乳糖诱导植物甜蛋白des-pGlu1-Brazzein在大肠杆菌中的表达

构建了植物甜蛋白des-pGlu1-Brazzein高效表达的工程菌株,对其乳糖诱导条件进行了优化。乳糖浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示,高浓度乳糖对菌株生长有抑制作用（P<0.01）,对目的蛋白的表达无显著影响(P>0.05),时间延长对于菌株生长有利（P<0.01）,对目的蛋白的表达因温度不同而不同。进一步的研究表明,以0.5% 乳糖在28℃～30℃诱导4h对菌株生长和目的蛋白的表达有利,目的蛋白的表达量可达20%左右。     

乳糖作为诱导剂对人β-防御素3蛋白表达的影响*

对人β-防御素3基因工程菌株BL21-pET-hBD3的乳糖诱导条件进行了研究。乳糖浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示,高浓度乳糖对菌株生长有抑制作用(P<0.01),对目的蛋白的表达无显著影响(P>0.05),延长诱导时间对菌株生长有利(P<0.01),但对蛋白的表达无显著影响(P>0.05)。以0.5%乳糖在37℃诱导4h对目的蛋白的表达有利,目的蛋白的含量可达28.1%。控制好诱导条件,乳糖与IPTG的     

乳糖作为诱导剂对人β-防御素3蛋白表达的影响

对人β-防御素3基因工程菌株BL21-pET-hBD3的乳糖诱导条件进行了研究。乳糖浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示,高浓度乳糖对菌株生长有抑制作用（P〈0．01）,对目的蛋白的表达无显著影响（P〉0.05）,延长诱导时间对菌株生长有利（P〈0．01）,但对蛋白的表达无显著影响（P〉0.05）。以0．5％乳糖在37℃诱导4h对目的蛋白的表达有利,目的蛋白的含量可达28,1％。控制好诱导条件,乳糖与IPTC的诱导效果基本相当。     

人β防御素3和植物des-pGLu1-brazzein融合蛋白表达菌的诱导条件优化及其活性分析

对人β防御素3和植物甜蛋白des-pGlu1-Brazzein嵌合基因的工程菌株BL-pET-hBD3-Bra的IPTG诱导表达条件进行了研究,同时对所表达的目的蛋白进行了纯化和活性分析.IPTG浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示:所取的IPTG浓度(0.2～1.0 mmol/L)对菌株生长和目的蛋白的表达无显著影响(P>0.05);菌株的生物量随着诱导时间的延长而增加,6 h优于4 h(P<0.01),但是蛋白的表达量无明显增加(P>0.05);其中温度是重要的影响因素,在30℃诱导时,目的蛋白的表达量占总蛋白的35%左右.进一步的研究表明,菌株在30℃-32℃生长,在30℃诱导最优.对目的蛋白的活性分析表明,所得到的hBD3-Bra融合蛋白有甜味,其甜度大约是蔗糖的200倍,但是其杀菌活性很弱,经凝血酶切割后,des-pGlu1-Brazzein的甜度大大提高,大约为蔗糖甜度的600倍,重组hBD3对大肠杆菌和金黄色葡萄球菌有明显的抑菌活性.     

A型产气荚膜梭菌α毒素基因表达及其免疫保护作用的初步研究

利用PCR技术,从A型产气荚膜梭菌标准株染色体DNA中扩增出α毒素基因,构建了含α毒素基因的重组菌株BL21(DE3)(pXETA02)。经酶切鉴定和序列测定证实,构建的表达质粒pXETA02含有α毒素基因序列。经SDS-PAGE、Western blot分析和ELISA检测,重组菌株表达的α毒素蛋白能够被α毒素单抗识别。表达优化结果表明,以IPTG为诱导剂诱导α毒素表达的优化条件是:培养基pH 7.5,培养温度37℃,IPTG浓度0.8mmol/L,菌体生长密度OD600达到0.8时加入IPTG,诱导时间5h,此时α毒素蛋白表达量为34.83%。以乳糖为诱导剂诱导α毒素表达的优化条件是:培养基pH7.5、培养温度37℃,乳糖浓度0.1g/L,菌体生长密度OD600达到0.8时加入乳糖,诱导时间5h,α毒素蛋白表达量为23.82%。动物实验结果表明,用重组菌株α毒素蛋白免疫的小鼠可以抵抗1MLD的A型产气荚膜梭菌标准株C57-1毒素攻击。     

人b防御素3和植物des-pGLu1-brazzein融合蛋白表达菌的诱导条件优化及其活性分析

对人b防御素3和植物甜蛋白des-pGlu1-Brazzein嵌合基因的工程菌株BL-pET-hBD3-Bra的IPTG诱导表达条件进行了研究, 同时对所表达的目的蛋白进行了纯化和活性分析。IPTG浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示: 所取的IPTG浓度(0.2~1.0 mmol/L)对菌株生长和目的蛋白的表达无显著影响(P>0.05); 菌株的生物量随着诱导时间的延长而增加, 6 h优于4 h(P<0.01), 但是蛋白的表达量无明显增加(P>0.05); 其中温度是重要的影响因素, 在30°C诱导时, 目的蛋白的表达量占总蛋白的35%左右。进一步的研究表明, 菌株在30°C~32°C生长, 在 30°C诱导最优。对目的蛋白的活性分析表明, 所得到的hBD3-Bra融合蛋白有甜味, 其甜度大约是蔗糖的200倍, 但是其杀菌活性很弱, 经凝血酶切割后, des-pGlu1-Brazzein的甜度大大提高, 大约为蔗糖甜度的600倍, 重组hBD3对大肠杆菌和金黄色葡萄球菌有明显的抑菌活性。     

人b防御素3和植物des-pGLu1-brazzein融合蛋白表达菌的诱导条件优化及其活性分析

对人b防御素3和植物甜蛋白des-pGlu1-Brazzein嵌合基因的工程菌株BL-pET-hBD3-Bra的IPTG诱导表达条件进行了研究, 同时对所表达的目的蛋白进行了纯化和活性分析。IPTG浓度、诱导时间和诱导温度对菌株生长和目的蛋白表达的试验结果显示: 所取的IPTG浓度(0.2~1.0 mmol/L)对菌株生长和目的蛋白的表达无显著影响(P>0.05); 菌株的生物量随着诱导时间的延长而增加, 6 h优于4 h(P<0.01), 但是蛋白的表达量无明显增加(P>0.05); 其中温度是重要的影响因素, 在30°C诱导时, 目的蛋白的表达量占总蛋白的35%左右。进一步的研究表明, 菌株在30°C~32°C生长, 在 30°C诱导最优。对目的蛋白的活性分析表明, 所得到的hBD3-Bra融合蛋白有甜味, 其甜度大约是蔗糖的200倍, 但是其杀菌活性很弱, 经凝血酶切割后, des-pGlu1-Brazzein的甜度大大提高, 大约为蔗糖甜度的600倍, 重组hBD3对大肠杆菌和金黄色葡萄球菌有明显的抑菌活性。     

乳糖代替IPTG诱导己糖激酶在大肠杆菌中的表达

构建了己糖激酶GLK高效表达的工程菌株BL21(DE3)/pET-glk,考察了乳糖代替IPTC诱导己糖激酶GLK在大肠杆菌BL21(DE3)中表达的可行性.实验结果表明,工程菌对数生长中期(OD<,600>约为1.0)添加终浓度为10 g/L的乳糖于25℃的条件下诱导6 h能获得最大量的目的蛋白和菌体量,目的蛋白表达...     

argE基因在大肠杆菌中的表达优化

N-乙酰鸟氨酸脱酰基酶可在重组菌BL21（DE3）-pET22b-argE中表达。首先确定了该酶的细胞表达定位,再研究了诱导温度、诱导剂种类及浓度、诱导起始菌体密度、诱导时间等因素对重组菌生长及目的蛋白表达活性的影响。结果表明,IPTG和乳糖皆可诱导目的蛋白表达,乳糖的诱导效果优于IPTG。在诱导起始0D600为0．46时加入15g／L乳糖,20℃诱导18h最适于目的蛋白的活性表达。表达条件优化后,酶活从1．68U／mL提高至282．99U／mL,约为原来的168倍。     

结核分枝杆菌H37Ra株HspX蛋白的表达条件优化、纯化和鉴定

以结核分枝杆菌H37Ra菌株基因组DNA为模板,利用PCR技术扩增获得HspX基因,通过DNA无缝克隆技术将其克隆至pET28a质粒中,构建重组表达质粒pET28a-HspX。将pET28a-HspX转化至大肠埃希菌表达菌株BL21(DE3),采用不同温度、IPTG浓度和时间诱导HspX蛋白表达。使用Ni-IDA亲和层析柱纯化目的HspX蛋白,透析去除咪唑,通过Western blot检测HspX抗原特异性。最终确定表达重组蛋白HspX的最佳诱导条件为：诱导温度37℃、IPTG浓度0.2 mmol/L、诱导时间8 h。结果表明,获得了高纯度和被特异性识别的可溶性Hsp X蛋白,为未来Hsp X蛋白用于结核病诊断试剂和疫苗奠定基础。     

转糖基β-半乳糖苷酶产生菌Enterobacter agglomerans B1：筛选鉴定、发酵产酶及其合成低聚半乳糖的研究

从土壤中筛选获得一株具有转糖基活性的β-半乳糖苷酶产生菌,综合其形态学特征、生理生化特征及16S rDNA序列同源分析结果,将其鉴定为成团肠杆菌(Enterobacter agglomerans)B1.通过单因子试验和正交试验,对B1菌株产转糖基β-半乳糖苷酶的培养条件进行了优化.最佳培养基主要组份为:乳糖1%,酵母粉1%,蛋白胨0.5%;发酵条件为:初始pH7.5,发酵温度25℃,发酵时间26 h.在该培养条件下产酶量为9.7U/mL.利用薄层层析技术研究了pH、温度、底物浓度和反应时间对该菌株全细胞以乳糖为底物生成低聚半乳糖的影响,确定最适反应条件为:pH7.5缓冲液配制的30%乳糖溶液;50℃反应12h.最优化反应的转糖基产物经HPLC、TLC和MS分析,确定低聚半乳糖产量为40.7%,组分为转移二糖、三糖和四糖.     

Influence of growth conditions on the production of a nisin-like bacteriocin by Lactococcus lactis subsp. lactis A164 isolated from kimchi

The influence of growth parameters on the fermentative production of a nisin-like bacteriocin by Lactococcus lactis subsp. lactis A164 isolated from kimchi was studied. The bacteriocin production was greatly affected by carbon and nitrogen sources. Strain A164 produced at least 4-fold greater bacteriocin in M17 broth supplemented with lactose than other carbon sources. The amount of 3% yeast extract was found to be the optimal organic nitrogen source. While the maximum biomass was obtained at 37 degrees C, the optimal temperature for the bacteriocin production was 30 degrees C. The bacteriocin production was also affected by pH of the culture broth. The optimal pH for growth and bacteriocin production was 6.0. Although the cell growth at pH 6.0 was nearly the same level at pH 5.5 and 6.5, the greater bacteriocin activity was observed at pH 6.0. Exponential growth took place only during an initial period of the cultivation, and then linear growth was observed. Linear growth rates increased from 0.160 g(DCW) x l(-1) x h(-1) to 0.245 g(DCW) x l(-1) x h(-1) with increases in lactose concentrations from 0.5 to 3.0%. Maximum biomass was also increased from 1.88 g(DCW) x l(-1) to 4.29 g(DCW) x l(-1). However, increase in lactose concentration did not prolong the active growth phase. After 20 h cultivation, cell growth stopped regardless of lactose concentration. Production of the bacteriocin showed primary metabolic kinetics. However, bacteriocin yield based on cell mass increased greatly during the late growth phase. A maximum activity of 131x10(3) AU x ml(-1) was obtained at early stationary growth phase (20 h) during the batch fermentation in M17L broth (3.0% lactose) at 30 degrees C and pH 6.0.     

