CN109382058A - A kind of Novel filtration enrichment facility and main reaction kettle device - Google Patents
A kind of Novel filtration enrichment facility and main reaction kettle device Download PDFInfo
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- CN109382058A CN109382058A CN201811302242.0A CN201811302242A CN109382058A CN 109382058 A CN109382058 A CN 109382058A CN 201811302242 A CN201811302242 A CN 201811302242A CN 109382058 A CN109382058 A CN 109382058A
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- cylinder
- filter core
- agitating paddle
- filtering
- decelerating motor
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- 238000001914 filtration Methods 0.000 title claims abstract description 34
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 47
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000010079 rubber tapping Methods 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims abstract description 12
- 230000008676 import Effects 0.000 claims abstract description 10
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 230000005540 biological transmission Effects 0.000 claims description 2
- 238000013461 design Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract 1
- 239000011162 core material Substances 0.000 description 38
- 239000000047 product Substances 0.000 description 27
- 239000002562 thickening agent Substances 0.000 description 14
- 238000003756 stirring Methods 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 8
- 239000012528 membrane Substances 0.000 description 8
- 230000004907 flux Effects 0.000 description 7
- 229910000765 intermetallic Inorganic materials 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000002243 precursor Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 229910015372 FeAl Inorganic materials 0.000 description 4
- 229910000943 NiAl Inorganic materials 0.000 description 4
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 4
- 229910010038 TiAl Inorganic materials 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000008929 regeneration Effects 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 230000032683 aging Effects 0.000 description 2
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 2
- 210000000481 breast Anatomy 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000005955 Ferric phosphate Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 229940032958 ferric phosphate Drugs 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical compound [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 1
- 229910000399 iron(III) phosphate Inorganic materials 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of Novel filtration enrichment facility and main reaction kettle devices, including cylinder A, the decelerating motor A of cylinder B and its top, decelerating motor B and its internal agitating paddle A, agitating paddle B further includes the tapping valve A of its bottom end simultaneously, tapping valve B and final concentrated product export A, and final concentrated product exports B；The top cylinder A is equipped with nitrogen inlet, regenerated liquid import, spray water inlet, cylinder A inner wall is equipped with annular core, the back blow port and purified liquor outlet and the filtering and concentrating liquid being connect with main reaction kettle outlet that cylinder A side wall is equipped with and filter core bottom connects, the top of cylinder B is equipped with material inlet, the side wall of cylinder B is equipped with overflow port and is connected to pans, is connected at the top of pans and filtering-condensing apparatus.Structure of the invention design it is more advanced rationally, install, dismantle, safeguard it is simple and convenient, can efficiently solve feed liquid layering, shake, sealing the problems such as, filtering accuracy is higher.
Description
Technical field
The present invention relates to field of chemical equipment, are a kind of Novel filtration enrichment facility and main reaction kettle device specifically.
Background technique
The shipment of the following power battery increases the promotion mainly from passenger car sales volume, it is contemplated that 2018-2025 power electric
Pond demand will keep the speed sustainable growth of 30-40%.Ternary battery will replace ferric phosphate lithium cell to become power battery shipment
Mainstream.Core material of the ternary precursor as ternary battery, the height of the quality of product directly determine ternary battery
Performance and security reliability.There are many index for measuring ternary precursor quality height, and wherein three keys such as TD, SEM, PSD refer to
Whether mark is by being affected using filter thickener.Good using the ternary precursor product ball-type degree of filter thickener production,
Density is high, and positive electrode capacity is high, recycles, and filter thickener has become the necessary equipment of high-quality ternary precursor production.
Summary of the invention
It is more advanced rationally that technical problem to be solved by the invention is to provide a kind of designs of structure, installation, disassembly, maintenance letter
Just, the problems such as capable of efficiently solving the layering of filter thickener feed liquid, shake, seal, equipment dependability and stability are higher for folk prescription
And operation expense is lower, filtering accuracy is higher, and intercepting efficiency is higher, can recycle the Novel filtration concentration of more price products
Device and main reaction kettle device.
