大孔吸附树脂对酯型儿茶素吸附性能的研究

系统研究了AB-8,PA,HPD600,NKA-9,NKA-II等5种大孔吸附树脂对EGCG的吸附性能。结果表明,这5种大孔吸附树脂对EGCG的吸附效率随AB-8,PA,HPD600,NKA-9,NKA-II的顺序依次减小。选择大孔吸附树脂PA为吸附剂,用PA对EGCG、ECG、GCG进行静态和动态吸附实验以及解吸剂的选择实验,研究了吸附速率曲线,确定了最佳吸附流速,根据解吸效果和绿色提取的需要,决定选用无毒有机溶剂C作为解脱剂。     

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。     

基于大孔树脂与制备液相色谱技术快速分离野地瓜茎中的绿原酸

建立了基于大孔吸附树脂快速富集,制备高效液相色谱高效分离野地瓜茎中绿原酸的制备方法:AB-8,D101,HPD600,CN206和NKA-Ⅱ5种树脂中,经静态吸附-解吸附试验发现NKA-Ⅱ型大孔树脂对目标化合物具有较好的吸附率和解析率;采用NKA-Ⅱ型大孔树脂,经4倍柱体积(bed volume,BV)5%(V/V)乙醇除杂后,用7 BV 10%(V/V)乙醇洗脱得到目标化合物组分,HPLC分析目标化合物的峰面积比达到80.8%;由制备高效液相色谱对目标化合物做进一步纯化并开发了重复进样分离模式,提高了分离效率,经纯化后目标化合物纯度达到98.6%;1H NM R和13C NM R鉴定目标化合物为绿原酸。该方法适合于野地瓜中绿原酸化合物的大规模制备。     

大孔树脂分离纯化丹酚酸的研究

比较了D301R、D392、D380大孔阴离子交换树脂和X-5.AB-8、NKA-9、SP825大孔吸附树脂对丹参水溶性成分的吸附和解吸能力,筛选出效果较好的SP825进行分离纯化丹酚酸的研究.实验表明,大孔吸附树脂SP825能分离出纯度为95.32%的丹参素,在梯度洗脱条件下可得到以丹参素(水洗脱)和丹酚酸B(乙醇洗脱)为主的产品.在最佳吸附与解吸工艺参数下,丹参素、紫草酸、迷迭香酸、丹酚酸A和丹酚酸B的收率分别为:36.92%、80.39%、82.45%、43.07%和41.03%.     

大孔树脂分离纯化宁夏枸杞总黄酮的研究

考察了NKA-9、S-8、XDA-1、AB-8、HPD-100、HPD-600 6种大孔吸附树脂对宁夏枸杞总黄酮的吸附和解吸性能,筛选出XDA-1树脂的效果最佳;考察了pH值、样液浓度、流速等对XDA-1树脂静态吸附效果的影响;并进行了动态吸附试验,确定出XDA-1树脂动态吸附枸杞总黄酮的最佳条件:样品液浓度为0.25mg/mL,控制流速为0.5mL/min,样品液pH 5;最佳洗脱条件:洗脱液为80%的乙醇水溶液,用量为35mL (5倍柱床体积).在此条件下,枸杞总黄酮含量从27.2%提高到79.8%,回收率为87.4%,表明XDA-1树脂可用于宁夏枸杞总黄酮的分离纯化.     

大孔吸附树脂分离纯化金银花中黄酮类物质的研究

比较了AB-8、S-8、NKA-9和D-101 4种大孔吸附树脂对金银花提取液中黄酮类物质的吸附及解吸附性能.在静态吸附试验基础上,筛选出效果较好的D-101树脂进行动态试验研究,结果表明,D-101树脂在30℃下对金银花黄酮类物质的静态吸附-动态解吸较优的工艺参数为:上样液pH值2.46,解吸液为95%乙醇,解吸液的流速为3mL/min,pH值11,4.5BV解吸液即可完全洗脱被树脂吸附的黄酮类物质,其解吸率高达98.00%.在试验研究范围内,树脂吸附金银花黄酮是自发性放热过程,并且符合Langmuir方程,此外树脂对黄酮的吸附动力学可用Pseudo-second-order模型较好地拟合,其表观吸附速率常数为Kso℃=3.43×10-2g/(mg·min).     

