CN205216259U - Plant is drawed system filter and draws system system of straining - Google Patents
Plant is drawed system filter and draws system system of straining Download PDFInfo
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- CN205216259U CN205216259U CN201520742828.4U CN201520742828U CN205216259U CN 205216259 U CN205216259 U CN 205216259U CN 201520742828 U CN201520742828 U CN 201520742828U CN 205216259 U CN205216259 U CN 205216259U
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Abstract
The utility model discloses a plant is drawed system filter and draws system system of straining, the plant is drawed the system filter and includes slurry tank, slurry tank's box is equipped with feed inlet, inlet, row's cinder notch and thick liquid export, and the radial direction along slurry tank in the slurry tank is provided with a baffle, and the baffle left side is the slurrying district, and the right side is the filtering area, feed inlet and inlet setting are distinguished in slurrying, the filtering area is equipped with the filter chamber, the thick liquid export sets up on the filtering area box in the filtering area outside, arranges cinder notch and filter chamber intercommunication, set up the spout hole on the baffle, the spout hole with the filter chamber intercommunication. The utility model discloses possess the integrative function of slurrying, filter pulp, mainly accomplishes in the plant extraction process solvent and to the dissolving and the residue separation of plant powder, realized the production process serialization, make slurrying, filter an organic whole completion.
Description
Technical field
The utility model relates to a kind of plant extract filter and extracts filter system processed, can be used for the pharmacy or other industry field that need plant extract.
Background technology
Plant extract technology is widely used in pharmacy and other industry field, present extraction equipment adopts single batch, discontinuous production mostly, price is high, production efficiency is lower, current plant extract raw material used needs through having bad luck, and can produce a large amount of dust in process of production, the working environment of staff is poor, the waste of part material also can be caused in the process of having bad luck
Utility model content
The problem that the production efficiency caused due to " single batch and discontinuous produce " in order to the plant extract that solves prior art is low, and in existing plant extract, producing the technical problem of a large amount of dust, the utility model provides a kind of plant extract filter and extracts filter system processed.
The utility model provides following technical scheme:
Plant extract filter, its special character is: comprise slurry tank;
The casing of slurry tank is provided with charging aperture, inlet, slag-drip opening and serum outlet, and the radial direction along slurry tank in slurry tank is provided with a dividing plate, and be slurrying district on the left of dividing plate, right side is filtering area;
Described charging aperture and inlet are arranged on slurrying district;
Described filtering area is provided with filter chamber, and described serum outlet is arranged on the filtering area casing outside filtering area, and slag-drip opening is communicated with filter chamber;
Described dividing plate arranges spout hole, and spout hole is communicated with described filter chamber.
The right side of above-mentioned filter chamber is connected with the right side casing of slurry tank, and the right side of filter chamber is provided with helical guide groove, and the right-hand member of helical guide groove is connected with slag-drip opening.
Above-mentioned plant extract filter also comprises slurry pump, and the inlet of slurry pump is connected with described slurrying district, and liquid outlet is connected with described filter chamber.
Be provided with in above-mentioned slurrying district and stir slurry rotor, stir that slurry rotor comprises rotating shaft, the revolver spoke be fixed in rotating shaft, right spoke and main stir plate, mainly stir plate and be fixedly connected with right spoke with revolver spoke;
Described master stirs plate and comprises slurrying transverse slat, slurrying web and guide vane; Guide vane and slurrying web are separately fixed at slurrying transverse slat both sides; Slurrying transverse slat is vertical with slurrying web;
Guide vane comprises forward blade and backward vane, and forward blade is β, β with the main angle stirred on plate length direction is acute angle; Reverse guide vane is γ, γ with the main angle stirred on plate length direction is obtuse angle.
Above-mentioned master stirs plate 6, and 3 master's guide vanes stirred on plate are forward blade, other 3 masters stir on plate guide vane comprise forward blade and backward vane, forward blade is arranged near filter chamber;
It is first mainly stir plate that the master that the main guide vane stirred on plate is forward blade stirs plate, main stir on plate guide vane to comprise forward blade and backward vane be second mainly stir plate, first mainly stirs plate and the second main plate interval of stirring is arranged.
The guide vane that each master stirs on plate all has 12; The master's forward blade stirred on plate being simultaneously provided with forward blade and backward vane has 4, backward vane has 8; Distance between the backward vane that Distance geometry between adjacent forward blade is adjacent is 50-80mm, and the distance between adjacent forward blade and backward vane is 50-100mm;
Described β is 30 °-70 °, and γ is 110 °-150 °.
