CN203021526U - Special tea seed cake evapo-separated machine - Google Patents
Special tea seed cake evapo-separated machine Download PDFInfo
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- CN203021526U CN203021526U CN 201220591151 CN201220591151U CN203021526U CN 203021526 U CN203021526 U CN 203021526U CN 201220591151 CN201220591151 CN 201220591151 CN 201220591151 U CN201220591151 U CN 201220591151U CN 203021526 U CN203021526 U CN 203021526U
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Abstract
The utility model discloses a special tea seed cake evapo-separated machine. The special tea seed cake evapo-separated machine is provided with three pre-separation layers which are used for pre-separation of most of solvent; a fourth layer is a desolventizing layer and is used for removing the residual solvent, a fifth layer and a sixth layer are drying layers and are used for adjusting water in seed cakes, and the consumption index of the solvent is reduced through the flexibility and tightness of a material door; and the height of a blanking layer can be finely adjusted by adopting an automatic material door; the temperature of preheating and desolventing the seed cakes in the evapo-separated machine is controlled at about 90 DEG C. The phenomena that machine halt caused by seed cake bridging blockage influences normal production is avoided through conveying. Through simplification of the integral structure, the effects of improving performances, prolonging the service life and reducing the maintenance cost of equipment are fulfilled.
Description
Technical field:
This project related products, after being applicable to the leaching of the food oils engineering tea dregs of rice, wet dregs of rice solvent oil removes the special technology field of operation.
Background technology:
At present, needing solvent to steam after the grease processing enterprise food oils raw material of domestic various scales leaches takes off.Because starch content in tea-seed pancake is relatively higher, do not notice that slightly material will conglomeration in equipment; Solvent removal difficulty but also be difficult for blanking not only.Take off material if frequently open inspection manhole, can cause solvent consumption high workshop also dangerous.Especially it is special different from other oil plants that processing is taken off in the solvent oil steaming that contains in the tea dregs of rice.Owing to containing the saponin(e water-swellable conglomeration when steaming precipitation of starch, saponin(e in the tea cake, when steaming is taken off, solvent is not easy to take off totally; Also can feed opening being blocked when conglomeration is excessive, cause serious obstruction.Easily lump after the leached tea oil slag preheating, solvent oil steams and can take off out; Cause and leach molten consumption increasing, increase tooling cost; Be unfavorable for simultaneously the preservation of the tea dregs of rice.The product that this project is related can address the above problem.
The utility model content:
The product that this project is related, the large characteristics of degree of getting out of trouble are steamed in conglomeration easy of leached tea oil slag.Eliminate the phenomenon of evapo-separated machine caking, be not only applicable to the steaming of the tea dregs of rice and take off, steaming is taken off the common oil plants such as cottonseed meal and the dish dregs of rice; Only adjust the material pendulum position of steaming delamination.This product is provided with three layers of pre-delamination, and the wet dregs of rice enter evapo-separated machine and at first use indirect steam heating; Take off in advance most of solvent.The 4th layer is the precipitation layer, and the limit interlayer passes into indirect vapour heating; The superheated vapour that end interlayer sprays into through heating directly contacts stripping with material and goes out residual solvent in the dregs of rice.Precipitation layer solvent gas by-passing out directly enters condenser.Layer 5 and layer 6 are that baking zone is adjusted the moisture in the dregs of rice.The handiness of bin gate is a prerequisite of the normal operation of evapo-separated machine, otherwise is difficult for keeping bed depth or easily causes the excessive motor damage of load and the stopping property of bin gate is directly connected to the consumption indicators of solvent.Adopt automatic material door blanking bed depth to finely tune, stainless steel main part and special sealing material not only guarantee handiness, the wear resistance of bin gate but also can guarantee its stopping property.The pressure that the evapo-separated machine interlayer passes into indirect steam is controlled at 90 ℃ of left and right at 0.5Mpa to the wet dregs of rice between 0.6Mpa carry out the preheating precipitation in evapo-separated machine temperature.Conveying puts up a bridge to stop up to cause to shut down for fear of grouts affects normal production.By simplifying one-piece construction, reach the effect that improves performance, increases the service life, reduces equipment maintenance cost.
Description of drawings:
Below in conjunction with drawings and Examples, the utility model is further illustrated, Fig. 1 is the related product structure schematic diagram of this project.
