酪氨酸酚裂解酶的固定化与转化条件的优化

以欧文氏菌(Erwinia herbicola)来源的酪氨酸酚裂解酶的重组大肠埃希菌Escherichia coli BL21为研究对象,研究固定化大肠埃希菌生产L-酪氨酸的条件。以海藻酸钠为载体,采用单因素实验分别考察了载体材料、明胶浓度、反应时间、苯酚浓度和辅助剂(二氧化硅、硅藻土和碳酸钙)等因素对L-酪氨酸生产的影响,发现明胶浓度、反应时间、苯酚和碳酸钙等因素的影响较为显著,进而通过正交实验探索最优条件。结果表明,生产L-酪氨酸的最优条件:载体为4%海藻酸钠与6%明胶的混合载体,苯酚浓度0.08 mol/L,反应时间8 h,于载体中添加0.6%碳酸钙。此条件下,连续反应9次后L-酪氨酸的产量达到64.5 g/L,比优化前提高了451.3%。     

Citrobacter freundii休止细胞催化合成L-多巴

以在L 酪氨酸诱导下高效表达酪氨酸酚解酶的菌株Citrobacterfreundii 4 80 0 3 3的休止细胞为生物催化剂 ,以邻苯二酚、丙酮酸钠、醋酸铵为前体 ,选择性合成L DOPA。研究了反应温度、pH和前体浓度等对合成L DOPA的影响。最优反应条件下 ,反应 1 2h ,L DOPA的量可达到 9 5g/L。     

正交试验优化精制酪氨酸的工艺条件

采用正交实验法 ,将所得实验数据进行统计分析 ,对结晶法精制酪氨酸的工艺条件进行优化。结果表明 :在酪氨酸粗品质量分数为 6 %的溶液中 ,脱色剂ζ(活性炭∶活性白土 ) =3∶1,氨水的浓度为 5 % ,反应终点pH值为 2 .0 ,中和反应恒温水浴的温度为 6 0℃的工艺条件下 ,粗品经一次脱色、结晶就能获得品质合格的产品     

Citrobacter freundii休止细胞催化合成L-多巴

以在L-酪氨酸诱导下高效表达酪氨酸酚解酶的菌株Citrobacter freundii 48003-3的休止细胞为生物催化剂,以邻苯二酚、丙酮酸钠、醋酸铵为前体,选择性合成L-DOPA。研究了反应温度、pH和前体浓度等对合成L-DOPA的影响。最优反应条件下,反应12h,L-DOPA的量可达到9．5g／L。     

铜(II)-酪氨酸螯合物合成与分析

研究了铜(II)-酪氨酸螯合物的合成方法,探讨了影响合成工艺的主要因素,确定了原料配比、pH值、温度、反应时间等最佳合成条件.采用X射线衍射光谱对螯合物进行了表征,结果表明铜(II)能与酪氨酸形成螯合物.     

亮氨酸脱氢酶偶联NADH再生体系合成L-2-氨基丁酸

文中以大肠杆菌BL21(DE3)为宿主,构建两株分别共表达亮氨酸脱氢酶(LDH,来源蜡样芽孢杆菌)/甲酸脱氢酶(FDH,来源水生弯杆菌)和亮氨酸脱氢酶(LDH,来源蜡样芽孢杆菌)/醇脱氢酶(ADH,来源红球菌)的重组大肠杆菌。通过偶联两种不同NADH再生体系,以L-苏氨酸为起始原料,利用苏氨酸脱氨酶(L-TD)与LDH-FDH或LDH-ADH一锅法合成L-2-氨基丁酸,并对LDH-FDH工艺和LDH-ADH工艺进行对比优化。LDH-FDH工艺的最适反应pH为7.5,最适反应温度为35℃,通过加入50 g/L甲酸铵、0.3 g/L NAD+、10%LDH-FDH粗酶液(V/V)和7 500 U/L的L-TD酶液,对L-苏氨酸进行分批补加,以便控制2-丁酮酸浓度小于15 g/L,反应28 h,实现了L-2-氨基丁酸的产量为161.8 g/L,产率97%。LDH-ADH工艺的最适pH为8.0,最适反应温度为35℃,通过加入0.3 g/L NAD+、10%LDH-ADH粗酶液(V/V)及7 500 U/L的L-TD酶液,分批补加L-苏氨酸及1.2倍摩尔量异丙醇,以便控制2-丁酮酸浓度小于15g/L,且每生成约40g/L的L-2-氨基丁酸,抽真空去除丙酮,反应24h,实现了L-2-氨基丁酸的产量为119.6 g/L,产率98%。文中所采用的工艺及结果可为L-2-氨基丁酸的工业化提供一定的参考依据。     

