CN206051548U - A kind of barium strontium salt produces subsequent leaching device - Google Patents
A kind of barium strontium salt produces subsequent leaching device Download PDFInfo
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- CN206051548U CN206051548U CN201620904402.9U CN201620904402U CN206051548U CN 206051548 U CN206051548 U CN 206051548U CN 201620904402 U CN201620904402 U CN 201620904402U CN 206051548 U CN206051548 U CN 206051548U
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- barium strontium
- leaching device
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Abstract
A kind of barium strontium salt produces subsequent leaching device, including the outlet of rotating cylinder cylinder, bearing base, salt slag, flushing water inlet, crude salt charging aperture, the outlet of dense halogen, electronic auger, internal coiling band and flight；Described rotating cylinder cylinder is arranged on bearing base；Described salt slag outlet is located at the high end position of rotating cylinder cylinder with water inlet is rinsed；Described crude salt charging aperture is respectively distributed to the lower position of rotating cylinder cylinder with the outlet of dense halogen；Blanking port is provided with above the electronic auger, described salt slag outlet is on electronic auger；Described internal coiling band is welded on rotating cylinder cylinder with flight, and the internal coiling band uniformly continuous are welded, and the flight is distributed on two sections in the high-end and centre position of rotating cylinder cylinder.The subsequent leaching device of the barium strontium salt production that this utility model is provided, realizes scalable in structure, realizes and automatically control in operation, for the very big convenience that actual production is provided.
Description
Technical field
This utility model is related to a kind of barium strontium salt production leaching device, more particularly to a kind of barium strontium salt production subsequent leaching dress
Put.
Background technology
Brium carbonate is a kind of important industrial chemicals, is mainly used in the adjuvant of ceramic coating, optical glass, electronic ceramics,
The manufacture of various electronic devices and components such as PTC thermistor, capacitor.Strontium carbonate can be used to manufacture color television cathode ray tube, special
PTC thermistor element, electric magnet, strontium ferrite etc., additionally, be additionally operable to the production of pyrotechnics, fluorescent glass, signal flare, papermaking,
Analytical reagent, metal zinc electrolyte are refined etc..
The production process of above-mentioned barium strontium salt, is usually forged through rotary kiln reduction by mined barite or celestite
Thick barium or thick strontium being burnt, then aqueous solution being obtained through leaching, thick barium or thick strontium are exactly soaked in water by leaching process, using its group
Divide the different solubilities in water, make readily soluble component barium sulfide or strontium sulfide dissolving, you can realization is separated with solid residue.State
Interior existing leaching method mainly includes：Spiral dipping vessel, stirs tub leacher, static leacher, hanging basket leacher etc., main
Will be based on static leacher, existing leaching mode has steam and dust is big, and production environment is poor, labor strength
Greatly, automaticity is low, the problems such as energy resource consumption is high.In actual production process, in order to obtain preferably leaching effect, thick barium
Or slightly leaching time of the strontium in water is longer, barium sulfide or strontium sulfide are oxidized easily with air Long contact time, and which is exposed
Process units and produce the severe production environment of a large amount of steam and be also easy to cause the generation of security incident, seriously govern enterprise
The development of industry.Therefore, develop a kind of continuous way leaching device that can improve production to be just particularly important.
Utility model content
This utility model seeks to overcome the shortcomings of existing process units, there is provided the continuous leaching in a kind of barium strontium salt production
Device is taken, the subsequent leaching device can realize the continuous production in production, it is also possible to improve production environment, greatly reduce work
Intensity, reduces production cost, while regulation performance is good, stable operation, simple structure is easily manufactured.
