CN203999586U - Novel cassava alcohol production device - Google Patents
Novel cassava alcohol production device Download PDFInfo
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- CN203999586U CN203999586U CN201420452366.8U CN201420452366U CN203999586U CN 203999586 U CN203999586 U CN 203999586U CN 201420452366 U CN201420452366 U CN 201420452366U CN 203999586 U CN203999586 U CN 203999586U
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Abstract
The utility model discloses a kind of Novel cassava Alcohol Production device, this device belongs to Alcohol Production mechanical field; Comprise: vibratory feeder, slimer, permanent magnetic pulley, steamer, brew kettle, fermentor tank, topping still, rectifying tower; It is characterized in that: between vibratory feeder and slimer, be provided with the first transfer roller, between slimer and permanent magnetic pulley, be provided with second conveyor, between permanent magnetic pulley and steamer, be provided with the 3rd transfer roller, between steamer and brew kettle, be provided with the first shurry pump and pipeline, between brew kettle and fermentor tank, be provided with the second shurry pump and pipeline, between fermentor tank and topping still, be provided with the 3rd shurry pump and pipeline, between topping still and rectifying tower, be provided with the first impeller pump and pipeline, rectifying tower is provided with acetaldehyde, ethyl acetate outlet, the outlet of fine work alcohol, potato spirit outlet.
Description
Technical field
The utility model belongs to Alcohol Production mechanical field, relates in particular to a kind of Novel cassava Alcohol Production device.
Background technology
Alcohol claims again ethanol, is a kind of inflammable, volatile colourless transparent liquid under normal temperature, normal pressure, and its aqueous solution has special, pleasant fragrance, and slightly with irritating, boiling point: 78.4 ℃.Having many uses of alcohol, can be used to manufacture acetic acid, beverage, essence, dyestuff, fuel etc., and the alcohol that in medical treatment, also conventional volume fraction is 70%-75% is made sterilizing agent.Alcohol product can be divided into potato alcohol, corn alcohol, molasses-spirit, biomass alcohol etc. according to raw materials for production difference, and alcohol product is divided into again superfine alcohol, high grade edible spirit, universal alcohol, industrial spirit according to quality difference.In recent years, along with grain understanding of importance is constantly strengthened, the non-grain cassava alcohol output market share expands year by year, cassava is a kind of perennial plant, is shrub shape, and root is slightly grown, abound with the ground such as Guangdong in south China, Guangxi, Fujian, Taiwan, the external main place of production is Thailand, Vietnam.The main chemical compositions of tapioca root is starch, and other compositions are as all less in protein, fatty equal size, and its quality can be differentiated from appearance color, take white blocks, sheet cassava as good, but price is relatively high, and white powdery takes second place; From the place of production, Thailand cassava is better, and Thailand WHITE powdery cassava skin is thin, moisture is few, color is pure white, starch content is high, and reasonable price is more satisfactory ethanol production materials.
Produce alcohol and also need following raw materials according, 1. amylase: referring to can hydrolyzed starch, the enzyme of the O-glucose key in glycogen and relevant polysaccharide, amylase has multiple, and what comprise that α-amylase, beta-amylase, gamma amylase (glucoamylase), the present invention used is liquid α-amylase; 2. saccharifying enzyme: claim again glucoamylase, it can produce glucose from non reducing end hydrolysis a-1.4 glucoside bond starch, also can slowly be hydrolyzed a-1.6 glucoside bond, is converted into glucose, also can be hydrolyzed dextrin, the non-reduced end of glycogen discharges β-D-Glucose simultaneously; 3. dry yeast; 4. saccharifying agent.
Summary of the invention
The problem that the utility model mainly solves is to provide a kind of new device of cassava as raw material production alcohol of take, it is raw material that this device be take cassava, amylase, saccharifying enzyme, distiller's yeast, saccharifying agent, take vibratory feeder, slimer, permanent magnetic pulley, steamer, brew kettle, fermentor tank, topping still, rectifying tower is equipment, after the pulverizing by cassava, boiling, saccharification, fermentation, distillation, makes finished product alcohol.