脂肪酶抑制剂产生菌Bacillus sp.LF深层发酵条件研究

随着生活水平的不断提高 ,肥胖在中国也开始成为影响人们健康的主要危险之一。目前市场上常见的减肥产品主要是作用于大脑 ,通过抑制食欲减少食物的摄入 ,由于这类药可能产生大脑、心血管及神经系统的副作用 ,不宜长期使用。瘦素 (Leptin)是一种肥胖基因表达的多肽激素 ,也是通过食欲中枢发挥作用 ,可以抑制食欲 ,提高代谢率 ,达到减肥的目的。因而另一类减肥药品脂肪酶抑制剂近年来受到国内外重视。脂肪酶抑制剂可直接阻断人体对脂肪的吸收 ,它不需要通过影响中枢神经系统来抑制人体的食欲 ,而是阻止脂肪在胃肠道的吸收。文献报道脂肪酶抑…     

Influence of ambient air temperature on the cooling/heating load of a single cell protein jacketed fermenter operating on cheese whey under continuous conditions

The heat generated by mixing and lactose metabolism, during the continuous production of single cell protein from cheese whey lactose using a jacketed fermenter with running cooling water, was calculated using a heat balance equation. The technique quantified the heat produced in and lost from the fermentation unit. Most of the heat generated by mixing in the cell-free system (97.47%) was lost with exhaust gas, while a very small amount (2.53%) was lost through the fermenter lid, wall, and bottom. The heat generated by mixing was significant (26.31% of the total heat generated in the fermentation system with an active yeast population present) and, therefore, cannot be ignored in heat balance calculations. About 19.71% of the total heat generated in the reactor was lost through the coolant at an ambient temperature of 22 +/- 0.5 degrees C, showing the need for a cooling system. A yeast population size of 986 million cells/mL and a lactose removal efficiency of 95.6% were observed. About 72.5% and 27.5% of the lactose consumed were used for growth and respiration, respectively. A yield of 0.66 g of cells/g of lactose was achieved. The heat released by unit biomass was 7.05 kJ/g of cells. The results showed the significant impact of ambient air temperature on the cooling load. The heat to be removed from the medium by the cooling system varied from 3.46 to 281.56 kJ/h when the temperature increased from 16 to 30 degrees C. A heating system is needed to maintain the medium temperature at 34 degrees C when the ambient air temperature is below 16 degrees C.     

Selection of yeast strain and fermentation conditions for high-yield ethanol production from lactose and concentrated whey

A total of 65 yeast strains were screened for their ability to grow and ferment lactose in a standard DURHAM tube test at 30 °C. Based on the kinetic parameters for lactose and whey lactose fermentations in shake flask cultures, the strain Candida psedotropicalis 65 was chosen for further studies. Some of the cultural parameters affecting ethanolic fermentations on lactose were standardized. At an initial lactose concentration of 100–120 g/l in the medium containing concentrated whey or lactose, at 40 °C and within 48 h, the selected strain reached an ethanol concentration of 41–59 g/l, an ethanol productivity of 1.3–3.0 g/l/h, a lactose consumption of 99%, an ethanol yield 0.4–0.49 g/g and a biomass yield of 0.027 g/g.     

