L-谷氨酸氧化酶的克隆表达、纯化及酶学性质研究

为提高微生物产L-谷氨酸氧化酶水平,将Streptomyces sp.X-119-6的L-谷氨酸氧化酶基因(LGOX)与表达载体pET28a连接,导入E.coli BL21(DE3),实现LGOX的高效表达.采用HisTrapTM FF亲和层析柱对重组L-谷氨酸氧化酶进行纯化,并对纯酶的酶学性质进行了研究.结果表明:在IPTG终浓度为0.4 mmol/L下,30℃诱导6h,可以获得比酶活为1.1 U/mg的粗酶液;重组酶的最适反应温度和pH分别为37℃和5.O;km值为2.12 mmol/L,Vmax为1.06μmol/min·mg,对L-谷氨酸具有专一性;具有良好的应用前景.     

sTACI-Fc-Myc重组质粒的构建、原核表达及活性鉴定

目的:构建s TACI-Fc-Myc重组质粒,并进行原核表达和纯化具有生物活性的融合蛋白。方法:通过PCR法获得s TACI-Fc-Myc重组片段,然后把融合基因片段与原核载体p ET28a连接在一起,并构建p ET28a-s TACI-Fc-Myc重组子,并转入BL21(DE3)中进行表达,用蛋白A凝胶亲和层析柱进行纯化及酶联免疫吸附剂(ELISA)法测定其生物学活性。结果:获得了s TACI-Fc-Myc重组质粒,且该质粒可以在BL21(DE3)中表达,亲和层析柱纯化后纯度可达到95%以上,与BAFF的结合活性具有剂量依赖性,浓度达到5 ng/μL时,两者的吸附达到饱和。结论:成功构建了s TACI-Fc-Myc原核表达载体,并使有生物学活性的融合蛋白在BL21(DE3)上获得了稳定表达,为进一步研究并筛选高活性BAFF拮抗肽奠定了基础。     

头孢菌素脱乙酰酶的重组表达及固定化

本文构建了利用trp启动子表达头孢菌素脱乙酰酶(CAH)的重组大肠杆菌DH5α-pCAH。重组菌在7L发酵罐(装液量2L)中发酵28 h,发酵液OD_(600)达到27,产酶313 kU/L发酵液,粗略估算重组蛋白占细胞总蛋白的70%。发酵生产的重组CAH粗酶液经过硫酸铵分级沉淀分离纯化和超滤除盐浓缩两步操作,纯化倍数为1.44,总酶活回收率56%,聚丙烯酰胺凝胶电泳检测纯化后蛋白没有明显杂蛋白条带出现。纯化后的CAH共价结合固定在环氧基载体LX-1000EP(c)上,通过对固定化条件的优化最终得到固定化酶比活443 U/g。该固定化酶重复催化50 mL 5%7-ACA底物100次后,酶活没有降低。     

应用纤维素结合域标签构建谷氨酸棒状杆菌表达系统

为优化谷氨酸棒状杆菌表达系统的纯化工艺,合成里氏木霉的CBD基因,将其与谷氨酸棒状杆菌分泌表达载体pXMJ19-sp连接,构建以CBD为纯化标签的重组载体pXMJ 19-sp-CBD.在该载体中插入GFP基因并转化至谷氨酸棒状杆菌,可获得分泌表达融合蛋白GFP-CBD的重组菌.该菌经IPTG诱导后的发酵液在紫外灯下显示强烈的绿色荧光,重组蛋白的分泌表达量达200 mg/L.利用CBD标签对纤维素柱的可逆性吸附,可直接对谷氨酸棒状杆菌分泌到培养基中的重组蛋白进行纯化,从而简化工艺和降低成本,为工业化大生产奠定基础.     

植物乳杆菌源胺氧化酶的异源表达及功能结构分析

【目的】生物胺是一类广泛存在发酵食品中潜在有害物质,可被胺氧化酶分解。本研究对来源于乳酸菌的胺氧化酶的酶学性质及其降生物胺能力进行了探究。【方法】本研究在大肠杆菌中异源表达了植物乳杆菌中多铜氧化酶基因SufI,经过优化表达条件与纯化重组酶后,分析了该酶的最适反应条件、酶稳定性、降生物胺能力、光谱与结构特性。【结果】重组酶的最适pH值为3.5,最适温度为20℃,在pH 4.0–10.0或15–65℃的条件下,相对酶活力保持在70%以上。重组酶具有较好的稳定性,酶活不受乙醇等抑制剂的影响。在8种生物胺的混合体系内,重组酶对生物胺总量的降解量可达403.23μg/mL,其中对酪胺的降解量最多,超过70μg/mL (34.99%)。在单一生物胺体系内,重组酶对酪的底物亲和性较高,酶活可达18.33U/mL。紫外-可见扫描光谱显示酶蛋白在600 nm处有多铜氧化酶家族特征吸收峰,傅里叶红外光谱解析酰胺Ⅰ带中α螺旋、β折叠、β转角和无规则卷曲的相对含量分别为21.52%、20.72%、33.80%和23.97%。同源建模预测该酶具有3个铜结合域,且含有组氨酸、半胱氨酸、甲硫氨酸和谷氨酸等铜配体结合...     