The technical solution adopted in the utility model is:
A Novel cassava Alcohol Production device, comprising: vibratory feeder 1, slimer 2, permanent magnetic pulley 3, steamer 4, brew kettle 5, fermentor tank 6, topping still 7, rectifying tower 8, it is characterized in that: vibratory feeder 1 is provided with cassava import 9, impurity outlet 10, 2 of vibratory feeder 1 and slimers are provided with the first transfer roller 11, 3 of slimer 2 and permanent magnetic pulleys are provided with second conveyor 12, permanent magnetic pulley 3 is provided with impurity outlet 13, 4, permanent magnetic pulley 3 and steamer are provided with the 3rd transfer roller 14, steamer 4 is provided with water, amylase, saccharifying enzyme import 15, 5 of steamer 4 and brew kettles are provided with the first shurry pump and pipeline 16, brew kettle 5 is provided with saccharifying agent import 17, 6 of brew kettle 5 and fermentor tanks are provided with the second shurry pump and pipeline 18, fermentor tank 6 is provided with distiller's yeast import 19, 7 of fermentor tank 6 and topping stills are provided with the 3rd shurry pump and pipeline 20, topping still 7 is provided with vinasse outlet 21, 8, topping still 7 and rectifying tower are provided with the first impeller pump and pipeline 22, rectifying tower 8 is provided with acetaldehyde, ethyl acetate outlet 23, fine work alcohol outlet 24, potato spirit outlet 25.
Further technical scheme of the present utility model is:
Described vibratory feeder is GZ2F 20t/h level.
Described slimer is JFS-112-63 type.
Described permanent magnetic pulley specification is Ф 550.
Described steamer volume is 45 cubic metres.
Described brew kettle volume is 100 cubic metres.
Described fermentor tank volume is 2000 cubic metres.
Described topping still JSP2200X25 plate.
Described rectifying tower JFB2000X75 plate.
First, second, third described transfer roller is scraper conveyor, and first, second, third shurry pump, the first impeller pump are stainless steel, and corresponding pipeline is polyethylene material.
The beneficial effects of the utility model are: a kind of Novel cassava Alcohol Production device is provided, the advantage of this device is: use general-purpose equipment combination, rational in infrastructure, technique simple, without high-temperature high-voltage reaction, environmental protection, that finished product goes out rate is high, product can be according to customer need, produce the alcohol of a plurality of kinds, of many uses.
Accompanying drawing explanation:
If Fig. 1 is structure of the present utility model and process flow diagram.
Embodiment
Below in conjunction with accompanying drawing, further illustrate the particular content that uses this new device to produce alcohol most preferred embodiment:
1, quantitative cassava is sent into vibratory feeder 1 by the cassava import 9 being arranged on vibratory feeder 1, mode by vibrations is removed silt, stone, silt, stone is discharged by the impurity outlet 10 being arranged on vibratory feeder 1, cassava is sent into slimer 2 by being arranged at the first transfer roller 11 of 2 of vibratory feeder 1 and slimers, pulverize as the particle of 1.2-1.5mm, by being arranged at the second conveyor 12 of 3 of slimer 2 and permanent magnetic pulleys, send into permanent magnetic pulley 3 immediately, when by permanent magnetic pulley 3, the particle of iron content is discharged by the impurity outlet 13 being arranged on permanent magnetic pulley 3 after being adsorbed, pure Tapioca Starch is sent into steamer 4 by being arranged at the 3rd transfer roller 14 of 4, permanent magnetic pulley 3 and steamer.
2, the volume of steamer 4 is 45 cubic metres, in steamer 4 in the ratio 1:7-8 of Tapioca Starch and water, amylase is pressed the 0.045-0.055% of Tapioca Starch weight, the addition of saccharifying enzyme by the amount of every pot of 0.74-0.76kg by being arranged at the water on steamer 4, amylase, steamer 4 is sent in saccharifying enzyme import 15, by the material even blend in steamer 4, after cassava raw material water suction at 120-125 ℃ of temperature boiling 90-100 minute, plant tissue and cell are thoroughly broken, make starch by particle, be become the paste liquid of dissolved state, then be cooled to the 55-70 ℃ of paste liquid obtaining and be called boiling wine with dregs.
3, boiling wine with dregs is sent into brew kettle 5 by being arranged at the first shurry pump and the pipeline 16 of 5 of steamer 4 and brew kettles, the temperature of boiling wine with dregs is down to 55 ℃-62 ℃, by being arranged at saccharifying agent import 17 on brew kettle 5, adding and account for even blend after the saccharifying agent that boiling wine with dregs total amount is 1%, saccharification 30-40 minute at the temperature of 58 ℃-60 ℃, obtains converted mash after saccharification finishes.
4, converted mash is sent into fermentor tank 6 by being arranged at the second shurry pump and the pipeline 18 of 6 of brew kettle 5 and fermentor tanks, by being arranged at distiller's yeast import 19 on fermentor tank 6, to fermentor tank 6, add middle interpolation to account for after the distiller's yeast of converted mash 15% to carry out primary fermentation after even blend, control temperature is 26-28 ℃, and the time is 6-8h; Leavening temperature is controlled as 30-34 ℃, and fermentation time is 10-14h; Again temperature is adjusted to 30-32 ℃, maintains 60-72h secondary fermentation and finish, fermentation makes converted mash under saccharomycetic effect, changes ripe wine with dregs into, and the composition of ripe wine with dregs is alcohol and carbonic acid gas and a small amount of impurity.
