CN106381221A - Leaching mechanism and leaching device - Google Patents
Leaching mechanism and leaching device Download PDFInfo
- Publication number
- CN106381221A CN106381221A CN201611017456.4A CN201611017456A CN106381221A CN 106381221 A CN106381221 A CN 106381221A CN 201611017456 A CN201611017456 A CN 201611017456A CN 106381221 A CN106381221 A CN 106381221A
- Authority
- CN
- China
- Prior art keywords
- leaching
- hopper
- feed liquor
- conveying unit
- extractant
- 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.)
- Granted
Links
- 230000007246 mechanism Effects 0.000 title claims abstract description 98
- 238000002386 leaching Methods 0.000 title claims abstract description 92
- 239000000463 material Substances 0.000 claims abstract description 75
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 238000005273 aeration Methods 0.000 claims description 14
- 238000004891 communication Methods 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 2
- 239000007921 spray Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 38
- 238000000605 extraction Methods 0.000 abstract description 20
- 238000010298 pulverizing process Methods 0.000 abstract description 6
- 238000005507 spraying Methods 0.000 abstract description 3
- 239000003921 oil Substances 0.000 description 25
- 230000000694 effects Effects 0.000 description 9
- 238000000034 method Methods 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000008187 granular material Substances 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 238000000638 solvent extraction Methods 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000346 nonvolatile oil Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention relates to a leaching mechanism and a leaching device, which belong to the technical field of leaching devices for effective constitutions of plants. The leaching mechanism comprises a hopper (1), and is characterized in that a liquid feeding mechanism used for spraying an extraction agent into the hopper (1) is arranged on the lower part of the hopper (1); an overflow channel (3) is arranged on the upper part of the hopper (1). The leaching mechanism can be used for extracting pulverizing extra fine material particles, the problem that the material particles block the bottom part of the leaching mechanism is avoided, the oil extraction rate of the materials is greatly improved, and the material particles can be favorably settled and are prevented from overflowing along with the extraction agent; the leaching device can be used for extracting the material particles repeatedly, so that the oil extraction rate of the materials is greatly improved; in addition, the leaching mechanism can adapt to the material particles with smaller particle size, so that the oil extraction rate of the materials is further improved, and the extraction efficiency is greatly improved.
Description
Technical field
A kind of leaching mechanism and leaching device, belong to effective ingredients in plant leaching equipment technical field.
Background technology
Edible oil is divided into expressed oil and leaches two kinds of oil, and expressed oil obtains oil using the mode of extruding, and leaching oil is to use
Some extractants obtain oil.The oil yield of solvent extraction method is high and low cost, therefore solvent extraction method are to extract the main production of big oil plant
Method.Material typically required pulverizing before leaching oil, then the big oil plant after pulverizing was placed in leaching mechanism, and to leaching
Go out addition extractant in mechanism, the oil in material is extracted by extractant, and flow out leaching mechanism through leaching the bottom of mechanism.
The oil yield of solvent extraction method can be affected by the material particles size after pulverizing, and material particles are less, and the oil yield leaching oil is got over
Height, but little material particles can block the bottom leaching mechanism, so that the big oil plant extracting cannot flow out in time.Cause
This, existing leaching mechanism, when using, in order to avoid blocking to leaching actuator base, generally deliberately can make pulverizing when pulverizing
Material particles afterwards are larger, thus leading to the oil yield of material to reduce.
Content of the invention
The technical problem to be solved in the present invention is：Overcome the deficiencies in the prior art, provide one kind it can be avoided that material particles
The leaching mechanism high to leaching actuator base blocking, material oil yield and leaching device.
The technical solution adopted for the present invention to solve the technical problems is：This leaching mechanism, including hopper, its feature exists
In：The bottom of described hopper is provided with the feed liquor mechanism for spraying into extractant into hopper, and the top of hopper is provided with overflow and leads to
Road.
Preferably, described feed liquor mechanism includes multiple aeration heads or multiple shower nozzle, and the bottom of hopper is sealed by installing plate
Close, aeration head or shower nozzle are arranged on the upside of installing plate, multiple aeration heads or shower nozzle pass through pipeline communication.
Preferably, described feed liquor mechanism includes feed liquor bucket and microwell plate, feed liquor bucket be arranged on the downside of hopper and with material
The lower seal of bucket connects, and microwell plate is arranged between hopper and feed liquor bucket and closes the bottom of hopper, and feed liquor bucket is provided with
Inlet.
