右旋糖酐酶的底物吸附

用35％乙醇保护,底物占旋糖酐能对右旋糖酐酶有效地吸附。采用0．2mol／L pH8．0的KzHPO4-KH2PO4缓冲液(内含30％乙醇)进行解吸,总同收率在80％以上。粗酶液经此过程提纯了9倍。低温对吸附有利。 在酶稳定范围内,pH对吸附影响不大。酶浓度过高,吸附效率下降。对稀酶液可连续多次吸附以达到浓缩目的。1．5％(W／V)的右旋糖酐使可得到满意的吸附效果,对五种不同来原的右旋糖酐酶吸附率都很高,但不同来源的底物适用情况差别很大。     

用粗淀粉吸附——洗脱回收Pseudomonas amyloderamonsa异淀粉酶

Ｐｓｅｕｄｏｍｏｎａｓ ａｍｙｌｏｄｅｒａｍｓａ Ｗｕ２１３０菌所产异淀粉酶吸附在粗淀粉上,用５０ｍＭ醋酸缓冲液的麦芽糖洗脱被吸附的酶。异淀粉酶对吸附剂的吸附作用受粗淀粉来源、温度、ＰＨ值的影响。然而,温度和洗脱时间对被吸附异淀粉酶的洗脱没有明显影响。粗淀粉有良好的再生性,在吸附－洗脱周期循环内能重复使用。回收到大约５２．９％的异淀粉酶,洗脱后的酶在提纯１３．３倍的情况睛,每毫克蛋白比活性为７２２     

壳聚糖固定化德氏根霉脂肪酶的研究

研究了壳聚糖吸附和戊二醛交联对脂肪酶固定化条件,在室温条件下将0．4g酶粉溶于pH6．0缓冲液中,加入10g壳聚糖,摇匀,再加入浓度为0．6％戊二醛交联6h,得到固定化酶,酶活力回收率约为54．2％。固定化酶的半失活温度比游离酶的高,半失活温度由游离酶的47℃提高到100℃,最适反应温度由40℃上升至80℃,最适pH由6下降到5．5,固定化酶K’m值由游离酶的Km 50mg／mL增加到56mg／mL。该固定化脂肪酶用于酯的合成;在80℃条件下经过10批次连续水解植物油反应,固定化酶的活力仍保持在82．6％以上。     

菊糖酶发酵生产条件的研究

脆壁克鲁维氏酵母（Kluyveromycesfragilis）在pH5．5的适当培养基中,28℃摇瓶培养30h后,进行分批发酵。结果表明：发酵初始pH为6．0～6．5,菊糖浓度为2％,接种量4％,控制前期发酵温度为28℃,33h后发酵温度为32～34℃。发酵周期为70h左右,最高产酶达240u／ml。在5L自控发酵罐中,产酶达到同样水平,发酵周期缩短约10h。     

果胶酶制剂中花色素酶的去除

以皂土为吸附剂,将花色素酶从粗果胶酶制剂中除去。分离效果受pH和皂土用量影响。皂土还具有一定的脱色作用。黑曲霉AS3.316麦麸固体曲用5倍重量的自来水于室温下抽提4小时。粗果胶酶拙提液中加入3％皂土,调pH至4.1,于室温下放置30分钟。过滤所得部分提纯酶液含果胶酶258u/ml,酶活力回收为88％。 100ml山楂汁和387u(1.5ml)上述部分提纯的果胶酶于50℃保温3小时后,澄清度由65％提高到98％;相对粘度由12.5下降到1.2;果胶完全水解;红色素完全保留着。     

壳聚糖酶产生菌的筛选及固定化细胞产酶

旨在筛选得到一株壳聚糖酶产生菌,并研究固定化细胞产酶的条件。在培养基中以壳聚糖为唯一碳源,对土壤样品进行筛选,获得一株无花果沙雷氏菌(Serratia ficaria CH-0203),该菌可被壳聚糖诱导产生壳聚糖酶。固定化细胞产酶的研究结果表明,多孔玻璃可以有效吸附CH—0203菌细胞。在最适发酵条件下(pH6．5,培养基与载体的总体积48ml,载体与培养基的比例为1．5g/4．0ml,吸附时间是20h-26h),发酵液酶活达到4．5U／ml,比游离细胞发酵提高了16％。采用半连续发酵的方式,固定化的细胞可以稳定发酵产酶120h左右。固定化细胞产酶的效率大大高于游离细胞。     