Above-mentioned plant extract filter also comprises drive unit, and drive unit is for driving described axis of rotation.
Plant extract system filter system, its special character is: comprise above-mentioned plant extract filter, also comprise storage tank, conveyer, fluid reservoir and liquid feeding pump, storage tank is connected with described charging aperture by conveyer, and fluid reservoir is connected with described inlet by liquid feeding pump.
Above-mentioned conveyer is conveying worm.
Above-mentioned plant extract filter also comprises stock pump, and the inlet going out stock pump is connected with described serum outlet.
The utility model has following technique effect:
Plant extract filter of the present utility model possesses slurrying, filter pulp one function simultaneously, mainly to complete in plant extract technique solvent and is separated the dissolving of plant powder and residue, achieve production process serialization, makes slurrying, filtration integratedly to complete.
Plant extract system filter system of the present utility model reaches optimal seal in operation process, a large amount of dust can not be produced in preparation process, improve dust pollution question, there is slurrying, filter pulp one function, substantially increase production efficiency, reduce labour intensity, improve the working environment of relevant staff, this system has reliable, simple to operate, the feature of easy to maintenance, less pollution.
The utility model can be used for the consecutive production of plant extract technique, can make the vegetable slurries of required concentration simultaneously, go back cocoa and be widely used in the industry such as pharmacy, cosmetics.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the main structure side view stirring plate;
Fig. 3 is that guide vane is at the main distribution map stirred on plate;
Wherein, a be guide vane distribution 1, b be guide vane distribution 2, c be guide vane distribution 3, d be guide vane distribution 4, e be guide vane distribution 5, f be guide vane distribution 6;
Fig. 4 is the A-A view of Fig. 1;
Wherein, a be guide vane distribution 1, b be guide vane distribution 2, c be guide vane distribution 3, d be guide vane distribution 4, e be guide vane distribution 5, f be guide vane distribution 6;
Fig. 5 is the schematic diagram of plant extract system filter system;
Reference numeral: 1-slurry pump, 2-charging aperture, 3-slurrying district, 4-dividing plate, 5-spout hole, 6-filtering area, 7-serum outlet, 8-drive unit, 9-inlet, 10-guide vane, 11-slurry tank, 12-helical guide groove, 13-slag-drip opening, 16-guide vane, 14-slurrying transverse slat, 15-slurrying web, 16-stirs slurry rotor.
Detailed description of the invention
As shown in Figure 1 to Figure 4, plant extract filter of the present utility model, comprises slurry tank 11;
The casing of slurry tank is provided with charging aperture 2, inlet 9, slag-drip opening 13 and serum outlet 7, and the radial direction along slurry tank in slurry tank is provided with a dividing plate 4, and be slurrying district 3 on the left of dividing plate, right side is filtering area 6;
Charging aperture and inlet are arranged on slurrying district; Filtering area is provided with filter chamber, and described serum outlet is arranged on the filtering area casing outside filtering area, and slag-drip opening is communicated with filter chamber; Dividing plate is arranged spout hole 5, spout hole is communicated with filter chamber.
The right side of filter chamber is connected with the right side casing of slurry tank, and the right side of filter chamber is provided with helical guide groove, and the right-hand member of helical guide groove is connected with slag-drip opening.
The utility model also comprises slurry pump 1 and goes out stock pump, and the inlet of slurry pump is connected with slurrying district, and liquid outlet is connected with filter chamber, and plant extract filter also comprises drive unit, and drive unit is used for drive shaft and rotates.
Slurrying district is a whirligig that can form swell type slurries, is provided with and stirs slurry rotor 16 in slurrying district, stirs that slurry rotor comprises rotating shaft, the revolver spoke be fixed in rotating shaft, right spoke and main stir plate, mainly stirs plate and is fixedly connected with right spoke with revolver spoke; Master stirs plate and comprises slurrying transverse slat 14, slurrying web 15 and guide vane 16; Guide vane and slurrying web are separately fixed at slurrying transverse slat both sides; Slurrying transverse slat is vertical with slurrying web;
Guide vane comprises forward blade and backward vane, and forward blade is β, β with the main angle stirred on plate length direction is acute angle; Reverse guide vane is γ, γ with the main angle stirred on plate length direction is obtuse angle, and wherein, β is 30 °-70 °, and γ is 110 °-150 °.
Main stir plate and have 6,3 master's guide vanes stirred on plate are forward blade, other 3 masters stir on plate guide vane comprise forward blade and backward vane, forward blade is arranged near filter chamber; It is first mainly stir plate that the master that the main guide vane stirred on plate is forward blade stirs plate, main stir on plate guide vane to comprise forward blade and backward vane be second mainly stir plate, first mainly stirs plate and the second main plate interval of stirring is arranged.
The guide vane that each master stirs on plate all has 12; The master's forward blade stirred on plate being simultaneously provided with forward blade and backward vane has 4, backward vane has 8;
Control material movement speed by different forward blade and backward vane quantity and angle layout, reach optimal dissolution effect.This version has reliable, steady, energy continuous slurrying, and service efficiency is high, is convenient to the feature safeguarded and keep in repair.
In order to both ensure carrying out smoothly of the utility model deslagging work, avoid again slag body wearing and tearing guide vane, distance between the backward vane that Distance geometry between the forward blade that the utility model is adjacent is adjacent is 50-80mm, and the distance between adjacent forward blade and backward vane is 50-100mm; Forward blade makes material move to slag notch, and backward vane makes material to the motion of charging aperture direction, and ensure that slag body, bulk particle can not be discharged rapidly, but is being discharged in filter chamber after being dissolved fully in slurry tank, discharges after filtration after device.
Based on the plant extract system filter system of plant extract filter of the present utility model, as Fig. 5, comprise storage tank, conveyer, fluid reservoir and liquid feeding pump, storage tank is connected with described charging aperture by conveyer, and fluid reservoir is connected with described inlet by liquid feeding pump.
Conveyer adopts conveying worm.Conveying worm operation principle is simple, it operationally, rely on the motive force of helical blade, by product smooth delivery of power to appointed place, be widely used, it is simple that conveying worm has structure, manufacture cost low, sealing be strong, the advantage such as easy-to-operate, centre can Multi point mounting, dismounting material, can convey materials in the vertical direction, and take up an area very little; Can carry out work in full-closed shell, bad-looking dust, avoids contaminated environment.
Plant extract system filter system also comprises stock pump, and the inlet going out stock pump is connected with described serum outlet, and the liquid outlet going out stock pump is communicated to subsequent processing.
Plant extract system filter system of the present utility model also comprises reflux pump, and the inlet of reflux pump is communicated between described serum outlet and the inlet going out stock pump, and the liquid outlet of reflux pump is communicated on the filtering area casing outside filtering area.
The operation principle of plant extract system filter system of the present utility model:
According to the concentration of slurry of preparation, calculate the proportionate relationship of raw material and respective liquid solvent, the transporting velocity of conveyer be set,
Then, pour the plant material pulverized into storage tank, the liquid flux of needs is added in fluid reservoir, raw material is by material rotary valve and conveyer (employing conveying worm), slurrying district is entered into from the charging aperture of slurry tank, liquid flux by liquid feeding pump by liquid from fluid reservoir, pump to slurrying district by the inlet of slurry tank, raw material mixes according to the slurrying district of required ratio at plant extract filter of the present utility model with liquid flux, and the pulping process in slurrying district is as follows:
Under the power drive of drive unit, under the driving of power, stir slurry rotor turns, its main plate that stirs is driven to rotate, master stirs plate rotating band action-oriented blade rotation, and in the process of stirring slurry rotor turns, master stirs plate and guide vane constantly pats impingement mix thing continuously, stir slurries, mixture is rolled up and down, and wave superposes, and makes material and the abundant mixed dissolution of liquid, the guide vane of different angles makes slurries surge rotation, liquid in impingement box.Slurries mixture, under the effect of gravity and all directions power, presents the turbulent wave of swell type, makes to produce strong collision between slurries mixture in whole slurrying district.Owing to constantly impacting between solid particle and liquid and washing away, accelerate dissolving of raw material, the utilization rate of raw material is improved.
The spout hole of slurries on dividing plate in slurrying district enters in the filter chamber of filtering area, and through filtering, the slurries made are by pulp transport pump to subsequent processing, and plant residue is discharged by slag-drip opening by helical guide groove, guarantee that equipment running process is clean.After equipment quits work, slurrying district residue slurries are sent into filter chamber by slurry pump and are filtered, and can not cause waste.
