CN110437053B - Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum - Google Patents
Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum Download PDFInfo
- Publication number
- CN110437053B CN110437053B CN201910861156.1A CN201910861156A CN110437053B CN 110437053 B CN110437053 B CN 110437053B CN 201910861156 A CN201910861156 A CN 201910861156A CN 110437053 B CN110437053 B CN 110437053B
- Authority
- CN
- China
- Prior art keywords
- extraction
- carbonyl
- temperature
- pressure
- zelanone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/78—Separation; Purification; Stabilisation; Use of additives
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B2200/00—Indexing scheme relating to specific properties of organic compounds
- C07B2200/07—Optical isomers
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2602/00—Systems containing two condensed rings
- C07C2602/02—Systems containing two condensed rings the rings having only two atoms in common
- C07C2602/14—All rings being cycloaliphatic
- C07C2602/26—All rings being cycloaliphatic the ring system containing ten carbon atoms
- C07C2602/28—Hydrogenated naphthalenes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Medicines Containing Plant Substances (AREA)
Abstract
本发明公开了一种从紫茎泽兰中提取分离泽兰酮类化合物的方法,步骤如下:药材风干粉碎、超临界CO2萃取、分子蒸馏分离、工业色谱纯化,最后得到9‑羰基‑10,11‑去氢泽兰酮和9‑羰基‑10Hβ泽兰酮,所得产品纯度较高、转移率高,整套工艺合理可行、过程简单、溶剂单一且易于回收,并且适用于大批量工业化生产,具有很强的实用价值。
The invention discloses a method for extracting and separating zelanone compounds from Euratopseria japonica. The steps are as follows: air-drying and pulverizing medicinal materials, supercritical CO 2 extraction, molecular distillation separation, industrial chromatography purification, and finally obtaining 9-carbonyl-10 ,11-dehydrozelenone and 9-carbonyl-10Hβ-zelenone, the obtained products have high purity and high transfer rate, the whole process is reasonable and feasible, the process is simple, the solvent is single and easy to recover, and it is suitable for large-scale industrial production, Has a strong practical value.
Description
技术领域technical field
本发明涉及天然产物活性成分提取分离技术领域,尤其涉及从紫茎泽兰中提取分离泽兰酮类化合物的方法。The present invention relates to the technical field of extraction and separation of active components of natural products, in particular to a method for extracting and separating zelanone compounds from Eurasian zelanus.
背景技术Background technique
紫茎泽兰(Eupatorium adenophorum Spreng)是菊科泽兰属多年生半灌木状草本植物,作为一种恶性杂草,现分布于世界30多个国家并对环境造成严重威胁。紫茎泽兰具有适应性强、传播速度快、繁殖能力强等特点,通过化感作用排斥本地植物衰退形成单一优势种群,在上世纪40年代传入我国云南,被列为我国首批外来入侵物种。现已广泛分布于我国西南地区,并成为我国危害最严重的外来入侵杂草。多年来,对紫茎泽兰的防除效果并不理想,对其进行综合利用为治理外来入侵物种提供一条新的途径。Eupatorium adenophorum Spreng is a perennial sub-shrub-like herb of the genus Asteraceae. As a malignant weed, it is distributed in more than 30 countries in the world and poses a serious threat to the environment. It has the characteristics of strong adaptability, fast transmission speed and strong reproductive ability. It repels the decline of native plants through allelopathic action to form a single dominant population. It was introduced to Yunnan in my country in the 1940s and was listed as one of the first foreign invasions in my country. species. It is now widely distributed in southwest China, and has become the most serious invasive alien weed in my country. For many years, the control effect of Euratopseria is not ideal, and its comprehensive utilization provides a new way to control invasive alien species.
研究表明,从紫茎泽兰叶中分离得到的泽兰酮类化合物9-羰基-10,11-去氢泽兰酮(euptoxA)、9-羰基-10Hβ泽兰酮(9-Oxoageraphorone)等泽兰酮类物质,具有较好的抗肿瘤、抗病毒、抑菌、杀虫等生物活性,作为植物源农药和疾病治疗药物的开发皆具有极大的潜力。目前对于紫茎泽兰中泽兰酮类化合物的提取纯化工艺研究仍处于实验室的小试阶段,需要对泽兰酮提取部位通过反复柱层析进行纯化,存在操作复杂、溶剂复杂且用量大、产品纯度低、收率低等问题。无法快速大量得到较高纯度的样品是制约泽兰酮类物质深入开发的主要因素。Studies have shown that the zelanone compounds such as 9-carbonyl-10,11-dehydrozeranone (euptoxA), 9-carbonyl-10Hβ zelanone (9-Oxoageraphorone), etc. Ranone substances have good anti-tumor, anti-virus, bacteriostatic, insecticidal and other biological activities, and have great potential for the development of botanical pesticides and disease treatment drugs. At present, the research on the extraction and purification process of zelanone compounds in A. chinensis is still in the laboratory stage. It is necessary to purify the extracted part of zelanone by repeated column chromatography, which is complicated in operation, complicated in solvent and large in amount. , low product purity, low yield and other problems. The inability to obtain high-purity samples quickly and in large quantities is the main factor restricting the further development of zelanones.
