反应介质对脂肪酶稳定性的影响

脂肪酶Ｌｉｐｏｚｙｍｅ＾ＩＭ在有机溶剂中的热稳定性显著提高,在水溶液中,热处理温度高于５０℃后,其催化甘油三酯水解的活力迅速下降,温度升到６０℃时,水解活力仅残存１３．６％,温度高于７０℃该酶完全失活,而在有机溶剂正庚烷中,温度高达８５℃仍表现出较高的活性,反应介质的疏水性越强,酶抗超声辐射变性作用的能力越强,经同样的超声辐射处理后,正已烷中Ｌｉｐｏｚｙｍｅ＾ＩＭ的酯水解活力仅损失１１．８％,而在     

有机溶剂对脂肪酶ipozyme^IM催化活性的影响

脂肪酶Ｌｉｐｏｚｙｍｅ＾ＩＭ经有机溶剂浸泡处理后活性显著提高。该文系统地探讨了有机溶剂特性,有机溶剂水含量以及有机溶剂包温度和浸泡时间对Ｌｉｐｏｚｙｍｅ＾ＩＭ催化活性的影响。发现Ｌｉｐｏｚｙｍｅ＾ＩＭ经疏水性较强的有机沉沦 泡处理后活性成倍增长;浸泡的最佳温度为６０℃左右,浸泡时间对酶活影响不大;随着有机溶剂水含量的增加,酶活性急剧下降。     

康宁木霉液体深层发酵生产纤维素酶

以康宁木霉（ Ｔｒｉｃｈｏｄｅｒｍａ　ｋｏｎｉｎｇｉｉ） Ｔ２１５为生产菌,在 ３０ｔ气升式发酵罐中进行了液体深层发酵生产纤维素酶的扩大试验。一、二级罐种子培养基由８％麦麸组成,种龄２４ｈ。产酶培养基由６％稻草粉,１％麦麸和１％蛋白胨组成,起始ｐＨ５．０。每罐装２２ｔ培养基,１０％接种量,通气量０．４ｖｖｍ,罐压０．０８ＭＰａ,２９℃±１℃培养 ９６ｈ。连续试验 ５批,平均发酵液酶活力： ＣＭＣ－Ｎａ活力 ７８．３ＩＵ／ｍＬ,脱脂棉活力 １.３ＩＵ／ｍＬ,水杨苷活力１.４ＩＵ／ｍＬ,滤纸活力     

D201—GM大孔树脂吸附交联固定菊粉酶的研究

克鲁维酵母Ｙ－８５产生的胞内菊粉酶,以Ｄ２０１－ＧＭ大孔径阴离子交换树脂吸附交联法固定化,其制备固定化酶（ＩＥ）的适宜条件：树脂吸附酶时ｐＨ６．５、温度３０℃、时间３ｈ;交联时戊二醛浓度０．０３％、温度４℃、时间３ｈ。上述条件下制得ＩＥ的活性产率可达６２％,水解菊粉底物的最适温度５５℃,对热的稳定性和贮存稳定性均有明显提高,用ＩＥ填充床反应器连续降解菊粉抽提液（总糖４．５％）的实验结果表明,进料空     

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％。     

影响微小毛霉凝乳酶活力的因素

介绍影响微小毛霉凝乳酶活力的几个因素．该微小毛霉凝乳酶的最适ｐＨ在５．４～７．０范围;在ｐＨ２～７之间酶活保持稳定;凝乳酸最适温度在２５～７０℃,并随温度的增高酶活增大;６０℃处理１０ｍｉｎ酶活损失６８％,并随时间的延长酶活损失加大;Ｆｅ２＋、Ｍｇ２＋对酶有激活作用,Ｎａ＋、Ｃｕ２＋对酶有抑制作用。     

产纤维素酶菌株宇佐美曲霉Y-11产酶条件及酶性质的研究

通过正交试验,对宇佐美曲霉纤维素酶固态发酵条件进行了研究,其较适培养基为：麸皮与稻草配比为２：３,氮源：尿素,含水量：２００％（液固比）,ｐＨ：５．５。２８－３０℃培养７２小时,ＣＭＣ酶活力为５．０５（ｕ／ｍｌ）,滤纸酶活力达到１．０４（ｕ／ｍｌ）。ＣＭＣ酶及滤纸酶最适ｐＨ分别为４．４１、６．０６;最适温度分别为６５℃、５５℃。酶的热稳定性与ｐＨ稳定性较高。     