The technical solution of the utility model
A kind of barium strontium salt produces subsequent leaching device, including the outlet of rotating cylinder cylinder, bearing base, salt slag, rinse water inlet,
Crude salt charging aperture, the outlet of dense halogen, electronic auger, internal coiling band and flight；Described rotating cylinder cylinder is arranged on bearing base；Institute
The salt slag outlet stated is located at the high end position of rotating cylinder cylinder with water inlet is rinsed；Described crude salt charging aperture is distinguished with the outlet of dense halogen
It is distributed in the lower position of rotating cylinder cylinder；Blanking port is provided with above the electronic cage, described salt slag outlet is positioned at electric mincing
Long Shang；Described internal coiling band is welded on rotating cylinder cylinder inboard wall with flight, and the internal coiling band uniformly continuous are welded, described to copy
Plate is distributed on two sections in the high-end and centre position of rotating cylinder cylinder.
Further, described bearing base provides the frequency conversion motor of power for connection.
Further, described rotating cylinder cylinder is arranged on described bearing base, the rotating cylinder tubular axis and level
Face is into 1.5 ° of angles.
Further, described internal coiling welding on rotating cylinder barrel, from low side to high-end continuous welding.
Further, described crude salt charging aperture is provided with dust cover.
The beneficial effects of the utility model
This utility model compared with existing leaching device, have the advantages that prominent be：（1）Continuous way is produced, and is subtracted significantly
Little labor intensity, improved production environment reduce the generation of accident；（2）The leaching environment of closing, makes steam no longer overflow, and reduces
Energy consumption；（3）The solid particle of larger crude salt can be isolated, leaching is further crushed, is improve overall leaching efficiency,
Reduce production cost；（4）Apparatus structure is simple, and high degree of automation is easy to operate.
Contacted by solid-liquid counter-current, the dynamic continuous way leaching of crude salt can be realized, solid material can be preferably contacted with water,
Leaching effect is lifted, so as to change existing leaching mode, leaching efficiency is high, and effect is good, and energy resource consumption is few, can utilize closed
Rotating cylinder, the steam of generation is no longer overflowed, substantially improve scene production environment, reduce labor intensity, so as to improve
Work efficiency, reduces production cost.Simultaneously can realize that the big material particles of crude salt are separated with short grained, make larger
Grain is separated, and the dense halogen suspension that little particle is formed with water is directly entered solid-liquid separation program.
The subsequent leaching device of the barium strontium salt production that this utility model is provided, realizes scalable, in operation in structure
Realize and automatically control, for the very big convenience that actual production is provided.
Description of the drawings
Accompanying drawing 1 is structural representation of the present utility model.
Accompanying drawing 2 is the profile of A-A in Fig. 1.
Accompanying drawing 3 is the profile of B-B in Fig. 1
In accompanying drawing：1- rotating cylinder cylinders；2- bearing bases；3- crude salt charging apertures；The dense halogen outlets of 4-；5- rinses water inlet；6-
Electronic auger；7- salt slag is exported；8- flights；9- internal coiling bands.
Specific embodiment
A kind of subsequent leaching device of barium strontium salt production, including rotating cylinder cylinder 1, bearing base 2, flushing water inlet 5, dense halogen
Outlet 4, crude salt charging aperture 3, electronic auger 6, salt slag outlet 7, internal coiling band 9, flight 8.Rotating cylinder cylinder 1 is arranged on bearing base
On 2, equipped with internal coiling band 9 and flight 8 in rotating cylinder inwall；Bearing base 2 provides power by frequency conversion motor and can adjust rotating cylinder
Velocity of rotation；Lower position of the crude salt charging aperture 3 in rotating cylinder, salt slag outlet 7 are located at the high end position of rotating cylinder, and salt slag outlet 7 is installed
In 6 position of electronic auger；Rinse high end position of the water inlet 5 in rotating cylinder, lower position of the dense halogen outlet 4 in rotating cylinder, thick barium or
Thick strontium is continuously entered from the lower position import of rotating cylinder, and flushing water is continuously entered from the high end position of rotating cylinder, in the dynamic of frequency conversion motor
Power is driven under the rotation of rotating cylinder, and thick barium or thick strontium are moved to high end position in the presence of internal coiling band 9, and with watery vomiting to connecing
Touch, thick barium or thick strontium are taken up by two groups of flights 8 in cylinder centre position, preferably contact with water mixing, while granule is compared
Little thick barium or thick strontium form the concentrator solid-liquor separation that dense halogen is into next section, one group of flight 8 of the high end position of rotating cylinder with water
Be to take up electronic auger 6 to be fallen into by 7 discharge of salt slag outlet by granule than larger barium or strontium slag, further crush leaching,
In the continuous rotation process of rotating cylinder, thick barium or thick strontium realize subsequent leaching process.