5, ripe wine with dregs is sent into topping still 7 and slightly heated up in a steamer by being arranged at the 3rd shurry pump of 7 of fermentor tank 6 and topping stills and pipeline 20, the waste liquid obtaining after distillation is called vinasse, its main component is water and a small amount of involatile substance, by the vinasse outlet 21 being arranged on topping still 7, discharges; The liquid obtaining is crude alcohol, crude alcohol is sent into rectifying tower 8 by being arranged at the first impeller pump and the pipeline 22 of 8, topping still 7 and rectifying tower, utilize the different principle of different substances boiling point, first distillate the materials such as acetaldehyde, ethyl acetate, distillate pure alcohol thereupon, distillate again fusel wet goods, by acetaldehyde, ethyl acetate, pure alcohol, potato spirit is respectively by being arranged at acetaldehyde, the ethyl acetate outlet 23 on rectifying tower, fine work alcohol outlet 24, potato spirit outlet 25
Discharge and reclaim.
Certainly, the utility model also has other embodiment, in the improvement of not leaving any technology, principle and the technique done under spiritual background of the present utility model, within all dropping on protection domain of the present utility model.
Claims (10)
1. a Novel cassava Alcohol Production device, comprising: vibratory feeder (1), slimer (2), permanent magnetic pulley (3), steamer (4), brew kettle (5), fermentor tank (6), topping still (7), rectifying tower (8), it is characterized in that: vibratory feeder (1) is provided with cassava import (9), impurity outlet (10), between vibratory feeder (1) and slimer (2), be provided with the first transfer roller (11), between slimer (2) and permanent magnetic pulley (3), be provided with second conveyor (12), permanent magnetic pulley (3) is provided with impurity outlet (13), between permanent magnetic pulley (3) and steamer (4), be provided with the 3rd transfer roller (14), steamer () 4 is provided with water, amylase, saccharifying enzyme import (15), between steamer (4) and brew kettle (5), be provided with the first shurry pump and pipeline (16), ) brew kettle (5) is provided with saccharifying agent import (17), between brew kettle (5) and fermentor tank (6), be provided with the second shurry pump and pipeline (18), fermentor tank (6) is provided with distiller's yeast import (19), between fermentor tank (6) and topping still (7), be provided with the 3rd shurry pump and pipeline (20), topping still (7) is provided with vinasse outlets (21), between topping still (7) and rectifying tower (8), be provided with the first impeller pump and pipeline (22), rectifying tower (8) is provided with acetaldehyde, ethyl acetate outlet (23), fine work alcohol outlet (24), potato spirit outlet (25).
2. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described vibratory feeder is GZ2F 20t/h level.
3. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described slimer is JFS-112-63 type.
4. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described permanent magnetic pulley specification is Ф 550.
5. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described steamer volume is 45 cubic metres.
6. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described brew kettle volume is 100 cubic metres.
7. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described fermentor tank volume is 2000 cubic metres.
8. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described topping still JSP2200X25 plate.
9. a kind of Novel cassava Alcohol Production device according to claim 1, is characterized in that: described rectifying tower JFB2000X75 plate.
10. a kind of Novel cassava Alcohol Production device according to claim 1, it is characterized in that: first, second, third described transfer roller is scraper conveyor, first, second, third shurry pump, the first impeller pump are stainless steel, and corresponding pipeline is polyethylene material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420452366.8U CN203999586U (en) | 2014-08-12 | 2014-08-12 | Novel cassava alcohol production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420452366.8U CN203999586U (en) | 2014-08-12 | 2014-08-12 | Novel cassava alcohol production device |
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| Publication Number | Publication Date |
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| CN203999586U true CN203999586U (en) | 2014-12-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420452366.8U Expired - Fee Related CN203999586U (en) | 2014-08-12 | 2014-08-12 | Novel cassava alcohol production device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110607327A (en) * | 2019-10-17 | 2019-12-24 | 安徽省金裕皖酒业有限公司 | Preparation method of rice wine vinasse extract |
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2014
- 2014-08-12 CN CN201420452366.8U patent/CN203999586U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110607327A (en) * | 2019-10-17 | 2019-12-24 | 安徽省金裕皖酒业有限公司 | Preparation method of rice wine vinasse extract |
| CN110607327B (en) * | 2019-10-17 | 2021-04-20 | 安徽省金裕皖酒业有限公司 | Preparation method of rice wine vinasse extract |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20141210 Termination date: 20200812 |