DEK蛋白的真核表达纯化及其活性检测

利用Bac-to-Bac杆状病毒表达系统表达DEK蛋白并进行纯化。首先以pFastBacI质粒构建重组质粒pFastBacI-DEK,转化DH10Bac大肠杆菌后获得重组穿梭载体Bacmid-DEK,通过脂质体介导转染Sf9细胞产生具有强感染力的重组杆状病毒AcNPV-DEK。用此重组杆状病毒AcNPV-DEK感染Sf9细胞表达His-DEK融合蛋白。在非变性条件下,利用Ni-NTA agarose对表达的His-DEK融合蛋白进行纯化,经SDS-PAGE和Western blotting分析,在50 kDa处出现特异性蛋白条带并证实其为His-DEK融合蛋白。凝胶迁移阻滞实验表明,融合蛋白His-DEK与DNA 的结合具有结构特异性,其与超螺旋型DNA结合活性强于与线性化DNA的结合活性。真核表达并纯化的融合蛋白His-DEK与DNA的结合活性要明显强于原核表达的融合蛋白His-CDB。DEK 蛋白的磷酸化修饰会阻碍其与DNA的结合,而Sf9细胞中表达的融合蛋白His-DEK存在磷酸化修饰,将His-DEK去磷酸化后,其与DNA的结合活性有所提高。     

重组GluV8的克隆表达、纯化及酶学性质研究

谷氨酰内切酶在生物制药及检测中应用较多,但来源受限,将全基因合成的金黄色葡萄球菌来源的谷氨酰内切酶功能区部分对应的基因进行改造后,克隆入表达载体pGEX-4T-2,导入E.coli BL21（DE3）,重组蛋白以可溶性形式表达。采用亲和层析等纯化步骤对重组蛋白进行纯化,用底物Z-Phe-Leu-Glu-pNA（L-2135）对重组蛋白的酶学性质进行了研究,用HPLC、LC-MS/MS检测方法对酶切融合蛋白的位点特异性进行了鉴定。结果表明该酶的相对活性为1568U/mg,最适作用温度为42℃、最适作用pH为8.0,在pH 9.0,50℃时仍有较高的酶活,将该酶与胰酶酶切融合蛋白所得肽段结合能够提升质谱检测结果的精确度。以上结果表明该重组酶具有良好的应用前景。     

L-谷氨酸氧化酶的研究进展

L-谷氨酸氧化酶（L-glutamate oxidase,GLOD）是一种以FAD为辅基的黄素蛋白酶类,可以专一性地氧化谷氨酸生成过氧化氢、氨和α-酮戊二酸,广泛应用于食品、医药、发酵等领域。从谷氨酸氧化酶的微生物来源、酶学性质、发酵条件、分离纯化及分析应用等方面进行阐述,并对其研究前景进行展望。     

抗大豆胰蛋白酶抑制剂单链抗体表达与纯化方法优化

[目的]利用大肠杆菌毒素蛋白VTB的五聚体化结构域(VT1B)及梭菌纤维素酶的纤维素结合结构域(CBD),异源表达其与抗大豆胰蛋白酶抑制剂单链抗体(anti-BBI Sc Fv)的融合蛋白,对该单链抗体表达与纯化方法进行优化。[方法]构建CBD-VT1B-anti-BBI Sc Fv融合蛋白大肠杆菌表达系统;应用Ni-NTA树脂与微晶纤维素两步亲和层析法提纯单链抗体融合蛋白。[结果]单链抗体融合蛋白在大肠杆菌中得到大量表达,通过两步纯化法获得了高纯度的融合蛋白,纯度比Ni-NTA树脂一步纯化法提高约12~34%;五聚体融合蛋白与纤维素的结合能力及蛋白纯化效率比单体蛋白提高约1倍。[结论]通过增加纤维素标签和五聚体化结构域,抗大豆胰蛋白酶抑制剂五聚体化单链抗体融合蛋白的纯化效果得到提高。     

