阳离子交换树脂二次纯化紫甘薯花色苷的研究

采用阳离子交换树脂二次纯化紫甘薯花色苷。以紫甘薯花色苷的吸附率,解吸率和花色苷含量等为考察指标,确定了阳离子交换树脂二次纯化紫甘薯花色苷的工艺条件。研究结果表明,D061树脂对紫甘薯花色苷的吸附量大,解吸容易,可用于二次纯化紫甘薯花色苷的工业化生产,其工艺条件为:上样液的pH值为2.6,上样液吸光度值在0.6×100左右,上样流速为1.0BV/h,50%乙醇(含2%盐酸)为洗脱液,洗脱流速为0.5BV/h,用此工艺条件D061树脂吸附花色苷的吸附量为10.5mg/g,洗脱剂用量为3.0BV,花色苷的收率为82.99%。二次纯化后,紫甘薯花色苷的花色苷含量达到29.38%,色价高达136.80。     

大孔吸附树脂分离纯化枳实中辛弗林的研究

以辛弗林的吸附量、解吸率和所得粉末中辛弗林的含量为指标,从选用的6种大孔吸附树脂中筛选出较好的AB-8树脂。通过静态和动态实验,对辛弗林在AB-8树脂上吸附和解吸的条件进行优化,并考察其吸附等温线、吸附和解吸性能。结果表明,在环境温度约25℃下,使用AB-8树脂纯化辛弗林的较优工艺参数为:上柱液pH值7～8,流速2BV/h,溶液处理量3BV,洗脱剂为20%乙醇,洗脱速度1BV/h,收集洗脱液3BV。按此工艺条件,辛弗林的解吸率为87.2%,3BV洗脱液浓缩干燥后,所得粉末中辛弗林含量为56.6%。     

大孔吸附树脂分离提取多杀菌素

采用大孔吸附树脂法分离提取多杀菌素.从11种大孔吸附树脂中筛选出DM11进行了静态、动态吸附性能实验,并考察了不同吸附、解吸条件的影响.结果表明,DM11的静态吸附容量为25.63mg/g(wet resin),其吸附等温线符合Langmuir吸附等温式.采用丙酮做洗脱剂,洗脱率为97.5%,动态吸附最佳吸附pH为9.5,吸附流速为6BV/h,穿透吸附容量为21.2mg/ml(wet resin),洗脱流速1.5BV/h.     

大孔吸附树脂分离纯化迷迭香酸的研究

采用大孔吸附树脂法研究迷迭香酸的精制工艺。筛选出适合的大孔吸附树脂,并对其分离纯化的条件进行考察。使用静态吸附法确定大孔吸附树脂NK109最适于迷迭香酸的精制。通过动态吸附性能的考察,确定最佳迷迭香酸上柱浓度838.6mg/L,流速为2.0BV/h上柱。通过动态解吸性能的考察,使用乙酸乙酯作为洗脱液,确定洗脱速度为1.0BV/h。利用大孔吸附树脂,迷迭香酸得到了较好的富集和纯化。纯化后的迷迭香酸纯度可以达到90%以上。     

大孔吸附树脂对莲房原花青素吸附纯化性能的研究

比较了14种大孔吸附树脂对莲房中原花青素(proanthocyanidins of lotus seedpod,LSPAs)的吸附及解吸性能,在研究静态吸附的基础上,筛选出效果较好的树脂进行动态实验研究,并对所得组分LSPAs含量及其相对分子量进行初步分析.结果表明,DM130大孔吸附树脂分离纯化LSPAs效果最佳,上样浓度为2.5mg/mL,流速为3BV/h时,饱和吸附量为4～4.5个BV;当用体积分数为50%乙醇以3BV/h的流速洗脱5BV时,LSPAs的累积回收率可达96.43%,含量从22.54%提高到95.31%;经质谱分析,(M+H)分子量范围为291.1～1155.3,聚合度≤4.     

XAD-16树脂分离纯化怀菊花黄酮的工艺研究

研究XAD-16树脂分离纯化怀菊花黄酮的工艺,探讨了吸附过程中树脂的等温吸附与吸附动力学,并应用Langmuir方程与Freundlich方程对吸附过程进行了拟合。确定了XAD-16树脂分离怀菊花黄酮的最佳工艺条件:上样浓度2.0mg/mL,上样流速1BV/h,冲洗杂质用水量11BV,洗脱剂为85%(体积分数)乙醇,洗脱流速2BV/h,洗脱剂体积5BV。此时总黄酮的解吸率为83.9%。在此条件下,经过XAD-16树脂分离纯化后,怀菊花总黄酮含量达到77.2%。     

大孔树脂分离纯化藏药白花龙胆花总黄酮的研究

考察了HPD-826、HPD-417、ADS-17、HPD-722、HPD-450、AB-8、HPD-600、D-101,共8种大孔树脂对藏药白花龙胆花总黄酮的吸附和解吸性能,通过静态吸附量和解吸附率及静态吸附曲线的绘制,筛选出AB-8树脂的效果最佳;以AB-8树脂为目标,进行了动态吸附实验,考察了上柱液浓度、pH值、上柱液流速、乙醇浓度、解吸剂流速、解吸体积等对AB-8树脂吸附和解吸效果的影响,确定出AB-8树脂动态吸附白花龙胆花总黄酮的最佳条件:上柱液浓度为6.5mg/mL,pH为3.79,上柱流速4BV/h;最佳洗脱条件:用50%乙醇进行洗脱,解吸流速为3BV/h,解吸体积4BV。在此条件下,白花龙胆花总黄酮纯度由原来的22.10%,变为65.75%,产品精制倍数为65.75%/22.10%=2.97,表明AB-8树脂可用于白花龙胆花总黄酮的分离纯化。     

大孔弱酸树脂对妥布霉素纯化的工艺研究

工业生产中妥布霉素发酵液粗提物的纯度只能达到50~60%,通常采用强酸树脂进行纯化,但纯化纯度很难达到国家药典要求。本文比较了5种阳离子交换树脂对妥布霉素的吸附性能,利用静态吸附与动态吸附实验优选出了大孔弱酸树脂HZ-3B,并对其纯化妥布霉素工艺进行了进一步的优化:选用浓度为5mg/m L,pH值为6.8~7.2的妥布霉素溶液以9BV/h的流速进行上样,上样200BV;然后利用0.125mol/L的氨水溶液作为解吸液,以6BV/h的流速进行解吸,合并解吸液。HPLC分析结果显示,妥布霉素纯度由50~60%提升到了97.15%,收率为89.52%,且无其他氨基糖苷类抗生素杂质,达到了国家药典的要求。     

杜仲叶中绿原酸提取分离工艺条件的研究

对杜仲叶绿原酸的提取分离进行研究.探讨了水以及不同浓度乙醇、甲醇和丙酮水溶液作为提取溶剂对绿原酸得率的影响,采用正交实验方法对影响绿原酸提取率的主要因素进行分析,并采用大孔树脂对其分离.结果表明,50℃水提绿原酸得率比较高,其得率为1.06%,从而确定水作为绿原酸提取溶剂;水提杜仲叶绿原酸的最佳工艺条件为:温度60℃,料液比1∶16,pH4,提取时间3h,所筛选的GC-I树脂是吸附分离绿原酸的最佳吸附剂,吸附最佳pH值为3,吸附流速为3BV/h;本实验条件下得到粗产品纯度为30.88%,收率为76.51%.     

大孔树脂纯化脱油油樟叶渣中总黄酮工艺研究

本研究以从脱油油樟叶渣中提取出的总黄酮粗提液为原料,采取静态吸附-解吸实验对5种大孔树脂进行筛选,选取最佳型号的大孔树脂AB-8进行实验,通过单因素试验选择出最佳纯化工艺条件。研究结果表明,最佳吸附和解吸条件:避光振摇下吸附时间为10h,避光振摇下解吸附时间为6h,样品溶液的pH值为5,洗脱液乙醇溶液浓度为80%,上样液中总黄酮浓度为0.5mg/mL,上样量为2.5BV,洗脱流速为1mL/min,洗脱量为2.5BV;在最佳条件下得到脱油油樟叶渣中总黄酮质量分数为(72.4±0.5)%。该方法简单可行,为脱油油樟叶渣中总黄酮的开发利用提供了技术参考与借鉴。     

大孔吸附树脂分离纯化异甘草素的研究

研究大孔吸附树脂分离纯化异甘草素的工艺条件及参数。通过研究HPD-600、D4020、D101、AB-8、NKA-II、AL-2和NKA-9树脂对异甘草素的吸附和解吸附能力,筛选最佳树脂为AB-8,并研究了其对异甘草素的吸附和解吸附性能,确定了最佳的吸附与解吸附工艺参数,吸附:pH=5,室温,流速1.5BV/h,溶液处理量为5BV;脱附:洗脱剂为70%的乙醇溶液,流速1BV/h,洗脱剂用量4.5BV。异甘草素样品溶液经AB-8树脂吸附与脱附后回收率为76.7%,纯度由2.02%提高到29.1%,提高了14.4倍。实验结果表明,AB-8树脂对异甘草素的吸附量大,脱附容易,可以应用于异甘草素的分离纯化。     

Optimization of luteolin separation from pigeonpea [Cajanus cajan (L.) Millsp.] leaves by macroporous resins

In the present study, the performance and separation characteristics of eight macroporous resins for the separation of luteolin (LU) from pigeonpea leaves extracts have been evaluated. The adsorption and desorption properties of LU on macroporous resins including AB-8, NKA-9, NKA-2, D3520, D101, H1020, H103 and AL-2 have been compared. AL-2 resin offers the best adsorption and desorption capacity for LU than other resins based on the research results, and its adsorption data at 25 degrees C fit best to the Freundlich isotherm. Dynamic adsorption and desorption experiments have been carried out with the column packed by AL-2 resin to optimize the separation process of LU from pigeonpea leaves extracts. The optimum parameters for adsorption were sample solution LU concentration 65.5 microg/ml, pH 5, processing volume 3 BV, flow rate 1.5BV/h, temperature 25 degrees C; for desorption were elution solvent ethanol-water (50:50, v/v) 2 BV and followed by ethanol-water (60:40, v/v) 2 BV, and flow rate 1BV/h. After treated with AL-2 resin, the LU content in the product was increased 19.8-fold from 0.129% to 2.55%, with a recovery yield of 78.54%. The results showed that AL-2 resin revealed a good ability to separate LU. Therefore, we conclude that results in this study may provide scientific references for the large-scale LU production from pigeonpea or other plants extracts.     

Separation of injectable salidroside by column chromatography of macroporous resins for treating myocardial ischemia

The objective of the present study is to develop a method for large-scale separating and purifying salidroside from rhodiola kirilowii roots and for preparing injectable medicinal ingredient.Crude extract of salidroside was prepared by water-ethanol system,and purified by column chromatography of macroporous resins.Static adsorption and desorption studies were performed on six kinds of macroporous resins,and SP825 resin was chosen,followed by optimizing process parameters.The optimum sample volume,feed concentration,ratio of diameter to height,and feeding flow rate were 1.5 bed volumes(BV),15 mg/mL,1:10 and 1 BV/h,respectively.Dynamic desorption was performed consecutively with 8 BV of distilled water,3 BV of 5% ethanol and 8 BV of 10% ethanol at a flow rate of 2 BV/h.After three cycles in separating 3.5 tons of rhodiola kirilowii roots,salidroside purity was increased from 3.4% in the crude extract to 93.6% in purified salidroside product.This study provides a novel method to separate salidroside for injectable use.     

Separation and purification of flavonoid from Taxus remainder extracts free of taxoids using polystyrene and polyamide resin

An efficient separation process of flavonoid from Taxus wallichiana var. mairei remainder extracts free of taxoids was developed in this study. AB‐8 macroporous resin and polyamide resin offered the fine adsorption capacity, and its adsorption rate at 30°C fitted well to the Langmuir and Freundich isotherms. Resin dynamic adsorption and desorption experiments were conducted to optimize the separation process of total flavonoids from T. wallichiana var. mairei remainder extracts free of taxoids. The optimum parameters for adsorption by AB‐8 resin were as follows: (1) the concentration of flavonoids in a sample solution of 5.61 mg/mL with a processing volume of 2 bed volume (BV) (60 mL); (2) for desorption, ethanol–water (80:20, v/v), with 6 BV as an eluent at a flow rate of 2 BV/h. After a one‐run treatment with AB‐8 resin, the content of flavonoids was increased 5.10‐fold from 4.05 to 20.65%. The optimum parameters for adsorption by polyamide resin were as follows: processing volume of 2 BV (30 mL); for desorption, ethanol–water (70:30, v/v), with 8 BV as an eluent at a flow rate of 2 BV/h. After one‐run treatment with polyamide resin, the content of total flavonoids increased from 20.65 to 65.21%. The method will provide a potential approach for large‐scale separation and purification of flavonoid for its wide pharmaceutical use.     

离子交换法从发酵液中提取L-亮氨酸

用离子交换法提取发酵液中的L-亮氨酸,比较了不同型号的强酸性阳离子树脂对L-亮氨酸的静态吸附量和吸附动力学,其中以WA-2型树脂对L-亮氨酸吸附量最大、吸附速度快,适于L-亮氨酸的提取.测定了WA-2型树脂对L-亮氨酸的吸附等温线,并回归得到Freundlich方程.考察了固定床操作工艺条件,结果表明:发酵液经预处理后,以1BV/h流速上柱吸附,上柱量为2BV;再用0.3mol/L的氨水洗脱,速度为1BV/h,洗脱效果较好,L-亮氨酸回收率达到95.7%.提取过程中WA-2型树脂不会受到不可逆的污染,也没有机械损坏,其使用寿命不受影响.     

Enrichment and purification of deoxyschizandrin and γ-schizandrin from the extract of Schisandra chinensis fruit by macroporous resins

In present study, the performance and separation characteristics of 21 macroporous resins for the enrichment and purification of deoxyschizandrin and γ-schizandrin, the two major lignans from Schisandra chinensis extracts, were evaluated. According to our results, HPD5000, which adsorbs by the molecular tiers model, was the best macroporous resin, offering higher adsorption and desorption capacities and higher adsorption speed for deoxyschizandrin and γ-schizandrin than other resins. Columns packed with HPD5000 resin were used to perform dynamic adsorption and desorption tests to optimize the technical parameters of the separation process. The results showed that the best adsorption time is 4 h, the rate of adsorption is 0.85 mL/min (4 BV/h) and the rate of desorption is 0.43 mL/min (2 BV/h). After elution with 90% ethanol, the purity of deoxy-schizandrin increased 12.62-fold from 0.37% to 4.67%, the purity of γ-schizandrin increased 15.8-fold from 0.65% to 10.27%, and the recovery rate was more than 80%.     

茶碱印迹酚醛吸附树脂的研究

采用反相悬浮聚合技术,合成了茶碱模板酚醛吸附树脂和非模板酚醛吸附树脂,比较了两种树脂对茶碱的吸附状况.结果表明.对茶碱的吸附数据符合Langmuir方程,吸附属于单分子层吸附.在一定浓度范围内的吸附数据符合Freundlich方程,表明吸附是优惠吸附.Scatchard分析表明茶碱模板酚醛树脂具有特定的高亲和性吸附位点...     

酚醛型吸附树脂对VB_(12)的吸附性能研究

研究了酚醛型吸附树脂JDW 1、JDW 2 (自制 )和DuoliteS 76 1对VB12 的静态和动态吸附 .结果表明 ,JDW 1对VB12 的吸附量达 84mg g ,明显优于DuoliteS 76 1;吸附VB12 的初始阶段 ,即达到 4 3%～6 9%平衡吸附时 ,吸附速率数据和半经验速率方程很吻合 ;酚醛型吸附树脂等温吸附VB12 的平衡吸附数据符合Langmuir方程 ,相关系数在 0 99以上 ,因此 ,酚醛型吸附树脂吸附VB12 属单分子层吸附 ;在动态条件下 ,用含甲醇 80 %溶液以 1 1BV h来洗脱吸附VB12 的JDW 2 ,在 4 2、6 4个床体积的洗脱率分别是 92 2 0 %、95 93% ,这表明酚醛型吸附树脂具有良好的洗脱性能 ,用含甲醇为 80 %溶液作洗脱剂从JDW 2洗脱VB12 ,效果很好     

离子交换法从发酵液中提取聚苹果酸

用离子交换法提取发酵液中的聚苹果酸,比较了不同型号的阴离子树脂对聚苹果酸的静态吸附量,其中以D296树脂对聚苹果酸的吸附量最大.通过静态和动态方法,考察了不同操作条件对固定床分离工艺的影响.结果表明,发酵液经预处理后,调pH至9.5,以lBV/h流速上柱吸附,上柱量为4BV;用0.5mol/L NaCl洗脱,速度为1BV/h.该工艺能够将发酵液中大部分杂质去除,PMLA样品的纯度达到 93.2%,提取收率为79.46%.