Preferably, described microwell plate is with ceramic capillary plate or metal micro-holes plate.
Preferably, described overflow ducts are provided with filter.
Preferably, described overflow ducts are arranged on hopper side surface upper part.
Preferably, the cross-sectional area of described hopper is gradually increased from the bottom to top.
A kind of leaching device it is characterised in that：Power list including circulation conveying unit, drive circulation conveying unit rotational
First and above-mentioned leaching mechanism, the hopper leaching mechanism is arranged on circulation conveying unit top and moves with circulation conveying unit
Dynamic, feed liquor mechanism is arranged on the downside of circulation conveying unit, and leaching mechanism follows ring supply unit and is provided with multiple, feed liquor mechanism installation
On the downside of circulation conveying unit, material leaches mechanism through one and enters, and extracts successively through the in-house extractant of multiple leaching.
Preferably, also include the casing of annular, be interval with polylith riser in casing, thus casing is separated into multiple institutes
State hopper, overflow ducts are arranged on casing and are corresponded with feed liquor mechanism；Circulation conveying unit is connected with riser, and drives
Riser moves.
Preferably, often the two neighboring described inlet of leaching mechanism and overflow ducts are connected by circulating line, extraction
Agent is taken to be overflowed by the overflow ducts of the described leaching mechanism adding material, by the leaching along circulation supply unit conveying direction end
The inlet of mechanism enters.
Compared with prior art, the present invention is had an advantageous effect in that：
1st, the feed liquor mechanism of this leaching mechanism is arranged on hopper bottom, and overflow ducts are arranged on the top of hopper, and extractant is by expecting
Bucket bottom enters and is overflowed by hopper top such that it is able to extract to the very thin material particles pulverized, and is not in thing
Material granule to leach actuator base blocking problem, substantially increase the oil yield of material, and extractant have bottom enter, on
Portion overflows, and makes to be full of extractant in whole hopper, is conducive to the sedimentation of material particles, it is to avoid material particles overflow with extractant,
Effect of extracting is good.
2nd, extractant can be sprayed in hopper by aeration head or shower nozzle by the bottom of hopper, the extraction being sprayed due to feed liquor mechanism
Take agent to have certain flow velocity such that it is able to play stirring action to material particles, improve effect of extracting.
3rd, extractant enters in feed liquor bucket, and the micropore crossing microwell plate is entered material bin such that it is able to make the spray of extractant
In material bin, and then impacting and stirring to the material in hopper, mixing effect is good, and rate of extraction is fast.
4th, the cross-sectional area of hopper is gradually increased from the bottom to top, so that the extractant on top is tended towards stability such that it is able to make extraction
Take in agent hopper and gradually settle out, be conducive to the sedimentation of material particles, it is to avoid material particles overflow with extractant.
5th, this leaching device repeatedly can be extracted to material particles, thus substantially increasing the oil yield of material, and
And leaching mechanism can adapt to the less material particles of granularity, thus further increasing the oil yield of material, also greatly improves
The efficiency of extraction, and when using easy to operate.
6th, multiple leaching mechanisms in series, and extractant are entered by the inlet of the leaching mechanism of end, by entrance material
Leaching mechanism overflow ducts overflow such that it is able to make the concentration highest extractant material particles most to oil content carry out
Extraction, defines counterflow leaching it is ensured that effect of extracting, thus maximized extracting will be had in material particles.
Brief description
Fig. 1 is the schematic front view leaching mechanism.
Fig. 2 is the schematic top plan view leaching mechanism.
Fig. 3 is the schematic front view of adverse current in-out apparatus.
Fig. 4 is the partial enlarged drawing at A in Fig. 3.
Fig. 5 is the schematic front view of leaching device in embodiment 2.
Fig. 6 is the schematic front view of leaching device in embodiment 3.
Fig. 7 is the schematic front view leaching mechanism in embodiment 4.
Fig. 8 is the schematic front view leaching mechanism in embodiment 5.
In figure：1st, hopper 2, feed liquor bucket 3, overflow ducts 4, inlet 5, microwell plate 6, casing 7, leaching
Mechanism 8, charging aperture 9, discharging opening 10, drag chain 11, riser.
Specific embodiment
Fig. 1 ~ 4 are highly preferred embodiment of the present invention, and 1 ~ 8 the present invention will be further described below in conjunction with the accompanying drawings.
