CN1288954A - Enzymolysis process of producing oligosaccharide - Google Patents
Enzymolysis process of producing oligosaccharide Download PDFInfo
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- CN1288954A CN1288954A CN 99117102 CN99117102A CN1288954A CN 1288954 A CN1288954 A CN 1288954A CN 99117102 CN99117102 CN 99117102 CN 99117102 A CN99117102 A CN 99117102A CN 1288954 A CN1288954 A CN 1288954A
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- enzyme digestion
- digestion reaction
- enzymolysis
- oligose
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Abstract
The present invention uses the plants as raw material and adopts the production steps of pretreatment, enzymolysis, inactivating, separating and screening, etc. to produce low-cost oligosaccharide with high biological activity.
Description
The present invention relates to a kind of production method of oligose, particularly a kind of is that raw material carries out the method that enzymolysis is produced oligose with the plant.
In the prior art, oligose is applied to a plurality of fields, and as medicine, healthcare products, food etc., patent application 96196047.7 provides a kind of bacteriostatic method of oligosaccharide compound.The traditional method of oligose production is synthetic with the organic chemistry method, also can obtain by the degraded of natural sugar, glycolipid, glycopeptide, separates from human milk.People also constantly invent some new production methods, patent application 98111000.2 provides a kind of " the tubular fibre enzyme mebrane reactor prepares the method for isomaltooligosaccharide continuously ", with starch is raw material, earlier prepare malto-oligosaccharide with a-amylase and Pullulanase saccharification, the back is changeed glycosides with a-glucosiduronate and fungal amylase and is made dextrinosan; Patent application 98108773.6 provides " a kind of preparation method who is rich in the dextrinosan slurry "; Patent application 96193563.4 provides a kind of " preparation method of sulfated oligosaccharides and purposes ".The production method of various oligose and compound thereof is had nothing in common with each other, and selectes according to actual.
The production method that the purpose of this invention is to provide a kind of new oligose, enzymolysis obtains oligose from the plant that contains polysaccharide material, creates new production approach, widens the Application Areas of oligose.
Purpose of the present invention can realize by following technical measures: the present invention is raw material with the plant, and production technique mainly contains pre-treatment, enzymolysis, deactivation, separation, screening step.Pre-treatment is that the foreign material of raw material are removed, and cleans up, and is ground into the small-particle powder after air-dry; Enzymolysis is that powder and water are added in the retort, stirs, heats, and adds enzyme again and carries out enzyme digestion reaction; Deactivation is to arrive when requiring when enzyme digestion reaction, and heat temperature raising is rapidly killed the activity of enzyme, enzymolysis reaction; Solid-liquid separation is that larger particles is removed in the material centrifugation behind the enzymolysis, obtains clear liquid through press filtration, smart filter again; Screening is with film clear liquid to be carried out ultrafiltration and reverse osmosis to concentrate, and obtains the oligose concentrated solution.The key of this processing method is the control of enzymolysis, deactivation.
Fig. 1 is the technological process of production figure that a kind of enzymolysis process is produced oligose.
