CN203403076U - Novel pre-separation disc of evapo-separated machine - Google Patents
Novel pre-separation disc of evapo-separated machine Download PDFInfo
- Publication number
- CN203403076U CN203403076U CN201320490697.6U CN201320490697U CN203403076U CN 203403076 U CN203403076 U CN 203403076U CN 201320490697 U CN201320490697 U CN 201320490697U CN 203403076 U CN203403076 U CN 203403076U
- Authority
- CN
- China
- Prior art keywords
- disk stripping
- evapo
- separation disc
- separated machine
- cutter
- 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
Images
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a novel pre-separation disc of an evapo-separated machine. The pre-separation disc is placed inside a barrel of the evapo-separated machine horizontally. An inclined discharge outlet is formed in the position where an angle of 180 degrees is formed between a side board of the pre-separation disc and the main axis of a feed seal packing auger conveyor and in a bottom board close to the top end of a stir cutter of the pre-separation disc. A main shaft is arranged in the circle center of the pre-separation disc and provided with the stir cutter. The distance between the lower edge of the stir cutter and the bottom board of a bottom interlayer of the pre-separation disc is 5mm. By heating and stirring, 80% of solvent oil in wet meal materials is converted into gas in a jacking disc and a second pre-separation layer, discharged through a pulling gas tube and then recovered, so that most solvent oil in the wet meal materials is recovered, operation difficulty of follow-up processes is reduced, residual solvent quantity in meal cakes is reduced, and the quality of the meal cakes is improved. Meanwhile, production cost is controlled, economic benefits are improved and the effect of adapting to market economic development is achieved.
Description
Technical field:
This project related products, are applicable to after the leaching of the food oils engineering tea dregs of rice, and wet dregs of rice solvent oil removes the special technology field of operation.
Background technology:
At present, it is de-that the grease processing enterprise food oils raw material of domestic various scales needs solvent steaming after leaching.Utilizing evapo-separated machine to steam after the solvent oil in the de-oiling fat raw material dregs of rice, dregs of rice cake is residual molten higher; Reason is the pre-pallet that is provided with of the evapo-separated machine the superiors, and pre-pallet discharge port is on the side plate top of pre-pallet; In pallet bottom of intermediate layer portion, preserving all the time the certain altitude bed of material in advance like this, forming and on heating interlayer plate, have the siccative of certain altitude row not go out; The wet dregs of rice that newly enter, above siccative layer, although there is whipping appts, can not all turn over the wet dregs of rice to bottom-heated interlayer; Making the wet dregs of rice and hot sandwich plate carry out big area contacts.Because the wet dregs of rice of major part do not carry out big area with hot sandwich plate, do not contact, the solvent oil in the wet dregs of rice does not reach pre-de-effect, is just stirred device and scrapes to discharge port and discharge, and so just causes pre-pallet not reach due function; Follow-up depository receipts technique is difficult to operation, steams the difficulty increase that desolventizing is steamed in delamination simultaneously, and solvent residual amount in dregs of rice cake is increased.When dregs of rice cake enters a large amount of solvent gas of baking zone and water vapor, form secondary steam and enter in atmosphere, cause solvent loss to increase; Because secondary steam does not have recovery value on general technology, and cost recovery is higher, turns round and look at and does not consider to access recovery system.The product that this project is related, can address the above problem.
Utility model content:
The pre-disk stripping of product Novel steam off line that the utility model is related, for the above-mentioned secondary steam that do not reclaim in the technique of evapo-separated machine, pre-delamination does not reach the required parameter index of technique, causes the increase of dregs of rice cake solvent residual amount and forms the problem that solvent loss increases.According to the structure of evapo-separated machine, the pre-cylindrical of disk stripping and the inwall of evapo-separated machine have very large space, by addressing the above problem the structure adjustment of pre-disk stripping.