耐高温重组CotA蛋白的胆红素氧化酶反应动力学及活性鉴定

已知源于枯草芽孢杆菌内生孢子的CotA蛋白具有漆酶和胆红素氧化酶活性。然而,其分离纯化极为困难。本研究对表达与纯化的重组CotA蛋白的胆红素氧化酶特性及氧化还原功能进行鉴定。基因转染及筛选获得了表达CotA的P. pastoris菌株|继而,表达的重组CotA蛋白经DEAE-Sepharose FF 及Sephadex G-75层析分离与纯化,产物得率为25%,纯化产物的酶比活性为 4 U/mg。经SDS-PAGE 和 MALDI-TOF MS 分析显示,其分子质量为65 kD。纯化的CotA蛋白能够催化胆红素氧化,生成胆绿素,且催化反应速率受反应溶液中溶解氧含量的影响,提示纯化的重组CotA具有胆红素氧化酶活性。酶反应进一步证明,CotA的胆红素氧化酶反应最适pH值为pH 8.0,最适温度为60℃。该酶在90℃条件下的半衰期为7 h,提示CotA胆红素氧化酶具有高度的热稳定性。CotA修饰的摄谱仪石墨电极可直接电催化分子氧（O2）还原,具有很好的电流响应。我们的结果表明,重组的CotA蛋白具有耐高温胆红素氧化酶活性。更重要的是,我们的结果还提示重组的CotA蛋白在酶生物燃料电池阴极的制备上具有较好的应用潜能。     

Ultrasound mediated enzymatic hydrolysis of cellulose and carboxymethyl cellulose

A recombinant Trichoderma reesei cellulase was used for the ultrasound‐mediated hydrolysis of soluble carboxymethyl cellulose (CMC) and insoluble cellulose of various particle sizes. The hydrolysis was carried out at low intensity sonication (2.4–11.8 W cm^?2 sonication power at the tip of the sonotrode) using 10, 20, and 40% duty cycles. [A duty cycle of 10%, for example, was obtained by sonicating for 1 s followed by a rest period (no sonication) of 9 s.] The reaction pH and temperature were always 4.8 and 50°C, respectively. In all cases, sonication enhanced the rate of hydrolysis relative to nonsonicated controls. The hydrolysis of CMC was characterized by Michaelis‐Menten kinetics. The Michaelis‐Menten parameter of the maximum reaction rate V_max was enhanced by sonication relative to controls, but the value of the saturation constant K_m was reduced. The optimal sonication conditions were found to be a 10% duty cycle and a power intensity of 11.8 W cm^?2. Under these conditions, the maximum rate of hydrolysis of soluble CMC was nearly double relative to control. In the hydrolysis of cellulose, an increasing particle size reduced the rate of hydrolysis. At any fixed particle size, sonication at a 10% duty cycle and 11.8 W cm^?2 power intensity improved the rate of hydrolysis relative to control. Under the above mentioned optimal sonication conditions, the enzyme lost about 20% of its initial activity in 20 min. Sonication was useful in accelerating the enzyme catalyzed saccharification of cellulose. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:1448–1457, 2013     

Detrimental effect of cellulose oxidation on cellulose hydrolysis by cellulase

To effectively convert complex and recalcitrant biomass carbohydrates to simple platform sugars useful for fuel and chemicals production, mechanical or chemical pre-treatments are often required to make the carbohydrates more accessible for enzymatic hydrolysis. Due to their harsh conditions, some pre-treatments might negatively affect enzymatic hydrolysis because of events such as cellulose oxidation. To study how oxidative modification may impact cellulose's reactivity toward hydrolysis by cellulases, we prepared three cellulose substrates by cupric ion and hypochlorite oxidations, and subjected the derived celluloses to hydrolysis by various cellobiohydrolases from glycoside hydrolase families 6 and 7, and one cellulolytic Hypocrea jecorina extracellular enzyme mixture. We observed a profound decrease of enzymatic hydrolysis on the oxidized celluloses. The effect was attributed to the interference, from oxidized functional groups in cellulose, on its binding/activation in the active pocket/tunnel of cellobiohydrolases. Potential implication of the observed effect from cellulose oxidation on pre-treatment optimization and cellulase improvement was discussed.     

A structural study of fluorinated cellulose: crystallization of fluorinated cellulose by conversion treatments used for cellulose

A deoxyfluorocellulose derivative, with regioselective substitution mostly at the C-6 carbon atoms, has been studied by an X-ray diffraction method. The results showed that the crystallinity of the fluorinated cellulose is low but can be enhanced by a specific conversion treatment. The hydrothermally treated sample displayed a spectrum similar to that of cellulose IV.     

