CN114836485B - Method for extracting and isolating ajoene from garlic - Google Patents
Method for extracting and isolating ajoene from garlic Download PDFInfo
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- IXELFRRANAOWSF-FNORWQNLSA-N (E)-Ajoene Chemical compound C=CCSS\C=C\CS(=O)CC=C IXELFRRANAOWSF-FNORWQNLSA-N 0.000 title claims abstract description 92
- IXELFRRANAOWSF-CYBMUJFWSA-N ajoene Natural products C=CCSSC=CC[S@](=O)CC=C IXELFRRANAOWSF-CYBMUJFWSA-N 0.000 title claims abstract description 92
- IXELFRRANAOWSF-UHFFFAOYSA-N cis-ajoene Natural products C=CCSSC=CCS(=O)CC=C IXELFRRANAOWSF-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 235000004611 garlic Nutrition 0.000 title claims abstract description 85
- 238000000034 method Methods 0.000 title claims abstract description 29
- 244000245420 ail Species 0.000 title 1
- 240000002234 Allium sativum Species 0.000 claims abstract description 84
- 238000000605 extraction Methods 0.000 claims abstract description 81
- 239000010647 garlic oil Substances 0.000 claims abstract description 64
- 244000223014 Syzygium aromaticum Species 0.000 claims abstract description 37
- 235000016639 Syzygium aromaticum Nutrition 0.000 claims abstract description 37
- 238000000199 molecular distillation Methods 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 239000012530 fluid Substances 0.000 claims abstract description 18
- 238000000746 purification Methods 0.000 claims abstract description 18
- 239000007791 liquid phase Substances 0.000 claims abstract description 17
- 238000006911 enzymatic reaction Methods 0.000 claims abstract description 9
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 27
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 25
- 239000001273 butane Substances 0.000 claims description 22
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 22
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 22
- 238000004237 preparative chromatography Methods 0.000 claims description 12
- 239000003480 eluent Substances 0.000 claims description 11
- 239000000945 filler Substances 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 2
- 238000004587 chromatography analysis Methods 0.000 claims 1
- 108010092760 Alliin lyase Proteins 0.000 abstract description 35
- XUHLIQGRKRUKPH-GCXOYZPQSA-N Alliin Natural products N[C@H](C[S@@](=O)CC=C)C(O)=O XUHLIQGRKRUKPH-GCXOYZPQSA-N 0.000 abstract description 14
- XUHLIQGRKRUKPH-UHFFFAOYSA-N S-allyl-L-cysteine sulfoxide Natural products OC(=O)C(N)CS(=O)CC=C XUHLIQGRKRUKPH-UHFFFAOYSA-N 0.000 abstract description 14
- XUHLIQGRKRUKPH-DYEAUMGKSA-N alliin Chemical compound OC(=O)[C@@H](N)C[S@@](=O)CC=C XUHLIQGRKRUKPH-DYEAUMGKSA-N 0.000 abstract description 14
- 235000015295 alliin Nutrition 0.000 abstract description 14
- JDLKFOPOAOFWQN-VIFPVBQESA-N Allicin Natural products C=CCS[S@](=O)CC=C JDLKFOPOAOFWQN-VIFPVBQESA-N 0.000 abstract description 4
- JDLKFOPOAOFWQN-UHFFFAOYSA-N allicin Chemical compound C=CCSS(=O)CC=C JDLKFOPOAOFWQN-UHFFFAOYSA-N 0.000 abstract description 4
- 235000010081 allicin Nutrition 0.000 abstract description 4
- 230000033228 biological regulation Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 description 19
- 230000000694 effects Effects 0.000 description 12
- 239000000126 substance Substances 0.000 description 11
- 239000012141 concentrate Substances 0.000 description 10
- 238000002161 passivation Methods 0.000 description 10
- 238000006555 catalytic reaction Methods 0.000 description 9
- 238000004821 distillation Methods 0.000 description 9
- 229940029982 garlic powder Drugs 0.000 description 9
- 239000003921 oil Substances 0.000 description 9
- 235000019198 oils Nutrition 0.000 description 9
- 239000000047 product Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 230000002779 inactivation Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000010828 elution Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- WLHNIAVMSNXYHO-UHFFFAOYSA-N S-allylsulfenic acid Chemical compound OSCC=C WLHNIAVMSNXYHO-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- KZJWDPNRJALLNS-VPUBHVLGSA-N (-)-beta-Sitosterol Natural products O[C@@H]1CC=2[C@@](C)([C@@H]3[C@H]([C@H]4[C@@](C)([C@H]([C@H](CC[C@@H](C(C)C)CC)C)CC4)CC3)CC=2)CC1 KZJWDPNRJALLNS-VPUBHVLGSA-N 0.000 description 1