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。     

神经节苷脂GM_3对肌质网Ca~（2＋）－ATP酶活力的调节

研究了神经节苷脂ＧＭ_３参入肌质网膜后Ｃａ~（２＋）－ＡＴＰ酶活力的变化,结果表明：ＧＭ_３参入肌质网膜后,对肌质网Ｃａ~（２＋）ＡＴＰ酶活性（ＡＴＰ水解活力与转运活力）有明显的激活作用．当参入的ＧＭ_３浓度为８μｍｏｌ／Ｌ、参入时间为１２０ｍｉｎ、温度为３０℃时,对Ｃａ~（２＋）－ＡＴＰ酶的激活作用最大．     

湖南尖吻蝮蛇毒两个出血毒素的纯化和理化性质

经ＳｅｐｈａｄｅｘＧ－７５凝胶过滤,ＱＡＥ－ＳｅｐｈａｄｅｘＡ－５０和ＣＭ－ＳｅｐｈａｄｅｘＣ－２５离子交换层析的步骤,从湖南产尖吻蝮（Ｄｉｅｎａｇｋｉｓｔｒｏｄｏｎａｃｕｔｕｓ）蛇毒中纯化出两个出血毒素（ＤａＨＴ－１和ＤａＨＴ－２）．ＳＤＳ－ＰＡＧＥ测得分子量均为２３．５ｋＤ,ＩＥＦ－ＰＡＧＥ测得等电点分别为５．６和５．２,两者具有相似的氨基酸组成,其中酸性氨基酸（Ａｓｘ,Ｇｌｘ）分别占２３％和２４％,ＤａＨＴ－１和ＤａＨＴ－２的最小出血剂量（ＭＨＤ）分别为０．５μｇ和０．８μｇ。都具蛋白水解酶活性,无对ＴＡＭＥ,ＢＡＥＥ的水解活性和ＰＬＡ２酶活性．两者的蛋白水解酶活力与出血活性并非正相关．ＤａＨＴ－１和ＤａＨＴ－２的最适温度分别为３５℃和４０℃,最适ｐＨ为６－９,对热均不稳定,温度高于６０℃活性完全丧失。金属离子的分析显示每摩尔毒素蛋白约含０．５ｍｏｌ的Ｚｎ,１ｍｏｌ的Ｃａ,较多的Ｎａ、Ｋ、Ｍｇ,不含Ｃｏ。     

有机相中超声辐照对脂肪酶活性的影响

酶在有机相中的催化作用是８０年代以来酶工程学研究的热点之一．虽然酶在有机相中的催化反应有许多优点［１］,但在工业生产上的应用却很有限,这主要是有机相中的酶促反应速度太慢,反应周期太长之故．１９９１年Ｖｕｌｆｓｏｎ等报道了超声辐照对有机相中枯草蛋白酶催...     

Different enzyme requirements for the synthesis of biodiesel: Novozym 435 and Lipozyme TL IM

Enzymatic syntheses of biodiesel via alcoholysis of different vegetable oils (sunflower, borage, olive and soybean) have been studied. Loss of lipase activity induced by the nucleophile is greater with methanol than with ethanol, and is greater for Lipozyme TL IM than for Novozym 435. The optimum volume of ethanol depends on the loading of solid biocatalyst and is higher for preparations of Novozym 435 than for Lipozyme TL IM. Maximum rates were obtained with Lipozyme TL IM, for a molar ratio of alcohol to FA residues of 0.33. By contrast, Novozym 435 requires at least a 2:1 ratio. Alcoholysis of the vegetable oils is faster with Lipozyme TL IM than with Novozym 435. Use of a high loading of Novozym 435 (50% w/w) and a large molar excess of ethanol are required to obtain an initial rate similar to that obtained with Lipozyme TL IM at a lower enzyme loading (10% w/w) and an equimolar ratio of ethanol and FA residues. Novozym 435 produces quantitative conversions in only 7h at 25 degrees C, but complete conversions are not obtained with Lipozyme TL IM. Three stage stepwise addition of ethanol yields 84% conversion to ethyl esters for Lipozyme TL IM. Hence use of Novozym 435 is preferred. After nine cycles in a batch reactor Novozym 435 retained 85% of its initial activity.     

