CN1067433C - Production of sugar from corn starch and glutamic acid fermentation - Google Patents
Production of sugar from corn starch and glutamic acid fermentation Download PDFInfo
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- CN1067433C CN1067433C CN97121661A CN97121661A CN1067433C CN 1067433 C CN1067433 C CN 1067433C CN 97121661 A CN97121661 A CN 97121661A CN 97121661 A CN97121661 A CN 97121661A CN 1067433 C CN1067433 C CN 1067433C
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- corn
- sugar
- glutamic acid
- acid fermentation
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Abstract
The present invention relates to production technology for making sugar by corn crude starches, and glutamic acid fermentation with the sugar as a culture medium by a biotin suboptimal method. The technology comprises: corn is soaked and crushed; embryos of the corn are removed; mixed slurry is then obtained by grinding with pins; the mixed slurry is directly liquefied and saccharified to obtain glucose. The sugar is used for preparing a culture medium to carry out glutamic acid fermentation by a biotin suboptimal mode. The present invention has the advantages of simple technology, low power consumption and maintenance cost, higher conversion rates from corn to sugar, higher by-product yield of corn, and obvious economic and social benefit. Moreover, the pollution to environment caused by waste water in the technical process from corn to sugar is reduced.
Description
The present invention relates to a kind ofly carry out the production technique of microbial fermentation, be meant with the thick starch refine dsugar of corn especially and prepare substratum with this and adopt vitamin H suboptimal dose method to carry out the glutamic acid fermentation production technique with Maize Production glucose and as substratum.
Utilize Maize Production glucose at present and prepare substratum that to adopt vitamin H suboptimal dose technology to carry out the technical process and the production and technical indication of glutamic acid fermentation as follows with this:
1, the technological process of production as shown in Figure 1
2, production and technical indication situation:
1), starch recoveries about 65% (with respect to corn)
2), pulverized sugar transformation efficiency about 90% (commodity starch relatively)
3), release the transformation efficiency 58.5% of corn to sugar from last two indexs
3), bloom (being Zein powder again) yield about 6% (with respect to corns)
4), maize peel yield about 8% (with respect to corn)
5), glucose acid invert ratio about 52%
6), extract yield about 90%
In sum, the shortcoming of existing technology is: corn after broken degerming pin mill is levigate, need through three grades of separation just can liquefy, saccharification, operational path is long, the equipment complexity, maintenance cost is big, and sugared yield is low, the sugar making cost height, and blowdown flow rate is big, increases the water treatment expense.
The object of the present invention is to provide a kind of with soaked corn after broken degerming pin mill is levigate, directly liquefy, saccharification obtains qualified Glucose Liquid, and, adopt vitamin H suboptimal dose method to carry out the production technique of glutamic acid fermentation with this sugar fluid configuration substratum.
The object of the present invention is achieved like this, and what it provided adopts vitamin H suboptimal dose method to carry out the production technique process following steps of glutamic acid fermentation with the thick starch refine dsugar of corn and with this sugar fluid configuration substratum:
1, purifies corn;
2, corn soaking is 65～72 hours, 60～65 ℃ of soaking temperatures;
3, broken apart plumule;
4, the feed liquid of removal plumule is levigate after the pin mill is with fragmentation;
5, pin being ground the feed liquid of getting off collects in the corresponding basin;
6, size mixing: as required sugared content is adjusted to suitable degree Beaume with the concentration of feed liquid in the jar of sizing mixing, and after adding alkali and transferring between pH value to 6.0～6.5, adds CaCl
2And amylase (20,000 unit) liquefies, and add-on is respectively 0.1～0.5% and 0.65～1.2 ‰ (relative 86% commodity starch);
7, liquefaction: 95～105 ℃ of steam ejection liquefaction temperature, 125～140 ℃ of second spraying liquefaction temperatures;
8, saccharification: transfer pH value to 4.2～4.4, add saccharifying enzyme (100,000 unit), add-on is 1.5～2.5 ‰ (relative 86% commodity starch), 60 ± 1 ℃ of saccharification temperatures;
9, filtration obtains qualified finished product Glucose Liquid;
10, use this Glucose Liquid, other adds an amount of K
+, PO
3- 4, Mg
2+, the preparation substratum carries out the suboptimal dose fermentation of L-glutamic acid;
11, etc. ionization is handed over and is extracted L-glutamic acid.
Technical process of the present invention and production and technical indication situation are as follows:
1, the technological process of production is as shown in Figure 2:
2, production and technical indication situation:
1), corn is to the yield about 70% (with respect to corn) of sugar
2), bloom (being Zein powder again) yield about 11% (with respect to corns)
3), maize peel yield about 3% (with respect to corn)
4), glucose acid invert ratio about 52%
5), extract yield about 90%
Performance analysis is as follows:
Corn to sugar benefit:
Promptly making sugared profit with one ton of corn of former technology is: 1754.9-1649.9=105 unit (wherein: 1754.9 are the output value, and 1649.9 is cost);
The profit of making sugar with one ton of corn of novel process is: 2125.5-1633.65=491.85 (wherein: 2125.5 are the output value, and 1633.65 is cost);
From top analysis as can be seen, process one ton of corn equally generates profit than former technology with novel process more: 491.85-105=386.95 unit.