As shown in Figure 1, steam delamination steam discharge pipe 1, mixed steam outlet 2, top inspection manhole 3, wet dregs of rice import 4, pre-disk stripping 5, thoroughly vapour dish 6, heating plate 7, transmission main shaft 8, fixedly stir cutter 9, directly vapour interlayer 10, stir cutter 11, automatic material door 12, bottom layer discharging mouth 13, pillar 14, step-down gear 15, motor 16, air-cooled interlayer 17, cooling layer 18, baking zone 19, side inspection manhole 20, indirect heating outer ring 21, the high bed of material 22, in advance take off three layer 23, in advance take off two layer 24, take off one deck 25, cylindrical shell 26 compositions in advance.
Embodiment:
The related product of this project as shown in Figure 1, equipment is vertically set in system by four pillars 14; Cylindrical shell 26 be provided with cooling layer 18, baking zone 19, the high bed of material 22, in advance take off three layer 23, in advance take off two layer 24, take off totally six layers of one decks 25 in advance; Every layer all by the staggered discharge port that is provided with in orientation.All be provided with side inspection manhole 20 and automatic material door 12 and indirect heating outer ring 21 at the sidepiece of every layer of cylindrical shell 26, automatic material door 12 is connected with the material pendulum of last layer.Place, 5 millimeters, plane all is provided with and stirs cutter 11 on the cylindrical shell 26 pre-disk strippings 5 of inner distance, saturating vapour dish 6, heating plate 7, direct vapour interlayer 10, air-cooled interlayer 17.Cylindrical shell 26 tops are provided with mixed steam outlet 2, top inspection manhole 3; Be provided with pre-disk stripping 5 taking off in advance one deck 25.Take off in advance one deck 25 internal overhaul problems, entered by top inspection manhole 3.Be provided with in the high bed of material 22 inside and fixedly stir cutter 9, fixedly stir cutter 9 and stir cutter 11 and produce relative movement in the equipment work process; Make the material stirring homogeneous heating of the high bed of material 22 inside, prevent that oil plant from stopping up bin gate because of heating at the inner caking of the high bed of material 22.Be provided with bottom layer discharging mouth 13 at air-cooled interlayer 17, oil plant is cooling is transported to dregs of rice storehouses by discharge port 13.Transmission main shaft went up axle in 8 minutes and lower shaft forms, and utilizes the folder shell that stirs cutter 11 to connect.Transmission main shaft 8 is fixed on air-cooled interlayer 17 and the bearing support that pre-disk stripping 5 is provided with, and is connected with step-down gear 15 by shaft coupling.Motor 16 is connected by associated mode with step-down gear 15; When leach carrying the wet dregs of rice of coming, the sealing spiral conveyer through being arranged on wet dregs of rice import 4 is transported to pre-disk stripping 5 to carry out solvent and takes off in advance; Because cylindrical shell 26 outsides are provided with indirect heating outer ring 21, the inner barrel temperature is raise, make that in the wet dregs of rice in pre-disk stripping 5, solvent oil is converted into gaseous state by liquid state; After discharging, mixed steam outlet 2 carries out recovered solvent oil.Leach the wet dregs of rice because sealing spiral conveyer provides continuously, the cylindrical shell of pre-disk stripping 5 is provided with breach; After stirring heating through stirring cutter, the wet dregs of rice enter from breach and take off in advance one deck 25.Take off in advance one deck 25 and be provided with vapour dish 6, when the material that takes off in advance one deck 25 to certain altitude; Due to the effect of stirring cutter, promote to take off in advance by material the bin gate that material pendulum that one deck 25 is provided with is provided with vapour dish 6 and open; Material enters and takes off in advance two layer 24 from taking off in advance one deck 25.Same effect material takes off three layer 23 in advance from taking off in advance to enter for two layer 24, taking off in advance two layer 24, taking off and be provided with heating plate 7 for three layer 23 and be connected with steam heating with 21 inside, indirect heating outer ring in advance, making solvent oil in the wet dregs of rice become gas and carry out recovered solvent oil through vapour dish 6 thoroughly after mixed steam outlet 2 discharges.Through three grades take off in advance after the wet dregs of rice enter the high bed of material 22, the high bed of material 22 bottoms are provided with the direct vapour interlayer 10 that is connected with steam; Again will there is no the solvent oil of reformed gas by direct superheated vapour and the effect of stirring cutter, carry out thermal conversion.Solvent gas and part water vapour reclaim through steaming delamination steam discharge pipe 1 discharge solvent recovering system.The mass transport of the high bed of material 22 is to baking zone 19, and baking zone 19 bottoms are provided with heating plate 7 and are connected with the steam heating oven dry with 21 inside, indirect heating outer ring; Material after oven dry enters cooling layer 18, and cooling layer 18 is provided with air-cooled interlayer 17, and the cold wind that transports by interlayer carries out cooling to material; Material is cooling is transported to dregs of rice storehouses by bottom layer discharging mouth 13.
Claims (3)
1. tea dregs of rice dedicated steaming off line, its feature: by four pillars (14), vertically arrange; Cylindrical shell (26) be provided with cooling layer (18), baking zone (19), the high bed of material (22), in advance take off three layers (23), in advance take off two layers (24), take off totally six layers of one decks (25) in advance; Every layer all by the staggered discharge port that is provided with in orientation; Sidepiece at every layer of cylindrical shell all is provided with side inspection manhole (20) and automatic material door (12) and indirect heating outer ring (21), and automatic material door is connected with the material pendulum of last layer; Be provided with three layers of pre-delamination, the 4th layer is the precipitation layer, and the limit interlayer passes into indirect vapour heating; The superheated vapour that end interlayer sprays into through heating directly contacts stripping with material and goes out residual solvent in the dregs of rice, and layer 5 and layer 6 are the moisture in the baking zone adjustment dregs of rice.
2. a kind of tea dregs of rice dedicated steaming off line according to claim 1, its feature: the pre-disk stripping of cylindrical shell (26) inner distance (5), thoroughly vapour dish (6), heating plate (7), directly vapour interlayer (10), place, upper 5 millimeters, the plane of air-cooled interlayer (17) all are provided with and stir cutter (11); Be provided with bottom layer discharging mouth (13) at air-cooled interlayer (17).
3. a kind of tea dregs of rice dedicated steaming off line according to claim 1, its feature: be provided with in the high bed of material (22) inside and fixedly stir cutter (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220591151 CN203021526U (en) | 2013-03-12 | 2013-03-12 | Special tea seed cake evapo-separated machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220591151 CN203021526U (en) | 2013-03-12 | 2013-03-12 | Special tea seed cake evapo-separated machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203021526U true CN203021526U (en) | 2013-06-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220591151 Expired - Fee Related CN203021526U (en) | 2013-03-12 | 2013-03-12 | Special tea seed cake evapo-separated machine |
Country Status (1)
| Country | Link |
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| CN (1) | CN203021526U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103468395A (en) * | 2013-09-02 | 2013-12-25 | 东北农业大学 | Vacuum wet meal desolventizing system |
| CN103977597A (en) * | 2014-06-02 | 2014-08-13 | 吉首大学 | Device for vertically evaporating residual solvents in eucommia ulmoides husks |
| CN104479860A (en) * | 2014-12-14 | 2015-04-01 | 博乐市家乐油脂有限责任公司 | Method for drying and desolventizing cottonseed meal and special drying and desolventizing equipment of method |
| CN109609262A (en) * | 2018-12-13 | 2019-04-12 | 太仓市宝马油脂设备有限公司 | A kind of wet dregs of rice evapo-separated machine |
-
2013
- 2013-03-12 CN CN 201220591151 patent/CN203021526U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103468395A (en) * | 2013-09-02 | 2013-12-25 | 东北农业大学 | Vacuum wet meal desolventizing system |
| CN103977597A (en) * | 2014-06-02 | 2014-08-13 | 吉首大学 | Device for vertically evaporating residual solvents in eucommia ulmoides husks |
| CN103977597B (en) * | 2014-06-02 | 2016-01-06 | 吉首大学 | A kind of vertical type steaming takes off the device of residual solvent in bark of eucommia shell |
| CN104479860A (en) * | 2014-12-14 | 2015-04-01 | 博乐市家乐油脂有限责任公司 | Method for drying and desolventizing cottonseed meal and special drying and desolventizing equipment of method |
| CN109609262A (en) * | 2018-12-13 | 2019-04-12 | 太仓市宝马油脂设备有限公司 | A kind of wet dregs of rice evapo-separated machine |
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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 |
Granted publication date: 20130626 Termination date: 20160312 |
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| CF01 | Termination of patent right due to non-payment of annual fee |