L-色氨酸的生产方法

专利要求的范围 用节杆菌属(?一丈。,夕夕一)中对一种或二种以上的色氨酸类似物具有抗性的LO色氨酸产生菌,在培养液中积累色氨酸,并从该培养液中提取L一色氨酸的发酵生产法。 本发明详细池叙述了节杆菌属中的L一色氨酸生产菌,通过培养,从发酵液中分离、回收L一色氨酸的方法,由于采用了生成L一色氨酸能力高的菌株,所以使必须氨基酸中的L-色氨酸达到了兼价工业生产的要求。 过去发酵法生产L一色氨酸,采用的是在培养基中添加叫噪或邻氨基苯甲酸的方法,此法因必须采用高价的引噪或邻氨基苯甲酸作前休物质,使色氨酸的生产存在着成本高的缺点…     

二阶导数光谱测定复合氨基酸注射液中的L-色氨酸和L-苯丙氨酸的含量

<正> 导数光谱法是解决光谱重叠和光谱干扰的新方法,操作简便。复合氨基酸注射液是含有11种氨基酸及甘露醇的一种复方制剂。用氨基酸分析仪测定时,未能测出L—色氨酸,而测出L—苯丙氨酸数值偏高,如果采用比色法测定L—包氨酸,操作繁复,准确度较差。由于11种氨基酸仅L—色氨酸和L—丙氨酸具有特征吸收光谱,     

发酵液中 L-色氨酸的提取

L-色氨酸为必需氨基酸之一,在人体代谢有着重要的功用,是配制复合结晶氨基酸注射液的基本原料,其价格昂贵,国内尚供不应求。至今,除用化学合成生产色氨酸外,利用微生物发酵法生产 L-色氨酸已越来越受到人们的重视,国内外均有不少研究报告。根据中国科学院微生物研究所的研究报告,我们于1976年采用邻氨基苯甲酸为前体物发酵法,协作进行了 L-色氨酸的试制工作。当时,由于受到强烈地震的影响,试制工作未能园满结束,但在克服重重困难之后,仍然摸索了一     

改造后的大肠杆菌氨基酸产量可望成倍增长

应用遗传工程学技术又获可喜成果。主要研究氨基酸、色氨酸生产方法的大阪大学工程学部的发酵工程数研室(合叶修一教授)研究小组,用大肠杆菌产生色氨酸研究成功。产生色氨酸的量是当代所采用的发酵法的两倍。 大肠杆菌以葡萄糖为原料,经过五种酶的复杂的连续地反应可以合成色氨酸。在一     

改造后的大肠杆菌氨基酸产量可望成倍增长

应用遗传工程学技术又获可喜成果。主要研究氨基酸、色氨酸生产方法的大阪大学工程学部的发酵工程数研室(合叶修一教授)研究小组,用大肠杆菌产生色氨酸研究成功。产生色氨酸的量是当代所采用的发酵法的两倍。 大肠杆菌以葡萄糖为原料,经过五种酶的复杂的连续地反应可以合成色氨酸。在一     

微生物发酵法生产L-色氨酸的代谢工程研究

L-色氨酸作为人体内的一种必需氨基酸,广泛应用于医药、食品与饲料等行业.工业上采用的色氨酸生产方法有化学合成法、转化法及微生物发酵法.近年来,随着代谢工程在色氨酸菌种选育中的成功运用,微生物发酵法逐渐成为主要的色氨酸生产方法.系统综述了微生物发酵法生产色氨酸所涉及的代谢工程策略,包括生物合成色氨酸的代谢调控机制以及途径...     

利用蚕蛹生产复合氨基酸营养物的研究——树脂法对酶介液中蚕蛹脱臭的研究

本文报导了用离子交换树脂法脱除蚕蛹酶解存在的蚕蛹本身的恶臭;用胰酶进行蚕蛹分解,酶解后经732树脂脱臭,获得无臭、黄色粉末的混合氨基酸,对蛋白质的收率达44%以上,保留了人体必需的色氨酸,弥补了蚕蛹酸解色氨酸被破坏的缺陷,符合要素膳对氨基酸的质量要求,从而可利用蚕蛹生产营养价值高的混合氨基酸。     

L-色氨酸对肝脏合成和酶诱导的作用

<正> 肝脏蛋白质合成及多核蛋白体聚集色氨酸是哺乳动物肝脏蛋白质中含量比较低的一种氨基酸。色氨酸在转录水平调节肝脏蛋白质合成。特别因饥饿不能合成蛋白质时,色氨酸就显得更为重要。Feigelson等观察到喂大白鼠色氨酸,肝脏合成蛋白质的速度加快,食物中没有色氨酸,氨基酸掺入蛋白质减少略喂大白鼠完全的混合氨基酸(即含有各种氨基酸),色氨酸在5-10分钟之内到达肝脏,并促进肝脏蛋白质合成。当肝脏中色氨酸的浓度比较高时,色氨酸促进蛋白质合成的作用就     

稻米色氨酸测定方法的改进

<正> 色氨酸是动物和人体中八种必需氨基酸之一,它对人和动物的生长发育、新陈代谢起着重要的作用,被称为第二必需氨基酸。目前测定蛋白质的氨基酸多采用氨基酸分析仪及气相色谱法测定其水解产物,这种方法需要昂贵的仪器,且在水解过程中色氨酸完全被破坏,尤其是象水稻这些含碳水化合物高的粮食作物,水解时即使采取了添加保护剂的办法,色氨酸的破坏仍是严重的,     

生物样品中色氨酸荧光测定法的改进

<正> 色氨酸是必需氨基酸之一,也是普遍食物中或日常膳食的主要限制氨基酸,食品中色氨酸的含量是评价其营养价值的重要指标。色氨酸对酸不稳定,当用酸水解蛋白质时,往往被破坏,所以不能用氨基酸分析仪按一般程序和其他氨基酸同时被分析定量,     

发酵液中L-色氨酸分离纯化工艺研究

通过静态吸附实验,考察了温度、pH值对001×7阳离子交换树脂平衡吸附量的影响,并测定了吸附动力学曲线。通过动态实验,测定了动态吸附曲线和洗脱曲线。最后确定了001×7阳离子交换树脂分离纯化L-色氨酸的最佳工艺条件:用001×7阳离子交换树脂吸附L-色氨酸,以浓度为2 mol.L-1氨水进行洗脱,收集的流份经D315阴离子交换树脂脱色,浓缩结晶后得L-色氨酸成品,总提取率为73.0%。     

The distribution of blood flow to the reproductive organs of rats near term.

The rate of ovarian and utero-placental blood flow through vessels of less than 25 mum diameter was examined with radioactive microspheres in 5 non-pregnant rats and 19 rats at Day 22 of pregnancy. Total blood flow to the reproductive organs was 0-559 ml/min in the non-pregnant animals and 13-2 ml/min in those near term, a 23-fold difference. The mean ovarian blood flow was high and increased from 0-202 ml/min to 0-845 ml/min. Myometrial and endometrial blood flow increased from 0-156 to 2-24 ml/min. The mean maternal placental blood flow at Day 22 of pregnancy was 0-76 ml/min or 121 ml.,min-1 .100 g-1. Litter size was negatively correlated with mean fetal weight but showed little relationship to mean placental weight or to mean maternal placental blood flow.     

AB-8大孔树脂吸附分离红花桑寄生总黄酮的影响因子研究

AB-8大孔吸附树脂对红花桑寄生总黄酮静态吸附和动态洗脱的效果,受提取液质量浓度、pH值及环境温度、振速以及洗脱剂乙醇浓度、流速等因素影响。试验表明,提取液质量浓度和pH值对AB-8树脂的吸附效果有显著影响,其吸附分离总黄酮的工艺条件为:浓度为1.2~2.0 mg/ml、pH 3.0~4.0的红花桑寄生提取液,置于摇床上,于室温条件下振荡(振速160 r/min)吸附2~3 h,然后用5倍于树脂体积(5BV)的50%乙醇以1.5 ml/min流速进行柱上动态解吸。AB-8树脂对红花桑寄生总黄酮的饱和吸附量可达29.0 mg/g,动态洗脱率达95.0%,获得产品中黄酮纯度为46.0%,得率为5.5%。     

