微波处理对人参皂苷生物转化影响的研究

利用微波技术分别对人参皂苷粗品及人参皂苷转化发酵液进行处理,探讨微波处理对人参皂苷生物转化效果的影响。实验结果通过高效液相色谱分析显示,经微波处理后,人参皂苷峰几乎消失,苷元峰突出,表明微波处理对人参皂苷的转化效果显著。并确定微波的最佳处理条件为微波功率30W,辐射60s。     

稀有人参皂苷IH901酶法转化与制备研究

本研究利用酶制剂蜗牛酶,酶法转化三七二醇组皂苷制备稀有人参皂苷IH901,正交实验优化酶解条件,建立酶法转化工艺.结果表明:超声法提取三七总皂苷正交实验优化条件为用75%乙醇溶液,15倍溶剂用量,超声波提取210 min作为最佳条件,三七总皂苷得率为12.21%;酶法转化二醇组人参皂苷制备稀有人参皂苷IH901,正交实验优化的条件为物料比为6/1、反应时间9 h、反应温度为45℃、pH值为3.0,酶解得率为54.24%;经硅胶柱分离获得IH901单体化合物,HPLC测定纯度达98%.酶法转化制备皂苷IH901的工艺方法简便,切实可行,可为中试生产提供参考.     

黑曲霉降解人参皂苷Rb1制备稀有皂苷Compound K

稀有人参皂苷Compound K(C-K)具有显著的生物学活性。从东北农耕土壤中分离出9株真菌,系统研究了其转化人参皂苷Rb1制备C-K的能力。其中,黑曲霉Aspergillus niger sp.J7能够高效转化人参皂苷Rb1生成C-K,转化途径为Rb1→Rd→F2→C-K。对黑曲霉J7转化Rb1制备C-K的条件进行优化,在最优条件下,Rb1可完全转化成C-K。将该转化体系扩大到200 m L,60 h内可将Rb1完全转化成C-K,转化率为74.7%。黑曲霉J7为人参皂苷Rb1高效水解为稀有人参皂苷C-K奠定了基础。     

响应面法优化人参不定根中总皂苷的提取工艺

以人参不定根为原材料,利用乙醇提取人参总皂苷,选择提取温度、乙醇浓度和料液比为主要影响因素,以人参总皂苷得率作为响应值,利用响应面法优化人参不定根总皂苷的提取工艺。根据Box-Behnken实验设计原理,采用三因素三水平的响应面分析法,建立了人参不定根总皂苷得率与三个因素变化的二次回归方程。依据回归模型进行计算机模拟及绘制曲面图,了解人参不定根总皂苷得率随主要因素水平的变化趋势及优化点。通过对各因素显著性和交互作用的分析,得到最佳工艺条件为:提取温度70.00℃、乙醇浓度73.50%、料液比1∶34.50(g/m L),此时人参皂苷的得率为1.86±0.01%。     

黑根霉对人参皂苷Re的生物转化

利用菌种黑根霉Rhizopus sp.对人参皂苷Re进行生物转化,并对人参皂苷Re及其发酵产物进行HPLC系统分析比较,经液相色谱-质谱分析得出人参皂苷Re转化率为92.16%,并制备出人参皂苷Re发酵产物中峰值升高的成分,转化后的人参皂苷发酵产物中化合物1确定为人参皂苷Rg2,化合物2为Rg2的同分异构体,得率为10.13%;化合物3和化合物4确定为人参皂苷Rg5/Rk1,得率为29.23%。从结果初步推测得出人参皂苷Re被黑根霉转化为人参皂苷Rg2的机理,人参皂苷Re转化成人参皂苷Rg5/Rk1的机理还有待于进一步研究。     

响应面法优化微波提取绞股蓝愈伤组织中人参皂苷Rb1的工艺研究

以绞股蓝愈伤组织为原料,优化绞股蓝人参皂苷Rb1的微波提取工艺,在单因素试验的基础上,选择液料比、微波功率和微波处理时间为自变量,人参皂苷Rb1为响应值,采用响应曲面法设计、分析研究各自变量及其交互作用对人参皂苷Rb1提取率的影响.利用响应面分析方法,模拟得到二次多项式回归方程的预测模型,并确定人参皂苷Rb1微波辅助提取工艺的最佳条件为：料液比1：20（g/mL）,处理时间6 min,微波功率200 W.在此最佳工艺条件下,人参皂苷Rb1得率为3.95 mg/g.     

