产氨基酰化酶米曲霉高产菌株的选育

采用亚硝基瓜抑菌圈法对米曲霉菌株3042,AF92011,AF93018,AF93020,AF93022,AF93332进行诱变处理,从诱变菌株中筛选到几个高产氨基酰化酶菌株(3042-5,AF93020-2,AF93020-6和AF93022-5),对DL-蛋氨酸的拆分活力分别比出发菌株提高34.1%、157.6%、152.4%和145.4%,其中米曲霉菌株3042的诱变菌株3042-5最高酶活力达203.1U/ml     

米曲霉产氨基酰化酶最佳活力条件的研究

通过在不同的反应时间,反应温度,缓冲液种类及pH条件下测定氨基酰化酶的活力,得出氨基酰化酶的最佳活力条件。试验结果表明,氨基酰化酶在反应温度为37℃、磷酸缓冲液pH为7.5、与底物反应30 m in时,活力最高。     

截流荧光法研究米曲霉氨基酰化酶的快速胍变性动力学

 用荧光光谱法、截流荧光法和酶活力测定法研究了在盐酸胍溶液中米曲霉氨基酰化酶变性动力学。我们发现在4.8mol/L盐酸胍溶液作用下(0.05mol/L磷酸缓冲溶液,pH7.4,25℃),氨基酰化酶二聚体解离成单亚基过程是一个十分快速的过程,反应速率常数k为3361l/s,即约需3ms时间完成;而单亚基分子的构象变化需要约20min方能到达平衡态,这是一个逐渐变化的缓慢过程。酶分子在胍作用下的失活现象同酶分子的结构变化紧密相关,在胍浓度大于4mol/L时酶完全失活。在高浓度盐酸胍下酶失活主要是因为酶二聚体迅速解离成单亚基的过程和单亚基构象逐渐变化的缓慢过程。双亚基解离常数大小标志着酶分子亚基间作用力的强弱。     

N+离子注入选育高产氨基酰化酶菌株的研究

选用N~+离子注入的方法对米曲霉(Aspergillus oryzae)CICC 2339-1进行诱变育种,通过三角瓶发酵法筛选氨基酰化酶高产株。N~+离子注入选择能量为10 KeV,剂量在(1.30～4.94)×10~(15)ions/cm~2之间。根据剂量与存活率以及剂量与突变率曲线选择最佳的注入剂量。通过三角瓶发酵筛选得到突变菌株SN-110-15其酶活提高率为139.5%,诱变试验效果显著。     

米曲氨基酰化酶菌株的选育*

利用原生质体融合技术对米曲霉3042和米曲霉10B,进行了营养互补融合。以30%PEG(MW=6000)、0.01mol/L CaCl₂、0.05mol/L Gly做为融合剂,融合频率达到0.47%。共获得26株绿色融合株,并对其杂合二倍体的孢子进行了PFA和UV的诱发分离,获得一株生长速度快、氨基酰化酶活性高的单倍体菌株。     

PAR对氨基酰化酶不可逆抑制动力学研究

本文将邹氏的在酶的活性修饰剂存在下的底物反应动力学理论应用于氨基酰化酶被金属螯合剂PAR脱锌而失活的动力学研究。通过对不同浓度的PAR存在下底物反应过程和含有PAR的不同浓度的底物中酶促反应的分析,讨论了PAR对氨基酰化酶的脱锌机制。这一过程很可能按如下机制进行:首先,PAR与酶分子活性部位的锌结合,形成一复合物,这一步是较快的反应,然后发生一个可逆的构象变化,最后是不可逆的去锌步骤。锌的存在显然稳定了酶活性部位的构象,而这正是酶活性所必需的。     

One-step purification of proteins from chicken egg white using counter-current chromatography

Proteins present in chicken egg white are separated by counter-current chromatography (CCC) in one step using a cross-axis coil planet centrifuge (X-axis CPC). The separation was performed with an aqueous polymer two-phase system composed of 16% (w/w) poly(ethylene glycol) 1000 and 12.5% (w/w) dibasic potassium phosphate by eluting the lower phase at a flow-rate of 1.0 ml/min. From about 20 g of the crude egg white solution, lysozyme, ovalbumin, and ovotransferrin were resolved within 5.5 h. Each component was identified by 12% SDS gel electrophoresis with Coomassie brilliant blue staining.     

白地霉脂肪酶的双水相萃取和反胶团提取

对影响双水相萃取和反胶团提取脂肪酶的各种因素进行了探讨,并通过正交实验进一步优化提取条件,PEG浓度15%,(NH4)2SO4浓度22.5%,pH8.0的条件下进行双水相萃取,脂肪酶纯化倍数达到7.5倍;CTAB浓度150mmol/L,相体积比4/2,水相pH8.0,温度40℃的条件下进行反胶团提取,脂肪酶的比活力达到最大,但其比活力稍有下降,约为原来的0.9倍。     

白地霉Cryytococcus neoformans脂肪酶的双水相萃取

本文研究了不同无机盐的双水相体系对白地霉脂肪酶的萃取分离效果,对PEG/（NH4）2SO4成相系统进行了系统的研究,通过考察体系PEG分子量、不同的无机盐、PEG浓度、（NH4）2SO4浓度、离子强度、pH值及（NH4）2SO4浓度对反萃取的影响,并通过正交实验进一步优化了实验条件,初步确定在PEG浓度15%,（NH4）2SO4浓度22.5%,pH8.0,不加NaCl的条件下进行双水相萃取,脂肪酶分离系数和纯化倍数分别为6.8和7.5,比活力达到40.3 U/mg蛋白。     

Pectinase partitioning in polyethylene glycol 1000/Na2SO4 aqueous two-phase system: statistical modeling of the experimental results

Statistical models concerning partitioning of pectinase in polyethylene glycol 1000/Na₂SO₄ aqueous two-phase system were established with response surface methodology. Concentrations of polyethylene glycol 1000 and Na₂SO₄ were selected as independent variables to evaluate their impact on parameters of partitioning in aqueous two-phase system—the partition coefficient of pectinase, purification factor and pectinase yield. An experimental space where over 2.5-fold purification was achieved, followed by over 90% yield of pectinase. The established models showed good prediction of partitioning parameters.     

Aqueous two-phase systems

Biphasic systems formed by mixing of two polymers or a polymer and a salt in water can be used for separation of cells, membranes, viruses, proteins, nucleic acids, and other biomolecules. The partitioning between the two phases is dependent on the surface properties and conformation of the materials, and also on the composition of the two-phase system. The mechanism of partitioning is, however, complex and not easily predicted. Aqueous two-phase systems (ATPS) have proven to be a useful tool for analysis of biomolecular and cellular surfaces and their interactions, fractionation of cell populations, product recovery in biotechnology, and so forth. Potential for environmental remediation has also been suggested. Because ATPS are easily scalable and are also able to hold high biomass load in comparison with other separation techniques, the application that has attracted most interest so far has been the large-scale recovery of proteins from crude feedstocks. As chemicals constitute the major cost factor for large-scale systems, use of easily recyclable phase components and the phase systems generated by a single-phase chemical in water are being studied.     

Recovery in aqueous two-phase systems of lutein produced by the green microalga Chlorella protothecoides

The objective of this study was to develop a chromatographic method for the analysis of the anti-androgen vinclozolin (V) and its metabolites 2-[[(3,5-dichlorophenyl)-carbamoyl]oxy]-2-methyl-3-butenoic acid (M1), 3',5'-dichloro-2-hydroxy-2-methylbut-3-enanilide (M2) and 3,5-dichloroaniline (M3) in rat serum. V, M1-M3 were resolved using an HPLC gradient program with a mobile phase consisting of 60-75% methanol:acetonitrile (70:30) and 0.05 M monobasic sodium phosphate buffer pH 3.3 at 1 ml/min, a C18 column, and monitored at 212 nm. Incubates of 0.01 M monobasic potassium phosphate buffer (PB) pH 7.4 and rat serum were spiked with V and its metabolites and processed by diluting samples (1:4) with 0.1M PB pH 3.3, to limit methodological hydrolysis of analytes, followed by addition of acetonitrile. Recoveries of V, M1 and M2 ranged from 85 to 105%, whereas recovery of M3 was <25%. V was hydrolyzed to M1 and M2 after incubation in PB pH 7.4 and rat serum, with M1 the predominant metabolite. This method was successfully applied in the analysis of V and its metabolites in the serum of a male rat after oral administration of V (100 mg/kg).