CN2060778U - Device for separating and recovering press residues of alcohol - Google Patents
Device for separating and recovering press residues of alcohol Download PDFInfo
- Publication number
- CN2060778U CN2060778U CN 89217463 CN89217463U CN2060778U CN 2060778 U CN2060778 U CN 2060778U CN 89217463 CN89217463 CN 89217463 CN 89217463 U CN89217463 U CN 89217463U CN 2060778 U CN2060778 U CN 2060778U
- Authority
- CN
- China
- Prior art keywords
- rice husk
- screen cloth
- separating
- chorista
- main shaft
- 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.)
- Withdrawn
Links
Images
Abstract
The utility model relates to a device for separating, dehydrating and recovering the grain husk and the grain slag in the press residues of the alcohol. The novelty and the progress lie in that the utility model combines the peeling and the separation of the husk and the slag into integration. The separating equipment has the advantages of simple structure, energy saving, water saving, low cost, etc. The dehydration of the grain husk adopts the secondary separation. The grain slag adopts the preconcentration before the dehydration and is matched with the relatively good separation parameter. The equipment has simple structure and cheap price and can be popularized in the common brewery.
Description
The utility model is that rice husk in the using solid distillers ' grains is separated the device of dewatering and recovery with residual grain slag.
Solid-state vinasse is to adopt solid state fermentation to produce the byproduct of liquor, and its formation mainly is rice husk and grain slag.The grain slag is lingering section and the unconverted starch after system wine raw grain (corn, Chinese sorghum, wheat etc.) transforms, the mixtures such as tropina that produce in dextrin and the fermenting process.Main component has after measured: crude protein (about 16.6%), and crude fat (about 7.2%), nitrogen-free extract (about 50.7%), coarse ash (about 6.2%), robust fibre (about 9.4%) is an ideal animal and fowl fodder comparatively.Rice husk is the stopping composition of system wine, and rice husk still has after drinking through the fermentation system and is in health state more than 80%, can be used for back chaff system wine once more.
In conventional the production, one ton of liquor of every production produces 5～8 tons in vinasse (wet poor) approximately, amounts to and does poor (over dry) about 2-3.2 ton.In dried being pickled with grains or in wine, rice husk accounts for 70% of gross weight, and the grain slag accounts for 30% of gross weight.
Firm vinasse temperature height (about 80 ℃) of discharging, acidity big (about 1.2), moisture content many (about 65%).In case stack very easily moldy metamorphism, produce stink, living maggot, living fly contaminate environment, (what have will hand over pollution charges) outwards raftinged with special train by therefore a lot of breweries.There is rice husk under-supply (even more serious in draining rice producing region especially) summer again in this external spring, influences the liquor ordinary production.
There are hundreds of families of large and medium-sized brewery (producing per year more than the liquor kiloton) in China at present, and small-sized brewery is just more, and the annual vinasse amount that produces is considerable, and therefore research is recycled, and is about to isolated rice husk and is used for back chaff system wine, and the grain slag is as feed.Turn harm into good like this, change useless, there are great economic benefit and social benefit in brewery for precious.
At present, domestic (adopting liquid state fermentation abroad) sold to outside the peasant feeds pigs with at a low price (1-2 branch/jin) the depolarization small portion that utilizes of using solid distillers ' grains, is divided into two big classes substantially: the one, vinasse oven dry back pulverizing is used as feed (as Sichuan Wen Jin brewery).This method advantage is that poor powder is convenient to store transportation, but the equipment manufacturing cost high energy consumption is big, and rice husk content height in the vinasse, makes crude fiber content in the vinasse powder up to about 21%, has both influenced quality of the fodder, has wasted the resource of rice husk again.This brewery to non-paddy rice producing region is very disadvantageous.Another kind of is vinasse to be carried out shell-slag with wet method (washing sieve point-score) separate, and is recycled respectively then.Because of the rice husk supply bottleneck, reasons such as the big processing difficulty of vinasse amount had once been carried out experimental study to this in 82 years some breweries (as Chaoyang, Jiang Cheng etc.), but all or because of water loss height (poor water than up to 1/20), or because of reasons such as the complicated energy consumption height of equipment, and be forced to end.Henan brewery once developed a wet separation equipment in 84 years, will isolate rice husk and be used for back chaff system wine.But because of its poor water than reason such as about 1/11 still, do not see formal popularization so far.
For overcoming above-mentioned shortcoming, it is simple in structure that the utility model provides a cover to have, water loss low (poor water ratio is 1/5), cheap vinasse separating and reclaiming device.
