CN201840906U - Faceplate type desolventizing machine - Google Patents
Faceplate type desolventizing machine Download PDFInfo
- Publication number
- CN201840906U CN201840906U CN2010205888219U CN201020588821U CN201840906U CN 201840906 U CN201840906 U CN 201840906U CN 2010205888219 U CN2010205888219 U CN 2010205888219U CN 201020588821 U CN201020588821 U CN 201020588821U CN 201840906 U CN201840906 U CN 201840906U
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- main shaft
- heating plate
- floral disc
- desolventizing
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Abstract
The utility model relates to a faceplate type desolventizing machine. An advance desolventizing layer, a desolventizing layer, a drying layer and a cooling layer are arranged in a cylinder body, a main shaft penetrating through the center of each layer is arranged, the lower part of the main shaft is connected with a power device, the upper part of each layer is correspondingly provided with a stirring knife connected onto the main shaft, the side face of the upper part of the cylinder body is provided with a feeding auger, each layer is correspondingly provided with an automatic control material door, the upper end of the cylinder body is provided with a mixed gas outlet, the mixed gas outlet is correspondingly provided with a dreg foam stopper, one to three layers of faceplates are additionally arranged between the advance desolventizing layer and the desolventizing layer, the faceplates are provided with steam pipeline networks which are fully distributed at one face of a heating plate, a plurality of vent holes are distributed on the heating plate, a center hole and a side blanking hole which penetrate out of the main shaft are remained on the heating plate, and each faceplate is correspondingly provided with a stirring knife and an automatic control material door. After the faceplates are additionally arranged in the utility model, the power consumption is lowered, steam is saved, the consumption of solvents is little, and the product quality of dreg materials is obviously enhanced.
Description
Technical field:
The utility model relates to a kind of floral disc formula desolventizing machine, is mainly used in the precipitation operation in the oil crops extract technologies such as soybean, peanut, cottonseed, vegetable seed, belongs to grease and leaches the complete set of equipments field.
Background technology:
Known desolventizing machine generally has pre-delamination, the precipitation layer, baking zone, several parts of cooling layer are formed, because the precipitation process need just can be finished through the regular hour (25-30min), therefore the material level of every layer of precipitation part will keep thicker material bed, precipitation could be more thorough, particularly precipitation layered material position will keep up to 1000-1300mm, desire to make direct vapour to penetrate the dregs of rice bed of material and deviate from solvent, control direct steam pressure and should reach 0.3-0.4Mpa, and stirring the cutter per minute stirs the material number of times and wants many, the speed of mainshaft (about 20rpm) is very fast, stir the mutual extrusion effect of cutter to dregs of rice material in addition, not only cause the precipitation temperature higher, dregs of rice material color and luster is dark partially, protein content descends in the dregs of rice, and the power consumption height, steam consumption is big, the precipitation effect is not satisfactory, thereby influences the product quality and the market sale of dregs of rice material.
Summary of the invention:
The purpose of this utility model provides a kind of floral disc formula desolventizing machine, thereby solves that power consumption height, steam and solvent consumption that thick, the direct steam pressure height of material level, the speed of mainshaft of every layer of traditional desolventizing machine precipitation part comparatively fast cause reach greatly that dregs of rice material color and luster is dark partially, the technical barrier of protein content decline in the dregs of rice.
The purpose of this utility model realizes as follows: pre-delamination is set in cylindrical shell, the precipitation layer, baking zone, cooling layer, the main shaft that passes each layer center is arranged, the bottom of main shaft is connected with power set, the cutter that stirs that is connected on the main shaft is arranged at corresponding each layer top, corresponding each layer is provided with the automatic control bin gate, the cylindrical shell upper side is provided with feeding packing auger, there is mixed gas outlet the cylindrical shell upper end, corresponding mixed gas outlet is provided with dregs of rice foam stopper, same as the prior art with top, characteristics of the present utility model are to set up 1-3 layer floral disc between pre-delamination and precipitation layer, floral disc is that the one side at heating plate is covered with the jet chimney net, be furnished with some passages on the heating plate, leave the centre bore and the side blanking hole that pass main shaft on the heating plate, cutter and automatic control bin gate are stirred in corresponding each floral disc setting.
