壳聚糖固定化木瓜蛋白酶的研究

以壳聚糖为载体,成二醛为交联剂将木瓜蛋白酶固定化。5％戊二醛在4-6℃下处理载体5h,加酶液(3.5mg/mL蛋白,pH7.2)固定12h,活力回收达32％,作用于酪蛋白的半衰期为36天,其表观K_m(酪蛋白)值为0.075％(W/V),溶液酶的K_m值为0.086％;最适pH7.0～7.5,溶液酶为7.0～8.5。固定化酶在pH8.5以下,溶液酶在9.0以下活力稳定。固定化酶在45℃以下,溶液酶在75℃以下稳定。用6mol/L脲洗脱固定化酶4次(5.5h)活力仍有54.5％。用固定化酶处理啤酒浊度比对照下降了1.5-3.7倍,蛋白质含量下降了44％,冷藏(4℃)120天无冷混浊现象发生并保持了啤酒原有风味和理化性状。     

假单胞菌株K9510产肌酐酰氨基水解酶的条件

肌酐酰氨基水解酶是酶法分析血清肌酐浓度的关键酶。本实验室从空气中分离到能分解肌酐的菌株K9510,K9511和K9512,其中K9510菌株初步分类鉴定为假单胞菌（Pseudomonas sp.)。菌株产酶条件优化研究结果表明：菌株在底物或底物类化物的诱导下产酶;混合金属离子溶液对菌株产酶有促进作用,菌株产肌酐酰氨基水解酶是适培养基组成为：肌酐9克,酵母提取物1．5g,麦芽汁0．9g,NH4Cl0.5g,定容1L。适量混合金属离子溶液,用0．1mol/L pH5.5磷酸缓冲液配制.。在250mL三角瓶中装50mL培养基,在250r/min的旋转摇床上35度振荡培养33h,在此条件下菌株产酶量可达1．0u/mL发酵液。     

原生质体激光诱变选育少根根霉脂肪酶高产菌株

对少根根霉BUCT-11原生质体制备、再生条件及激光诱变育种进行了研究.结果显示,少根根霉BUCT-11原生质体形成及再生最佳条件为:菌龄24 h,混合酶由27 mg/mL的蜗牛酶和53 mg/mL的纤维素酶组成,酶解时间1.5 h,酶解温度30 ℃,渗透压稳定剂为0.6 mol/L NH4Cl、0.02 mol/L ...     

基于响应面法对香菇原生质体制备条件的优化

香菇Lentinula edodes是我国食用菌年产量最大的单品,优化香菇原生质体的制备条件,获得高质量、高活力的原生质体可以为香菇育种和遗传多样性分析提供技术保障。本研究利用单因素试验对稳渗剂浓度、酶解液类型、酶解时间、酶解温度4个因素的最优作用条件和相关性进行检验和筛选;依据单因素试验的结果,对酶解时间、酶解温度、酶解液种类进行响应面法3因素3水平试验优化分析。单因素试验结果表明,使用2%的溶壁酶+蜗牛酶+纤维素酶混合酶制剂为酶解液、0.6mol/L甘露醇为稳渗剂的效果显著高于其他处理(P<0.05)。经Box-Behnken设计得出香菇原生质体最佳制备条件为酶解时间3.25h,酶解液浓度1.7%,酶解温度30.49℃,获得原生质体产量为14.02×10⁶ CFU/mL,与理论产量(13.862×10⁶ CFU/mL)偏差小,可为后续原生质体融合育种和多样性分析提供重要基础。     

