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Adsorption resin method separation technology of scutellarin in fleabane flower extract

A scutellarin and adsorption resin technology, which is applied in the field of high-selectivity adsorption resin synthesis, can solve the problems of single structure, poor selectivity of adsorption and separation methods, and difficulty in meeting the requirements of purity, and achieves simple separation and purification process and improved storage stability. performance, good practical application prospects

Inactive Publication Date: 2011-08-10
NANKAI UNIV
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  • Application Information

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Problems solved by technology

However, since the commercial adsorption resin skeleton is still dominated by polystyrene, the structure is single, and the adsorption mechanism is mainly hydrophobic adsorption, which results in relatively poor selectivity of the adsorption separation method.
In the extraction and purification of breviscapine, the macroporous adsorption resin is more used as the enrichment material for the active ingredients with a lower content, and it is difficult to truly remove impurities and prepare high-purity extracts. For example, Lou Yunyan et al. discussed The feasibility of using commercial polystyrene macroporous resins to purify scutellarin, studies have shown that these resins can effectively remove some impurities, but it is difficult to prepare high-purity scutellarin (Lou Yunyan et al., static adsorption method Selection of macroporous resin for purifying breviscapine [J], Journal of Traditional Chinese Medicine, 2006, 24(6): 1129)
Zhang Renwei and others disclosed a Chinese invention patent, which used commercialized AB-8 and D101 macroporous polystyrene-type adsorption resins as separation materials for the further purification of commercially available scutellarin raw materials, and obtained a purity of about 90%. scutellarin, but in the purification process disclosed in the patent, the purity of scutellarin in the desorption solution obtained only through the resin "adsorption-desorption" one-step process is difficult to meet the requirements, and the pH value of the desorption solution still needs to be adjusted The scutellarin in it is separated out in the form of precipitation to achieve the purpose of further purification. Therefore, it is difficult to realize the continuous operation process, and the high acidity (pH=1~2) will destroy the structural stability of scutellarin
More importantly, although a large number of impurities were removed after the two-step treatment of resin adsorption and precipitation, the purity of scutellarin increased from 80% to 90%, but due to the adsorption selectivity of AB-8 or D101 resin Poor, it is difficult to realize the separation of scutellarin A and B with similar structure, so using the separation process disclosed in the patent, it is impossible to obtain a scutellarin sample with higher purity and no scutellarin (Zhang Renwei et al. Preparation method of refined scutellarin bulk drug with porous resin, application number 200710065713.6, publication number CN101037461A)

Method used

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  • Adsorption resin method separation technology of scutellarin in fleabane flower extract
  • Adsorption resin method separation technology of scutellarin in fleabane flower extract
  • Adsorption resin method separation technology of scutellarin in fleabane flower extract

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Experimental program
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Effect test

Embodiment 1

[0030] The preparation method of amide resin is realized through the following steps:

[0031] Step 1: Dissolve 4.5g of polyvinyl alcohol (PVA) and 22.5g of sodium chloride (NaCl) in water in a 1L three-necked bottle to make 500mL of aqueous solution, and heat it to 45°C. In addition, 24g of methyl acrylate, 12g of styrene, 24g of divinylbenzene, 60g of toluene, 30g of n-heptane, and 1.2g of azobisisobutyronitrile (AIBN) were evenly mixed, then added to a three-necked flask, started to stir, and at the same time, the reaction The temperature of the system was raised to 65°C for 5 hours, and the temperature was further raised to 80°C for 4 hours. Stop the reaction, filter, wash, and dry to obtain the initial adsorption resin.

[0032] The second step: add N,N-dimethylformamide (DMF) 150mL to fully swell the obtained 54.8g resin, add 20g of NH 2 (CH 2 ) 2 NH 2 , after mixing evenly, raise the temperature to 95°C, fully react for 10 hours, stop the reaction, filter and wash ...