During work, floral disc can make steam heat pass to dregs of rice material by heating plate, makes the vaporization of being heated of solvent in the dregs of rice material; After setting up the floral disc layer between pre-delamination and the precipitation layer, make precipitation functional section part dregs of rice materials flow journey lengthening, dregs of rice material upset increased frequency; Every layer of floral disc design has bin gate automatic control mechanism and a lot of passage, can control each floral disc layered material position mist is passed through smoothly; Under the same maintenance prerequisite of necessary precipitation time, every layer dregs of rice material thickness can reduce; Particularly precipitation layer dregs of rice material thickness can reduce half, the direct steam pressure of precipitation layer reduced after also penetrable precipitation layer material; The speed of mainshaft is complied with reduction, stir the cutter per minute and stir the material number of times and tail off, dregs of rice material through pre-delamination and floral disc after, the solvent major part has been vaporized, so the molten load of precipitation pull-up has reduced a lot.
The jet chimney network arrangements of floral disc is below heating plate.
The utility model reduces the desolventizing machine speed of mainshaft, and power consumption descends; Directly steam pressure descends, and saves steam; The mixed gas outlet gas phase temperature descends, and the later process solvent condenses reclaims load and alleviates clearly, and solvent-oil ratio obviously reduces, and the product quality of dregs of rice material obviously improves.
Description of drawings:
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the front view of floral disc of the present utility model.
Fig. 3 is the vertical view of floral disc of the present utility model.
The specific embodiment:
With reference to Fig. 1, Fig. 2, Fig. 3, pre-delamination 4 is set in cylindrical shell 8, precipitation layer 9, baking zone, cooling layer, the main shaft that passes each layer center is arranged, the bottom of main shaft is connected with power set, corresponding each layer top has to be connected stirs cutter 7 on the main shaft, corresponding each layer is provided with automatic control bin gate 13, cylindrical shell 8 upper side are provided with feeding packing auger 3, there is mixed gas outlet 1 cylindrical shell 8 upper ends, corresponding mixed gas outlet 1 is provided with dregs of rice foam stopper 2, corresponding precipitation layer 9 is provided with electric autocontrol device 12 and wind stopping device 11, between pre-delamination 4 and precipitation layer 9, set up 3 layers of floral disc 6, floral disc 6 is covered with jet chimney net 23 below heating plate 22, jet chimney net 23 is provided with steam inlet a and is used to be connected vapour source with steam (vapor) outlet b, be furnished with some passages 24 on the heating plate 22, leave the centre bore and the side blanking hole that pass main shaft on the heating plate 22, corresponding each floral disc 6 is provided with and stirs cutter 7 and automatic control bin gate 13.Some visors 10 are set on cylindrical shell 8 outer walls, and corresponding ground floor and the 3rd layer of floral disc 6 are provided with bin level indicator 5.Dregs of rice material at first enters pre-delamination 4 tops by feeding packing auger 3, feed steam in pre-delamination 4 interlayers to the heating of the solvent in dregs of rice material vaporization, simultaneously each layer stir cutter 7 under main shaft drives constantly to the dregs of rice material stirring seethe, the mist of formation passes dregs of rice foam stopper 2 and is discharged by mixed gas outlet; Under automatic control bin gate 13 effect, control certain technology thickness of feed layer of taking off in advance, and make dregs of rice material enter upper strata floral disc 6; Feed steam in the jet chimney net 23 of floral disc 6, conduct heat to dregs of rice material by heating plate 22, the solvent in the dregs of rice material is further heated vaporization remove, mist passes between pre-delamination 4 and the cylindrical shell 8 peripheral space and dregs of rice foam stopper 2 by mixed gas outlet 1 discharge; Dregs of rice material is discharged to down one deck floral disc 6 by automatic control bin gate 13, use bin level indicator 5 and the certain technology thickness of feed layer of visor 10 controls simultaneously, further to the heating of the solvent in dregs of rice material vaporization, the passage 24 that mist passes in the upper strata floral disc 6 enters in the upper space lower floor's floral disc 6 again; Process according to this, dregs of rice material through 6 heating of three layers of floral disc after, the solvent major part has been vaporized; Dregs of rice material is discharged to precipitation layer 9 by automatic control bin gate 13, realize the thickness of feed layer automatic control by electric autocontrol device 12 and wind stopping device 11, feed direct vapour in precipitation layer 9 interlayer, directly vapour enters dregs of rice material and all takes remaining solvent heating vaporization out of discharging behind drying layer, the cooling layer then.