The invention will be further described below in conjunction with accompanying drawing: with reference to Fig. 1, present method is a raw material with the plant that contains polysaccharide material, but the tender shoots of draft, xylophyta, as the seedling bud of the tender shoots of trees, rice wheat, bean sprouts, hotbed chives etc., as long as contain the polysaccharide composition, can use as raw material.The raw material of gathering is carried out pre-treatment, foreign material is removed, after cleaning up, air-dry pulverizing, sieve powder, powder can directly be supplied with enzymolysis, it is standby also can to pack refrigeration.Powder and water are added in the retort, stirring and adjusting pH value is 3.5～5.5, be heated to 30～55 ℃, add an amount of enzyme, constant temperature carries out enzyme digestion reaction, Heating temperature and enzyme concentration directly influence the speed of enzyme digestion reaction, and Heating temperature, enzyme concentration are directly proportional with speed of response, can select by actual needs.When enzyme digestion reaction reaches requirement, heat to deactivation more than 80 ℃ rapidly, kill the active postcooling of enzyme, enzyme digestion reaction is to use the enzyme liberating polysaccharide, and the vigor of enzyme exists, and reaction is just proceeded, polysaccharide is degraded to oligose, is degraded to monose again, the material of reaction is the mixture of multiple sugar, our needs are oligose, to proceed to oligose maximum when reaction, and polysaccharide, monose more just reach requirement, heat up rapidly and kill the vigor of enzyme, enzymolysis reaction.Material behind the enzymolysis is carried out solid-liquid separation, can carry out coarse filtration earlier, remove the material slag, on whizzer, remove macrobead again, remove small-particle, obtain clear liquid through filter press, smart filter, millipore filtration etc.Clear liquid is carried out molecular screening, select for use the film of holding back 10000 molecular weight to carry out ultrafiltration earlier, discard macromole liquid, get, select the film of holding back 500 molecular weight again for use, under certain pressure, concentrate, discard small molecules liquid, obtain the concentrated solution of 500～10000 molecular weight through liquid.If the production aqua product, but sterilising packaging is a finished product; If the production powder product can carry out lyophilize to concentrated solution, be packaged as finished product through crushing screening.
Present method has been opened up oligose production new way, the operational path of selecting for use is reasonable, is raw materials for production with the plant, and raw material solves easily, cheap, the technology of producing is simpler, control easily, the oligose product biologically active of production, it can induce plant synthetic, accumulation plant protecting chemical, expansion toxin, the Application Areas of anti-wide oligose has new breakthrough to biotechnology applications.
Claims (6)
1. the processing method that enzymolysis process is produced oligose is characterized in that with the plant being raw material, after the pre-treatment, adding water stirs, heats, add enzyme and carry out enzyme digestion reaction, when enzyme digestion reaction arrival requires, heat temperature raising deactivation rapidly, enzymolysis reaction, carry out solid-liquid separation, obtain clear liquid, screen again, with film clear liquid is carried out ultrafiltration and reverse osmosis and concentrate, hold back oligosaccharides molecule.
2. processing method according to claim 1 is characterized in that raw material is the plant that contains polysaccharide material.
3. processing method according to claim 1, the Heating temperature that it is characterized in that enzyme digestion reaction is 30～55 ℃.
4. processing method according to claim 1 is characterized in that the material pH value of enzyme digestion reaction is adjusted into 3.5～5.5.
5. processing method according to claim 1 heats to rapidly more than 80 ℃ when it is characterized in that deactivation.
6. processing method according to claim 1 is characterized in that screening and selects for use the film of holding back 10000 molecular weight to carry out ultrafiltration, selects for use the film of holding back 500 molecular weight to concentrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB991171020A CN1140630C (en) | 1999-09-21 | 1999-09-21 | Enzymolysis process of producing oligosaccharide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB991171020A CN1140630C (en) | 1999-09-21 | 1999-09-21 | Enzymolysis process of producing oligosaccharide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1288954A true CN1288954A (en) | 2001-03-28 |
| CN1140630C CN1140630C (en) | 2004-03-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB991171020A Expired - Fee Related CN1140630C (en) | 1999-09-21 | 1999-09-21 | Enzymolysis process of producing oligosaccharide |
Country Status (1)
| Country | Link |
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| CN (1) | CN1140630C (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7582453B2 (en) | 2004-01-15 | 2009-09-01 | Advance Will Technology Limited | Method to control the distribution of the starch sugar's molecular weight in oligosaccharides production |
| US7906314B2 (en) | 2004-01-15 | 2011-03-15 | Advance Will Technology Limited | Method for the removal of monosaccharide in oligosaccharides production |
-
1999
- 1999-09-21 CN CNB991171020A patent/CN1140630C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7582453B2 (en) | 2004-01-15 | 2009-09-01 | Advance Will Technology Limited | Method to control the distribution of the starch sugar's molecular weight in oligosaccharides production |
| US7906314B2 (en) | 2004-01-15 | 2011-03-15 | Advance Will Technology Limited | Method for the removal of monosaccharide in oligosaccharides production |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1140630C (en) | 2004-03-03 |
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Granted publication date: 20040303 Termination date: 20120921 |