中国发明专利公告号为CN103274935B,发明名称为《一种提取紫茎泽兰中泽兰酮化合物的方法》,公开了如下技术方案:第一步,粉碎紫茎泽兰叶至粉末;第二步,采用甲醇或水超声震荡提取,减压浓缩得到浸膏;第三步,甲醇溶解浸膏、水稀释,乙酸乙酯萃取多次,合并萃取液,浓缩;第四步,硅胶柱层析分离,洗脱剂依次是二氯甲烷,二氯甲烷、乙酸乙酯的混合液;第五步,大孔树脂脱色,洗脱液是甲醇、水、三氯甲烷混合液;第六步,再次硅胶柱层析,洗脱液是二氯甲烷和乙酸乙酯。该技术方案虽然能够提取出2-脱氧-2-乙酰氧基-9-羰基泽兰酮、9-羰基-10Hβ泽兰酮、9-羰基-10Hα泽兰酮、9-羰基-10,11去氢泽兰酮,但是提取工艺步骤复杂,而且过程中使用了二氯甲烷、三氯甲烷这些有毒危险溶剂,而且在硅胶柱层析分离、大孔树脂脱色所用洗脱剂复杂。The Chinese invention patent announcement number is CN103274935B, and the name of the invention is "A method for extracting zelanone compounds in A. chinensis". , extract with methanol or water by ultrasonic vibration, and concentrate under reduced pressure to obtain the extract; the third step, dissolve the extract in methanol, dilute with water, extract multiple times with ethyl acetate, combine the extracts, and concentrate; the fourth step, separate by silica gel column chromatography , the eluent is a mixture of dichloromethane, dichloromethane and ethyl acetate in turn; the fifth step, the macroporous resin is decolorized, and the eluent is a mixture of methanol, water and chloroform; the sixth step, silica gel again Column chromatography, the eluents were dichloromethane and ethyl acetate. Although this technical solution can extract 2-deoxy-2-acetoxy-9-carbonyl zelenone, 9-carbonyl-10Hβ zelenone, 9-carbonyl-10Hα zelenone, 9-carbonyl-10,11 de- Hydrozelanone, but the extraction process steps are complicated, and the toxic and dangerous solvents such as dichloromethane and chloroform are used in the process, and the eluents used in silica gel column chromatography separation and macroporous resin decolorization are complicated.
中国发明专利公布号为:CN103351290A,发明名称为《紫茎泽兰两种化感活性次生物质的提取纯化方法》公开了如下技术方案:第一步,蒸馏水浸泡得到水提液;第二步,正己烷萃取;第三步,两次玻璃硅胶柱色谱分离,洗脱液是乙酸乙酯和三氯甲烷混合液,薄层层析硅胶板检测,定性收集泽兰二酮和羟基泽兰酮。虽然该技术方案的步骤不多,但是其中使用了三氯甲烷有毒危险溶剂,而且最后分离出来的是泽兰二酮和羟基泽兰酮,并不是9-羰基-10,11-去氢泽兰酮、9-羰基-10Hβ泽兰酮。The Chinese invention patent publication number is: CN103351290A, and the name of the invention is "The Extraction and Purification Method of Two Allelopathic Active Secondary Substances of Echinacea". The following technical scheme is disclosed: the first step is to soak in distilled water to obtain an aqueous extract; , n-hexane extraction; the third step, two glass silica gel column chromatography separation, the eluent is a mixture of ethyl acetate and chloroform, TLC silica gel plate detection, qualitative collection of zerandione and hydroxyzeranone . Although there are not many steps in this technical solution, chloroform is used as a toxic and dangerous solvent, and zerandione and hydroxyzelanone are finally separated, not 9-carbonyl-10,11-dehydrozelan Ketone, 9-Carbonyl-10Hβ Zelenone.
