CN2260295Y - Equipment for drying residual from brewery - Google Patents
Equipment for drying residual from brewery Download PDFInfo
- Publication number
- CN2260295Y CN2260295Y CN 96221696 CN96221696U CN2260295Y CN 2260295 Y CN2260295 Y CN 2260295Y CN 96221696 CN96221696 CN 96221696 CN 96221696 U CN96221696 U CN 96221696U CN 2260295 Y CN2260295 Y CN 2260295Y
- Authority
- CN
- China
- Prior art keywords
- drying
- casing
- distribution grid
- main shaft
- equipment
- 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
Links
Abstract
The utility model relates to equipment for drying a residual from brewery, which uses a consecutive variable pitch spiral body and a megaphone-shaped outlet formed by a mushroom-shaped barrier head fixed on a main shaft and the inner hole of a support body for the extrusion and the dehydration The utility model matches with a spiral type feeder, a toothed harrow type stirrer, and air flow supplied by the air inlet branch pipe for hot air and cold air to cause materials to flow on a distribution plate for conducting the dehumidification of a brewer groove via a fluidizing drying device. The utility model has the advantages of simple equipment, convenient operation, low power consumption, high productive efficiency, and good quality.
Description
The utility model relates to the drying equipment of eliminating liquid from bulk materials, is specially adapted to the drying of wet brewex's grains.
At present, the mode that the drying of brewex's grains all adopts mechanical dehydration and drying and dewatering to combine, mechanical dehydration generally is to utilize spiral dewater to finish, drying and dewatering then adopts the batch (-type) drying unit to realize mostly.The shortcoming of its existence is: 1. can not produce continuously, production efficiency is low; 2. power consumption is big; 3. since feeding and discharging all need finish rapidly, so relevant device is all very huge; 4. discharge and device cleaning trouble because of product, device is maximized have any problem.
The purpose of this utility model is at above-mentioned problems of the prior art, and provides a kind of dehydrating effect good, oven dry thermal efficiency height, but continuous feed, and discharging continuously forms the drying of beer lees equipment that continuous high-efficient is produced.
The technical scheme that realizes above-mentioned purpose is: a kind of drying of beer lees equipment that mainly is made of screw extrusion dewaterer and fluidized drying device, its spirochetal pitch that is fixed on the screw extrusion dewaterer main shaft reduces from front to back in succession, the supporting endoporus forms loudspeaker tubular outlet after being fixed with mushroom-shaped retaining head and cylindrical shell on the terminal main shaft of conveyor screw, and supporting top and main shaft rear support top are provided with cylinder lever connecting rod behind the cylindrical shell; The fluidized drying device has a rectangular box, the distribution grid that has the aperture that gathers is fixed on the casing middle and lower part obliquely, the air intake branch of loudspeaker tubular is distributed on below the distribution grid and is communicated with hot blast trunk line and cold wind trunk line respectively, be provided with the screw-pushing type charger in the front of casing, the position of the material bin of this charger is corresponding with its discharging opening below the screw extrusion dewaterer, the back of casing is provided with discharging overflow plate and discharge bucket, be respectively arranged with tooth harrow formula agitator and wind exhausting outlet at the casing top, the tooth harrow of agitator be fixed on vertically stretch into the tooth harrow axle in the casing front end in the distribution grid upper front part.
The technical solution of the utility model also comprises: the cylindrical shell of screw extrusion dewaterer is for having the double wall tube in the hole of gathering respectively, and the size in its hole is that outer big internal layer is little relatively; Before and after the spirochetal pitch than being 4: 1; The angle of inclination of distribution grid is 1 °-2 ° of downward and horizontal sextant angles from front to back in the fluidized drying device.
The utility model is compared with existing same category of device has following advantage:
1, continuous feed, discharging continuously, production efficiency height.
2, make the miniaturization of input and output material relevant device, reduced power consumption, reduced production cost.
3, easy and simple to handle, the dewatering whole stillage drying effect is good.
Accompanying drawing is this beer groove drying equipment structure front view.
The utility model is described in further detail below in conjunction with drawings and Examples.
Provide as accompanying drawing, this equipment mainly is made up of a screw extrusion dewaterer and horizontal fluidized drying device.Extruding-desiccation machine is placed in the upper left side of fluidized drying device, and it has preceding supporting 2, back supporting 28 and the rear support 11 that is emitted in succession on the base 1.Cylindrical shell 8 is a double wall barrel structure of being with the hole of gathering respectively, is fixed on the forward and backward supporting mass, and internal layer is an aperture, and skin is a macropore.Feed hopper 5 places above the cylindrical shell front portion.Supporting 28 tops and rear support 11 tops are provided with two ends and are fixedly coupled pull bar 10 through nut behind the cylindrical shell.Main shaft 6 before bearing fixing is assemblied in, support 2 and rear support 11 on.The pitch that is fixed in the conveyor screw 7 on the main shaft reduces from front to back in succession, and pitch ratio is 4: 1 before and after it.The endoporus of supporting 28 forms a loudspeaker tubular discharging opening after fixing mushroom-shaped retaining 9 and cylindrical shell on the conveyor screw 7 terminal main shafts 6.The left end of main shaft connects gearbox 3 through shaft coupling 4.The fluidized drying device has rectangular casing 15, and the distribution grid 18 that is provided with the aperture that gathers is fixed therein the bottom, has 1 ° inclination angle.Be provided with the air intake branch 24 of five loudspeaker tubulars below the distribution grid, debug the butterfly valve of solar term amount on each air intake branch, preceding two air intake branches are communicated with corresponding hot blast trunk line 23 and the cold wind trunk line 21 that its below is set respectively with back three air intake branches, its hot blast trunk line connects air blast through the interface 25 of front end, and cold wind trunk line side direction has natural air inlet mouth 22.In the front of casing screw-pushing type charger 26 is installed, the material bin 27 of this charger is corresponding with its discharging opening below dewaterer.At discharging opening place, the back of casing 15 overflow plate 17 and discharge bucket 16 are installed, dispose tooth harrow formula agitator 12 and a maintenance inlet and two wind exhausting outlets 14 at the top of casing, respectively be provided with seven shielding windows 13 in two sides of casing.The tooth harrow 19 of agitator is through vertically stretching into the corresponding first hot blast air intake branch place, top that tooth harrow axle 20 in the casing is suspended in distribution grid 18.
