CN111635451A - Process for refining tanshinone IIA by multistage countercurrent extraction method - Google Patents

Process for refining tanshinone IIA by multistage countercurrent extraction method Download PDF

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Publication number
CN111635451A
CN111635451A CN202010515755.0A CN202010515755A CN111635451A CN 111635451 A CN111635451 A CN 111635451A CN 202010515755 A CN202010515755 A CN 202010515755A CN 111635451 A CN111635451 A CN 111635451A
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China
Prior art keywords
phase
tanshinone iia
countercurrent extraction
multistage countercurrent
extraction
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CN202010515755.0A
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Chinese (zh)
Inventor
吴学文
谢欢欢
史姣雯
欧阳小玉
粟寒星
李维
曹旭媛
熊艳
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Xiangtan University
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Xiangtan University
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Priority to CN202010515755.0A priority Critical patent/CN111635451A/en
Publication of CN111635451A publication Critical patent/CN111635451A/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J73/00Steroids in which the cyclopenta[a]hydrophenanthrene skeleton has been modified by substitution of one or two carbon atoms by hetero atoms
    • C07J73/001Steroids in which the cyclopenta[a]hydrophenanthrene skeleton has been modified by substitution of one or two carbon atoms by hetero atoms by one hetero atom
    • C07J73/003Steroids in which the cyclopenta[a]hydrophenanthrene skeleton has been modified by substitution of one or two carbon atoms by hetero atoms by one hetero atom by oxygen as hetero atom

Abstract

The invention discloses a process for refining tanshinone IIA by a multistage countercurrent extraction method. The preparation method comprises the following steps: suspending the red sage root coarse powder in an aqueous solution (phase B) to a certain concentration, placing the red sage root coarse powder in a multistage countercurrent extraction tank, taking an organic solvent as an extraction phase (phase S), adjusting the flow rate of the phase S and the phase B, extracting tanshinone IIA in the red sage root by using a multistage countercurrent extraction mode, recovering an S phase solvent to obtain red solid, namely the tanshinone IIA coarse powder. The invention adopts a multi-stage countercurrent extraction process, ensures that all materials are fully contacted with the solvent, keeps larger concentration difference, accelerates the extraction rate and saves the dosage of the solvent. In addition, the operation temperature is room temperature, so that the thermal instability components are not decomposed, the energy consumption is saved, the extraction cost is reduced, and the extraction efficiency of the tanshinone IIA is improved.

