CN101289676B - Process for producing alcohol form queensland arrowroot - Google Patents
Process for producing alcohol form queensland arrowroot Download PDFInfo
- Publication number
- CN101289676B CN101289676B CN200810070515A CN200810070515A CN101289676B CN 101289676 B CN101289676 B CN 101289676B CN 200810070515 A CN200810070515 A CN 200810070515A CN 200810070515 A CN200810070515 A CN 200810070515A CN 101289676 B CN101289676 B CN 101289676B
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- CN
- China
- Prior art keywords
- alcohol
- ratio
- thorough mixing
- hour
- edible canna
- 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.)
- Expired - Fee Related
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- 235000005273 Canna coccinea Nutrition 0.000 title claims abstract description 34
- 244000292211 Canna coccinea Species 0.000 title claims description 30
- 125000003158 alcohol group Chemical group 0.000 title claims description 8
- 238000000034 method Methods 0.000 title abstract description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000000855 fermentation Methods 0.000 claims abstract description 25
- 230000004151 fermentation Effects 0.000 claims abstract description 25
- 238000002156 mixing Methods 0.000 claims abstract description 25
- 238000004821 distillation Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000003756 stirring Methods 0.000 claims abstract description 12
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 12
- 229930006000 Sucrose Natural products 0.000 claims description 12
- 238000004140 cleaning Methods 0.000 claims description 12
- 238000012856 packing Methods 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000013467 fragmentation Methods 0.000 claims description 8
- 238000006062 fragmentation reaction Methods 0.000 claims description 8
- 241000234588 Canna indica Species 0.000 abstract 4
- 239000004382 Amylase Substances 0.000 abstract 1
- 102000013142 Amylases Human genes 0.000 abstract 1
- 108010065511 Amylases Proteins 0.000 abstract 1
- 238000006424 Flood reaction Methods 0.000 abstract 1
- 235000019418 amylase Nutrition 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000005086 pumping Methods 0.000 abstract 1
- 239000002028 Biomass Substances 0.000 description 2
- 241000234586 Cannaceae Species 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 241000684239 Canna x generalis Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- 244000297179 Syringa vulgaris Species 0.000 description 1
- 235000004338 Syringa vulgaris Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
- C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
- C12P7/06—Ethanol, i.e. non-beverage
-
- 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
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- General Chemical & Material Sciences (AREA)
- Biotechnology (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The invention relates to a method of producing alcohol, in particular to a method of using edible canna to produce alcohol. The method comprises the steps of crushing clean fresh edible canna with a crusher, mixing the crushed raw material with clean water sufficiently at the ratio of 100:20-25 and with sugar at the ratio of 100:0.5-1 sufficiently, adding amylase at the ratio of 100:3-5, then stirring for 2 to 5 hours at a temperature of between 15 and 30 DEG C for saccharification, and then putting the mixture in a fermentation device to ferment for 65 to 85 hours continuously, pumping sterile air to fermented mash liquor, adding the fermented mash liquid into an alcohol distillation device, and distilling at a temperature of between 90 and 110 DEG C continuously to obtain finished alcohol. The method can take full advantage of the edible canna and reduce grain consumption. The edible canna can replace grain to be used as the raw material to process the alcohol depending on the advantages of vigorous growth potential, strong adaptability, more drought-resistance, floods resistance, low planting cost and high yield, thereby the cost which is used to produce the alcohol is low but the raw material to produce the alcohol is very rich.
Description
Invention field
The present invention relates to alcohol producing process, be specifically related to a kind of method of producing alcohol form queensland arrowroot.
Background technology
Edible canna (edible canna), the cultivar during Cannaceae (Cannaceae) Canna generalis Bailey belongs to, per nnial herb.Formal name used at school Canna edu1is Ker., another name any of several broadleaf plants lotus root, achira, opinion can stir-fry and eat, pickled, also can process system starch and bean vermicelli.Starch-containing 12-14g in every 100g stem tuber.Capable of using as feed and the paper making raw material of cauline leaf, edible canna also are ornamental plants, and there is fragmentary plantation in provinces such as China Fujian, Jiangxi, Zhejiang, and stem is upright, sturdy, lilac red, elliptic leaf shape, long 40-50cm, wide 20-30cm, green, back purple.Raceme, the premium look, stem tuber has joint, the Beijing opera look; Meat white, about 30 of tuberizations are managed to make do in every strain, the rhizome edible, people are only boiling with the primary method and are eating; Nutritive value can not fully be developed, and present one jin of wine needs about five jin grain through processing approximately, has wasted a large amount of grains, has aggravated crisis in food; Existing biomass to alcohol conversion process of while, production cost is high, is that the biomass to alcohol conversion process of raw material also is difficult to realize industrialized production with the edible canna.