For achieving the above object, the utility model proposes following technical scheme:
A kind of using solid distillers ' grains separating and reclaiming device that is used for, its special character is that it is mainly by feeder (1), vinasse separating machine (3), rice husk water extracter (4), settling bowl (2), liquid pump (5), grain residues hydroextractor (6) is formed, advance to be pickled with grains or in wine mouthful (13) of the discharge port of feeder (1) and vinasse separating machine (3) join, on the vinasse separating machine (3) go out faucal (17) and dreg discharging liquid mouth (9) respectively with rice husk water extracter (4) on hopper (27) link to each other with settling bowl (2), leakage fluid dram (28) on the rice husk water extracter (4) links with settling bowl (2), between settling bowl (2) and the grain residues hydroextractor (6) liquid pump (5) is housed.
Above-mentioned vinasse separating machine (3), its special character is the main shaft (11) that it can mainly be equipped with by casing and Qi Nei, fixed blade (12) gone up by screen cloth (14) and main shaft (11) and cone spiral vane (15) is formed, cone spiral vane (15) is contained in out faucal (17) and locates, screen cloth (14) is contained in main shaft (11) bottom, casing top is provided with into poor mouthful (13) and water-in (16), the bottom is provided with dreg discharging liquid mouth (9), go out faucal (17) bottom slide plate (18) is housed, the reduction box (10) that is driven by motor (8) is equipped with in the end of main shaft (11), and casing is bearing on the frame (7).
The special character of above-mentioned main shaft (11) is that level inclination can be 20 °～40 °, and blade (12) inclination angle on the main shaft (11) is 40 °～60 °, has aperture on the blade.
More than said rice husk water extracter (4), its special character is that it can be mainly by awl basket (23), secondary separation screen cloth (25), chorista (21), annular liquid flume (24) is formed, the awl basket (23) that is driven by motor (20) is loaded in the chorista (21) that has leg (19), awl basket (23) wall is a screen cloth, awl basket (23) top is covered with secondary screen cloth (25), which is provided with hopper (27), secondary screen cloth (25) outside is provided with cover plate (26), form annular liquid flume (24) between them and also communicate with chorista (21), be provided with rice husk slide plate (22) on the formed annular cavity between annular liquid flume (24) inwall and the chorista (21) by return line (29).
More than said grain residues hydroextractor (6), its special character is that it can mainly be by being loaded in the chorista (32), and form by awl basket (34) and loam cake (35), hopper (37) that motor (31) drives, awl basket (34) wall is screen cloth (34), chorista (32) is provided with leakage fluid dram (33) and leg (30) is housed, and loam cake (35) is provided with discharge gate (36).
The working process of this device is as follows:
Vinasse are sent into the vinasse separating machine through feeder rice husk are separated with the grain slag, and the rice husk of separating is sent into the rice husk water extracter, and wherein water and slag are sent into settling bowl, and rice husk is used for back chaff system wine.Separate the grain slag by the vinasse separating machine and send into settling bowl, the supernatant liquor in the pond is drained, and the grain slag is squeezed into the grain residues hydroextractor through liquid pump, and that comes out behind the water of draining is feed or makes granulated feed.
The key part of this device is vinasse separating machine, rice husk water extracter and grain residues hydroextractor.Below in conjunction with accompanying drawing in detail content of the present invention is described in detail.
The vinasse separating machine is mainly by main shaft (11), blade (12), screen cloth (14) and cone spiral vane compositions such as (15).
Its principle of work is: go up the agitaion that is subjected to blade (12) in the water when vinasse enter screen cloth (14) by inlet (13), realizing shell, in the process that slag is peeled off, the grain slag has been subjected to the screening effect of sieve (14), action of gravity and concentration diffusion and constantly from the sieve tell, the running of screw arrangement cone spiral vane (15), constantly push rice husk to outlet by inlet, realized non-stop run, water-in (16) is located near the rice husk outlet (17), leakage fluid dram (9) is located at into poor mouthful (13) lower end, its flow direction has not only increased poor water motion has been helped the separation of shell slag, realized that also rice husk moves to low concentration region from the high concentration region of slag liquid, water then is to be flowed to high concentration region by low concentration region, so promptly help the sedimentation of grain slag and arrange from, guarantee the high density of drainage region again, utilized the water yield preferably.When being released the water surface, be subjected to the drip washing of clear water for rice husk again, entered the rice husk water extracter with the degree of cleaning higher state at last by cone spiral vane (15).Further separate and dehydration.Make the rice husk slag-containing rate, water ratio and the acidity that finally obtain all can satisfy back the requirement of chaff system wine.