- CSVWWLUMXNHWSU-UHFFFAOYSA-N (22E)-(24xi)-24-ethyl-5alpha-cholest-22-en-3beta-ol Natural products C1CC2CC(O)CCC2(C)C2C1C1CCC(C(C)C=CC(CC)C(C)C)C1(C)CC2 CSVWWLUMXNHWSU-UHFFFAOYSA-N 0.000 description 1
- KLEXDBGYSOIREE-UHFFFAOYSA-N 24xi-n-propylcholesterol Natural products C1C=C2CC(O)CCC2(C)C2C1C1CCC(C(C)CCC(CCC)C(C)C)C1(C)CC2 KLEXDBGYSOIREE-UHFFFAOYSA-N 0.000 description 1
- 241000383638 Allium nigrum Species 0.000 description 1
- LPZCCMIISIBREI-MTFRKTCUSA-N Citrostadienol Natural products CC=C(CC[C@@H](C)[C@H]1CC[C@H]2C3=CC[C@H]4[C@H](C)[C@@H](O)CC[C@]4(C)[C@H]3CC[C@]12C)C(C)C LPZCCMIISIBREI-MTFRKTCUSA-N 0.000 description 1
- ARVGMISWLZPBCH-UHFFFAOYSA-N Dehydro-beta-sitosterol Natural products C1C(O)CCC2(C)C(CCC3(C(C(C)CCC(CC)C(C)C)CCC33)C)C3=CC=C21 ARVGMISWLZPBCH-UHFFFAOYSA-N 0.000 description 1
- UQBOJOOOTLPNST-UHFFFAOYSA-N Dehydroalanine Chemical compound NC(=C)C(O)=O UQBOJOOOTLPNST-UHFFFAOYSA-N 0.000 description 1
- UBJVUCKUDDKUJF-UHFFFAOYSA-N Diallyl sulfide Natural products C=CCSCC=C UBJVUCKUDDKUJF-UHFFFAOYSA-N 0.000 description 1
- 239000006000 Garlic extract Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- MJVXAPPOFPTTCA-UHFFFAOYSA-N beta-Sistosterol Natural products CCC(CCC(C)C1CCC2C3CC=C4C(C)C(O)CCC4(C)C3CCC12C)C(C)C MJVXAPPOFPTTCA-UHFFFAOYSA-N 0.000 description 1
- LGJMUZUPVCAVPU-UHFFFAOYSA-N beta-Sitostanol Natural products C1CC2CC(O)CCC2(C)C2C1C1CCC(C(C)CCC(CC)C(C)C)C1(C)CC2 LGJMUZUPVCAVPU-UHFFFAOYSA-N 0.000 description 1
- NJKOMDUNNDKEAI-UHFFFAOYSA-N beta-sitosterol Natural products CCC(CCC(C)C1CCC2(C)C3CC=C4CC(O)CCC4C3CCC12C)C(C)C NJKOMDUNNDKEAI-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 210000000805 cytoplasm Anatomy 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- -1 diallyl sulfide compound Chemical class 0.000 description 1
- 238000007323 disproportionation reaction Methods 0.000 description 1
- 235000020706 garlic extract Nutrition 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- KZJWDPNRJALLNS-VJSFXXLFSA-N sitosterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CC[C@@H](CC)C(C)C)[C@@]1(C)CC2 KZJWDPNRJALLNS-VJSFXXLFSA-N 0.000 description 1
- 229950005143 sitosterol Drugs 0.000 description 1
- NLQLSVXGSXCXFE-UHFFFAOYSA-N sitosterol Natural products CC=C(/CCC(C)C1CC2C3=CCC4C(C)C(O)CCC4(C)C3CCC2(C)C1)C(C)C NLQLSVXGSXCXFE-UHFFFAOYSA-N 0.000 description 1
- 235000015500 sitosterol Nutrition 0.000 description 1
- 210000003934 vacuole Anatomy 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P11/00—Preparation of sulfur-containing organic compounds
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
- C07C319/26—Separation; Purification; Stabilisation; Use of additives
- C07C319/28—Separation; Purification
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
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Abstract
本发明公开了一种从蒜中提取分离阿霍烯的方法,属于农产品精深加工技术领域。本发明的方法包括以下步骤:对蒜瓣进行预处理,预处理条件:真空、压力为400MPa以上、时间为10min以上;预处理后的蒜瓣先在‑4℃以下进行粉碎,然后使其在100‑200MPa、25‑35℃的条件下进行酶促反应,获得蒜末;蒜末采用亚临界流体进行萃取获得蒜油;对蒜油依次进行分子蒸馏和液相纯化,获得阿霍烯。本发明首先利用超高压将蒜氨酸酶钝化将蒜氨酸提取出来,再制得蒜氨酸酶液,然后利用超高压对大蒜中蒜氨酸酶进行激活,能加快酶促反应的速度,生成更多的大蒜素进而生成更高含量的阿霍烯,最后通过超高压调控、亚临界流体萃取、分子蒸馏、制备液相纯化得到高收率、高纯度阿霍烯产品。
The invention discloses a method for extracting and separating ajoene from garlic, and belongs to the technical field of intensive processing of agricultural products. The method of the present invention includes the following steps: pretreatment of garlic cloves, pretreatment conditions: vacuum, pressure of more than 400MPa, time of more than 10 minutes; the pretreated garlic cloves are first crushed below -4°C, and then allowed to cool at 100- Enzymatic reaction is carried out under the conditions of 200MPa and 25-35℃ to obtain minced garlic; the minced garlic is extracted with subcritical fluid to obtain garlic oil; the garlic oil is sequentially subjected to molecular distillation and liquid phase purification to obtain ajoene. The present invention first uses ultra-high pressure to passivate alliinase to extract alliin, and then prepares alliinase liquid, and then uses ultra-high pressure to activate alliinase in garlic, which can speed up the enzymatic reaction. , generate more allicin and then generate a higher content of ajoene, and finally obtain a high-yield and high-purity ajoene product through ultra-high pressure regulation, subcritical fluid extraction, molecular distillation, and preparative liquid phase purification.
