CN105820148B - Technology for purifying tea catechin from tea polyphenol - Google Patents

Technology for purifying tea catechin from tea polyphenol Download PDF

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CN105820148B
CN105820148B CN201510001063.3A CN201510001063A CN105820148B CN 105820148 B CN105820148 B CN 105820148B CN 201510001063 A CN201510001063 A CN 201510001063A CN 105820148 B CN105820148 B CN 105820148B
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tea
concentration
catechin
water
ethyl acetate
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CN105820148A (en
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涂云飞
张士康
杨秀芳
朱跃进
谭蓉
王静
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Hangzhou Tea Research Institute China Coop
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Abstract

The invention relates to a technology for purifying tea catechin from tea polyphenol. Comprises enriching and refining catechin components by silica gel column chromatography and series connection of low-substitution hydroxypropyl cellulose, so as to remove water-soluble and fat-soluble pigments in tea polyphenol and completely remove caffeine components. The chromatographic and enriched filler can be recycled after being activated and regenerated, and reagents used in the preparation process of the tea catechin product are green and environment-friendly.

Description

A technique for purifying tea catechin from tea polyphenols
Technical field
The invention belongs to Separation of Natural Products technical field of purification, and in particular to a kind of to utilize silica gel and low degree of substitution hydroxypropyl The purifying from tea polyphenols of the mode of base cellulose tandem compound prepares the technology of tea catechin.
Background technology
Tea tree source originate in Chinese yunnan Xishuangbanna (old rafter again discuss tea tree source area Tea Industry be notified to, 1981,01:20- 25.), be under the jurisdiction of Theaceae (Theacea) Camellia (Camellia Sinensis(L.) O. Ktze.) plant (plant by China Object will, the 49th (3) volume).The young leaves that tea tree is sprouted can be made into a kind of favorite beverage of consuming public, have in China thousands of Year drinks history, and often drink can promote the production of body fluid to quench thirst, disease salubrity and improving eyesight benefit is gone to think, beneficial to physically and mentally healthy (the natural antioxygens of the roads Zhao Bao The health benefit and its mechanism Acta Biophysica Sinicas of agent tea polyphenols, 2012,28 (5):426-437.||Chung S.Yang. Cancer Prevention by Vitamin E and Tea Polyphenols:Lessons Learned from Studies in Animal Models and humans.Progress in Chemistry, 2013,25(9):1492- 1500.)。
Tealeaves through separation identification about 700 kinds of compound (as if dawn spring tealeaves biochemistry, Chinese agriculture publishing house, 2003), including tea polyphenols, organic acid, theanine, alkaloid, Tea Saponin, aromatic substance, etc..Tea polyphenols are in tea tree Polyphenols mixture, with flavylium ion mutter based on flavanols compounds-tea catechin of structure account for bulk composition. Tea catechin generally comprises phenotype catechin (Epicatechin, EC), epi-nutgall type catechin (Epigallocatechin, EGC), L-Epicatechin gallate (Epicatechin gallate, ECG), epi-nutgall Catechin and gallate (Epigallocatechin gallate, EGCG), gross mass number are generally greater than in dry tea 7% (w/w) tea catechins have anti-oxidant, anti-inflammatory, antiviral and antitumor, etc. characteristics.
China's Resources of Tea Plant is abundant, has 2279.94 thousand hectares of tea place area in fact, can pick 1735.2 thousand hectare (2012 Annual national statistics office data), 192.45 ten thousand tons of tea yield (2013 annual national statistics office data).The fresh tea leaves of picking pass through The dry tea being processed into generally comprises Famous High-quality Tea and large tea.By taking Zhejiang Province's tea industry as an example (Mao Zufa enumerates ten thousand, Lu Debiao, The Famous High-quality Tea Industry Countermeasures for Sustainable Development research Chinese teas processing of the Zhejiang Province equal, 2012,2:9-12.), Famous High-quality Tea in 2010 Yield (6.5 ten thousand tons) and the output value (84.4 hundred million yuan) are the 39.2% and 93.3% of total output and the output value respectively.Therefore large Summer-autumn tea is deposited In the problem that yield is big, the output value is low.Large tea phenol ammonia is than high, with deep processing means come to develop and use polyphenol therein will be its hair One of exhibition approach.It is reported that current tea comprehensive processing enterprise of Zhejiang Province about 40, year about 8.2 ten thousand tons of dry tea is consumed, be mainly used to give birth to Tea polyphenols, instant tea are produced, etc..Tea polyphenols are the main product of tea comprehensive processing enterprise at present, and product mainly applies to tea-drinking Material, food additives and health-related product.But with the development of plant extracts, the progress of biochemistry polishing purification technology, And people constantly pursue high-quality product, ingredient natural products product that is single, concentrating opposite with function will be following a kind of Development trend.Therefore, a kind of health elements of the tea catechin as the mankind are purified purifying and meet current big health industry Development.