Lipase-catalyzed transesterification of rapeseed oils for biodiesel production with a novel organic solvent as the reaction medium

tert-Butanol, as a novel reaction medium, has been adopted for lipase-catalyzed transesterification of rapeseed oil for biodiesel production, with which both the negative effects caused by excessive methanol and by-product glycerol could be eliminated. Combined use of Lipozyme TL IM and Novozym 435 was proposed further to catalyze the methanolysis and the highest biodiesel yield of 95% could be achieved under the optimum conditions (tert-butanol/oil volume ratio 1:1; methanol/oil molar ratio 4:1; 3% Lipozyme TL IM and 1% Novozym 435 based on the oil weight; temperature 35 °C; 130 rpm, 12 h). There was no obvious loss in lipase activity even after being repeatedly used for 200 cycles with tert-butanol as the reaction medium. Furthermore, waste oil was also explored for biodiesel production and it has been found that lipase also showed good stability in this novel system.     

Improved high-pressure enzymatic biodiesel batch synthesis in near-critical carbon dioxide

The enzymatic synthesis of biodiesel by a high-pressure semi-continuous process in near-critical carbon dioxide (NcCO(2)) was studied. Biodiesel synthesis was evaluated in both batch and semi-continuous systems to develop an effective process. Batch processing demonstrated the advantageous properties of NcCO(2) as an alternative reaction medium. Three immobilized lipases (Novozym 435, Lipozyme RM IM, and Lipozyme TL IM from Novozymes) were tested, with Lipozyme TL IM the most effective, showing the highest conversion. Biodiesel conversion from several edible and non-edible oil feedstocks reached >92%. Higher conversion (99.0%) was obtained in a shorter time by employing repeated batch processes with optimized conditions: 44.3 g (500 mM) canola oil, a substrate molar ratio (methanol:oil) of 3:1, an enzyme loading of 20 wt% (of the oil used), at 30 °C, 100 bar, and 300 rpm agitation. The enzyme maintained 80.2% of its initial stability after being reused eight times. These results suggest that this method produces biodiesel energy-efficiently and environment-friendly.     

Lipase-catalyzed synthesis and antibacterial activity of N-vanillylnonanamide

N-vanillylnonanamide (VAN) was successfully synthesized from vanillylamine hydrochloride by enzymatic catalysis in supercritical carbon dioxide (SC–CO₂). Five commercial lipases, Novozyme 435, Lipozyme IM, Amano PS, Amano G and Sigma Candida cylindracea type VII, as biocatalysts for VAN synthesis were compared. Lipozyme IM exhibited best yields of tested lipases. Various parameters such as time, temperature, pressure and vanillylamine hydrochloride/nonanoic anhydride ratio that influenced the reaction were investigated. Nonanoic anhydride showed the best acyl donor of the employed substrates. An amidation yield of 40% was obtained when nonanoic anhydride and Lipozyme IM were used at 170 bar and 50 °C for 23 h in SC–CO₂. Besides, addition of 2 mM divalent salts (CuCl₂ and ZnCl₂) significantly increased 11–23% yield of the VAN. The enzyme operational stability suggested that Lipozyme IM maintained over 50 °C of the initial activity for the synthesis of VAN after reuse for 69 h. Furthermore, in vitro, VAN behaved as a potential antibacterial against Escherichia coli.     

Production of diacylglycerols from glycerol monooleate and ethyl oleate through free and immobilized lipase-catalyzed consecutive reactions

The ability of free and immobilized lipase on the production of diacylglycerols (DAG) by transesterification of glycerol monooleate (GMO) and ethyl oleate was investigated. Among three free lipases such as lipase G (Penicillium cyclopium), lipase AK (Pseudomonas fluorescens) and lipase PS (Pseudomonas cepacia), lipase PS exhibited the highest DAG productivity, and the DAG content gradually increased up to 24 hours reaction and then remained steady. The comparative result for DAG productivity between free lipase PS and immobilized lipases (lipase PS-D and Lipozyme RM IM) during nine times of 24 hours reaction indicated that total DAG production was higher in immobilized lipase PS-D (183.5mM) and Lipozyme RM IM (309.5mM) than free lipase PS (122.0mM) at the first reaction, and that the DAG production rate was reduced by consecutive reactions, in which more sn-1,3-DAG was synthesized than sn-1,2-DAG. During the consecutive reactions, the activity of lipase PS was relatively steady by showing similar DAG content, whereas DAG production of lipase PS-D and Lipozyme RM IM was gradually decreased to 69.9 and 167.1mM at 9th reaction, respectively, resulting in 62% and 46% reduced production when compared with 1st reaction. Interestingly, from 7th reaction lipase PS produced more DAG than immobilized lipase PS-D, and exhibited a stable activity for DAG production. Therefore, the present study suggested that DAG productivity between GMO and ethyl oleate was higher in immobilized lipases than free lipases, but the activity was reduced with repeated uses.     