The technical scheme to solve the above technical problems is that a kind of Novel filtration enrichment facility, including the electricity that slows down
It is machine A, nitrogen inlet, cylinder A, the outlet of filtering and concentrating liquid, agitating paddle A, filter core, back blow port, purified liquor outlet, tapping valve A, final dense
Contracting products export A and manhole；Decelerating motor A is on the top cylinder A；The top cylinder A is equipped with the regenerated liquid being connected to inside cylinder A
Import, spray water inlet and nitrogen inlet；Agitating paddle A and filter core are each provided at the inside of cylinder A, and agitating paddle A is located at filter core
The periphery at middle part, filter core is fixedly connected with the inner wall of cylinder A, and inner wall upper layer and lower layer of the filter core in cylinder A are distributed；Decelerating motor A
Output shaft and agitating paddle A top transmission connection for driving agitating paddle A axially to rotate, agitating paddle A is designed as being bonded lower vertebra
Body curve shape；Back blow port and purified liquor outlet are fixed on the side wall of cylinder A, back blow port and purified liquor outlet are in the side of cylinder A
The distribution of wall upper layer and lower layer, is connected to by connecting tube with the bottom of filter core；It states and is fixed with filtering and concentrating liquid on the side wall of cylinder A
Outlet and the upper end for being located at upper layer filter core in cylinder A, the outlet of filtering and concentrating liquid pass through pneumatic discharge valve and connecting tube and main reaction
Kettle connection；The lower end cylinder A is equipped with the tapping valve A being connected to inside cylinder A and final concentrated product outlet A；It is provided on cylinder A
Manhole.
A kind of main reaction kettle device, including such as Novel filtration enrichment facility and decelerating motor B, stoste feed inlet, cylinder
B, agitating paddle B, overflow port, tapping valve B, pans, final concentrated product export B；The outlet of filtering and concentrating liquid passes through pipeline and cylinder
The lower end of body B is connected to, and decelerating motor B is on the top cylinder B；The top cylinder B is equipped with the stoste being connected to inside cylinder B and feeds
Mouthful；Agitating paddle B is located at the bosom position of cylinder B；The output shaft of decelerating motor B and the top of agitating paddle B are sequentially connected and use
In drive agitating paddle B axle to rotation；Overflow port is fixed on the side wall of cylinder B；Overflow port is connected by connecting tube and pans
It connects, pans at the top of diaphragm pump and connecting tube and filtering-condensing apparatus by connecting；The lower end cylinder B is equipped with and connects inside cylinder B
Logical tapping valve B and final concentrated product export B.
The beneficial effect of the utility model filtering-condensing apparatus is: structure design is more advanced rationally, and installation, disassembly, maintenance are simple
It is convenient, efficiently solve the problems, such as that filter thickener feed liquid is layered, product quality is more preferable, efficiently solves blender rolling
Dynamic, the problems such as Seal Head Strength is inadequate, equipment dependability is higher, and filter core is improved to be threadedly coupled with interior endless tube by mating, nothing
Leakage, easy to disassemble, installation, realize the recycling of filter core, optimize valve and endless tube group, reduce device fails
Probability, stability is higher, and filter core uniform pore diameter, flux decline is slow, and surface is smooth, is not easy to paste film, and operation expense is lower,
Filtering accuracy is higher, and intercepting efficiency is higher, can recycle more price products.
Based on the above technical solution, the present invention can also be improved as follows.
Further, filter core is using threaded connection.
Beneficial effect using above-mentioned further scheme is: being convenient for overhaul of the equipments or filter element replacing.
Further, deflector is had additional on filter core.
Beneficial effect using above-mentioned further scheme is: improving solid-liquid state, is uniformly mixed, it is equal to be conducive to product particle
Even property narrows PSD.
Further, the material that filter core uses is intermetallic compound.
Beneficial effect using above-mentioned further scheme is: the metal membrane cartridge that intermetallic compound is formed has high-precision
Degree, big flux, corrosion resistant feature reduce obstruction in thickener, and the more conducively feed liquid in thickener is sufficiently mixed, and reduce product
Material improves finished product rate.
Further, intermetallic compound is the one of which of TiAl or NiAl or FeAl.