酪氨酸流加方式对重组大肠杆菌发酵生产L-苯丙氨酸的影响

研究了流加浓度对酪氨酸重组大肠杆菌Escherichia coli BR-165(pAP-B03)发酵生产L-苯丙氨酸的影响.结果表明,诱导后L-酪氨酸流加加速了菌体的生长,提高了生产强度,缩短了发酵周期.在流加浓度为75 mg/h时,最大菌体干重达到了40.13 g/L(对照11.48 g/L),生产周期缩短到30 h(对照48 h),生产强度达到1.409 g/h/L(对照0.876 g/h/L).但是L-酪氨酸的流加对L-苯丙氨酸的最终产量没有明显的影响,因此可认为流加酪氨酸是减少发酵时间并提高生产强度的有效方法.本研究获得的酪氨酸流加方式对L-苯丙氨酸的工业化生产具有一定的指导意义.     

蛋白质体积对其亚细胞定位的影响

为了探索N(2)-L-丙氨酰-L-谷氨酰胺的合成工艺,确定最佳工艺以符合工业化生产的需求,以L-谷氨酰胺为原料,通过氨解反应合成L-丙氨酰-L-谷氨酰胺,并对反应条件及精制工艺进行优化.实验结果显示,当设定氨解反应温度为60℃,反应压力为0.5 MPa,反应时间为5.5h,以及氨水体积与α-D-氯丙酰-L-谷氨酰胺质量之比(V∶m)为1.5∶1时,将所得粗品用75％乙醇溶液进行精制,合成得到的N(2)-L-丙氨酰-L-谷氨酰胺经检测含量为99.65％,总收率约为55.77％.结果表明,经优化后的工艺简便安全、条件温和易控、生产周期短,适合工业化大量生产,且产品纯度、收率较高.     

甲基苯丙氨酸的合成与拆分

用取代的氯苄衍生物以及乙酰氨基丙二酸二乙酯为原料,合成了邻位、对位、间位甲基取代苯基丙氨酸。以上3种混旋氨基酸在37℃、pH值7.0、底物浓度0.1mol·L-1条件下用氨基酰化酶拆分得到6个光学异构体。本实验中采用的合成工艺适合工业化。     

非水溶剂中Rhizopus arrhizus脂肪酶催化合成三种酯的最佳条件(英文)

以少根根霉 (Rhizopusarrhizus)脂肪酶为催化剂 ,有机溶剂为反应介质 ,合成了 3种短链脂肪酸酯 .研究了反应温度、溶剂、底物浓度、底物摩尔比、吸水剂用量等因素对酯化反应的影响 .确定了3种酯的最佳合成条件 :(1)己酸乙酯 :反应温度为 4 0℃ ,环己烷为溶剂 ,0 2 5mol L底物浓度 ,酸醇摩尔比为 1∶1 2 ;(2 )乙酸异丙酯 :5 0℃ ,环己烷为溶剂 ,0 15mol L底物浓度 ,摩尔比为 1∶1;(3)乙酸异戊酯 :5 0℃ ,异辛烷为溶剂 ,0 2 0mol L底物浓度 ,摩尔比为 1∶1.三种酯合成时均需 0 12 5g ml的0 5nm分子筛为吸水剂 ,在 8h后 ,合成酯转化率达到 97%～ 99% .     

漆酶催化苯甲醇氧化制备苯甲醛

以自制的高活性漆酶为催化剂,考察漆酶催化苯甲醇制备苯甲醛的工艺条件(底物浓度、介质体系、溶剂体系、氢受体、酶的用量、通氧方式等)对氧化反应的影响。结果发现:优化反应条件为以2,2,6,6-四甲基哌啶-1-氧基(TEMPO)为介质体系且TEMPO与苯甲醇的摩尔比为1∶4、60 mmol/L的丙酮为氢受体、漆酶比酶活80 U/mL、60mmol/L的苯甲醇,反应体系通O20.5 h后密闭反应36 h,苯甲醛的产率达98%。     

Enzymatic synthesis of benzyl benzoate using different acyl donors: Comparison of solvent-free reaction techniques

