CN106518940A - Method for purifying vincoside lactam - Google Patents

Method for purifying vincoside lactam Download PDF

Info

Publication number
CN106518940A
CN106518940A CN201610971856.2A CN201610971856A CN106518940A CN 106518940 A CN106518940 A CN 106518940A CN 201610971856 A CN201610971856 A CN 201610971856A CN 106518940 A CN106518940 A CN 106518940A
Authority
CN
China
Prior art keywords
ethanol
vincoside
lactam
liquid
band
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.)
Granted
Application number
CN201610971856.2A
Other languages
Chinese (zh)
Other versions
CN106518940B (en
Inventor
王绍艳
姚海旭
张伟
石爽
魏伯峰
李守江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
University of Science and Technology Liaoning USTL
Original Assignee
University of Science and Technology Liaoning USTL
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by University of Science and Technology Liaoning USTL filed Critical University of Science and Technology Liaoning USTL
Priority to CN201610971856.2A priority Critical patent/CN106518940B/en
Publication of CN106518940A publication Critical patent/CN106518940A/en
Application granted granted Critical
Publication of CN106518940B publication Critical patent/CN106518940B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H17/00Compounds containing heterocyclic radicals directly attached to hetero atoms of saccharide radicals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00Processes for the preparation of sugar derivatives
    • C07H1/06Separation; Purification
    • C07H1/08Separation; Purification from natural products

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

The invention provides a method for purifying vincoside lactam and belongs to the technical field of purification of natural plant monomers. According to the method, firstly, a common camptotheca fruit is extracted with an ethanol water solution, a common camptotheca fruit crude extract is obtained, vincoside lactam in the common camptotheca fruit crude extract is purified by the aid of three-zone simulated moving bed chromatography separation, a vincoside lactam extracting liquid is obtained and then is treated after being concentrated and crystalized, and high-purity vincoside lactam is obtained. The method can be used for purifying vincoside lactam efficiently on a large scale, stable, continuous and automatic operation is realized in the simulated moving bed chromatography separation process, a solid phase and a mobile phase can be repeatedly utilized, and the purification cost is reduced.