Description

Process for refining tanshinone IIA by multistage countercurrent extraction method
Technical Field
The invention belongs to the technical field of natural extract extraction and the field of medicines, and particularly relates to a process for refining tanshinone IIA by using a multistage countercurrent extraction method, which is applied to the field of medical health.
Background
Salvia miltiorrhiza is the dried root and rhizome of Salvia miltiorrhiza belonging to Labiatae, and is the most common Chinese medicine for promoting blood circulation and removing blood stasis in clinic. Salvia miltiorrhiza also has the effects of stimulating menstrual flow, relieving pain, clearing away heart-fire, relieving restlessness, cooling blood and resolving carbuncle. The salvia miltiorrhiza is applied to Chinese patent medicine preparations for treating cardiovascular diseases, such as tablets, capsules, granules and injection, has the functions of expanding blood vessels, reducing blood pressure and resisting thrombus, and has obvious curative effects on treating coronary heart disease, angina and tachycardia. Wherein tanshinone IIA is dissolved in organic solvent such as ethanol, acetone, diethyl ether, benzene, etc., and is slightly soluble in water. The extraction of tanshinone IIA has attracted great attention, and although a large number of literature reports exist on the extraction of tanshinone IIA, how to greatly improve the purity of tanshinone IIA is not high, which is the direction of development and research of related technicians.
In clinical practice, the traditional Chinese medicine salvia miltiorrhiza has been widely applied to the treatment of cardiovascular and cerebrovascular diseases and stroke diseases. Tanshinone IIA has potential therapeutic effect on cardiovascular disease, cerebrovascular disease, tumor, leukemia, etc.
Aiming at the low content of tanshinone IIA extracted from Salvia miltiorrhiza, the invention provides a process for refining tanshinone IIA by using a multi-stage countercurrent extraction method.
Disclosure of Invention
Aiming at the low content of tanshinone IIA extracted from Salvia miltiorrhiza, the invention provides a process for refining tanshinone IIA by using a multi-stage countercurrent extraction method.
The invention is realized by adopting the following technical scheme:
a process for refining tanshinone IIA by using a multistage countercurrent extraction method comprises the following steps: suspending Saviae Miltiorrhizae radix coarse powder in aqueous solution (phase B), placing into a multistage countercurrent extraction tank, taking organic solvent as extractant (phase S), adjusting flow rate of phase S and phase B, extracting and purifying tanshinone IIA in Saviae Miltiorrhizae radix by multistage countercurrent extraction, recovering solvent of phase S, and obtaining red solid.
In order to detect the content of tanshinone IIA in the tanshinone IIA extract, the content and purity of the extract are measured by the method, and the measuring method comprises the following steps:
chromatographic conditions and system applicability test, the chromatographic column is ODSC18 column; water-acetonitrile (20: 80) is used as a mobile phase; the detection wavelength is 272 nm; flow rate: 1.0 mL/min.
Preparation of a reference stock solution: accurately weighing 10.0 mg of tanshinone IIA reference substance dried under reduced pressure for 24 h, placing in a 10 mL brown volumetric flask, adding mobile phase for dissolving, fixing volume to scale, and shaking to obtain tanshinone IIA reference substance stock solution.
And (3) sample determination: precisely sucking 20 μ L of sample solution, injecting into high performance liquid chromatograph, and measuring by the method.
The invention has the following advantages:
the invention adopts the countercurrent extraction process, maintains larger concentration difference, increases the extraction driving force, accelerates the extraction rate, saves the solvent consumption, has low extraction temperature, ensures that the thermal unstable components are not decomposed by low-temperature extraction, saves energy consumption, greatly reduces the extraction cost, improves the concentration of the effective components in the final solvent, and improves the extraction efficiency of the tanshinone IIA. The organic solvent is adopted for extraction, so that the workload of subsequent separation and concentration procedures is reduced, the production period of products is shortened, the labor production efficiency is greatly improved, and the energy consumption is reduced.
Compared with the prior art, the method for purifying the tanshinone IIA extract disclosed by the invention is different from the method for purifying the tanshinone IIA extract by adopting resin purification or preparative chromatography and the like reported in general literatures, has the advantages of simplicity and effectiveness in operation, easiness in industrialization and the like, and can effectively avoid the use of organic reagents which are toxic and harmful to human bodies. The purified tanshinone II A extract is more beneficial to exerting the pharmacological activity and eliminating the side effect of ineffective impurities.
The invention adopts low-cost organic solvent as the purification reagent, improves the content of tanshinone IIA higher than other reagents, and greatly reduces the process cost.
Detailed Description
The following examples are intended to further illustrate the invention, but are not intended to limit the invention.
Example 1
A process for refining tanshinone IIA by using a multistage countercurrent extraction method comprises the following steps: taking 20 mg/ml of salvia miltiorrhiza coarse powder aqueous solution in a primary countercurrent extractor, wherein the flow rate of S phase is as follows: phase B flow rate =1: 1. Recovering solvent from S phase, drying to obtain red solid, and measuring tanshinone II A content in coarse powder to be 1.60% and refined tanshinone II A purity to be 19.44% by high performance liquid chromatography.
Example 2
A process for refining tanshinone IIA by using a multistage countercurrent extraction method comprises the following steps: suspending l radix Salviae Miltiorrhizae coarse powder in 1% sodium bicarbonate water solution, wherein the concentration of radix Salviae Miltiorrhizae coarse powder is 30 mg/ml, placing in a two-stage countercurrent extractor, selecting ethyl acetate as S phase, and the flow rate of S phase is as follows: b phase flow rate =1: 5. Recovering solvent from S phase, drying to obtain red solid, determining tanshinone II A content in coarse powder to be 1.60% by high performance liquid chromatography, and refined tanshinone II A purity to be 31.00%.
Example 3
A process for refining tanshinone IIA by using a multistage countercurrent extraction method comprises the following steps: suspending l red sage root coarse powder in 5% sodium bicarbonate water solution, wherein the concentration of the red sage root coarse powder is 50 mg/ml, placing the red sage root coarse powder in a three-stage countercurrent extractor, selecting ethyl acetate as an S phase, and the flow rate of the S phase is as follows: b phase flow rate =3: 2. Recovering solvent from S phase, drying to obtain red solid, determining tanshinone II A content in coarse powder to be 1.60% by high performance liquid chromatography, and refined tanshinone II A purity to be 59.06%.

Claims (6)

1. A process for refining tanshinone IIA by a multistage countercurrent extraction method is characterized by comprising the following steps: suspending Saviae Miltiorrhizae radix coarse powder in water solution (B phase) to a certain concentration, placing in a countercurrent extraction tank, adjusting flow rate of S phase and B phase with organic solvent as extractant (S phase), extracting tanshinone IIA in Saviae Miltiorrhizae radix by multistage countercurrent extraction process, volatilizing solvent, and drying to obtain red solid.
2. The process for refining tanshinone IIA by multistage countercurrent extraction as claimed in claim 1, wherein: the concentration of the red sage root coarse powder is 5-100 mg/mL.
3. The process for refining tanshinone IIA by multistage countercurrent extraction as claimed in claim 1, wherein: the S phase is organic solvent immiscible with water, such as ethyl acetate, chloroform, dichloromethane, n-butanol, etc., preferably ethyl acetate.
4. The process for refining tanshinone IIA by multistage countercurrent extraction as claimed in claim 1, wherein: the phase B solvent is water or alkaline aqueous solution, such as tap water, purified water, sodium bicarbonate aqueous solution, sodium carbonate aqueous solution, sodium hydroxide aqueous solution, lime aqueous solution, etc., preferably alkaline aqueous solution.
5. The process for refining tanshinone IIA by multistage countercurrent extraction as claimed in claim 1, wherein: the phase ratio is S phase (extractant): phase B (crude solvent) =1:5-5: 1.
6. The process for refining tanshinone IIA by multistage countercurrent extraction as claimed in claim 1, wherein: the countercurrent extraction mode is multistage, and the stage number can be single stage, two stages, three stages, four seasons, five stages and the like.
CN202010515755.0A 2020-06-09 2020-06-09 Process for refining tanshinone IIA by multistage countercurrent extraction method Pending CN111635451A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101073599A (en) * 2007-06-18 2007-11-21 石任兵 Total tanshinone and total phenolic acid extract in red-rooted salvia root and its production
CN103479723A (en) * 2013-08-21 2014-01-01 浙江中医药大学 Diterpenoid tanshinone effective part and countercurrent chromatography preparation method and cancer treatment application thereof
CN103665094A (en) * 2013-10-22 2014-03-26 南京慧博生物科技有限公司 Preparation method for extracting and purifying tanshinone monomeric compounds from red sage root
CN109248467A (en) * 2018-10-30 2019-01-22 安阳晶森生物科技有限公司 A kind of technique extracting total-tanshinone from Radix Salviae Miltiorrhizae
CN110063981A (en) * 2019-05-14 2019-07-30 西南医科大学 A kind of technique and its application preparing total-tanshinone from Radix Salviae Miltiorrhizae

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101073599A (en) * 2007-06-18 2007-11-21 石任兵 Total tanshinone and total phenolic acid extract in red-rooted salvia root and its production
CN103479723A (en) * 2013-08-21 2014-01-01 浙江中医药大学 Diterpenoid tanshinone effective part and countercurrent chromatography preparation method and cancer treatment application thereof
CN103665094A (en) * 2013-10-22 2014-03-26 南京慧博生物科技有限公司 Preparation method for extracting and purifying tanshinone monomeric compounds from red sage root
CN109248467A (en) * 2018-10-30 2019-01-22 安阳晶森生物科技有限公司 A kind of technique extracting total-tanshinone from Radix Salviae Miltiorrhizae
CN110063981A (en) * 2019-05-14 2019-07-30 西南医科大学 A kind of technique and its application preparing total-tanshinone from Radix Salviae Miltiorrhizae

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Title
杨志伟 等: "丹参中丹参酮ⅡA和隐丹参酮的提取纯化工艺", 《扬州大学学报(自然科学版)》 *
苏会东等: "《水污染控制工程》", 31 May 2017, 中国建材工业出版社 *

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