Summary of the invention
The object of the invention provides a kind of method of producing alcohol form queensland arrowroot; Make full use of the value of edible canna, reduce the consumption of grain, this method overcomes that not have edible canna be that raw material production alcohol technology is difficult to industrialized shortcoming at present; And greatly reduce the production cost of alcohol and abundant raw material.
For realizing the foregoing invention purpose, the method for producing alcohol form queensland arrowroot: the bright edible canna of getting earlier after cleaning is used crusher in crushing, and the raw material after the fragmentation is in 100: the ratio of 20-25 and clear water thorough mixing; With in 100: the ratio of 0.5-1 and white sugar thorough mixing; By 100: 3-5 adds glycase, then mixes at 15 ℃ to 30 ℃ and stirs 2-5 hour, carries out saccharification; Again in 100: the ratio of 3-5 adds the glycase starter and mixes stirring; The fermentation equipment of then packing into was continuously fermented 65-85 hour at 20 ℃ to 30 ℃, in fermentation liquid, fed sterile air again, with the mash adding alcohol distillation equipment of fermenting-ripening; 90 ℃ to 110 ℃ following continuous still batterys, can get finished product alcohol.
Further can adopt ripe, it produces the method for alcohol: the bright edible canna of getting after cleaning is used crusher in crushing, and then boiling is ripe; After boiling, be cooled to again between 15 ℃ to 35 ℃, then respectively in 100: the ratio of 20-25 and clear water thorough mixing; With in 100: the ratio of 0.5-1 and white sugar thorough mixing, in 100: the ratio of 2-3 adds glycase, mixes at 15 ℃ to 30 ℃ and stirs 2-5 hour; The fermentation equipment of then packing into was continuously fermented 24-50 hour at 20 ℃ to 30 ℃, in fermentation liquid, fed sterile air again, with the mash adding alcohol distillation equipment of fermenting-ripening; 90 ℃ to 110 ℃ following continuous still batterys, can get finished product alcohol.
Further can adopt dry plate, it produces the method for alcohol: the bright edible canna fragmentation of getting after cleaning is dried, in 100: the ratio of 40-50 and clear water thorough mixing; Again in 100: the ratio of 1-2 and white sugar thorough mixing; In 100: the ratio of 6-10 adds glycase, mixes at 15 ℃ to 30 ℃ and stirs 5-8 hour, and the fermentation equipment of then packing into was continuously fermented 60-85 hour at 20 ℃ to 30 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ to 110 ℃ continuous still batterys.
This method can make full use of the value of edible canna, reduces the consumption of grain, because edible canna growth potential is vigorous, flexibility is strong; More drought-enduring, be not afraid of waterlogging, planting cost is low, and output is high; Instead grain is as the raw material of processing alcohol, and the production cost of alcohol is low, and abundant raw material.
Embodiment
Embodiment 1
The bright edible canna of getting earlier after cleaning is used crusher in crushing; Raw material after the fragmentation is in 100: the ratio of 20-25 and clear water thorough mixing and in 100: the ratio of 0.5-1 and white sugar thorough mixing, and in 100: the ratio of 3-5 adds glycase; Then mix and stirred 5 hours at 15 ℃; Carry out saccharification, the fermentation equipment of then packing into was continuously fermented 85 hours at 20 ℃, in fermentation liquid, fed sterile air again.The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 100 ℃ of following continuous still batterys.
Embodiment 2
The bright edible canna of getting earlier after cleaning is used crusher in crushing, and the raw material after the fragmentation is in 100: the ratio of 20-25 and clear water thorough mixing and in 100: the ratio of 0.5-1 and white sugar thorough mixing; In 100: the ratio of 3-5 adds glycase; Then mix at 30 ℃ and stirred 2 hours, carry out saccharification, the fermentation equipment of then packing into was continuously fermented 65 hours at 30 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ of continuous still batterys.