Description
技术领域Technical field
本发明涉及一种从蒜中提取分离阿霍烯的方法,属于农产品精深加工技术领域。The invention relates to a method for extracting and separating ajoene from garlic, and belongs to the technical field of intensive processing of agricultural products.
背景技术Background technique
大蒜含有蒜氨酸和蒜氨酸酶,但蒜氨酸和蒜氨酸酶分别存在于细胞质和液泡中,蒜氨酸酶不能对蒜氨酸作用。大蒜破碎时,蒜氨酸在蒜氨酸酶的作用下转化为烯丙次磺酸和脱氢丙氨酸,烯丙次磺酸通过歧化反应生成大蒜辣素,大蒜辣素极不稳定,会进一步分解为二烯丙基硫醚化合物、二噻烯及阿霍烯,因此,可以说阿霍烯是蒜氨酸的第二降解产物。自然条件下,大蒜中阿霍烯的生成量极少,且阿霍烯的稳定性差,因此阿霍烯的提取是人们研究的重点。Garlic contains alliin and alliinase, but alliin and alliinase exist in the cytoplasm and vacuole respectively, and alliinase cannot act on alliin. When garlic is crushed, alliin is converted into allylsulfenic acid and dehydroalanine under the action of alliinase. Allylsulfenic acid generates allicin through a disproportionation reaction. Allicin is extremely unstable and will It is further decomposed into diallyl sulfide compound, dithiene and ajoene. Therefore, it can be said that ajoene is the second degradation product of alliin. Under natural conditions, the amount of ajoene produced in garlic is very small, and the stability of ajoene is poor. Therefore, the extraction of ajoene is the focus of research.
中国专利CN1324142C公开了一种脱除了谷甾醇等其它脂溶性物质含有阿霍烯的脱脂大蒜提取物及其制备方法和应用。中国专利CN104974068公开了一种阿霍烯的制备方法,将大蒜破碎,加入提取液混合,得到产物后进行处理,再进行过滤和/或离心处理,得到的产物去掉溶剂再加入植物油混合,得到的产物加入吸附剂再进行洗脱从而得到高浓度的阿霍烯产品。但上述两种方法存在阿霍烯制备率低、纯度不高的问题。Chinese patent CN1324142C discloses a defatted garlic extract containing ajoene in which sitosterol and other fat-soluble substances have been removed, as well as its preparation method and application. Chinese patent CN104974068 discloses a method for preparing ajoene. Garlic is crushed, and the extract is added and mixed. After obtaining the product, it is processed, and then filtered and/or centrifuged. The solvent is removed from the obtained product and then vegetable oil is added and mixed. The obtained product The product is added to the adsorbent and then eluted to obtain a high concentration of ajoene product. However, the above two methods have the problems of low preparation rate and low purity of ajoene.
发明内容Contents of the invention
本发明的目的是为了克服现有技术的上述不足,提供一种从蒜中提取分离阿霍烯的方法。The object of the present invention is to overcome the above-mentioned shortcomings of the prior art and provide a method for extracting and separating ajoene from garlic.
为实现上述目的,本发明采用下述技术方案:In order to achieve the above objects, the present invention adopts the following technical solutions:
从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and isolating ajoene from garlic includes the following steps:
对蒜瓣进行预处理,预处理条件:真空、压力为400MPa以上、时间为10min以上;Pretreatment of garlic cloves, pretreatment conditions: vacuum, pressure of more than 400MPa, time of more than 10 minutes;
预处理后的蒜瓣先在-4℃以下进行粉碎,然后使其在100-200MPa、25-35℃的条件下进行酶促反应,获得蒜末;The pretreated garlic cloves are first crushed below -4°C, and then subjected to an enzymatic reaction at 100-200MPa and 25-35°C to obtain minced garlic;
蒜末采用亚临界流体进行萃取获得蒜油;Minced garlic is extracted with subcritical fluid to obtain garlic oil;
对蒜油依次进行分子蒸馏和液相纯化,获得阿霍烯。Garlic oil is subjected to molecular distillation and liquid phase purification in sequence to obtain ajoene.
本发明通过实验研究发现:从大蒜中提取分离阿霍烯时,阿霍烯不稳定从而导致阿霍烯收率低。本发明的方法通过对蒜瓣进行预处理,能将蒜中的蒜氨酸酶钝化;从而使得在粉碎蒜瓣、释放蒜氨酸的过程中,蒜氨酸酶不会与蒜氨酸反应、不会造成阿霍烯的流失,从而使得阿霍烯的产率明显提高。The present invention finds through experimental research that when ajoene is extracted and separated from garlic, ajoene is unstable, resulting in a low yield of ajoene. The method of the present invention can inactivate alliinase in garlic by pretreating garlic cloves; thus, during the process of crushing garlic cloves and releasing alliin, alliinase will not react with alliin and will not react with alliin. It will cause the loss of ajoene, thereby significantly increasing the yield of ajoene.
本发明首先利用超高压将蒜氨酸酶钝化将蒜氨酸提取出来,再制得蒜氨酸酶液,然后利用超高压对大蒜中蒜氨酸酶进行激活,能加快酶促反应的速度,生成更多的大蒜素进而生成更高含量的阿霍烯,最后通过超高压调控、亚临界流体萃取、分子蒸馏、制备液相纯化得到高纯度阿霍烯产品。The invention first uses ultra-high pressure to passivate alliinase to extract alliin, and then prepares alliinase liquid, and then uses ultra-high pressure to activate alliinase in garlic, which can speed up the enzymatic reaction. , generate more allicin and then generate a higher content of ajoene, and finally obtain a high-purity ajoene product through ultra-high pressure regulation, subcritical fluid extraction, molecular distillation, and preparative liquid phase purification.
本发明的方法,既可以用于从大蒜中提取分离阿霍烯,也可以用于从黑蒜中提取阿霍烯。The method of the present invention can be used to extract and separate ajoene from garlic, and can also be used to extract ajoene from black garlic.
对蒜瓣进行预处理时,压力达到400MPa即可起到使蒜中的蒜氨酸酶钝化作用。随着压力的进一步增大蒜氨酸酶钝化效果变好;但是,并不是压力越大,蒜氨酸酶钝化效果越好。实验研究证明,当压力超过650MPa时,蒜氨酸酶钝化效果明显下降。所以,本发明将压力条件限定为400-600MPa;而在此压力条件范围内,当压力为500-600时,蒜氨酸酶钝化效果更好。具体的,压力条件可以为520-550MPa或者550-580MPa。When pretreating garlic cloves, the pressure reaching 400MPa can inactivate the alliinase in garlic. As the pressure further increases, the alliinase inactivation effect becomes better; however, it does not mean that the greater the pressure, the better the alliinase inactivation effect. Experimental studies have shown that when the pressure exceeds 650MPa, the alliinase passivation effect decreases significantly. Therefore, the present invention limits the pressure condition to 400-600MPa; within this pressure condition range, when the pressure is 500-600, the alliinase passivation effect is better. Specifically, the pressure condition can be 520-550MPa or 550-580MPa.
对蒜瓣进行预处理时,时间达到10min即可起到使蒜中的蒜氨酸酶钝化作用。随着时间的进一步延长,蒜氨酸酶钝化效果变好;但是,并不是时间越大,蒜氨酸酶钝化效果越好。实验研究证明,当时间超过35min时,蒜氨酸酶钝化效果明显下降。所以,本发明将时间限定为10-30min,而在此时间范围内,当时间为15-20min时,蒜氨酸酶钝化效果更好。When pretreating garlic cloves, the alliinase in garlic can be inactivated if the time reaches 10 minutes. As time is further extended, the alliinase inactivation effect becomes better; however, it does not mean that the longer the time, the better the alliinase inactivation effect. Experimental studies have shown that when the time exceeds 35 minutes, the alliinase passivation effect decreases significantly. Therefore, the present invention limits the time to 10-30 minutes, and within this time range, when the time is 15-20 minutes, the alliinase passivation effect is better.
其中,蒜氨酸酶钝化效果以大蒜油的收率进行衡量;大蒜油的收率越高表明蒜氨酸酶钝化效果越好。Among them, the alliinase passivation effect is measured by the yield of garlic oil; the higher the yield of garlic oil, the better the alliinase passivation effect.
对预处理后的蒜瓣进行粉碎时,当温度达到-4℃时,大蒜油的收率开始明显提高;随着温度的降低,大蒜油的收率随之升高;但是当温度低于-20℃时,大蒜油的收率反而明显下降。可能的原因是,在-4℃至-20℃温度范围内,能使蒜氨酸酶维持良好的钝化状态,蒜氨酸酶在粉碎过程中不会被激活,不会与蒜氨酸反应,不会导致阿霍烯流失。而当温度高于-4℃时,不能使蒜氨酸酶维持良好的钝化状态,蒜氨酸酶在粉碎过程中会被激活,从而与与蒜氨酸反应,导致阿霍烯流失。而当温度低于-20℃时,虽然能使蒜氨酸酶维持良好的钝化状态,但是效果不理想,且成本较高。所以,可以将对预处理后的蒜瓣进行粉碎时的温度限定为-4℃至-20℃。When the pretreated garlic cloves are crushed, the yield of garlic oil begins to increase significantly when the temperature reaches -4°C; as the temperature decreases, the yield of garlic oil increases; but when the temperature is lower than -20 At ℃, the yield of garlic oil decreased significantly. The possible reason is that in the temperature range of -4°C to -20°C, alliinase can maintain a good passivation state. Alliinase will not be activated during the crushing process and will not react with alliin. , will not cause ajoene loss. When the temperature is higher than -4°C, alliinase cannot maintain a good passivation state. Alliinase will be activated during the crushing process, thereby reacting with alliin, resulting in the loss of ajoene. When the temperature is lower than -20°C, although alliinase can be maintained in a good passivation state, the effect is not ideal and the cost is high. Therefore, the temperature when crushing the pretreated garlic cloves can be limited to -4°C to -20°C.