Presently commercially available tea polyphenols product is mainly carried using water or the ethanol solution of water extracts, is concentrated and dried and obtains, powder In yellowish-brown.Tea catechin typically results in preferable reservation, and the impurity only to accompany with it is more, especially fat-soluble and water Dissolubility pigment composition influence product quality.Collect the tea polyphenols of the different content specification of market sale early period in our laboratories Product is mainly derived from Zhejiang Orient Tea Development Co., Ltd., Sichuan Yujia Tea Industry Technology Co., Ltd., morning twilight biotechnology Group Plc, Zhejiang Ta Ta Tea Industry Science and Technology Ltd., Zhejiang University of Technology, the Fujian sources Li Kang Bioengineering Co., Ltd, Jiangxi Lv Kang natural products Co., Ltd, Hunan Jinnong Biological Resources Co., Ltd., peace Emblem Red Star medicine company Co., Ltd, and the tea as contained by national standard man tealeaves standard GB/T 8313-2008 determine it is more Phenol, tea catechin ingredient (being shown in Table 1).The result shows that tea catechin total amount accounts for tea polyphenols mass percent in 50 %-88.8 % models It encloses.
Tea polyphenols, gallic acid and tea catechin content (%, w/w) in 1 commercially available tea polyphenols product of table
Note:Each ingredient is indicated with average ± standard deviation (n=3) in sample in table.
The purification process of tea catechin mainly have the precipitation method (ZL02139219.6), resin adsorption method (Zhang Sheng, Liu Zhonghua, Huang Jianan waits adsorption resin methods to prepare the research tea sciences of high-purity catechin, 2002,22 (2): 125-130| |Zhang Sheng, Liu Zhonghua, Huang Jianan wait journal (natural section of high ECG type catechin purifying process research Agricultural University Of Hunan Learn version), 2003,29 (2):144-146.||Gong Yushun, Liu Zhonghua, Huang Jianan wait macroporous absorbent resins to detach tea catechu Element and caffeine research Agricultural University Of Hunan's journals (natural science edition), 2005,31 (1):50-52||Li Huixing resin methods Technical study HeFei University of Technologys prepared by extraction purification catechin and catechin monomers EGCG separation, 2006.||Zhong Shian, He Guowen, Tu Qiuyun wait research ion exchanges and the absorption of Adsorption of Ester Catechins With Macroporous Resins, 2007, 23(5): 392-399.||The separation purifying technique research Dalian University of Technology of Zhang swallow Lai ester catechins, 2006||EP1767097, Process for preparing epigallocatechin gallate||Yang Xingmin, Liu Qing Plum, Gao Haiyue, Ying Min, poplar stay in bright tea polyphenols EGCG separation purifying techniques to optimize Chinese food journals, and 2006,6 (5): 77-80.||Wang Chuanjin, Wei Yunyang, Zhu Guangjun wait the separation of polyamide chromatographies to prepare high-purity epigallocatechin gallate Catechin gallate applied chemistries, 2007,24 (4): 443-447.||Gong Zhihua, Huang Tian, Pang Yuelan wait HP-20 macroporous absorbent resins isolate and purify the effect Agricultural University Of Hunan journal (natural science edition) of catechin EGCG, 2010, 36(1): 87-90||Jianhan Huang, Kelong Huang, Suqin Liu, Qiong Luo, Mancai Xu. Adsorption properties of tea polyphenols onto three polymeric adsorbents with amide group. Journal of colloid and interface science.||Ruiying Zhao, Yu Yan, Mingxian Li, Husheng Yan. Selective adsorption of tea polyphenols from aqueous solution of the mixture with caffeine on macroporous crosslinked poly (N-Vinyl-2-pyrrolidinone). Reactive & Functional Polymers 68 (2008) 768-774.| |Yang Wenhong, Zhao Changqing, Gao Jie wait to be selectively adsorbing and separating tea polyphenols and coffee with macropore aminomethyl polystyrene resin Because of ion exchanges and absorption, 2007,23 (6): 481-488.||Tang's text, Zhou Chunshan, Zhong Shian wait polyamide Resin is to tea polyphenols and caffeine adsorptive selectivity research spectroscopy and spectrum analysis, 2003,23 (1): 143-145.), 18 filler column chromatography of reverse phase carbon (the natural ester catechin EGCG of Zhou Qingqiu isolate and purify and the Heilungkiang study of pharmacy is big It learns, 2008.||Lindane, Li Chunmiao is fresh different, waits in and preparative liquid chromatography quick separating is pressed to prepare catechin monomers natural products Research and development, 2013,25 (1):92-95,100.||Lai Ronghui, the research of yellow Asia brightness medium and low pressure column chromatography catechins Ion exchange and absorption, 2012,28 (2):165-170.), (Zhang Jianyong, Jiang Yongwen, Jiang Heyuan wait UF membrane mistakes to membrane separation process Catechin and caffeine content Changeement Agriculture of Anhui science, 2013,41 (2) in journey:493-496.), gel filtration chromatography method (Huang Jing high-purity catechins monomer EGCGs and ECG separation and purifying process research HeFei University of Technologys, 2004), etc..
Silica gel has been widely used in the separation of active ingredient in plant extracts as a kind of Nantural non-toxic separation material With purifying, the no exception (Shanxi Gong Zhengli, Pu Jian, the Liu Qin tea catechins extraction of preparation purifying of the tea catechin of tea polyphenols With purifying research Agricultural University Of Southwest journal, 1995,17 (6):546-549||Yang Lei, high Yan China, Zu YuanGang are waited and are pressed in The research chemistry of forest product of EGCG and ECG and industry, 2007,27 (2) in silica gel column chromatography continuous purification tealeaves: 100- 104.||Yuan Hua, Wu Li, Wu Yuanxin wait the research Central China Normal University journal of silica gel column chromatographies purification tea polyphenols (natural Science version), 2007,41 (4):553-556..||Lu Tao, Lan Xianqiu, Zhu Bin, wait in difference tea polyphenols the measurement of catechin and Column chromatography extracts the comparison chemical industry progress of EGCG, 2008,27 (5):749-752.||Bis- chromatography systems of Zhu Bin, Chen Xiaoguang The technical study food of standby high-purity Epigallo-catechin gallate (EGCG) (EGCG) and machinery, 2009,25 (4): 83- 85.).The method that inventor is provided with document is that column chromatography filler is pure to tea catechin progress in commercially available tea polyphenols using silica gel Change confirmatory experiment.As described in document, glue silicon using anhydrous ethyl acetate as dress column and elution solvent, tea polyphenols can be divided into compared with For apparent visible component up and down, but contain tea catechin in component up and down, separation is not thorough;And the polarity adsorbed compared with Strong pigment constituents, which are difficult to elute, can not be ignored.On the other hand, it could be used after the silica gel after use need to be dried so that silica gel Special separating property is difficult to industrialization application and preparation.If being purified from tea polyphenols using gel Sephadex LH-20 as column packing Refined tea catechin also has that pigment pollution is difficult to elute, and regenerative elution need to use the highly basic and salt of high concentration, increase and divide From period and experiment difficulty, to reduce the application prospect of its industrialization.Therefore using existing technique filler as absorption and layer Analysis, obtains the tea catechin of high-purity, and effectively removing is seemed particularly by the pigment of filling adsorption and the improvement of the Combinatorial Optimization of technique It is necessary and urgent.
Invention content
The purpose of the present invention is to provide a kind of mode with silica gel and low degree of substitution hydroxypropyl cellulose tandem compound is pure Change prepares the technology of tea catechin, and particular technique route is shown in Fig. 1.Compared with the existing technology using only silica gel column chromatography, the technique It can make the significantly more efficient separation of tea catechin and enrichment.
The present invention also aims to provide it is a kind of effectively remove by the complete solidity pigment after silica gel absorption, after adsorption chromatography Silica gel activating it is simpler feasible, recycled for a long time so as to realize.One kind provided by the invention is pure from tea polyphenols Change the technology of tea catechin, including:
(1) by water dissolution of the tea polyphenols powder containing acetic acid, tea polyphenols solution is obtained;
(2) the prepared tea polyphenols solution of centrifugation step (1) obtains supernatant;
(3) supernatant of step (2) is sufficiently mixed with water saturated ethyl acetate, after being layered, obtains upper layer ester phase Extract liquor;
(4) the upper layer ester phase extract liquor of concentration step (3) obtains concentrate;
(5) concentrate of step (4) is splined on silica gel column chromatography;
(6) it is eluted with water saturation ethyl acetate, and collects eluent;
(7) eluent of concentration step (6) obtains tea catechin purified product (I) to remove ethyl acetate;
(8) silica gel in aqueous sodium potassium tartrate zeolite regeneration step (5) is utilized;
(9) the tea catechin purified product (I) in step (7) is diluted with water, obtains aqueous solution;
(10) by the aqueous solution loading of step (9) and it is adsorbed in low degree of substitution hydroxypropyl cellulose;
(11) it is eluted with water;
(12) ethanol elution of 15-45 % (v/v) is used, and collects eluent;
(13) eluent of concentration step (12) obtains concentrate;
(14) low degree of substitution hydroxypropyl cellulose in the water elution regeneration step (10) containing ethyl acetate is utilized;
(15) ethyl acetate is added into the concentrate of step (13) to be sufficiently mixed, after being layered, obtains upper layer ester and mutually extract Take liquid;
(16) the upper layer ester phase extract liquor of concentration step (15) obtains tea catechin purified product to remove ethyl acetate (II);
(17) the tea catechin purified product (II) of further vacuum drying step (16), obtains the tea catechu of polishing purification Element.
Preferentially, the wherein water containing acetic acid described in step (1), acetate concentration is in 1-4 mol/L.
Preferentially, wherein the water containing acetic acid described in step (1), acetate concentration are 2 mol/L.
Preferentially, the tea polyphenols solution wherein described in step (1), tea polyphenols concentration are higher than 5 % (w/v).
Preferentially, the tea polyphenols solution wherein described in step (1), a concentration of 10 % (w/v) of tea polyphenols.
Preferentially, the r/min of the centrifuge speed wherein described in step (2) >=3000.
Preferentially, the min of the centrifugation time wherein described in step (2) >=10.
Preferentially, the water saturation ethyl acetate wherein described in step (3) is 0.5-1.5 times of volume of supernatant.
Preferentially, wherein step (3) the water saturated ethyl acetate is 1 times of supernatant.
Preferentially, wherein step (3) the water saturated ethyl acetate is 1 times of supernatant, is extracted 2 times.
Preferentially, wherein step (4), (7), (13), (16) and (17) is in -0.07 MPa ~ -0.1 of vacuum degree MPa is carried out under the conditions of 35 DEG C ~ 50 DEG C of temperature.
Preferentially, the concentration of solution is controlled in the % of 0.5 % ~ 5 (w/v) wherein in step (9).
Preferentially, wherein step (11) elutes remaining acetic acid.
Preferentially, the wherein a concentration of mmol/L of 35 mmol/L ~ 50 of the sodium potassium tartrate tetrahydrate of step (8).
Main advantages of the present invention are:
(1) not purified tea polyphenols (polyphenol content is generally below 80 %, w/w) have a part with room temperature water dissolution Adhesive component is difficult to dissolve, insoluble that precipitation is collectively formed at branch's a certain amount of tea catechin of absorption;Such as with a certain concentration Acetate dissolution tea polyphenols, then can promote precipitation in tea catechin be redissolved in water, to reduce the damage of tea catechin It loses.
(2) it is extracted by water saturation ethyl acetate before silicagel column adsorption chromatography, is on the one hand enriched tea catechin, another party Face reduces water colo(u)r ingredient and excessive suction-operated occurs with silica gel column chromatography filler.
(3) water loads silica gel, fully after activation, then with water saturation ethyl acetate balance, and is eluted in this, as column chromatography Agent can then enable caffeine and water-soluble strong pigment retain by force and adsorb, and tea catechin and fat-soluble stronger yellowish red color Pigment elutes simultaneously with eluant, eluent, to realize more sufficient first step chromatographic purifying.
(4) activating and regenerating of silica gel column chromatography directly uses the aqueous solution of sodium potassium tartrate tetrahydrate, is convenient for water saturation ethyl acetate Balance recycle, to simple realization column chromatography filler the repeatable purpose recycled.
Description of the drawings
Fig. 1 is the purifying tea catechin technology path schematic diagram from tea polyphenols.
Fig. 2 is tea polyphenol raw materials, silica gel column chromatography water saturation ethyl acetate eluent, low-substituted hydroxypropyl cellulose washing (gallic acid, epigallocatechin, caffeine, epicatechin, epigallocatechin do not have each ingredient in de- liquid and desorbed solution Infanticide acid esters, L-Epicatechin gallate) HPLC collection of illustrative plates.
Specific implementation mode
With reference to embodiment, the purport of the present invention is further illustrated.
It is following that examples are only for illustrating the present invention and not for limiting the scope of the present invention.
The analysis of tea catechin is all made of national standard method (GB/T 8313-2008, Tea Polyphenols in Tea in following embodiments With the detection method of catechin content).High performance liquid chromatography Waters (1525 pumps, column oven, 2487 UV, visible light bilaterals Road detector, 717-plus autosamplers,BreezeControl software packet), chromatographic column is 5 μm of Phenomenex Luna Phenyl-Hexyl, 250 mm × 4.6 mm.Using caffeine as each ingredient of internal standard coefficient standard measure.Coffee is taken respectively 50 mg/L of alkali standard solution, 100 mg/L, 150 mg/L sample introductions, 10 μ L, after high performance liquid chromatography separation, in 278 nm items Corresponding product peak area is respectively 1311154 (μ V × Sec), 2671194 (μ V × Sec), 4058875 (μ V under part × Sec);The standard curve for being forced across coordinate axis origin is ψ (peak area)=26900 × χ (concentration mg/L), R2 = 0.999。
Tea polyphenols described in following embodiments are same batch, tea catechu prepared by tea polyphenol raw materials, silica gel column chromatography The HPLC figures of each ingredient are as shown in Figure 2 in plain crude product, low-substituted hydroxypropyl cellulose water elution and desorbed solution.The GA, EGC, CAF, EC, EGCG, ECG are respectively gallic acid, epigallocatechin, caffeine, epicatechin, epi-nutgall catechu Plain gallate, L-Epicatechin gallate.The L-HPC is low degree of substitution hydroxypropyl cellulose.
Material, reagent etc., are commercially available unless otherwise specified used in following experimental examples.
The acquisition of experimental data is completed in October, 2014 in December, 2014 in following embodiments.
1 pure water of embodiment dissolves tea polyphenols powder
It takes 0.5 g of tea polyphenols powder to be placed in 10mL plastics graded tubes, and adds the pure water of 5 mL, be sufficiently stirred and through 3500 After r/min centrifuges 10 min, constant volume in supernatant to 10 mL volumetric flasks is shifted.After 50 times of dilution, efficient liquid phase is carried out into 10 μ L Chromatography.Precipitation in plastics graded tube takes out precision weighing after fully dry 5 h of 80 DEG C of hot winds.The result shows that through fixed A concentration of 164.2 mg/L of EGCG in the supernatant of appearance, a concentration of 22.2 mg/L of ECG, precipitation weigh 0.1088 g.
Water dissolution tea polyphenols powder of the embodiment 2 containing acetic acid
It takes 0.5 g of tea polyphenols powder to set in 10 mL plastics graded tubes, and adds the aqueous acetic acid of 5 mL (acetate concentration is 0.2 mol/L), it is sufficiently stirred and after 3500 r/min centrifuge 10 min, shifts constant volume in supernatant to 10 mL volumetric flasks.It is dilute After releasing 50 times, efficient liquid phase chromatographic analysis is carried out into 10 μ L.Precipitation in plastics graded tube is through fully dry 5 h of 80 DEG C of hot winds After take out precision weighing.The result shows that in the supernatant through constant volume EGCG a concentration of 189.8 mg/L, ECG's is a concentration of 22.9 mg/L, precipitation weigh 0.0901 g.
Water dissolution tea polyphenols powder of the embodiment 3 containing acetic acid
It takes 0.5 g of tea polyphenols powder to set in 10 mL plastics graded tubes, and adds the aqueous acetic acid of 5mL (acetate concentration is 0.5 mol/L), it is sufficiently stirred and after 3500 r/min centrifuge 10 min, shifts constant volume in supernatant to 10 mL volumetric flasks.It is dilute After releasing 50 times, efficient liquid phase chromatographic analysis is carried out into 10 μ L.Precipitation in plastics graded tube is through fully dry 5 h of 80 DEG C of hot winds After take out precision weighing.The result shows that in the supernatant through constant volume EGCG a concentration of 206.2 mg/L, ECG's is a concentration of 29.5 mg/L, precipitation weigh 0.0735 g.
Water dissolution tea polyphenols powder of the embodiment 4 containing acetic acid
It takes 0.5 g of tea polyphenols powder to set in 10 mL plastics graded tubes, and adds the aqueous acetic acid (acetate concentration 1 of 5mL Mol/L), it is sufficiently stirred and after 3500 r/min centrifuge 10 min, shifts constant volume in supernatant to 10 mL volumetric flasks.Dilution 50 After times, efficient liquid phase chromatographic analysis is carried out into 10 μ L.Precipitation in plastics graded tube takes after the fully dry 5h of 80 DEG C of hot winds Go out precision weighing.The result shows that in the supernatant through constant volume EGCG a concentration of 253.4 mg/L, a concentration of the 37.1 of ECG Mg/L, precipitation weigh 0.0427 g.
Water dissolution tea polyphenols powder of the embodiment 5 containing acetic acid
It takes 0.5 g of tea polyphenols powder to set in 10 mL plastics graded tubes, and adds the aqueous acetic acid (acetate concentration 2 of 5 mL Mol/L), it is sufficiently stirred and after 3500 r/min centrifuge 10 min, shifts constant volume in supernatant to 10 mL volumetric flasks.Dilution 50 After times, efficient liquid phase chromatographic analysis is carried out into 10 μ L.Precipitation in plastics graded tube takes after fully dry 5 h of 80 DEG C of hot winds Go out precision weighing.The result shows that in the supernatant through constant volume EGCG a concentration of 258.8 mg/L, a concentration of the 37.6 of ECG Mg/L, precipitation weigh 0.025 g.
Water dissolution tea polyphenols powder of the embodiment 6 containing acetic acid
It takes 0.5 g of tea polyphenols powder to set in 10 mL plastics graded tubes, and adds the aqueous acetic acid (acetate concentration 4 of 5 mL Mol/L), it is sufficiently stirred and after 3500 r/min centrifuge 10 min, shifts constant volume in supernatant to 10 mL volumetric flasks.Dilution 50 After times, efficient liquid phase chromatographic analysis is carried out into 10 μ L.Precipitation in plastics graded tube takes after fully dry 5 h of 80 DEG C of hot winds Go out precision weighing.The result shows that in the supernatant through constant volume EGCG a concentration of 267.5 mg/L, a concentration of the 40.8 of ECG Mg/L, precipitation weigh 0.012 g.
In above-described embodiment, control takes 20 mg tea polyphenols to be completely dissolved with 50 % (v/v) ethyl alcohol to be dissolved in 10 mL surely, into 10 μ L carry out efficient liquid phase chromatographic analysis.The result shows that in the solution through constant volume GA, EGC, CAF, EC, EGCG and ECG it is dense Degree is respectively 11.9 mg/L, 68.6 mg/L, 97.1 mg/L, 17.8 mg/L, 100.2 mg/L, 23.7 mg/L.Tea polyphenols are former The mass fraction of each ingredient GA, EGC, CAF, EC, EGCG and ECG are respectively 0.6 %, 3.4 %, 4.8 %, 0.9 %, 5.0 in material %、1.2 %。
7 silica gel column chromatography purification enrichment tea catechin of embodiment
With commercially available 5 g of tea polyphenols powder for a purification enrichment unit, used per unit steps are as follows:
1. accurately weighing 5 g of tea polyphenols powder, 50 mL of acetic acid water of 2 mol/L is added, after being sufficiently stirred, is put into centrifugation After 3500 r/min centrifuge 10 min in machine, takes supernatant and 25 mL water saturation ethyl acetate are added, fully shake simultaneously stratification Afterwards, upper layer ester is taken mutually to be splined on silica gel column chromatography (100 g of about 200 mesh silica gel, the column diameter 3.5 of water saturation ethyl acetate balance Cm, 26 cm of pillar height, 80 mL of interstitial volume in column bed), and eluted with water saturation ethyl acetate, collection starts from eluent and contains Yellowish red color pigment is until eluent is colourless.Concentrate eluant is dried in vacuo to obtain 0.42 g of tea catechin crude product to after doing.
2. accurately weighing 5 g of tea polyphenols powder, 50 mL of acetic acid water of 2 mol/L is added, after being sufficiently stirred, is put into centrifugation After 3500 r/min centrifuge 10 min in machine, takes supernatant and 50 mL water saturation ethyl acetate are added, fully shake simultaneously stratification Afterwards, upper layer ester is taken mutually to be splined on silica gel column chromatography (100 g of about 200 mesh silica gel, the column diameter 3.5 of water saturation ethyl acetate balance Cm, 26 cm of pillar height, 80 mL of interstitial volume in column bed), and eluted with water saturation ethyl acetate, collection starts from eluent and contains Yellowish red color pigment is until eluent is colourless.Concentrate eluant is dried in vacuo to obtain tea catechin crude product 0.53g to after doing.
3. accurately weighing 5 g of tea polyphenols powder, 50 mL of acetic acid water of 2 mol/L is added, after being sufficiently stirred, is put into centrifugation After 3500 r/min centrifuge 10 min in machine, takes supernatant and 150 mL water saturation ethyl acetate are added, fully shake and stand point After layer, takes upper layer ester phase and be concentrated into its volume less than 100 mL;Concentrate is taken to be splined on the silicon of water saturation ethyl acetate balance Glue chromatographic column (100 g of about 200 mesh silica gel, 3.5 cm of column diameter, 26 cm of pillar height, 80 mL of interstitial volume in column bed), and with water It is saturated ethyl acetate elution, collection starts from eluent and contains yellowish red color pigment until eluent is colourless.Concentrate eluant is to dry Afterwards, it is dried in vacuo to obtain 0.57 g of tea catechin crude product.
It is 1.52 to merge the above tea catechin crude product (tea catechin purified product (I)) 1. 2. 3. obtained by unit of mixing g.The mass fraction (%, w/w) that GA, EGC, EC, EGCG and ECG contained by it are detected through HPLC be respectively 2.3 %, 4.1 %, 4.9 %,34.0 %,9.1 %.Using the aqueous solution zeolite regeneration silica gel of sodium potassium tartrate tetrahydrate.
8 L-HPC adsorption columns of embodiment are enriched with tea catechin
7 gained tea catechin crude product of Example, 0.5 g is dissolved in and is settled to 100 mL, with the flow velocity of 1 cm/min It is splined on the L-HPC (5 g L-HPC, 1.6 cm of column diameter, 13.5 cm of pillar height, 10 mL of interstitial volume in column bed) of water balance, And eluted with 30 % (v/v) ethanol water, it is collected simultaneously eluent.It has been observed that eluent is slight yellowish, and The peony pigment of L-HPC absorption is not eluted.By eluent vacuum carry out concentration fling to ethyl alcohol after, carried out using ethyl acetate It is enriched with dry that refined 0.25 g of tea catechin product, the wherein mass fraction (%, w/w) of GA, EGC, EC, EGCG and ECG are distinguished For 3.2 %, 4.5 %, 7.7 %, 59.5 %, 13.0 %.
9 L-HPC adsorption columns of embodiment are enriched with tea catechin
7 gained tea catechin crude product of Example, 0.5 g is dissolved in and is settled to 100 mL, with the flow velocity of 1 cm/min It is splined on the L-HPC (5 g L-HPC, 1.6 cm of column diameter, 13.5 cm of pillar height, 10 mL of interstitial volume in column bed) of water balance, And eluted with 40 % (v/v) ethanol water, it is collected simultaneously eluent.It has been observed that eluent is faint yellow, and L- The peony pigment of HPC absorption is not eluted.Eluent vacuum is carried out after concentration flings to ethyl alcohol, to utilize ethyl acetate to carry out rich Collect dry that refined 0.27 g of tea catechin product, the wherein mass fraction (%, w/w) of GA, EGC, EC, EGCG and ECG are respectively 3.7 %、6.5 %、7.9 %、56.8 %、16.0 %。
10 L-HPC adsorption columns of embodiment are enriched with tea catechin
7 gained tea catechin crude product of Example, 0.5 g is dissolved in and is settled to 100 mL, with the flow velocity of 1 cm/min It is splined on the L-HPC (5 g L-HPC, 1.6 cm of column diameter, 13.5 cm of pillar height, 10 mL of interstitial volume in column bed) of water balance, And eluted with 50 % (v/v) ethanol water, it is collected simultaneously eluent.It has been observed that eluent is faint yellow, and L- The peony pigment of HPC absorption is not eluted.Eluent vacuum is carried out after concentration flings to ethyl alcohol, to utilize ethyl acetate to carry out rich Collect dry that refined 0.31 g of tea catechin product, the wherein mass fraction (%, w/w) of GA, EGC, EC, EGCG and ECG are respectively 3.8 %、6.6 %、7.6 %、52.8 %、16.5 %。

Claims (15)

1. a kind of method isolating and purifying tea catechin class compound from tea polyphenols, including:
(1) by water dissolution of the tea polyphenols powder containing acetic acid, tea polyphenols solution is obtained;
(2) the prepared tea polyphenols solution of centrifugation step (1) obtains supernatant;
(3) supernatant of step (2) is sufficiently mixed with water saturated ethyl acetate, after being layered, obtains upper layer ester and mutually extract Liquid;
(4) the upper layer ester phase extract liquor of concentration step (3) obtains concentrate;
(5) concentrate of step (4) is splined on silica gel column chromatography;
(6) it is eluted with water saturation ethyl acetate, and collects eluent;
(7) eluent of concentration step (6) obtains tea catechin crude product to remove ethyl acetate;
(8) silica gel in aqueous sodium potassium tartrate zeolite regeneration step (5) is utilized;
(9) the tea catechin crude product in step (7) is diluted with water, obtains aqueous solution;
(10) by the aqueous solution loading of step (9) and it is adsorbed in low degree of substitution hydroxypropyl cellulose;
(11) it is eluted with water;
(12) ethanol elution of 15-45v/v% is used, and collects eluent;
(13) eluent of concentration step (12) obtains concentrate;
(14) low degree of substitution hydroxypropyl cellulose in the water elution regeneration step (10) containing ethyl acetate is utilized;
(15) ethyl acetate is added into the concentrate of step (13) to be sufficiently mixed, after being layered, obtains upper layer ester phase extract liquor;
(16) the upper layer ester phase extract liquor of concentration step (15), to remove ethyl acetate, rear further vacuum drying obtains refining pure The tea catechin class compound of change, the tea catechin class compound are epigallocatechin, epicatechin, epigallocatechin gallate Catechin gallate, L-Epicatechin gallate.
2. the water containing acetic acid described in the method as described in claim 1, wherein step (1), acetate concentration is in 1-4mol/L.
3. the water containing acetic acid described in method as claimed in claim 2, wherein step (1), acetate concentration 2mol/L.
4. the tea polyphenols solution described in the method as described in claim 1, wherein step (1), tea polyphenols concentration is higher than 5w/v%.
5. the tea polyphenols solution described in method as claimed in claim 4, wherein step (1), a concentration of 10w/v% of tea polyphenols.
6. centrifuge speed >=3000r/min described in the method as described in claim 1, wherein step (2).
7. centrifugation time >=10min described in the method as described in claim 1, wherein step (2).
8. the water saturation ethyl acetate described in the method as described in claim 1, wherein step (3) is the 0.5-1.5 of supernatant Times volume.
9. method as claimed in claim 8, wherein step (3) the water saturated ethyl acetate are 1 times of supernatant.
10. the method as described in claim 1, wherein step (3) water saturated ethyl acetate are 1 times of supernatant, extraction It takes 2 times.
11. the method as described in claim 1, wherein step (4), (7), (13), (16) vacuum degree -0.07MPa~- 0.1MPa is carried out under the conditions of 35 DEG C~50 DEG C of temperature.
12. the concentration of solution is controlled in 0.5%~5w/v% in the method as described in claim 1, wherein step (9).
13. the method as described in claim 1, wherein step (11) elute remaining acetic acid.
14. a concentration of 35mmol/L~50mmol/ of the sodium potassium tartrate tetrahydrate of the method as described in claim 1, wherein step (8) L。
15. the tea polyphenols used in the method as described in claim 1, wherein step (1) derive from green tea or oolong tea.
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