CN1966695A - Circulation production process for alcohol with potatoes as main materials - Google Patents
Circulation production process for alcohol with potatoes as main materials Download PDFInfo
- Publication number
- CN1966695A CN1966695A CNA2006100976230A CN200610097623A CN1966695A CN 1966695 A CN1966695 A CN 1966695A CN A2006100976230 A CNA2006100976230 A CN A2006100976230A CN 200610097623 A CN200610097623 A CN 200610097623A CN 1966695 A CN1966695 A CN 1966695A
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- Prior art keywords
- alcohol
- fermentation
- digestive system
- raw material
- potato
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- 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.)
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Links
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 244000061456 Solanum tuberosum Species 0.000 title claims abstract description 12
- 235000002595 Solanum tuberosum Nutrition 0.000 title claims abstract description 12
- 239000000463 material Substances 0.000 title abstract description 6
- 235000012015 potatoes Nutrition 0.000 title 1
- 238000000855 fermentation Methods 0.000 claims abstract description 33
- 230000004151 fermentation Effects 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims abstract description 8
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 7
- 239000010802 sludge Substances 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims abstract description 6
- 210000002249 digestive system Anatomy 0.000 claims description 24
- 238000004821 distillation Methods 0.000 claims description 16
- 102000004190 Enzymes Human genes 0.000 claims description 13
- 108090000790 Enzymes Proteins 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 12
- 238000009413 insulation Methods 0.000 claims description 10
- 229920002472 Starch Polymers 0.000 claims description 6
- 229920001592 potato starch Polymers 0.000 claims description 6
- 235000019698 starch Nutrition 0.000 claims description 6
- 239000008107 starch Substances 0.000 claims description 6
- 239000008399 tap water Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 235000020679 tap water Nutrition 0.000 claims description 5
- 240000003183 Manihot esculenta Species 0.000 claims description 4
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 claims description 4
- 238000000926 separation method Methods 0.000 claims description 4
- 244000017020 Ipomoea batatas Species 0.000 claims description 3
- 235000002678 Ipomoea batatas Nutrition 0.000 claims description 3
- 239000000446 fuel Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 238000001816 cooling Methods 0.000 abstract description 7
- 238000005516 engineering process Methods 0.000 abstract description 7
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000004615 ingredient Substances 0.000 abstract description 2
- 102000013142 Amylases Human genes 0.000 abstract 1
- 108010065511 Amylases Proteins 0.000 abstract 1
- 102000004139 alpha-Amylases Human genes 0.000 abstract 1
- 108090000637 alpha-Amylases Proteins 0.000 abstract 1
- 229940024171 alpha-amylase Drugs 0.000 abstract 1
- 238000012258 culturing Methods 0.000 abstract 1
- 229940111205 diastase Drugs 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 238000005273 aeration Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- 101710089042 Demethyl-4-deoxygadusol synthase Proteins 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 239000002921 fermentation waste Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 235000012976 tarts Nutrition 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 206010006895 Cachexia Diseases 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000012262 fermentative production Methods 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 208000016318 wasting Diseases 0.000 description 1
Classifications
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The invention relates a annuliform production technique for producing alcohol with potato materials by utilizing anaerobic digesting solution as the technology ingredient water. The invention comprises the steps of: crushing potato starchiness materials, adding digesting solution, alpha- amylase, stirring uniformly, heating, incubating, liquefying, cooling, adding diastase, cooling after saccharification, inoculating yeast, culturing at constant temperature, distilling to obtain the product of alcohol, cooling the distilled waste mash, anaerobic-fermenting to obtain biogas, separating the broth to obtain digest and active sludge, and recycling the digest into the next fermentation to form a ring cycle. The distilled waste mash only needs anaerobic fermentation, which reduces the occupied ground area greatly and fixed asset investment. anaerobic fermentation is low cost, recycle of the digest can realize zero release of fermentation wastewater, completely eliminate the environmental pollution caused by the high concentration wastewater released by the present production of alcohol, and save large amount of water.
Description
Technical field
The present invention relates to a kind of annular production technique of utilizing anaerobic digestion solution to produce, belong to fermentation alcohol industrial technology field as the ethanol with potato raw material of technology batching water.