粉碎后的蒜瓣,将其温度升高为25-35℃、并将压力升至100-200MPa,此时,处于钝化状态的蒜氨酸酶被激活,与在粉碎过程中释放出的蒜氨酸迅速反应,即进行酶促反应。其中,25-35℃为蒜氨酸酶的活性温度;而将压力升至100-200MPa的目的是将钝化的蒜氨酸酶激活,且能提高大蒜油的收率。可能的原因是,该压力条件能提高蒜氨酸酶与蒜氨酸的反应速率,从而能显著减少阿霍烯分解流失。压力条件为150-180MPa时高大蒜油的收率更高。The temperature of the crushed garlic cloves is raised to 25-35°C and the pressure is raised to 100-200MPa. At this time, the inactive alliinase is activated and combines with the alliin released during the crushing process. The acid reacts rapidly, i.e., it undergoes an enzymatic reaction. Among them, 25-35°C is the activity temperature of alliinase; and the purpose of raising the pressure to 100-200MPa is to activate the passivated alliinase and increase the yield of garlic oil. The possible reason is that this pressure condition can increase the reaction rate of alliinase and alliin, thereby significantly reducing the decomposition loss of ajoene. When the pressure condition is 150-180MPa, the yield of high garlic oil is higher.
酶促反应的反应时间以完全反应为宜,即蒜氨酸酶的酶活反应完全。The reaction time of the enzymatic reaction is appropriate for complete reaction, that is, the enzymatic reaction of alliinase is complete.
预处理后的蒜瓣,如果不能及时进行下一步的处理,可以于-4℃冷冻储存以下备用。为了保证预处理后的蒜瓣中蒜氨酸酶的钝化状态,冷冻储存温度可以为-4至-20℃。If the pretreated garlic cloves cannot be processed in time, they can be frozen and stored at -4°C for later use. In order to ensure the passivation state of alliinase in the pretreated garlic cloves, the frozen storage temperature can be -4 to -20°C.
所述蒜末采用亚临界流体进行萃取获得蒜油是指:以丁烷作为萃取剂,于-0.1Mpa、20-50℃条件下进行萃取,然后将萃取液的压力减压至-0.1Mpa,将丁烷与蒜油分离,获取蒜油;The extraction of minced garlic using subcritical fluid to obtain garlic oil means: using butane as the extraction agent, extracting under the conditions of -0.1Mpa and 20-50°C, and then reducing the pressure of the extraction liquid to -0.1Mpa. Separate butane from garlic oil to obtain garlic oil;
所述分子蒸馏的条件为:50-100℃,真空度30-35Pa,蒜油的滴加速度为1-3滴/3秒,The conditions for molecular distillation are: 50-100°C, vacuum degree 30-35Pa, garlic oil dripping speed 1-3 drops/3 seconds,
所述液相纯化是指:将分子蒸馏收集的阿霍烯馏分用5-8倍体积的50-80%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,90-95%乙醇为洗脱剂,以10-30mL/min的流速进行洗脱,收集阿霍烯分离液,50-70℃减压浓缩至油状物,即得阿霍烯。The liquid phase purification means: dissolving the ajoene fraction collected by molecular distillation with 5-8 times the volume of 50-80% ethanol, filtering and then applying to preparative chromatography, using Innoval ODS-2 as filler, 90-95% ethanol As the eluent, elute at a flow rate of 10-30 mL/min, collect the ajoene separated liquid, and concentrate under reduced pressure at 50-70°C to an oily substance to obtain ajoene.
所述亚临界流体萃取、分子蒸馏及液相纯化中的其他操作步骤、条件及参数均为现有技术;本发明不再赘述。Other operating steps, conditions and parameters in the subcritical fluid extraction, molecular distillation and liquid phase purification are all existing technologies; they will not be described in detail in the present invention.
本发明的有益效果是:The beneficial effects of the present invention are:
本发明首次采用超高压——亚临界流体萃取——分子蒸馏分离——制备色谱纯化为核心成套技术从从蒜中提取分离阿霍烯的方法,提高了阿霍烯的得率和纯度,该工艺合理、可行,过程简单,溶剂毒性小,溶剂方便回收,并且可以大批量工业化生产,具有很强的实用价值。For the first time, the present invention adopts ultra-high pressure - subcritical fluid extraction - molecular distillation separation - preparative chromatography purification as the core set of technologies to extract and separate ajoene from garlic, which improves the yield and purity of ajoene. The technology is reasonable and feasible, the process is simple, the solvent has low toxicity, the solvent is easy to recycle, and it can be industrially produced in large quantities, so it has strong practical value.
本发明中,若无特别说明,所述%均为质量百分数。In the present invention, unless otherwise specified, the % mentioned are all mass percentages.
附图说明Description of drawings
图1是本发明具体实施方式中,对步骤(4)产物阿霍烯含量测定的液相色谱图谱;Figure 1 is a liquid chromatography chart for measuring the ajoene content of the product of step (4) in the specific embodiment of the present invention;
图2是本发明具体实施方式中,对步骤(5)产物使用液相色谱法测定阿霍烯含量的图谱。Figure 2 is a chromatogram for determining the ajoene content of the product of step (5) using liquid chromatography in a specific embodiment of the present invention.
