CN1888079A - Saccharizing process in glucose production - Google Patents
Saccharizing process in glucose production Download PDFInfo
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- CN1888079A CN1888079A CN 200610045539 CN200610045539A CN1888079A CN 1888079 A CN1888079 A CN 1888079A CN 200610045539 CN200610045539 CN 200610045539 CN 200610045539 A CN200610045539 A CN 200610045539A CN 1888079 A CN1888079 A CN 1888079A
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- glucose
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Abstract
The saccharizing process for glucose production includes the following steps: setting crystallized glucose mother liquid or the mixture of crystallized glucose mother liquid and starch emulsion into saccharifying tank; and saccharifying via adding enzyme of 0.4-0.5 L/T at pH 4.2-4.5 and 60-62 deg.c for 40-60 hr. The process has raised crystallized glucose mother liquid utilizing rate, disaccharide, trisaccharide and other oligosaccharides converted into glucose, DE value up to 91-96 %, raised glucose yield and low production cost.
Description
Technical field:
What the present invention relates to a kind of crystalline dextrose mother liquor effectively utilizes method, specifically with the mother liquor saccharification once more that produces in the engineering of producing crystalline dextrose, makes disaccharides, trisaccharide and polysaccharide in the mother liquor be converted into glucose.
Background technology:
Glucose is the most general monose material and important Essential Chemistry pharmaceuticals, one of main energy sources material of human body and animal.Be widely used in industries such as food, medicine, chemistry.Have a large amount of glucose mother liquid in the dextrose production process and produce, mother liquor generally contains the dry amount about 50%, and the DE value is (glucose is about 78%, and disaccharides is about 13%, trisaccharide and above sugar about 4%) about 89%.Therefore, except the glucose that contains more amount, also contain a large amount of oligose components in the mother liquor.It is good healthy food material.
At present, the processing mode of glucose mother liquid has two kinds, and a kind of is to sell with the form of waste material, and another kind is a raw material of mother liquor being used as biological fermentation, and the equal ubiquity of above dual mode the recovery problem.Make a large amount of glucose can better effectively not utilize, caused the on the low side of glucose yield and economic benefit.And,, also caused the waste of raw material because most of microbe can not be utilized wherein disaccharides, trisaccharide and other oligose as fermentation raw material.
Summary of the invention:
The objective of the invention is to overcome the deficiency that above-mentioned traditional treatment method exists and a kind of new method of effectively utilizing is provided, it squeezes into saccharifying tank separately with the crystalline dextrose mother liquor, or the crystalline dextrose mother liquor squeezed into starch milk liquefaction liquid carries out saccharification in the saccharifying tank, with disaccharides, trisaccharide and oligose in the crystalline dextrose mother liquor once more saccharification be converted into glucose.
Purpose of the present invention can realize by following technical measures: crystalline dextrose mother liquor or crystalline dextrose mother liquor mix with starch milk liquefaction liquid, squeeze into saccharifying tank.
Controlled variable in the saccharifying is as follows: saccharification time 40～60h, pH value 4.2～4.5, temperature 60-62 ℃, enzyme concentration 0.4～0.5L/T
Butt
Enzyme concentration is used as standard with contained butt amount in the mother liquor, so enzyme concentration of the present invention is that the required saccharifying enzyme quantity of mother liquor that whenever contains 1 ton of butt is 0.4～0.5 liter.
The crystalline dextrose mother liquor is after above-mentioned saccharification, and the DE value can reach 91%～94%.
Crystalline dextrose mother liquor and starch milk liquefaction liquid mix carry out above-mentioned saccharification after, the DE value can reach 93%～96%, effect is better than separately mother liquor being carried out saccharification result, transformation efficiency is higher.
Outstanding feature of the present invention is: improved the utilization ratio of crystallization glucose mother liquid, made wherein disaccharides, trisaccharide and oligose further be converted into glucose.Thereby improved the yield of glucose, reduced cost, improved economic benefit and value-added content of product.
Embodiment:
Embodiment 1
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 40 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 91% glucose solution.