植物乳杆菌RS2-2发酵法生产乳酸脱氢酶

筛选到一株产乳酸脱氢酶的植物乳杆菌RS2-2（Lactobacillus plantarum RS2-2）。产酶条件研究表明,以蔗糖为碳源,酵母膏为氮源,起始pH6．5左右,30℃发酵,接种量为10％,产酶量最高。在25L发酵罐放大实验,并通过流加NaOH控制发酵过程中的pH,所产乳酸脱氢酶比活力为18．73U／mg,菌重量为lg／L以上。粗酶液经分离纯化得到成品酶液,比酶活提高了51．7倍,达到1210、7U／mg,总收率为30、2％。用凝胶过滤检测其分子量分布,分子量约为85,000Da,酶纯度为88％。     

吸附层析法从啤酒废酵母中提取谷胱甘肽

以壳聚糖作为吸附剂,通过吸附层析法从啤酒废酵母泥为原料,经预处理和细胞破碎后得到的富含谷胱甘肽的抽提液中,分离纯化还原型谷胱甘肽。根据试验结果确定最佳提取条件为：上柱啤酒废酵母抽提液的最适pH值为7．0,最适洗脱剂为pH值为4．4的磷酸盐缓冲液。在最适吸附条件下,还原型谷胱甘肽的平均洗脱率为84．18％,平均回收率79．55％。说明此法是可行的。     

疏水作用层析纯化脂肪酶

报道了以对β-硫酸酯己砜基苯胺（SESA）为活化剂制备疏水作用层析剂方法及其柱层析纯化脂肪酶的工艺条件。实验结果表明：活化剂对-β-硫酸酯己砜基苯胺（SESA）最适用量为1．0g／g湿纸纤维素。笨胺：丙酮比为1：4．以0．2mol／L磷酸缓冲液（pH8.0）=1mol／LNaCl为淋洗剂,以0．2mol／L磷酸缓冲液（pH8．0）＋8％吐温80为洗脱刘纯化脂肪酶具有较好的分辨率,酶活回收率64．0％,比活提高6．70倍。     

大孔吸附树脂吸附链霉菌702抗真菌活性物质工艺

研究大孔吸附树脂吸附链霉菌702抗真菌活性物质的工艺条件。采用5种不同大孔吸附树脂吸附链霉菌702发酵液提取液中抗真菌活性物质,选择吸附效果较佳树脂进行吸附条件优化,以桔青霉为指示菌,纳他霉素为对照抗生素．采用“管碟法”测定抗真菌活性物质含量。结果发现,XAD18树脂吸附效果较好,获得优化吸附条件：上样液pH6,NaCl质量浓度10g/L,上样量22．63mg／g湿树脂,吸附流速2．5mL／min,水洗体积180mL,洗脱流速1．5mL／min,洗脱剂为体积分数10％、50％和90％的甲醇,洗脱方式为梯度洗脱。在确定的工艺条件下XAD18对链霉菌702抗真菌活性物质的吸附率可达90％,洗脱率可达75％,回收率可达80％。     