Embodiment 2

[0034] Step 1: Dissolve 23g of polyvinyl alcohol (PVA) and 32g of sodium chloride (NaCl) in water in a 2L three-necked bottle to make 900mL of aqueous solution, and heat it to 35°C. In addition, mix 60g of methyl acrylate, 18g of styrene, 42g of divinylbenzene, 90g of toluene, 50g of liquid wax, and 1.2g of benzoyl peroxide (BPO) evenly, then add them into a three-necked bottle, start stirring, and raise the temperature of the reaction system at the same time. React at 78°C for 6 hours, then continue to raise the temperature to 90°C for 4 hours. Stop the reaction, filter and wash to obtain the initial adsorption resin.

[0035] Step 2: After adding 400mL of diethylbenzene to fully swell the obtained 108.7g resin, add 40g of NH 2 (CH 2 ) 2 NHCOCH 3 , after mixing evenly, heat up to 110°C, fully react for 8 hours, stop the reaction, filter and wash to obtain a macroporous adsorption resin with amide functional groups, which is amide resin.

Embodiment 3

[0037] Step 1: Dissolve 100g of polyvinyl alcohol (PVA) and 100g of sodium chloride (NaCl) in water in a 5L three-necked bottle to make 2000mL of aqueous solution, and heat it to 40°C. In addition, 75g methyl acrylate, 62.5g styrene, 112.5g divinylbenzene, 150g toluene, 150g of 200 # After gasoline and 7.5g of azobisisobutyronitrile (AIBN) were mixed evenly, they were added into a three-necked flask, and stirring was started. At the same time, the temperature of the reaction system was raised to 65°C for 4 hours, and then the temperature was raised to 80°C for 5 hours. Stop the reaction, filter and wash to obtain the initial adsorption resin.

[0038] Step 2: After adding 700mL of acetophenone to fully swell the obtained 225.9g resin, add 90g of NH 2 (CH 2 ) 2 NHCOCH 2 CH 3 , after mixing evenly, heat up to 120°C, fully react for 12 hours, stop the reaction, filter and wash to obtain a macroporous adsorption resin with amide functional groups, which is amide resin.

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Abstract

The invention discloses an adsorption resin method separation technology of scutellarin in a fleabane flower extract. Based on scutellarin and fleabane flower essence A which have very similar structures, the difference of intermolecular hydrogen bonding capacities is formed, an amide functional group capable of forming hydrogen bonds is introduced on a macroporous adsorption resin skeleton, highly selective adsorption is carried out on the scutellarin by the synergic action of dewatering and the hydrogen bonds, a commercially available extract is used as a raw material, and a specimen with the content of the scutellarin more than 98% and the content of the fleabane flower essence A less than 0.5% is prepared by a one-step continuous technology of adsorption and desorption. The invention avoids using a poisonous organic solvent with low boiling point and does not need the assistance of other purification methods, so that the invention has simple operation and is environment-friendly, resin can be recycled simultaneously, the production cost is greatly reduced, and the invention is suitable for large-scale industrial production. The obtained specimen can meet the requirements for further enhancing the quality standard of a breviscapine preparation, reducing clinical side reactions and the like, and the invention has favorable application prospect.

Description

【Technical field】: [0001] The invention belongs to the technical field of separation and purification of monomeric active ingredients in natural plants. In particular, the adsorption separation process of two monomer components with very similar structures in the scutellarin extract - scutellarin and scutellarin, and the synthesis method of the highly selective adsorption resin used in the separation process. 【Background technique】: [0002] Erigeron breviscapus (Vant.) Hand.Mazz. is the dry whole plant of the genus Erigeron breviscapus (Vant.) Hand.Mazz. in the family Asteraceae. It is mainly distributed in Yunnan, Guangxi and other provinces in southwest my country. . Scutellarin is the main flavonoid active ingredient in the extract of scutellarin, which has obvious protective effects on the heart, brain, liver and kidney. Various preparations using breviscapine extracts as raw materials have been widely used clinically, such as the treatment of hypertension, coronary he...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07H17/07C07H1/06B01D15/08
Inventor 王春红施荣富赵艳
Owner NANKAI UNIV
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