虎纹捕鸟蛛毒液中透明质酸酶的纯化和部分性质的研究

用分子筛（岛津ＤＩＯＬ－１５０柱）和阳离子交换（岛津ＷＣＸ－１柱）高效液相色谱从虎纹捕鸟蛛（Ｓｅｌｅｎｏｃｏｓｍｉａｈｕｗｅｎａ）毒液中分离提纯透明质酸酶（Ｈｙａｌｕｒｏｎｉｄａｓｅ,ＥＣ３．２．１．３５）．经等电聚焦电泳为一条带,ｐＩ＝７．２．经ＳＤＳ－聚丙烯酰胺凝胶电泳测得分子量为４０ｋＤ,经凝胶过滤测得分子量为４０．７ｋＤ。以透明质酸为底物时在ｐＨ３．５─５．５范围内有较大活性,最适ｐＨ值为４．０;在ｐＨ４．５─６．０范围内稳定,在反应温度为３０─６０℃时有较大活性,最适温度为５０℃;对热稳定,０．１５ｍｏｌ／Ｌ的ＮａＣｌ对酶活性有一定的稳定作用．３％的肝素、５００μｍｏｌ／Ｌ的Ｈｇ~（２＋）、Ｆｅ~（２＋）、Ｃｕ~（２＋）对酶活性有明显的抑制作用。     

脂肪酶协同催化猪油合成生物柴油工艺研究

探讨了以乙酸甲酯为酰基受体两种脂肪酶协同催化猪油转酯合成生物柴油的工艺条件。首先利用单因子试验确定2种固定化脂肪酶Novozym435、Lipozyme TLIM单独作为催化剂时的最佳酶用量为40％,反应温度为50℃,乙酸甲酯用量为14（相对于油的摩尔比）。在此基础上,采用3因素5水平和3个中心点的中心组分旋转设计法研究了上述2种脂肪酶协同使用时脂肪酶用量（g/g）、混合酶的配比（%/%）以及乙酸甲酯用量诸因素共同作用对转酯反应转化率的影响。优化后的反应条件为：总酶用量为40％,混合酶配比为50/50,乙酸甲酯用量为14,在该条件下甲酯得率可达97.6％,比同质量的Novozym435、Lipozyme TLIM的催化活性分别高出7.6％、22.3％。表明脂肪酶协同催化猪油合成生物柴油工艺可以较好地提高甲酯得率,并且节约生产成本。     

缢蛏碱性磷酸酶胍溶液中分子折叠与活力变化研究

报道了缢蛏碱性磷酸酶（简称ＡＬＰ）经不同浓度盐酸胍处理时酶的分子构象所发生的变化以及酶变化和失活的动力学过程。在胍中酶荧光发射峰强度下降,紫外差光谱在２４６ｎｍ和２８５ｎｍ处出现２个负峰,ＣＤ谱中酶的α螺旋度下降,且随浓度增大,变化程度也加大。动力学研究表明,酶在０．５ｍｏｌ／Ｌ、１．０ｍｏｌ／Ｌ、２．０ｍｏｌ／Ｌ３．０ｍｏｌ／Ｌ、４．０ｍｏｌ／Ｌ盐酸胍中的变性速度常数分别为３．２１×１０~（－４）ｓ~（－１）、６．３８×１０~（－４）ｓ~（－１）、２．１７×１０~（－３）ｓ~（－１）、２．３３×１０~（－３）ｓ~９－１）、５．１７×１０~（－３）ｓ~（－１）;而酶在相应盐酸胍中的失活速度常数分别为２．３３×１０~（－４）ｓ~（－１）、３．５７×１０~（－４）ｓ~（－１）、５．８６×１０~（－４）ｓ~（－１）、１．１４×１０~（－３）ｓ~（－１）、３．４５×１０~（－３）ｓ~（－１）;表现为失活与构象伸展变化基本平行。