糖苷酶转化人参皂苷研究进展

人参皂苷为人参主要的药理活性组成部分,通过水解二醇系人参皂苷的糖苷配基是制备稀有人参皂的常用方法。酶法转化因其底物高度专一、条件温和、副产物少等潜在优势而被作为结构修饰和生理研究的主要技术手段。本文主要对糖苷酶转化人参皂苷研究进展进行了综述,为其工业化生产高活性皂苷提供理论依据。     

一种真菌对人参皂苷Rg3的转化

[目的]筛选长白山人参土壤中的活性微生物,转化人参总皂苷及单体人参皂苷产生稀有抗肿瘤成份.[方法]从长白山人参根际土壤中分离各类菌株,对人参总皂苷及单体人参皂苷进行微生物转化,并通过硅胶柱层析等方法对转化产物进行分离纯化,采用波谱解析及理化常数对其进行结构鉴定;结合菌落形态、产孢结构、孢子形态特征以及菌株ITS rDNA核酸序列分析,对活性菌株进行鉴定.[结果]从长白山人参根际土壤中分离各类真菌菌株68株,有12株菌株对人参总皂苷有转化活性,其中菌株SYP2353对二醇组人参皂苷Rg3具有较强的转化活性.[结论]阳性菌株SYP2353被鉴定为疣孢漆斑菌(Myrothecium verrucaria),能将人参皂苷Rg3转化为稀有人参皂苷Rh2及二醇组人参皂苷苷元PPD,为稀有人参皂苷Rh2的制备提供了新的方法.     

动态连续逆流提取绞股蓝皂苷的研究

本文在中试条件下,通过单因素试验和正交试验考察不同因素对绞股蓝皂苷提取得率的影响,从而探讨动态连续逆流提取绞股蓝皂苷的最佳工艺。结果表明:动态连续逆流提取绞股蓝皂苷最佳条件为:提取溶剂温度为80℃,料液比为1∶35(g/mL),提取时间为50 min。在此条件下,绞股蓝提取物平均提取得率为33.95%,皂苷得率为8.9%;动态连续逆流提取绞股蓝皂苷具有生产连续性好、皂苷提取得率高、产品纯度高等优点。     

分光光度法测定降血脂片中总皂苷含量的方法研究

建立一种简便、可靠的降血脂片中总皂苷含量的测定方法。以香草醛-高氯酸为显色体系,以人参皂苷为对照品,采用分光光度法测定降血脂片中总皂苷含量。比较分析了索氏提取法和超声波提取法对总皂苷提取分离效果的影响,并对大孔树脂填充高度进行了优化,最后对所建立的方法进行了重复性和加标回收率实验验证。结果表明,所测标准曲线的相关系数为09994,确立超声波提取法和3 cm大孔树脂填充高度为最佳实验条件,样品中总皂苷重复性相对标准偏差为18%,加标回收率为964%～990%,总皂苷测定重复性和回收率均良好。     

酵母菌转化人参皂苷Rb1的动力学

在分批发酵中,对酵母菌转化人参皂苷的动力学进行了研究。应用Logistic方程和Luedeking-Piret方程,得到了描述分批发酵过程中,酵母菌体生长、底物消耗和产物合成的动力学模型及模型参数,并对实验数据与模型进行了验证比较,模型计算值与实验值拟合良好,所建模型能很好地描述酵母菌转化人参皂苷的动力学特征。为进一步研究和预测酵母菌生物转化过程奠定理论基础。     

Modeling and optimization of cloned invertase expression in Saccharomyces cerevisiae

The aim of this study is to determine the medium feeding strategy to maximize the invertase productivity of recombinant Saccharomyces Cerevisiae using a fed-batch mode of operation. The yeast contains the plasmid, pRB58, which contains the yeast SUC2 gene, coding for the enzyme invertase. The expression of this gene is repressed at high glucose levels. A Goal-oriented model is development to describe the kinetics of fed-batch fermentations. This simple model could quantitatively describe previous experimental results. A conjugate gradient algorithm is then used, in conjunction gradient algorithm is then used, in conjunction with this mathematical model, to compute the optimum feed rate for maximization of invertase productivity. The optimal feeding procedure results in an initial high cell growth phase followed by a high invertase production phase. (c) 1993 Wiley & Sons, Inc.     

