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WO2012055253A1 - Regeneration method of silica gel for chromatographing coenzyme q10 - Google Patents

Regeneration method of silica gel for chromatographing coenzyme q10 Download PDF

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Publication number
WO2012055253A1
WO2012055253A1 PCT/CN2011/076093 CN2011076093W WO2012055253A1 WO 2012055253 A1 WO2012055253 A1 WO 2012055253A1 CN 2011076093 W CN2011076093 W CN 2011076093W WO 2012055253 A1 WO2012055253 A1 WO 2012055253A1
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Prior art keywords
column
polar solvent
silica gel
coenzyme
chromatographic
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PCT/CN2011/076093
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French (fr)
Chinese (zh)
Inventor
王炳荣
詹光煌
吴轶
付志杰
张斌
刘华英
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Inner Mongolia Kingdomway Pharmaceutical Ltd
Xiamen Kingdomway Group Co
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Inner Mongolia Kingdomway Pharmaceutical Ltd
Xiamen Kingdomway Group Co
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Publication of WO2012055253A1 publication Critical patent/WO2012055253A1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/10Selective adsorption, e.g. chromatography characterised by constructional or operational features
    • B01D15/20Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the conditioning of the sorbent material
    • B01D15/203Equilibration or regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/103Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/281Sorbents specially adapted for preparative, analytical or investigative chromatography
    • B01J20/282Porous sorbents
    • B01J20/283Porous sorbents based on silica
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/3433Regenerating or reactivating of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/34Regenerating or reactivating
    • B01J20/345Regenerating or reactivating using a particular desorbing compound or mixture
    • B01J20/3475Regenerating or reactivating using a particular desorbing compound or mixture in the liquid phase
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C403/00Derivatives of cyclohexane or of a cyclohexene or of cyclohexadiene, having a side-chain containing an acyclic unsaturated part of at least four carbon atoms, this part being directly attached to the cyclohexane or cyclohexene or cyclohexadiene rings, e.g. vitamin A, beta-carotene, beta-ionone
    • C07C403/02Derivatives of cyclohexane or of a cyclohexene or of cyclohexadiene, having a side-chain containing an acyclic unsaturated part of at least four carbon atoms, this part being directly attached to the cyclohexane or cyclohexene or cyclohexadiene rings, e.g. vitamin A, beta-carotene, beta-ionone having side-chains containing only carbon and hydrogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/16Systems containing only non-condensed rings with a six-membered ring the ring being unsaturated