Background technology
Starchy material fermentative production alcohol is one of main method of Alcohol Production.In traditional starchy material fermentation producing wine Seiko skill, size mixing by water through pulverizing, adding for starchy material, boiling liquefaction and slight saccharification, inoculate then the distillery yeast fermentation (as " alcohol industry handbook one book is introduced, volumes such as Zhang Kechang, light industry press).The average alcohol per ton of traditional zymotic production technique will discharge 12～15 tons of useless mash, mash COD
CrMore than 40000～50000mg/L, not only cause serious water resource pollution, also cause a large amount of wastings of resources.
Existing Alcohol Production method of wastewater treatment mainly contains: the concentrate drying method is produced DDGS and first anaerobically fermenting and is produced behind the biogas aeration aerobic treatment etc.The concentrate drying method is produced DDGS and is had problems such as investment is big, working cost height.This method processed waste water energy qualified discharge, but still need to drop into certain working cost, therefore, the concentrate drying method is produced DDGS and is had good social benefit, and does not have economic benefit.Elder generation's anaerobically fermenting produce subject matter one that the method for aeration aerobic treatment behind the biogas exists be take up an area of big, investment is high, the 2nd, later stage aeration aerobic treatment has only to drop into does not have output, the treatment cost of waste water per ton up to 20 yuan about, the 3rd, waste water treatment is difficult to thoroughly, the waste water COD of discharging
CrStill about 500mg/L.The technology that adopts the slops circular batching is also arranged, but owing to contain a large amount of organic acids in the useless mash of the distillation after the zymamsis, the pH value is between 3.0～3.5, cause Ye Huamei can not normally bring into play vigor (optimum pH of Ye Huamei is between 6.0～6.5) when preparing burden the back liquefying starchiness raw material, cause slops partly to circulate, and circulation is batch limited, and a large amount of high-concentration wastewater emission are still arranged, and this method does not adopt on commercial production scale.
Summary of the invention
The objective of the invention is to overcome above-mentioned weak point, thereby provide a kind of alcohol annular production technique, the useless wine with dregs of tart distillation is through behind the anaerobically fermenting, and organism such as organic acid are degraded to biogas, has guaranteed that the reuse batching of Digestive system can not exert an influence to operations such as liquefaction, saccharification, fermentations; The useless mash of distillation only needs one step of anaerobically fermenting to handle, and can significantly reduce floor space and investment in fixed assets; The running cost of anaerobically fermenting is low, and the Digestive system recycle can realize the zero release of fermentation waste water, can eliminate the high-concentration waste liquid environmental pollution caused by discharge in the present Alcohol Production fully, and can save a large amount of precious water resource.
Main solution of the present invention is achieved in that
The present invention is the following processing step of alcohol annular production employing of main raw material with the potato class:
1, gets the potato starch raw material and pulverize upward batch Digestive system of back adding, the ratio of potato starch and Digestive system is 1: 2～5, adopt tap water to supply when Digestive system is not enough, after mixing, add high temperature resistant α-Dian Fenmei, the α-Dian Fenmei addition is 6～15U/g starch, and post-heating stirs, Heating temperature: 90～105 ℃, insulation liquefaction 50～120 minutes; Fast cooling to 60～65 ℃;
2, add saccharifying enzyme, the saccharifying enzyme addition is 80～150U/g starch, is 60～65 ℃ of insulation saccharification 0.5～1.5hr down in temperature, and saccharification is cooled to 28～35 ℃ after finishing;
3, insert the distillery yeast that spreads cultivation (yeast-inoculated amount) of 8～10%V/V, constant temperature culture fermentation 40～72hr, the ethanol concn in the maturing fermentation liquid is 8.0～15%v/v, obtains finished product alcohol through distillation;
4, the useless mash of getting after the above-mentioned distillation of distillation is cooled to 40～70 ℃, sends into anaerobic fermentation tank, and the constant temperature anaerobically fermenting was produced biogas in 10～15 days; The biogas supply boiler that acts as a fuel; Anaerobic fermented liquid obtains Digestive system and active sludge through solid-liquid separation; Digestive system loops back the next batch fermentation, constitutes annular collar, an infinite loop successively.
Potato starch raw material of the present invention can adopt potato raw materials such as Ipomoea batatas, cassava.
The pH value of Digestive system of the present invention is 6.0～8.0.
Compared with the prior art the present invention has the following advantages:
The useless wine with dregs of tart distillation among the present invention is through behind the anaerobically fermenting, and the useless mash of distillation is produced biogas by anaerobically fermenting, COD in the waste water
CrDrop to about 2000mg/L, the pH value rises to 6.0～8.0, and organism such as organic acid are degraded to biogas, has guaranteed that the reuse batching of Digestive system can not exert an influence to operations such as liquefaction, saccharification, fermentations; 2, the useless mash of the distillation among the present invention only needs one step of anaerobically fermenting to handle, and has significantly reduced floor space and investment in fixed assets; 3, got rid of the high aeration aerobic treatment of running cost among the present invention, and the running cost of anaerobically fermenting is low, the useless mash of distillation of adding alcohol per ton can produce about 350m
3The active sludge (can process about 300 kilograms of compound bio matter fertilizers) of the biogas of (mark attitude) (amounting to 350 kilograms of commercial coals approximately) and 200 kilograms, therefore, this technology has good economic benefit; 4, anaerobically fermenting Digestive system recycle among the present invention realizes the zero release of fermentation waste water, does not have fermentable discharge of wastewater, can eliminate the high-concentration waste liquid environmental pollution caused by discharge in the present Alcohol Production fully, and can save a large amount of precious water resource.
Description of drawings
Fig. 1 is a process flow sheet of the present invention.
Embodiment
Embodiment during following the present invention incites somebody to action in conjunction with the accompanying drawings is further described:
The present invention is the following processing step of alcohol annular production employing of main raw material with the potato class:
Embodiment one:
Get sweet potato powder 260g, batch Digestive system 850ml and 150ml tap water in the adding, 0.13 milliliter of the high temperature resistant α-Dian Fenmei that adding enzyme unit alive is 20000U/ml, the post-heating that stirs, 95 ℃ of insulations were liquefied 60 minutes; Fast cooling to 62 ℃ then, adding the enzyme unit that lives is 0.26 milliliter in the saccharifying enzyme of 100000U/ml, 62 ℃ of insulation saccharification 1hr, saccharification is cooled to 30 ℃ after finishing, and inserts the distillery yeast that spreads cultivation (yeast-inoculated amount) of 10%V/V, constant temperature culture fermentation 64hr; Fermentation ends, maturing fermentation liquid is long-pending to be 1165ml, ethanol concn is 8.8% (v/v); Obtain finished product alcohol 118ml (95.2%v/v), slops 1050ml through distillation; Slops is cooled to 55 ℃, sends into anaerobic fermentation tank, produces biogas, COD in the waste water through constant temperature anaerobically fermenting fortnight again
CrDrop to about 2000mg/L, the pH value is raised between 6.0～8.0.Through solid-liquid separation (filtration), obtain 60g active sludge and Digestive system 850ml; But active sludge processing biomass fertilizer, Digestive system can partly or entirely return ingredient station and the mixing of potato class powder is sized mixing, and insufficient section can replenish with the waste water after tap water or the aerobic treatment, realizes the water resources recycle.Digestive system loops back the next batch fermentation, and the technology main body constitutes an annular collar.
Embodiment two:
Tapioca Starch 2100g, batch slops 4500ml and 1000ml tap water in the adding, 1.4 milliliters of the high temperature resistant α-Dian Fenmei that adding enzyme unit alive is 20000U/ml, the post-heating that stirs, 95 ℃ of insulations were liquefied 50 minutes; Fast cooling to 62 ℃, adding the enzyme unit that lives is 2.6 milliliters in the saccharifying enzyme of 100000U/ml, 62 ℃ of insulation saccharification 1hr, saccharification is cooled to 30 ℃ after finishing, and inserts the distillery yeast constant temperature culture fermentation that spreads cultivation of 8%V/V, fermentation 68hr; Fermentation ends, maturing fermentation liquid is long-pending to be 6350ml, ethanol concn is 11.2% (v/v); Obtain finished product alcohol 1030ml (95.3%v/v) through distillation, slops 5400ml, slops are cooled to 55 ℃, send anaerobic fermentation tank constant temperature anaerobically fermenting fortnight, Digestive system obtains 200g active sludge and Digestive system 4500ml after filtration, and Digestive system loops back the next batch fermentation test.
Embodiment three:
Tapioca Starch 7800kg, crowd slops 29m in the adding
3And 5m
3Tap water, 5850 milliliters of the high temperature resistant α-Dian Fenmei that adding enzyme unit alive is 20000U/ml, the post-heating that stirs, 95 ℃ of insulations were liquefied 60 minutes; Fast cooling to 62 ℃, adding the enzyme unit that lives is 11700 milliliters in the saccharifying enzyme of 100000U/ml, 62 ℃ of insulation saccharification 0.8hr, saccharification is cooled to 28 ℃ after finishing, and inserts the distillery yeast fermentation that spreads cultivation of 8%V/V, fermentation 66hr; Fermentation ends, maturing fermentation liquid is long-pending to be 35.5m
3, ethanol concn is 10.3% (v/v); Obtain 3.1 tons of alcohol of finished product (95.2%v/v), slops 32.2m through distillation
3, through sending anaerobic fermentation tank behind the settling tank separation silt particle, 55～60 ℃ of leavening temperatures are collected metering and are obtained biogas 1056m
3(pressure 7KPa) filters back Digestive system 29m altogether
3, loop back the next batch fermentation.
Claims (3)
1, a kind of is the alcohol annular production technique of main raw material with the potato class, it is characterized in that adopting following processing step:
(1), gets the potato starch raw material and pulverize upward batch Digestive system of back adding, the ratio of potato starch and Digestive system is 1: 2～5, adopt tap water to supply when Digestive system is not enough, after mixing, add high temperature resistant α-Dian Fenmei, the α-Dian Fenmei addition is 6～15U/g starch, and post-heating stirs, Heating temperature: 90～105 ℃, insulation liquefaction 50～120 minutes; Be cooled to 60～65 ℃;
(2), add saccharifying enzyme, the saccharifying enzyme addition is 80～150U/g starch, is 60～65 ℃ of insulation saccharification 0.5～1.5hr down in temperature, saccharification is cooled to 28～35 ℃ after finishing;
(3), insert the distillery yeast that spreads cultivation of 8～10%V/V, constant temperature culture fermentation 40～72hr hr, the ethanol concn in the maturing fermentation liquid is 8.0～15%v/v, obtains finished product alcohol through distillation;
(4), the useless mash of distillation got after the above-mentioned distillation is cooled to 40～70 ℃, sends into anaerobic fermentation tank, the constant temperature anaerobically fermenting produced biogas in 10～15 days; The biogas supply boiler that acts as a fuel; Anaerobic fermented liquid obtains Digestive system and active sludge through solid-liquid separation; Digestive system loops back the next batch fermentation, constitutes annular collar, an infinite loop successively.
2, according to claim 1 is the alcohol annular production technique of main raw material with the potato class, it is characterized in that described potato starch raw material can adopt Ipomoea batatas, cassava.
3, according to claim 1 is the alcohol annular production technique of main raw material with the potato class, and the pH value that it is characterized in that described Digestive system is 6.0～8.0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100976230A CN100478445C (en) | 2006-11-10 | 2006-11-10 | Circulation production process for alcohol with potatoes as main materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100976230A CN100478445C (en) | 2006-11-10 | 2006-11-10 | Circulation production process for alcohol with potatoes as main materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1966695A true CN1966695A (en) | 2007-05-23 |
| CN100478445C CN100478445C (en) | 2009-04-15 |
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ID=38075677
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100976230A Active CN100478445C (en) | 2006-11-10 | 2006-11-10 | Circulation production process for alcohol with potatoes as main materials |
Country Status (1)
| Country | Link |
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| CN (1) | CN100478445C (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1930404A1 (en) * | 2006-12-07 | 2008-06-11 | Organic Waste Systems, Naamloze Vennootschap | Method and device for the anaerobic fermentation of organic material |
| CN101974567A (en) * | 2010-09-20 | 2011-02-16 | 江南大学 | Method for ecologically producing alcohol by taking tuberous crop as raw material |
| CN101676398B (en) * | 2008-09-19 | 2011-11-30 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN101676397B (en) * | 2008-09-19 | 2011-12-14 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN102311977A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Method for producing ethanol by using cassava residues |
| CN101586125B (en) * | 2008-05-23 | 2012-06-27 | 中粮集团有限公司 | Method for preparing ethanol from yam raw materials |
| CN101676394B (en) * | 2008-09-19 | 2012-07-04 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN102703516A (en) * | 2012-06-08 | 2012-10-03 | 广西平果凯特生物化工有限公司 | Alcohol cycle production technology by taking cassava and molasses as raw materials |
| CN102994567A (en) * | 2012-11-23 | 2013-03-27 | 吴江永祥酒精制造有限公司 | Coupled ethanol-methane dual thick mash fermentation process used for cassava raw material mash rough filtrate |
| CN103243123A (en) * | 2013-05-14 | 2013-08-14 | 江南大学 | Novel recycling technology for high-value conversion of tubers vinasse |
| CN104531777A (en) * | 2014-11-11 | 2015-04-22 | 广西武鸣县安宁淀粉有限责任公司 | Acid-free fermentation method for producing ethyl alcohol with fresh cassava full pulp as raw materials |
| CN106591379A (en) * | 2016-12-02 | 2017-04-26 | 江南大学 | Alcohol production method based on comprehensive utilization of waste water |
| CN107604007A (en) * | 2017-07-24 | 2018-01-19 | 江苏联海生物科技有限公司 | A kind of method that organic fertilizer is produced using cassava as raw material |
-
2006
- 2006-11-10 CN CNB2006100976230A patent/CN100478445C/en active Active
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1930404A1 (en) * | 2006-12-07 | 2008-06-11 | Organic Waste Systems, Naamloze Vennootschap | Method and device for the anaerobic fermentation of organic material |
| CN101200693B (en) * | 2006-12-07 | 2011-04-20 | 有机废物系统有限公司 | Method and device for the anaerobic fermentation of organic material |
| CN101586125B (en) * | 2008-05-23 | 2012-06-27 | 中粮集团有限公司 | Method for preparing ethanol from yam raw materials |
| CN101676398B (en) * | 2008-09-19 | 2011-11-30 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN101676397B (en) * | 2008-09-19 | 2011-12-14 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN101676394B (en) * | 2008-09-19 | 2012-07-04 | 中粮集团有限公司 | Method for preparing alcohol by utilizing potato materials |
| CN102311977A (en) * | 2010-07-07 | 2012-01-11 | 中国石油化工股份有限公司 | Method for producing ethanol by using cassava residues |
| CN101974567A (en) * | 2010-09-20 | 2011-02-16 | 江南大学 | Method for ecologically producing alcohol by taking tuberous crop as raw material |
| CN102703516A (en) * | 2012-06-08 | 2012-10-03 | 广西平果凯特生物化工有限公司 | Alcohol cycle production technology by taking cassava and molasses as raw materials |
| CN102994567A (en) * | 2012-11-23 | 2013-03-27 | 吴江永祥酒精制造有限公司 | Coupled ethanol-methane dual thick mash fermentation process used for cassava raw material mash rough filtrate |
| CN103243123A (en) * | 2013-05-14 | 2013-08-14 | 江南大学 | Novel recycling technology for high-value conversion of tubers vinasse |
| CN103243123B (en) * | 2013-05-14 | 2015-12-09 | 江南大学 | A kind of high level transforms the New Cycle technique of potato vinasse |
| CN104531777A (en) * | 2014-11-11 | 2015-04-22 | 广西武鸣县安宁淀粉有限责任公司 | Acid-free fermentation method for producing ethyl alcohol with fresh cassava full pulp as raw materials |
| CN106591379A (en) * | 2016-12-02 | 2017-04-26 | 江南大学 | Alcohol production method based on comprehensive utilization of waste water |
| CN106591379B (en) * | 2016-12-02 | 2020-08-04 | 江南大学 | Alcohol production method based on comprehensive utilization of wastewater |
| CN107604007A (en) * | 2017-07-24 | 2018-01-19 | 江苏联海生物科技有限公司 | A kind of method that organic fertilizer is produced using cassava as raw material |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100478445C (en) | 2009-04-15 |
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Application publication date: 20070523 Assignee: Guangxi Pingguo Kate Biological Chemical Co.,Ltd. Assignor: Jiangnan University Contract record no.: 2012320010163 Denomination of invention: Circulation production process for alcohol with potatoes as main materials Granted publication date: 20090415 License type: Common License Record date: 20120806 |
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Application publication date: 20070523 Assignee: Guangxi Pingguo Kate Biological Chemical Co.,Ltd. Assignor: Jiangnan University Contract record no.: 2012320010163 Denomination of invention: Circulation production process for alcohol with potatoes as main materials Granted publication date: 20090415 License type: Common License Record date: 20120806 |
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Application publication date: 20070523 Assignee: Jiangsu Jin Maoyuan Biological Chemical Co., Ltd. Assignor: Jiangnan University Contract record no.: 2015320010145 Denomination of invention: Circulation production process for alcohol with potatoes as main materials Granted publication date: 20090415 License type: Common License Record date: 20151008 |
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| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: Liangxi District Food Science and Technology Park, 7th floor, South Building, 898 Tongsha Road, Liangxi District, Wuxi City, Jiangsu Province Patentee after: Jiangnan University Address before: No. 1800 road 214122 Jiangsu Lihu Binhu District City of Wuxi Province Patentee before: Jiangnan University |