具体实施方式Detailed ways
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and examples.
本说明书附图所绘示的结构、比例、大小等,均仅用以配合说明书所揭示的内容,以供熟悉此技术的人士了解与阅读,并非用以限定本发明可实施的限定条件,故不具技术上的实质意义,任何结构的修饰、比例关系的改变或大小的调整,在不影响本发明所能产生的功效及所能达成的目的下,均应仍落在本发明所揭示的技术内容涵盖的范围内。同时,本说明书中所引用的如“上”、“下”、“左”、“右”、“中间”及“一”等的用语,亦仅为便于叙述的明了,而非用以限定本发明可实施的范围,其相对关系的改变或调整,在无实质变更技术内容下,当亦视为本发明可实施的范畴。The structures, proportions, sizes, etc. shown in the drawings of this specification are only used to coordinate with the content disclosed in the specification and are for the understanding and reading of those familiar with this technology. They are not used to limit the conditions under which the present invention can be implemented. Therefore, It has no technical substantive significance. Any structural modifications, changes in proportions or adjustments in size shall still fall within the scope of the technology disclosed in the present invention as long as it does not affect the effectiveness and purpose of the present invention. within the scope of the content covered. At the same time, terms such as "upper", "lower", "left", "right", "middle" and "one" cited in this specification are only for convenience of description and are not used to limit the scope of this specification. The scope of the invention that can be implemented, and changes or adjustments in their relative relationships, as long as there is no substantial change in the technical content, shall also be regarded as the scope of the invention that can be implemented.
实施例1Example 1
一种从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and separating ajoene from garlic includes the following steps:
(1)预处理蒜:称取100g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在500MPa压力条件下预处理10min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 100g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them for 10 minutes under a pressure of 500MPa. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件下进行粉碎,然后放入超高压腔,在压力100MPa、温度25℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 100MPa and a temperature of 25°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末150g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷600mL,萃取温度为30℃,时间为120min,萃取3次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油0.82g,大蒜油提取率为0.55%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 150g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 600mL, the extraction temperature is 30°C, the time is 120min, and the extraction time is 3 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 0.82g of garlic oil. The garlic oil extraction rate is 0.55%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至50℃,控制真空度至30Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 50°C, control the vacuum to 30Pa, and drop at a speed of 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(5)制备液相纯化:阿霍烯馏分用5倍体积的50%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为97.7%。(5) Preparative liquid phase purification: Dissolve the ajoene fraction with 5 times the volume of 50% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 20% ethyl acetate as the eluent, 15 mL/min Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 97.7%.
实施例2Example 2
一种从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and separating ajoene from garlic includes the following steps:
(1)预处理蒜:称取150g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在520MPa压力条件下预处理15min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 150g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them under 520MPa pressure conditions for 15 minutes. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣-4℃至-20℃温度条件进行粉碎,然后放入超高压腔,在压力100MPa、温度35℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 100MPa and a temperature of 35°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末200g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷900mL,萃取温度为40℃,时间为120min,萃取4次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油1.28g,大蒜油提取率为0.64%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 200g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum degree is -0.1Mpa; add butane 900mL, the extraction temperature is 40°C, the time is 120min, and the extraction is 4 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 1.28g of garlic oil. The extraction rate of garlic oil is 0.64%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至70℃,控制真空度至35Pa,滴加速度为2滴/3秒,开始蒸馏过程,收集阿霍烯馏分;(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 70°C, control the vacuum to 35Pa, and the dropping speed is 2 drops/3 seconds. Start the distillation process and collect the ajoene fraction;
(5)制备液相纯化:阿霍烯馏分用5倍体积的60%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为98.1%。(5) Preparative liquid phase purification: The ajoene fraction was dissolved in 5 times the volume of 60% ethanol, filtered and then subjected to preparative chromatography, using Innoval ODS-2 as the filler and 20% ethyl acetate as the eluent, at 15 mL/min. Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 98.1%.
实施例3Example 3
一种从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and separating ajoene from garlic includes the following steps:
(1)预处理蒜:称取150g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在550MPa压力条件下预处理20min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 150g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them under 550MPa pressure conditions for 20 minutes. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件进行粉碎,然后放入超高压腔,在压力180MPa、温度35℃的压力腔中进行酶催化反应35min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 180MPa and a temperature of 35°C for 35 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末200g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷1200mL,萃取温度为50℃,时间为120min,萃取4次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油1.20g,大蒜油提取率为0.60%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 200g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum degree is -0.1Mpa; add butane 1200mL, the extraction temperature is 50℃, the time is 120min, and the extraction is 4 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 1.20g of garlic oil. The garlic oil extraction rate is 0.60%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至80℃,控制真空度至35Pa,滴加速度为2滴/3秒,开始蒸馏过程,收集阿霍烯馏分;(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 80°C, control the vacuum to 35Pa, and the dropping speed is 2 drops/3 seconds. Start the distillation process and collect the ajoene fraction;
(5)制备液相纯化:阿霍烯馏分用6倍体积的60%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以10mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为98.4%。(5) Preparative liquid phase purification: Dissolve the ajoene fraction with 6 times the volume of 60% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 20% ethyl acetate as the eluent, 10 mL/min Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 98.4%.
实施例4Example 4
一种从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and separating ajoene from garlic includes the following steps:
(1)预处理蒜:称取200g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在580MPa压力条件下预处理20min,完成后取出置于-4℃至--20℃环境下备用。(1) Pretreatment of garlic: Weigh 200g of garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them for 20 minutes under a pressure of 580MPa. After completion, take them out and place them at -4°C to - Reserved in -20℃ environment.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件进行粉碎,然后放入超高压腔,在压力150MPa、温度40℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 150MPa and a temperature of 40°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末300g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷2000mL,萃取温度为40℃,时间为150min,萃取4次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油1.82g,大蒜油提取率为0.60%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 300g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 2000mL, the extraction temperature is 40°C, the time is 150min, and the extraction time is 4 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 1.82g of garlic oil. The garlic oil extraction rate is 0.60%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至80℃,控制真空度至35Pa,滴加速度为3滴/3秒,开始蒸馏过程,收集阿霍烯馏分;(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 80°C, control the vacuum to 35Pa, and the dropping speed is 3 drops/3 seconds. Start the distillation process and collect the ajoene fraction;
(5)制备液相纯化:阿霍烯馏分用5倍体积的80%乙醇溶解,过滤后上制备色谱,以Flash Slica为填料,20%乙酸乙酯为洗脱剂,以20mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为98.8%。(5) Preparative liquid phase purification: The ajoene fraction was dissolved in 5 times the volume of 80% ethanol, filtered and then subjected to preparative chromatography, using Flash Slica as the filler, 20% ethyl acetate as the eluent, and a flow rate of 20 mL/min. Carry out elution, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 98.8%.
实施例5Example 5
一种从蒜中提取分离阿霍烯的方法,包括以下步骤:A method for extracting and separating ajoene from garlic includes the following steps:
(1)预处理蒜:称取250g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在600MPa压力条件下预处理30min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 250g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them for 30 minutes under a pressure of 600MPa. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件进行粉碎,然后放入超高压腔,在压力200MPa、温度35℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 200MPa and a temperature of 35°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末300g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷2000mL,萃取温度为50℃,时间为120min,萃取5次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油1.74g,大蒜油提取率为0.58%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 300g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 2000mL, the extraction temperature is 50°C, the time is 120min, and the extraction is performed 5 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 1.74g of garlic oil. The extraction rate of garlic oil is 0.58%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至100℃,控制真空度至35Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 100°C, control the vacuum to 35Pa, and drop at a speed of 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(5)制备液相纯化:阿霍烯馏分用5倍体积的无水乙醇溶解,过滤后上制备色谱,以Flash Slica为填料,20%乙酸乙酯为洗脱剂,以30mL/min的流速进行洗脱,收集阿霍烯分离液,50℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为99.1%。(5) Preparative liquid phase purification: The ajoene fraction was dissolved in 5 times the volume of absolute ethanol, filtered and then subjected to preparative chromatography, using Flash Slica as the filler, 20% ethyl acetate as the eluent, and a flow rate of 30 mL/min. Carry out elution, collect the ajoene separated liquid, and concentrate under reduced pressure at 50°C to an oily substance to obtain ajoene. The purity of ajoene is 99.1%.
对比例1Comparative example 1
(1)预处理蒜:称取100g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在500MPa压力条件下预处理35min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 100g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them under 500MPa pressure conditions for 35 minutes. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件下进行粉碎,然后放入超高压腔,在压力100MPa、温度25℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 100MPa and a temperature of 25°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末150g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷600mL,萃取温度为30℃,时间为120min,萃取3次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油0.60g,大蒜油提取率为0.40%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 150g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 600mL, the extraction temperature is 30°C, the time is 120min, and the extraction is performed 3 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 0.60g of garlic oil. The garlic oil extraction rate is 0.40%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至50℃,控制真空度至30Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 50°C, control the vacuum to 30Pa, and drop at a speed of 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(5)制备液相纯化:阿霍烯馏分用5倍体积的50%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为97.1%。(5) Preparative liquid phase purification: Dissolve the ajoene fraction with 5 times the volume of 50% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 20% ethyl acetate as the eluent, 15 mL/min Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 97.1%.
对比例2Comparative example 2
(1)预处理蒜:称取100g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在650MPa压力条件下预处理10min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 100g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them for 10 minutes under a pressure of 650MPa. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件下进行粉碎,然后放入超高压腔,在压力100MPa、温度25℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber with a pressure of 100MPa and a temperature of 25°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末150g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷600mL,萃取温度为30℃,时间为120min,萃取3次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油0.54g,大蒜油提取率为0.36%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 150g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 600mL, the extraction temperature is 30°C, the time is 120min, and the extraction is performed 3 times; after the extraction is completed, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 0.54g of garlic oil. The extraction rate of garlic oil is 0.36%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至50℃,控制真空度至30Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 50°C, control the vacuum to 30Pa, and drop at a speed of 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(5)制备液相纯化:阿霍烯馏分用5倍体积的50%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为96.8%。(5) Preparative liquid phase purification: Dissolve the ajoene fraction with 5 times the volume of 50% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 20% ethyl acetate as the eluent, 15 mL/min Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 96.8%.
