CN1687435A - Technique for producing high purity chlorogenic acid in industrialization scale - Google Patents
Technique for producing high purity chlorogenic acid in industrialization scale Download PDFInfo
- Publication number
- CN1687435A CN1687435A CN 200510020706 CN200510020706A CN1687435A CN 1687435 A CN1687435 A CN 1687435A CN 200510020706 CN200510020706 CN 200510020706 CN 200510020706 A CN200510020706 A CN 200510020706A CN 1687435 A CN1687435 A CN 1687435A
- Authority
- CN
- China
- Prior art keywords
- chlorogenic acid
- ethyl acetate
- technique
- folium eucommiae
- acid
- 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
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
This invention relates to industrial production technique of Chlorogenic Acid. When we add compounded enzymes, it can enhance the extraction rate. This technology is a breakthrough of Chlorogenic Acid production, because the reductive solvent protects Chlorogenic Acid groups, avoids it to be oxidated. It works out problems such as phenol hydroxyl oxidated, alkene diethylene glycol dinitrate bond hydrolysis, isomerization of seriate molecular lactone migration. The first enterprise, who has adapted this technology, has completed the industrialization produces of the high pure chlorogenic acid, about 500kg per year. Its purity reaches 99%, absolutely satisfies the production criterion of freeze-dry powder. In the production the solvent amount are few, the product solvent remains may meet the national related requirements and each criterion.
Description
Technical field the present invention relates to the preparation technology of medicine material, particularly the technology of high purity chlorogenic acid in industrialization scale production.
" research of the pure product of chlorogenic acid extracting from Folium Eucommiae " that background technology 1. is write at Ma Xihan etc. is (referring to " Xibei Forest College's journal " 1996,11 (2): 58-60), adopt chloroform degreasing, chemical extraction, inorganic salt to sink, this processing method fails effectively to remove the impurity (as protein, colloid, Mierocrystalline cellulose) in the Folium Eucommiae, make chlorogenic acid be difficult to stripping, and only be applicable to the low dose of preparation in laboratory.2. " extraction of the chlorogenic acid material research in the Folium Eucommiae " of being write at Wang Hongwu etc. is (referring to " Jiangxi Normal University's journal " (natural science edition) 1997,21 (4): 339-341), what adopt is solvent extraction, alkaline Pb (OAc) and KOAc precipitation, the dissolution extraction recrystallization makes again, but plumbous meeting have residual in the chlorogenic acid product, leaded extraction waste liquid can cause detrimentally affect to environment, and therefore, this method is not suitable for large-scale industrialization production.3. " extraction of Folium Eucommiae chlorogenic acid, separation and the evaluation " of writing at Qi Xiangyang etc. is (referring to " plant resources and environment " 1998,7 (1): 61-62), adopt flooding, 101 resin isolation, organic solvent extraction purifying, its chlorogenic acid contents only is 24.33%.Above Technology to chlorogenic acid extract, various influence factors in the purge process do not give to take all factors into consideration and solve, all can not reach the content more than 99% and the rule of suitability for industrialized production and touch.
Summary of the invention the present invention proposes a kind of the solve contained phenolic hydroxyl group oxidation of chlorogenic acid in the production process, olefin(e) acid ester linkage hydrolyzing and intramolecularly ester group migration and problem such as isomery takes place in succession just in order to overcome above-mentioned weak point of the prior art; And breakthrough suitability for industrialized production yield is low, content does not reach the bottleneck that requires more than 99%.
Technique for producing high purity chlorogenic acid in industrialization scale branch following steps of the present invention are finished:
1. pre-treatment: the sherwood oil that adds 2 to the 3 times of weight of Folium Eucommiae after the pulverizing takes off ester with Folium Eucommiae, filters the compound bio-enzyme preparation that adds 0.5-1% in the back in Folium Eucommiae and also puts into encloses container and store 24-36 hour; Wherein the compound bio zymin is made up of 45%-65% cellulase, 5%-10% proteolytic enzyme and 30%-45% polygalacturonase.
2. extract: with the 4-5 of Folium Eucommiae weight doubly, concentration is ethanol or the butanols of 40%-60%, extracts 0.5-1 hour under 40 ℃ of-50 ℃ of temperature, extracts twice with identical condition, centrifuging is also squeezed;
3. purify: add 2%-3% composite reduction solvent in extracting solution, this composite reduction solvent is by being to have than the inorganic salt of strong reducing property to form, as being made up of 85%-95% Sulfothiorine and 5%-15% sodium bisulfite.The extracting solution that is added with the reduction solvent is concentrated the back transfer pH to 2-3 with concentrated hydrochloric acid, with twice of concentrated solution 3-4 ethyl acetate extraction doubly, get ethyl acetate layer, wherein adding the neutralization of 3%-5%NaOH liquid makes the chlorogenic acid in the ethyl acetate enter water, separate out the chlorogenic acid precipitation with concentrated hydrochloric acid acid again after the aqueous phase separation, with the incomplete dissolving-recrystallization of a spot of ethyl acetate, be drying to obtain the chlorogenic acid crude product after the precipitate and separate, content is generally about 95%-98%, extraction yield about 2.7%;
4. finished product is refining: chlorogenic acid crude product and deionized water are with the solid-liquid ratio of 1: 3 or 1: 4, at the high pure nitrogen that leads to 99.99% continuously, keep malleation, under the condition of pressure reduction＞5Pa, dissolving also adds the 8%-10% activated carbon and is heated to 50-60 ℃ of backflow 0.5-1 hour, filtration, crystallisation by cooling, crystallization with 2-5 analytical pure acetone doubly clean, vacuum-drying obtains 99% above high-purity chlorogenic acid.
The description of drawings Figure of description is detailed process flow figure of the present invention.
Below be the positively effect that the present invention is compared with prior art had:
1. adding compound bio-enzyme improves the solubility rate of chlorogenic acid and reduction solvent protection chlorogenic acid molecular radical to avoid oxidized technology is the important breakthrough that high-purity chlorogenic acid is produced; use of the present invention; first finishes the enterprise of commercial scale production high-purity chlorogenic acid (content is more than 99%) to make the applicant, and annual production reaches 500 kilograms.
2. chlorogenic acid purity reaches more than 99%, can satisfy every index of producing freeze-dried powder fully.
3. solvent load is few, and the product dissolvent residual can reach national relevant requirements and every index
Specific embodiments:
Embodiment 1: a kind of technique for producing high purity chlorogenic acid in industrialization scale, it is the Folium Eucommiae that to pulverize, sherwood oil with 2 times takes off ester with Folium Eucommiae, and add 1% therein, by 65% cellulase, the compound bio-enzyme preparation that 5% proteolytic enzyme and 30% polygalacturonase are formed, handled 24 o'clock, divide 2 times 40 ℃ of refluxing extraction with 4 times 40% ethanolic soln again, the 1st time 0.5 hour, the 2nd time 0.5 hour, each after-filtration that extracts, merging filtrate adds 3% in filtrate, by 90% Sulfothiorine, the composite reduction solvent that 10% sodium bisulfite is formed, and filtrate liquid concentrated the back transfer pH to 2 with concentrated hydrochloric acid, add 3 times of ethyl acetate extractions 2 times, ethyl acetate layer.Add the neutralization of 3%NaOH liquid, water separates out chlorogenic acid with concentrated hydrochloric acid acid again, separates the back with the incomplete dissolving-recrystallization of a spot of ethyl acetate, is drying to obtain the chlorogenic acid crude product.With the solid-liquid ratio of chlorogenic acid crude product with 1: 4, keep malleation at the high pure nitrogen that feeds 99.99% continuously, under the condition of pressure reduction＞5Pa, add 10% gac backflow 0.5 hour, filtration, crystallisation by cooling in water, crystallization is 99.25% high-purity chlorogenic acid with 0.5 times the cleaning of analytical pure acetone, vacuum-drying acquisition content.
Embodiment 2: a kind of technique for producing high purity chlorogenic acid in industrialization scale, it is the Folium Eucommiae that to pulverize, sherwood oil with 2 times takes off ester with Folium Eucommiae, and add 1% therein, by 45% cellulase, 10% proteolytic enzyme and 45% polygalacturonase are formed the compound bio-enzyme preparation, handled 28 o'clock, divide 2 times 45 ℃ of refluxing extraction with 6 times 50% ethanolic soln again, the 2nd time 0.5 hour, the 2nd time 1 hour, each after-filtration that extracts, merging filtrate adds 3% in filtrate, by 85% Sulfothiorine, the composite reduction solvent that 15% sodium bisulfite is formed, and filtrate liquid concentrated the back transfer pH to 2.5 with concentrated hydrochloric acid, add 3 times of ethyl acetate extractions 2 times, ethyl acetate layer.Add the neutralization of 4%NaOH liquid, water separates out chlorogenic acid with concentrated hydrochloric acid acid again, separates the back with the incomplete dissolving-recrystallization of a spot of ethyl acetate, is drying to obtain the chlorogenic acid crude product.With the solid-liquid ratio of chlorogenic acid crude product with 1: 5, keep malleation at the high pure nitrogen that feeds 99.99% continuously, under the condition of pressure reduction＞5Pa, add 10% gac backflow 0.5 hour, filtration, crystallisation by cooling in water, crystallization is 99.76% high-purity chlorogenic acid with 0.5 times the cleaning of analytical pure acetone, vacuum-drying acquisition content.
Embodiment 3: a kind of technique for producing high purity chlorogenic acid in industrialization scale, it is the Folium Eucommiae that to pulverize, sherwood oil with 2 times takes off ester with Folium Eucommiae, and add 1% compound bio-enzyme preparation (identical) therein and handled 32 o'clock with embodiment 1, divide 2 times 50 ℃ of refluxing extraction with 6 times 60% ethanolic soln again, the 1st time 1 hour, the 2nd time 1 hour, each after-filtration that extracts, merging filtrate adds 3% in filtrate, by 85% Sulfothiorine, the composite reduction solvent that 15% sodium bisulfite is formed, filtrate liquid is concentrated the back transfer pH to 3, add 3 times of ethyl acetate extractions 2 times, get ethyl acetate layer with concentrated hydrochloric acid.Add the neutralization of 5%NaOH liquid, water separates out chlorogenic acid with concentrated hydrochloric acid acid again, separates the back with the incomplete dissolving-recrystallization of a spot of ethyl acetate, is drying to obtain the chlorogenic acid crude product.With the solid-liquid ratio of chlorogenic acid crude product with 1: 5, keep malleation at the high pure nitrogen that feeds 99.99% continuously, under the condition of pressure reduction＞5Pa, add 10% gac backflow 1 hour, filtration, crystallisation by cooling in water, crystallization is 99.99% high-purity chlorogenic acid with 1 times the cleaning of analytical pure acetone, vacuum-drying acquisition content.
Embodiment 4: the technology of production is as described in the embodiment 1, and different is with 40% butanol solution as extracting solution, and obtaining chlorogenic acid content is 99.56%.
Embodiment 5: the technology of production is as described in the embodiment 2, and different is to add 1% compound bio-enzyme preparation, forms with embodiment 2, handles 36 o'clock; 4 times of ethyl acetate extractions 3 times, obtaining content is 99.52% chlorogenic acid.
Embodiment 6: production technique is as described in the embodiment 2, different is with the solid-liquid ratio of chlorogenic acid crude product with 1: 3, keeps malleation at the high pure nitrogen that feeds 99.99% continuously, under the condition of pressure reduction＞5Pa, add 8% gac and refluxed 1 hour in water, obtaining content is 99.7% chlorogenic acid.
Embodiment 7: the technology of production is as described in the embodiment 3, and different is to add 3%, and by the composite reduction solvent that 95% Sulfothiorine, 5% sodium bisulfite are formed, acquisition content is 99.89% chlorogenic acid.
Claims (3)
1. technique for producing high purity chlorogenic acid in industrialization scale is characterized in that the branch following steps finish:
1.1 pre-treatment: the sherwood oil that adds 2 to the 3 times of weight of Folium Eucommiae after the pulverizing takes off ester with Folium Eucommiae, filters the compound bio-enzyme preparation that adds 0.5-1% in the back in Folium Eucommiae and also puts into encloses container and store 24-36 hour;
1.2 extract: with the 4-5 of Folium Eucommiae weight doubly, concentration is ethanol or the butanols of 40%-60%, extracts 0.5-1 hour under 40 ℃ of-50 ℃ of temperature, extracts twice with identical condition, centrifuging is also squeezed;
1.3 purify: in extracting solution, add 2%-3% composite reduction solvent, extracting solution is concentrated the back transfer pH to 2-3 with concentrated hydrochloric acid, with twice of concentrated solution 3-4 ethyl acetate extraction doubly, get ethyl acetate layer, wherein adding the neutralization of 3%-5%NaOH liquid makes the chlorogenic acid in the ethyl acetate enter water, separate out the chlorogenic acid precipitation with concentrated hydrochloric acid acid again after the aqueous phase separation, after the precipitate and separate with the incomplete dissolving-recrystallization of a spot of ethyl acetate, be drying to obtain the chlorogenic acid crude product, content is generally about 95%-98%, extraction yield about 2.7%;
1.4 finished product is refining: chlorogenic acid crude product and deionized water are with the solid-liquid ratio of 1: 3 or 1: 4, keep malleation at the high pure nitrogen that feeds 99.99% continuously, under the condition of pressure reduction＞5Pa, dissolving also adds the 8%-10% activated carbon and is heated to 50-60 ℃ of backflow 0.5-1 hour, filtration, crystallisation by cooling, crystallization with 2-5 analytical pure acetone doubly clean, vacuum-drying obtains 99% above high-purity chlorogenic acid.
2. technique for producing high purity chlorogenic acid in industrialization scale according to claim 1 is characterized in that: said compound bio zymin is made up of 45%-65% cellulase, 5%-10% proteolytic enzyme and 30%-45% polygalacturonase.
3. technique for producing high purity chlorogenic acid in industrialization scale according to claim 1 is characterized in that: said composite reduction solvent is formed as 85%-95% Sulfothiorine and 5%-15% sodium bisulfite by being to have than the inorganic salt of strong reducing property to form.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100207065A CN100494393C (en) | 2005-04-14 | 2005-04-14 | Technique for producing high purity chlorogenic acid in industrialization scale |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100207065A CN100494393C (en) | 2005-04-14 | 2005-04-14 | Technique for producing high purity chlorogenic acid in industrialization scale |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1687435A true CN1687435A (en) | 2005-10-26 |
| CN100494393C CN100494393C (en) | 2009-06-03 |
Family
ID=35305477
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100207065A Expired - Fee Related CN100494393C (en) | 2005-04-14 | 2005-04-14 | Technique for producing high purity chlorogenic acid in industrialization scale |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100494393C (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805261A (en) * | 2010-03-26 | 2010-08-18 | 汉中天然谷生物科技有限公司 | Method for preparing competitive product of chlorogenic acid by folium cortex eucommiae |
| CN101486651B (en) * | 2009-02-10 | 2012-05-09 | 江苏省苏微微生物研究有限公司 | Method for extracting chlorogenic acid from Eucommia leaves and use thereof |
| CN102476997A (en) * | 2010-11-23 | 2012-05-30 | 陕西理工学院 | Method for preparing chlorogenic acid by freezing, concentrating and crystallizing |
| CN102687777A (en) * | 2011-03-24 | 2012-09-26 | 湖北太阳峰生物科技有限公司 | Preparation method of eucommia green tea powder |
| CN103535727A (en) * | 2013-10-23 | 2014-01-29 | 蒙思瑾 | Preparation method of blood pressure reducing electuary |
| CN101157827B (en) * | 2007-09-27 | 2014-03-05 | 贵州大学 | Method for extracting filament gutta-percha from eucommia leaf and skin |
| CN103798520A (en) * | 2014-01-22 | 2014-05-21 | 唐忠海 | Feed additive for substituting antibiotics and preparation method thereof |
| CN103815141A (en) * | 2014-01-22 | 2014-05-28 | 向华 | Eucommia ulmoides leaf feed additive and preparation method thereof |
| WO2015178786A1 (en) | 2014-05-23 | 2015-11-26 | PETER-WIRSKI, Maciej | Method of synthesis of monocaffeoylquinic or dicaffeoylquinic acid |
| CN110240544A (en) * | 2019-06-03 | 2019-09-17 | 西北农林科技大学 | A kind of chlorogenic acid method for extraction and purification and application |
-
2005
- 2005-04-14 CN CNB2005100207065A patent/CN100494393C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101157827B (en) * | 2007-09-27 | 2014-03-05 | 贵州大学 | Method for extracting filament gutta-percha from eucommia leaf and skin |
| CN101486651B (en) * | 2009-02-10 | 2012-05-09 | 江苏省苏微微生物研究有限公司 | Method for extracting chlorogenic acid from Eucommia leaves and use thereof |
| CN101805261A (en) * | 2010-03-26 | 2010-08-18 | 汉中天然谷生物科技有限公司 | Method for preparing competitive product of chlorogenic acid by folium cortex eucommiae |
| CN102476997A (en) * | 2010-11-23 | 2012-05-30 | 陕西理工学院 | Method for preparing chlorogenic acid by freezing, concentrating and crystallizing |
| CN102476997B (en) * | 2010-11-23 | 2014-04-02 | 陕西理工学院 | Method for preparing chlorogenic acid by freezing, concentrating and crystallizing |
| CN102687777A (en) * | 2011-03-24 | 2012-09-26 | 湖北太阳峰生物科技有限公司 | Preparation method of eucommia green tea powder |
| CN103535727A (en) * | 2013-10-23 | 2014-01-29 | 蒙思瑾 | Preparation method of blood pressure reducing electuary |
| CN103798520A (en) * | 2014-01-22 | 2014-05-21 | 唐忠海 | Feed additive for substituting antibiotics and preparation method thereof |
| CN103815141A (en) * | 2014-01-22 | 2014-05-28 | 向华 | Eucommia ulmoides leaf feed additive and preparation method thereof |
| CN103798520B (en) * | 2014-01-22 | 2016-08-24 | 吉首大学 | A kind of feed additive of substitute antibiotics and preparation method thereof |
| WO2015178786A1 (en) | 2014-05-23 | 2015-11-26 | PETER-WIRSKI, Maciej | Method of synthesis of monocaffeoylquinic or dicaffeoylquinic acid |
| CN110240544A (en) * | 2019-06-03 | 2019-09-17 | 西北农林科技大学 | A kind of chlorogenic acid method for extraction and purification and application |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100494393C (en) | 2009-06-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100494393C (en) | Technique for producing high purity chlorogenic acid in industrialization scale | |
| CN101973976B (en) | Method for extracting dihydromyricetin, ampelopsis grossedentata amylase and ampelopsis grossedentata polyphenol from ampelopsis grossedentata | |
| CN102491938B (en) | A kind of purification process of S-GI | |
| CN100396783C (en) | Chinese starjasmine stem lignin aglycone total extract and its extracting process | |
| CN102675188A (en) | Extraction method of 1-desoxynojirimycin in mulberry leaf | |
| CN103266154A (en) | Biological transformation method for preparing high-activity theasaponin | |
| CN1765935A (en) | Method for separating lentinan | |
| CN102993328A (en) | Method for comprehensively extracting polysaccharides, polyphenol and saponin from camellia oleifera abel defatted cakes | |
| CN102643315A (en) | Method for purifying phlorizin from apple velamen | |
| CN102327312A (en) | Method for extracting effective ingredients from leaf, stem and vine of honeysuckle | |
| CN101818184A (en) | Method for extracting rutin from sophora japonica | |
| CN1303078C (en) | Process for preparing effective constituent in tea | |
| CN202465570U (en) | Device for comprehensively extracting active substances in asparagus through multi-level membrane separation and purification | |
| CN107857826B (en) | Separation and purification method of blood sugar-reducing banana flower polysaccharide | |
| CN102432575B (en) | Method for extracting high-purity hesperetin from immature bitter orange | |
| CN102002072A (en) | Process for extracting flavone from date pit | |
| CN107857825A (en) | A kind of extracting method of radix tetrastigme polysaccharide | |
| CN1253462C (en) | Process for preparing morinda officinalis total oligosaccharide | |
| CN111349124A (en) | Method for extracting and separating phlorizin from lithocarpus polystachyus rehd | |
| CN102276751B (en) | Method for extracting glycosaminoglycan from bullacta exarata | |
| CN101962386A (en) | Process for extracting arteannuin by biological compound enzymes | |
| CN107954883B (en) | Method for extracting synephrine from mature navel orange peel | |
| CN102675106B (en) | Method for preparing high-purity chlorogenic acid by aluminum salt precipitation | |
| CN1506360A (en) | Method of extracting effective components in kudzu vine root | |
| CN105420293A (en) | Method for separating and purifying resveratrol from traditional Chinese medicine polygonum cuspidatum extraction solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: SICHUAN JIUZHANG BIOLOGICAL TECHNOLOGY CO., LTD. Free format text: FORMER NAME: JIUZHANG BIO-CHEMICAL ENGINEERING TECH. + SCIENCE DEVELOPMENT CO., LTD., SICHUAN |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 610041 Sichuan high tech Zone, Chengdu Province Park, No. two South Road, No. 10 Patentee after: SICHUAN JIUZHANG BIOTECHNOLOGY CO., LTD. Address before: 610041 Sichuan high tech Zone, Chengdu Province Park, No. two South Road, No. 10 Patentee before: Jiuzhang Bio-Chemical Engineering Tech. & Science Development Co., Ltd., Sichuan |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090603 Termination date: 20200414 |