Concrete scheme: be horizontal mode in evapo-separated machine inner barrel pre-disk stripping is set, pre-disk stripping top is provided with feeding seal screw conveyor; When evapo-separated machine moves, material has been filled in feeding seal screw conveyor inside; The outlet of feeding seal screw conveyor has certain difference of altitude with pre-disk stripping, has formed bank; Utilize material, make between feeding seal screw conveyor and evapo-separated machine very close to each other; Material, in the pre-disk stripping of evapo-separated machine, heats by steam jacket the solvent oil making in material and evaporates the gas being transformed into; Because feeding seal screw conveyor inner chamber is very close to each other, solvent gas can not leak out.On pre-disk stripping side plate, be the position of 180 ° with the main axis of feeding seal screw conveyor, on the base plate that stirs cutter top end near pre-disk stripping, be provided with an oblique discharge port; The outside of discharge port is provided with a receiving hopper, and the discharging mouth of pipe of receiving hopper is near the pre-delamination of the second layer, but do not affect that the pre-delamination of the second layer is provided with stir cutter rotation.The center of circle of pre-disk stripping is provided with a main shaft, and main shaft is provided with and stirs cutter; The lower edge that stirs cutter with the base plate of interlayer at the bottom of pre-disk stripping apart from 5mm.When material enters pre-pallet from the outlet of feeding seal screw conveyor, by stirring the effect of cutter, material is shakeout, thereby make wet dregs of rice material contact and produce solvent gas with pre-pallet bottom of intermediate layer plate big area; Through pulling out after tracheae is discharged, reclaim.Wet dregs of rice material constantly enters pre-pallet, the material of oven dry slowly be squeezed into discharge bucket, by transfer lime, be transported to the pre-delamination of the second layer; The control of the discharge port valve being provided with through the second layer pre-delamination, makes in wet dregs of rice material 80% solvent oil in pre-pallet and the pre-delamination reformed gas of the second layer, through reclaiming through pulling out after tracheae is discharged.
By the setting of said structure, make in wet dregs of rice material that solvent oil is most of to be reclaimed, reduced subsequent handling operation easier, reduced solvent residual amount in dregs of rice cake, improved dregs of rice cake quality; Control production cost simultaneously, increased economic efficiency, reached the effect that adapts to market economic development.
Accompanying drawing explanation:
Below in conjunction with drawings and Examples, the utility model is further illustrated, Fig. 1 is the product structure schematic diagram of the pre-disk stripping of Novel steam off line.
As shown in Figure 1: main shaft 1, stir cutter 2, pre-disk stripping 3, web member 4, evapo-separated machine cylindrical shell 5,
Transfer roller support 6, feeding seal screw conveyor 7, transmitting gear 8, holding bolt 9,
Lamina tecti 10, pull out tracheae 11, visor 12, top inspection manhole 13, handle 14,
Briquetting 15, discharge port of screw conveyor 16, stir tool rest 17, discharge bucket 18,
Heating interlayer 19, transfer lime 20.
Embodiment:
As shown in Figure 1, the mode that pre-disk stripping 3 is level by web member 4 is arranged on evapo-separated machine cylindrical shell 5 inside to the related product of this project; Pre-disk stripping 3 tops are provided with feeding seal screw conveyor 7, by holding bolt 9, are fixed on evapo-separated machine cylindrical shell 5; On pre-disk stripping 3 side plates, be the position of 180 ° with the main axis of feeding seal screw conveyor 7, on the base plate that stirs cutter 2 top ends near pre-disk stripping 3, be provided with an oblique discharge port; The outside of discharge port is provided with a receiving hopper 18, and receiving hopper 18 is connected to transfer lime 20.The center of circle of pre-disk stripping 3 is provided with a main shaft 1, and main shaft 1 is provided with and stirs cutter 2; Stir cutter 2 and be fastened on main shaft 1 by stirring tool rest 17, make to stir the lower edge of cutter 2 and the base plate of pre-disk stripping 3 end interlayer apart from 5mm.
When evapo-separated machine moves, main shaft 1 drives and stirs cutter 2 rotations; Material enters feeding seal screw conveyor 7 from opening for feed, material is from feeding seal screw conveyor 7, after discharge port of screw conveyor 16 enters pre-pallet 3, by stirring the effect of cutter 2, material is shakeout, thereby make wet dregs of rice material contact and produce solvent gas with pre-pallet bottom of intermediate layer plate big area; Through pulling out after tracheae is discharged, reclaim.Wet dregs of rice material constantly enters pre-pallet 3, the material of oven dry slowly be squeezed into discharge bucket 18, by transfer lime 20, be transported to the pre-delamination of the second layer; The control of the discharge port valve being provided with through the second layer pre-delamination, makes in wet dregs of rice material 80% solvent oil in pre-pallet 3 and the pre-delamination reformed gas of the second layer, through reclaiming through pulling out after tracheae 11 is discharged.
Claims (3)
1. the pre-disk stripping of Novel steam off line, is characterized in that: in evapo-separated machine cylindrical shell (5) inside, be horizontal mode pre-disk stripping (3) is set, pre-disk stripping top is provided with feeding seal screw conveyor (7); Be the position of 180 ° with the main axis of feeding seal screw conveyor, on the base plate that stirs cutter (2) top end near pre-disk stripping, be provided with an oblique discharge port, the outside of discharge port is provided with a receiving hopper (18), the discharging mouth of pipe of receiving hopper (18) is near the pre-delamination of the second layer, but do not affect that the pre-delamination of the second layer is provided with stir cutter rotation; The center of circle of pre-disk stripping (3) is provided with a main shaft (1), and main shaft is provided with and stirs cutter (2); The lower edge that stirs cutter with the base plate of interlayer at the bottom of pre-disk stripping apart from 5mm.
2. the pre-disk stripping of Novel steam off line according to claim 1, is characterized in that: described feeding seal screw conveyor (7), is fixed on evapo-separated machine cylindrical shell (5) by holding bolt (9).
3. the pre-disk stripping of Novel steam off line according to claim 1, is characterized in that: the described cutter (2) that stirs is fastened on main shaft (1) by stirring tool rest (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320490697.6U CN203403076U (en) | 2013-08-13 | 2013-08-13 | Novel pre-separation disc of evapo-separated machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320490697.6U CN203403076U (en) | 2013-08-13 | 2013-08-13 | Novel pre-separation disc of evapo-separated machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203403076U true CN203403076U (en) | 2014-01-22 |
Family
ID=49939014
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320490697.6U Expired - Fee Related CN203403076U (en) | 2013-08-13 | 2013-08-13 | Novel pre-separation disc of evapo-separated machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203403076U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103966017A (en) * | 2014-06-03 | 2014-08-06 | 吉首大学 | Vertical steam removal device for residual solvent in rapeseed meal |
| CN107057841A (en) * | 2017-03-30 | 2017-08-18 | 中粮粮油工业（荆州）有限公司 | A kind of wet dregs of rice steam the isolation between de- tower to DTDC and disconnect device |
-
2013
- 2013-08-13 CN CN201320490697.6U patent/CN203403076U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103966017A (en) * | 2014-06-03 | 2014-08-06 | 吉首大学 | Vertical steam removal device for residual solvent in rapeseed meal |
| CN107057841A (en) * | 2017-03-30 | 2017-08-18 | 中粮粮油工业（荆州）有限公司 | A kind of wet dregs of rice steam the isolation between de- tower to DTDC and disconnect device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105219514B (en) | The treatment process and refine system automatically that a kind of Non-intermittent formula commercial grease refines | |
| CN107446599B (en) | Vertical pyrolysis device of solid organic waste | |
| CN105135852A (en) | Continuous drying system for three-waste comprehensive recycling treatment | |
| CN106434233A (en) | Intelligent control system and control method of liquor production | |
| CN113209927B (en) | Full-automatic environment-friendly cellulose ether production device and synthesis process thereof | |
| CN203403076U (en) | Novel pre-separation disc of evapo-separated machine | |
| CN107189863A (en) | A kind of spent bleaching clay nuisanceless disposal Processes and apparatus | |
| CN107777858A (en) | A kind of sludge freezing prilling process and device | |
| CN105157399B (en) | The segmentation dehydration drying system of high humidity coal and using method thereof | |
| CN209816109U (en) | Anaerobic fermentation system for kitchen waste | |
| CN103387841A (en) | Papermaking waste residue oil refining drying and cracking unit | |
| CN107814472A (en) | A kind of sludge drying processing method and device | |
| CN103849524A (en) | Mechanical automatic production line for strong-flavor type liquor brewing | |
| CN103913049B (en) | The continuous drying system of slurry or powder | |
| CN108800883B (en) | Stone mill flour secondary heating and three-effect continuous drying equipment and working method thereof | |
| CN203021526U (en) | Special tea seed cake evapo-separated machine | |
| CN101408371A (en) | Hot plate type continuous vacuum drying system | |
| CN103805333A (en) | Desolventizer toaster special for tea seed meal | |
| CN104087343A (en) | Slag discharging device of coal gas generator | |
| CN105886115A (en) | Method for ordinary pressure continuous extraction of grease from schizochytrium limacinum cake and equipment thereof | |
| CN104371821A (en) | Novel pre-separation disc of evapo-separated machine | |
| CN103602342A (en) | Charging equipment in shaft kiln system of coal chemical industry and charging method | |
| CN203411507U (en) | Drying and cracking device for refining oil from papermaking waste residues | |
| CN204944131U (en) | The segmentation dehydration drying system of high humidity coal | |
| CN203403078U (en) | Automatic scraping plate type animal grease refining machine |
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: 20140122 Termination date: 20160813 |