Overall benefit: 5800 cubic metres of "Lotus" gourmet powder group of enterprises fermentation volumes, on average produce 6380 tons of bran acid the whole month, should consume about 14036 tons of pure sugar, need 24922 tons of corns, by above reckoning, new skill mutually uses one ton of corn can increase by 386.95 yuan of benefits than former technology, and complete or collected works rolled into a ball and increased benefit 964.4 ten thousand yuan more the whole month so, and annual complete or collected works roll into a ball and increase benefit 1.16 hundred million yuan more.If national msg output then can increase benefit 5.14 hundred million yuan every year by producing 400000 tons of calculating per year more.Save 370,000 tons of corns.
2. fermention medium adds vitamin H no longer in addition, and other nutrition accessory can reduce, and adds up to ton L-glutamic acid can reduce cost 20 yuan, and then whole group can increase by 1,530,000 yuan of benefits year more.
3. because of operational path is simple, also save a large amount of electric power and sewage disposal expense and maintenance of equipment expense.
Advantage of the present invention is as follows:
1., soaked corn directly liquefies after broken degerming pin mill is levigate, saccharification, simplified the production technique of corn to glucose, and electric power and maintenance cost are descended greatly.
2., it is broken that this process using is soaked the back earlier, vitamin H excessive in the corn is soaked out, the Glucose Liquid that makes fermentation industry utilize the thick starch of corn to make over several years can only adopt homobiotin method fermentation and the difficult problem that can not carry out the fermentation of vitamin H suboptimal dose method has obtained solution.
3., corn is dropped to present 1 ton to the quantity of wastewater effluent of glucose for 7 tons by an original ton corn, the waste water control expense reduces greatly.
4., corn brings up to 72% to the yield of glucose by original 58%.
5., corn by original 19.95%, brings up to 21.3% to the yield of glucose solid substance.
6., nutritious in the liquid glucose that makes with this processing method, the supplementary product onsumption in the fermention medium has obtained decline.
Embodiments of the invention are provided below:
Present embodiment is a kind of with the thick starch refine dsugar of corn and with this sugar fluid configuration substratum, adopts vitamin H suboptimal dose method to carry out the production technique of glutamic acid fermentation, these technology process following steps:
1, the corn that purifies is transported in the steeping tank for 118.5 tons;
2, soaked 70 hours, soaking temperature is controlled at 60 ℃;
3, broken apart plumule;
4, the feed liquid behind the separated plumule is levigate through the pin mill;
5, collect pin and grind the feed liquid of getting off in corresponding basin;
6, the Baume (filtering the back) of feed liquid is transferred to 12Be °, adds alkali and transfer PH to 6.3, add CaCl
20.2% (relative 86% commodity starch) and amylase (20,000 unit) 0.8 ‰ (relative 86% commodity starch) liquefy;
7, liquefaction temperature: 105 ℃ of steam ejection liquefaction temperature, 130 ℃ of second spraying liquefaction temperatures;
8, liquefaction finishes to transfer PH to 4.2 after iodine examination fully, adds saccharifying enzyme (100,000 unit) 2.0 ‰ (relative 86% commodity starch), carries out saccharification, 60 ± 1 ℃ of saccharification temperatures;
9, obtain qualified finished product Glucose Liquid after the filtration, survey DE value 98.5% (the DE value is the content of reducing sugar), transparence 85%, glucose content 17%, liquid glucose volume 502m
3, corn is to sugared yield 72.02%;
10, use KCl, 0.15% the Na of the liquid glucose adding 0.1% that makes
2HPO
4, 0.07% MgSO
4, the preparation substratum carries out the suboptimal dose fermentation of L-glutamic acid;
11, etc. ionization is handed over and is extracted L-glutamic acid, and three batch fermentation liquid are 160m
3(volume) produces acid and is respectively 9.0% (containing 9 tons in L-glutamic acid in 100 cubic metres of fermented liquids), 8.8%, 9.5%, and average glucose acid invert ratio is 52.35%, receives 40.3 tons of bran acid altogether.
Claims (1)
1, a kind of sugar from corn starch and glutamic acid fermentation production technique is characterized in that through following steps:
(1) purifies corn;
(2) corn soaking is 65～72 hours, 60～65 ℃ of soaking temperatures;
(3) broken apart plumule;
(4) feed liquid of removal plumule is levigate after the pin mill is with fragmentation;
(5) pin being ground the feed liquid of getting off collects in the corresponding basin;
(6) as required sugared content is adjusted to suitable degree Beaume with the concentration of feed liquid in the jar of sizing mixing, and after adding alkali and transferring between pH value to 6.0～6.5, adds CaCl
2Liquefy with amylase, add-on is respectively 0.1～0.5% and 0.65～1.2 ‰;
95～105 ℃ of (7) steam ejection liquefaction temperature, 125～140 ℃ of second spraying liquefaction temperatures;
(8) transfer pH value to 4.2～4.4, add saccharifying enzyme and carry out saccharification, add-on is 1.5～2.5 ‰, 60 ± 1 ℃ of saccharification temperatures;
(9) filtration obtains Glucose Liquid;
(10) use this Glucose Liquid, other adds an amount of K
+, PO
3- 4, Mg
2+, the preparation substratum carries out the suboptimal dose fermentation of L-glutamic acid;
(11) etc. ionization is handed over and is extracted L-glutamic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97121661A CN1067433C (en) | 1997-11-24 | 1997-11-24 | Production of sugar from corn starch and glutamic acid fermentation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97121661A CN1067433C (en) | 1997-11-24 | 1997-11-24 | Production of sugar from corn starch and glutamic acid fermentation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1218111A CN1218111A (en) | 1999-06-02 |
| CN1067433C true CN1067433C (en) | 2001-06-20 |
Family
ID=5176358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97121661A Expired - Fee Related CN1067433C (en) | 1997-11-24 | 1997-11-24 | Production of sugar from corn starch and glutamic acid fermentation |
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| Country | Link |
|---|---|
| CN (1) | CN1067433C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101688226A (en) * | 2007-07-06 | 2010-03-31 | 巴斯夫欧洲公司 | Method for the production of an aqueous glucose solution from corn |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102004026152A1 (en) | 2004-05-28 | 2005-12-15 | Basf Ag | Fermentative production of fine chemicals |
| DE102005056667A1 (en) | 2005-11-28 | 2007-05-31 | Basf Ag | Fermentative preparation of organic compounds, useful for making e.g. amino acids or enzymes, comprises using a starch source from which non-starch solids have not been removed, hydrolyzed and gelatinized with steam |
| DE102005056669A1 (en) | 2005-11-28 | 2007-05-31 | Basf Ag | Fermentative preparation of organic compounds, useful for making, e.g. amino acids or enzymes, using a starch source from which non-starch solids have not been removed, hydrolyzed and enzymatically converted to monosaccharides |
| DE102005056668A1 (en) | 2005-11-28 | 2007-05-31 | Basf Ag | Fermentative preparation of organic compounds, useful for making e.g. amino acids or enzymes, comprises using a starch source from which non-starch solids have not been removed, hydrolyzed and mixed with sugars |
| DE102009028549A1 (en) | 2009-08-14 | 2011-02-17 | Acs Agrochemische Systeme Gmbh | Preparing glucose solution from starch comprises e.g. transferring starch milk into liquefaction container containing amylase, maintaining at specified temperatures, and transferring into saccharification container comprising glucoamylase |
| CN101914584B (en) * | 2010-09-03 | 2013-07-10 | 王东阳 | Method for producing L-tryptophan |
| CN102511658B (en) * | 2011-11-04 | 2013-09-04 | 中粮生物化学（安徽）股份有限公司 | Processing method of sugar slag generated in wet-method sugar preparation, endosperm protein product and wet-method sugar preparation method |
| CN105124518B (en) * | 2015-09-09 | 2018-02-09 | 广东百味佳味业科技股份有限公司 | A kind of technique of potato starch manufacture monosodium glutamate |
| CN110004199A (en) * | 2019-03-13 | 2019-07-12 | 浙江华太生物科技有限公司 | A kind of rice protein, glutamic acid slag processing method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1071698A (en) * | 1991-10-12 | 1993-05-05 | 广东江门生物技术开发中心酶制剂厂 | Produce Sodium Glutamate with double-enzyme method sugar making |
-
1997
- 1997-11-24 CN CN97121661A patent/CN1067433C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1071698A (en) * | 1991-10-12 | 1993-05-05 | 广东江门生物技术开发中心酶制剂厂 | Produce Sodium Glutamate with double-enzyme method sugar making |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101688226A (en) * | 2007-07-06 | 2010-03-31 | 巴斯夫欧洲公司 | Method for the production of an aqueous glucose solution from corn |
| US8293504B2 (en) | 2007-07-06 | 2012-10-23 | Basf Se | Method for the production of an aqueous glucose solution |
| CN101688226B (en) * | 2007-07-06 | 2014-07-30 | 巴斯夫欧洲公司 | Method for the production of an aqueous glucose solution from corn |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1218111A (en) | 1999-06-02 |
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