因此,开发一种新的技术获得9-羰基-10,11-去氢泽兰酮、9-羰基-10Hβ泽兰酮是必要的。Therefore, it is necessary to develop a new technology to obtain 9-carbonyl-10,11-dehydrozelenone and 9-carbonyl-10Hβ-zelenone.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种从紫茎泽兰中提取分离泽兰酮类化合物的方法,解决现有技术提取纯化泽兰酮化合物的方法工艺复杂、溶剂复杂且用量大、产品纯度低、收率低等问题。The object of the present invention is to provide a kind of method for extracting and separating zelanone compounds from E. japonica, and solve the problem that the method for extracting and purifying zelanone compounds in the prior art is complicated in process, complicated in solvent, large in dosage, low in product purity, and in yield. problems such as low rates.
为了达到上述目的本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
(1)药材处理:采集紫茎泽兰叶后阴凉处风干,用粉碎机粉碎得到紫茎泽兰粉末。(1) Treatment of medicinal materials: After collecting the leaves of Rhizoma Rhizopus chinensis, it was air-dried in a cool place, and pulverized with a pulverizer to obtain Rhododendron chinensis powder.
(2)超临界CO2萃取:将步骤(1)制备的粉末加至超临界CO2萃取装置萃取釜,对萃取装置分别进行升温、升压至萃取循环条件,开始循环萃取,保持恒温恒压至所需萃取时间,调节解析釜温度和压力,得到紫茎泽兰提取物;(2) supercritical CO 2 extraction: add the powder prepared in step (1) to the extraction kettle of the supercritical CO 2 extraction device, and the extraction device is respectively heated and pressurized to the extraction cycle condition, and the cyclic extraction is started, and the constant temperature and pressure are maintained. To the required extraction time, adjust the temperature and pressure of the analysis kettle to obtain the Echinacea japonica extract;
(3)分子蒸馏分离:将步骤(2)所得紫茎泽兰提取物加至分子蒸馏装置恒温槽,升温至所需蒸馏温度,调节真空度至所需压力,控制紫茎泽兰提取物滴加速度,开始蒸馏,收集泽兰酮富集馏分;(3) molecular distillation separation: adding the extract of Step (2) gained Euratopsis to the molecular distillation device constant temperature tank, be warming up to the required distillation temperature, adjust the vacuum degree to the required pressure, and control the E. Accelerate, start distillation, collect zelenone-enriched fractions;
(4)工业色谱纯化:将步骤(3)所得泽兰酮富集馏分溶解,过滤后上工业色谱,用有机溶剂洗脱,收集9-羰基-10,11-去氢泽兰酮和9-羰基-10Hβ泽兰酮洗脱液,减压浓缩、干燥,得9-羰基-10,11-去氢泽兰酮和9-羰基-10Hβ泽兰酮产品。可以采用流动相溶解步骤(3)所得泽兰酮富集馏分,当然本领域技术人员也可以根据本发明公开的技术内容结合领域常识自行配置合适的溶剂。(4) Industrial chromatographic purification: Dissolve the enriched fractions of zelanone obtained in step (3), filter and apply industrial chromatography, elute with organic solvent, collect 9-carbonyl-10,11-dehydrozelanone and 9- The carbonyl-10Hβ-zelenone eluate was concentrated under reduced pressure and dried to obtain 9-carbonyl-10,11-dehydrozelenone and 9-carbonyl-10Hβzelenone products. The zelanone-enriched fraction obtained in the mobile phase dissolving step (3) can be used. Of course, those skilled in the art can also configure a suitable solvent by themselves according to the technical content disclosed in the present invention and common knowledge in the field.
进一步的,所述步骤(1)中,紫茎泽兰叶粉碎至60~120目粉末,优选粉碎至80目。Further, in the step (1), the leaves of Rhododendron chinensis are pulverized to 60-120 mesh powder, preferably to 80 mesh.
进一步的,所述步骤(2)中,萃取压力为25~35MPa,萃取温度为45~65℃,萃取时间为0.5~1.5h,优选的:萃取压力为30MPa,萃取温度为55℃,萃取时间为1.0h。Further, in the step (2), the extraction pressure is 25-35MPa, the extraction temperature is 45-65°C, and the extraction time is 0.5-1.5h. Preferably, the extraction pressure is 30MPa, the extraction temperature is 55°C, and the extraction time is 55°C. is 1.0h.
进一步的,所述步骤(2)中,解析釜I压力为12~21MPa,温度为45~55℃,优选的:解析釜I压力为18MPa,温度为50℃。解析釜II的压力为6MPa,温度为45℃。Further, in the step (2), the pressure of the analysis kettle I is 12 to 21 MPa, and the temperature is 45 to 55 ° C, preferably: the pressure of the analysis kettle I is 18 MPa, and the temperature is 50 ° C. The pressure of the analysis kettle II was 6MPa and the temperature was 45°C.
进一步的,所述步骤(3)中,紫茎泽兰提取物进料流速为0.5滴/秒~4滴/秒,蒸馏温度为120~200℃,真空度为10~40Pa,刮膜转速为200~300r/min,冷凝温度为0~50℃;优选的:进料流速为2滴/秒,蒸馏温度为150℃,真空度为20Pa,刮膜转速为250r/min,冷凝温度为25℃。Further, in the step (3), the feed flow rate of E. chinensis extract is 0.5 drops/sec~4 drops/sec, the distillation temperature is 120~200°C, the vacuum degree is 10~40Pa, and the speed of the scraping film is 200~300r/min, condensing temperature is 0~50 ℃; preferably: feed flow rate is 2 drops/second, distillation temperature is 150 ℃, vacuum degree is 20Pa, film scraping speed is 250r/min, condensing temperature is 25 ℃ .
进一步的,所述步骤(4)中,工艺色谱的填料为UniPS10、UniPMM10、UniPSA 10、UniPSN 10、UniSil 10中的一种或两种以上。Further, in the step (4), the filler of the process chromatography is one or more of UniPS10, UniPMM10, UniPSA 10, UniPSN 10 and UniSil 10.
进一步的,所述步骤(4)中,洗脱所用的有机溶剂为乙醇、甲醇或乙腈,优选为甲醇。Further, in the step (4), the organic solvent used for elution is ethanol, methanol or acetonitrile, preferably methanol.
进一步的,所述步骤(4)中,洗脱所用的有机溶剂的体积分数为50%-80%,优选为70%。Further, in the step (4), the volume fraction of the organic solvent used for elution is 50%-80%, preferably 70%.
进一步的,所述步骤(4)中,洗脱时有机溶剂以流速为6~15mL/min分次进行洗脱,优选为10mL/min。Further, in the step (4), during elution, the organic solvent is eluted in stages at a flow rate of 6-15 mL/min, preferably 10 mL/min.
进一步的,所述步骤(4)中,在检测波长为230nm的情况下,收集9-羰基-10,11-去氢泽兰酮及9-羰基-10Hβ泽兰酮洗脱峰;减压浓缩温度是55℃。Further, in the step (4), under the condition that the detection wavelength is 230 nm, the elution peaks of 9-carbonyl-10,11-dehydrozelenone and 9-carbonyl-10Hβ-zelenone are collected; concentrated under reduced pressure The temperature was 55°C.
本发明的有益效果为:以超临界CO2萃取-分子蒸馏分离-工业色谱纯化为核心成套技术从紫茎泽兰中提取分离泽兰酮类化合物,建立了一条从紫茎泽兰中提取、分离、纯化泽兰酮类化合物的工艺路线,该工艺所得产品纯度较高、转移率高,整套工艺合理可行、过程简单、溶剂单一且易于回收,并且易于大批量工业化生产,具有很强的实用价值。The beneficial effects of the invention are as follows: taking supercritical CO 2 extraction-molecular distillation separation-industrial chromatographic purification as the core complete set of technology to extract and separate zelanone compounds from E. The process route of separating and purifying zelanone compounds, the product obtained by this process has high purity and high transfer rate, the whole process is reasonable and feasible, the process is simple, the solvent is single and easy to recover, and it is easy to be industrialized in large quantities, and has strong practicality. value.
附图说明Description of drawings
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1为9-羰基-10,11-去氢泽兰酮的分子结构图;Fig. 1 is the molecular structure diagram of 9-carbonyl-10,11-dehydrozelanone;
图2为9-羰基-10Hβ泽兰酮的分子结构图;Fig. 2 is the molecular structure diagram of 9-carbonyl-10Hβ zelanone;
图3为本发明实施例1中分子蒸馏馏分的高效液相色谱图,色谱峰1和峰2分别为9-羰基-10,11-去氢泽兰酮和9-羰基-10Hβ泽兰酮;Fig. 3 is the high performance liquid chromatogram of molecular distillation fraction in the embodiment of the
图4为本发明实施例1中工业色谱的色谱图(230nm),色谱峰1和峰2分别为9-羰基-10,11-去氢泽兰酮和9-羰基-10Hβ泽兰酮。4 is a chromatogram (230 nm) of an industrial chromatogram in Example 1 of the present invention, and the
图5为本发明实施例1中工业色谱纯化后产品的高效液相色谱图,色谱峰1为9-羰基-10,11-去氢泽兰酮;Fig. 5 is the high performance liquid chromatogram of the product after industrial chromatographic purification in the embodiment of the
图6为本发明实施例1中工业色谱纯化后产品的高效液相色谱图,峰2为9-羰基-10Hβ泽兰酮。Fig. 6 is the high-performance liquid chromatogram of the product after purification by industrial chromatography in Example 1 of the present invention, and
具体实施方式Detailed ways
下面将结合具体实施例来详细说明本发明,在此以本发明的示意性实施例及说明用来解释本发明,但并不作为对本发明的限定。The present invention will be described in detail below with reference to specific embodiments, and the illustrative embodiments and descriptions of the present invention are used to explain the present invention, but are not intended to limit the present invention.
实施例1Example 1
(1)药材处理:采集紫茎泽兰叶后阴凉处风干,用粉碎机粉碎至80目的粉末;(1) Treatment of medicinal materials: After collecting the leaves of Eurasian chinensis, air-dry them in a cool place, and pulverize them to 80 mesh powder with a pulverizer;
(2)超临界CO2萃取:称取步骤(1)制备的粉末1.0Kg,装于超临界CO2萃取装置萃取釜,萃取釜升压至30MPa,升温至55℃;解析釜I升压至18MPa,升温至50℃;解析釜II升压至6MPa,升温至45℃,开始循环萃取,保持恒温恒压,萃取1.0h,萃取完成后收集解析釜II萃取物,得到萃取物65.2g;(2) supercritical CO 2 extraction: take by weighing 1.0Kg of the powder prepared in step (1), put it in a supercritical CO 2 extraction device extraction kettle, and the extraction kettle is boosted to 30MPa, and heated to 55°C; 18MPa, heated to 50°C; pressure of analysis kettle II was increased to 6MPa, heated to 45°C, cyclic extraction was started, constant temperature and pressure were maintained, extraction was performed for 1.0h, after extraction was completed, the extract of analysis kettle II was collected to obtain 65.2g of extract;
(3)分子蒸馏分离:取步骤(2)所得的萃取物60.0g,加至分子蒸馏装置恒温槽,升温至150℃,调节真空度至20Pa,刮膜转速250r/min,冷凝温度25℃。以2滴/秒的速度开始蒸馏过程,收集泽兰酮馏分40.8g;(3) Molecular distillation separation: take 60.0 g of the extract obtained in step (2), add it to a constant temperature tank of a molecular distillation device, heat up to 150 ° C, adjust the vacuum to 20 Pa, wipe the film rotation speed 250 r/min, and
(4)工业色谱纯化:取步骤(3)所得泽兰酮富集馏分10.0g,加70%甲醇溶解,过滤后上工业色谱,以UniSil 10为填料,70%甲醇为洗脱剂,以10mL/min的流速分次进行洗脱,在230nm波长下,收集9-羰基-10,11-去氢泽兰酮及9-羰基-10Hβ泽兰酮洗脱峰,55℃减压浓缩、干燥,得9-羰基-10,11-去氢泽兰酮产品7.43g、9-羰基-10Hβ泽兰酮产品1.51g。(4) Industrial chromatographic purification: take 10.0 g of the zelenone-enriched fraction obtained in step (3), add 70% methanol to dissolve, filter and apply to industrial chromatography, use UniSil 10 as the filler, 70% methanol as the eluent, and use 10 mL of The elution was carried out at a flow rate of /min in stages, and at a wavelength of 230 nm, the elution peaks of 9-carbonyl-10,11-dehydrozelenone and 9-carbonyl-10Hβ-zelenone were collected, concentrated under reduced pressure at 55°C, and dried. 7.43 g of 9-carbonyl-10,11-dehydrozelenone product and 1.51 g of 9-carbonyl-10Hβ zelenone product were obtained.
实验结果如图3-6所示,化合物1为:9-羰基-10,11-去氢泽兰酮(euptoxA);化合物2为:9-羰基-10Hβ泽兰酮(9-Oxoageraphorone)。The experimental results are shown in Figures 3-6.
实施例2Example 2
(1)药材处理:采集紫茎泽兰叶后阴凉处风干,用粉碎机粉碎至60目的粉末;(1) Treatment of medicinal materials: After collecting the leaves of Eurasian chinensis, air-dry them in a cool place, and pulverize them to 60 mesh powder with a pulverizer;
(2)超临界CO2萃取:称取步骤(1)制备的粉末1.0Kg,装于超临界CO2萃取装置萃取釜,萃取釜升压至35MPa,升温至45℃;解析釜I升压至21MPa,升温至45℃;解析釜II升压至6MPa,升温至45℃,开始循环萃取,保持恒温恒压,萃取0.5h,萃取完成后收集解析釜II萃取物,得到萃取物65.9g;( 2 ) supercritical CO extraction: take by weighing 1.0Kg of the powder prepared in step (1), put it in a supercritical CO extraction device extraction kettle, the extraction kettle is boosted to 35MPa, and heated to 45°C; the
(3)分子蒸馏分离:取步骤(2)所得的萃取物60.0g,加至分子蒸馏装置恒温槽,升温至200℃,调节真空度至40Pa,刮膜转速300r/min,冷凝温度0℃。以4滴/秒的速度开始蒸馏过程,收集泽兰酮馏分41.2g;(3) Molecular distillation separation: take 60.0 g of the extract obtained in step (2), add it to a constant temperature tank of a molecular distillation device, heat up to 200 ° C, adjust the vacuum to 40 Pa, wipe the film rotation speed 300 r/min, and
(4)工业色谱纯化:取步骤(3)所得泽兰酮富集馏分10.0g,加50%乙腈溶解,过滤后上工业色谱,以UniPS10为填料,50%乙腈为洗脱剂,以15mL/min的流速分次进行洗脱,在230nm波长下,收集9-羰基-10,11-去氢泽兰酮及9-羰基-10Hβ泽兰酮洗脱峰,55℃减压浓缩、干燥,得9-羰基-10,11-去氢泽兰酮产品7.25g、9-羰基-10Hβ泽兰酮产品1.43g。(4) Industrial chromatographic purification: take 10.0 g of the zelenone enriched fraction obtained in step (3), add 50% acetonitrile to dissolve, filter and apply to industrial chromatography, use UniPS10 as the filler, 50% acetonitrile as the eluent, take 15 mL/ The elution was carried out at a flow rate of 1 min, and at a wavelength of 230 nm, the elution peaks of 9-carbonyl-10,11-dehydrozelenone and 9-carbonyl-10Hβ-zelenone were collected, concentrated under reduced pressure at 55 °C, and dried to obtain 7.25 g of 9-carbonyl-10,11-dehydrozelenone product and 1.43 g of 9-carbonyl-10Hβ zelenone product.
实施例3Example 3
(1)药材处理:采集紫茎泽兰叶后阴凉处风干,用粉碎机粉碎至120目的粉末。(1) Treatment of medicinal materials: After collecting the leaves of Rhododendron chinensis, air-dry them in a cool place, and pulverize them to 120 mesh powder with a pulverizer.
(2)超临界CO2萃取:称取步骤(1)制备的粉末1.0Kg,装于超临界CO2萃取装置萃取釜,萃取釜升压至25MPa,升温至65℃;解析釜I升压至18MPa,升温至55℃;解析釜II升压至6MPa,升温至45℃,开始循环萃取,保持恒温恒压,萃取1.0h,萃取完成后收集解析釜II萃取物,得到萃取物64.7g;(2) supercritical CO 2 extraction: take by weighing 1.0Kg of the powder prepared in step (1), put it in a supercritical CO 2 extraction device extraction kettle, the extraction kettle is boosted to 25MPa, and heated to 65°C; 18MPa, the temperature was raised to 55°C; the pressure of the analysis kettle II was increased to 6MPa, the temperature was raised to 45°C, the cyclic extraction was started, the constant temperature and pressure were maintained, and the extraction was performed for 1.0 h. After the extraction was completed, the extract of the analysis kettle II was collected to obtain 64.7g of extract;
(3)分子蒸馏分离:取步骤(2)所得的萃取物60.0g,加至分子蒸馏装置恒温槽,升温至120℃,调节真空度至10Pa,刮膜转速200r/min,冷凝温度25℃。以0.5滴/秒的速度开始蒸馏过程,收集泽兰酮馏分40.9g;(3) Molecular distillation separation: take 60.0 g of the extract obtained in step (2), add it to a constant temperature tank of a molecular distillation device, heat up to 120 ° C, adjust the vacuum degree to 10 Pa, wipe the film rotation speed 200 r/min, and condense
(4)工业色谱纯化:取步骤(3)所得泽兰酮富集馏分10.0g,加80%乙醇溶解,过滤后上工业色谱,以UniPSN 10为填料,80%乙醇为洗脱剂,以6mL/min的流速分次进行洗脱,在230nm波长下,收集9-羰基-10,11-去氢泽兰酮及9-羰基-10Hβ泽兰酮洗脱峰,55℃减压浓缩、干燥,得9-羰基-10,11-去氢泽兰酮产品7.33g、9-羰基-10Hβ泽兰酮产品1.47g。(4) Industrial chromatographic purification: take 10.0 g of the zelenone-enriched fraction obtained in step (3), add 80% ethanol to dissolve, filter and apply to industrial chromatography, use
实施例4Example 4
分别对实施例1、实施例2、实施例3中各步骤的泽兰酮样品进行液相色谱检测,并根据高效液相色谱检测结果记录峰面积,对照标准品溶液中有效成分的峰面积与浓度的线性关系,计算出各步骤中泽兰酮类化合物的含量和转移率。化合物1为:9-羰基-10,11-去氢泽兰酮(euptoxA);化合物2为:9-羰基-10Hβ泽兰酮(9-Oxoageraphorone)。详情如下表:The zelanone samples of each step in Example 1, Example 2, and Example 3 were detected by liquid chromatography, and the peak area was recorded according to the detection result of high performance liquid chromatography. The peak area of the active ingredient in the reference standard solution was the same as the The linear relationship between the concentrations was used to calculate the content and transfer rate of zelanone compounds in each step.
表1泽兰酮类化合物超临界CO2萃取结果Table 1 Results of supercritical CO extraction of zeranone compounds
表2分子蒸馏富集结果Table 2 Molecular distillation enrichment results
表3工业色谱分离结果Table 3 Industrial chromatographic separation results
表4工业色谱分离结果Table 4 Industrial chromatographic separation results
另外,为了验证对粉碎后药材进行不同提取方法会获得不同技术效果,以下做了三种不同的提取实验:In addition, in order to verify that different extraction methods of crushed medicinal materials will obtain different technical effects, three different extraction experiments were performed as follows:
第一种:本发明实施例1的超临界CO2萃取;The first: the supercritical CO extraction of the embodiment of the
第二种:水蒸气蒸馏法,过程如下:取紫茎泽兰干燥叶(粗粉)320g,加入适量水,蒸馏6h后,收集淡黄色挥发油,4℃冰箱避光密封保存;The second method: steam distillation method, the process is as follows: take 320 g of dried leaves (coarse powder) of Rhododendron chinensis, add an appropriate amount of water, and after distillation for 6 hours, collect the pale yellow volatile oil, and store it in a refrigerator at 4°C in a dark place and sealed;
第三种:溶剂超声提取法,过程如下:精密称取紫茎泽兰干燥叶2.0g,加入40mL甲醇试剂,室温超声提取30min,提取液离心后合并,定容至50mL量瓶,4℃冰箱避光密封保存;The third type: solvent ultrasonic extraction method, the process is as follows: Accurately weigh 2.0 g of dried leaves of Eurasian japonica, add 40 mL of methanol reagent, ultrasonically extract at room temperature for 30 min, centrifuge the extracts and combine them, dilute to a 50 mL volumetric flask, and refrigerate at 4°C Store in an airtight seal away from light;
把以上三种提取方法的技术效果进行比较,如下表5,可明显得出本发明技术方案是具有较大优势的。Comparing the technical effects of the above three extraction methods, as shown in Table 5 below, it can be clearly concluded that the technical solution of the present invention has great advantages.
表5三种提取方法技术效果比较Table 5 Comparison of technical effects of three extraction methods
从以上对比可以获悉,只有以超临界CO2萃取-分子蒸馏分离-工业色谱纯化完整的技术为核心工艺才能得到较佳的技术效果,常规技术替换其中的操作是不能够获得本发明的技术效果的。From the above comparison, it can be known that only with the complete technology of supercritical CO 2 extraction-molecular distillation separation-industrial chromatographic purification as the core process can a better technical effect be obtained, and the conventional technology can not obtain the technical effect of the present invention by replacing the operation therein. of.
以上对本发明实施例所提供的技术方案进行了详细介绍,本文中应用了具体个例对本发明实施例的原理以及实施方式进行了阐述,以上实施例的说明只适用于帮助理解本发明实施例的原理;同时,对于本领域的一般技术人员,依据本发明实施例,在具体实施方式以及应用范围上均会有改变之处,综上所述,本说明书内容不应理解为对本发明的限制。The technical solutions provided by the embodiments of the present invention have been introduced in detail above. The principles and implementations of the embodiments of the present invention are described in this paper by using specific examples. The descriptions of the above embodiments are only applicable to help understand the embodiments of the present invention. At the same time, for those of ordinary skill in the art, according to the embodiments of the present invention, there will be changes in the specific implementation and application scope. To sum up, the content of this specification should not be construed as a limitation of the present invention.
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910861156.1A CN110437053B (en) | 2019-09-12 | 2019-09-12 | Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910861156.1A CN110437053B (en) | 2019-09-12 | 2019-09-12 | Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum |
Publications (2)
Publication Number | Publication Date |
---|---|
CN110437053A CN110437053A (en) | 2019-11-12 |
CN110437053B true CN110437053B (en) | 2022-08-26 |
Family
ID=68439991
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910861156.1A Active CN110437053B (en) | 2019-09-12 | 2019-09-12 | Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110437053B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112535180A (en) * | 2020-11-30 | 2021-03-23 | 湖南人文科技学院 | Eupatorium adenophorum spreng extract and application thereof in preventing and controlling paddy field weeds |
CN114521612A (en) * | 2022-01-20 | 2022-05-24 | 西南林业大学 | Resource utilization method of Eupatorium adenophorum |
CN115894201B (en) * | 2022-09-19 | 2024-04-19 | 扬州大学 | A method for extracting and separating eupatoriandion from Eupatorium adenophorum and its application |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102980956A (en) * | 2012-11-18 | 2013-03-20 | 四川农业大学 | Quick extraction and detection method of 9-oxo-10,11-dehydroagerophorone |
CN103274935A (en) * | 2013-05-20 | 2013-09-04 | 中国农业科学院植物保护研究所 | Method for extracting nepetin compounds from crofton weed |
CN103351290A (en) * | 2013-08-01 | 2013-10-16 | 扬州大学 | Extraction purification method for two allelopathy activity secondary substances of ageratina adenophora sprengel |
-
2019
- 2019-09-12 CN CN201910861156.1A patent/CN110437053B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102980956A (en) * | 2012-11-18 | 2013-03-20 | 四川农业大学 | Quick extraction and detection method of 9-oxo-10,11-dehydroagerophorone |
CN103274935A (en) * | 2013-05-20 | 2013-09-04 | 中国农业科学院植物保护研究所 | Method for extracting nepetin compounds from crofton weed |
CN103351290A (en) * | 2013-08-01 | 2013-10-16 | 扬州大学 | Extraction purification method for two allelopathy activity secondary substances of ageratina adenophora sprengel |
Non-Patent Citations (1)
Title |
---|
超临界CO2提取紫茎泽兰叶中泽兰酮类物质的工艺研究;汪杰等;《中药材》;20180430;第41卷(第4期);第938-942页 * |
Also Published As
Publication number | Publication date |
---|---|
CN110437053A (en) | 2019-11-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109369344A (en) | A method for separating and extracting cannabidiol from industrial hemp plants | |
CN102106931B (en) | Method for producing diverse extracts of berry tea | |
CN102976909B (en) | Method for extracting and purifying 6-gingerol from ginger | |
CN110437053B (en) | Method for extracting and separating eupatorium adenophorum ketone compounds from eupatorium adenophorum | |
CN102351819B (en) | Extraction, purification and preparation method of high-purity salvianolic acid B | |
CN104861019B (en) | The method that high speed adverse current chromatogram prepares flavone compound 1,2 in tea seed shell | |
CN101289478B (en) | Method for separating and preparing salidroside | |
WO2020063894A1 (en) | Industrial utilization method for stevia rebaudiana and stevioside and chlorogenic acid of stevia rebaudiana | |
CN111960930A (en) | Method for separating and purifying cannabidiol from industrial cannabis sativa leaves | |
CN107998212B (en) | Preparation method of rehmannia iridoid glycoside extract | |
CN105859803B (en) | A kind of preparation method of galloyl glucose | |
CN110613739A (en) | Method for separating flavonoid compounds in cotton rose based on high-speed countercurrent chromatography | |
CN101289480A (en) | A kind of separation preparation method of liquiritin | |
CN106317148A (en) | Method for extracting cordycepin from cordyceps militaris | |
CN102627677A (en) | Method for separating and purifying monomer compounds from Rhizoma Polygoni Cuspidati | |
CN107098942A (en) | A kind of method of kaempferia galamga glycosides in Subcritical Water Extraction radish leaves | |
CN114702469B (en) | Method for extracting, separating and purifying 4 kinds of phthalide lactones from ligusticum wallichii | |
CN104876900A (en) | Method for extracting, separating and purifying costunolide and dehydrocostus lactone from elecampane | |
CN106946833A (en) | A kind of method that high-purity sinensetin is extracted from Mao Xu Cao | |
CN107382943A (en) | A kind of method of dihydroquercetin in Subcritical Water Extraction sorghum bran | |
CN102391328B (en) | Method for simultaneously preparing chemical reference substances magnoloside A and magnoloside B | |
CN107929367A (en) | The method that ion-exchange separation from elegant jessamine prepares elegant jessamine alkaloid | |
CN103193750B (en) | Method for preparing shikimic acid and anise flavonoid by joint separation of macroporous resin XAD7HP | |
CN104447642B (en) | The preparation of industrialization chromatographic separation and purification method of andrographolide | |
CN105732653A (en) | Method for preparing oridonin from isodon japonica |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |