CN1566352A - Process for preparing isoflavone aglycon - Google Patents
Process for preparing isoflavone aglycon Download PDFInfo
- Publication number
- CN1566352A CN1566352A CN 03112420 CN03112420A CN1566352A CN 1566352 A CN1566352 A CN 1566352A CN 03112420 CN03112420 CN 03112420 CN 03112420 A CN03112420 A CN 03112420A CN 1566352 A CN1566352 A CN 1566352A
- Authority
- CN
- China
- Prior art keywords
- isoflavone
- enzyme
- isoflavones
- water
- glucoside
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- CJWQYWQDLBZGPD-UHFFFAOYSA-N isoflavone Natural products C1=C(OC)C(OC)=CC(OC)=C1C1=COC2=C(C=CC(C)(C)O3)C3=C(OC)C=C2C1=O CJWQYWQDLBZGPD-UHFFFAOYSA-N 0.000 title claims abstract description 103
- 235000008696 isoflavones Nutrition 0.000 title claims abstract description 103
- GOMNOOKGLZYEJT-UHFFFAOYSA-N isoflavone Chemical compound C=1OC2=CC=CC=C2C(=O)C=1C1=CC=CC=C1 GOMNOOKGLZYEJT-UHFFFAOYSA-N 0.000 title claims description 44
- 238000004519 manufacturing process Methods 0.000 title abstract description 11
- DKVBOUDTNWVDEP-NJCHZNEYSA-N teicoplanin aglycone Chemical compound N([C@H](C(N[C@@H](C1=CC(O)=CC(O)=C1C=1C(O)=CC=C2C=1)C(O)=O)=O)[C@H](O)C1=CC=C(C(=C1)Cl)OC=1C=C3C=C(C=1O)OC1=CC=C(C=C1Cl)C[C@H](C(=O)N1)NC([C@H](N)C=4C=C(O5)C(O)=CC=4)=O)C(=O)[C@@H]2NC(=O)[C@@H]3NC(=O)[C@@H]1C1=CC5=CC(O)=C1 DKVBOUDTNWVDEP-NJCHZNEYSA-N 0.000 title description 17
- 238000000034 method Methods 0.000 claims abstract description 36
- 229930182478 glucoside Natural products 0.000 claims abstract description 32
- -1 isoflavone glucoside Chemical class 0.000 claims abstract description 24
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- 108090000790 Enzymes Proteins 0.000 claims abstract description 23
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 3
- 241000196324 Embryophyta Species 0.000 claims description 37
- 244000068988 Glycine max Species 0.000 claims description 26
- 235000010469 Glycine max Nutrition 0.000 claims description 26
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- 101000925662 Enterobacteria phage PRD1 Endolysin Proteins 0.000 claims description 19
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- 102000006995 beta-Glucosidase Human genes 0.000 claims description 8
- 108010047754 beta-Glucosidase Proteins 0.000 claims description 8
- 239000000758 substrate Substances 0.000 claims description 4
- 229930182470 glycoside Natural products 0.000 abstract description 2
- 150000002338 glycosides Chemical class 0.000 abstract description 2
- 229930182486 flavonoid glycoside Natural products 0.000 abstract 1
- 150000007955 flavonoid glycosides Chemical class 0.000 abstract 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 61
- 150000002515 isoflavone derivatives Chemical class 0.000 description 38
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 37
- 239000003960 organic solvent Substances 0.000 description 27
- 239000005418 vegetable material Substances 0.000 description 26
- 235000019441 ethanol Nutrition 0.000 description 24
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 18
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 18
- 239000000284 extract Substances 0.000 description 15
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- 150000008131 glucosides Chemical group 0.000 description 11
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- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 8
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- ZQSIJRDFPHDXIC-UHFFFAOYSA-N daidzein Chemical compound C1=CC(O)=CC=C1C1=COC2=CC(O)=CC=C2C1=O ZQSIJRDFPHDXIC-UHFFFAOYSA-N 0.000 description 7
- 239000000706 filtrate Substances 0.000 description 7
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
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- TZBJGXHYKVUXJN-UHFFFAOYSA-N genistein Natural products C1=CC(O)=CC=C1C1=COC2=CC(O)=CC(O)=C2C1=O TZBJGXHYKVUXJN-UHFFFAOYSA-N 0.000 description 5
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- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 4
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- ZCOLJUOHXJRHDI-CMWLGVBASA-N genistein 7-O-beta-D-glucoside Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC(O)=C2C(=O)C(C=3C=CC(O)=CC=3)=COC2=C1 ZCOLJUOHXJRHDI-CMWLGVBASA-N 0.000 description 4
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- TWCMVXMQHSVIOJ-UHFFFAOYSA-N Aglycone of yadanzioside D Natural products COC(=O)C12OCC34C(CC5C(=CC(O)C(O)C5(C)C3C(O)C1O)C)OC(=O)C(OC(=O)C)C24 TWCMVXMQHSVIOJ-UHFFFAOYSA-N 0.000 description 3
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- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 3
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- LOKCTEFSRHRXRJ-UHFFFAOYSA-I dipotassium trisodium dihydrogen phosphate hydrogen phosphate dichloride Chemical compound P(=O)(O)(O)[O-].[K+].P(=O)(O)([O-])[O-].[Na+].[Na+].[Cl-].[K+].[Cl-].[Na+] LOKCTEFSRHRXRJ-UHFFFAOYSA-I 0.000 description 3
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- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical class CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
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- XUCIJNAGGSZNQT-JHSLDZJXSA-N (R)-amygdalin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@H](O[C@@H](C#N)C=2C=CC=CC=2)O1 XUCIJNAGGSZNQT-JHSLDZJXSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
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- ATWHGWYKSFRYBN-UHFFFAOYSA-N Amygdaloside Natural products O1C(=O)C2(C)CCCC(C3CC4)(C)C2C1OCC3(C1)CC4C1(O)COC1OC(CO)C(O)C(O)C1O ATWHGWYKSFRYBN-UHFFFAOYSA-N 0.000 description 1
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- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
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Landscapes
- Medicines Containing Plant Substances (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The invention relates to a process for preparing iisoflavones, in particular a method for preparing flavonoid glycoside by extracting isoflavone glucoside from leguminous plants and converting isoflavone glucoside through utilizing plant source glycoside hydrolytic enzyme.
Description
The affiliated field of invention
The present invention relates to the method for production isoflavones, particularly relate to the glycosidic link lytic enzyme that from leguminous plants, extracts isoflavone glucoside and use plant origin and transform the method for producing isoflavone by isoflavone glucoside.
The background of invention
Isoflavones be mainly be present in leguminous plants particularly the class in the soybean have the phytochemicals of simple two benzene ring structures.In plant, isoflavones mainly exists with following several forms: (1) aglycon form; (2) can pass through β-glucoside bond and sugar moieties (as glucose) bonded aglycone form; (3) glucosides form+malonyl-part; (4) glucosides form+acetyl moiety.Wherein the glucoside form is water miscible and is that isoflavones is convenient to the main existence form transporting and store in plant.In vegetable cell, beta-glucosidase enzyme cracking sugar moieties produces and to have stronger biologic activity but isoflavones that water-fast basically aglycone is the aglycon form.
Discover that isoflavones is as a class phytoestrogen, have adjusting and reduce with women's endogenous estrogen level with alleviation or change relevant symptom (referring to United States Patent (USP) 5,569,459,5,498,631,5,516528 and WO99/48496), in addition, isoflavones also has anti-oxidant (referring to United States Patent (USP) 4,232122 and 4,366,082), reduce body inner cholesterol content (referring to Anthony et al., J.Nutr., 125:Suppl.3S:803S-804S, 1995), keep and improve osseous tissue growth (referring to United States Patent (USP) 6,369,200), and keep normal blood vessels function (Circulation, 90:1259,1994) isoreactivity.Particularly nearest research also shows, the isoflavone that contains in vegetable material such as the soybean (iso-flavone glucoside aglucon) can suppress human tumor cells' such as mammary cancer and prostate cancer growth (Biochem.And Biophy.Reas.Commmun.179:1,661-667,1991; The Prostate, 22:335-345,1993).
Isoflavone is the molecule with free two benzene ring structures that do not contain sugar moieties, mainly comprises than iso-flavone glucoside having stronger active genistein (Gen), daidzein (Den) and Daidezin.From as medicine and protective foods application point, the extraction of isoflavone and preparation have caused people's bigger interest.
The general method that the isoflavones binding substances that is connected with the glucosides group is converted into the isoflavone that does not contain glycosyl be known (for example referring to United States Patent (USP) 5,827,682,5,851,792 and 6,146,668; Japanese patent application 22258,669, Japanese Patent 89-345164/47 and International Patent Application PCT/US/94/10699).In the prior art, the method that is changed into isoflavone by naturally occurring iso-flavone glucoside or isoflavones binding substances (be the isoflavones that is connected with other extentions on the glucose molecule, for example 6 "-O-oxalyl Genistoside) comprises:
The one, at first in low pH down heating (80-100 ℃) handle soybean protein extract, make it then with can the cracking molecule in β-1, the lytic enzyme contact of 4-glycosidic link.After the hydrolysis, insoluble vegetable material and aqueous phase separation are opened, added suitable organic solvent then, extract thus and separate and obtain required isoflavone.Employed lytic enzyme can be naturally occurring in the vegetable material, or add.Wherein, the glycosylhydrolase that adds comprises beta-glucosidase enzyme, beta-galactosidase enzymes, beta-glucanase and beta-xylanase etc.Under the active situation of the natural enzyme that in utilizing vegetable material, exists, generally vegetable material (for example soyflour) need be heated several hours (referring to Japanese Patent 89-345164/47) under 45-55 ℃ of condition.But under the situation of only utilizing endogenous enzyme, can only reach about 50% transformation efficiency.
Second method is at first with ground plant (soybean) material and water mixing certain hour (several days to several hours), to make the isoflavones of natural glucosides form fully be dissolved in aqueous phase.Behind aqueous phase separatin non-soluble material, re-use above-mentioned enzymatic hydrolysis process the isoflavones of aqueous phase is changed into its aglycon form, reclaim it then.Perhaps, also can at first from aqueous mixture, optionally remove aglycon with the ion exchange resin absorption method, make water then: ORGANIC SOLVENT MIXTURES wash-out isoflavones from the resin column, use enzymatic digestion or heating/acid hydrolysis process that isoflavones is changed into its aglycon form (referring to Japanese Patent 95-272884/36) after the evaporation concentration.
The shortcoming that all has the following aspects of above-mentioned these methods: a plurality of treatment steps of (1) needs; (2) need heat and strong acid or highly basic processing; (3) productive rate of isoflavones is lower; And the cost of (4) employed lytic enzyme is very high.Therefore, it is a kind of more easy that this area is necessary to provide, and be suitable for large-scale industrial production and use, and the method for the lower production isoflavone of cost.
The purpose of invention
An object of the present invention is to provide and a kind ofly utilize exogenous glycosidic link lytic enzyme to prepare the method for isoflavone, be characterised in that wherein said glycosidic link lytic enzyme is the mixed enzyme of plant origin from the isoflavone glucoside of leguminous plants material source.
According to a preferred embodiment of the invention, wherein said leguminous plants material is selected from seeds of leguminous plant, chitting piece, plumule or de-fatted soybean dregs.
According to a preferred embodiment of the invention, wherein said leguminous plants is selected from soybean and black soya bean.
According to a preferred embodiment of the invention, wherein said mixed enzyme is to have β-1, the amygdalase of 4-glycosidic link hydrolytic activity and the mixture of prunase.
According to a preferred embodiment of the invention, wherein the add-on of said mixed enzyme accounts for the 0.1-10% of substrate weight.
The detailed description of invention
The present invention relates to the method for production isoflavones, particularly relate to from leguminous plants and to extract and use the enzyme of plant origin to transform the method that obtains isoflavone by isoflavone glucoside.
As previously mentioned, isoflavones is that form with isoflavone glucoside exists basically in plant materials under the native state.At intracellular biochemical function position, the sugar moieties of endogenous beta-glucosidase enzyme cracking molecule, producing has stronger biologic activity but isoflavones that water-fast basically aglycone is the aglycon form.
According to the present invention, those skilled in the art can be according to any known method by leguminous plants isoflavone glucoside and its binding substances that particularly separating natural exists in soybean or the black soya bean, utilize the particularly β-1 in Semen Armeniacae Amarum source of plant then, 4-glycosidic link lytic enzyme, and under the help of the endogenous enzyme of vegetable material (the particularly seeds of leguminous plant of leguminous plants plumule or germination) itself, iso-flavone glucoside is changed into its aglycon form with transformation efficiency near 100%.
Can use multiple diverse ways from vegetable material, to separate and purifying comprises the isoflavones of glucosides and two kinds of forms of aglycon.For example, can water and the mixture (for example 60% ethanol) of organic solvent extract the exsiccant vegetable material; Organic solvent is opened and removed to extract and insoluble plant material separation; The concentrated aqueous then required isoflavones (International Patent Application WO 99/23069) that promptly obtains mutually.Perhaps, the mixture of water and organic solvent (for example 60% ethanol) extracts pre-dried vegetable material (for example Semen astragali sinici); Remove insoluble vegetable material and organic solvent also with other organic solvents such as Petroleum ether extraction water; Separate the isoflavones (International Patent Application WO 99/43335) that obtains containing the aromatics chromophoric group with the HPLC method after removing organic solvent and dry water.Perhaps, at first the mixture of water and organic solvent (for example 60% ethanol) extracts dry and ground fresh plant material; The separation and Extraction thing is also removed organic solvent; Use organic solvent such as sherwood oil, hexane or ethyl acetate extraction water again; Remove organic solvent and dry water then and promptly obtain required isoflavone compositions (International Patent Application WO 99/48496).The aqueous extractant extraction isoflavone-containing and the proteinic vegetable material that perhaps, can at first be higher than isoelectric points of proteins in the vegetable material with the pH value; Separate aqueous extract then and approximately handling said extract under 45-75 ℃ and the pH6-10 condition, the isoflavones binding substances is changed into isoflavone glucoside (referring to United States Patent (USP) 5,726,034 and 6,015,785).
Sum up above-mentioned these methods, a common feature is, before with the organic solvent extraction isoflavones, best water or (exsiccant) vegetable material is flooded the sufficiently long time at first with the miscible organic solvent of water, discharge as much as possible in the hope of the glycosidic link lytic enzyme that vegetable material is contained self, and play a role in position, separating in conjunction with very infirm isoflavones-sugared combination.Wherein employed water miscibility organic solvent can be the alcohol (as methyl alcohol, ethanol, propyl alcohol and butanols) that contains 1-4 carbon atom, and ethylene glycol, propylene glycol, butyleneglycol, ethyl acetate and acetone etc.Steeping process is preferably under about 25 ℃ of lucifuges and the inert environments and finishes, and preferably in advance impregnated vegetable material is ground.
Therefore, in order from the leguminous plants material, to obtain the extract of enough homoisoflavones (particularly isoflavone) content, can be at first with at least a and miscible organic solvent extraction exsiccant vegetable material of water; Separate remove insoluble vegetable material after, the solution of using aliphatic hydrocrbon (for example normal heptane) to handle again as above to obtain is to remove oil substances; After removing organic solvent and drying, promptly obtain containing the particularly solid residue of isoflavone of relatively large isoflavones.
Yet, since vegetable material for example in soyflour or its extract content of endogenous glucoside lytic enzyme limited, adding organic solvent may destroy the decomposition that enzyme causes, so in the practice of suitability for industrialized production isoflavone, usually need be after the isoflavones product that obtains based on the glucosides form, utilize the β-1 of external source again, 4-glycosidic link lytic enzyme changes into iso-flavone glucoside the free isoflavones of aglycon form.Perhaps, from vegetable material, extract in the process of isoflavone, add the exogenous glycoside hydrolase of appropriate amount, have the productive rate of the isoflavone of stronger and more extensive biologic activity with increase in the endogenous enzyme of utilizing vegetable material.
As previously mentioned, be used for the β-1 of this conversion, 4-glycosidic link lytic enzyme comprises but is not only limited to beta-glucosidase enzyme, beta-galactosidase enzymes, beta-glucanase and beta-xylanase etc.Yet, mainly the price of the glycoside hydrolase by microorganism (particularly some fungi and bacterium) fermentative production and purifying is all very expensive for these, cause the production cost of isoflavone to improve, thereby be unfavorable for its being extensive use of as medicine and Foods or drinks additive.Therefore, this area demands providing a kind of wide material sources, the β that is used for above-mentioned conversion-1 easy to prepare and with low cost, 4-glycosidic link lytic enzyme preparation urgently.The inventor finds in the practice of using leguminous plants material extraction isoflavone, and the enzyme composition that is for example extracted in the Semen Armeniacae Amarum by the certain plants material promptly is to be used for the fabulous zymin of this purpose.
Therefore, the object of the present invention is to provide and a kind ofly utilize exogenous lytic enzyme to prepare the method for isoflavone, be characterised in that wherein said lytic enzyme is the particularly mixed enzyme that comprises amygdalase and prunase in Semen Armeniacae Amarum source of plant by the isoflavone glucoside of leguminous plants material source.
According to the present invention, those skilled in the art can select to use foregoing any known method to separate from vegetable material and obtain iso-flavone glucoside or comprise glucosides and the isoflavone extract of two kinds of forms of aglycon.Then, can in the said extracted thing, add the glucoside lytic enzyme composition of appropriate amount plant origin, iso-flavone glucoside be changed into its aglycon form with transformation efficiency near 100%.
According to the preferred embodiments of the invention, the leguminous plants that wherein is used to extract isoflavones can be soybean and black soya bean.In a preferred embodiment of the invention, said vegetable material can be mature seed, de-fatted soybean dregs, germinated soybean or black soya bean seed or its plumule (hypocotyl part) of leguminous plants such as soybean or black soya bean.
In order from Semen Armeniacae Amarum, to extract required enzyme composition, can at first use ether to handle fresh Semen Armeniacae Amarum dry and that pulverize, to remove grease wherein.Use the mixture (for example saturated aqueous solution of chloroform) of organic solvent and water fully to extract about 8-32 hour then.Use acid (for example Glacial acetic acid) precipitating proteins after removing by filter insolubles.And then filter, collect filtrate and use volume excess ethanol (more than 90%) to extract.Collect extract and, be drying to obtain required enzyme composition repeatedly with after the washing with alcohol.The mixing enzyme preparation that mainly comprises amygdalase and peach leaf enzyme that so obtains need not be further purified and can be directly used in the above-mentioned Enzymatic transformation that is become isoflavone by iso-flavone glucoside.
In general, be about 3-4% by described method by the rate of recovery of the synaptase preparation for preparing in the vegetable material.Can use amygdaloside (100mg) as substrate, detect the glycoside hydrolysis activity of the synaptase that so obtains according to standard method known in the art.
According to the preferred embodiments of the invention, when being used for that iso-flavone glucoside changed into isoflavone, in the enzymatic reaction system enzyme-added weight of formulation ratio account for the 0.1-10% of substrate (glucoside) dry weight, and preferably account for 5-8% (W/W).Our experimental result confirms, is approximately under the condition that 5-7 and temperature be approximately 30-60 ℃ at pH, and after enzyme digestion reaction 4-8 hour, the Enzymatic transformation rate that iso-flavone glucoside becomes isoflavone is not less than 90%.Therefore as seen, in the suitability for industrialized production of isoflavone, use is from the natural plant material β-1 in Semen Armeniacae Amarum source particularly, 4-glycosidic link lytic enzyme is finished the Enzymatic transformation that is become isoflavone by iso-flavone glucoside, not only greatly reduce production cost, but also can possess fabulous transformation efficiency.
For the purposes of the present invention, can use following method by extracting and reclaim the soybean isoflavones that mainly is the aglycon form in the soybean material usually: at first in soyflour, to add the water of 3-4 times of volume and its pH is transferred to about 5-5.5.25-45 ℃ dipping is after 6-12 hour down, and adding is equivalent to the as above synaptase of preparation of raw material weight 0.1%, and in 30-60 ℃ of following enzymolysis 4-8 hour.Centrifugal collection residue also uses 5-8 times of each refluxing extraction of excess ethyl alcohol of 60% and 80% once successively.Merging filtrate is also placed the back decompression recycling ethanol that spends the night.The pH of solution is transferred to isoelectric points of proteins (6.7-9.7) and the temperature (about 75-85 ℃) that raises time heat treated 1-2 hour with HCL.Centrifugal collection supernatant and water use conventional ultrafiltration device (molecular weight cut-off 100,000) ultrafiltration after it is diluted to 10 times of original volume.Then, collect filtrate and also cross polyamide column.Use ethanol gradient elution and obtain purity about 80% and the isoflavone product of high genistein content is arranged in 20-50% alcohol concn section.
As the alternative simplified method of another kind, also can be with vegetable material, water, β-1,4-glycosidic link lytic enzyme or its composition, and organic solvent combines, form and separate phase mixture: the organic phase that comprises the isoflavone that produces after wherein containing enzyme and vegetable material aqueous phase and being assigned enzymolysis.After being separated, can from organic solvent, separate obtaining required isoflavone.
In this step extracting method, being used for the enzyme that the cracking iso-flavone glucoside makes it to be converted into aglycon is the mixing enzyme preparation in above-mentioned Semen Armeniacae Amarum source.The advantage activity of said mixing enzyme preparation is the glucoside bond between cracking isoflavones and its sugar moieties.Under appropriate reaction conditions (30-60 ℃ and pH5-7), the relative reactivity of zymin (percentage transformation efficiency) is not less than 80%.Particularly, in the method for the many agent combination of above-mentioned formation, employed water-containing organic solvent (for example 60% ethanol) can not cause the inactivation of the zymin that adds simultaneously.
Employed vegetable material obtains from leguminous plants, and soybean, Semen astragali sinici, black soya bean, garbanzo, Lens culinaris and the broad bean of higher isoflavone content wherein preferably arranged.Wherein particularly preferably be the soybean and the black soya bean that are ground into subparticle.In some cases, in order to obtain the isoflavones output of more endogenous glycoside hydrolase and Geng Gao, also can use soybean germ or the germinated soybean of having that breaks out in the decortication processing than homoisoflavone and endogenous glycoside hydrolase content.
Employed solvent comprises alcohol (as ethanol, propyl alcohol and butanols), ester acid (as ethyl acetate, dimethyl phosphate), ketone (as acetone, ethyl methyl ketone), aldehyde and the ether etc. with 1 to 6 carbon atom in the isoflavones extracting method.Preferably select the organic solvent that toxicity is less relatively and easy volatilization is removed.The water that is used for present method can be distilled water, distilled water or deionized water.Ratio to water and organic solvent in the mixing proposition liquid does not have strict restriction, but uses the mixture of about equal-volume water and organic solution usually.
Be worth should be mentioned that especially, owing to can in single reactions steps, finish enzymatic digestion and two primary processes of solvent extraction, so this method can reduce production costs under the prerequisite that does not influence the isoflavones productive rate greatly.
Can use reduction vaporization or distillatory method to remove organic solvent, from residue, to reclaim isoflavone compounds.After removing organic phase, may also have the oil that is rich in isoflavone in a small amount in the remaining thing.For this reason, can use easy dissolving oil in case of necessity but remove these oil than hexane or heptane equal solvent that indissoluble is separated isoflavone.In addition, behind the enzymic digestion iso-flavone glucoside, also be necessary immediately to remove residual leguminous plants material.
The isoflavone of the aglycon form that as above prepares can be cooperated with appropriate carriers or vehicle, make and be suitable for oral pharmaceutical composition or other health compositions such as food, beverage.For example, can make tablet, capsule, pill, powder agent, suppository and solution and suspension agent according to the pharmaceutical composition that known method in the pharmaceutical industry will contain isoflavones.Wherein preferably be suitable for capsule and tablet through gastrointestinal administration.When preparation is suitable for the capsule, tablet, pill of oral administration and powder agent, can use sucrose, lactose, semi-lactosi, W-Gum, gelatin, Microcrystalline Cellulose, carboxymethyl cellulose etc. as carrier or vehicle.In addition, also can use in the pharmaceutical industry known method and ancillary component said pharmaceutical composition to be made solution and the suspension agent that is suitable for oral administration.In order to prepare solution or the suspension agent that is suitable for the outer administration of gi tract, can use distilled water, water for injection, isotonic sodium chlorrde solution or glucose solution, perhaps lower concentration (for example 1-100mM) phosphate buffered saline (PBS) (PBS) is as carrier or thinner.In case of necessity, can add one or more other ancillary components or additives in the preparation of these gi tract external administrations, for example can use xitix as antioxidant, use Sodium Benzoate etc. are as sanitas.In the preparation of these formulations, can also contain other appropriate solubilizing agent, disintegrating agent, lubricant, tinting material, dispersion agent or tensio-active agent.
The following example is intended to further illustrate rather than limit the present invention.Under the prerequisite of the spirit and principles in the present invention, all will fall into the present invention and await the reply in the claim scope inventing any change that indivedual technological steps carry out and changing.
Embodiment
Embodiment 1: the preparation of synaptase
With the about 50g of living Semen Armeniacae Amarum be placed in the boiling water soak 2 minutes after, remove crust and airing.Then in mortar with its grinding powder and with ether extraction to remove grease wherein.Further pulverize residue and add the about 100ml of the saturated distilled water of chloroform, in mortar, grind with even back room temperature and placed 24 hours.Filter to collect filtrate and to wherein adding 10 in Glacial acetic acid, with precipitation protein wherein.And then filter, collect 95% ethanol that clarifying filtrate also under agitation adds 2 times of volumes.Place after 1 hour, discard the remaining part of supernatant liquid and vacuum filtration, behind 95% ethanol repetitive scrubbing throw out, vacuum-drying promptly obtains the required zymin of about 1.671g.
Embodiment 2: extract from soyflour and preparation isoflavone (1)
Get soyflour 1kg, to wherein adding about 4000ml water and will using 1N hydrochloric acid that its pH is transferred to 5.5.30 ℃ down dipping add the as above synaptase (10g) of preparation that is equivalent to raw material weight 1% after 8 hours, and in 40 ℃ of following enzymolysis 6 hours.Centrifugal collection residue is also used 5 times of 60 and 80% excessive each refluxing extraction of ethanol once successively.Get the supernatant decompression recycling ethanol after merging filtrate and cold heavy the spending the night, till not having the ethanol flavor.Descended heat treated 1 hour in the temperature (about 80 ℃) that raises then.Centrifugal collection supernatant and water behind 10 times of original volume, use PLHK type ultrafiltration instrument (molecular weight cut-off 100,000) ultrafiltration with solution dilution.Then, collect filtrate and also cross polyamide resin (chemical plant is celebrated in Changzhou forever) post.Water, 20% ethanol, 50% ethanol, 70% ethanol and 95% ethanol gradient elution successively, and collect in 20-50% alcohol concn section and to obtain the isoflavone product.
(developping agent: benzene/butanone/methyl alcohol=3: 1: 1) analytical results shows the polymeric amide thin-layer chromatography, and as above Zhi Bei product is with genistein and daidzein.Analyze through HPLC, the content of the free aglucon of total isoflavone accounts for 88% (W/W) in the product.
Embodiment 3: extract from the defatted soybean meal powder and preparation isoflavone (2)
The 50kg defatted soyflour is placed on contains in 50L deionized water and 100g the stainless steel vessel by the synaptase of embodiment 1 described method preparation.On aqeous suspension, add the 10L ethyl acetate then gently to obtain two-phase compositions.Use vertical spiral shell paddle mixer to continue to stir then to mix water and organic phase.At this moment, promptly there is isoflavone to move into organic solvent mutually by water gradually in water and the organic solvent part that contacts.Wherein continuing to stir water can make the isoflavones of hydrolysis touch ethyl acetate as much as possible, continue to stir organic solvent and then help in the high isoflavones concentration gradient of two alternate formation mutually, thereby accelerate the dissolution rate of water-insoluble isoflavone in ethyl acetate.
After about 20 hours, stop to stir and making two to be separated.After ethyl acetate is removed in evaporation, adding about 2L hexane and mixing about 5 minutes in the oil that is not evaporated (about 200ml).Standing over night then is so that the particulate material of isoflavone-containing aglycon sinks to ending container bottom.Discard hexane: behind the oil phase, in lower floor's suspension (slurry), add about 50ml hexane to remove residual oil.Leave standstill this mixture once more with further deposit seeds material, discard hexane: oil phase, collect and dry remaining semi-solid slurry, promptly obtain extract.
High pressure liquid chromatography (HPLC) (HPLC) analysis revealed contains the isoflavones of the above aglycon form of 60% (W/W) of having an appointment in the gained material, and wherein the rate of recovery of genistein, daidzein and Daidezin all more than 80%.
Claims (5)
1, utilize exogenous glycosidic link lytic enzyme to prepare the method for isoflavone from the isoflavone glucoside of leguminous plants material source, be characterised in that wherein said glycosidic link lytic enzyme is the mixed enzyme of plant origin.
2, according to the process of claim 1 wherein that said leguminous plants material is selected from seeds of leguminous plant, chitting piece, plumule or de-fatted soybean dregs.
3, according to the process of claim 1 wherein that said leguminous plants is selected from soybean and black soya bean.
4, according to the process of claim 1 wherein that said mixed enzyme is to have β-1, the amygdalase of 4-glycosidic link hydrolytic activity and the mixture of prunase.
5, according to the process of claim 1 wherein that the add-on of said mixed enzyme accounts for the 0.1-10% of substrate weight.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN114214374A (en) * | 2021-12-24 | 2022-03-22 | 四川宇奥生物科技有限公司 | Method for preparing soybean isoflavone aglycone by fermentation method |
| CN114315782A (en) * | 2021-12-24 | 2022-04-12 | 四川宇奥生物科技有限公司 | A kind of preparation method of soybean isoflavone |
| US20230181652A1 (en) * | 2021-12-14 | 2023-06-15 | Naturewise Biotech & Medicals Corporation | Composition for enhancing cognitive abilities and use thereof |
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2003
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US20230181652A1 (en) * | 2021-12-14 | 2023-06-15 | Naturewise Biotech & Medicals Corporation | Composition for enhancing cognitive abilities and use thereof |
| CN114214374A (en) * | 2021-12-24 | 2022-03-22 | 四川宇奥生物科技有限公司 | Method for preparing soybean isoflavone aglycone by fermentation method |
| CN114315782A (en) * | 2021-12-24 | 2022-04-12 | 四川宇奥生物科技有限公司 | A kind of preparation method of soybean isoflavone |
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