Rotating cylinder cylinder 1 is arranged on described bearing base 2, and 1 axis of rotating cylinder cylinder is with the horizontal 1.5 ° of angles.Rotating cylinder
Cylinder 1 and then affects leaching effect by the speed that rotates come the time of contact of control process amount and slag and water.
Internal coiling band 9 is welded on rotating cylinder barrel, from low side to high-end continuous welding.
Flight 8 has two kinds of forms, two groups of Main Functions of cylinder middle part be by granule less thick barium or thick strontium with
Water is mixed to form dense halogen and discharges, and is that big granule is ferreted out into salt slag outlet 7 near the flight 8 of 1 high end position of rotating cylinder cylinder.
Crude salt charging aperture 3 is provided with dust cover, has flying dust to fly out in preventing dropping process.
Electronic auger 6 is arranged on the high end position of rotating cylinder cylinder, is provided with blanking port, the oarse-grained slag that flight is taken up above
Fall in auger and discharge.
Below in conjunction with the accompanying drawings this utility model is described further.As Figure 1-3, thick barium or thick strontium are from the low of rotating cylinder
End position crude salt charging aperture 3 is continuously entered, and flushing water is continuously entered from rotating cylinder high end position flushing water import 5, frequency modulation motor
Power drives the rotation of rotating cylinder cylinder 1, thick barium or thick strontium in the presence of internal coiling band 9 to high end position by bearing base 2
It is mobile, and with watery vomiting to contact, thick barium or thick strontium are taken up, are preferably mixed with water and connect by two groups of flights 8 in cylinder centre position
Touch, it is while granule smaller thick barium or thick strontium and water are formed dense halogen discharged by dense halogen outlet 4, dense into next section
Machine carries out solid-liquor separation, and one group of flight 8 of the high end position of rotating cylinder is to take up and fall into electric mincing granule than larger barium or strontium slag
Dragon 6 passes through the salt slag outlet 7 of barium or strontium and discharges, and further crushes leaching, in the continuous rotation process of rotating cylinder, thick barium or thick strontium
Realize subsequent leaching process.
Finally it should be noted that：Above example only not limits the skill described by this utility model to illustrate this explanation
Art scheme；Therefore, although this specification has been carried out detailed description with reference to the above embodiments to this utility model,
It will be understood by those within the art that, still this utility model can be modified or equivalent；And all
Technical scheme and its improvement without departing from spirit and scope of the present utility model, which all should be covered will in right of the present utility model
Ask in the middle of scope.
Claims (5)
1. a kind of barium strontium salt produces subsequent leaching device, it is characterised in that：Including rotating cylinder cylinder（1）, bearing base（2）, salt slag
Outlet（7）, rinse water inlet（5）, crude salt charging aperture（3）, the outlet of dense halogen（4）, electronic auger（6）, internal coiling band（9）And flight
（8）；Described rotating cylinder cylinder（1）Installed in bearing base（2）On；Described salt slag outlet（7）With flushing water inlet（5）It is located at
Rotating cylinder cylinder（1）High end position；Described crude salt charging aperture（3）Export with dense halogen（4）It is respectively distributed to rotating cylinder cylinder（1）'s
Lower position；The electronic auger（6）Blanking port, described salt slag outlet are provided with above（7）Positioned at electronic auger（6）On；Institute
The internal coiling band stated（9）With flight（8）It is welded on rotating cylinder cylinder（1）On inwall, the internal coiling band（9）Uniformly continuous are welded,
The flight（8）It is distributed in rotating cylinder cylinder（1）High-end and centre position two sections on.
2. a kind of barium strontium salt as claimed in claim 1 produces subsequent leaching device, it is characterised in that：Described bearing base
（2）The frequency conversion motor of power is provided for connection.
3. a kind of barium strontium salt as claimed in claim 1 produces subsequent leaching device, it is characterised in that：Described rotating cylinder cylinder
（1）Installed in described bearing base（2）On, the rotating cylinder cylinder（1）Axis is with the horizontal 1.5 ° of angles.
4. a kind of barium strontium salt as claimed in claim 1 produces subsequent leaching device, it is characterised in that：Described internal coiling band
（9）It is welded in rotating cylinder inwall, from low side to high-end continuous welding.
5. a kind of barium strontium salt as described in any one of claim 1-4 produces subsequent leaching device, it is characterised in that：Described is thick
Salt charging aperture（3）It is provided with dust cover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620904402.9U CN206051548U (en) | 2016-08-19 | 2016-08-19 | A kind of barium strontium salt produces subsequent leaching device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620904402.9U CN206051548U (en) | 2016-08-19 | 2016-08-19 | A kind of barium strontium salt produces subsequent leaching device |
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| Publication Number | Publication Date |
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| CN206051548U true CN206051548U (en) | 2017-03-29 |
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| CN201620904402.9U Active CN206051548U (en) | 2016-08-19 | 2016-08-19 | A kind of barium strontium salt produces subsequent leaching device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107447106A (en) * | 2017-07-20 | 2017-12-08 | 长沙矿冶研究院有限责任公司 | A kind of continuous leaching method of the reduction roasting of barite deposit and spiral for leaching leach cylinder |
| CN107697890A (en) * | 2017-11-13 | 2018-02-16 | 仝六斗 | A kind of improved thick barium, the leaching device and its leaching technology of strontium |
| CN110510582A (en) * | 2019-09-09 | 2019-11-29 | 重庆庆龙精细锶盐化工有限公司 | A kind of strontium barium salt subsequent leaching, production system of slagging tap and production technology |
| CN114939286A (en) * | 2022-07-05 | 2022-08-26 | 广西来宾市国宏钙业科技有限公司 | Continuous leaching device |
-
2016
- 2016-08-19 CN CN201620904402.9U patent/CN206051548U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107447106A (en) * | 2017-07-20 | 2017-12-08 | 长沙矿冶研究院有限责任公司 | A kind of continuous leaching method of the reduction roasting of barite deposit and spiral for leaching leach cylinder |
| CN107447106B (en) * | 2017-07-20 | 2023-09-05 | 长沙矿冶研究院有限责任公司 | Reduction roasting-continuous leaching method for heavy-crystal stone ore and spiral leaching barrel for leaching |
| CN107697890A (en) * | 2017-11-13 | 2018-02-16 | 仝六斗 | A kind of improved thick barium, the leaching device and its leaching technology of strontium |
| CN110510582A (en) * | 2019-09-09 | 2019-11-29 | 重庆庆龙精细锶盐化工有限公司 | A kind of strontium barium salt subsequent leaching, production system of slagging tap and production technology |
| CN114939286A (en) * | 2022-07-05 | 2022-08-26 | 广西来宾市国宏钙业科技有限公司 | Continuous leaching device |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210329 Address after: Xinji City, Shijiazhuang City, Hebei Province Patentee after: Hebei Nissin Chemical Co.,Ltd. Address before: 052360 No. 45 Chemical Road, Xinji City, Shijiazhuang, Hebei Patentee before: HEBEI XINJI CHEMICAL GROUP Co.,Ltd. |
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| TR01 | Transfer of patent right |