Definitions

  • the invention belongs to the field of enzymology and organic chemistry, and relates to a method for regenerating chromatographic silica gel, in particular to a method for regenerating coenzyme Q10 chromatography silica gel. Background technique
  • Coenzyme Q10 (Ubiquinone, Coenzyme Q10, CoQI O) plays an important role in the transport of electrons and protons in the oxidative respiratory chain. It is the key to the formation of ATP, which protects and restores the integrity of biofilm structure, stabilizes membrane potential and enhances immune response. The role is widely used in the adjuvant treatment of heart failure, coronary heart disease, hypertension, diabetes, cancer, AIDS, acute and chronic hepatitis, Parkinson's disease and other diseases. In addition, Coenzyme Q10 is widely used in food, health care products and cosmetics industries, and the market prospect is very broad.
  • the traditional coenzyme Q10 production methods at home and abroad mainly include animal and plant tissue extraction methods, chemical synthesis methods and microbial fermentation methods.
  • the extraction method of animal and plant tissue is limited by the content of coenzyme Q10 in the raw material, and the extraction yield is low and the cost is high.
  • the chemical synthesis method produces cis and trans isomerism during synthesis, and a mixture of various isomers is obtained, which needs to be separated.
  • the synthesis cost is increased, and some toxic reagents are added during chemical synthesis, which also puts forward higher requirements for purification to obtain clinically applicable products;
  • microbial fermentation method is a new production method which has emerged in recent years, because microbial cells are easy to grow in large scale.
  • the product is completely natural in all-trans configuration, has high bioavailability, and is safe and efficient relative to chemical synthesis. There is almost no chemical poison residue in the product, easy to separate and purify, and the clinical curative effect is good, which is the most promising prospect. Production method.
  • the microbial fermentation method produces coenzyme Q10, and the purification process generally adopts the following process: After the fermentation liquid is filtered, the filter residue is dried and granulated to obtain coenzyme Q10 powder, and the powder is then soaked and extracted with an organic solvent. The extract is concentrated to a certain content and then subjected to silica gel column chromatography. The petroleum ether and the acetone mixed solvent are eluted, and the eluate is concentrated and concentrated under reduced pressure, and crystallized with anhydrous ethanol, and dried by filtration to obtain a crude crystal of coenzyme Q10.
  • silica gel As a kind of adsorbent, silica gel has a large specific surface area and strong adsorption capacity, and is widely used in column chromatography separation and purification in various industries such as medicine and chemical industry. During the column stratification, silica gel will adsorb some highly polar impurities, block the pores of the particles, and reduce their activity. The production cost of silica gel is also relatively high, and its production process pollutes the environment.
  • the column chromatography process accounts for more than 50% of the cost, and the silica gel consumption and solvent loss ⁇ A occupy the most important cost, making the production cost of coenzyme Q10 high.
  • Cipheral Patent Publication No. CN 101445435A describes a cleaning and purification process of coenzyme Q10: Coenzyme Q10 is dissolved in an organic solvent, and is packed in a high pressure liquid phase preparative column or a medium pressure silica gel packed column, eluted with an eluent, and collected in stages to obtain a high Purified coenzyme Q10 product. The packed silica gel is activated at a high temperature of 200 - 300 ° C and reused 10 - 200 times.
  • the method for regenerating silica gel adopts a high-temperature activation method, and the method has high energy consumption, and each time the column chromatography process is completed, the silica gel needs to be removed from the column, which not only has high labor intensity, but also causes solvent evaporation, Safety problems such as static ignition occur, and solvent loss is also large.
  • the high-temperature calcination method can remove the organic impurities in the silica gel, it also changes the internal pore structure of the silica gel, resulting in a decrease in the adsorption capacity of the silica gel.
  • U.S. Patent No. 2007/0025976 A1 discloses a purification process for coenzyme Q10, mentioning a method for regenerating silica gel: eluting with 1 column volume of ethanol at room temperature, and then using 4 - 5 column volumes of hexane at 50 Elution at °C.
  • the inventor discovered a coenzyme by creative labor and a large number of experiments.
  • the regeneration method of Q10 chromatography silica gel and surprisingly found that the silica gel column after separation and purification of coenzyme Q10 can be reused after being treated by the method of the invention (ie, for chromatography of coenzyme Q10), and thus used-regenerated
  • the number of cycles can be up to 20 or even more than 100 times, while the chromatographic yield can be maintained at 90% or 95% or even 98%.
  • a method for regenerating a coenzyme Q10 chromatography silica gel which comprises washing a column in a reverse direction from a bottom of a column with a highly polar solvent.
  • silica gel column chromatography itself is a normal phase chromatography.
  • the weakly polar substances are eluted first, and the strong polar impurities are adsorbed on the column head. Columns, when the strong polar impurities are eluted downward, will again contaminate the silica gel without adsorbing strong polar impurities, thus causing the use of silica gel to be greatly reduced.
  • a regeneration method according to any one of the present invention, characterized by any one or more of the following items (1) to (4):
  • the highly polar solvent is one or more selected from the group consisting of ethyl acetate, acetone, methyl ethyl ketone, ethanol (preferably acetone), or a mixture of a highly polar solvent and a low polar solvent, wherein The polar solvent accounts for more than 50% by volume of the mixed liquid, and is preferably greater than 90%;
  • the high polar solvent is used in an amount of from 1 to 5 column volumes, preferably from 2-3 times column volume;
  • the volume of the column is 0. 5 - 2 times the column volume / hour, preferably 0.5 - 1 column volume / hour;
  • the temperature of the highly polar solvent used for column washing is 20 - 50.
  • a regeneration method characterized in that Afterwards, a low polarity solvent is introduced from the top of the column for forward equilibrium.
  • a regeneration method according to any one of the inventions, characterized by the following (1)
  • the low-polar solvent is selected from one or more of petroleum ether, pentane, n-hexane, and heptane, or a mixture of a highly polar solvent and a low-polar solvent, wherein the low-polar solvent accounts for The volume of the mixed solution is greater than 50%, and preferably greater than 90%;
  • the low polar solvent is used in an amount of from 1 to 5 column volumes, preferably from 2 to 4 column volumes, more preferably from 3 column volumes;
  • the equilibrium flow rate is 0.5 - 2 column volumes / hour, preferably 0.5 - 1 column volume / hour;
  • the temperature of the lower-grade solvent used for the balance is 20* € - 50* €.
  • the coenzyme Q10 chromatography silica gel subjected to the regeneration treatment according to the method described in any one of the above is used for separating and purifying the coenzyme Q10, and the "regeneration-use” process is carried out one or more times; preferably, 15 to 25 times, More preferably, it is carried out 20 to 25 times, and more preferably 20 times. This allows the column to be reused more than 20 times.
  • the "regeneration” refers to a regeneration treatment according to the method described in any one of the above, wherein the "use” refers to the separation of the coenzyme Q10 chromatography silica gel after the regeneration treatment according to the method described above. Purification of coenzyme Q10.
  • the "use” step may be a method commonly used in the art, for example, referring to the product specification or the steps shown in the embodiment 1.
  • the regeneration method is carried out according to the following steps 1) - 4):
  • the pH of the hydrogen peroxide can be adjusted with K0H or NaOH.
  • Step 1) The action of the hydrogen peroxide is to remove the oxidized impurities of the impurities adsorbed in the silica gel. Since hydrogen peroxide is alkaline, it is necessary to replace the alkaline hydrogen peroxide with hot water, otherwise it will remain in the silica gel column and affect the next chromatography. Hydrogen peroxide and hot water can effectively remove the strong polar impurities that are difficult to elute from organic solvents.
  • the regeneration method according to any one of the invention, wherein the water in the step 2) is preferably deionized water.
  • the amount of hydrogen peroxide and water is independently from 1 to 5 column volumes; preferably two column volumes.
  • the temperature of the hydrogen peroxide and the water is independently 50* € - ⁇ ⁇ ; preferably 70 - 80* €.
  • the regeneration method according to any one of the present invention, wherein the drying in the step 3) is atmospheric drying or reduced pressure drying, and preferably drying under reduced pressure.
  • the term "silica gel” or “silica gel column” or “silica gel column” has the same meaning unless specifically stated otherwise, specifically, a silica gel column after separation and purification of coenzyme Q10.
  • the inner diameter is 25 - 500 mm
  • the column length is 300 - 5000 mm
  • the silica gel mesh is 60 - 400 mesh
  • the inner diameter is 400 legs and the column length is 4000 legs.
  • the column pressure is 0. 1 - 2 MPa.
  • Coenzyme Q10 Chromatography Silica Gel refers to a silica gel column after separation and purification of Coenzyme Q10; specifically, the sample solution is an extract extracted from Coenzyme Q10 powder by an organic solvent.
  • the organic solvent may be one or more of petroleum ether, pentane, n-hexane, heptane, preferably petroleum ether and or n-hexane.
  • the term "highly polar solvent” means a solvent having a solvent polarity index of > 4. 0.
  • the highly polar solvent is one or more selected from the group consisting of ethyl acetate, acetone, methyl ethyl ketone, and ethanol, or a mixture of a high polar solvent and a low polar solvent, wherein the high polar solvent accounts for The volume of the mixed liquor is greater than 50%, and preferably greater than 90%, more preferably 100%.
  • the term "low-polar solvent” means a solvent having a solvent polarity index ⁇ 0.2.
  • the low-polar solvent is selected from one or more of petroleum ether, pentane, n-hexane, and heptane, or a mixture of a highly polar solvent and a low-polar solvent, wherein the low-polar solvent accounts for The volume of the mixed liquor is greater than 50%, and preferably greater than 90%, more preferably 100%.
  • the calculation method of the chromatographic yield the chromatographic solution containing the coenzyme Q10 is collected in stages, and the chromatographic solution containing only the coenzyme Q10 spot is combined by TLC, and the coenzyme Q10 in the chromatographic solution is detected by HPLC.
  • chromatographic yield (chromatography volume X chromatography liquid external standard content) I (loading volume X sample liquid content) X picture.
  • the effect of the repeated use of the silica gel is judged: comparing the chromatographic yields under the same loading amount, eluent, and elution conditions, when the chromatographic yield is greater than or equal to 90%, it is judged that the re-use effect is higher.
  • the chromatographic yield is less than 90%, it is judged that the repeated use effect is deteriorated.
  • Adopt column-washing column to achieve continuous production, reduce the number of disassembly and assembly columns, and achieve a fully enclosed system throughout the production process, which not only reduces labor intensity, but also reduces solvent volatilization and achieves the purpose of clean production;
  • Fig. 1 Schematic diagram of the silica gel regeneration process. detailed description
  • Example 1 Chromatographic effect of a new silica gel column (first use)
  • the inner diameter of the column is 400 legs, the column length is 4000 legs, and the silica gel is 200Kg (200 ⁇ 300 mesh).
  • the column is packed by wet method, and the column is hammered with a rubber hammer to make the silica gel tightly packed.
  • the packed column was equilibrated with petroleum ether for 2 hours.
  • Example 1 After eluting the column after coenzyme Q10, 1500 L of acetone 30 was pumped from the bottom of the column at a flow rate of 500 L/h to wash the column in the opposite direction until the top of the column was colorless, and then 500 L/ from the top of the column. The flow rate of h is pumped into a petroleum ether equilibrium column at a temperature of 1500 L. The chromatographic yield was 94.8%, chromatographic. The chromatographic yield of the recombination was 94.8%, and the chromatographic yield of the recombination was 94.8%. 10% ⁇ The liquid primary peak HPLC area normalized content of 98. 10%.
  • Example 3 Chromatographic effect of a silica gel column after regeneration (after 20 "regeneration-use" processes)
  • the silica gel chromatography column was repeatedly used according to the column washing method and the chromatographic method of Example 2. According to the sample loading, elution method and collection method of the same example, the 20th chromatographic yield was 93. 8% ⁇ The HPLC content of the main peak of the chromatographic solution was 98.7%.
  • Example 4 Chromatographic effect of a silica gel column after regeneration (after 21 "regeneration-use" processes)
  • the silica gel column used in Example 3 was used 20 times, and was pumped from the bottom of the column to a pH of 1:1, a concentration of 5%, and a temperature of 80. (, the amount of 1000L of hydrogen peroxide, and then pumped into 1000L temperature 80 e C hot water wash, after washing, use N 2 to dry the water, remove the silica gel, placed in a 150 ⁇ drier vacuum drying to silica gel moisture less than 5 %.
  • the crystallization, the chromatographic yield was 94.5%, the layer was subjected to the 21st chromatography.
  • the chromatography yield was 94.5%.
  • the HPLC main area of the main peak of the liquid separation is 98. 08% 0
  • Example 5 The chromatographic effect of the silica gel column after regeneration (after 100 "regeneration-use" processes)
  • Example 4 The silica gel column of Example 4 was used, and the regeneration method combined with Example 2 and Example 4 (i.e., 20 "regeneration-use” processes per the regeneration method of Example 2 was carried out, and the regeneration method of Example 4 was repeated once. 05% ⁇ The chromatographic solution of the main peak HPLC area normalized content of 98. 05%, the chromatographic yield of the main peak of the chromatographic solution is 98.05%. . Comparative Example 1: Chromatographic effect of silica gel column using positive direction column regeneration treatment. Silica gel was chromatographed once in the same manner as in Example 1.