Claims (2)
1. floral disc formula desolventizing machine, pre-delamination is set in cylindrical shell, the precipitation layer, baking zone, cooling layer, the main shaft that passes each layer center is arranged, the bottom of main shaft is connected with power set, the cutter that stirs that is connected on the main shaft is arranged at corresponding each layer top, corresponding each layer is provided with the automatic control bin gate, the cylindrical shell upper side is provided with feeding packing auger, there is mixed gas outlet the cylindrical shell upper end, corresponding mixed gas outlet is provided with dregs of rice foam stopper, it is characterized in that: between pre-delamination (4) and precipitation layer (9), set up 1-3 layer floral disc (6), floral disc (6) is that the one side at heating plate (22) is covered with jet chimney net (23), be furnished with some passages (24) on the heating plate (22), leave the centre bore and the side blanking hole that pass main shaft on the heating plate (22), corresponding each floral disc (6) setting is stirred cutter (7) and automatic control bin gate (13).
2. floral disc formula desolventizing machine according to claim 1 is characterized in that: the jet chimney net (23) of floral disc (6) is arranged in below the heating plate (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205888219U CN201840906U (en) | 2010-10-20 | 2010-10-20 | Faceplate type desolventizing machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205888219U CN201840906U (en) | 2010-10-20 | 2010-10-20 | Faceplate type desolventizing machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201840906U true CN201840906U (en) | 2011-05-25 |
Family
ID=44035811
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205888219U Expired - Fee Related CN201840906U (en) | 2010-10-20 | 2010-10-20 | Faceplate type desolventizing machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201840906U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102516802A (en) * | 2011-12-12 | 2012-06-27 | 山东凯斯达机械制造有限公司 | Method for extracting capsicum red pigment and capsaicin |
| CN102527081A (en) * | 2011-11-29 | 2012-07-04 | 青岛青大物产股份有限公司 | Evaporation removal device for extracting capsochrome |
| CN102899160A (en) * | 2012-09-29 | 2013-01-30 | 济南中棉生物科技有限公司 | Desolventizing humidifier |
| CN103040080A (en) * | 2013-01-14 | 2013-04-17 | 山东凯斯达机械制造有限公司 | Method for preparing full-fat puffed material |
| CN103497829A (en) * | 2013-09-29 | 2014-01-08 | 东北农业大学 | Vertical evapo-separated machine |
| 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 |
| CN104560373A (en) * | 2013-10-09 | 2015-04-29 | 宁夏琪凯节能设备有限公司 | Novel energy-saving evapo-separated machine |
| CN104673487A (en) * | 2015-03-19 | 2015-06-03 | 艾和美 | Improved toast-desolventizing machine |
| CN114705025A (en) * | 2022-03-14 | 2022-07-05 | 山东凯斯达机械制造有限公司 | Conduction and convection combined type drying device of desolventizer-toaster and using method |
-
2010
- 2010-10-20 CN CN2010205888219U patent/CN201840906U/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527081A (en) * | 2011-11-29 | 2012-07-04 | 青岛青大物产股份有限公司 | Evaporation removal device for extracting capsochrome |
| CN102516802A (en) * | 2011-12-12 | 2012-06-27 | 山东凯斯达机械制造有限公司 | Method for extracting capsicum red pigment and capsaicin |
| CN102899160B (en) * | 2012-09-29 | 2014-02-26 | 济南中棉生物科技有限公司 | Desolventizing humidifier |
| CN102899160A (en) * | 2012-09-29 | 2013-01-30 | 济南中棉生物科技有限公司 | Desolventizing humidifier |
| CN103040080B (en) * | 2013-01-14 | 2015-05-27 | 山东凯斯达机械制造有限公司 | Method for preparing full-fat puffed material |
| CN103040080A (en) * | 2013-01-14 | 2013-04-17 | 山东凯斯达机械制造有限公司 | Method for preparing full-fat puffed material |
| CN103497829A (en) * | 2013-09-29 | 2014-01-08 | 东北农业大学 | Vertical evapo-separated machine |
| CN103497829B (en) * | 2013-09-29 | 2016-04-06 | 东北农业大学 | A kind of vertical type steaming off line |
| CN104560373A (en) * | 2013-10-09 | 2015-04-29 | 宁夏琪凯节能设备有限公司 | Novel energy-saving evapo-separated machine |
| 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 |
| CN104673487A (en) * | 2015-03-19 | 2015-06-03 | 艾和美 | Improved toast-desolventizing machine |
| CN114705025A (en) * | 2022-03-14 | 2022-07-05 | 山东凯斯达机械制造有限公司 | Conduction and convection combined type drying device of desolventizer-toaster and using method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110525 Termination date: 20131020 |