A kind of leaching mechanism, including hopper 1, the bottom of hopper 1 is provided with the liquid filling machine for spraying into extractant into hopper 1
Structure, the top of hopper 1 is provided with overflow ducts 3.The feed liquor mechanism of this leaching mechanism 7 is arranged on hopper 1 bottom, and overflow ducts 3 set
Put the top in hopper 1, extractant by hopper 1 bottom enter and by hopper 1 top overflow such that it is able to pulverize very thin
Material particles are extracted, and are not in the problem to the bottom blocking of leaching mechanism 7 for the material particles, substantially increase going out of material
Oil cut rate, and extractant has bottom to enter, top is overflowed, and makes to be full of extractant in whole hopper 1, is conducive to the heavy of material particles
Fall, it is to avoid material particles overflow with extractant, effect of extracting is good.
Embodiment 1
As shown in Figure 1 and 2：Feed liquor mechanism includes feed liquor bucket 2 and microwell plate 5, and feed liquor bucket 2 is arranged on the bottom of hopper 1, microwell plate 5
It is arranged on feed liquor bucket 2 upside the upside closing by feed liquor bucket 2.
Hopper 1 is all uncovered cylinder of upper and lower ends, and feed liquor bucket 2 is inverted positive quadrangular frustum pyramid shaped, and feed liquor bucket 2 is also upper
The cylinder of lower open at both ends.
Microwell plate 5 is provided with multiple micropores, and microwell plate 5 can allow for extractant and passes through, and can stop material particles simultaneously
Pass through.Microwell plate 5 can be ceramic wafer or the metallic plate being evenly equipped with micropore.Microwell plate 5 is nanoscale, preferably micron order（Micro-
The aperture in hole is more than 1um）Such that it is able to extract to nano level granule.Microwell plate 5 may be replaced by screen or hole
Plate, when the granularity of material particles is larger, during using screen or orifice plate, it is possible to increase the circulation rate of extractant, thus improve
Extraction efficiency.
Inlet 4 is arranged on feed liquor bucket 2, is preferably provided at the bottom of inlet 4, and extractant is entered by inlet 4, and
And enter in material bin through microwell plate 5 after full of feed liquor bucket 2.Because extractant has certain pressure, enter back in hopper 1
When can in hopper 1 material particles produce impact, thus serve to material particles stirring effect, make material particles and extraction
Take the more uniform of agent mixing, improve the efficiency of extraction, inlet 4 is arranged on the downside of feed liquor bucket 2, extractant enter into
Directly enter in material bin 1 such that it is able to avoid feed liquor bucket 2 side wall that the flow velocity of extractant is caused to subtract through microwell plate 5 after liquid bucket 2
Slow.
Hopper 1 side surface upper part is provided with overflow ducts 3, in the present embodiment, before overflow ducts 3 are symmetricly set on hopper 1
Both sides afterwards.Overflow ducts 3 are provided with filter such that it is able to filter to the extractant overflowing hopper 1, it is to avoid in the oil plant of extraction
Containing impurity.
As shown in Fig. 3 ~ 4：This leaching device includes circulation conveying unit, drives the power unit of circulation conveying unit rotational
And above-mentioned leaching mechanism 7, leach mechanism 7 hopper 1 be arranged on circulation conveying unit top and with circulation conveying unit move
Dynamic, feed liquor mechanism is arranged on the downside of circulation conveying unit, leaches mechanism 7 and is provided with multiple, feed liquor mechanism peace along circulation supply unit
It is contained on the downside of circulation conveying unit, material leaches mechanism 7 through one and enters, and through multiple extractants leaching in mechanism 7 successively
Extraction.This leaching device repeatedly can be extracted to material particles, thus substantially increasing the oil yield of material, and leaches
Mechanism 7 can adapt to the less material particles of granularity, thus further increasing the oil yield of material, also substantially increases extraction
Efficiency, and easy to operate when using.