Enhancement of enzymatic saccharification of cellulose by cellulose dissolution pretreatments

Attempts were made to enhance cellulose saccharification by cellulase using cellulose dissolution as a pretreatment step. Four cellulose dissolution agents, NaOH/Urea solution, N-methylmorpholine-N-oxide (NMMO), ionic liquid (1-butyl-3-methylimidazolium chloride; [BMIM]Cl) and 85% phosphoric acid were employed to dissolve cotton cellulose. In comparison with conventional cellulose pretreatment processes, the dissolution pretreatments were operated under a milder condition with temperature <130 °C and ambient pressure. The dissolved cellulose was easily regenerated in water. The regenerated celluloses exhibited a significant improvement (about 2.7- to 4.6-fold enhancement) on saccharification rate during 1st h reaction. After 72 h, the saccharification yield ranged from 87% to 96% for the regenerated celluloses while only around 23% could be achieved for the untreated cellulose. Even with high crystallinity, cellulose regenerated from phosphoric acid dissolution achieved the highest saccharification rates and yield probably due to its highest specific surface area and lowest degree of polymerization (DP).     

Polymorphism of cellulose I family: reinvestigation of cellulose IVI

Polymorphs of cellulose I, III(I), and IV(I) have been investigated by X-ray diffraction, FT-IR, and solid-state (13)C NMR spectroscopy. Highly crystalline cellulose III(I) samples were prepared by treating cellulose samples in supercritical ammonia at 140 degrees C for 1 h, and conventional cellulose III(I) samples were prepared by liquid ammonia treatment. The cellulose IV(I) sample of highest crystallinity was that prepared from Cladophora cellulose III(I) in supercritical ammonia, followed by the sample treated in glycerol at 260 degrees C for 0.5 h, whereas the lowest crystallinity was observed in ramie cellulose prepared by conventional liquid ammonia treatment followed by glycerol annealing. In general, the perfection of cellulose IV(I) depends on the crystallinity of the original material: either of the starting cellulose I or of the cellulose III(I) after ammonia treatment. The product thus obtained was analogous to cellulose I(beta), which is what it should be called rather than cellulose IV(I). If the existence of the polymorph cellulose IV(I) is not accepted, the observations on which it has been based may be explained by the fact that the structure termed cellulose IV(I) is cellulose I(beta) which contains lateral disorder.     

Pyrolysis of cellulose

Pyrolysis of cellulose under vacuum and atmospheric pressure gave a tar containing various amounts of 1,6-anhydro-β-D-glucopyranose, 1,6-anhydro-β-D-glucofuranose, α- and β-D-glucose, 3-deoxy-D-erythro-hexosulose, oligo- and polysaccharides, and some dehydration products. The polysaccharide fraction had no reducing end-group, was randomly linked, contained some furanoid rings, and was very similar to the polysaccharide condensation-product of 1,6-anhydro-β-D-glucose. These results are consistent with a series of inter- and intra-molecular transglycosylation and dehydration and rehydration reactions.     

Chemoreception for cellulose

Rats that had been trained to avoid a suspension containing1% purified cellulose, subsequently avoided suspensions containingas little as 0.1% cellulose, but did not avoid suspensions containingcom, wheat or rice starch. Subsequent experiments examined thebasis for this unusual form of chemoreception. Viscosity measurementsindicated that cellulose and starch have similar effects ofviscosity; the suspending agent used in these experiments, xanthangum, masked much of the textural effects of cellulose or starchin water. Therefore, it does not seem likely that rats sensecellulose via its textural effects. On the other hand, ratsthat had been trained to avoid cellulose suspensions, also avoidedaqueous extracts of cellulose that had been filtered to removecellulose particles. This result suggests that a water-solubleimpurity contributes to cellulose chemoreception. This water-solubleimpurity could be washed off cellulose with water, but returnedafter the washed cellulose was dried. It is likely that cellulosereacts with the atmosphere to produce small amounts of water-solublecompounds that rats can sense     

Manufacture of cellulose nanocrystals by cation exchange resin-catalyzed hydrolysis of cellulose

Cellulose nanocrystals (CNC) were prepared from microcrystalline cellulose (MCC) by hydrolysis with cation exchange resin (NKC-9) or 64% sulfuric acid. The cation exchange resin hydrolysis parameters were optimized by using the Box–Behnken design and response surface methodology. An optimum yield (50.04%) was achieved at a ratio of resin to MCC (w/w) of 10, a temperature of 48 °C and a reaction time of 189 min. Electron microscopy (EM) showed that the diameter of CNCs was about 10–40 nm, and the length was 100–400 nm. Regular short rod-like CNCs were obtained by sulfuric acid hydrolysis, while long and thin crystals of cellulose were obtained with the cation exchange resin. X-ray diffraction (XRD) showed that, compared with MCC, the crystallinity of H₂SO₄-CNC and resin-CNC increased from 72.25% to 77.29% and 84.26%, respectively. The research shows that cation exchange resin-catalyzed hydrolysis of cellulose could be an excellent method for manufacturing of CNC in an environmental-friendly way.