Claims (10)
1. plant extract filter, is characterized in that: comprise slurry tank;
The casing of slurry tank is provided with charging aperture, inlet, slag-drip opening and serum outlet, and the radial direction along slurry tank in slurry tank is provided with a dividing plate, and be slurrying district on the left of dividing plate, right side is filtering area;
Described charging aperture and inlet are arranged on slurrying district;
Described filtering area is provided with filter chamber, and described serum outlet is arranged on the filtering area casing outside filtering area, and slag-drip opening is communicated with filter chamber;
Described dividing plate arranges spout hole, and spout hole is communicated with described filter chamber.
2. plant extract filter according to claim 1, is characterized in that: the right side of described filter chamber is connected with the right side casing of slurry tank, and the right side of filter chamber is provided with helical guide groove, and the right-hand member of helical guide groove is connected with slag-drip opening.
3. plant extract filter according to claim 2, is characterized in that: described plant extract filter also comprises slurry pump, and the inlet of slurry pump is connected with described slurrying district, and liquid outlet is connected with described filter chamber.
4. the plant extract filter according to claim 1 or 2 or 3, it is characterized in that: be provided with in described slurrying district and stir slurry rotor, stir that slurry rotor comprises rotating shaft, the revolver spoke be fixed in rotating shaft, right spoke and main stir plate, mainly stir plate and be fixedly connected with right spoke with revolver spoke;
Described master stirs plate and comprises slurrying transverse slat, slurrying web and guide vane; Guide vane and slurrying web are separately fixed at slurrying transverse slat both sides; Slurrying transverse slat is vertical with slurrying web;
Guide vane comprises forward blade and backward vane, and forward blade is β, β with the main angle stirred on plate length direction is acute angle; Reverse guide vane is γ, γ with the main angle stirred on plate length direction is obtuse angle.
5. plant extract filter according to claim 4, it is characterized in that: described master stirs plate 6,3 master's guide vanes stirred on plate are forward blade, other 3 masters stir on plate guide vane comprise forward blade and backward vane, forward blade is arranged near filter chamber;
It is first mainly stir plate that the master that the main guide vane stirred on plate is forward blade stirs plate, main stir on plate guide vane to comprise forward blade and backward vane be second mainly stir plate, first mainly stirs plate and the second main plate interval of stirring is arranged.
6. plant extract filter according to claim 5, is characterized in that: the guide vane that each master stirs on plate all has 12; The master's forward blade stirred on plate being simultaneously provided with forward blade and backward vane has 4, backward vane has 8; Distance between the backward vane that Distance geometry between adjacent forward blade is adjacent is 50-80mm, and the distance between adjacent forward blade and backward vane is 50-100mm;
Described β is 30 °-70 °, and γ is 110 °-150 °.
7. plant extract filter according to claim 6, is characterized in that: described plant extract filter also comprises drive unit, and drive unit is for driving described axis of rotation.
8. plant extract system filter system, it is characterized in that: comprise the arbitrary described plant extract filter of claim 1 to 7, also comprise storage tank, conveyer, fluid reservoir and liquid feeding pump, storage tank is connected with described charging aperture by conveyer, and fluid reservoir is connected with described inlet by liquid feeding pump.
9. plant extract system filter system according to claim 8, is characterized in that: described conveyer is conveying worm.
10. according to claim 8 or claim 9 plant extract system filter system, it is characterized in that: described plant extract filter also comprises stock pump, the inlet going out stock pump is connected with described serum outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520742828.4U CN205216259U (en) | 2015-09-23 | 2015-09-23 | Plant is drawed system filter and draws system system of straining |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520742828.4U CN205216259U (en) | 2015-09-23 | 2015-09-23 | Plant is drawed system filter and draws system system of straining |
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| CN205216259U true CN205216259U (en) | 2016-05-11 |
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| CN201520742828.4U Active CN205216259U (en) | 2015-09-23 | 2015-09-23 | Plant is drawed system filter and draws system system of straining |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126384A (en) * | 2015-09-23 | 2015-12-09 | 西安森兰科贸有限责任公司 | Plant extraction filter and extraction filter system |
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2015
- 2015-09-23 CN CN201520742828.4U patent/CN205216259U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105126384A (en) * | 2015-09-23 | 2015-12-09 | 西安森兰科贸有限责任公司 | Plant extraction filter and extraction filter system |
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