In this study, benzyl benzoate was successfully synthesized via enzymatic acylation using three immobilized enzymes as biocatalysts. Different acyl donors (benzoic acid and benzoic anhydride), operation regimes (batch, fed-batch), mixing modes (conventional mechanical stirring and ultrasound), process parameters (temperature, substrate molar ratio of acyl donor to acyl acceptor), presence or absence of solvents, enzyme amount and type were evaluated. Benzoic acid is a solid that is difficult to solubilize and, thus, was not efficient as acyl donor for the synthesis of benzyl benzoate. On the other hand, benzoic anhydride was very effective for the acylation of benzyl benzoate, and the presence of an excess of benzyl alcohol was essential to ensure the solute-solvent intermolecular attractions and good substrate solubilization, allowing the ester synthesis to be performed in the absence of organic solvents. The ultrasound was effective in increasing increase the initial reaction rate and the final conversion (88 %). However, the Lipozyme TL-IM and RM-IM supports were damaged, and the reuse was unfeasible. The batch and fed-batch approaches in conventional stirring ensured high conversions of 92 and 90 %, respectively, for batch (anhydride: alcohol 1:6) and fed-batch (1:3) using the Lipozyme TL-IM as biocatalyst. The controlled addition of the anhydride (fed-batch) allowed the reduction of alcohol molar ratio but decreased the reaction rates, and the maximum conversions were reached only after 24 h, while the batch approach had 92 % of conversion after 6 h. The yield of benzyl benzoate was high at 6 wt.% of enzyme, low temperature (50 °C), and simple reactor operation (batch). Results show the feasibility of the synthesis of benzyl benzoate via acylation using a green process that may be an alternative route to the chemical synthesis.     

A comparative analysis of characteristic floral scent compounds in Prunus mume and related species

In order to investigate the difference in their characteristic floral scents between Prunus mume Siebold & Zucc. and the related Prunus species, their headspace volatiles and endogenous extraction were analyzed by gas chromatography–mass spectrometry. The efficiency of substrate utilization of the flowers was studied by incubating them with different alcohol substrates. Our results indicated that benzyl acetate is a dominant compound influencing the characteristic floral scent of P. mume. An alcohol substrate concentration of 4?mmol?L^?1 and a reaction time of 2?h were constituted the reaction condition for catalysis of exogenous alcohol substrates by the flowers. Under these conditions, Prunus sibirica exhibited the highest utilization efficiency for benzyl alcohol substrate while the utilization efficiency of Prunus persica was the lowest. Comparative analysis of several alcohol substrates indicated that the flowers of the tested species had selective specificity for benzyl alcohol substrates.     

Use of cyclodextrins as a cosmetic delivery system for fragrance materials: Linalool and benzyl acetate

The aim of this study was to increase the stability and water solubility of fragrance materials, to provide controlled release of these compounds, and to convert these substances from liquid to powder form by preparing their inclusion complexes with cyclodextrins (CDs). For this purpose, linalool and benzyl acetate were chosen as the fragrance materials. The use of beta-cyclodextrin (beta CD) and 2-hydroxypropyl-beta-cyclodextrin (2-HP beta CD) for increasing the solubility of these 2 fragrance materials was studied. Linalool and benzyl acetate gave a B-type diagram with beta CD, whereas they gave an A(L)-type diagram with 2-HP beta CD. Therefore, complexes of fragrance materials with 2-HP beta CD at 1:1 and 1:2 molar ratios (guest:host) were prepared. The formation of inclusion complexes was confirmed using proton nuclear magnetic resonance ((1)H-NMR) spectroscopy and circular dichroism spectroscopy. The results of the solubility studies showed that preparing the inclusion complex with 2-HP beta CD at a 1:1 molar ratio increased the solubility of linalool 5.9-fold and that of benzyl acetate 4.2-fold, whereas the complexes at a 1:2 molar ratio increased the solubility 6.4- and 4.5-fold for linalool and benzyl acetate, respectively. The stability and in vitro release studies were performed on the gel formulations prepared using uncomplexed fragrance materials or inclusion complexes of fragrance materials at a 1:1 molar ratio. It was observed that the volatility of both fragrance materials was decreased by preparing the inclusion complexes with 2-HP beta CD. Also, in vitro release data indicated that controlled release of fragrances could be possible if inclusion complexes were prepared.     