吸附树脂分离纯化枇杷花总黄酮的研究

比较了D-101、D-160、AB-8、NKA-9和聚酰胺等5种吸附树脂对枇杷花总黄酮的吸附及解吸附性能。在静态吸附和动态吸附实验基础上,筛选出效果较好的AB-8树脂进行动态吸附参数的研究。考察了样品液pH值、样品液浓度、洗脱液浓度、上样速度、洗脱速度等对AB-8树脂吸附和解吸效果的影响,确定了AB-8树脂动态吸附枇杷花总黄酮的最佳条件。获得的最佳纯化条件如下,样品液pH值为5.5,样品液浓度为12mg/mL,洗脱液为30%的乙醇水溶液,上样速度为2BV/h,洗脱速度为1BV/h。纯化后样品总黄酮含量达86.7%,比纯化前总黄酮含量高5~6倍。实验结果表明,AB-8树脂可用于分离纯化枇杷花总黄酮。     

大孔吸附树脂分离纯化金银花绿原酸研究

以金银花粗提物为原料,比较了NKA-2、D1400、聚酰胺、HP2MGL、ADS-21、D101及AB-8 7种大孔吸附树脂对金银花绿原酸静态吸附与解吸的效果,并通过单因子实验、正交试验与验证实验,优化了树脂分离纯化金银花绿原酸的工艺技术参数.结果表明,NKA-2树脂吸附效果最好,静态饱和吸附量可达212.17 mg/...     

大孔树脂对麻黄细辛附子汤生物碱成分静态吸附及解吸附性能研究

采用高效液相色谱法(HPLC)测定麻黄细辛附子(MXF)汤复方水提液中盐酸麻黄碱、盐酸伪麻黄碱、苯甲酰新乌头原碱、苯甲酰乌头原碱、苯甲酰次乌头原碱含量,考察了4种大孔树脂(HPD–100,HPD–722,HPD–400,HPD–600型)对5种生物碱的静态吸附、解吸附性能,筛选出分离纯化麻黄细辛附子汤中生物碱的最佳树脂。结果显示,HPD–722型树脂对5种生物碱的吸附过程稳定且吸附量大,具有较高的解吸附率(87.26%),优于其它3种树脂。HPD–722型大孔树脂适用于富集麻黄细辛附子汤中的生物碱类化合物。     

大孔吸附树脂对大豆皂苷的吸附研究

比较了5种大孔吸附树脂对大豆皂苷的吸附等温线、吸附容量、解吸率和吸附动力学。发现ZTC-1树脂对大豆皂苷吸附量大、解吸容易、吸附速度快，是一种良好的大豆皂苷吸附荆，AB-8树脂次之．选择ZTC-l树脂纯化大豆皂苷粗提液，得到大豆皂苷产品纯度为78．2％(干物质)，回收率为93．1％．     

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.     

大孔吸附树脂对天麻素的吸附与分离特性的研究

研究了AB 8、NKA 9和S 83种大孔吸附树脂对中药天麻提取液中有效成分天麻素的吸附与分离特性。结果表明,NKA 9和S 8树脂对天麻素具有较好的吸附和解吸特性。其中经NKA-9树脂纯化的天麻素纯度为16.4%,比粗提物的天麻素纯度提高了1倍多。     

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%.     