Microbial conversion of ginsenoside Rd from Rb1 by the fungus mutant Aspergillus niger strain TH-10a

Ginsenoside Rd, one of the ginsenosides with significant pharmaceutical activities, is getting more and more attractions on its biotransformation. In this study, a novel fungus mutant, the Aspergillus niger strain TH-10a, which can efficiently convert ginsenoside Rd from Rb1, was obtained through screening survival library of LiCl and ultraviolet (UV) irradiation. The transformation product ginsenoside Rd, generated by removing the outer glucose residue from the position C20 of ginsenoside Rb1, was identified through high-performance liquid chromatography (HPLC) analysis. Factors for the microbial culture and biotransformation were investigated in terms of the carbon sources, the nitrogen sources, pH values, and temperatures. This showed that maximum mycelia growth could be obtained at 28°C and pH 6.0 with cellobiose and tryptone as the carbon source and the nitrogen source, respectively. The highest transformation rate (～86%) has been achieved at 32°C and pH 5.0 with the feeding time of substrate 48 hr. Also, Aspergillus niger strain TH-10a could tolerate even 40 mg/mL ginseng root extract as substrate with 60% bioconversion rate after 72 hr of treatment at the optimal condition. Our results highlight a novel ginsenoside Rd transformation fungus and illuminate its potentially practical application in the pharmaceutical industries.     

Biotransformation of Panax notoginseng saponins into ginsenoside compound K production by Paecilomyces bainier sp. 229

Aims: Development and optimization of an efficient and inexpensive biotransformation process for ginsenoside compound K production by Paecilomyces bainier sp. 229. Methods and Results: We have determined the optimum culture conditions required for the efficient production of ginsenoside compound K by P. bainier sp. 229 via biotransformation of ginseng saponin substrate. The optimal medium constituents were determined to be: 30 g sucrose, 30 g soybean steep powder, 1 g wheat bran powder, 1 g (NH₄)₂SO₄, 2 g MgSO₄·7H₂O and 1 g CaCl₂ in 1 l of distilled water. An inoculum size of 5–7·5% with an optimal pH range of 4·5–5·5 was essential for high yield. Conclusions: The Mol conversion quotient of ginseng saponins increased from 21·2% to 72·7% by optimization of the cultural conditions. Scale‐up in a 10 l fermentor, under conditions of controlled pH and continuous air supply in the optimal medium, resulted in an 82·6% yield of ginsenoside compound K. Significant and Impact of the Study: This is the first report on the optimization of culture conditions for the production of ginsenoside compound K by fungal biotransformation. The degree of conversion is significantly higher than previous reports. Our method describes an inexpensive, rapid and efficient biotransformation system for the production of ginsenoside compound K.     

氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸

3-羟基丙酸是一种潜在的重要化工产品,可作为中间体合成多种有经济价值的工业用化合物。文中利用氧化葡萄糖酸杆菌生物催化1,3-丙二醇合成3-羟基丙酸。首先在50 mL摇瓶中(转化体系为10 mL)考察细胞加入量、底物和产物浓度等对催化反应的影响。在此基础上,在2 L鼓泡塔中(转化体系为1 L),采取适当的补料方式和生物转化与分离相耦合的手段解除抑制,以提高目标产物终浓度。结果表明:高底物和产物浓度通过降低反应初速度抑制转化的进行,并确定了最佳催化反应条件为6 g/L菌体量,pH 5.5。利用流加补料方式维持反应体系中底物浓度在15~20 g/L,经过60 h的反应,3-羟基丙酸的浓度达到60.8 g/L,生产强度为1.0g/(L.h),转化率为84.3%。采用生物转化与分离相耦合的方法,经过50 h的转化反应,3-羟基丙酸的总产量达76.3 g/L,生产强度为1.5 g/(L.h),转化率83.7%。研究结果对利用氧化葡萄糖酸杆菌的不完全氧化醇类化合物特性实现其在工业生物催化中的应用具有一定的指导意义。     

Constitutive production of human leptin by fed-batch culture of recombinant rpoS- Escherichia coli