Also include the casing 6 of vertically arranged annular, the section of casing 6 is rectangle, and circulation conveying unit is arranged on case
In body 6.It is interval with polylith riser 11, the length of riser 11 is equal to or slightly less than the length in casing 6 section, riser in casing 6
11 width is equal to or slightly less than the width in the section of casing 6, thus forming multiple hoppers 1 in casing 6.Circulation conveying unit
For drag chain 10, drag chain 10 is connected with riser 11 and drives riser 11 mobile, thus driving material to move.Casing 6 upper left-hand sets
Have soft baffle plate, soft baffle plate is fixed on casing 6, when drag chain 10 drive riser 11 to take exercises when, soft baffle plate can be under riser 11
Side is closed, it is to avoid extractant enters in the casing 6 of downside along gap, so that extractant forms concentration ladder in casing 6
Spend different extractants.
Along the conveying direction interval setting of drag chain 10, drag chain 10 rotates around the axle of level for multiple mechanisms 7 that leach.Upper right end
Leaching mechanism 7 hopper 1 suitable for reading for charging aperture 8, material particles by upper right end leaching mechanism 7 hopper 1 addition suitable for reading,
Drag chain 10 drives material to move, thus driving material particles to be moved to the left and sequentially passing through multiple leaching mechanisms 7, and under process
After the leaching mechanism 7 of portion's right-hand member, discharged by discharging opening 9.
In the leaching mechanisms 7 of top often adjacent two, the overflow ducts 3 of leaching mechanism 7 in left side and the leaching machine on right side
The inlet 4 of structure 7 connects；In two often adjacent leaching mechanisms 7 of bottom, overflow ducts 3 and the left side of leaching mechanism 7 on right side
Leaching mechanism 7 inlet 4 connect.The overflow ducts 3 of leaching mechanism 7 of bottom left end and the leaching mechanism 7 of upper left end
Inlet 4 connect so that each leach mechanism 7 connect, thus forming circulation line.Two often adjacent leaching mechanisms 7
Between be equipped with circulating pump.Extractant is entered by the inlet 4 of the leaching mechanism 7 along drag chain 10 conveying direction end, by top
The overflow ducts 3 of the leaching mechanism 7 of right-hand member overflow such that it is able to make the concentration highest extractant material minimum to oil content
Grain is extracted the multitple extraction it is achieved that material particles, and effect of extracting is good.
It is provided with the right side of the leaching mechanism 7 of bottom right-hand member and drain machine for suction out the extractant in material particles
Structure, drains mechanism and includes draining room and jet vacuum pump, the room of draining is airtight chamber, and the bottom draining room is provided with micro-
Hole or the loading plate of thin seam.The inlet end of jet vacuum pump and outlet side are all connected with a reserving liquid tank, drain the loading plate of room
The outlet side by pipeline communication jet vacuum pump for the downside, thus inhale draining the extractant being mixed with indoor material.Material
Grain enters and drains interior and be placed on loading plate, and jet vacuum pump is to draining room evacuation such that it is able to make in material particles
Extractant quickly discharge.Compared with freely flowing out with the extractant adopting in prior art, substantially increase the efficiency draining,
And save the energy of drying materials consumption.And the content of effective ingredients in plant is high in the extractant of this leaching device, side
Continue the separation of effective ingredients in plant after an action of the bowels.
Embodiment 2
Embodiment 2 is with the difference of embodiment 1：Feed liquor mechanism includes multiple aeration heads, and aeration head is arranged on the upper of installing plate
Simultaneously uniformly on a mounting board, multiple aeration heads pass through pipeline communication for side.Aeration head could alternatively be shower nozzle.
As shown in Figure 4：Two-layer is separated into by the dividing plate of level, in casing 6 in casing 6 rectangular box body, and casing 6
Two sheaf space interior circulation conveying materials.Riser 11 is matched with the dividing plate of the level in casing 6 side wall and casing 6 respectively, thus
Form multiple hoppers.Being dragged into material mouth 8 is the upper port leaching mechanism 7 hopper 1 being arranged on upper right end, and discharging opening 9 is arranged on
The lower right side of frame 1.Aeration head be arranged on drag chain 10 downside and with drag chain 10 interval setting, thus material can either be driven
Granule moves, and hinders it can be avoided that producing to aeration head.Feed liquor bucket 2 is arranged on the downside of casing 6, is provided with the peace of aeration head
Dress plate is arranged in feed liquor bucket 2, and extractant is sprayed in the hopper 1 in casing 6.
Embodiment 3
As shown in Figure 5：Embodiment 3 is with the difference of embodiment 1：Casing 6 is horizontally disposed annular, and drag chain 10 is around vertical
Axle rotates.The left upper portion of casing 6 is provided with feeding packing auger, and charging aperture 8 is arranged in feeding packing auger.Discharging opening 9 is arranged on right side
Bottom.