尼龙固定化木瓜蛋白酶及其应用研究

 尼龙经CaCl_2和H_2O的甲醇溶液处理,稀HCl水解用戊二醛交联以制备固定化木瓜蛋白酶。在溶液酶浓度为1mg/mL pH7.5—8.0、4—15℃条件下固定3h,活力回收42.5％,相对活力46％,偶联效率52％,半衰期72天。溶液酶Km值和固定化酶K_m~(aPP)值(底物酪蛋白W/V,％)分别为0.28％和0.35％。溶液酶和固定化酶分别在pH6.5和pH8.0以下活力稳定;最适pH分别为7.0和8.0;在65℃处理30min活力分别为原有活力的89％和66％。当酪蛋白浓度为1.5％和2.5％以上活力分别受到抑制。固定化酶在6mol/L脲中连续浸洗5次共6h其活力稳定,仍有原活力的44.4％;用以处理啤酒浊度比对照下降了2-11倍;蛋白质含量下降了55％;冷藏(4℃)120天,无冷混浊发生;同时各项理化指标和风味不变。     

蓝色犁头霉原生质体的制备与再生

研究了氢化可的松生产菌蓝色犁头霉原生质体的形成与再生。通过对溶解酶系统的选择,影响原生质体形成的因素如渗透压稳定剂、酶浓度、菌龄、菌丝培养基和培养方式等因素进行考察,发现以0．4mol/L NH4Cl做为稳定剂、2．5mg/mL溶壁酶和5mg/mL纤维素酶组成的混合酶液溶解菌丝,4h后原生质体量可达10^6cell/mL。通过显微镜观察原生质体的形成过程以及在高渗培养基上的再生情况,再生率为15．6％。     

丝状真菌AL18的原生质体制备和再生条件的优化

目的:为了建立起产苝醌类光敏剂丝状真菌AL18原生质体制备和再生体系。方法:采用单因素实验法研究了预处理方式、渗透压稳定剂和酶解条件对原生质体制备率和再生率的影响。结果:原生质体制备及再生的最佳条件是用0.3%的β-巯基乙醇预处理15 min,酶解液以0.6 mol/L的MgSO4·7H2O作为渗透压稳定剂,0.02 mol/L的磷酸盐缓冲液pH值为5.8,纤维素酶:蜗牛酶=2:3,酶的总浓度为15mg/mL,36℃酶解2h;以0.6mol/L的蔗糖作为再生培养基的渗透压稳定剂。结论:原生质体的制备率和再生率可分别达到1.42×107/mL和3.2%。     

漆酶在磁性壳聚糖微球上的固定及其酶学性质研究

以磁性壳聚糖微球为载体,戊二醛为交联剂,共价结合制备固定化漆酶。探讨了漆酶固定化的影响因素,并对固定化漆酶的性质进行了研究。确定漆酶固定化适宜条件为：50 mg磁性壳聚糖微球,加入10mL 0.8mg/mL 漆酶磷酸盐缓冲液（0.1mol/L,pH 7.0）,在4℃固定2h。固定化酶最适pH为3.0, 最适温度分别为10℃和55℃,均比游离酶降低5℃。在pH 3.0,温度37℃时,固定化酶对ABTS的表观米氏常数为171.1μmol/L。与游离酶相比,该固定化漆酶热稳定性明显提高,并具有良好的操作和存储稳定性。     

混合菌株降解褐藻胶的筛选、鉴定及产酶条件优化

为获得仿刺参（Apostichopus japonicus）肠道菌群中可有效降解褐藻胶的混合菌株,以海藻酸钠为唯一碳源配制培养基,以透明圈法进行初筛,DNS法和紫外法复筛,从已驯化仿刺参肠道中筛选得到4株高酶活力褐藻胶降解菌株S1、S2、S10和S11,经16S rDNA序列分析、电镜观察,确定菌株S2与S11分别为微杆菌属（Microbacterium sp.）和微小杆菌属（Exiguobacterium sp.）。对该4株菌株分别进行混合培养,获得菌株S2与S11最佳配比组合,并通过单因素试验及响应面优化试验对影响混合菌株产酶条件的发酵初始pH值、NaCl质量浓度、装液量和发酵温度4个因素进行优化。得到混合菌株最佳产酶条件为pH 8,NaCl质量浓度为40 g/L,装液量80 mL,温度28 ℃。在最佳发酵条件下,混合菌株酶活力可达94.78 U/mL,相比于优化前提高了43.9%,优化后混合菌株的酶活力显著提高。     

羊肚菌原生质体制备与再生*

羊肚菌原生质体制备的最佳条件为以培养3d的菌丝体为材料,0.6mol/L蔗糖溶液为稳渗剂,1.5%浓度的溶壁酶30℃条件下酶解3个小时,可得原生质体产量最高为3.35×106个/100mg.以0.6mol/L的蔗糖溶液做稳渗剂,CYM再生培养基上得到原生质体再生率为0.171%.这一研究结果为羊肚菌通过原生质体技术进行菌株的遗传改良提供了重要技术参数.     

融合牛肠激酶轻链EKL包涵体蛋白的复性纯化

大肠杆菌高密度发酵表达肠激酶轻链融合蛋白DsbA-rEKL,主要以包涵体形式存在。包涵体经4mol/L尿素和0.5%TritonX-100洗涤,以6mol/L盐酸胍、100mmol/LDTT溶解,在胱氨酸存在下,以脉冲加样方式复性。融合蛋白复性在6mmol/L胱氨酸存在下、脉冲加量0.03mg/mL和复性终蛋白浓度0.3mg/mL为最佳复性方案。复性的融合蛋白加2mmol/LCaCL2后快速自切。经IDA-Sepharose及Q-Sepharose纯化,rEKL纯度可达95%以上,可高效酶切重组瑞特普酶融合蛋白Trx-rPA。实现了大规模生产rEKL,每升发酵液经复性及纯化后,可得rEKL60mg/L以上,使以融合蛋白表达rPA等药用蛋白成为现实。     

Pharmacokinetics Study of Recombinant Hirudin in the Plasma of Rats Using Chromogenic Substrate,ELISA, and Radioisotope Assays

Aim

To compare the analytical methods used to study the pharmacokinetics of recombinant hirudin in the plasma of rats that had been injected with ¹²⁵I-recombinant hirudin.

Methods

2.0 mg/kg ¹²⁵I-recombinant hirudin were injected intravenously into rats. The recombinant hirudins in the plasma was analyzed by chromogenic substrate assay, enzyme-linked immunosorbent assay (ELISA), total radioisotope assay (RA) and trichloroacetic acid pre-treated total radioisotope assay (TCA-RA).

Results

The chromogenic substrate assay standard curve was linear over the concentration range from 3.12 to 40.00 ng/ml for the recombinant hirudin in plasma. The relative standard deviations (RSD) for the intra- and inter-day variation were 5.0 to 6.3% and 11.9 to 12.6%, respectively. The recoveries of recombinant hirudin was 89.8% to 100.7%. The limit of quantification (LOQ) was 3.12 ng/ml. The concentration-time curve of the recombinant hirudin in the plasma could be explained as a two-compartment model. Pharmacokinetic parameters, including the half-life of distribution phase (t_1/2 α), the half-life of elimination phase (t_1/2 β), volume of apparent distribution (Vd), and area under the concentration-time curve from zero to infinite time (AUC_0–t) were 7.59 min, 46.99 min, 0.17 L/kg, and 204.5 mg/L/min, respectively, as determined by chromogenic substrate assay; 6.41 min, 47.28 min, 1.24 L/kg, and 575.18 mg/L/min, respectively, as determined by ELISA; 3.69 min, 701.90 min, 0.04 L/kg, and 4189 mg/L/min, respectively as determined by RA; and 4.57 min, 724.9 min, 0.09 L/kg, and 2329 mg/L/min, respectively, as determined by TCA-RA.

Conclusions

The chromogenic substrate assay on the concentration dynamics of the recombinant hirudin in the plasma is a specific, sensitive, and accurate analytical method for pharmacokinetic studies. Moreover, the pharmacokinetic parameters determined by the chromogenic substrate assay and ELISA are congruent except for AUC.     