Embodiment 2
Glucose mother liquid finished product and starch milk liquefaction liquid are squeezed into saccharifying tank by 1: 99 mixed, saccharification time 41 hours, and pH 4.2～4.5,61 ℃ of temperature, enzyme concentration 0.45L/T
ButtAfter the saccharification the DE value is 96% glucose solution.
Embodiment 3
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 42 hours, pH4.2～4.5,62 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 91.5% glucose solution.
Embodiment 4
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 2: 8 mixed, saccharification time 43 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.45L/T
ButtAfter the saccharification the DE value is 95.5% glucose solution.
Embodiment 5
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 44 hours, pH4.2～4.5,61 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 92% glucose solution.
Embodiment 6
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 45 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 92% glucose solution.
Embodiment 7
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 3: 7 mixed, saccharification time 46 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 95% glucose solution.
Embodiment 8
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 47 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.45L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 9
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 48 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 94% glucose solution.
Embodiment 10
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 49 hours, pH4.2～4.5,61 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 11
Glucose mother liquid finished product and starch milk liquefaction liquid are squeezed into saccharifying tank by 4: 6 mixed, saccharification time 50 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.45L/T
ButtAfter the saccharification the DE value is 94.5% glucose solution.
Embodiment 12
Glucose mother liquid finished product and starch milk liquefaction liquid are squeezed into saccharifying tank by 5: 5 mixed, saccharification time 51 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 94% glucose solution.
Embodiment 13
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 52 hours, pH4.2～4.5,62 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 14
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 6: 4 mixed, saccharification time 53 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93.5% glucose solution.
Embodiment 15
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 54 hours, and pH 4.2～4.5,61 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 93.5% glucose solution.
Embodiment 16
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 55 hours, pH4.2～4.5,60 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 17
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 56 hours, and pH 4.2～4.5,61 ℃ of temperature, enzyme concentration 0.45L/T
ButtAfter the saccharification the DE value is 93.5% glucose solution.
Embodiment 18
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 7: 3 mixed, saccharification time 57 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 93.5% glucose solution.
Embodiment 19
The glucose mother liquid that obtains in the continuous conversion technology is squeezed into saccharifying tank, saccharification time 58 hours, pH4.2～4.5,62 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 20
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 8: 2 mixed, saccharification time 59 hours, and pH 4.2～4.5,61 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 21
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 60 hours, and pH 4.2～4.5,60 ℃ of temperature, enzyme concentration 0.4L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 22
Glucose mother liquid finished product and starch milk liquefaction liquid are squeezed into saccharifying tank by 9: 1 mixed, saccharification time 48 hours, and pH 4.2～4.5,62 ℃ of temperature, enzyme concentration 0.5L/T
ButtAfter the saccharification the DE value is 93% glucose solution.
Embodiment 23
Glucose mother liquid that obtains in the continuous conversion technology and starch milk liquefaction liquid are squeezed into saccharifying tank by 8: 2 mixed, saccharification time 62 hours, and pH 4.2～4.7,64 ℃ of temperature, enzyme concentration 0.3L/T
ButtAfter the saccharification the DE value is 91% glucose solution.
Embodiment 24
The glucose mother liquid finished product is squeezed into saccharifying tank, saccharification time 38 hours, and pH 4.0～4.5,58 ℃ of temperature, enzyme concentration 0.6L/T
ButtAfter the saccharification the DE value is 91% glucose solution.
Embodiment 25
Glucose mother liquid finished product and starch milk liquefaction liquid are squeezed into saccharifying tank by 1: 9 mixed, saccharification time 65 hours, and pH 4.0～4.8,58 ℃ of temperature, enzyme concentration 0.3L/T
ButtAfter the saccharification the DE value is 92% glucose solution.
Claims (4)
1.-the method for saccharifying in the kind dextrose production process is characterized in that: the crystalline dextrose mother liquor is directly squeezed into saccharifying tank carry out saccharification.
2. the method for saccharifying in the dextrose production process as claimed in claim 1 is characterized in that: crystalline dextrose mother liquor and starch milk liquefaction liquid is mixed squeeze into saccharifying tank and carry out saccharification.
3. the method for saccharifying in the dextrose production process as claimed in claim 1 or 2 is characterized in that: the controlled variable in the saccharifying is: saccharification time is 40～60h, pH value 4.2～4.5,60～62 ℃ of temperature, enzyme concentration 0.4～0.5L/T
Butt
4. the method for saccharifying in the dextrose production process as claimed in claim 3 is characterized in that: the saccharification time in the saccharifying is 45～50h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100455394A CN100425704C (en) | 2006-07-21 | 2006-07-21 | Saccharizing process in glucose production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100455394A CN100425704C (en) | 2006-07-21 | 2006-07-21 | Saccharizing process in glucose production |
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| Publication Number | Publication Date |
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| CN1888079A true CN1888079A (en) | 2007-01-03 |
| CN100425704C CN100425704C (en) | 2008-10-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2006100455394A Expired - Fee Related CN100425704C (en) | 2006-07-21 | 2006-07-21 | Saccharizing process in glucose production |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101386894B (en) * | 2008-09-08 | 2011-01-26 | 西王集团有限公司 | Sugar melting equipment and method in anhydrous dextrose production |
| CN101280331B (en) * | 2008-06-02 | 2011-07-20 | 湖南农业大学 | Fast liquefying-saccharifying method for starch |
| CN101205550B (en) * | 2006-12-20 | 2011-08-17 | 凯能高科技工程（上海）有限公司 | Retreatment method of glucose crystallization mother liquor |
| CN103484511A (en) * | 2012-12-20 | 2014-01-01 | 西王药业有限公司 | Production method for high-pH anhydrous glucose |
| CN104911236A (en) * | 2015-05-22 | 2015-09-16 | 山东祥瑞药业有限公司 | Corn starch milk hydrolysis technology |
| CN104911235A (en) * | 2015-05-22 | 2015-09-16 | 山东祥瑞药业有限公司 | Medical dextrose monohydrate production technology |
| CN108866123A (en) * | 2018-07-24 | 2018-11-23 | 河南飞天农业开发股份有限公司 | A kind of production technology that jam is syrup dedicated |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1319677A (en) * | 2001-01-16 | 2001-10-31 | 雷尘恩 | Cost-saved solid glucose production process |
| CN1301334C (en) * | 2005-07-01 | 2007-02-21 | 江南大学 | Method for extracting high purity glucose and functional oligose from crystalline glucose mother liquid |
-
2006
- 2006-07-21 CN CNB2006100455394A patent/CN100425704C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101205550B (en) * | 2006-12-20 | 2011-08-17 | 凯能高科技工程（上海）有限公司 | Retreatment method of glucose crystallization mother liquor |
| CN101280331B (en) * | 2008-06-02 | 2011-07-20 | 湖南农业大学 | Fast liquefying-saccharifying method for starch |
| CN101386894B (en) * | 2008-09-08 | 2011-01-26 | 西王集团有限公司 | Sugar melting equipment and method in anhydrous dextrose production |
| CN103484511A (en) * | 2012-12-20 | 2014-01-01 | 西王药业有限公司 | Production method for high-pH anhydrous glucose |
| CN104911236A (en) * | 2015-05-22 | 2015-09-16 | 山东祥瑞药业有限公司 | Corn starch milk hydrolysis technology |
| CN104911235A (en) * | 2015-05-22 | 2015-09-16 | 山东祥瑞药业有限公司 | Medical dextrose monohydrate production technology |
| CN108866123A (en) * | 2018-07-24 | 2018-11-23 | 河南飞天农业开发股份有限公司 | A kind of production technology that jam is syrup dedicated |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100425704C (en) | 2008-10-15 |
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| C14 | Grant of patent or utility model | ||
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| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Shandong Xiwang Biochemical Technology Co., Ltd. Assignor: Shandong Xiwang Sugar Co., Ltd. Contract fulfillment period: 2007.6.1 to 2017.6.1 Contract record no.: 2010370000032 Denomination of invention: Saccharizing process in glucose production Granted publication date: 20081015 License type: Exclusive license Record date: 2010.1.18 |
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| LIC | Patent licence contract for exploitation submitted for record |
Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2007.6.1 TO 2017.6.1; CHANGE OF CONTRACT Name of requester: SHANDONG XIWANG BIOCHEMICAL SCIENCE AND TECHNOLOGY Effective date: 20100118 |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081015 Termination date: 20180721 |