Embodiment 3
Further can adopt ripe: the bright edible canna of then getting after cleaning is used crusher in crushing, and boiling then is ripe, after boiling; Be cooled to 35 ℃ again, then respectively in 100: the ratio of 20-25 and clear water thorough mixing and: the ratio of 0.5-1 and white sugar thorough mixing in 100; By 100: 2-3 adds glycase; Mix stirring 2 hours at 30 ℃, the fermentation equipment of then packing into was continuously fermented 24 hours at 30 ℃, in fermentation liquid, fed sterile air again.The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ of continuous still batterys.
Embodiment 4
Further can adopt ripe: the bright edible canna of then getting after cleaning is used crusher in crushing, and boiling then is ripe, after boiling; Be cooled to again between 15 ℃ to 35 ℃, then respectively in 100: the ratio of 20-25 and clear water thorough mixing and: the ratio of 0.5-1 and white sugar thorough mixing in 100; By 100: 2-3 adds glycase; Mix stirring 2-5 hour at 15 ℃ to 30 ℃, the fermentation equipment of then packing into was continuously fermented 24-50 hour at 20 ℃ to 30 ℃, in fermentation liquid, fed sterile air again.The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ to 110 ℃ continuous still batterys.
Embodiment 5
Further can adopt dry plate: the bright edible canna fragmentation of then getting after cleaning is dried, in 100: and the ratio of 40-50 and clear water thorough mixing, again in 100: the ratio of 1-2 and white sugar thorough mixing; By 100: 6-10 adds glycase, mixes at 30 ℃ and stirs 5 hours, and the fermentation equipment of then packing into was being continuously fermented 85 hours at 20 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 100 ℃ of continuous still batterys.
Embodiment 6
Further can adopt dry plate: the bright edible canna fragmentation of then getting after cleaning is dried, in 100: and the ratio of 40-50 and clear water thorough mixing, again in 100: the ratio of 1-2 and white sugar thorough mixing; By 100: 6-10 adds glycase, mixes at 15 ℃ and stirs 5-8 hour, and the fermentation equipment of then packing into was continuously fermented 60 hours at 30 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 110 ℃ of continuous still batterys.
Claims (3)
1. the method for producing alcohol form queensland arrowroot is characterized in that: the bright edible canna of getting earlier after cleaning is used crusher in crushing, and the raw material after the fragmentation is in 100: the ratio of 20-25 and clear water thorough mixing; With in 100: the ratio of 0.5-1 and white sugar thorough mixing, by 100: 3-5 adds glycase, then mixes stirrings 2-5 hour at 15 ℃ to 30 ℃; Carry out saccharification; The fermentation equipment of then packing into was continuously fermented 65-85 hour at normal temperatures, in fermentation liquid, fed sterile air again, with the mash adding alcohol distillation equipment of fermenting-ripening; 90 ℃ to 110 ℃ following continuous still batterys, can get finished product alcohol.
2. the method for producing alcohol form queensland arrowroot according to claim 1 is characterized in that: adopt ripe: the bright edible canna of then getting after cleaning is used crusher in crushing, and then boiling is ripe; After boiling, be cooled to again between 15 ℃ to 35 ℃, then respectively in 100: the ratio of 20-25 and clear water thorough mixing; With in 100: the ratio of 0.5-1 and white sugar thorough mixing; By 100: 2-3 adds glycase, mixes at 15 ℃ to 30 ℃ and stirs 2-5 hour, and the fermentation equipment of then packing into was continuously fermented 24-50 hour at 20 ℃ to 30 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ to 110 ℃ continuous still batterys.
3. the method for producing alcohol form queensland arrowroot according to claim 1 is characterized in that: adopt dry plate: the bright edible canna fragmentation of then getting after cleaning is dried, in 100: the ratio of 40-50 and clear water thorough mixing; Again in 100: the ratio of 1-2 and white sugar thorough mixing; By 100: 6-10 adds glycase, mixes at 15 ℃ to 30 ℃ and stirs 5-8 hour, and the fermentation equipment of then packing into was being continuously fermented 60-85 hour at 20 ℃ to 30 ℃; In fermentation liquid, feed sterile air again; The mash of fermenting-ripening is added alcohol distillation equipment,, can get finished product alcohol 90 ℃ to 110 ℃ following continuous still batterys.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810070515A CN101289676B (en) | 2008-01-22 | 2008-01-22 | Process for producing alcohol form queensland arrowroot |
| PCT/CN2009/070184 WO2009094927A1 (en) | 2008-01-22 | 2009-01-16 | A method for producing alcohol by using of edible canna |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200810070515A CN101289676B (en) | 2008-01-22 | 2008-01-22 | Process for producing alcohol form queensland arrowroot |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101289676A CN101289676A (en) | 2008-10-22 |
| CN101289676B true CN101289676B (en) | 2012-10-03 |
Family
ID=40034121
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200810070515A Expired - Fee Related CN101289676B (en) | 2008-01-22 | 2008-01-22 | Process for producing alcohol form queensland arrowroot |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN101289676B (en) |
| WO (1) | WO2009094927A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101289676B (en) * | 2008-01-22 | 2012-10-03 | 泉州市博大纳米科技有限公司 | Process for producing alcohol form queensland arrowroot |
| CN104911219A (en) * | 2015-05-14 | 2015-09-16 | 陈中志 | Method for producing alcohol by utilization of canna edulis ker and plant straws |
| CN116396821A (en) * | 2023-02-16 | 2023-07-07 | 四川省食品发酵工业研究设计院有限公司 | Rose-flavored fermented wine and brewing process thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1038305A (en) * | 1988-06-04 | 1989-12-27 | 内江市政协咨询服务部 | The novel method of making alcohol from fresh musa paradisiaca |
| CN1696295A (en) * | 2005-05-26 | 2005-11-16 | 贵州大学 | Method for producing alcohol by using dry plate of banana dasheen as raw material |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1083530A (en) * | 1992-11-24 | 1994-03-09 | 沈阳市北陵制酒厂 | A kind of method of low temperature non-steaming and non-boiling producing alcohol |
| CN1780560B (en) * | 2003-03-10 | 2011-05-25 | 布罗因联合公司 | Method for producing ethanol using raw starch |
| ZA200608032B (en) * | 2004-03-10 | 2008-07-30 | Broin And Associates Inc | Methods and systems for producing ethanol using raw starch and fractionation |
| CN101289676B (en) * | 2008-01-22 | 2012-10-03 | 泉州市博大纳米科技有限公司 | Process for producing alcohol form queensland arrowroot |
-
2008
- 2008-01-22 CN CN200810070515A patent/CN101289676B/en not_active Expired - Fee Related
-
2009
- 2009-01-16 WO PCT/CN2009/070184 patent/WO2009094927A1/en active Application Filing
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1038305A (en) * | 1988-06-04 | 1989-12-27 | 内江市政协咨询服务部 | The novel method of making alcohol from fresh musa paradisiaca |
| CN1696295A (en) * | 2005-05-26 | 2005-11-16 | 贵州大学 | Method for producing alcohol by using dry plate of banana dasheen as raw material |
Non-Patent Citations (3)
| Title |
|---|
| 吴天祥等.芭蕉芋原料酒精固态发酵工艺条件的初探.《酿酒》.2003,第30卷(第2期),71-73. * |
| 朱作华等.芭蕉芋的性质及其淀粉的工业应用研究.《生物加工过程》.2005,第3卷(第4期),66-70. * |
| 陈叶福等.芭蕉芋糖化液酒精发酵条件研究.《酿酒》.2002,第29卷(第6期),63-65. * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101289676A (en) | 2008-10-22 |
| WO2009094927A1 (en) | 2009-08-06 |
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Effective date of registration: 20150818 Address after: 362600, Gaoping County, Fujian City, Yongchun province Quanzhou Town, Lake Village 3 Patentee after: Yongchun Jiulong Valley eco agriculture cooperatives Address before: 362000 Fujian province Quanzhou detai economic and Technological Development Zone, Road No. 51 Building 2 layer B business incubator base area Patentee before: QUANZHOU CITY BODA NANO SCIENCE & TECHNOLOGY CO., LTD. |
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Effective date of registration: 20170524 Address after: 362600, No. 67, Taoyuan village, Lake Yang Town, Yongchun County, Quanzhou, Fujian Patentee after: Permanent spring Fuxing Agricultural Technology Co Ltd Address before: 362600, Gaoping County, Fujian City, Yongchun province Quanzhou Town, Lake Village 3 Patentee before: Yongchun Jiulong Valley eco agriculture cooperatives |
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