从火棘果中提取精氨酸的研究

以天然野生植物火棘果为原料分离提取精氨酸,考察了树脂类型、吸附方式、温度、pH值、洗脱液、脱色及精制方法等因素对提取精氨酸的影响,并对产物进行了分析鉴定。结果表明,在20℃、pH值7-8的条件下,选用D001型大孔阳离子交换树脂静态吸附,40 min即达到饱和;以3 mol.L-1氨水为洗脱液,流速控制在40 mL.h-1,精氨酸的洗脱率达到90%以上;采用711型阴离子树脂进行脱色,D001型大孔阳离子交换树脂动态精制,精氨酸的提取率达到95.83%。     

Continuous adsorption and recovery of Cr(VI) in different types of reactors

This study reports the results of experiments on continuous adsorption and desorption of Cr(VI) ions by a chemically modified and polysulfone-immobilized biomass of the fungus Rhizopus nigricans. A fixed quantity of polymer-entrapped biomass beads corresponding to 2 g of dry biomass powder was employed in packed bed, fluidized bed, and stirred tank reactor for monitoring the continuous removal and recovery of Cr(VI) ions from aqueous solution and synthetic chrome plating effluent. Parameters such as flow rate (5, 10 and 15 mL/min), inlet concentration of Cr(VI) ions (50, 100, 150 and 250 mg/L) and the depth of biosorbent packing (22.8, 11.2 and 4.9 cm) were evaluated for the packed bed reactor. The breakthrough time and the adsorption rates in the packed bed column were found to decrease with increasing flow rate and higher Cr inlet concentrations and to increase with higher depths of sorbent packing. To have a comparative analysis of Cr adsorption efficiency in different types of reactors, the fluidized bed reactor and stirred tank reactor were operated using the same quantities of biosorbent material. For the fluidized bed reactor, Cr(VI) solution of 100 mg/L was pumped at 5 mL/min and fluidized by compressed air at a flow rate of 0.5 kg/cm.(2) The stirred tank reactor had a working volume of 200 mL capacity and the inlet/outlet flow rate was 5 mL/min. The maximum removal efficiency (mg Cr/g biomass) was obtained for the stirred tank reactor (159.26), followed by the fluidized reactor (153.04) and packed bed reactor (123.33). In comparison to the adsorption rate from pure chromate solution, approximately 16% reduction was monitored for synthetic chrome plating effluent in the packed bed. Continuous desorption of bound Cr ions from the reactors was effective with 0.01 N Na(2)CO(3) and nearly 80-94% recoveries have been obtained for all the reactors.     

Isolation of L-theanine from tea solution by cation exchange resin in batch and fixed bed column

L-Theanine, a bioactive compound in tea, was isolated from tea solution using cation exchange resin no.732. The adsorption of L-theanine by cation exchange resin no.732 fit the Langmuir isotherm model and was a monolayer molecular interaction process. Thermodynamic studies revealed that the adsorption of L-theanine by resin no.732 was an exothermic and spontaneous physically driven process. The adsorption capacity was influenced by temperature, initial concentration, and pH. The L-theanine adsorption capacity under conditions at room temperature, pH 4.73, and initial L-theanine concentration 18 g/L was 241.731 ± 3.679 mg/g. The Thomas model was fit to describe the column adsorption data at different flow rates and initial concentrations. The L-theanine adsorbed by resin no.732 could be desorbed by 0.134 mol/L Na₂HPO₄ aqueous solution with a recovery rate of 84.96%. These findings indicate that resin no.732 was a promising material for isolating L-theanine from tea solution.     

