CN105462806A - Alcohol production machinery device by using cassava as raw material - Google Patents
Alcohol production machinery device by using cassava as raw material Download PDFInfo
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- CN105462806A CN105462806A CN201410393784.9A CN201410393784A CN105462806A CN 105462806 A CN105462806 A CN 105462806A CN 201410393784 A CN201410393784 A CN 201410393784A CN 105462806 A CN105462806 A CN 105462806A
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Abstract
The invention discloses an alcohol production machinery device by using cassava as the raw material, and belongs to the field of alcohol production machinery. The device comprises a vibration feeder, a fine crushing machine, a permanent magnet rotary drum, a steaming pot, a saccharification pot, a fermentation tank, a coarse distillation tower and a fine distillation tower, and is characterized in that a first conveying machine is arranged between the vibration feeder and the fine crushing machine; a second conveying machine is arranged between the fine crushing machine and the permanent magnet rotary drum; a third conveying machine is arranged between the permanent magnet rotary drum and the steaming pot; a first slurry pump and a pipeline are arranged between the steaming pot and the saccharification pot; a second slurry pump and a pipeline are arranged between the saccharification pot and the fermentation tank; a third slurry pump and a pipeline are arranged between the fermentation tank and the coarse distillation tower; a first centrifugal pump and a pipeline are arranged between the coarse distillation tower and the fine distillation tower; and an acetaldehyde and ethyl acetate outlet, a high-quality alcohol outlet and a fusel oil outlet are arranged in the fine distillation tower.
Description
Technical field
The invention belongs to Alcohol Production mechanical field, particularly relating to a kind of take cassava as the mechanism of raw material production alcohol.
Background technology
Alcohol is also known as ethanol, and be a kind of inflammable, volatile colourless transparent liquid under normal temperature, normal pressure, its aqueous solution has special, pleasant fragrance, and slightly pungency, boiling point: 78.4 DEG C.Having many uses of alcohol, can be used to manufacture acetic acid, beverage, essence, dyestuff, fuel etc., and medically also conventional volume fraction is that sterilizing agent made by the alcohol of 70%-75%.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, constantly strengthen along with to grain understanding of importance, the non-grain cassava alcohol output market share expands year by year, cassava is a kind of perennial plant, and in shrub shape, root is thick and grow, abound with in the Guangdong of south China, Guangxi, Fujian, Taiwan and other places, 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, and be good with white blocks, sheet cassava, but price is relatively high, white powder 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, reasonable price, is more satisfactory ethanol production materials.
Produce alcohol and also need following raw materials according, 1. amylase: refer to energy hydrolyzed starch, glycogen and the enzyme about the O-glucose key in polysaccharide, amylase has multiple, comprises α-amylase, beta-amylase, gamma amylase (glucoamylase), the present invention use liquid α-amylase; 2. saccharifying enzyme: also known as glucoamylase, it can produce glucose starch from non reducing end hydrolysis a-1.4 glucoside bond, also can slowly be hydrolyzed a-1.6 glucoside bond, be converted into glucose, simultaneously also can hydrolyse dextrin, the non-reducing end release β-D-Glucose of glycogen; 3. dry yeast; 4. saccharifying agent.
Summary of the invention
It take cassava as the mechanism of raw material production alcohol that the problem that the present invention mainly solves is to provide a kind of, this device with cassava, amylase, saccharifying enzyme, distiller's yeast, saccharifying agent for raw material, with vibratory feeder, slimer, permanent magnetic pulley, steamer, brew kettle, fermentor tank, topping still, rectifying tower for equipment, by the pulverizing of cassava, boiling, saccharification, fermentation, distillation obtained finished product alcohol afterwards.
The technical solution used in the present invention is:
Take cassava as a mechanism for raw material production alcohol, 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, impurities outlet 10, the first transfer roller 11 is provided with between vibratory feeder 1 and slimer 2, second conveyor 12 is provided with between slimer 2 and permanent magnetic pulley 3, permanent magnetic pulley 3 is provided with impurities outlet 13, the 3rd transfer roller 14 is provided with between permanent magnetic pulley 3 and steamer 4, steamer 4 is provided with water, amylase, saccharifying enzyme import 15, the first shurry pump and pipeline 16 is provided with between steamer 4 and brew kettle 5, brew kettle 5 is provided with saccharifying agent import 17, the second shurry pump and pipeline 18 is provided with between brew kettle 5 and fermentor tank 6, fermentor tank 6 is provided with distiller's yeast import 19, the 3rd shurry pump and pipeline 20 is provided with between fermentor tank 6 and topping still 7, topping still 7 is provided with vinasse outlet 21, the first impeller pump and pipeline 22 is provided with between topping still 7 and rectifying tower 8, 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 invention is:
Described vibratory feeder is GZ2F20t/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 fermenter 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 invention has the beneficial effects as follows: providing a kind of take cassava as the mechanism of raw material production alcohol, the advantage of this device is: use that general-purpose equipment combination, rational in infrastructure, technique are simple, without high-temperature high-voltage reaction, environmental protection, that finished product goes out rate is high, product can according to customer need, produce the alcohol of multiple kind, of many uses.
Accompanying drawing illustrates:
If Fig. 1 is Structure and energy FB(flow block) of the present invention.
Embodiment
The particular content using this mechanism to produce alcohol most preferred embodiment is further illustrated below in conjunction with accompanying drawing:
1, quantitative cassava is sent into vibratory feeder 1 by the cassava import 9 be arranged on vibratory feeder 1, silt is removed by the mode of vibrations, stone, silt, stone is discharged by the impurities outlet 10 be arranged on vibratory feeder 1, cassava sends into slimer 2 by the first transfer roller 11 be arranged between vibratory feeder 1 and slimer 2, pulverize the particle for 1.2-1.5mm, permanent magnetic pulley 3 is sent into immediately by the second conveyor 12 be arranged between slimer 2 and permanent magnetic pulley 3, discharged by the impurities outlet 13 be arranged on permanent magnetic pulley 3 after the particle by iron content during permanent magnetic pulley 3 is adsorbed, pure Tapioca Starch sends into steamer 4 by the 3rd transfer roller 14 be arranged between permanent magnetic pulley 3 and steamer 4.
2, the volume of steamer 4 is 45 cubic metres, in the ratio 1:7-8 of Tapioca Starch and water in steamer 4, amylase presses 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, cassava materials water suction after at 120-125 DEG C of temperature boiling 90-100 minute, plant tissue and cell are thoroughly broken, starch is made to become the paste liquid of dissolved state by particle, then be cooled to the 55-70 DEG C of paste liquid obtained and be called boiling wine with dregs.
3, by boiling wine with dregs by being arranged at the first shurry pump between steamer 4 and brew kettle 5 and brew kettle 5 sent into by pipeline 16, the temperature of boiling wine with dregs is down to 55 DEG C-62 DEG C, added by the saccharifying agent import 17 be arranged on brew kettle 5 that to account for boiling wine with dregs total amount be even blend after the saccharifying agent of 1%, at the temperature of 58 DEG C-60 DEG C, saccharification 30-40 minute, obtains converted mash after saccharification terminates.
