditions for the grafting reaction were: 1 h at 15 mM BP and 2.3 M GMA, the optimum enzyme concentration for immobilization was 1 mg/ml. After optimization of the immobilization process a physical and chemical characterization of the immobilized enzyme was performed. Furthermore, the thermal, pH, storage and operational stability of the immobilized enzyme in comparison to the free form was tested.     

Phytate degradation by immobilized<Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> phytase in soybean-curd whey

Saccharomyces cerevisiae CY phytase-producing cells were immobilized in calcium alginate beads and used for the degradation of phylate. The maximum activity and immobilization yield of the immobilized phytase reached 280 mU/g-bead and 43%, respectively. The optimal pH of the immobilized cell phytase was not different from that of the free cells. However, the optimum temperature for the immobilized phytase was 50°C, which was 10°C higher than that of the free cells; pH and thermal stability were enhanced as a consequence of immobilization. Using the immobilized phytase, phytate was degraded in a stirred tank bioreactor. Phytate degradation, both in a buffer solution and in soybean-curd whey mixture, showed very similar trends. At an enzyme dosage of 93.9 mU/g-phytate, half of the phytate was degraded after 1 h of hydrolysis. The operational stability of the immobilized beads was examined with repeated batchwise operations. Based on 50% conversion of the phytate and five times of reuse of the immobilized beads, the specific degradation (g phytate/g dry cell weight) for the immobilized phytase increased 170% compared to that of the free phytase.