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A regeneration method of chromatographic silica gel, especially a regeneration method of silica gel for chromatographing coenzyme Q10 is provided, wherein a high polar solvent is fed from the bottom of the chromatographic column to wash the column in the reverse direction. The treated chromatographic column can be repeatedly used to separate and purify coenzyme Q10. The regeneration method allows the repeated use of the chromatographic column for over 20 times, even over 100 times, while maintaining a good chromatographic effect. The method also has decreased production cost and labor intensity, and is safe and environment-friendly.

Description

一种辅酶 Q10层析硅胶的再生方法 技术领域  Method for regenerating coenzyme Q10 chromatography silica gel

本发明属于酶学和有机化学领域, 涉及一种层析硅胶的再生 方法, 特别涉及一种辅酶 Q10层析硅胶的再生方法。 背景技术  The invention belongs to the field of enzymology and organic chemistry, and relates to a method for regenerating chromatographic silica gel, in particular to a method for regenerating coenzyme Q10 chromatography silica gel. Background technique

辅酶 Q10 (Ubiquinone, Coenzyme Q10, CoQI O) 在氧化呼吸链 中起传递电子和质子的重要作用, 是形成 ATP的关键, 具有保护和 恢复生物膜结构的完整性、 稳定膜电位和增强免疫反应等作用, 被 广泛应用于心力衰竭、 冠心病、 高血压病、糖尿病、 癌症、 艾滋病、 急慢性肝炎、 帕金森症等疾病的辅助性治疗。 此外, 辅酶 Q10还被 广泛地用于食品、 保健品和化妆品等行业, 市场前景十分广阔。  Coenzyme Q10 (Ubiquinone, Coenzyme Q10, CoQI O) plays an important role in the transport of electrons and protons in the oxidative respiratory chain. It is the key to the formation of ATP, which protects and restores the integrity of biofilm structure, stabilizes membrane potential and enhances immune response. The role is widely used in the adjuvant treatment of heart failure, coronary heart disease, hypertension, diabetes, cancer, AIDS, acute and chronic hepatitis, Parkinson's disease and other diseases. In addition, Coenzyme Q10 is widely used in food, health care products and cosmetics industries, and the market prospect is very broad.

国内外传统的辅酶 Q10生产方法主要有动植物组织提取法、化 学合成法和微生物发酵法三种。动植物组织提取法受限于原料中辅 酶 Q10的含量, 提取的产量低、 成本高; 化学合成法在合成时会发 生顺、 反异构, 得到各类异构体的混合物, 需要分离, 也增加了合 成成本, 在化学合成时会加入一些有毒试剂, 对纯化获得适用于临 床的产品也提出了更高的要求;微生物发酵法是近年兴起的新生产 方法, 由于微生物细胞易于大规模培养生长, 产品完全为天然的全 反式构型, 生物利用度高, 而且相对于化学合成法安全、 高效, 产 品中几乎无化学毒害物质残留, 易于分离純化, 临床疗效较好, 是 最有开发前景的生产方法。  The traditional coenzyme Q10 production methods at home and abroad mainly include animal and plant tissue extraction methods, chemical synthesis methods and microbial fermentation methods. The extraction method of animal and plant tissue is limited by the content of coenzyme Q10 in the raw material, and the extraction yield is low and the cost is high. The chemical synthesis method produces cis and trans isomerism during synthesis, and a mixture of various isomers is obtained, which needs to be separated. The synthesis cost is increased, and some toxic reagents are added during chemical synthesis, which also puts forward higher requirements for purification to obtain clinically applicable products; microbial fermentation method is a new production method which has emerged in recent years, because microbial cells are easy to grow in large scale. The product is completely natural in all-trans configuration, has high bioavailability, and is safe and efficient relative to chemical synthesis. There is almost no chemical poison residue in the product, easy to separate and purify, and the clinical curative effect is good, which is the most promising prospect. Production method.

微生物发酵法生产辅酶 Q10, 其提纯过程一般采用如下工艺: 发酵液经过过滤后, 滤渣干燥制粒, 得到辅酶 Q10菌粉, 菌粉再用 有机溶剂浸泡提取。 提取液浓缩至一定含量后上硅胶柱层析, 采用 石油醚、 丙酮混合溶剂进行洗脱, 洗脱液经减压浓缩干, 加无水乙 醇结晶, 过滤烘干得到辅酶 Q10结晶粗品。 The microbial fermentation method produces coenzyme Q10, and the purification process generally adopts the following process: After the fermentation liquid is filtered, the filter residue is dried and granulated to obtain coenzyme Q10 powder, and the powder is then soaked and extracted with an organic solvent. The extract is concentrated to a certain content and then subjected to silica gel column chromatography. The petroleum ether and the acetone mixed solvent are eluted, and the eluate is concentrated and concentrated under reduced pressure, and crystallized with anhydrous ethanol, and dried by filtration to obtain a crude crystal of coenzyme Q10.