Fatty acid alcohol ester-synthesizing activity of lipoprotein lipase

The fatty acid alcohol ester-synthesizing activity of lipoprotein lipase (LPL) was characterized using bovine milk LPL. Synthesizing activities were determined in an aqueous medium using oleic acid or trioleylglycerol as the acyl donor and equimolar amounts of long-chain alcohols as the acyl acceptor. When oleic acid and hexadecanol emulsified with gum arabic were incubated with LPL, palmityl oleate was synthesized, in a time- and dose-dependent manner. Apo-very low density lipoprotein (apoVLDL) stimulated LPL-catalyzed palmityl oleate synthesis. The apparent equilibrium ratio of fatty acid alcohol ester/oleic acid was estimated using a high concentration of LPL and a long (20 h) incubation period. The equilibrium ratio was affected by the incubation pH and the alcohol chain length. When the incubation pH was below pH 7.0 and long chain fatty acyl alcohols were used as substrates, the fatty acid alcohol ester/free fatty acid equilibrium ratio favored ester formation, with an apparent equilibrium ratio of fatty acid alcohol ester/fatty acid of about 0.9/0.1. The equilibrium ratio decreased sharply at alkaline pH (above pH 8.0). The ratio also decreased when fatty alcohols with acyl chains shorter than dodecanol were used. When a trioleoylglycerol/fatty acyl alcohol emulsion was incubated with LPL, fatty acid alcohol esters were synthesized in a dose- and time-dependent fashion. Fatty acid alcohol esters were easily synthesized from trioleoylglycerol when fatty alcohols with acyl chains longer than dodecanol were used, but synthesis was decreased with fatty alcohols with acyl chain lengths shorter than decanol, and little synthesizing activity was detected with shorter-chain fatty alcohols such as butanol or ethanol.     

米胚芽中胰脂肪酶抑制剂的提取工艺

以米胚芽为原料,提取具有抑制胰脂肪酶活力的胚芽蛋白。经工艺优化得到提取条件为:原料颗粒60目,料液比1∶6,pH 10.18,温度55℃,提取时间4h,水提后离心速度4 456r.min-1,等电点沉降pH 5.1,等电点沉降后离心速度3 692r.min-1。在此条件下提取得到的胰脂肪酶抑制剂的蛋白质纯度为60.7%。15.18g/L的胚芽蛋白对30.1U/mg的猪胰脂肪酶的平均抑制率达71.17%。     

以玉米秸秆为原料同步糖化发酵生产燃料乙醇

以玉米秸秆为原料,经酸法预处理后,采用同步糖化发酵SSF工艺生产燃料乙醇。正交试验获得的最佳体系为:培养温度34℃、发酵pH值5.5、发酵的液固比8:1、当发酵108h后,乙醇浓度可达8.33g/L。该实验为纤维质燃料乙醇的产业化生产提供技术依据。     

固定化脂肪酶催化制备L-薄荷醇

用大孔树脂NKA固定高选择性的脂肪酶,催化有机相中转酯化反应,从而拆分八异构体消旋薄荷醇来制备L-薄荷醇。研究pH、载体与酶比例对固定化酶制备的影响及固定化酶的反应稳定性;考察温度、转酯化过程醇酯比例、及底物醇异构组成变化对拆分效果的影响。结果表明:固定化酶的最适pH为8,载体与酶的比例为5∶1时,所得固定化酶的反应稳定性比游离酶的反应稳定性提高了约50%;转酯化反应的最优温度为40℃,醇酯比例为1.5∶1时最佳,改进八异构体消旋薄荷醇组分比例后,非对映体选择率dep达到了95.1%。     

Synthesis of L-tyrosine glyceryl ester catalyzed by α-chymotrypsin in water-miscible organic solvents: A possible sun-tan accelerator product

Summary The synthesis of L-tyrosine glyceryl ester, from glycerol and L-tyrosine methyl ester, was carried out by a transesterification reaction catalyzed by -chymotrypsin. Values of 60 % (v/v) for glycerol and 200 mM for L-tyrosine methyl ester were optimal for the transesterification reaction. Additionally to glycerol, several other water miscible cosolvents (acetonitrile, N,N'-dimetyl formamide and tetrahydrofurane) were tested in the reaction media, but their presence did not give an enhancement on the transesterification activity with respect to the glycerol/water medium. However, increasing the hydrophobicity of the cosolvent resulted in a reduction of the enzyme activity, the water:glycerol mixture being the best reaction media.