Efficient synthesis of Guanfu base G via highly regioselective lipase-catalyzed acylation in non-aqueous phase

Lipase-catalyzed acylation of Guanfu alcohol-amine (GFAA) with vinyl acetate (VA) was performed in non-aqueous system for the preparation of Guanfu base G (GFG), a plant-originated alkaloid with significant antiarrhythmic activity. Among the eight lipases from different origins, Novozym 435 was found to be the best biocatalyst. The most suitable molecular sieve amount, substrate concentration, molar ratio of VA to GFAA, enzyme amount and reaction temperature were proved to be 40 mg/mL, 6 μmol/mL, 10:1, 2mg/mL and 50 °C, respectively. A maximum GFG yield of 37.4% was achieved under the selected conditions with methanol served as the optimal reaction medium. The structure of the acetylated product was elucidated by (1)H NMR and (13)C NMR analysis.     

难溶于二甲亚砜多糖的甲基化方法研究

本文对难溶于二甲亚砜(DMSO)但易溶于水的多糖——羊栖菜褐藻糖胶的甲基化方法进行了研究。10mg多糖用0．1mL水溶解后,加和3mL DMSO,使多糖转溶于DMSO,然后加人2mL 3A分子筛脱除水分。将DNSO溶液过滤后,滤液中加入50mg NaOH粉末,室温下反应10min。加入0．5mL碘甲烷,室温下反应60min。加1mL水终止反应,加1mol／L HAc中和、透析、冻干。该法简便易行,所得产物的甲基化程度比较高。     

Refolding of the Fusion Protein of Recombinant Enterokinase Light Chain rEKL

The fusion protein of enterokinase light chain, DsbA-rEK_L, was expressed mainly in the inclusion body in E. coli. The recombinant bacteria were fermented to high density, with high expression of the fusion protein. After being washed with 0.5 % Triton X-100 and 4 mol/L urea, the inclusion body was dissolved in 6 mol/L guanidine and 100 mmol/L DTT, derivatized by cystine and refolded by pulse refolding. The strategy of pulse refolding involved the addition of 0.03 mg/mL of fusion protein until its final concentration reached 0.3 mg/mL. The refolded protein was autocleaved, and the active EK_L molecule was released after the addition of 2 mmol/L of CaCl₂. Using the two-step purification processes of IDA-Sepharose chromatography and Q-Sepharose chromatography, the purity of rEK_L was found to be above 95 %, with a high activity to cleave the recombinant reteplase fusion protein, Trx-rPA. The yield of purified rEK_L was more than 60 mg/L of cultures. As a result, the therapeutic proteins like rPA could be produced on a large scale in a way such as expressed in the form of fusion proteins.     

Experimental and kinetic studies on methylene blue adsorption by coir pith carbon

Varying the parameters such as agitation time, dye concentration, adsorbent dose, pH and temperature carried out the potential feasibility of thermally activated coir pith carbon prepared from coconut husk for removal of methylene blue. Greater percentage of dye was removed with decrease in the initial concentration of dye and increase in amount of adsorbent used. Kinetic study showed that the adsorption of dye on coir pith carbon was a gradual process. Lagergren first-order, second-order, intra particle diffusion model and Bangham were used to fit the experimental data. Equilibrium isotherms were analysed by Langmuir, Freundlich, Dubnin-Radushkevich, and Tempkin isotherm. The adsorption capacity was found to be 5.87 mg/g by Langmuir isotherm for the particle size 250-500 microm. The equilibrium time was found to be 30 and 60 min for 10 and 20 mg/L and 100 min for 30, 40 mg/L dye concentrations, respectively. A maximum removal of 97% was obtained at natural pH 6.9 for an adsorbent dose of 100 mg/50 mL and 100% removal was obtained for an adsorbent dose of 600 mg/50 mL of 10 mg/L dye concentration. The pH effect and desorption studies suggest that chemisorption might be the major mode of the adsorption process. The change in entropy (DeltaS0) and heat of adsorption (DeltaH0) of coir pith carbon was estimated as 117.20 J/mol/K and 30.88 kJ/mol, respectively. The high negative value of change in Gibbs free energy indicates the feasible and spontaneous adsorption of methylene blue on coir pith carbon.     

