CN2488025Y - Steaming drying cooling machine - Google Patents
Steaming drying cooling machine Download PDFInfo
- Publication number
- CN2488025Y CN2488025Y CN 01250253 CN01250253U CN2488025Y CN 2488025 Y CN2488025 Y CN 2488025Y CN 01250253 CN01250253 CN 01250253 CN 01250253 U CN01250253 U CN 01250253U CN 2488025 Y CN2488025 Y CN 2488025Y
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- CN
- China
- Prior art keywords
- steaming
- drying device
- drying
- cooling device
- cooling
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- 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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Abstract
The utility model relates to a steaming drying cooling machine; the utility model is a vertical type cylinder (1) which comprises a material steaming device; the bottom of the material steaming device of the cylinder (1) is in series connected with a drying device (2); the steaming device is communicated with the drying device (2) through a spiral feed-out device (4); the bottom of the drying device is in series connected with a cooling device (3); the drying device (2) is communicated with the cooling device (3) through a material door (5); the bottom of the cooling device (3) is provided with a discharge port (18); a hot air inlet (14) and a cold air inlet (13) are arranged on the drying device (2) and the cooling device (3) respectively. With the utility model, the extractive material can have exsolution, toasting, drying and cooling simultaneously in order to make the produced material come from the machine in a room temperature, thereby being convenient for subsequent treatment (packing) and improving productivity effect of the factory to achieve automatization of manufacturing production.
Description
Technical field
The utility model relates to food production equipment, particularly utilizes water vapour that material is heated, steams slide, baking so that leach the material steaming baking device that contained separated from solvent is gone out in the material.
Background technology
In the existing at home extract technology, the separated from solvent that leaches material is mainly adopted steaming baking method, promptly material is carried out precipitation and baking with dryer.The temperature of charge height of this desolventizing method output needs a lot of storage capacity to deposit so that lower the temperature, and is not easy to next one and produces processing, has both influenced operating efficiency, accounts for a lot of warehouses again.
Summary of the invention
Technical problem to be solved in the utility model is: provide a kind of and can dry dry cooler to the steaming that material carry out dry cooling.
The technical scheme that its technical problem that solves the utility model adopts is: it is vertical cylindrical shell, comprise in the cylindrical shell that material steams the baking device, the bottom of the steaming baking device in the cylindrical shell is serially connected with drying device, steam the baking device by spiral discharging device and drying device UNICOM, the bottom of drying device is serially connected with cooling device, drying device is by bin gate and cooling device UNICOM, and the cooling device bottom is provided with discharge port, is respectively equipped with hot-wind inlet and cold air inlet on drying device and the cooling device.
Take off the material that finishes through steaming the steaming of baking device, enter drying device through the sealing screw discharger and carry out drying, then enter cooling device and cool off.
Owing to adopted technique scheme, the utility model can carry out precipitation, baking, drying and cooling simultaneously to leaching material, makes the output material at room temperature go out machine, is convenient to subsequent treatment (packing), to improve plant produced efficient, make industrial production can realize automation.
Description of drawings
Fig. 1 is the utility model example structure schematic diagram
Fig. 2 is chuck 9 schematic diagrames of first and second layer of the utility model embodiment
Fig. 3 be the utility model embodiment third and fourth, five layers chuck 8 schematic diagrames
Fig. 4 is chuck 7 schematic diagrames of the 6th, seven, eight layers of the utility model embodiment
The specific embodiment
The utility model embodiment as shown in Figure 1, it is a vertical cylindrical shell 1, is provided with in the cylindrical shell 1 to steam baking device, drying device 2, cooling device 3; Cylindrical shell 1 is separated into eight layers of ground floors to the from top to bottom, and the bottom of each layer all is provided with chuck; Ground floor to layer 6 is formed steaming baking device, finish the task of sloughing solvent, wherein first and second layer is to heat with indirect steam, material steamed in advance take off, ensuing third and fourth, five, six layers be to steam to take off (baking) layer, be equipped with the Steam Heating and 8 ends of diffusion chuck, all live (open) steams all spray into material from layer 6 chuck 7, and the solvent vapo(u)r that goes out with stripping rises to the top by the 5th, four, three interlayer up-hole plates respectively then.Seven, eight layers of drying device 2 and cooling device 3 that is respectively material, finish dry and cooling task, drying device 2 is serially connected in the bottom (bottom of layer 6) of steaming the baking device, steam the baking device by spiral discharging device 4 and drying device 2 UNICOMs, cooling device 3 is serially connected in the bottom of drying device 2, drying device 2 is by bin gate 5 and cooling device 3 UNICOMs, and cooling device 3 bottoms are provided with discharge port 18.
Chuck 7,8,9 shown in Fig. 2,3,4, all have discharge port on it.First and second chuck 9 structures are identical, are cylinders isometrical but highly very little with cylindrical shell, are furnished with water vapour discrepancy pipe, condensed water adapter, feed indirect steam in it, have the aperture 19 of certain density on the top panel 21, and material is carried out indirect.Third and fourth, five chucks, 8 structures are identical, are circular orifices, have the aperture 19 of certain density on it, be convenient to lower floor's gas and pass through, and utilize the mist stripping upper materials of lower floor's heat to reach the counter-current operation effect; Be welded with the angle steel 20 that communicates with one another below the orifice plate, form chuck, be furnished with water vapour discrepancy pipe, condensed water adapter, feed indirect steam in the chuck, material is carried out indirect.Six, chuck 7 structural similarities of seven, eight layers of bottom, it is a tubular, isometrical but highly very little, have the aperture 19 of certain density on the top panel 21 of chuck 7, make the steam that feeds chuck 7 directly spray into material and go out solvent, on the discharge port 18 of the chuck 7 of layer 6 bottom spiral discharging device 4 has been installed with stripping; Be respectively equipped with hot-wind inlet 14 and cold air inlet 13 on the chuck 7 of drying device 2 and cooling device 3 bottoms, be respectively equipped with hot-blast outlet 11 and cold wind outlet 12 on drying device 2 and the cooling device 3 residing cylindrical shells 1.Also be respectively equipped with sparge pipe assembly 6 on the chuck 7 of drying device 2 and cooling device 3, to regulate the moisture of output material.
Spiral discharging device 4 is installed on the layer 6 chuck 7; Because solvent is a kind of inflammable and explosive toxic gas, must be limited in the closed system, spiral discharging device 4 was both salable, but also discharging has avoided solvent to leak because of discharging; Spiral discharging device 4 can be driven by an electronic transmission, and electronic transmission can be regulated by level sensor and electronic controller, controls each layered material layer height voluntarily.The second layer has been installed level detector, links by sensing cable and computer, the controlling level information of being obtained is passed to computer and controlled speed changer by computer drive spiral discharging device 4.
All be furnished with mixing arm 10 near layer bottom in each layer of the utility model embodiment, mixing arm 10 is contained on the main shaft 17, forms agitator.Main shaft 17 links to each other with reductor, and reductor then together is installed on the installing plate with other drive unit.For ease of installing, main shaft 17 is divided into upper and lower two sections, makes upper and lower two sections to join together with shaft coupling 23.
Because it is very big to mix the flow velocity of gas, some materials (dregs of rice) of can carrying under one's arms rise to the solvent vapo(u)r exit, for preventing that the dregs of rice from being taken out of, are equipped with umbrella shape retaining dregs of rice plate 22 on ground floor top near the solvent vapo(u)r exit, to reduce steam flow speed, stop that the dregs of rice are taken out of by high-speed mixing vapour.
The door to access 15 of easy access also is installed on every layer of cylindrical shell 1 and be convenient to observe every layer in the visor 16 of material situation.
The utility model embodiment has following characteristic:
1, will steam the dry cooling of oven dry and be integrated in one and carry out, reduce equipment investment and floor space;
2, be suitable for mass automatic production, labor intensity of operating staff is low;
3, product goes out machine with room temperature, can pack immediately;
4, stable and reliable operation, energy consumption is low, unit treating capacity big (can reach 6000 ton per days);
5, can regulate the moisture of output material, make product quality reach the requirement standard;
6, simple to operate, be convenient to maintenance;
Claims (6)
1, steams the dry cooler of oven dry, it is vertical cylindrical shell (1), comprise in the cylindrical shell (1) that material steams the baking device, it is characterized in that: the bottom of the steaming baking device in the cylindrical shell (1) is serially connected with drying device (2), steam the baking device by spiral discharging device (4) and drying device (2) UNICOM, the bottom of drying device (2) is serially connected with cooling device (3), drying device (2) is by bin gate (5) and cooling device (3) UNICOM, cooling device (3) bottom is provided with discharge port (18), is respectively equipped with hot-wind inlet (14) and cold air inlet (13) on drying device (2) and the cooling device (3).
2, dry cooler is dried in steaming as claimed in claim 1, it is characterized in that: the bottom of drying device (2) and cooling device (3) is respectively equipped with chuck (7), chuck (7) is a tubular, hot-wind inlet (14) is arranged on the chuck (7) of drying device (2), and cold air inlet (13) is arranged on the chuck (7) of cooling device (3); Have aperture (19) on the top panel (21) of chuck (7).
3, dry cooler is dried in steaming as claimed in claim 2, it is characterized in that: be respectively equipped with sparge pipe assembly (6) on the chuck (7) of drying device (2) and cooling device (3).
4, dry cooler is dried in steaming as claimed in claim 1 or 2, it is characterized in that: be equipped with mixing arm (10) in drying device (2) and the cooling device (3), mixing arm (10) is contained on the main shaft (17).
5, dry cooler is dried in steaming as claimed in claim 1 or 2, it is characterized in that: be respectively equipped with visor (16) on drying device (2) and the residing cylindrical shell of cooling device (3) (1).
6, dry cooler is dried in steaming as claimed in claim 1 or 2, it is characterized in that: be respectively equipped with door to access (15) on drying device (2) and the residing cylindrical shell of cooling device (3) (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01250253 CN2488025Y (en) | 2001-08-02 | 2001-08-02 | Steaming drying cooling machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01250253 CN2488025Y (en) | 2001-08-02 | 2001-08-02 | Steaming drying cooling machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2488025Y true CN2488025Y (en) | 2002-04-24 |
Family
ID=33660456
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01250253 Expired - Fee Related CN2488025Y (en) | 2001-08-02 | 2001-08-02 | Steaming drying cooling machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2488025Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104132525A (en) * | 2014-08-13 | 2014-11-05 | 北京广厦环能科技有限公司 | Powder material drying and cooling integrated device |
-
2001
- 2001-08-02 CN CN 01250253 patent/CN2488025Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104132525A (en) * | 2014-08-13 | 2014-11-05 | 北京广厦环能科技有限公司 | Powder material drying and cooling integrated device |
| CN104132525B (en) * | 2014-08-13 | 2016-08-24 | 北京广厦环能科技股份有限公司 | Powder material is dried cooling integration equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Xu Daoying Document name: Notification of Termination of Patent Right |
|
| 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 |