Description

A kind of method of purification vincoside-lactam
Technical field
The invention belongs to natural plants monomer purification technical field, more particularly to a kind of method of purification vincoside-lactam.
Background technology
Fructus Camptothecae Acuminatae is the fruit of China endemic tree Fructus seu radix camptothecae acuminatae (Fructus Camptothecae Acuminatae), and since ancient times, Fructus seu radix camptothecae acuminatae (Fructus Camptothecae Acuminatae) is important medical material among the people, and can be complete Strain medication, for treating pernicious treatment poison, tumor.Main chemical compositions in Fructus Camptothecae Acuminatae include:Camptothecine, 10-hydroxycamptothecine, 11- methoxycamptothecines, deoxocamptothecin, venoterpine, betulinic acid and vincoside-lactam.Research discovery, vincoside-lactam and camptothecine Class compound has active anticancer, and vincoside-lactam also has antibacterial, antiviral, antiinflammatory, paroxysmal pain, antipyretic purposes.
By vincoside-lactam is extracted in Fructus Camptothecae Acuminatae, it is worth with important practical.The method for extracting separation vincoside-lactam at present is mainly Column chromatography, such as:Ou Lailiang et al. (CN 1295239C, 2007) by Fructus Camptothecae Acuminatae ethanol solution percolation or ethanol solution 25-80 DEG C heat is extracted, extracting solution adsorbs in being passed through the resin column equipped with macroporous adsorbent resin (AL-2 adsorbent resiies), uses ethanol water The step such as washing and desorbing, effluent concentrated by rotary evaporation and recrystallization obtains wedding fruits glycoside product;Wang Ruifang et al. (applied chemistry, 2005, 22(1):24-29) with macropore super high cross-linked adsorbing resin (Rf18) and its methylamine (Rs3), the N- methyl vinyl aminations of synthesis (Rs4), diformazan amination (Rs5), column chromatography for separation is carried out to camptothecine and vincoside-lactam after front three amination (Rs6);Shi Weiguo et al. (CHINA JOURNAL OF CHINESE MATERIA MEDICA, 2008,32 (21):2487-2489) with polyamide separation and purification 10-hydroxycamptothecine and vincoside-lactam;King Auspicious virtue et al. (applied chemistry, 2009,26 (5):593-596) Fructus Camptothecae Acuminatae is carried by the nano adsorption resin from different structure The camptothecine and vincoside-lactam (CPT and VCS-LT) taken in liquid carries out chromatography.The technique that existing column chromatography purifies vincoside-lactam Batch process is, eluant consumption is big, it is impossible to continuous to produce automatically.
Simulated moving bed chromatography (abbreviation SMBC) is the high efficiency separation means for purifying compound.Simulated moving bed chromatography is in system On the basis of standby chromatograph, continuous operating mechanism is introduced, the separation of automatization and scale can be carried out.
The content of the invention
The purpose of the present invention is the deficiency for the presence of vincoside-lactam method is isolated and purified in prior art, there is provided Yi Zhongti The method of pure vincoside-lactam.The method extracts Fructus Camptothecae Acuminatae crude extract with ethanol water first, recycles three band Simulation moving bed colors Vincoside-lactam in spectrum separating-purifying Fructus Camptothecae Acuminatae crude extract, obtains vincoside-lactam extract, then after extract is concentrated and crystallized Process obtains highly purified vincoside-lactam.The method can be with scale, efficiently purify vincoside-lactam, and simulated moving bed chromatography point Sane, continuous, automatic running is realized from process, fixing phase and mobile phase can be recycled, and reduce cost for purification.
A kind of method of purification vincoside-lactam, comprises the steps:
(1) Fructus Camptothecae Acuminatae crude extract is prepared, i.e.,:Raw material pre-treatment
After Fructus Camptothecae Acuminatae raw material is smashed, leached 1-3 time with solvent, obtain leaching liquid;After leaching liquid is concentrated, plus ethanol or water And ethanol, make that the mixeding liquid volume is the leaching liquid volume 1/5~1/20, and in the mixed liquor ethanol volume basis Content is 60~100%, and the precipitation produced in removing mixed liquor obtains filtrate;Water and ethanol dilution filtrate are used again, obtain Fructus Camptothecae Acuminatae thick Extract enters sample liquid;
The solid-liquid ratio of the Fructus Camptothecae Acuminatae raw material and solvent is 1g: 10mL~1g: 20mL;The volume hundred of ethanol in the solvent Content is divided to be 50~100%, balance of water;
The Fructus Camptothecae Acuminatae crude extract enter vincoside-lactam in sample liquid concentration be 0.1~3mg/mL, the volumn concentration of ethanol For 40~65%;
(2) vincoside-lactam is purified with SMBC
1) SMBC separation conditions are as follows:
Chromatographic column:3~10;
Fixing phase:Octadecylsilane chemically bonded silica ODS, 10~60 μm;
Operational mode:Three band SMBC are set, and three bands include elution band, refined band and absorption band, and a is elution band chromatographic column number Mesh, 1≤a≤2;B is refined band chromatographic column number, 1≤b≤4;C is absorption band chromatographic column number, and 1≤c≤4, operational mode are used A-b-c is represented;
Flowing phase composition:Mobile phase P of elution band is ethanol and the mixed solution or ethanol of water, ethanol in mobile phase P Volumn concentration is 50~100%;Mobile phase D of refined band and absorption band is ethanol and the mixed solution of water, the body of ethanol Product percentage composition is 50~70%;
Flow rate of mobile phase:In refined band and absorption band, eluent D flow velocity QDFor 1~10 times of column volume, i.e., 1 per hour ~10BV/h, as eluent D flow velocity QDUnit is mL/min, and chromatograph column radius r units are cm, and column's length L units are cm When, then 1 BV/h is equivalent to 60QD/(πr2L);Enter sample liquid F flow velocity QFFor 0.1QD~1.0QD, raffinate R flow velocity QR=QD+QF; In elution band, eluent P flow velocity QpFor 0.5QD~2QD, extract E flow velocity QE=Qp
Switching time TS:8~20min;
Simulation moving bed operation temperature:Room temperature;
2) SMBC separation processes are as follows:
SMBC separation is carried out under above-mentioned SMBC working condition, Fructus Camptothecae Acuminatae crude extract sample introduction is continuously pumped into by material liquid entrance Liquid, SMBC automatic control systems press switching time TSAlong mobile phase direction by eluent entrance, extract export, material liquid entrance Next root chromatogram column is moved to successively simultaneously with the position of raffinate outlet, removes various front impurity from raffinate R outlets, from extraction Take liquid E outlets and obtain vincoside-lactam extract;
(3) post processing is carried out to extract
Vincoside-lactam extract will be contained and be concentrated into muddiness, stratification will discard upper strata milky white liquid, with distilled water to lower floor Precipitation is cleaned, until cleanout fluid is colourless;Wedding fruits glycoside product is obtained to lower sediment recrystallization with ethanol again.
A kind of method of above-mentioned purification vincoside-lactam, can substitute ethanol as solvent or mobile phase with methanol.
It is of the invention compared with existing preparative hplc isolation technics, which significantly has the beneficial effect that:
1st, in the present invention, pre-treatment of the ethanol-water solution to Fructus Camptothecae Acuminatae raw material fully can be removed into sample liquid insoluble matter, it is ensured that The stable operation of SMBC, the extract obtained by SMBC can obtain highly purified vincoside-lactam in conjunction with post processing, and purity is higher than 98%.
2nd, the present invention being capable of scale, sane, continuous, automatic, the efficiently purification happiness from Fructus Camptothecae Acuminatae using SMBC technologies Fruit glycosides, in the extract of SMBC, product recovery rate is higher than 90% higher than 99%, HPLC purity, and fixing phase and mobile phase can be anti- It is multiple to utilize, cost for purification is reduced, belongs to environmental protection separation process.
Description of the drawings
In Fig. 1, embodiment 1, Fructus Camptothecae Acuminatae enters the HPLC spectrograms of sample liquid.
Three band SMBC systems in Fig. 2, embodiment 1.
The three HPLC spectrograms with SMBC raffinates in Fig. 3, embodiment 1.
The three HPLC spectrograms with SMBC extracts in Fig. 4, embodiment 1.
The HPLC spectrograms of post-treated wedding fruits glycoside product in Fig. 5, embodiment 1.
The crystal scanning electron microscope (SEM) photograph of post-treated wedding fruits glycoside product in Fig. 6, embodiment 1.
Specific embodiment
A kind of method of purification vincoside-lactam, comprises the steps:
(1) prepare Fructus Camptothecae Acuminatae crude extract
After Fructus Camptothecae Acuminatae raw material is smashed, leached 1-3 time with solvent, obtain leaching liquid;After leaching liquid is concentrated, plus ethanol or water And ethanol, make that the mixeding liquid volume is the leaching liquid volume 1/5~1/20, and in the mixed liquor ethanol volume basis Content is 60~100%, and the precipitation produced in removing mixed liquor obtains filtrate;Water and ethanol dilution filtrate are used again, obtain Fructus Camptothecae Acuminatae thick Extract enters sample liquid;
The solid-liquid ratio of the Fructus Camptothecae Acuminatae raw material and solvent is 1g: 10mL~1g: 20mL, and in solvent, the volume basis of ethanol contain Measure as 50~100%, balance of water;
The Fructus Camptothecae Acuminatae crude extract enter vincoside-lactam in sample liquid concentration be 0.1~3mg/mL, the volumn concentration of ethanol For 40~65%;
(2) vincoside-lactam is purified with SMBC
1) SMBC separation conditions are as follows:
Chromatographic column:3~10;
Fixing phase:Octadecylsilane chemically bonded silica ODS, 10~60 μm;
Operational mode:Three band SMBC are set, and three bands include elution band, refined band and absorption band, and a is elution band chromatographic column number Mesh, 1≤a≤2;B is refined band chromatographic column number, 1≤b≤4;C is absorption band chromatographic column number, and 1≤c≤4, operational mode are used A-b-c is represented;
Flowing phase composition:Mobile phase P of elution band is ethanol and the mixed solution or ethanol of water, ethanol in mobile phase P Volumn concentration is 50~100%;Mobile phase D of refined band and absorption band is ethanol and the mixed solution of water, the body of ethanol Product percentage composition is 50~70%;
Flow rate of mobile phase:In refined band and absorption band, eluent D flow velocity QDFor 1~10 times of column volume, i.e., 1 per hour ~10BV/h, as eluent D flow velocity QDUnit is mL/min, and chromatograph column radius r units are cm, and column's length L units are cm When, then 1 BV/h is equivalent to 60QD/(πr2L);Enter sample liquid F flow velocity QFFor 0.1QD~1.0QD, raffinate R flow velocity QR=QD+QF; In elution band, eluent P flow velocity QpFor 0.5QD~2QD, extract E flow velocity QE=Qp
Switching time TS:8~20min;
Simulation moving bed operation temperature:Room temperature;
2) SMBC separation processes are as follows:
SMBC separation is carried out under above-mentioned SMBC working condition, Fructus Camptothecae Acuminatae crude extract sample introduction is continuously pumped into by material liquid entrance Liquid, SMBC automatic control systems press switching time TSAlong mobile phase direction by eluent entrance, extract export, material liquid entrance Next root chromatogram column is moved to successively simultaneously with the position of raffinate outlet, removes various front impurity from raffinate R outlets, from extraction Take liquid E outlets and obtain vincoside-lactam extract;
(3) post processing is carried out to extract
Vincoside-lactam extract will be contained and be concentrated into muddiness, stratification will discard upper strata milky white liquid, with distilled water to lower floor Precipitation is cleaned, until cleanout fluid is colourless;Wedding fruits glycoside product is obtained to lower sediment recrystallization with ethanol again.
A kind of method of above-mentioned purification vincoside-lactam, can substitute ethanol as solvent or mobile phase with methanol.
The detection method method of vincoside-lactam is:
High performance liquid chromatograph:Agilent 1200;Analysis chromatographic column:Extend-C18,5 μm, 150mm × 4.6mm I.D.;Mobile phase:V (methanol): V (water)=60: 40;Detection wavelength:256nm flow velocitys:1.2mL/min;Column temperature:25℃.By liking Fruit glycosides standard substance are demarcating the content of prepare liquid vincoside-lactam.
The present invention is described in detail with embodiment below in conjunction with the accompanying drawings.
Embodiment 1
1st, prepare Fructus Camptothecae Acuminatae crude extract
The Fructus Camptothecae Acuminatae raw material of 100g crushing is taken, adds 1L ethanol, supersonic leaching 2 times at 60 DEG C to leach 60min every time, Obtain leaching liquid;Then leaching liquid is concentrated into into 75mL, plus 25mLH2O, stratification remove the precipitation that the mixed liquor is produced, Take filtrate;Filtrate is diluted with water-ethanol (volume ratio 5: 5), obtain Fructus Camptothecae Acuminatae crude extract enters sample liquid, wherein, vincoside-lactam concentration is 0.56mg/mL, its chromatographic purity are 23.79%, see Fig. 1.
2nd, vincoside-lactam is purified with SMBC from Fructus Camptothecae Acuminatae crude extract
1) SMBC separation conditions are as follows:
Chromatographic column:6, diameter 1cm, long 20cm;
Fixing phase:Octadecylsilane chemically bonded silica ODS, 20~30 μm;
Operational mode:1-3-2, i.e. elution band:1 root chromatogram column;Refined band:3 root chromatogram columns;Absorption band:2 root chromatogram columns, As shown in Figure 2;
Flowing phase composition:Mobile phase P of elution band is 95% ethanol;Refined band and absorption band mobile phase D be ethanol with The mixed solution of water, the volumn concentration of ethanol is 60%;
Flow rate of mobile phase:In elution band, eluent P flow velocity QpFor 1.5mL/min, extract E flow velocity QE=Qp;In essence In band processed and absorption band, eluent D flow velocity QDFor 1.53mL/min, enter sample liquid F flow velocity QFFor 0.29mL/min, raffinate R flow velocitys QR=QD+QF
Switching time:9.3min;
Simulation moving bed operation temperature:Room temperature;
2) SMBC separation processes are as follows:
SMBC separation is carried out under above-mentioned SMBC working condition, entering for Fructus Camptothecae Acuminatae crude extract is pumped into by material liquid entrance continuously Sample liquid, SMBC automatic control systems press switching time TSEluent entrance, extract are exported along mobile phase direction, material liquid enters The position of mouth and raffinate outlet is moved to next root chromatogram column simultaneously successively, removes various front impurity from raffinate R outlets, extracts Extraction raffinate HPLC spectrogram obtains vincoside-lactam extract as shown in figure 3, exporting from extract E, the chromatographic purity of vincoside-lactam in extract For 91.56%, yield 99.28%, extract HPLC spectrograms are as shown in Figure 4.
3rd, post processing is carried out to extract
Vincoside-lactam extract will be contained and be concentrated into muddiness, stratification will discard upper strata milky white liquid, with distilled water to lower floor Precipitation is cleaned, until solution is colourless, with ethanol to precipitating three recrystallization, obtains the vincoside-lactam that chromatographic purity is 99.1% Product, its HPLC spectrogram is as shown in figure 5, the stereoscan photograph of its pattern is shown in Fig. 6.
Embodiment 2
In addition to the description below, other conditions are with step with embodiment 1;
Prepare Fructus Camptothecae Acuminatae crude extract and enter sample liquid:After 100g Fructus Camptothecae Acuminatae is crushed, with the mixing of ethanol and water (volume ratio 7: 3) At 60 DEG C of solution, supersonic leaching is secondary, and each supersonic leaching 60min, solid-liquid ratio 1: 15 obtain leaching liquid;After leaching liquid dense doing Plus ethanol and water (volume ratio 7: 3) 100mL, mixed liquor is obtained, the precipitation of mixed liquor is removed, is taken filtrate;With ethanol and water (volume Than 5: filtrate is diluted 5), obtain Fructus Camptothecae Acuminatae crude extract enters sample liquid, wherein, the concentration of vincoside-lactam is 1.14mg/mL.
Vincoside-lactam extract is obtained from SMBC extracts E outlets, the chromatographic purity and yield of vincoside-lactam are respectively 91.07% With 99.34%.
Post processing is carried out to extract and obtains the wedding fruits glycoside product that chromatographic purity is 98.80%.
Embodiment 3
In addition to the description below, other conditions are with step with embodiment 1;
Prepare Fructus Camptothecae Acuminatae crude extract and enter sample liquid:After 100g Fructus Camptothecae Acuminatae is crushed, with the mixing of ethanol and water (volume ratio 7: 3) Solution supersonic leaching is secondary, and each supersonic leaching 60min, solid-liquid ratio 1: 15 obtain leaching liquid;Leaching liquid it is dense it is dry after plus ethanol with Water (volume ratio 6: 4) 150mL, obtains mixed liquor, removes the precipitation of mixed liquor, obtains filtrate;It is dilute with ethanol and water (volume ratio 6: 4) Filtrate is released, obtain Fructus Camptothecae Acuminatae crude extract enters sample liquid, wherein, the concentration of vincoside-lactam is 1.0mg/mL.
Chromatographic column:4, diameter 2cm, long 20cm;
Fixing phase:Octadecylsilane chemically bonded silica ODS, 30~40 μm;
Operational mode:1-1-2;
Eluent P flow velocity QpFor 6mL/min, extract E flow velocity QE=Qp;Eluent D flow velocity QDFor 6mL/min, enter sample liquid F flow velocity QFFor 1.2mL/min, raffinate R flow velocity QR=QD+QF
Export from SMBC extracts E, obtain vincoside-lactam extract, vincoside-lactam chromatographic purity 91.90%, the response rate 99.50%.
Post processing is carried out to extract and obtains the wedding fruits glycoside product that chromatographic purity is 98.85%.

Claims (4)

1. it is a kind of purification vincoside-lactam method, it is characterised in that comprise the steps:
(1) prepare Fructus Camptothecae Acuminatae crude extract
After Fructus Camptothecae Acuminatae raw material is smashed, leached 1-3 time with solvent, obtain leaching liquid;After leaching liquid is concentrated, plus ethanol or water and second Alcohol, make that the mixeding liquid volume is the leaching liquid volume 1/5~1/20, and in the mixed liquor ethanol volumn concentration For 60~100%;The precipitation produced in removing mixed liquor, obtains filtrate;Water and ethanol dilution filtrate are used again, obtain Fructus Camptothecae Acuminatae crude extract Enter sample liquid;
(2) vincoside-lactam is purified with simulated moving bed chromatography abbreviation SMBC
1) SMBC separation conditions are as follows:
Chromatographic column:3~10;
Fixing phase:Octadecylsilane chemically bonded silica ODS, 10~60 μm;
Operational mode:Three band SMBC are set, and three bands include elution band, refined band and absorption band, a is elution band chromatographic column number, 1 ≤a≤2;B is refined band chromatographic column number, 1≤b≤4;C is absorption band chromatographic column number, 1≤c≤4, operational mode a-b- C is represented;
Flowing phase composition:Mobile phase P of elution band is ethanol and the mixed solution or ethanol of water, the volume of ethanol in mobile phase P Percentage composition is 50~100%;Mobile phase D of refined band and absorption band is ethanol and the mixed solution of water, the volume hundred of ethanol Content is divided to be 50~70%;
Flow rate of mobile phase:In refined band and absorption band, eluent D flow velocity QDFor 1~10 times of column volume per hour, enter sample liquid F stream Fast QFFor 0.1QD~1.0QD, raffinate R flow velocity QR=QD+QF;In elution band, eluent P flow velocity QpFor 0.5QD~2QD, extraction Take liquid E flow velocity QE=Qp
Switching time TS:8~20min;
Simulation moving bed operation temperature:Room temperature;
2) SMBC separation processes are as follows:
SMBC separation is carried out under above-mentioned SMBC working condition, Fructus Camptothecae Acuminatae crude extract is continuously pumped into by material liquid entrance and is entered sample liquid, SMBC automatic control systems press switching time TSAlong mobile phase direction by eluent entrance, extract export, material liquid entrance and The position of raffinate outlet is moved to next root chromatogram column simultaneously successively, removes various front impurity from raffinate R outlets, from extraction Liquid E outlets obtain vincoside-lactam extract;
(3) post processing is carried out to extract
Vincoside-lactam extract is concentrated into into muddiness, stratification discards upper strata milky white liquid, lower sediment entered with distilled water Row cleaning, until cleanout fluid is colourless;Wedding fruits glycoside product is obtained to lower sediment recrystallization with ethanol again.
2. it is according to claim 1 it is a kind of purification vincoside-lactam method, it is characterised in that in the step (1), Fructus Camptothecae Acuminatae The solid-liquid ratio of raw material and solvent is 1g: 10mL~1g: 20mL;In the solvent, the volumn concentration of ethanol is 50~100%, Balance of water.
3. it is according to claim 1 it is a kind of purification vincoside-lactam method, it is characterised in that in the step (1), Fructus Camptothecae Acuminatae It is 0.1~3mg/mL that crude extract enters the concentration of vincoside-lactam in sample liquid, and the volumn concentration of ethanol is 40~65%.
4. the method for a kind of purification vincoside-lactam according to claims 1 to 3 any one, it is characterised in that replaced by methanol For ethanol as solvent or mobile phase.
CN201610971856.2A 2016-11-07 2016-11-07 Method for purifying vincoside-lactam Active CN106518940B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610971856.2A CN106518940B (en) 2016-11-07 2016-11-07 Method for purifying vincoside-lactam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610971856.2A CN106518940B (en) 2016-11-07 2016-11-07 Method for purifying vincoside-lactam

Publications (2)

Publication Number Publication Date
CN106518940A true CN106518940A (en) 2017-03-22
CN106518940B CN106518940B (en) 2020-09-01

Family

ID=58326135

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610971856.2A Active CN106518940B (en) 2016-11-07 2016-11-07 Method for purifying vincoside-lactam

Country Status (1)

Country Link
CN (1) CN106518940B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1634951A (en) * 2004-11-25 2005-07-06 南开大学 Process for extracting camptothecin
CN101313914A (en) * 2007-05-29 2008-12-03 江苏康缘药业股份有限公司 Uses and preparations of common camptotheca fruit glycosides of common camptotheca fruit extract
CN103936816A (en) * 2014-04-14 2014-07-23 辽宁科技大学 Method for purifying tanshinone IIA in salvia miltiorrhiza crude extract through simulated moving bed chromatography

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1634951A (en) * 2004-11-25 2005-07-06 南开大学 Process for extracting camptothecin
CN101313914A (en) * 2007-05-29 2008-12-03 江苏康缘药业股份有限公司 Uses and preparations of common camptotheca fruit glycosides of common camptotheca fruit extract
CN103936816A (en) * 2014-04-14 2014-07-23 辽宁科技大学 Method for purifying tanshinone IIA in salvia miltiorrhiza crude extract through simulated moving bed chromatography

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
史伟国,等: "聚酰胺分离纯化喜树果中10-羟基喜树碱和喜果苷的研究", 《中国中药杂志》 *
张志远,等: "自动纯化系统纯化和制备胆木中4种生物碱类化合物", 《中华中医药杂志》 *
欧来良,等: "树脂法分离纯化喜树果中喜果苷的研究", 《中草药》 *
王瑞芳,等: "大孔吸附树脂对喜树果中喜树碱和喜果苷的分离纯化研究", 《中草药》 *

Also Published As

Publication number Publication date
CN106518940B (en) 2020-09-01

Similar Documents

Publication Publication Date Title
JP2022510832A (en) Separation and purification method of cannabidiol by high-speed countercurrent chromatography
CN1974527B (en) Process of preparing high purity chlorogenic acid and flavonid with eucommia leaf
CN1321961C (en) New method for picking-up purified resveratrol from giant knotweed
CN101314568B (en) Novel method for adsorption separation of high purity chlorogenic acid
CN108383890B (en) Preparation method of high-content ginsenoside Re extract
CN106749448B (en) A kind of method that Simulated Moving Bed Chromatography method extracts steviol glycoside in STEVIA REBAUDIANA
CN102001947A (en) Method for preparing honeysuckle chlorogenic acid
CN108176079B (en) A method for decolorizing Glycyrrhrizae radix extract
EP2650301A1 (en) Method for preparing albiflorin and paeoniflorin
CN113398157A (en) Method for continuously extracting and separating multiple natural active ingredients from momordica grosvenori flower
CN102924537A (en) Method for preparing hyperoside and isoquercitrin simultaneously from dogbane leaves
CN110669096B (en) Method for preparing astragaloside from astragalus
US10301341B2 (en) Technology for extracting and preparing high-purity raffinose from defatted wheat germ
CN105111061B (en) A kind of preparation method of active compound for anti tumor
CN106674312A (en) Separation and purification method for high-purity monomer sweroside series components
CN102920727B (en) Method for preparing extracts rich in vitexin rhamnoside and vitexin glucoside
CN106518940A (en) Method for purifying vincoside lactam
CN101353294A (en) Separation and purification method of high-content resveratrol
CN114702469A (en) Method for extracting, separating and purifying 4 phthalides lactones from ligusticum wallichii
CN108440619A (en) The method that cornel extractive prepares high-purity horse loganin
CN106046098B (en) A kind of acetyl group ginsenoside Rd and preparation method thereof
CN102432420A (en) Method for extracting and separating beta-elemene from Lantana camara
CN102389456A (en) Method for extracting isodon japonica var.galaucocalyx total diterpenoids or Glaucocalyxin A
CN105273015A (en) Preparation method of high-purity paeoniflorin and albiflorin
CN109021045A (en) The method for separating hemp glycosides, Yi Quercetin skin glycosides and chlorogenic acid simultaneously in largeleaf poacynum leaf leaf

Legal Events

Date Code Title Description
C06 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