Enrichment and purification of madecassoside and asiaticoside from Centella asiatica extracts with macroporous resins

In present study, the performance and separation characteristics of five macroporous resins for the enrichment and purification of asiaticoside and madecassoside from Centella asiatica extracts have been evaluated. The adsorption and desorption properties of total triterpene saponins (80% purity) on macroporous resins including HPD100, HPD300, X-5, AB-8 and D101 have been compared. According to our results, HPD100 offered higher adsorption and desorption capacities and higher adsorption speed for asiaticoside and madecassoside than other resins. Column packed with HPD100 resin was used to perform dynamic adsorption and desorption tests to optimize the separation process of asiaticoside and madecassoside from C. asiatica extracts. After the treatment with gradient elution on HPD100 resin, the content of madecassoside in the product increased from 3.9 to 39.7%, and the recovery yield was 70.4%; for asiaticoside the content increased from 2.0 to 21.5%, and the recovery yield was 72.0%. The results showed that HPD100 resin revealed a good ability to separate madecassoside and asiaticoside, and the method can be referenced for the separation of other triterpene saponins from herbal raw materials.     

大孔树脂精制6种含黄连复方水提液体系的吸附动力学比较研究

研究含黄连的不同复方水提液体系经大孔吸附树脂精制后,黄连中主要指标性成分生物碱的变化,阐明不同复方组合-配伍对药方中组成药味指标性成分的影响,为大孔树脂精制技术在中药复方中的应用提供实验依据.选用黄连用量和复方总用量均相同,组方药味不同的复方1～6.通过考察5种树脂AB-8、S-8、X-5、NKA-II、NKA-9对黄连中盐酸小檗碱的静态吸附率,确定AB-8树脂作为复方1～6吸附动力学比较研究的树脂;通过比较复方1～6水提液体系在相同树脂环境下的静态吸附过程,考察6种不同复方组成药味对复方中指标性成分分离纯化的影响.实验结果表明,由于体系本身溶液环境的差异,复方1～6各指标性成分达到吸附平衡的时问均有差异.AB～8树脂对复方1～6水提液体系的静态吸附在开始阶段吸附量的增加比较明显,在40min后,由于吸附竞争点饱和的原因,吸附量的增加均比较平稳;黄连与不同药材配伍时,虽然配伍药材所含的化合物类型差异较大,但黄连中生物碱类成分均可以在树脂上被选择性吸附,可知在复方水提液复杂体系中可以选择性地分离纯化生物碱类有效成分.     

Separation of 7-xylosyl-10-deacetyl paclitaxel and 10-deacetylbaccatin III from the remainder extracts free of paclitaxel using macroporous resins

The separation and enrichment of 10-deacetylbaccatin III (10-DAB III) and 7-xylosyl-10-deacetyl paclitaxel were studied on seven macroporous resins with special structures. The performance of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III on macroporous resins including AB-8, ADS-17, ADS-21, ADS-31, ADS-8, H1020 and NKA-II was compared according to their adsorption and desorption properties. AB-8 provided a much higher adsorption capacity for 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III than other resins, and its adsorption data fitted well to the Langmuir and Freundlich isotherm. According to the adsorption and desorption capacities and the adsorption isotherms, AB-8 demonstrated a remarkable capability for the preparative separation of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III from the remainder extracts free of paclitaxel. In order to optimize parameters of separation, dynamic adsorption and desorption experiments were carried out on the columns packed with AB-8 resin. The optimal conditions were: the processing volume 15 BV; concentrations of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III in feed solution 0.0657 mg/mL and 0.1494 mg/mL; flow rate 1 mL/min; temperature 35 degrees C. The gradient elution program was as follows: 30% ethanol for 3 BV, then 80% of ethanol for 6 BV, flow rate 1 mL/min. After the AB-8 resin treatment, the contents of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III in the product had increased from 0.053% and 0.2% to 3.34% and 1.69%, which were 62.43-fold and 8.54-fold of those in the untreated extracts, respectively, and the recoveries of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III were 85.85% and 52.78%. The performance achieved good separation and higher recovery of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III from remainder extracts free of paclitaxel by using AB-8 resin. It is a fast and effective method for the separation and enrichment of 7-xylosyl-10-deacetyl paclitaxel and 10-DAB III.