CN106045890A - A stachydrine preparing method - Google Patents

A stachydrine preparing method Download PDF

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Publication number
CN106045890A
CN106045890A CN201610306944.0A CN201610306944A CN106045890A CN 106045890 A CN106045890 A CN 106045890A CN 201610306944 A CN201610306944 A CN 201610306944A CN 106045890 A CN106045890 A CN 106045890A
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CN
China
Prior art keywords
stachydrine
extract
crude extract
component
supercritical fluid
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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.)
Pending
Application number
CN201610306944.0A
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Chinese (zh)
Inventor
杨成东
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Nanjing Zelang Medical Technology Co Ltd
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Nanjing Zelang Medical Technology Co Ltd
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Application filed by Nanjing Zelang Medical Technology Co Ltd filed Critical Nanjing Zelang Medical Technology Co Ltd
Priority to CN201610306944.0A priority Critical patent/CN106045890A/en
Publication of CN106045890A publication Critical patent/CN106045890A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D207/00Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D207/02Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
    • C07D207/04Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members
    • C07D207/10Heterocyclic compounds containing five-membered rings not condensed with other rings, with one nitrogen atom as the only ring hetero atom with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having no double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D207/16Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Medicines Containing Plant Substances (AREA)

Abstract

The invention relates to a stachydrine preparing method simple in operation and low in pollution. The method includes (1) adding crushed motherwort herb powder into a supercritical fluid extraction device, and performing supercritical fluid extraction to obtain an extract liquid, (2) allowing the extract liquid to pass through a membrane separation system, concentrating and drying to obtain a crude extract product, (3) separating and purifying stachydrine in the crude extract product through preparative liquid chromatography, monitoring on line with ultraviolet, and collecting the stachydrine component, and (4) subjecting the stachydrine component to vacuum concentration, and crystallizing with methanol to obtain the stachydrine. The stachydrine prepared by the method is high in product purity and prone to industrial scale-up.

Description

A kind of preparation method of stachydrine
Technical field
The invention belongs to Chinese medicine extraction separation technology field, relate to a kind of from Herba Leonuri separation prepare the side of stachydrine Method.
Background technology
Stachydrine, also known as proline glycine betaine, is simplest pyrrolidine alkaloid, for white, needle-shaped crystals, is dissolved in water, first Alcohol, ethanol, diluted acid, hot chloroform, be practically insoluble in ether, acetone, cold chloroform and petroleum ether.Stachydrine is medicinal plants Herba Leonuri One of main active, have good medical value, there is excited uterus, improve hemorheology, antithrombotic effect.
Herba Leonuri is the fresh or dry aerial parts of Labiatae mother wort plant, original name motherwort, another name Herba Leonuri Chinese mugwort, hardship Grass, Herba Leonuri etc., its acrid in the mouth, micro-hardship, cold nature, enter pericardium, Liver Channel, there is invigorate blood circulation the tune stasis of blood, effect of inducing diuresis to remove edema.Clinically Treatment for diseases such as menoxenia, stasis of blood pain in puerperal, cardiovascular and cerebrovascular disease, hematopathys.
At present, the purification process of stachydrine is rarely found, not yet finds to be suitable for preparing in a large number the industrial method of stachydrine Patent or document report.
Summary of the invention
It is an object of the invention to provide the preparation method of a kind of stachydrine.
The present invention is achieved by the following technical programs:
(1) will pulverize after Herba Leonuri powder be placed in supercritical fluid extraction equipment, with account for total extractant volume 4% second Alcohol is entrainer, is passed through CO2, at extracting pressure 20~30MPa, extraction temperature 40~50 DEG C, CO2Flow velocity be 20~30L/h Under the conditions of extract, collect extract;
(2) it is the nanofiltration of 300 by extract by ultrafilter membrane ultrafiltration and the molecular cut off that molecular cut off is 2000~3000 Membrance concentration, operation pressure is 0.7~1.5MPa, and vacuum drying obtains crude extract;
(3) using the stachydrine in the isolated and purified crude extract of preparative liquid chromatography, on-line ultraviolet is monitored, and collects stachydrine group Point;
(4) stachydrine component is concentrated in vacuo, methanol crystallization, obtains stachydrine.
In described step (3) preparative liquid chromatography with 75~82% methanol solution for flowing phase.
This method good effect is:
(1) this method uses supercritical fluid extraction, mild condition, it is to avoid traditional method localized hyperthermia is to Product Activity Adverse effect;
(2) this method uses membrane separation technique, can effectively remove plurality of impurities, and will not destroy the biological activity of effective ingredient;
(3) this method uses preparative liquid chromatography, and yield is high, preparation amount is big, manufacturing cycle is short, solves column chromatography efficiency low And with serious pollution technological deficiency;
(4) operation of this method processing step is relatively simple, easily operates, and products obtained therefrom purity is high.
Further illustrate the present invention below in conjunction with detailed description of the invention, but the scope of protection of present invention is not limited to In following embodiments.
Detailed description of the invention
Embodiment 1:
Will pulverize after Herba Leonuri powder be placed in supercritical fluid extraction equipment, with account for total extractant volume 4% ethanol be Entrainer, is passed through CO2, at extracting pressure 20MPa, extraction temperature 40 DEG C, CO2Flow velocity be to extract under conditions of 20L/h, Collect extract;It is the NF membrane of 300 by extract by ultrafilter membrane ultrafiltration and the molecular cut off that molecular cut off is 2000 Concentrating, operation pressure is 0.7MPa, vacuum drying, obtains crude extract;Use in the isolated and purified crude extract of preparative liquid chromatography Stachydrine, monitors for flowing phase, on-line ultraviolet with 75% methanol solution, collects stachydrine component;Stachydrine component is carried out vacuum Concentrating, methanol crystallization, obtain stachydrine, its purity is 96.3%.
Embodiment 2:
Will pulverize after Herba Leonuri powder be placed in supercritical fluid extraction equipment, with account for total extractant volume 4% ethanol be Entrainer, is passed through CO2, at extracting pressure 25MPa, extraction temperature 45 DEG C, CO2Flow velocity be to extract under conditions of 25L/h, Collect extract;It is the NF membrane of 300 by extract by ultrafilter membrane ultrafiltration and the molecular cut off that molecular cut off is 3000 Concentrating, operation pressure is 1.0MPa, vacuum drying, obtains crude extract;Use in the isolated and purified crude extract of preparative liquid chromatography Stachydrine, monitors for flowing phase, on-line ultraviolet with 80% methanol solution, collects stachydrine component;Stachydrine component is carried out vacuum Concentrating, methanol crystallization, obtain stachydrine, its purity is 98.1%.
Embodiment 3:
Will pulverize after Herba Leonuri powder be placed in supercritical fluid extraction equipment, with account for total extractant volume 4% ethanol be Entrainer, is passed through CO2, at extracting pressure 30MPa, extraction temperature 50 DEG C, CO2Flow velocity be to extract under conditions of 30L/h, Collect extract;It is the NF membrane of 300 by extract by ultrafilter membrane ultrafiltration and the molecular cut off that molecular cut off is 2500 Concentrating, operation pressure is 1.5MPa, vacuum drying, obtains crude extract;Use in the isolated and purified crude extract of preparative liquid chromatography Stachydrine, monitors for flowing phase, on-line ultraviolet with 82% methanol solution, collects stachydrine component;Stachydrine component is carried out vacuum Concentrating, methanol crystallization, obtain stachydrine, its purity is 97.2%.

Claims (2)

1. the preparation method of a stachydrine, it is characterised in that comprise the following steps:
(1) will pulverize after Herba Leonuri powder be placed in supercritical fluid extraction equipment, with account for total extractant volume 4% second Alcohol is entrainer, is passed through CO2, at extracting pressure 20~30MPa, extraction temperature 40~50 DEG C, CO2Flow velocity be 20~30L/h Under the conditions of extract, collect extract;
(2) it is the nanofiltration of 300 by extract by ultrafilter membrane ultrafiltration and the molecular cut off that molecular cut off is 2000~3000 Membrance concentration, operation pressure is 0.7~1.5MPa, and vacuum drying obtains crude extract;
(3) using the stachydrine in the isolated and purified crude extract of preparative liquid chromatography, on-line ultraviolet is monitored, and collects stachydrine group Point;
(4) stachydrine component is concentrated in vacuo, methanol crystallization, obtains stachydrine.
The preparation method of a kind of stachydrine the most according to claim 1, it is characterised in that preparative in described step (3) Liquid chromatograph with 75~82% methanol solution for flowing phase.
CN201610306944.0A 2016-05-11 2016-05-11 A stachydrine preparing method Pending CN106045890A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610306944.0A CN106045890A (en) 2016-05-11 2016-05-11 A stachydrine preparing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610306944.0A CN106045890A (en) 2016-05-11 2016-05-11 A stachydrine preparing method

Publications (1)

Publication Number Publication Date
CN106045890A true CN106045890A (en) 2016-10-26

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610306944.0A Pending CN106045890A (en) 2016-05-11 2016-05-11 A stachydrine preparing method

Country Status (1)

Country Link
CN (1) CN106045890A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106928115A (en) * 2017-03-29 2017-07-07 广西壮族自治区梧州食品药品检验所 A kind of method that ASE methods extract stachydrine hydrochloride in motherwort
CN108586308A (en) * 2018-06-15 2018-09-28 南京中医药大学 A kind of method that film combination refines both sexes alkaloid

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106928115A (en) * 2017-03-29 2017-07-07 广西壮族自治区梧州食品药品检验所 A kind of method that ASE methods extract stachydrine hydrochloride in motherwort
CN108586308A (en) * 2018-06-15 2018-09-28 南京中医药大学 A kind of method that film combination refines both sexes alkaloid
CN108586308B (en) * 2018-06-15 2021-06-22 南京中医药大学 Method for refining amphoteric alkaloid by membrane combination

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Application publication date: 20161026

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