硅胶作为一种吸附剂, 由于具有很大的比表面积, 吸附力强, 广泛应用于医药、 化工等多种行业的柱层析分离提純。 硅胶在柱层 析过程中, 会吸附一些强极性的杂质, 堵塞颗粒孔道, 使其活性下 降。 硅胶的生产成本也比较高, 而且其生产过程会污染环境。  As a kind of adsorbent, silica gel has a large specific surface area and strong adsorption capacity, and is widely used in column chromatography separation and purification in various industries such as medicine and chemical industry. During the column stratification, silica gel will adsorb some highly polar impurities, block the pores of the particles, and reduce their activity. The production cost of silica gel is also relatively high, and its production process pollutes the environment.

在辅酶 Q10的提纯过程中, 柱层析工序所占成本超过 50%, 其 中硅胶消耗及溶剂损耗^ A占据最主要的成本,使得辅酶 Q10的生 产成本居高不下。  In the purification process of coenzyme Q10, the column chromatography process accounts for more than 50% of the cost, and the silica gel consumption and solvent loss ^ A occupy the most important cost, making the production cost of coenzyme Q10 high.

中国专利公开号 CN 101445435A介绍了一种辅酶 Q10清洁纯化 工艺: 将辅酶 Q10用有机溶剂溶解, 应用高压液相制备柱或中压硅 胶填充柱, 以洗脱剂洗脱,分段收集,获得高纯度的辅酶 Q10产品。 所述装柱的硅胶经 200 - 300°C高温活化后重复使用 10 - 200次。其 硅胶再生的方法采用的是高温活化的方法, 该方法能耗大, 而且每 次柱层析过程完成后均需将硅胶从柱内拆下来, 不但劳动强度大, 而且还会造成溶剂挥发、产生静电着火等安全问题,溶剂损耗也大。 高温煅烧的方法虽能将硅胶内的有机杂质去除,但同时也会改变硅 胶内部孔径结构, 造成硅胶吸附力下降。  Chinese Patent Publication No. CN 101445435A describes a cleaning and purification process of coenzyme Q10: Coenzyme Q10 is dissolved in an organic solvent, and is packed in a high pressure liquid phase preparative column or a medium pressure silica gel packed column, eluted with an eluent, and collected in stages to obtain a high Purified coenzyme Q10 product. The packed silica gel is activated at a high temperature of 200 - 300 ° C and reused 10 - 200 times. The method for regenerating silica gel adopts a high-temperature activation method, and the method has high energy consumption, and each time the column chromatography process is completed, the silica gel needs to be removed from the column, which not only has high labor intensity, but also causes solvent evaporation, Safety problems such as static ignition occur, and solvent loss is also large. Although the high-temperature calcination method can remove the organic impurities in the silica gel, it also changes the internal pore structure of the silica gel, resulting in a decrease in the adsorption capacity of the silica gel.

美国专利 US2007/0025976A1公开了一种辅酶 Q10的提纯工艺, 提到一种硅胶的再生方法: 在室温下用 1倍柱体积的乙醇洗脱, 然 后用 4 - 5倍柱体积的己烷在 50°C下洗脱。  U.S. Patent No. 2007/0025976 A1 discloses a purification process for coenzyme Q10, mentioning a method for regenerating silica gel: eluting with 1 column volume of ethanol at room temperature, and then using 4 - 5 column volumes of hexane at 50 Elution at °C.

此外, 还有专利文献报道了制备其它产品后硅胶柱的再生方 法。  In addition, there is a patent document reporting a method of regenerating a silica gel column after preparing other products.

但是, 现有的专利文献关于硅胶柱(特别是制备辅酶 Q10后的 硅胶柱)的再生方法的相关报道, 都是采用正向洗柱的方法, 硅胶 重复使用的次数少。 发明内容 However, the related patent documents report on the regeneration method of the silica gel column (especially the silica gel column after the preparation of the coenzyme Q10) are all based on the method of positive column washing, and the number of times the silica gel is repeatedly used is small. Summary of the invention

本发明人经过创造性的劳动和大量的试验, 发现了一种辅酶 The inventor discovered a coenzyme by creative labor and a large number of experiments.

Q10 层析硅胶的再生方法, 并且惊奇地发现, 对于分离提纯辅酶 Q10 后的硅胶柱, 经过本发明的方法处理后能够再次使用 (即用 于辅酶 Q10 的层析) , 并且如此使用 -再生的循环次数可达 20 甚至 100次以上,同时层析收率能够保持 90%或 95%甚至 98%以上。 由此提供了下述发明: 一种辅酶 Q10层析硅胶的再生方法, 其特征在于, 从柱底进 高极性溶剂进行反方向洗柱。 The regeneration method of Q10 chromatography silica gel, and surprisingly found that the silica gel column after separation and purification of coenzyme Q10 can be reused after being treated by the method of the invention (ie, for chromatography of coenzyme Q10), and thus used-regenerated The number of cycles can be up to 20 or even more than 100 times, while the chromatographic yield can be maintained at 90% or 95% or even 98%. Thus, the following invention is provided: A method for regenerating a coenzyme Q10 chromatography silica gel, which comprises washing a column in a reverse direction from a bottom of a column with a highly polar solvent.

不拘于理论的束缚, 一种可能的原因是硅胶柱层析本身是一种 正相层析,弱极性物质先被洗脱下来,强极性杂质被吸附在柱头上, 若采用正向洗柱, 强极性杂质被往下洗脱的过程中会再次污染没有 吸附强极性杂质的硅胶, 从而造成硅胶的使用次数大大减少。  Without being bound by theory, one possible reason is that silica gel column chromatography itself is a normal phase chromatography. The weakly polar substances are eluted first, and the strong polar impurities are adsorbed on the column head. Columns, when the strong polar impurities are eluted downward, will again contaminate the silica gel without adsorbing strong polar impurities, thus causing the use of silica gel to be greatly reduced.

根据本发明任一项所述的再生方法, 其特征在于如下的 (1 ) - ( 4 )项中的任一项或多项:  A regeneration method according to any one of the present invention, characterized by any one or more of the following items (1) to (4):

( 1 )所述高极性溶剂为选自乙酸乙酯、丙酮、丁酮、 乙醇(优 选丙酮) 中的一种或者多种、 或者高极性溶剂和低极性溶剂的混 合液, 其中高极性溶剂占混合液的体积大于 50%, 并且优选大于 90%;  (1) The highly polar solvent is one or more selected from the group consisting of ethyl acetate, acetone, methyl ethyl ketone, ethanol (preferably acetone), or a mixture of a highly polar solvent and a low polar solvent, wherein The polar solvent accounts for more than 50% by volume of the mixed liquid, and is preferably greater than 90%;

( 2 ) 所述高极性溶剂的用量为 1 - 5倍柱体积, 优选 2-3倍 柱体积;  (2) The high polar solvent is used in an amount of from 1 to 5 column volumes, preferably from 2-3 times column volume;

( 3 )所述洗柱的流速为 0. 5 - 2倍柱体积 /小时, 优选 0. 5 - 1倍柱体积 /小时;  The volume of the column is 0. 5 - 2 times the column volume / hour, preferably 0.5 - 1 column volume / hour;

( 4 ) 洗柱所用高极性溶剂的温度为 20 - 50 。  (4) The temperature of the highly polar solvent used for column washing is 20 - 50.