对比例3Comparative example 3
(1)预处理蒜:称取100g蒜瓣,将其装入超高压专用袋中,真空密封后放入压力腔中,在500MPa压力条件下预处理10min,完成后取出置于-4至-20℃环境下备用。(1) Pretreatment of garlic: Weigh 100g garlic cloves, put them into a special ultra-high pressure bag, vacuum seal them and put them into a pressure chamber. Pretreat them for 10 minutes under a pressure of 500MPa. After completion, take them out and place them at -4 to -20 ℃ environment for use.
(2)将预处理的蒜瓣在-4℃至-20℃温度条件下进行粉碎,然后放入超高压腔,在常压、温度25℃的压力腔中进行酶催化反应30min;获得蒜末。(2) Crush the pretreated garlic cloves at a temperature of -4°C to -20°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction in a pressure chamber at normal pressure and temperature of 25°C for 30 minutes; obtain minced garlic.
(3)亚临界流体萃取制备大蒜油:称取蒜粉末150g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷600mL,萃取温度为30℃,时间为120min,萃取3次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油0.53g,大蒜油提取率为0.35%。(3) Prepare garlic oil by subcritical fluid extraction: weigh 150g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 600mL, the extraction temperature is 30°C, the time is 120min, and the extraction is performed 3 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 0.53g of garlic oil. The garlic oil extraction rate is 0.35%.
(4)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至50℃,控制真空度至30Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(4) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 50°C, control the vacuum to 30Pa, and drop at a speed of 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(5)制备液相纯化:阿霍烯馏分用5倍体积的50%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,20%乙酸乙酯为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为97.4%。(5) Preparative liquid phase purification: Dissolve the ajoene fraction with 5 times the volume of 50% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 20% ethyl acetate as the eluent, 15 mL/min Elute at a flow rate, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 97.4%.
对比例4Comparative example 4
(1)将蒜瓣在0℃温度条件下进行粉碎,然后放入超高压腔,在压力100MPa、温度25℃的压力腔中进行酶催化反应30min;获得蒜末。(1) Crush the garlic cloves at a temperature of 0°C, then place them into an ultra-high pressure chamber, and perform an enzyme-catalyzed reaction for 30 minutes in a pressure chamber with a pressure of 100MPa and a temperature of 25°C; obtain minced garlic.
(2)亚临界流体萃取制备大蒜油:称取蒜粉末150g装入一个料袋,置于亚临界萃取罐中,然后对萃取罐进行抽真空,抽至真空度为-0.1Mpa;加入丁烷600mL,萃取温度为30℃,时间为150min,萃取3次;萃取结束后,将萃取液引入分离罐,将压力减压至-0.1Mpa,将丁烷与大蒜油分离,获取大蒜油0.36g,大蒜油提取率为0.24%。(2) Prepare garlic oil by subcritical fluid extraction: weigh 150g of garlic powder and put it into a bag, place it in a subcritical extraction tank, and then vacuum the extraction tank until the vacuum is -0.1Mpa; add butane 600mL, the extraction temperature is 30°C, the time is 150min, and the extraction is performed 3 times; after the extraction, introduce the extraction liquid into the separation tank, reduce the pressure to -0.1Mpa, separate the butane from the garlic oil, and obtain 0.36g of garlic oil. The extraction rate of garlic oil is 0.24%.
(3)分子蒸馏分离:大蒜油装至分子蒸馏装置恒温槽,热油机升温至50℃,控制真空度至30Pa,滴加速度为1滴/3秒,开始蒸馏过程,收集阿霍烯馏分。(3) Molecular distillation separation: Put the garlic oil into the constant temperature tank of the molecular distillation device, heat the hot oil machine to 50°C, control the vacuum to 30Pa, and the dropping speed is 1 drop/3 seconds. Start the distillation process and collect the ajoene fraction.
(4)制备液相纯化:阿霍烯馏分用5倍体积的50%乙醇溶解,过滤后上制备色谱,以Innoval ODS-2为填料,90%乙醇为洗脱剂,以15mL/min的流速进行洗脱,收集阿霍烯分离液,60℃减压浓缩至油状物,即得阿霍烯,阿霍烯的纯度为97.6%。(4) Preparative liquid phase purification: Dissolve the ajoene fraction with 5 times the volume of 50% ethanol, filter and apply to preparative chromatography, using Innoval ODS-2 as the filler, 90% ethanol as the eluent, and a flow rate of 15mL/min Carry out elution, collect the ajoene separated liquid, and concentrate under reduced pressure at 60°C to an oily substance to obtain ajoene. The purity of ajoene is 97.6%.
上述虽然结合附图对本发明的具体实施方式进行了描述,但并非对本发明保护范围的限制,所属领域技术人员应该明白,在本发明的技术方案的基础上,本领域技术人员不需要付出创造性劳动即可作出的各种修改或变形仍在本发明的保护范围以内。Although the specific embodiments of the present invention have been described above in conjunction with the accompanying drawings, they do not limit the scope of the present invention. Those skilled in the art should understand that based on the technical solutions of the present invention, those skilled in the art do not need to perform creative work. Various modifications or variations that can be made are still within the protection scope of the present invention.
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