Embodiment 4
As shown in Figure 6：Embodiment 4 is with the difference of embodiment 1：Leach mechanism 7 to be used alone, feed liquor bucket 2 is by under hopper 1
Mouth closing, microwell plate 5 is arranged between hopper 1 and feed liquor bucket 2.Leach mechanism 7 and be equipped with circulating pump, the feed tube of circulating pump is simultaneously
Connect with two overflow ducts 3, the drain pipe of circulating pump is connected with inlet 4, so that the extractant leaching in mechanism 7 is formed
Circulation, improves the efficiency of oil plant extraction.Hopper 1 is inverted positive quadrangular frustum pyramid shaped such that it is able to make the material on top tend to steady
Fixed, be conducive to the sedimentation of material.
Embodiment 5
As shown in Figure 7：Embodiment 5 is with the difference of embodiment 1：Hopper 1 is used alone, and the right side of hopper 1 also is provided with micropore
Plate 5, microwell plate 5 is vertically arranged.The right side of hopper 1 is additionally provided with feed liquor bucket 2, and the right side of feed liquor bucket 2 is provided with inlet 4.Extractant
Can enter in material bin 1 such that it is able to stir to material particles from right side and bottom from the bottom of hopper 1 and right side simultaneously
Mix.The lower mouth of hopper 1 is closed by the feed liquor bucket 2 of hopper 1 bottom.
Microwell plate 5 can also be arranged on the both sides of hopper 1 or around the setting of the side of hopper 1, microwell plate 5 can also be gone up
Hold outward-dipping setting.
The above, be only presently preferred embodiments of the present invention, is not the restriction that the present invention is made with other forms, appoints
What those skilled in the art possibly also with the disclosure above technology contents changed or be modified as equivalent variations etc.
Effect embodiment.But every without departing from technical solution of the present invention content, according to the present invention technical spirit to above example institute
Any simple modification, equivalent variations and the remodeling made, still falls within the protection domain of technical solution of the present invention.
Claims (9)
1. a kind of leaching mechanism, including hopper（1）It is characterised in that：Described hopper（1）Bottom be provided with for hopper
（1）Inside spray into the feed liquor mechanism of extractant, hopper（1）Top be provided with overflow ducts（3）.
2. according to claim 1 leaching mechanism it is characterised in that：Described feed liquor mechanism includes multiple aeration heads or many
Individual shower nozzle, hopper（1）Bottom closed by installing plate, aeration head or shower nozzle are arranged on the upside of installing plate, multiple aeration heads
Or shower nozzle passes through pipeline communication.
3. according to claim 1 leaching mechanism it is characterised in that：Described feed liquor mechanism includes feed liquor bucket（2）And
Microwell plate（5）, feed liquor bucket（2）It is arranged on hopper（1）Downside and hopper（1）Lower seal connect, microwell plate（5）It is arranged on
Hopper（1）With feed liquor bucket（2）Between and by hopper（1）Bottom closing, feed liquor bucket（2）It is provided with inlet（4）.
4. according to claim 1 leaching mechanism it is characterised in that：Described overflow ducts（3）It is provided with filter.
5. according to claim 1 leaching mechanism it is characterised in that：Described overflow ducts（3）It is arranged on hopper（1）Side
Face top.
6. the leaching mechanism according to claim 1,2,3 or 5 it is characterised in that：Described hopper（1）Cross-sectional area by
Under supreme be gradually increased.
7. a kind of leaching device it is characterised in that：Power unit including circulation conveying unit, drive circulation conveying unit rotational
And the leaching mechanism described in any one of claim 1 ~ 6（7）, leach mechanism（7）Hopper（1）It is arranged on circulation conveying unit
Top is simultaneously moved with circulation conveying unit, and feed liquor mechanism is arranged on the downside of circulation conveying unit, leaches mechanism（7）Along circulation conveying
Unit is provided with multiple, and feed liquor mechanism is arranged on the downside of circulation conveying unit, and material is through a leaching mechanism（7）Enter, and through many
Individual leaching mechanism（7）Interior extractant extracts successively.
8. leaching device according to claim 7 it is characterised in that：Also include the casing of annular（6）, casing（6）Between interior
Every being provided with polylith riser（11）, thus by casing（6）It is separated into multiple described hoppers（1）, overflow ducts（3）It is arranged on casing
（6）Above and with feed liquor mechanism correspond；Circulation conveying unit and riser（11）It is connected, and drive riser（11）Mobile.