Optimization of a pseudo-affinity process for penicillin acylase purification

A pseudo-affinity process for penicillin acylase (EC 3.5.1.11) purification using an affinity ligand (Ampicillin) attached on Sepharose 4B-CNBr was optimized. The enzyme adsorption on this affiant (Amp-Seph) is independent of pH between 5.5 and 8.8, in 100?mM phosphate containing 22% (w/v) ammonium sulphate. The desorption of the penicillin acylase from the affinity gels was carried out, the best desorption results being obtained through a non specific eluent, 100?mM phosphate pH 4.6 with 15% (w/v) ammonium sulphate. The best purification results were obtained with an enzymatic extract, produced through osmotic shock of Escherichia coli cells (3.7?IU/mg prot). With this extract and an affinity gel of Sepharose 4B-CNBr derivatized with ampicillin (3.8?μmol/cm³?gel), a maximum activity capacity adsorbed of 20?IU/cm³?gel was obtained for initial values of activity and protein concentration of 1.7?IU/cm³ and 0.4?mg prot/cm³, respectively. With the optimized eluent it was possible to obtain penicillin acylase in only one purification step with a desorption yield of enzyme activity higher than 90%. The penicillin acylase produced with this process was characterized by a maximum purity of 34?IU/mg prot, corresponding to a purification degree higher than 150 in relation to the lowest pure enzymatic extract. The enzyme purity of the eluted fractions was certified by SDS gel electrophoresis and liquid chromatography through a Mono Q column in a FPLC apparatus. The gel electrophoresis presented 4 main stained bands with 2 corresponding to α and β subunits of the penicillin acylase with equivalent molecular weights of 27 and 63?kDa. No external diffusion resistance on penicillin acylase and total protein adsorption on this affiant (Amp-Seph 3.8?μmol/cm³?gel) were observed for continuous adsorption processes performed at two different agitation speeds (120 and 400?rpm).     

Leakage of recombinant penicillin G acylase from Escherichia coli by adding chloroform under fermentation conditions

A simple method was developed to release periplasmic penicillin G acylase from Escherichia coli BL21(DE3) during the fermentation process. More than 80% of the total penicillin G acylase was released into the broth when 3% (v/v) chloroform was added at 3 h after induction. The activity of extracellular penicillin G acylase reached 20699 U/l. This method was efficient and would facilitate further investigation of penicillin G acylase for industrial applications.     

Biosynthesis of penicillin V acylase by Fusarium sp.: effect of culture conditions

Penicillin V acylase was produced, both intracellularly and extracellularly, by Fusarium sp. SKF 235 grown in submerged fermentation. When neopeptone was added to the medium, >95% of the penicillin V acylase was extracellular. In the absence of a complex organic nitrogen source, the fungus produced low levels of totally intracellular penicillin V acylase. MgSO₄ was essential for synthesis of the enzyme, which was induced by phenoxyacetic acid and penicillin V. The maximum yield of penicillin V acylase was 430 IU/g dry cell wt. The optimum pH value and temperature for the penicillin V acylase were 6.5 and 55°C, respectively.     

胞外青霉素酰化酶产生菌的选育

利用纸片显色方法,从土壤甲诀速筛选出98株产胞外青霉素酰化酶的菌种,经复筛其中10株酶活力较高,经鉴定均属于巨大芽孢杆菌。经单株分离得46号菌,用这株菌进行了产酶条件的研究,在最适产酶条件下,酶话力比开始提高了3．6倍。在此基础上又进行了物理化学因素处理,得突变株UL-81,酶活力达720u／1 Ooml发酵液。对原株和突变株进行比较,发现UL-81菌落、细胞形态、诱导剂苯乙酸用量及添加时间等明显不同于原株。在500L罐发酵酶活达8 20u／1OOml发酵液,为开始酶活的16倍。     

Purification of penicillin G acylase using immobilized metal affinity membranes

The immobilized metal affinity membrane (IMAM) with modified regeneration cellulose was employed for purification of penicillin G acylase (PGA). For studying PGA adsorption capacity on the IMAM, factors such as chelator surface density, chelating metal, loading temperature, pH, NaCl concentration and elution solutions were investigated. The optimal loading conditions were found at 4 degrees C, 0.5 M NaCl, 32.04 micromol Cu(2+) per disk with 10 mM sodium phosphate buffer, pH 8.5, whereas elution conditions were: 1 M NH(4)Cl with 10 mM sodium phosphate buffer, pH 6.8. By applying these chromatographic conditions to the flow experiments in a cartridge, a 9.11-fold purification in specific activity with 90.25% recovery for PGA purification was obtained. Meanwhile, more than eight-times reusability of the membrane was achieved with the EDTA regeneration solutions.     

Production of polygalacturonase from <Emphasis Type="Italic">Coriolus versicolor</Emphasis> grown on tomato pomace and its chromatographic behaviour on immobilized metal chelates

Tomato pomace and pectin were used as the sole carbon sources for the production of polygalacturonase from a strain of Coriolus versicolor in submerged culture. The culture of C. versicolor grown on tomato pomace exhibited a peak of polygalacturonase activity (1,427 U/l) on the third day of culture with a specific activity of 14.5 U/mg protein. The production of polygalacturonase by C. versicolor grown on pectin as a sole carbon source increased with the time of cultivation, reaching a maximum activity of 3,207 U/l of fermentation broth with a specific activity of 248 U/mg protein. The levels of different isoenzymes of polygalacturonase produced during the culture growth were analysed by native PAGE. Differential chromatographic behaviour of lignocellulosic enzymes produced by C. versicolor (i.e. polygalacturonase, xylanase and laccase) was studied on immobilized metal chelates. The effect of ligand concentration, pH, the length of spacer arm and the nature of metal ion were studied for enzyme adsorption on immobilized metal affinity chromatography (IMAC). The adsorption of these lignocellulosic enzymes onto immobilized metal chelates was pH-dependent since an increase in protein adsorption was observed as the pH was increased from 6.0 to 8.0. The adsorption of polygalacturonase as well as other enzymes to immobilized metal chelates was due to coordination of histidine residues which are available at the protein surface since the presence of imidazole in the equilibration buffer abolished the adsorption of the enzyme to immobilized metal chelates. A one-step purification of polygalacturonase from C. versicolor was devised by using a column of Sepharose 6B-EPI 30-IDA-Cu(II) and purified enzyme exhibited a specific activity of about 150 U/mg protein, final recovery of enzyme activity of 100% and a purification factor of about 10. The use of short spacer arm and the presence of imidazole in equilibration buffer exhibited a higher selectivity for purification of polygalacturonase on this column with a high purification factor. The purified enzyme preparation was analysed by SDS-PAGE as well as by "in situ" detection of enzyme activity.     

Single-step purification of lipase from Burkholderia multivorans using polypropylene matrix

Lipase from Burkholderia multivorans was purified with high yields directly from fermentation broth by a single-step purification protocol involving adsorption and desorption. The crude enzyme (lyophilized powder) from B. multivorans was loaded on Accurel (Membrana, Germany), a polypropylene matrix, using butanol as the solvent in a buffer at pH 9.0 and ambient temperature for a period of 12 h. The enzyme adsorbed onto the matrix with high specific activity (33 units mg^–1 protein). This was followed by desorption of the enzyme from the matrix using Triton X-100 as the eluent. The enzyme was finally recovered by precipitation with acetone (50%, v/v). Thus, an overall enzyme yield of 66% with a 3.0-fold purification was obtained. The purity of the enzyme was ascertained by SDS-PAGE. The phenomenon of adsorption and desorption on Accurel was studied for three more lipases, viz. Mucor meihei lipase (Sigma–Aldrich Co.), Lipolase (Novo Nordisk, Denmark) and Pseudomonas aeruginosa lipase (laboratory isolate).     

聚丙烯腈纤维固定化青霉素酰化酶合成头孢氨苄的研究

将巨大芽孢杆菌胞外青霉素酰化酶通过共价键结合到聚丙烯腈纤维的衍生物上。制成的丝状固定化青霉素酰化酶表现活力达 1 5 3U g(湿重 )。固定化酶合成头孢氨苄的最适pH为 6 5 ,最适温度为 40℃。 7 ADCA的投料浓度以 4%为好 ,7 ADCA与PGME的投料量比率为1∶2 ,最佳用酶量为 1 70U g 7 ADCA。在pH6 5、温度 3 0℃时 ,固定化酶对 7 ADCA的表观米氏常数K7 ADCA为 0 1 6 2mol L ,对PGME的表观米氏常数KPGME为 0 3 6 4mol L ,最大反应速度Vmax为0 0 4 6 2mol·L- 1·min- 1,用固定化酶合成头孢氨苄 ,使用 5 0次保留酶活力 83 9%     

A support-spacer-ligand system for specific affinity adsorption of penicillin acylase

Summary An affinity system for specific adsorption of penicillin acylase is reported in the present work. When all the active enzyme was adsorbed by an appropriate amount of carrier, 50% of the total protein containing only inactive portion remained in solution exhibiting strong and preferential adsorption of enzyme.     

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％。