乳糖诱导的重组人血管内皮抑素(rhEndostatin)蛋白的表达

研究用乳糖替代IPTG作为诱导剂进行重组蛋白的表达,观察乳糖对乳糖操纵子调控的基因工程菌发酵及重组血管内皮抑素表达的影响,从而选取最佳诱导表达条件。以重组人血管内皮抑素表达工程菌pETrhEN/BL21(DE3)作为研究对象,分别用IPTG和乳糖作为诱导剂,在摇瓶中进行表达实验。并对重组蛋白质表达量进行分析。然后在5 L发酵罐中进行验证。在摇瓶培养条件下,乳糖浓度大于0.5 g/L即可以诱导目的蛋白的表达。乳糖浓度1 g/L时诱导目的蛋白表达量与1 mmol/L的IPTG相当,当乳糖浓度为10 g/L,目的蛋白表达量达到最大。在发酵罐培养条件下,补料4 h后葡萄糖浓度基本耗尽,此时开始加入乳糖。诱导后1 h,即有重组蛋白表达,在诱导后4 h达到高峰(占菌体可溶性蛋白的56%),与此同时,诱导后5 h菌体浓度也达到最高值。在以乳糖操纵子为调控手段的工程菌表达系统中,可以使用乳糖作为诱导剂,诱导应在葡萄糖消耗完后进行。     

Influence of the lactose plasmid on the metabolism of galactose by Streptococcus lactis.

Streptococcus lactis strain DR1251 was capable of growth on lactose and galactose with generation times, at 30 degrees C, of 42 and 52 min, respectively. Phosphoenolpyruvate-dependent phosphotransferase activity for lactose and galactose was induced during growth on either substrate. This activity had an apparent K(m) of 5 x 10(-5) M for lactose and 2 x 10(-2) M for galactose. beta-d-Phosphogalactoside galactohydrolase activity was synthesized constitutively by these cells. Strain DR1251 lost the ability to grow on lactose at a high frequency when incubated at 37 degrees C with glucose as the growth substrate. Loss of ability to metabolize lactose was accompanied by the loss of a 32-megadalton plasmid, pDR(1), and Lac(-) isolates did not revert to a Lac(+) phenotype. Lac(-) strains were able to grow on galactose but with a longer generation time. Galactose-grown Lac(-) strains were deficient in beta-d-phosphogalactoside galactohydrolase activity and phosphoenolpyruvate phosphotransferase activity for both lactose and galactose. There was also a shift from a predominantly homolactic to a heterolactic fermentation and a fivefold increase in galactokinase activity, relative to the Lac(+) parent strain grown on galactose. These results suggest that S. lactis strain DR1251 metabolizes galactose primarily via the tagatose-6-phosphate pathway, using a lactose phosphoenolpyruvate phosphotransferase activity to transport this substrate into the cell. Lac(-) derivatives of strain DR1251, deficient in the lactose phosphoenolpyruvate phosphotransferase activity, appeared to utilize galactose via the Leloir pathway.     

Growth of Pseudomonas aeruginosa in tap water in relation to utilization of substrates at concentrations of a few micrograms per liter.

Five Pseudomonas aeruginosa strains were tested for the utilization of 47 low-molecular-weight compounds as their sole sources of carbon and energy for growth at a concentration of 2.5 g/liter. Of these compounds, 31 to 35 were consumed. Growth experiments in tap water at 15 degrees C were carried out with one particular strain (P1525) isolated from drinking water. This strain was tested for the utilization of 30 compounds supplied at a concentration of 25 microgram of C per liter. The growth rate (number of generations per hour) of strain P1525 in this tap water was approximately 0.005 h-1, and with 10 compounds it was larger than 0.03 h-1. An average yield of 6.2 x 10(9) colony-forming units per mg of C was obtained from the maximum colony counts (colony-forming units per milliliter). The average yield and maximum colony count of strain P1525 grown in tap water supplied with a mixture of 45 compounds, each at a concentration of 1 microgram of C per liter, enabled us to calculate that 28 compounds were utilized. Growth rates of two P. aeruginosa strains (including P1525) in various types of water at 15 degrees C were half of those of a fluorescent pseudomonad. The concentrations of assimilable organic carbon calculated from maximum colony counts and average yield values amounted to 0.1 to 0.7% of the total organic carbon concentrations in five types of tap water. The assimilable organic carbon percentages were about 10 times larger in river water and in water after ozonation.