High-level production of human leptin by fed-batch culture of recombinant Escherichia coli using constitutive promoter system was investigated. For the constitutive expression of the obese gene encoding human leptin, the strong constitutive HCE promoter cloned from the D-amino acid aminotransferase gene of Geobacillus toebii was used. To develop an optimal host-vector system, several different recombinant E. coli strains were compared for leptin production. In flask cultures, E. coli FMJ123, which is a rpoS mutant strain, showed the highest level of leptin production (41% of total proteins). By comparing the expression levels of leptin in several different rpoS- and rpoS+ strains, it could be concluded that rpoS mutation positively affected constitutive production of leptin. For the large-scale production of human leptin, fed-batch cultures of recombinant E. coli FMJ123 were carried out using three different feeding solutions--chemically defined, yeast extract-containing, and casamino acid-containing feeding solutions. Among these, the use of casamino acid-containing feeding solution allowed production of leptin up to 2.1 g/L, which was 2.1- and 1.8-fold higher than that obtained with chemically defined and yeast extract-contained feeding solutions, respectively. These results suggest that the HCE promoter can be used for the efficient production of leptin, and most likely other recombinant proteins, in a constitutive manner.     

以糙米为原料流加L-蛋氨酸的S-腺苷蛋氨酸发酵优化

研究了S-腺苷甲硫氨酸(SAM)高产菌啤酒酵母S-W55的廉价培养基及分批补料发酵过程优化.对啤酒酵母S-W55生长和SAM产量影响最为重要的糙米水解糖和酵母粉进行了响应面优化,得到了最优化的配方为糙米水解糖51.4g/L、酵母粉4.74g/L,此条件下啤酒酵母S-W55的SAM产量达2.61 g/L.不同分批补料发酵...     

Effects of environmental conditions and methanol feeding strategy on lipase-mediated biodiesel production using soybean oil

Methanol is a commonly used acyl acceptor for lipase-driven biodiesel production, but a high concentration of methanol is detrimental for lipase activity. To overcome this drawback, a simple fed-batch process was developed by optimization of the methanol feeding strategy and reaction conditions. For the feeding strategy, an equal volume of pure methanol was fed twice with specified time intervals into a reactor initially containing a 1:1 molar ratio of soybean oil to methanol in order to adjust the net molar ratio of the oil to methanol to 1:3. In contrast with the batch reaction, a higher agitation speed in the fed-batch process elevated the conversion yield of soybean oil to biodiesel. An agitation speed of 600 rpm and a reaction temperature of 70°C were chosen as the optimal environmental conditions. Residual lipase activities for the fed-batch operation at 40 ∼ 70°C and 600 rpm were 7.1 ± 1.4 times higher than that of the batch method at 40°C with the same agitation speed, indicating that methanol feeding can prevent significant deactivation of lipase. Finally, two times feeding methanol at 2 and 6 hr resulted in a biodiesel productivity of 10.7%/h and 94.9% final conversion yield under the optimal conditions.     

Optimization of biphasic growth of Saccharomyces carlsbergensis in fed-batch culture

The optimal glucose feeding policy for the fed-batch culture of Saccharomyces carlsbergensis is presented. The biphasic nature of growth results in a singular feed rate policy that is unique to this organism. When the operating cost is high, the reduction in operating time forces the cells to utilize both glucose and ethanol toward the end of fermentation time and results in a decreasing rate of glucose addition, unlike the normally observed in creasing feed rate. The optimal feeding policy depends heavily on the initial conditions and is highly sensitive to changes in kinetic parameters. A semiempirical scheme for feedback optimization is suggested for the fed-batch yeast culture.     

Feasibility study of exponential feeding strategy in fed-batch cultures for phenol degradation using Cupriavidus taiwanensis

An indigenous phenol-degrading bacterial isolate Cupriavidus taiwanensis R186 was used to degrade phenol from an aqueous solution under fed-batch operation. An exponential feeding strategy combined with dissolved oxygen control was applied based on kinetic characteristics of cell growth and phenol degradation to meet sufficient metabolic needs for cellular growth and achieve the best phenol removal efficiency. Without the stress of phenol inhibition, the optimal set point of specific growth rate of exponential feeding for fed-batch phenol degradation was found to be 0.50–0.55μ_max (μ_max denotes the maximum specific growth rate from Monod model). Meanwhile, the sufficient set point of dissolved oxygen for maximal phenol degradation efficiency was approximately at 10–55% air saturation. With the optimal operation conditions, the best phenol degradation rate was 0.213 g phenol h⁻¹, while a shortest treatment time of 15 h was achieved for complete degradation of 11.35 mM (ca. 3.20 g) of phenol.