During the work of this equipment, wet stock dewaters to water content 60% by the screw extrusion dewaterer, then through the oven dry of screw-pushing type charger feeding drying box.The tooth harrow formula mixer that adds in the dry materials porch is eliminated caking in order to break up material, makes it keep good fluidized state on distribution grid.Distribution grid has 1 °-2 ° inclination approximately, is convenient to material and forward flows.Two air inlet EAT differences make the wet stock heat drying earlier, and then cooling is discharged.
Claims (4)
1, a kind of drying of beer lees equipment, comprise screw extrusion dewaterer and fluidized drying device, it is characterized in that: the pitch that is fixed in the conveyor screw (7) on the screw extrusion dewaterer main shaft (6) reduces from front to back in succession, the endoporus that is fixed with mushroom-shaped retaining head (9) and cylindrical shell (8) back supporting (28) on the terminal main shaft of conveyor screw (7) (6) forms loudspeaker tubular outlet, and supporting (28) top and main shaft (6) rear support (11) top are provided with cylinder lever connecting rod (10) behind the cylindrical shell; The fluidized drying device has a rectangular box (15), the distribution grid (18) that has the aperture that gathers is fixed on the casing middle and lower part obliquely, the air intake branch of loudspeaker tubular (24) is distributed on below the distribution grid and is communicated with hot blast trunk line (23) and cold wind trunk line (21) respectively, be provided with screw-pushing type charger (26) in the front of casing (15), the position of the material bin of this charger (27) is corresponding with its discharging opening below the screw extrusion dewaterer, the back of casing (15) is provided with discharging overflow plate (17) and discharge bucket (16), be respectively arranged with tooth harrow formula agitator (12) and wind exhausting outlet (14) at casing (15) top, the tooth harrow (19) of agitator (12) be fixed on vertically stretch into the tooth harrow axle (20) in the casing (15) front end in distribution grid (18) upper front part.
2, drying of beer lees equipment according to claim 1 is characterized in that: before and after the pitch of conveyor screw (7) than being 4: 1.
3, drying of beer lees equipment according to claim 1 is characterized in that: the angle of inclination of distribution grid (18) is for from front to back downwards and 1 °-2 ° of horizontal sextant angles.
4, drying of beer lees equipment according to claim 1 is characterized in that: cylindrical shell (8) is for having the double wall tube in the hole of gathering respectively, and the size in its hole is that outer big internal layer is little relatively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96221696 CN2260295Y (en) | 1996-09-17 | 1996-09-17 | Equipment for drying residual from brewery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96221696 CN2260295Y (en) | 1996-09-17 | 1996-09-17 | Equipment for drying residual from brewery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2260295Y true CN2260295Y (en) | 1997-08-20 |
Family
ID=33901525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96221696 Expired - Fee Related CN2260295Y (en) | 1996-09-17 | 1996-09-17 | Equipment for drying residual from brewery |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2260295Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100548518C (en) * | 2005-06-08 | 2009-10-14 | 江南环境工程（嘉兴）有限公司 | The compression drying under reduced pressure method of house refuse etc. and compression drying under reduced pressure machine |
| CN101586906B (en) * | 2009-06-08 | 2012-06-27 | 上海泽玛克敏达机械设备有限公司 | Drying tube for drying lignite, drying bucket body as well as method for drying lignite |
| CN107906853A (en) * | 2017-11-09 | 2018-04-13 | 湖州览春酒业有限公司 | Wine brewing vinasse press filtration drying mechanism |
| CN108458566A (en) * | 2018-05-02 | 2018-08-28 | 朱增伟 | A kind of vinasse dryer |
| CN108731457A (en) * | 2018-05-02 | 2018-11-02 | 朱增伟 | A kind of vinasse airflow dryer |
| CN109514755A (en) * | 2018-12-24 | 2019-03-26 | 青岛海诺中天科技股份有限公司 | A kind of drying system for plastic foam particle overlay film |
-
1996
- 1996-09-17 CN CN 96221696 patent/CN2260295Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100548518C (en) * | 2005-06-08 | 2009-10-14 | 江南环境工程（嘉兴）有限公司 | The compression drying under reduced pressure method of house refuse etc. and compression drying under reduced pressure machine |
| CN101586906B (en) * | 2009-06-08 | 2012-06-27 | 上海泽玛克敏达机械设备有限公司 | Drying tube for drying lignite, drying bucket body as well as method for drying lignite |
| CN107906853A (en) * | 2017-11-09 | 2018-04-13 | 湖州览春酒业有限公司 | Wine brewing vinasse press filtration drying mechanism |
| CN108458566A (en) * | 2018-05-02 | 2018-08-28 | 朱增伟 | A kind of vinasse dryer |
| CN108731457A (en) * | 2018-05-02 | 2018-11-02 | 朱增伟 | A kind of vinasse airflow dryer |
| CN109514755A (en) * | 2018-12-24 | 2019-03-26 | 青岛海诺中天科技股份有限公司 | A kind of drying system for plastic foam particle overlay film |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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 |