甘蓝型油菜与芝麻菜体的细胞杂交

为拓宽油菜育种的基因资源库, 改良油菜品种, 以甘蓝型油菜(Brassica napus)花油3号下胚轴和芝麻菜(Eruca sativa)下胚轴为材料分离制备原生质体; 然后采用PEG-高Ca2+-高pH法进行原生质体融合, 当PEG浓度为35%, 原生质体融合密度为5×105个/mL时, 融合25 min时, 融合率可达18.2%。融合后在培养密度为1×105个/mL时, 以附加1.0 mg/L 2,4-D +0.5 mg/L 6-BA+0.5 mg/L NAA+ 200 mg/L肌醇+300 mg/L水解酪蛋白的改良的KM8p为融合体培养基, 以0.1 mol/L 蔗糖+0.2 mol/L葡萄糖+0.2 mol/L甘露醇作渗透稳定剂进行液体浅层培养, 效果较好, 愈伤组织再生率最高为6.8%。将融合体再生的小愈伤组织转移至培养基(B5无机盐+0.087 mol/L蔗糖+0.2 mg/L 2, 4-D+0.5 mg/L NAA+0.2 mg/L 6-BA+ 0.5% Agar, pH 5.8)上增殖培养, 待愈伤组织长至直径为3~5 mm时, 及时将其转至分化培养基(MS无机盐+0.087 mol/L 蔗糖+0.1 mg/L IAA+0.8 mg/L 6-BA+0.8% Agar, pH 5.8)中诱导不定芽再生, 芽分化率为35.7%。当不定芽长为2~3 cm时, 将其切下转入附加0.5 mg/L IBA+0.2 mg/L 6-BA的1/2MS生根培养基中诱导生根, 14 d左右即可形成再生植株, 生根率可达88%。同时, 以紫外线(60 μW/cm2)照射芝麻菜原生质体, 进行不对称融合, 照射2 min的获得了愈伤组织和再生植株, 照射4 min的只获得愈伤组织, 而照射5 min以上的没有获得愈伤组织, 但其愈伤组织再生、增殖及植株再生均不如对称融合。从细胞学鉴定的21块杂种愈伤组织上再生出16株杂种植株。     

甘蓝型油菜与芝麻菜体的细胞杂交

为拓宽油菜育种的基因资源库, 改良油菜品种, 以甘蓝型油菜(Brassica napus)花油3号下胚轴和芝麻菜(Eruca sativa)下胚轴为材料分离制备原生质体; 然后采用PEG-高Ca2+-高pH法进行原生质体融合, 当PEG浓度为35%, 原生质体融合密度为5×105个/mL时, 融合25 min时, 融合率可达18.2%。融合后在培养密度为1×105个/mL时, 以附加1.0 mg/L 2,4-D +0.5 mg/L 6-BA+0.5 mg/L NAA+ 200 mg/L肌醇+300 mg/L水解酪蛋白的改良的KM8p为融合体培养基, 以0.1 mol/L 蔗糖+0.2 mol/L葡萄糖+0.2 mol/L甘露醇作渗透稳定剂进行液体浅层培养, 效果较好, 愈伤组织再生率最高为6.8%。将融合体再生的小愈伤组织转移至培养基(B5无机盐+0.087 mol/L蔗糖+0.2 mg/L 2, 4-D+0.5 mg/L NAA+0.2 mg/L 6-BA+ 0.5% Agar, pH 5.8)上增殖培养, 待愈伤组织长至直径为3~5 mm时, 及时将其转至分化培养基(MS无机盐+0.087 mol/L 蔗糖+0.1 mg/L IAA+0.8 mg/L 6-BA+0.8% Agar, pH 5.8)中诱导不定芽再生, 芽分化率为35.7%。当不定芽长为2~3 cm时, 将其切下转入附加0.5 mg/L IBA+0.2 mg/L 6-BA的1/2MS生根培养基中诱导生根, 14 d左右即可形成再生植株, 生根率可达88%。同时, 以紫外线(60 μW/cm2)照射芝麻菜原生质体, 进行不对称融合, 照射2 min的获得了愈伤组织和再生植株, 照射4 min的只获得愈伤组织, 而照射5 min以上的没有获得愈伤组织, 但其愈伤组织再生、增殖及植株再生均不如对称融合。从细胞学鉴定的21块杂种愈伤组织上再生出16株杂种植株。     