4, by converted mash by being arranged at the second shurry pump between brew kettle 5 and fermentor tank 6 and fermentor tank 6 sent into by pipeline 18, to add after middle interpolation accounts for the distiller's yeast of converted mash 15% to fermentor tank 6 and carry out primary fermentation by being arranged at distiller's yeast import 19 on fermentor tank 6 after even blend, control temperature is 26-28 DEG C, and the time is 6-8h; Control leavening temperature for 30-34 DEG C, fermentation time is 10-14h; Again temperature is adjusted to 30-32 DEG C, maintain 60-72h secondary fermentation and terminate, 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 slightly heat up in a steamer by being arranged at the 3rd shurry pump between fermentor tank 6 and topping still 7 and pipeline 20, the waste liquid obtained after distillation is called vinasse, its main component is water and a small amount of involatile substance, is discharged by the vinasse outlet 21 be arranged on topping still 7; The liquid obtained is crude alcohol, by crude alcohol by being arranged at the first impeller pump between topping still 7 and rectifying tower 8 and rectifying tower 8 sent into by pipeline 22, utilize the principle that different substances boiling point is different, first distillate the material such as acetaldehyde, ethyl acetate, distillate pure alcohol thereupon, distillate fusel wet goods again, by acetaldehyde, ethyl acetate, pure alcohol, potato spirit is respectively by the acetaldehyde be arranged on rectifying tower, ethyl acetate outlet 23, fine work alcohol outlet 24, potato spirit outlet 25
Discharge is reclaimed.
Certainly, the present invention also has other embodiment, not leaving the improvement of any technology, principle and the technique done under spiritual background of the present invention, all drops within protection scope of the present invention.
Claims (10)
1. be a mechanism for raw material production alcohol with cassava, comprise: 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), impurities outlet (10), the first transfer roller (11) is provided with between vibratory feeder (1) and slimer (2), second conveyor (12) is provided with between slimer (2) and permanent magnetic pulley (3), permanent magnetic pulley (3) is provided with impurities outlet (13), the 3rd transfer roller (14) is provided with between permanent magnetic pulley (3) and steamer (4), steamer () 4 is provided with water, amylase, saccharifying enzyme import (15), the first shurry pump and pipeline (16) is provided with between steamer (4) and brew kettle (5), ) brew kettle (5) is provided with saccharifying agent import (17), the second shurry pump and pipeline (18) is provided with between brew kettle (5) and fermentor tank (6), fermentor tank (6) is provided with distiller's yeast import (19), the 3rd shurry pump and pipeline (20) is provided with between fermentor tank (6) and topping still (7), topping still (7) is provided with vinasse outlet (21), the first impeller pump and pipeline (22) is provided with between topping still (7) and rectifying tower (8), rectifying tower (8) is provided with acetaldehyde, ethyl acetate outlet (23), fine work alcohol outlet (24), potato spirit outlet (25).
2. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described vibratory feeder is GZ2F20t/h level.
3. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described slimer is JFS-112-63 type.
4. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described permanent magnetic pulley specification is Ф 550.
5. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described steamer volume is 45 cubic metres.
6. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described brew kettle volume is 100 cubic metres.
7. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described fermenter volume is 2000 cubic metres.
8. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described topping still JSP2200X25 plate.
9. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, it is characterized in that: described rectifying tower JFB2000X75 plate.
10. according to claim 1 a kind of take cassava as the mechanism of raw material production alcohol, 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 |
|---|---|---|---|
| CN201410393784.9A CN105462806A (en) | 2014-08-12 | 2014-08-12 | Alcohol production machinery device by using cassava as raw material |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410393784.9A CN105462806A (en) | 2014-08-12 | 2014-08-12 | Alcohol production machinery device by using cassava as raw material |
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| Publication Number | Publication Date |
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| CN105462806A true CN105462806A (en) | 2016-04-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410393784.9A Pending CN105462806A (en) | 2014-08-12 | 2014-08-12 | Alcohol production machinery device by using cassava as raw material |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106434769A (en) * | 2016-09-27 | 2017-02-22 | 广西罗城科潮基业科技发展有限公司 | Processing method for alcohol production by cassava residues and molasses |
-
2014
- 2014-08-12 CN CN201410393784.9A patent/CN105462806A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106434769A (en) * | 2016-09-27 | 2017-02-22 | 广西罗城科潮基业科技发展有限公司 | Processing method for alcohol production by cassava residues and molasses |
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Application publication date: 20160406 |