根据本发明任一项所述的再生方法, 其特征在于, 在洗柱之 后, 从柱顶进低极性溶剂进行正向平衡。 A regeneration method according to any one of the present invention, characterized in that Afterwards, a low polarity solvent is introduced from the top of the column for forward equilibrium.

根据本发明任一项所述的再生方法, 其特征在于如下的 (1) A regeneration method according to any one of the inventions, characterized by the following (1)

- (4)项中的任一项或多项: - Any one or more of (4):

(1) 所述低极性溶剂选自石油醚、 戊烷、 正己烷、 庚烷中 的一种或者多种, 或者高极性溶剂和低极性溶剂的混合液, 其中 低极性溶剂占混合液的体积大于 50%, 并且优选大于 90%;  (1) The low-polar solvent is selected from one or more of petroleum ether, pentane, n-hexane, and heptane, or a mixture of a highly polar solvent and a low-polar solvent, wherein the low-polar solvent accounts for The volume of the mixed solution is greater than 50%, and preferably greater than 90%;

(2)所述低极性溶剂的用量为 1-5倍柱体积, 优选地, 为 2 - 4倍柱体积, 更优选地, 为 3倍柱体积;  (2) The low polar solvent is used in an amount of from 1 to 5 column volumes, preferably from 2 to 4 column volumes, more preferably from 3 column volumes;

(3)所述平衡的流速为 0.5- 2倍柱体积 /小时, 优选 0.5-1 倍柱体积 /小时;  (3) the equilibrium flow rate is 0.5 - 2 column volumes / hour, preferably 0.5 - 1 column volume / hour;

(4)平衡所用低级性溶剂的温度为 20*€ - 50*€。  (4) The temperature of the lower-grade solvent used for the balance is 20*€ - 50*€.

将按照上述任一项所述的方法进行再生处理后的辅酶 Q10层 析硅胶用于分离提纯辅酶 Q10, 并且将这样的 "再生-使用" 过 程进行一次或多次;优选进行 15 - 25次, 更优选进行 20 - 25次, 进一步优选进行 20次。 如此可实现层析柱重复使用 20次以上。 所述 "再生" 是指按照上述任一项所述的方法进行再生处理, 所 述 "使用" 是指将按照上述任一项所述的方法进行再生处理后的 辅酶 Q10层析硅胶用于分离提纯辅酶 Q10。 所述 "使用" 的步骤 可以是本领域常用的方法, 例如参照产品说明书或者实施例 1所 示的步骤。  The coenzyme Q10 chromatography silica gel subjected to the regeneration treatment according to the method described in any one of the above is used for separating and purifying the coenzyme Q10, and the "regeneration-use" process is carried out one or more times; preferably, 15 to 25 times, More preferably, it is carried out 20 to 25 times, and more preferably 20 times. This allows the column to be reused more than 20 times. The "regeneration" refers to a regeneration treatment according to the method described in any one of the above, wherein the "use" refers to the separation of the coenzyme Q10 chromatography silica gel after the regeneration treatment according to the method described above. Purification of coenzyme Q10. The "use" step may be a method commonly used in the art, for example, referring to the product specification or the steps shown in the embodiment 1.

每当层析柱重复使用 15- 25次(优选 20次)之后, 再生方 法按照如下的步骤 1 ) - 4 )进行:  Whenever the column is reused 15-25 times (preferably 20 times), the regeneration method is carried out according to the following steps 1) - 4):

1)用双氧水反方向洗柱一次或多次;  1) Wash the column one or more times with hydrogen peroxide in the opposite direction;

2)用水反方向洗柱一次或多次;  2) Washing the column one or more times with the opposite direction of water;

3)拆下硅胶于 1001C - 150X烘干至水分小于 5% (w/w) ; 4 ) 重新装柱。 该方法能够实现硅胶的使用次数达到 100次以上。 3) Remove the silica gel and dry it at 1001C - 150X until the moisture is less than 5% (w/w); 4) Repack the column. The method can achieve the use of silica gel more than 100 times.

根据本发明任一项所述的再生方法, 其中, 步骤 1 ) 中双氧 水的 pH为 9 - 11; 优选为 10. 5-11。 所述双氧水的 pH可以用 K0H 或 NaOH调节。  The regeneration method according to any one of the present invention, wherein the pH of the hydrogen peroxide in the step 1) is 9 - 11; preferably 10. 5 - 11. The pH of the hydrogen peroxide can be adjusted with K0H or NaOH.

步骤 1 ) 中双氧水作用是使吸附在硅胶内的杂质氧化分解除 去。 由于双氧水是碱性的, 所以需用热水再将碱性的双氧水置换 出来, 否则会残留在硅胶柱内, 对下一次的层析造成影响。 双氧 水洗和热水可有效清除有机溶剂难以洗脱掉的那部分强极性杂 质。  Step 1) The action of the hydrogen peroxide is to remove the oxidized impurities of the impurities adsorbed in the silica gel. Since hydrogen peroxide is alkaline, it is necessary to replace the alkaline hydrogen peroxide with hot water, otherwise it will remain in the silica gel column and affect the next chromatography. Hydrogen peroxide and hot water can effectively remove the strong polar impurities that are difficult to elute from organic solvents.

根据本发明任一项所述的再生方法, 其中, 步骤 1 ) 中双氧 水的浓度为 3 % - 20 % ( w/w ) ; 优选 5%- 10% ( w/w ) 。  The regeneration method according to any one of the present invention, wherein the concentration of the hydrogen peroxide in the step 1) is from 3 % to 20% (w/w); preferably from 5% to 10% (w/w).

根据本发明任一项所述的再生方法, 其中, 步骤 2 ) 中的水 优选去离子水。  The regeneration method according to any one of the invention, wherein the water in the step 2) is preferably deionized water.

根据本发明任一项所述的再生方法,其中, 步骤 1 )和 2 )中, 双氧水和水的用量独立地为 1 - 5倍柱体积; 优选 2倍柱体积。  The regeneration method according to any one of the invention, wherein, in steps 1) and 2), the amount of hydrogen peroxide and water is independently from 1 to 5 column volumes; preferably two column volumes.

根据本发明任一项所述的再生方法,其中, 步骤 1 )和 2 )中, 双氧水和水的温度独立地为 50*€ - Ι ΟΟ ; 优选 70 - 80*€。  The regeneration method according to any one of the present invention, wherein, in the steps 1) and 2), the temperature of the hydrogen peroxide and the water is independently 50*€ - Ι ΟΟ; preferably 70 - 80*€.

根据本发明任一项所述的再生方法, 其中, 步骤 3 ) 中的烘 干为常压烘干或减压烘干, 并且优选减压烘干。 在本发明中, 除非有特别说明, 术语 "硅胶" 或 "硅胶柱" 或 "硅胶层析柱" 具有相同的含义, 具体地是指经分离提纯辅酶 Q10后的硅胶层析柱。 在本发明的一个实施方案中, 其内径 25 - 500mm, 柱长 300 - 5000mm, 硅胶目数 60 - 400目; 在本发明的一 个具体的实施方案中, 其内径 400腿, 柱长 4000腿, 硅胶 200Kg ( 200 - 300目 )。 可选地, 上述硅胶的水分小于 5%, 柱压 0. 1 - 2MPa。 The regeneration method according to any one of the present invention, wherein the drying in the step 3) is atmospheric drying or reduced pressure drying, and preferably drying under reduced pressure. In the present invention, the term "silica gel" or "silica gel column" or "silica gel column" has the same meaning unless specifically stated otherwise, specifically, a silica gel column after separation and purification of coenzyme Q10. In one embodiment of the invention, the inner diameter is 25 - 500 mm, the column length is 300 - 5000 mm, and the silica gel mesh is 60 - 400 mesh; in a specific embodiment of the invention, the inner diameter is 400 legs and the column length is 4000 legs. Silicone 200Kg (200 - 300 mesh). 5 - The column pressure is 0. 1 - 2 MPa.

在本发明中, 除非有特别说明, 术语 "辅酶 Q10层析硅胶" 是指分离提纯辅酶 Q10后的硅胶柱; 具体地, 其上样液为用有机 溶剂从辅酶 Q10菌粉中提取的提取液, 所述有机溶剂可以是石油 醚、 戊烷、 正己烷、 庚烷中的一种或多种, 优选石油醚和或正己 烷。  In the present invention, unless otherwise specified, the term "Coenzyme Q10 Chromatography Silica Gel" refers to a silica gel column after separation and purification of Coenzyme Q10; specifically, the sample solution is an extract extracted from Coenzyme Q10 powder by an organic solvent. The organic solvent may be one or more of petroleum ether, pentane, n-hexane, heptane, preferably petroleum ether and or n-hexane.

在本发明中, 术语 "高极性溶剂" 是指溶剂极性指数 > 4. 0 的溶剂。 具体地, 所述高极性溶剂为选自乙酸乙酯、 丙酮、 丁酮、 乙醇中的一种或者多种、或者高极性溶剂和低极性溶剂的混合液, 其中高极性溶剂占混合液的体积大于 50%, 并且优选大于 90%, 更 优选为 100 %。  In the present invention, the term "highly polar solvent" means a solvent having a solvent polarity index of > 4. 0. Specifically, the highly polar solvent is one or more selected from the group consisting of ethyl acetate, acetone, methyl ethyl ketone, and ethanol, or a mixture of a high polar solvent and a low polar solvent, wherein the high polar solvent accounts for The volume of the mixed liquor is greater than 50%, and preferably greater than 90%, more preferably 100%.

在本发明中, 术语 "低极性溶剂" 是指溶剂极性指数 < 0. 2 的溶剂。 具体地, 所述低极性溶剂选自石油醚、 戊烷、 正己烷、 庚烷中的一种或者多种,或者高极性溶剂和低极性溶剂的混合液, 其中低极性溶剂占混合液的体积大于 50%, 并且优选大于 90%, 更 优选为 100 %。  In the present invention, the term "low-polar solvent" means a solvent having a solvent polarity index < 0.2. Specifically, the low-polar solvent is selected from one or more of petroleum ether, pentane, n-hexane, and heptane, or a mixture of a highly polar solvent and a low-polar solvent, wherein the low-polar solvent accounts for The volume of the mixed liquor is greater than 50%, and preferably greater than 90%, more preferably 100%.

在本发明中, 层析收率的计算方法: 分段收集含辅酶 Q10的 层析液, 采用 TLC检测, 合并只含辅酶 Q10斑点的层析液, 取样 用 HPLC检测层析液中的辅酶 Q10外标含量及面积归一法含量,层 析收率 = (层析液体积 X层析液外标含量) I (上样液体积 X上样液 含量) X画。  In the present invention, the calculation method of the chromatographic yield: the chromatographic solution containing the coenzyme Q10 is collected in stages, and the chromatographic solution containing only the coenzyme Q10 spot is combined by TLC, and the coenzyme Q10 in the chromatographic solution is detected by HPLC. External standard content and area normalized content, chromatographic yield = (chromatography volume X chromatography liquid external standard content) I (loading volume X sample liquid content) X picture.

在本发明中, 硅胶重复使用效果判断: 对比相同上样量、 洗 脱剂、 洗脱条件下层析收率的高低, 当层析收率大于或等于 90%, 则判断为重复使用效果较好, 当层析收率小于 90%, 则判断为重 复使用效果变差。 发明的有益效果 In the present invention, the effect of the repeated use of the silica gel is judged: comparing the chromatographic yields under the same loading amount, eluent, and elution conditions, when the chromatographic yield is greater than or equal to 90%, it is judged that the re-use effect is higher. Preferably, when the chromatographic yield is less than 90%, it is judged that the repeated use effect is deteriorated. Advantageous effects of the invention

1. 采用反方向洗柱技术,有效防止正向洗柱时吸附柱头的强 极性杂质再次污染其他硅胶,使层析硅胶可重复使用 100次以上, 大大降低层析硅胶的消耗, 从而降低生产成本;  1. Adopting the reverse column washing technology to effectively prevent the strong polar impurities of the adsorption column head from contaminating other silica gels during the forward washing process, so that the chromatography silica gel can be reused more than 100 times, which greatly reduces the consumption of chromatography silica gel, thereby reducing production. Cost

2. 采用柱内洗柱, 实现连续生产, 减少拆装柱的次数, 整个 生产过程做到全封闭体系, 既减轻劳动强度, 又减少溶剂挥发, 达到清洁生产的目的;  2. Adopt column-washing column to achieve continuous production, reduce the number of disassembly and assembly columns, and achieve a fully enclosed system throughout the production process, which not only reduces labor intensity, but also reduces solvent volatilization and achieves the purpose of clean production;

3. 采用在线洗柱替代传统的锅内搅拌洗涤,洗涤时溶剂浓度 梯度大, 显著提高了洗柱的效率。 附图说明  3. Online washing column is used to replace the traditional in-pot stirring and washing. The solvent concentration gradient is large during washing, which significantly improves the efficiency of column washing. DRAWINGS

Fig. 1: 硅胶再生流程示意图。 具体实施方式  Fig. 1: Schematic diagram of the silica gel regeneration process. detailed description

下面将结合实施例对本发明的实施方案进行详细描述, 但是 本领域技术人员将会理解, 下面的实施例仅用于说明本发明, 而 不应视为限定本发明的范围。 实施例中未注明具体条件者, 按照 常规条件或制造商建议的条件进行。 所用试剂或仪器未注明生产 厂商者, 均为可以通过市购获得的常规产品。 实施例 1 : 新的硅胶柱的层析效果(第 1次使用)  The embodiments of the present invention will be described in detail below with reference to the accompanying drawings. If no specific conditions are specified in the examples, they are carried out according to the general conditions or the conditions recommended by the manufacturer. If the reagents or instruments used are not specified by the manufacturer, they are all commercially available products. Example 1 : Chromatographic effect of a new silica gel column (first use)

层析柱内径 400腿,柱长 4000腿,硅胶 200Kg( 200 ~ 300目 ), 采用湿法装柱, 边装边用橡皮锤敲打柱体,使硅胶装的紧密结实。 装完后的层析柱用石油醚平衡 2小时。  The inner diameter of the column is 400 legs, the column length is 4000 legs, and the silica gel is 200Kg (200 ~ 300 mesh). The column is packed by wet method, and the column is hammered with a rubber hammer to make the silica gel tightly packed. The packed column was equilibrated with petroleum ether for 2 hours.

取 300L辅酶 Q10浸膏(采用石油醚从辅酶 Q10菌粉中提取的 浓缩物, 含量 30mg/ml ) , 通过柱塞式计量泵上硅胶柱层析, 上 完样后用石油醚 /丙酮(20/1 )混合溶剂进行洗脱, TLC检测收集 辅酶 Q10层析液,合并合格的层析液,取样用 HPLC检测层析液中 的辅酶 Q10含量, 层析收率为 95. 3%, 层析液主峰 HPLC面积归一 法含量为 98. 12%。 实施例 2: 再生后硅胶柱的层析效果(经过 1个 "再生-使 用" 过程) Take 300L Coenzyme Q10 extract (concentrated with petroleum ether from coenzyme Q10 powder, content 30mg/ml), through silica gel column chromatography on a plunger metering pump After completion, elute with petroleum ether/acetone (20/1) mixed solvent, collect Coenzyme Q10 chromatography solution by TLC, combine qualified chromatographic solution, and sample the HPLC to detect the content of coenzyme Q10 in the chromatographic solution. The yield of the HPLC method of the main peak of the chromatographic solution was 98.12%. Example 2: Chromatographic effect of a silica gel column after regeneration (after a "regeneration-use" process)

实施例 1洗脱完辅酶 Q10后的层析柱,从柱底以 500L/h的流 速泵入 1500L 温度 30 的丙酮进行反方向洗柱至柱顶流出液无 色, 再从柱顶以 500L/h的流速泵入 1500L温度 的石油醚平 衡层析柱。 平衡后的层析柱重新用来进行辅酶 Q10浸膏的层析, 按同实施例 1的上样量、 洗脱方式及收集方法, 重复使用的层析 收率为 94. 8%, 层析液主峰 HPLC面积归一法含量为 98. 10%。 实施例 3: 再生后硅胶柱的层析效果(经过 20个 "再生-使 用" 过程)  Example 1 After eluting the column after coenzyme Q10, 1500 L of acetone 30 was pumped from the bottom of the column at a flow rate of 500 L/h to wash the column in the opposite direction until the top of the column was colorless, and then 500 L/ from the top of the column. The flow rate of h is pumped into a petroleum ether equilibrium column at a temperature of 1500 L. The chromatographic yield was 94.8%, chromatographic. The chromatographic yield of the recombination was 94.8%, and the chromatographic yield of the recombination was 94.8%. 10%。 The liquid primary peak HPLC area normalized content of 98. 10%. Example 3: Chromatographic effect of a silica gel column after regeneration (after 20 "regeneration-use" processes)

按实施例 2的洗柱方法和层析方法对该硅胶层析柱连续重复 使用, 按同实施例 1 的上样量、 洗脱方式及收集方法, 至第 20 次层析收率为 93. 8%,层析液主峰 HPLC面积归一法含量为 98. 07%。 实施例 4: 再生后硅胶柱的层析效果(经过 21个 "再生-使 用" 过程)  The silica gel chromatography column was repeatedly used according to the column washing method and the chromatographic method of Example 2. According to the sample loading, elution method and collection method of the same example, the 20th chromatographic yield was 93. 8%。 The HPLC content of the main peak of the chromatographic solution was 98.7%. Example 4: Chromatographic effect of a silica gel column after regeneration (after 21 "regeneration-use" processes)

取实施例 3使用过 20次的硅胶层析柱,从柱底泵入预先用氢 氧化钠调节至 PH=11、 浓度为 5%、 温度 80。 ( 、 用量为 1000L的双 氧水, 再泵入 1000L温度 80eC热水洗涤, 洗完后用 N2将水压干, 拆下硅胶, 置于 150Ό干燥器内抽真空烘干至硅胶水分小于 5%。 烘干后的硅胶呈灰白色, 重新装入层析柱, 按同实施例 1的上样 量、洗脱方式及收集方法,进行第 21次层析,层析收率为 94. 5%, 层析液主峰 HPLC面积归一法含量为 98. 08%0 实施例 5: 再生后硅胶柱的层析效果(经过 100个 "再生-使 用" 过程) The silica gel column used in Example 3 was used 20 times, and was pumped from the bottom of the column to a pH of 1:1, a concentration of 5%, and a temperature of 80. (, the amount of 1000L of hydrogen peroxide, and then pumped into 1000L temperature 80 e C hot water wash, after washing, use N 2 to dry the water, remove the silica gel, placed in a 150 Ό drier vacuum drying to silica gel moisture less than 5 %. The crystallization, the chromatographic yield was 94.5%, the layer was subjected to the 21st chromatography. The chromatography yield was 94.5%. The HPLC main area of the main peak of the liquid separation is 98. 08% 0 Example 5: The chromatographic effect of the silica gel column after regeneration (after 100 "regeneration-use" processes)

取实施例 4的硅胶层析柱, 按照实施例 2和实施例 4结合的 再生方法(即每按实施例 2再生方法进行 20个 "再生-使用" 过 程, 按实施例 4再生方法再生 1次) 重复使用, 使用至 100次, 按实施例 1的上样量、 洗脱方式及收集方法, 层析收率为 92. 1%, 层析液主峰 HPLC面积归一法含量为 98. 05%。 对照例 1: 采用正方向洗柱再生处理的硅胶柱的层析效果 按实施例 1方法层析一次后的硅胶, 从柱顶泵入 3倍柱体积 的丙酮进行正向洗柱至柱底流出液无色, 再从柱顶泵入 3倍柱体 积的石油醚平衡。 平衡后的层析柱重新用来进行辅酶 Q10浸膏的 层析, 按同实施例 1的上样量、 洗脱方式及收集方法, 层析收率 为 93. 8%,层析液主峰 HPLC面积归一法含量为 98. 10%。按此洗柱 方法和层析方法用该硅胶层析柱连续重复使用, 第 5次使用层析 收率为 83. 2%,层析液主峰 HPLC面积归一法含量为 98. 02%,重复 使用效果变差。 尽管本发明的具体实施方式已经得到详细的描述, 本领域技 术人员将会理解。 根据已经公开的所有教导, 可以对那些细节进 行各种修改和替换, 这些改变均在本发明的保护范围之内。 本发 明的全部范围由所附权利要求及其任何等同物给出。  The silica gel column of Example 4 was used, and the regeneration method combined with Example 2 and Example 4 (i.e., 20 "regeneration-use" processes per the regeneration method of Example 2 was carried out, and the regeneration method of Example 4 was repeated once. 05%。 The chromatographic solution of the main peak HPLC area normalized content of 98. 05%, the chromatographic yield of the main peak of the chromatographic solution is 98.05%. . Comparative Example 1: Chromatographic effect of silica gel column using positive direction column regeneration treatment. Silica gel was chromatographed once in the same manner as in Example 1. Pumping 3 times column volume of acetone from the top of the column for forward washing to the bottom of the column The solution was colorless and was pumped from the top of the column to a column of 3 volumes of petroleum ether. The lysate of the chromatographic peak was HPLC. The chromatographic yield was 93.8%, and the chromatographic peak was analyzed by HPLC. The chromatographic yield was 93.8%. 10%。 The area normalized content of 98. 10%. The singularity of the HPLC method is 98.2%, repeating. The effect of use is worse. Although specific embodiments of the invention have been described in detail, those skilled in the art will understand. Various modifications and substitutions may be made to those details in light of the teachings of the invention, which are within the scope of the invention. The full scope of the invention is indicated by the appended claims and any equivalents thereof.

Claims

权利要求 Rights request 1. 一种辅酶 Q10层析硅胶的再生方法, 其特征在于, 从柱底 进高极性溶剂进行反方向洗柱。 A method for regenerating a coenzyme Q10 chromatography silica gel, which comprises washing a column in the opposite direction from a highly polar solvent at the bottom of the column. 2. 根据权利要求 1 所述的方法, 其特征在于如下的 (1) - (4) 项中的任一项或多项:  2. The method according to claim 1, characterized by any one or more of the following items (1) - (4): (1)所述高极性溶剂为选自乙酸乙酯、 丙酮、 丁酮、 乙醇中 的一种或者多种、 或者高极性溶剂和低极性溶剂的混合液, 其中 高极性溶剂占混合液的体积大于 50%;  (1) The highly polar solvent is one or more selected from the group consisting of ethyl acetate, acetone, methyl ethyl ketone, and ethanol, or a mixture of a highly polar solvent and a low polar solvent, wherein the high polar solvent accounts for The volume of the mixed solution is greater than 50%; ( 2 ) 所述高极性溶剂的用量为 1 - 5倍柱体积;  (2) the high polar solvent is used in an amount of from 1 to 5 column volumes; ( 3 ) 所述洗柱的流速为 0.5 - 2倍柱体积 /小时;  (3) the flow rate of the washing column is 0.5 - 2 column volumes / hour; (4) 所用高极性溶剂的温度为 20*€ - 50*€。  (4) The temperature of the highly polar solvent used is 20*€ - 50*€. 3. 根据权利要求 1或 2中任一项所述的方法, 其特征在于, 在洗柱之后, 从柱顶进低极性溶剂进行正向平衡。  The method according to any one of claims 1 or 2, characterized in that after the column is washed, a low polarity solvent is introduced from the column for positive equilibrium. 4. 根据权利要求 3 所述的方法, 其特征在于如下的 (1) - (4) 项中的任一项或多项:  4. The method according to claim 3, characterized by any one or more of the following items (1) - (4): (1) 所述低极性溶剂选自石油醚、 戊烷、 正己烷、 庚烷中 的一种或者多种, 或者高极性溶剂和低极性溶剂的混合液, 其中 低极性溶剂占混合液的体积大于 50%;  (1) The low-polar solvent is selected from one or more of petroleum ether, pentane, n-hexane, and heptane, or a mixture of a highly polar solvent and a low-polar solvent, wherein the low-polar solvent accounts for The volume of the mixed solution is greater than 50%; ( 2 ) 所述低极性溶剂的用量为 1 - 5倍柱体积;  (2) the low polar solvent is used in an amount of from 1 to 5 column volumes; ( 3 ) 所述平衡的流速为 0.5 - 2倍柱体积 /小时;  (3) the equilibrium flow rate is 0.5 - 2 column volumes / hour; (4) 所用低级性溶剂的温度为 50 。  (4) The temperature of the lower-grade solvent used is 50. 5. 根据权利要求 1至 4中任一项所述的方法, 其中, 将按照 权利要求 1至 4中任一项所述的方法进行再生处理后的辅酶 Q10 层析硅胶用于分离提纯辅酶 Q10, 并且将这样的 "再生-使用" 过程进行一次或多次; 优选进行 15-25次, 更优选进行 20-25 次, 进一步优选进行 20次。 The method according to any one of claims 1 to 4, wherein the coenzyme Q10 chromatography silica gel subjected to regeneration treatment according to the method of any one of claims 1 to 4 is used for separation and purification of coenzyme Q10 And performing such a "regeneration-use" process one or more times; preferably 15-25 times, more preferably 20-25 More preferably, it is 20 times. 6. 根据权利要求 5所述的方法, 其还包括下述步骤:  6. The method of claim 5 further comprising the steps of: 1)用双氧水反方向洗柱一次或多次;  1) Wash the column one or more times with hydrogen peroxide in the opposite direction; 2)用水反方向洗柱一次或多次;  2) Washing the column one or more times with the opposite direction of water; 3)拆下硅胶于 1001C - 150X烘干至水分小于 5% (w/w) ; 4 )重新装柱。  3) Remove the silica gel and dry it at 1001C - 150X until the moisture is less than 5% (w/w); 4) Repack the column. 7. 根据权利要求 6所述的方法, 其中, 步骤 1) 中双氧水的 pH为 9-11。  7. The method according to claim 6, wherein the pH of the hydrogen peroxide in step 1) is 9-11. 8. 根据权利要求 6所述的方法, 其中, 步骤 1) 中双氧水的 浓度为 3% -20% (w/w) 。  8. The method according to claim 6, wherein the concentration of hydrogen peroxide in step 1) is from 3% to 20% (w/w). 9. 根据权利要求 6所述的方法, 其中, 步骤 1)和 2) 中, 双氧水和水的用量独立地为 1 - 5倍柱体积。  9. The method according to claim 6, wherein, in steps 1) and 2), the amount of hydrogen peroxide and water is independently from 1 to 5 column volumes. 10. 根据权利要求 6所述的方法, 其中, 步骤 1)和 2) 中, 双氧水和水的温度独立地为 50*€ - 100X。  10. The method according to claim 6, wherein in steps 1) and 2), the temperature of the hydrogen peroxide and the water are independently 50*€ - 100X.
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