9. leaching device according to claim 7 it is characterised in that：Often two neighboring described leaching mechanism（7）Enter
Liquid mouth（4）And overflow ducts（3）Connected by circulating line, extractant is by the leaching mechanism adding material（7）Overflow ducts
（3）Overflow, by the leaching mechanism along circulation supply unit conveying direction end（7）Inlet（4）Enter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611017456.4A CN106381221B (en) | 2016-11-19 | 2016-11-19 | Leaching mechanism and leaching device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611017456.4A CN106381221B (en) | 2016-11-19 | 2016-11-19 | Leaching mechanism and leaching device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106381221A true CN106381221A (en) | 2017-02-08 |
| CN106381221B CN106381221B (en) | 2023-11-07 |
Family
ID=57957479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611017456.4A Active CN106381221B (en) | 2016-11-19 | 2016-11-19 | Leaching mechanism and leaching device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106381221B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103060085A (en) * | 2013-02-04 | 2013-04-24 | 济南中棉生物科技有限公司 | Total-immersion continuous differential countercurrent extractor |
| CN204134637U (en) * | 2014-10-14 | 2015-02-04 | 江西东鹏新材料有限责任公司 | A kind of modified pollucite Leaching reaction device |
| CN105886118A (en) * | 2016-05-23 | 2016-08-24 | 迈安德集团有限公司 | Extraction technology for loop type extractor |
| CN206428211U (en) * | 2016-11-19 | 2017-08-22 | 王芹 | One kind leaches mechanism and leaching device |
-
2016
- 2016-11-19 CN CN201611017456.4A patent/CN106381221B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103060085A (en) * | 2013-02-04 | 2013-04-24 | 济南中棉生物科技有限公司 | Total-immersion continuous differential countercurrent extractor |
| CN204134637U (en) * | 2014-10-14 | 2015-02-04 | 江西东鹏新材料有限责任公司 | A kind of modified pollucite Leaching reaction device |
| CN105886118A (en) * | 2016-05-23 | 2016-08-24 | 迈安德集团有限公司 | Extraction technology for loop type extractor |
| CN206428211U (en) * | 2016-11-19 | 2017-08-22 | 王芹 | One kind leaches mechanism and leaching device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106381221B (en) | 2023-11-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206428211U (en) | One kind leaches mechanism and leaching device | |
| CN106422420A (en) | Horizontal type oil and water phase separator | |
| CN105689157B (en) | It is a kind of to wave stirring-type floatation equipment with function of sizing mixing certainly | |
| CN204996275U (en) | Photovoltaic module lamination vacuum pump oil gas separator | |
| CN109277206A (en) | A kind of portable three-phase sedimentation disk centrifugal separator inner flow passage structure | |
| CN204093169U (en) | Separator | |
| CN204471656U (en) | The knot screen of plastic bottle sheet | |
| CN105880035B (en) | It is a kind of possess from size mixing and self-defoaming function ore pulp driving stirring-type floatation equipment | |
| CN206887188U (en) | A kind of duster and aluminum liquid purifying device | |
| CN104772231B (en) | A kind of pre- de slime flotation complete set of equipments | |
| CN106381221A (en) | Leaching mechanism and leaching device | |
| CN108392850A (en) | A kind of leaching device and its application method | |
| CN207169111U (en) | A kind of liquid phase separator | |
| CN209501185U (en) | Device for recovering powder in a kind of calcined coke production process | |
| WO2019056826A1 (en) | Extraction device having compact structure | |
| CN207384959U (en) | A kind of processing coating filter device | |
| CN207012617U (en) | A kind of desanding sedimentation device for producing starch | |
| CN207169669U (en) | A kind of oil-gas-water three-phase separation for esterification | |
| CN206168032U (en) | Liquid medicine filter equipment | |
| CN206244731U (en) | A kind of three phases separator | |
| CN211462181U (en) | Continuous separation device for light and heavy phase mixture | |
| CN208340164U (en) | A kind of leaching device | |
| CN206011431U (en) | A kind of ceramic capacitor dielectric porcelain damping device | |
| CN203408501U (en) | Multifunctional slime water treatment tank | |
| CN209530740U (en) | A kind of environmentally friendly production system of pulvis |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |