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谷氨酸脱羧酶(GAD)是生物法制备γ-氨基丁酸GABA以及一些含氮化合物的关键酶,其催化活力受p H值调控。研究GAD的pH值调控性质具有重要的理论和应用价值。研究通过氨基酸序列比对,发现了一个影响GAD 1407催化p H特性的关键位点:S307。通过对这个位点进行饱和突变,构建突变文库,从中筛选出催化pH范围拓宽的突变酶S307N,并对该突变酶的酶学性质进行了研究。为了解GAD 1407结构与功能之间的相互关系提供了一定的依据。 相似文献
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为了降低细胞壁和细胞膜的传质阻力对全细胞催化过程的不利影响,采用有机溶剂对表达重组谷氨酸脱羧酶(GAD)的工程菌BL21(DE3)-p ET28a-gad B进行了透性化处理。结果表明,菌体GAD表观催化活力的改善程度与有机溶剂的介电系数和疏水性具有较强相关性,低介电常数(6),高疏水性(log P0.68)的有机溶剂可以有效提高工程菌的GAD催化活性,其中最有效的透性化试剂为二甲苯(介电常数为2.4,log P为3.1)。当二甲苯的用量为5μL?mg?1(干重细胞)、处理时间5 min时,菌体表观催化活力达到最优值,为7.94 U?mg?1(干重细胞),是处理前表观催化活力的12.4倍。为了充分利用菌体的催化活力,采用海藻酸钙包埋的方法对二甲苯处理过的菌体进行固定化,结果发现固定化的透性化菌体可以较好地保持催化活力,反复催化10次后发现,第10次的GABA产率为第1次GABA产率的72.04%。研究为系统的选择有机溶剂来有效提高GAD工程菌表观催化活性提供了参考,同时制备的固定化的透性化菌体显示了良好工业应用前景。 相似文献
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高产酸乳酸菌的分离鉴定及生物学特性研究 总被引:1,自引:0,他引:1
《山东化工》2015,(22)
采用改良乳酸菌选择性培养基从豆清发酵液中分离纯化出3株菌落形态各异的乳酸菌,对这3种菌发酵过程中p H及产酸量进行监测,筛选出一株产酸较多的优势菌株(编号LDS201)。结果表明:该菌落呈圆形,乳白色,边缘整齐,不透明,革兰氏染色阳性,菌体呈短杆状,单生或呈短链;经生理生化和16S rRNA基因序列分析鉴定该菌株为产酸解淀粉乳杆菌。 相似文献
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利用p ETDuet-1为载体在宿主细胞E.coli BL21(DE3)中重组表达了粪产碱菌(Alcaligenes faecalis)来源的天冬氨酸-β-脱羧酶(Asd),研究了其酶学性质,考察了p H、p H稳定性、温度、热稳定性、底物浓度对酶活的影响。结果表明,天冬氨酸-β-脱羧酶重组表达成功;最适反应温度和p H分别为45℃和6.0;动力学常数Km和Vmax分别为0.72 mmol/L和10.52 mol/(L·min·g)。0.1 g菌体细胞在10 m L 0.2 mol/L磷酸缓冲溶液中催化2.0 g L-天冬氨酸,40℃,p H=6.0反应15 h,L-天冬氨酸的摩尔转化率达到98.6%。 相似文献
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酪氨酸脱羧酶能以L-酪氨酸为底物脱羧生成酪胺。本文利用pET-28a为载体在宿主细胞E. coli BL21(DE3)中重组表达了短乳杆菌来源的酪氨酸脱羧酶,并研究了其酶学性质,考查了起始pH、温度、辅酶、底物浓度等因素对酶活的影响。结果表明,酪氨酸脱羧酶重组表达成功,酶促反应工艺为:在1 mL转化液中含有0.18 g的L-酪氨酸,0.02 g湿菌体,0.2 M的醋酸缓冲溶液和0.2 mM的5'-磷酸吡哆醛,40℃,pH 5.5反应7 h,L-酪氨酸的摩尔转化率达到99%。酪氨酸脱羧酶酶活为29.2 U/g,Km值和Vmax为0.71 mM和9.31 mol/L?min?g。 相似文献
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酪氨酸脱羧酶能以L-酪氨酸为底物脱羧生成酪胺。该文利用pET28a为载体在宿主细胞E.coli BL21(DE3)中重组表达了短乳杆菌来源的酪氨酸脱羧酶,并研究了其酶学性质,考察了起始pH、温度、辅酶、底物浓度等因素对酶活的影响。结果表明,酪氨酸脱羧酶重组表达成功,酶促反应工艺为:在1 mL转化液中含有0.18 g L-酪氨酸,0.02 g湿菌体,0.2 mol/L的醋酸缓冲溶液和0.2 mmol/L的5'-磷酸吡哆醛,40℃,pH=5.5,反应7 h,L-酪氨酸的摩尔转化率达到99%。酪氨酸脱羧酶酶活为29.2 U/g,Km值和Vmax为0.71 mmol/L和9.31mol/(L·min·g)。 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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D. G. Gordeev L. F. Gudarenko M. V. Zhernokletov V. G. Kudel’kin M. A. Mochalov 《Combustion, Explosion, and Shock Waves》2008,44(2):177-189
A semi-empirical equation of state for metals is described. Its capabilities are demonstrated by the example of the equation
of state for aluminum. New experimental data are presented on the location of the isentrope of aluminum for unloading from
the state at p = 229.71 GPa on the shock adiabat to an aerogel (SiO2) of density 0.08 g/cm3.
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Translated from Fizika Goreniya i Vzryva, Vol. 44, No. 2, pp. 61–75, March–April, 2008. 相似文献
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Jorge Marcelo Romero Soledad Bustillo Hugo Enrique Ramirez Maisuls Nelly Lidia Jorge Manuel Eduardo Gómez Vara Eduardo Alberto Castro Alicia H. Jubert 《International journal of molecular sciences》2007,8(7):688-694
A thermochemical rather simple experimental technique is applied to determine the enthalpy of formation of Diperoxide of ciclohexanone. The study is complemented with suitable theoretical calculations at the semiempirical and ab initio levels. A particular satisfactory agreement between both ways is found for the ab initio calculation at the 6–311G basis This set level. Some possible extensions of the present procedure are pointed out. 相似文献
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A perturbation viscometer is a differential capillary viscometer that measures the logarithmic viscosity gradient of the viscosity-composition curve for gas mixtures. Measurements are made at different gas mixture compositions. Integration of the logarithmic viscosity gradients measured over the full composition range gives the mixture viscosity relative to the viscosity of one of the pure components of the gas mixture. This method is attractive because, for measurements of equal precision, integration of the gradients is potentially an order of magnitude more precise than measurement of the viscosities directly. It can also work at high and low temperatures and perhaps high pressures.The perturbation viscometer has been used to make measurements on ideal gas mixtures at ambient and elevated temperatures. The situation is more complicated when the gas mixtures are non-ideal. Extra effects due to density differences, molar volume change on mixing and differential thermal expansion may be measured in addition to the desired viscosity change producing systematic errors in the results. Thus, a more sophisticated apparatus is required. The standard perturbation viscometer has been modified to separate out the extra effects to permit measurement of the true change in viscosity. In addition, the theoretical operation of the modified apparatus has been revised to account for the design changes to permit calculation of the viscosity-composition profiles from the results.The apparatus has been tested using helium-HFC-125 mixtures and two new viscosity-composition profiles are presented for these mixtures at 23 and . Internal consistency tests have been used to confirm that the data produced are of high quality with an estimated uncertainty in the viscosity ratio data at of 0.9% and at of 1.5%. 相似文献
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塔设备改造选型的分析 总被引:2,自引:0,他引:2
就当前扩产增容中塔设备设计和改造时板式塔和填料塔的选型问题加以分析。在评述目前国内常用的几种塔板和新型填料之后,着重介绍一种新型塔板(导向梯形浮阀塔板)和一种新型填料(波环填料——乾隆帕克)。 相似文献