Arterial perfusion of frog tongue for intracellular recording of taste cell receptor potential

The frog tongue was perfused through its artery with a Ringer solution using a peristaltic pump, and a method was developed to record stable intracellular receptor potentials of taste cells. Perfusing at 0.05 ml/min with a Ringer solution containing 5% dextran did not cause tongue edema, but perfusing at the same rate with Ringer without dextran caused edema. After perfusion at 0.05 ml/min with 100 mM K Ringer, the membrane potential of taste cells gradually decreased and reached a constant level in about 30 min, indicating that the intercellular fluid of the tongue could be replaced within this time period. While the artery of the frog tongue was perfused at 0.05 ml/min with Ringer containing 5% dextran, intracellular receptor potentials of taste cells elicited by four basic taste stimuli (1 M NaCl, 10 mM quinine-HCl (Q-HCl), 1 mM acetic acid and 1 M galactose) were similar to those obtained from the control taste cells under normal blood flow.     

AB-8大孔树脂纯化欧洲鳞毛蕨总黄酮的研究

目的:对AB-8大孔吸附树脂对欧洲鳞毛蕨总黄酮的纯化工艺条件进行了系统的研究。方法:采用静态和动态的吸附-解吸实验,利用紫外可见分光光度计测量欧洲鳞毛蕨总黄酮的含量,研究不同的工艺条件对总黄酮纯化的影响。结果:AB-8大孔树脂对欧洲鳞毛蕨总黄酮的饱和吸附量是25.53mg/g,洗脱率达到98.3%,提取液的pH值对树脂的吸附能力有很大的影响,当pH值为4.08(原液pH值)时树脂吸附能力达到最大。采用0.5mg/mL流速上样,1.2BV 30%和1BV 50%乙醇1.0 mg/mL流速洗脱可较好的分离纯化欧洲鳞毛蕨总黄酮。结论:AB-8大孔树脂是欧洲鳞毛蕨总黄酮纯化的理想吸附剂。     

Breakthrough performance of linear-DNA on ion-exchange membrane columns

Breakthrough performance of linear-DNA adsorption on ion-exchange membrane columns was theoretically and experimentally investigated using batch and fixed-bed systems. System dispersion curves showed the absence of flow non-idealities in the experimental arrangement. Breakthrough curves were not significantly affected by flow-rate or inlet solution concentration. In the theoretical analysis a model was integrated by the serial coupling of the membrane transport model and the system dispersion model. A transport model that considers finite kinetic rate and column dispersed flow was used in the study. A simplex optimization routine coupled to the solution of the partial differential model equations was employed to estimate the maximum adsorption capacity constant, the equilibrium desorption constant and the forward interaction rate-constant, which are the parameters of the membrane transport model. Through this approach a good prediction of the adsorption phenomena is obtained for inlet concentrations and flow rates greater than 0.2 mg/ml and 0.16 ml/min.     

Improvement of renal preservation by adding lidoflazine to University of Wisconsin solution. An experimental study in the rat.

The purpose of this study was to investigate the possibility of improving the organ preservation properties of the University of Wisconsin (UW) solution by adding the calcium entry blocker lidoflazine. We also investigated the possibility of decreasing the cold ischemia and reperfusion damage by pretreatment with lidoflazine of the donor and/or recipient. The protective effects of lidoflazine treatment were estimated by measuring the amount of trapped erythrocytes in the rat renal medulla after 48 h of cold storage, subsequent transplantation, and 20 min of reperfusion. Lidoflazine (20 mg/liter) added to the UW solution decreased the amount of erythrocyte trapping from 14.8 +/- 3.1% in controls to 8.6 +/- 1.7% (P less than 0.01). The flow rate of the flush-out solution during the harvesting procedure was also significantly (P less than 0.01) increased when lidoflazine was included in the UW solution (1.10 +/- 0.21 ml/min vs 0.75 +/- 0.22 ml/min). Administration of lidoflazine (0.28 mg/kg body wt) to the donor and/or the recipient did not further reduce the postischemia/reperfusion damage as estimated by the degree of erythrocyte trapping. In conclusion, the results indicate that the preservation properties of the UW solution can be significantly improved by adding lidoflazine to the solution.