巨大芽孢杆菌WSH-002丙氨酸脱氢酶066晶体制备及X-射线衍射分析

丙氨酸脱氢酶可逆催化丙氨酸脱氨生成丙酮酸,在氨基酸和酮酸的合成及代谢中至关重要.本研究通过PCR从巨大芽孢杆菌WSH-002中克隆并构建了丙氨酸脱氢酶基因(aldBM066)的原核表达载体,经原核表达后,采用Ni-NTA亲和层析法和阴离子交换色谱法纯化获得蛋白AldBM066,在289 K下以座滴法进行晶体生长条件筛选和制备.通过对蛋白质结晶条件的筛选,最终在蛋白质浓度为15 mg/mL及含有0.1 mol/L 乙酸钠（pH 5.0）和2.4 mol/L甲酸钠的缓冲液中获得了理想的蛋白质晶体,晶体大小约为210 μm×180 μm×150 μm,X-射线衍射数据显示,该蛋白质晶体衍射分辨率为2.88 A,空间群为三方晶系,晶胞参数为a=b=118.71 A,c=150.51 A,α=β=90°,γ=120°,每个不对称单位中含有1个AldBM066单体,马修斯系数为2.62 A3/Da,溶剂含量约为53.02%.衍射数据的成功收集为解析巨大芽孢杆菌WSH-002中丙氨酸脱氢酶的三维结构奠定了前期基础,将有助于阐明以单体存在的丙氨酸脱氢酶的催化机制.     

Effect of substrate concentration on dual-species biofilm population densities of Klebsiella oxytoca and Burkholderia cepacia in porous media

The long-term operation of bioremediation technologies relies on the success of the contaminant-degrading microorganism(s) to compete for available resources with microorganisms already present in an aquifer or those that may contaminate a bioreactor. Though research has been performed studying the interaction of multiple species in batch and chemostat reactors, little work has been done looking at multi-species interactions in environments that more closely resemble field-scale applications. The research presented herein examined the interaction of Burkholderia cepacia PR1-pTOM(31c), an aerobic trichloroethylene (TCE)-degrading bacterium, with Klebsiella oxytoca, a facultative bacterium, in a flow-through porous media (PM) reactor. Growth characteristics and population distributions in PM were compared to previously reported values from batch and chemostat reactors. The faster growing organism in batch experiments (K. oxytoca) did not always have the greater population density in dual-species PM experiments. The biofilm population distribution was influenced by substrate concentration, with B. cepacia having a greater dual-species population density than K. oxytoca at a low (30 mg/L dissolved organic carbon [DOC]) substrate concentration and K. oxytoca having a greater population density at a high (700 mg/L DOC) substrate concentration. This change in species population distribution with change in substrate concentration, which was not observed in batch reactors, was also observed in chemostat reactors. Therefore, manipulation of substrate concentration enabled the control of species dominance to the advantage of the TCE degrading population in this dual-species PM system and may provide a mechanism to enhance bioremediation scenarios involving TCE or other contaminants of concern.