Through the isolated rice husk of vinasse separating machine general moisture higher (can reach about 80%) and carry a small amount of grain slag secretly.It is very unfavorable that this brews alcoholic beverages to time chaff, and particularly the water content height has influence on the water content of spice homogeneity and pit entry fermentation material embryo, so must further separate and dehydration isolated rice husk.
Rice husk water extracter in this device is to make rice husk after awl basket primary dewatering and obtain acceleration, with high speed impact secondary separation screen cloth, make that moisture content is separated by the secondary separation screen cloth in impact process with the grain slag in the rice husk, final rice husk water ratio and slag-containing rate are greatly reduced, satisfy back the requirement of chaff system wine.
Its principle of work is: in the time of when rice husk is entered high speed rotating awl basket (23) by import hopper (27) in, under centrifugal action, rice husk is along boring upwards slip (warp-wise of basket, circumferentially) simultaneously, moisture content in the rice husk is separated by awl net hole with a small amount of grain slag, to obtain bigger acceleration when rice husk leaves the awl basket, with high speed impact secondary separation screen cloth (25), its moisture content is further separated with the grain slag.Rice husk after the separation drops on the slide plate (22), and grain slag liquid falls in the ring groove (24), and along discharging by liquid discharge pipe (28) in return line (29) the inflow chorista.Realized like this working continuously.
The slag liquid concentration of discharging through vinasse separating machine leakage fluid dram (comprising the rice husk water extracter) is low-down (weight concentration is 5.5%), and this does not promptly utilize to feed raises, also is unfavorable for transportation and postorder processing, so must be to its concentration.This skill scheme is to put into the settling bowl sedimentation from the isolated slag liquid of vinasse separating machine (comprising the rice husk water extracter), behind the sedimentation certain hour, bleeds off supernatant liquor and makes slag liquid concentration reach certain value, puts it into the rice husk water extracter dehydration with optimum revolution then.
The rice husk water extracter is to adopt the conic basket type whizzer, and its dewatering test shows that there is a certain optimum revolution in slag liquid concentration when low, and it is not good to be higher or lower than optimum revolution dehydrating effect in period.But after concentration reaches a certain value (title threshold concentration), will not have the optimum revolution phenomenon, at this moment, along with the increase of rotating speed, the water ratio of dehydration back grain slag descends.The principle of work of rice husk water extracter is: when giving spissated grain slag liquid when being entered in the awl basket (34) of rotation by hopper (37), under centrifugal action, moisture content is discharged by the mesh of awl basket (34), and the grain slag is discharged from discharge (36) along sliding on the awl basket bus.
Such scheme provided by the utility model has the following advantages: owing to the peeling off with to divide exsolution be one of shell one slag, make the designs simplification of tripping device, energy consumption is low, saves the water yield (poor water is than being 1:5); The rice husk water extracter makes its designs simplification owing to adopt secondary separation, and energy consumption is low, has utilized the kinetic energy impact principle preferably, and the slag-containing rate of final acquisition rice husk and water ratio are greatly reduced; The dehydration of grain slag greatly reduces the material of processing, and can carry out continuously dehydrating in this machine owing to enter dewatering unit after concentrated (settling process) comparatively simply given in employing in advance.
Description of drawings:
Fig. 1 is the general illustration of using solid distillers ' grains separating and reclaiming device;
Fig. 2 is the vinasse separating machines for (3) among Fig. 1;
Fig. 3 is the rice husk water extracter for (4) among Fig. 1;
Fig. 4 is the grain residues hydroextractor for (6) among Fig. 1;
(1) is feeder among the figure, and (2) are settling bowl, and (3) are the vinasse separating machine, (4) be the rice husk water extracter, (5) are liquid pump, and (6) are the grain residues hydroextractor, (7) be frame, (8) are motor, and (9) are the dreg discharging liquid mouth, (10) be reduction box, (11) are main shaft, and (12) are blade, (13) for advancing to be pickled with grains or in wine mouth, (14) are screen cloth, and (15) are cone spiral vane, (16) be water-in, (17) for going out faucal, (18) are slide plate, (19) be leg, (20) are motor, and (21) are chorista, (22) be the rice husk slide plate, (23) are the awl basket, and (24) are that annular liquid is poor, (25) be the secondary separation screen cloth, (26) are cover plate, and (27) are hopper, (28) be leakage fluid dram, (29) be return line, (30) are leg, and (31) are motor, (32) be chorista, (33) be leakage fluid dram, (34) are the awl basket, and (35) are loam cake, (36) be discharge gate, (37) are hopper.
In order to implement the such scheme that the utility model proposes, an existing only act wherein example is illustrated.The using solid distillers ' grains separating and reclaiming device is mainly by feeder (1), vinasse separating machine (3), and settling bowl (2), rice husk water extracter (4), liquid pump (5), grain residues hydroextractor (6) is formed.What the feeder of this device (1) adopted is the moveable belt type feeder, and its transport capacity is 2-4 ton/time, and its drive-motor adopts 2.2KW.
Main shaft (11) level inclination on the vinasse separating machine (3) is 25 °, is fixed with 16 blades on it, and blade is 51 ° with the inclination angle of axle.Screen cloth (14) adopts metal knitted sieve, and its aperture is 2 * 2mm.The speed of mainshaft is 80～90 rev/mins.The processing power of this machine be 1 ton/time, water loss be 5 tons/time, installed capacity is 3KW, the rice husk rate of recovery is more than 85%, the rice husk degree of cleaning are more than 80%, the rice husk percentage of head rice is more than 70%.
Awl basket cone angle on the rice husk water extracter (4) is 43 °, and its rotating speed is 1450 rev/mins, and the screen cloth of awl basket is metal knitted sieve, and its aperture is 2 * 2mm.The processing power of this machine be 2 tons/time, installed capacity is 0.75KW, the dehydration water ratio be about 59%, slag-containing rate is about 10%.
The awl basket radial angle of grain residues hydroextractor is 44 °, and rotating speed is 1450 rev/mins, and the screen cloth of awl basket is a nylon wire, and the aperture is 200 orders.The processing power of this machine be 2.5 tons/time, installed capacity is 1.5KW, dehydration back grain slag water ratio is about 65%.
The liquid pump that this device adopts is 1.5～2 inches, and motor is 1.5KW.
Claims (5)
1, a kind ofly be used for solid-state vinasse separating and reclaiming device, it is characterized in that it is mainly by feeder (1), vinasse separating machine (3), rice husk water extracter (4), settling bowl (2), liquid pump (5), grain residues hydroextractor (6) is formed, advance to be pickled with grains or in wine mouthful (13) of the discharge port of feeder (1) and vinasse separating machine (3) join, vinasse separating machine (3) go out faucal (17) and dreg discharging liquid mouth (9) respectively with rice husk water extracter (4) on hopper (27) and settling bowl (2) link, leakage fluid dram (28) on the rice husk water extracter (4) links with settling bowl (2), between settling bowl (2) and the grain residues hydroextractor (6) liquid pump (5) is housed.
2, a kind of using solid distillers ' grains separating and reclaiming device that is used for according to claim 1, it is characterized in that said vinasse separating machine (3) mainly is the main shaft (11) that is equipped with by casing and Qi Nei, screen cloth (14), and main shaft (11) is gone up fixed blade (12) and cone spiral vane (15) is formed, cone spiral vane (15) is contained in out faucal (17) and locates, screen cloth (14) is contained in main shaft (11) bottom, casing top is provided with into poor mouthful (13) and water-in (14), the bottom is provided with dreg discharging liquid mouth (9), go out faucal (17) bottom slide plate (18) is housed, the reduction box (10) that is driven by motor (8) is equipped with in the end of main shaft (1), and casing is bearing on the support (7).
3, a kind of using solid distillers ' grains separating and reclaiming device that is used for according to claim 1 and 2, it is characterized in that said main shaft (11) level inclination is 20 °～40 °, blade (12) inclination angle on the main shaft (11) is 40 °～60 °, and blade has aperture on (12).
4, a kind of using solid distillers ' grains separating and reclaiming device that is used for according to claim 1, it is characterized in that said rice husk water extracter (6) mainly is by awl basket (23), secondary separation screen cloth (25), chorista (21), annular liquid poor (24) is formed, drive by motor (20), awl basket (23) is loaded in the chorista (21) that has leg (19), awl basket (23) wall is a screen cloth, awl basket (23) top is covered with secondary screen cloth (25), which is provided with hopper (27), cover plate (26) is equipped with in secondary screen cloth (25) outside, form annular liquid poor (24) between them, and communicate with chorista (21), be provided with rice husk slide plate (22) on the formed annular cavity between poor (24) inwall of annular liquid and the chorista (21) by return line (29).
5, a kind of using solid distillers ' grains separating and reclaiming device that is used for according to claim 1, it is characterized in that said grain residues hydroextractor (6) mainly is by being loaded in the chorista (23), and form by awl basket (34) and loam cake (35), hopper (37) that motor (31) drives, awl basket (34) wall is screen cloth (34), chorista (32) is provided with leakage fluid dram (33) and leg (30) is housed, and loam cake (35) is provided with discharge gate (36).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89217463 CN2060778U (en) | 1989-10-04 | 1989-10-04 | Device for separating and recovering press residues of alcohol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 89217463 CN2060778U (en) | 1989-10-04 | 1989-10-04 | Device for separating and recovering press residues of alcohol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2060778U true CN2060778U (en) | 1990-08-22 |
Family
ID=4872713
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 89217463 Withdrawn CN2060778U (en) | 1989-10-04 | 1989-10-04 | Device for separating and recovering press residues of alcohol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2060778U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106615685A (en) * | 2009-05-26 | 2017-05-10 | 富禄德奎普有限公司 | Method for producing high-protein corn flour from whole vinasse byproducts |
| CN107881051A (en) * | 2017-10-23 | 2018-04-06 | 甘肃滨河食品工业（集团）有限责任公司 | A kind of method lost poor recycle device and lose grain recycling |
| CN111217625A (en) * | 2020-03-09 | 2020-06-02 | 青岛天人环境股份有限公司 | Lees treatment facility assembly line |
| CN113857201A (en) * | 2021-09-01 | 2021-12-31 | 四川轻化工大学 | Lees integrated processing system of assembly line formula |
| CN115449446A (en) * | 2022-09-02 | 2022-12-09 | 安徽省金裕皖酒业有限公司 | Health-preserving white spirit brewing slag material recycling system and method |
-
1989
- 1989-10-04 CN CN 89217463 patent/CN2060778U/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106615685A (en) * | 2009-05-26 | 2017-05-10 | 富禄德奎普有限公司 | Method for producing high-protein corn flour from whole vinasse byproducts |
| CN107881051A (en) * | 2017-10-23 | 2018-04-06 | 甘肃滨河食品工业（集团）有限责任公司 | A kind of method lost poor recycle device and lose grain recycling |
| CN111217625A (en) * | 2020-03-09 | 2020-06-02 | 青岛天人环境股份有限公司 | Lees treatment facility assembly line |
| CN113857201A (en) * | 2021-09-01 | 2021-12-31 | 四川轻化工大学 | Lees integrated processing system of assembly line formula |
| CN115449446A (en) * | 2022-09-02 | 2022-12-09 | 安徽省金裕皖酒业有限公司 | Health-preserving white spirit brewing slag material recycling system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8753848B2 (en) | Method of producing corn starch by enzymatic process | |
| US9689003B2 (en) | Dry grind ethanol production process and system with front end milling method | |
| CN102080104B (en) | Comprehensive treatment method for preparing gas and fertilizer by utilizing kitchen waste | |
| CN101245354B (en) | Novel method for producing ethanol with potato raw material | |
| CN205926564U (en) | A complete sets that is used for kitchen garbage preliminary treatment edulcoration, proposes oil and slurrying | |
| CN101235391B (en) | Method and system for continuously separating ethanol and utilizing residual heat based on solid-state fermentation material | |
| CN101076497A (en) | Industrial olive oil mill by-products producing method and resulting products | |
| CN101993900B (en) | Pretreatment process of citric acid raw material | |
| CN113733631A (en) | Efficient sand and impurity removing and oil extracting method and system for kitchen waste | |
| CN1948434A (en) | Two stage dewatering technology of fine coal mud | |
| CN2060778U (en) | Device for separating and recovering press residues of alcohol | |
| CN111360034A (en) | Kitchen waste pretreatment system and method | |
| CN117082971A (en) | System and method for improving corn wet milling and dry milling process | |
| CN110899303B (en) | System for utilize heisui river horsefly to carry out kitchen garbage resourceful treatment | |
| CN201341390Y (en) | Complete equipment for industrialized production of rice bran oil | |
| US20190211365A1 (en) | Dry grind biochemical production process and system with front end milling method | |
| CN1662138A (en) | Preservation of sugar cane and other plant materials | |
| CN216092642U (en) | Kitchen waste treatment system | |
| CN104974264A (en) | Extraction system and extraction method of duckweed starch | |
| CN101717802A (en) | Energy-saving production method of bio-ethanol | |
| CN103773812A (en) | Method for preparing fuel alcohol from acorns and resource utilization of acorns | |
| CN102612934A (en) | Raw material storage device for tapioca chips | |
| CN104862428B (en) | The sugar-free grains enrichment and separation device and method of a kind of enzyme process starch sugar | |
| CN113101728A (en) | Kitchen waste separating device | |
| CN201173663Y (en) | Polyester drinking bottle re-use dewaterer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |