利用麻风树油驯化筛选高活性脂肪酶产生菌及其催化酯化反应

以1株分解麻风树油的脂肪酶产生菌Pseudomonas sp. LP-1为出发菌株, 通过麻疯树油定向驯化筛选获得1株酶活较高且产酶稳定的菌株P. sp. X-2-45, 其水解酶活为29.79 U/mL, 比原始菌株提高了288%。对P. sp. X-2-45生长与产酶特征、对植物油脂水解能力及在有机相中催化脂肪酸和有机醇间的酯化反应研究发现, 该菌株生长速率和产酶速率明显加快, 培养30 h时生物量和酶活达到最大, 稳定期延长, 培养过程中脂肪酶在培养基中的稳定性提高。以麻疯树油诱导合成的P. sp. X-2-45脂肪酶对麻疯树油的水解能力比原始菌株提高了378%, 说明采用麻风树油定向驯化可提高脂肪酶对相应底物的水解能力。X-2-45脂肪酶可以催化月桂酸与正丁醇、正辛醇、月桂醇和丙三醇之间, 棕榈酸、硬脂酸与甲醇、正辛醇、月桂醇和丙三醇之间, 油酸与甲醇、正丁醇、正辛醇、月桂醇和丙三醇之间发生酯化反应。     

脂肪酶假单胞菌的分离培养及最佳产酶条件研究

以麻疯树油为唯一碳源,从以粉碎的麻疯树种子处理过的土壤中分离筛选出1株脂肪酶活性较高的菌株,初步鉴定为假单胞菌属(Pseudomonas).实验观察了碳源、氮源、无机盐及发酵工艺对产酶的影响,摇瓶发酵结果表明.该菌株最适产酶培养基的组成是(%,w/v):橄榄油2,酵母膏0.5,(NH4)2SO4 0.5,MgCl2·6H2O 0.5,最适产酶温度为30℃,最佳产酶pH为6.5,转速180r/min,发酵培养36h酶活达到最高,为14.17U/mL.本研究为以麻疯树油为原料酶法生产生物柴油奠定了一定的基础.     

酵母菌促进铅和镉胁迫下麻疯树生长的研究

为了筛选对铅和镉具有抗性和吸附性的酵母菌,构建麻疯树根系-酵母菌联合修复体系,促进高浓度铅和镉胁迫下麻疯树的生长。该研究分别从麻疯树的根段、珙桐的茎段、珙桐的根段分离到3株具有铅、镉抗性的酵母菌,分别命名为Jc、Di1、Di2,测定了三者对铅、镉的抗性和吸附性,并将筛选出的2株能吸附铅、镉的酵母菌菌株接种到麻疯树幼苗,研究接种两种酵母菌的麻疯树植株对铅、镉胁迫的响应。结果表明:经形态学和生理生化特征观察,Jc初步鉴定红酵母属(Rhodotorula sp.),Di1为假丝酵母属(Candida sp.),Di2为德巴利酵母属(Debaryomyces sp.)。三种酵母菌对铅、镉都有一定的抗性,其抗性能力的大小为JcDi2Di1。Di1和Jc对铅和镉都具有一定的吸附性将其用于接种麻疯树幼苗。与不接种酵母菌(CK)的麻疯树植株相比,接种Di1和Jc的麻疯树植株在根、茎、叶、全株干重方面显著增加,叶绿素、全株氮、全株磷浓度显著增加,SOD、POD、CAT的活性提高,丙二醛(MDA)浓度显著下降。从综合接种效应来看,Jc、Di1作为铅、镉的钝化剂,是铅、镉胁迫下促进麻疯树生长的备选菌株,这对于提高麻疯树对铅、镉污染土壤修复效率具有重要的意义。     

麻疯树种子的研究进展

麻疯树（Jatropha curcas L．）为大戟科（Euphorbiaceae）麻疯树属半肉质小乔木或大灌木,具有很强的抗旱、耐贫瘠的特性。麻疯树的根、树皮、叶和种子均可人药。种子中主要含有脂肪类物质、蛋白质和萜类物质,其毒素为麻疯树毒蛋白和种子油。种仁中的含油量约为50％,可作为理想的生物柴油;毒蛋白、种子油及其他种子提取物可作为生物农药。关于麻疯树种子的发育、脱水行为及其调控研究较少。麻疯树是二种具有重要经济价值的战略资源。     

具有ACC脱氨酶活性的麻疯树根际促生菌(PGPR)的分离筛选及系统发育分析

[目的]获得具有产ACC、IAA,铁载体,能固氮或解磷的潜在促生菌株.[方法]通过稀释涂布的方法,从麻疯树根际土壤中分离得到98株细菌,从中选取28株以产l-氨基环丙烷-1-羧酸(ACC)脱氨酶为主要促生指标进行筛选,同时检测了其产吲哚乙酸(IAA)、固氮、解磷及铁载体等促生指标的能力.[结果]结果显示,46％的菌株能产ACC脱氨酶,其含量最高可达到128.308 μmol α-KA/(mg.h),68％的菌株能产生IAA,54％的菌株有固氮的能力,32％的菌株有解磷的能力.少量菌株同时具有产ACC脱氨酶、IAA,固氮,解磷等能力.挑选代表性菌株进行16S rRNA序列分析,这些菌株属于芽孢杆菌属(Bacillus)、节杆菌属(Arthrobacter)、假单胞菌属(Pseudomonas)和产碱杆菌属(Advenella)等8个属,其中多数菌株(50％)属于芽孢杆菌属,系统发育分析表明菌株KLBMP 4817、KLBMP 4821和KLBMP 4824为窄食单胞菌属(Stenotrophomonas)和类芽孢杆菌属(Paenibacillus)的潜在新种.[结论]攀枝花麻疯树根际土壤细菌中含有丰富的遗传多样性,且存在大量的促生菌株.其中,菌株KLBMP 4804产ACC脱氨酶含量最高.菌株KLBMP4820产IAA含量最显著.     

白地霉一新变种的鉴定及其脂肪酶的研究

从各种加工厂采集的污泥、废水样品中,分离出157株菌落呈白色,绒毛状或粉状,皮膜型或脂泥型有脂肪酶活力的菌株。经筛选,获得一株产生高活力脂肪酶的菌株——S863,其发     

麻疯树分子生物学研究进展

麻疯树Jatropha curcas L.作为一种新兴的生物柴油型能源树种已经得到广泛的认可,关于它的各项研究持续升温。文中综述了近年来国内外关于麻疯树分子生物学方面的研究进展,一是揭示麻疯树遗传多样性和系统分类的分子标记研究;二是全面解析麻疯树分子网络的基因组、转录组和蛋白质组研究;三是以培育优质高抗品系为目标的代谢和发育调控相关基因的分离、克隆和功能研究;最后讨论了目前研究的不足和麻疯树未来分子生物学研究的方向。     

麻疯树的二萜成分

从麻疯树（Jatropha curcas L.)的根中分离得到3个二萜,鉴定为麻疯树酚酮A（iatropholone A)。麻疯树酚酮B（jatropholone B)和一个新的二萜,其结构推定为16－羟基麻疯树酚酮（16-hydroxyjatropholonc),定名麻疯树醇（jatrophol),同时还得到麻疯素（jatrophin),β-谷甾醇－β-D－葡萄糖甙（β－D－glucoside-β-sitosterol),tomentin,蒲公英脑（taraxerol)以及β-谷甾醇。     

麻疯树的二萜成分

从麻疯树（Jatropha curcas L.)的根中分离得到3个二萜,鉴定为麻疯树酚酮A（iatropholone A)。麻疯树酚酮B（jatropholone B)和一个新的二萜,其结构推定为16－羟基麻疯树酚酮（16-hydroxyjatropholonc),定名麻疯树醇（jatrophol),同时还得到麻疯素（jatrophin),β-谷甾醇－β-D－葡萄糖甙（β－D－glucoside-β-sitosterol),tomentin,蒲公英脑（taraxerol)以及β-谷甾醇。     

三种植物油及其生物柴油中脂肪酸组成的比较研究

生物柴油油料植物的选择是多样化的。通过对麻疯树,青刺果及乌桕三种产于西南的油料植物油分的理化性质及它们的生物柴油进行GC/MS分析,以麻疯树油为参照油分,对比青刺果油和乌桕油,找出适合作生物柴油油料植物油分的特点,为生物柴油油料植物的选择提供了依据。     

Selection of lipase producing yeasts for methanol-tolerant biocatalyst as whole cell application for palm-oil transesterification

Methanol-tolerant lipase producing yeast was successfully isolated and selected thorough ecological screening using palm oil-rhodamine B agar as one step-approach. All 49 lipase-producing yeasts exhibited the ability to catalyze esterification reaction of oleic acid and methanol at 3 molar equivalents. However, only 16 isolates catalyzed transesterification reaction of refined palm oil and methanol. Rhodotorula mucilagenosa P11I89 isolated from oil contaminated soil showed the strongest hydrolytic lipase activity of 1.2U/ml against palm oil. The production of oleic methyl ester and fatty acid methyl ester (FAME) of 64.123 and 51.260% was obtained from esterification and transesterification reaction catalyzed by whole cell of R. mucilagenosa P11I89 in the presence of methanol at 3 molar equivalents against the substrates, respectively. FAME content increased dramatically to 83.29% when 6 molar equivalents of methanol were added. Application of the methanol-tolerant-lipase producing yeast as a whole cell biocatalyst was effectively resolved major technical obstacles in term of enzyme stability and high cost of lipase, leading to the feasibility of green biodiesel industrialization.     

Immobilization of Burkholderia sp. lipase on a ferric silica nanocomposite for biodiesel production

In this work, lipase produced from an isolated strain Burkholderia sp. C20 was immobilized on magnetic nanoparticles to catalyze biodiesel synthesis. Core-shell nanoparticles were synthesized by coating Fe(3)O(4) core with silica shell. The nanoparticles treated with dimethyl octadecyl [3-(trimethoxysilyl) propyl] ammonium chloride were used as immobilization supporters. The Burkholderia lipase was then bound to the synthesized nanoparticles for immobilization. The protein binding efficiency on alkyl-functionalized Fe(3)O(4)-SiO(2) was estimated as 97%, while the efficiency was only 76% on non-modified Fe(3)O(4)-SiO(2). Maximum adsorption capacity of lipase on alkyl-functionalized Fe(3)O(4)-SiO(2) was estimated as 29.45 mg g(-1) based on Langmuir isotherm. The hydrolytic kinetics (using olive oil as substrate) of the lipase immobilized on alkyl-grafted Fe(3)O(4)-SiO(2) followed Michaelis-Menten model with a maximum reaction rate and a Michaelis constant of 6251 Ug(-1) and 3.65 mM, respectively. Physical and chemical properties of the nanoparticles and the immobilized lipase were characterized by Brunauer-Emmett-Teller (BET) analysis, scanning electron microscope (SEM), and Fourier transform infrared spectroscopy (FT-IR). Moreover, the immobilized lipase was used to catalyze the transesterification of olive oil with methanol to produce fatty acid methyl esters (FAMEs), attaining a FAMEs conversion of over 90% within 30 h in batch operation when 11 wt% immobilized lipase was employed. The immobilized lipase could be used for ten cycles without significant loss in its transesterification 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.     

复合脂肪酶协同催化制备生物柴油的研究

【目的】探讨复合酶协同催化体系在含水量较高的体系中催化油脂制备生物柴油的工艺条件。【方法】通过基因工程手段在毕赤酵母中分别高效分泌表达南极假丝酵母脂肪酶(CALB)和米根霉脂肪酶(ROL),构建CALB和ROL复合酶协同催化体系制备生物柴油,利用单因素实验优化工艺条件,以甲酯化得率作为复合酶协同催化体系效能的评价标准。【结果】优化工艺条件为:CALB?ROL最佳复合酶配比为7?3,每克大豆油中加入16 U的复合脂肪酶,甲醇与大豆油摩尔比为4?1,并按0 h时2?1醇油摩尔比,12 h和24 h时以1?1醇油摩尔比分批加入甲醇,含水量为30%-60%之间,40°C反应29-34 h,甲酯得率达到93%。【结论】该复合酶协同催化体系对环境友好,与常规酶法制备生物柴油工艺相比对酶的使用量和催化时间减少幅度都在50%以上,本复合酶协同催化体系能有效降低生物柴油制备成本,具有较好的工业化应用前景。     

脂肪酶催化合成生物柴油的研究

生物柴油是用动植物油脂或长链脂肪酸与甲醇等低碳醇合成的脂肪酸甲酯,是一种替代能源。这里探讨了生物法制备生物柴油的过程,采用脂肪酶酯化和酯交换两条工艺路线进行催化合成。深入研究制备过程中,不同脂肪酶、酶的用量和纯度、有机溶剂、低碳醇的抑制作用、吸水剂的作用、反应时间和进程、底物的特异性和底物摩尔比等参数对酯化过程的影响。试验结果表明,采用最佳酯化反应参数和分批加入甲醇并用硅胶作脱水剂的工艺过程,酯化率可以达到92％,经分离纯化后的产品GC分析的纯度可达98％以上,固定化酶的使用半衰期可达到360h。同时对酯交换制备生物柴油过程中,甲醇的用量和甲醇的加入方式对脂肪酶催化过程的影响作了初步研究,优化后的酯交换率可达到83％。     

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)).     

Biocatalytic methanolysis activities of cross-linked protein-coated microcrystalline lipase toward esterification/transesterification of relevant palm products

Biocatalysis by immobilized lipase is an efficient alternative process for conversion of crude vegetable oil with high free fatty acid content to biodiesel, which is the limit of the conventional alkaline-catalyzed reaction. In this study, influences of solid-state organic and inorganic buffer core matrices with different pK_a on catalytic performance of cross-linked protein coated microcrystalline biocatalysts prepared from Thermomyces lanuginosus lipase (CL-PCMC-LIP) toward esterification of palmitic acid (PA), transesterification of refined palm oil (RPO), and co-ester/transesterification of crude palm oil (CPO) to fatty acid methyl ester (FAME) was studied. Glycine, CAPSO (3-(cyclohexylamino)-2-hydroxy-1-propanesulfonic acid), and TAPS ([(2-hydroxy-1,1-bis(hydroxymethyl)ethyl)amino]-1-propanesulfonic acid) were shown to be potent core matrices for these reactions. The optimal reaction contained 4:1 [methanol]/[fatty acid] molar equivalence ratio with 20% (w/w) CL-PCMC-LIP on glycine in the presence of tert-butanol as a co-solvent. Deactivation effect of glycerol on the biocatalyst reactive surface was shown by FTIR, which could be alleviated by increasing co-solvent content. The maximal FAME yields from PA, RPO, and CPO reached 97.6, 94.9, and 95.5%, respectively on a molar basis under the optimum conditions after incubation at 50 °C for 6 h. The biocatalyst retained >80% activity after recycling in five consecutive batches. The work demonstrates the potential of CL-PCMC-LIP on one-step conversion of inexpensive crude fatty acid-rich feedstock to biodiesel.     

Enzymatic transesterification of Jatropha oil

Background  

Transesterification of Jatropha oil was carried out in t-butanol solvent using immobilized lipase from Enterobacter aerogenes. The presence of t-butanol significantly reduced the negative effects caused by both methanol and glycerol. The effects of various reaction parameters on transesterification of Jatropha oil were studied.     

Lipase catalyzed methanolysis to produce biodiesel: Optimization of the biodiesel production

A lipase from Candida sp., suitable for transesterification of fats and oils to produce fatty acid methyl ester (FAME), was immobilized on a cheap cotton membrane, in this paper. The conversion ratio of salad oil to biodiesel could reach up to 96% with the optimal reaction conditions. Continuous reaction in a fixed bed reactor was also investigated. A three-step transesterification with methanol (methanolysis) of oil was conducted by using a series of nine columns packed with immobilized Candida sp. 99–125 lipase. As substrate of the first reaction step, plant or waste oil was used together with 1/3 molar equivalent of methanol against total fatty acids in the oil. Mixtures of the first- and second-step eluates and 1/3 molar equivalent of methanol were used for the second- and third-reaction steps. A hydrocyclone was used in order to on-line separate the by-product glycerol after every 1/3 molar equivalent of methanol was added. Petroleum ether was used as solvent (3/2, v/v of oil) and the pump was operated with a flow rate of 15 L/h giving an annual throughput of 100 t. The final conversion ratio of the FAME from plant oil and waste oil under the optimal condition was 90% and 92%, respectively. The life of the immobilized lipase was more than 10 days. This new technique has many strongpoints such as low pollution, environmentally friendly, and low energy costs.