Beneficial effect using above-mentioned further scheme is: the intermetallic compound porous membrane material of TiAl or NiAl or FeAl
Particle is completely embedded, and percent opening is high, and substrate pore size is big, and film layer aperture is small, and substrate is consistent with membrane material.
Further, the material that filter core uses is the one of which of PE or PA or ceramics.
Beneficial effect using above-mentioned further scheme is: PE, PA or ceramic element, better mechanical property will not occur
Aging rupture, acidproof, alkaline-resisting, resistance to aldehyde, resistance to aliphatic hydrocarbon, radioresistens irradiation and the chemical properties such as water-fast are excellent, organic solvent-resistant
Performance it is also fine.
Further, filter core is annular in shape.
Beneficial effect using above-mentioned further scheme is: circular filter core is capable of increasing the contact area of filter core, is promoted
Filter efficiency.
Further, the liquidometer for detecting liquid level in cylinder A is provided on cylinder A.
Using the beneficial effect of above-mentioned further scheme is: to realize automatic running, and can be dropped with accurate measurements liquid level
It is low to lead to failure because liquid level is out of control, improve equipment continuous and steady operation.
Detailed description of the invention
Fig. 1 is structure of the invention figure；
Fig. 2 is filter core top view of the present invention；
In attached drawing, parts list represented by the reference numerals are as follows:
1, decelerating motor A, 2, regenerated liquid import, 3, spray water inlet, 4, nitrogen inlet, 5, cylinder A, 6, process concentrate
Outlet, 7, agitating paddle A, 8, filter core, 9, back blow port 10, purified liquor outlet, 11, tapping valve A, 12, decelerating motor B, 13, stoste charging
Mouthful, 14, cylinder B, 15, agitating paddle B, 16, overflow port, 17, tapping valve B, 18, pans, 19, final concentrated product outlet A,
20, final concentrated product exports A, 21, manhole.
Specific embodiment
The principle and features of the present invention will be described below with reference to the accompanying drawings, and the given examples are served only to explain the present invention, and
It is non-to be used to limit the scope of the invention.
Embodiment 1:
As shown in Figure 1 and Figure 2, a kind of Novel filtration enrichment facility and main reaction kettle device in this example, including decelerating motor
It is A1, regenerated liquid import 2, spray water inlet 3, nitrogen inlet 4, cylinder A5, process concentrated solution outlet 6, agitating paddle A7, filter core 8, anti-
Mouthpiece 9, purified liquor outlet 10, tapping valve A11, decelerating motor B12, stoste feed inlet 13, cylinder B14, agitating paddle B15, overflow port
16, tapping valve B17, pans 18, final concentrated product outlet A19, final concentrated product export A20, manhole 21.
On the top cylinder A5, the output shaft of decelerating motor A1 and the top of agitating paddle A7 are sequentially connected and use decelerating motor A1
It is axially rotated in drive agitating paddle A；The top cylinder A5 is equipped with the regenerated liquid import 2 being connected to inside cylinder A5, spray water inlet 3
With nitrogen inlet 4, when work, is increased or reduced by adjusting thickener top nitrogen (or other inert gases) pressure and realized
Adjusting to filtration flux.After the completion of work, regenerated liquid import 2 sprays chemical regeneration liquid and carries out cleaning and regeneration, spray to filter core 8
Water drenching import 3 sprays liquid to cleaning inside cylinder A5；Agitating paddle A7 and filter core 8 are each provided at the inside of cylinder A5, and stir
The middle part that paddle A7 is located at filter core is mixed, the periphery of filter core is fixedly connected with the inner wall of cylinder A5, and filter core 8 is above and below the inner wall of cylinder A5
Two layers of distribution, filter core 8 is annular in shape and using being threadedly coupled, and is convenient for overhaul of the equipments or replacement using being threadedly coupled, filter core 8 is annular in shape
It is capable of increasing the contact area of filter core 8, promotes filter efficiency, filter core 8 is using in TiAl or NiAl or FeAl intermetallic compound
One of which metal membrane cartridge is made or uses material non-metallic film filter core is made for the one of which of PE or PA or ceramics.
Metal membrane cartridge has high-precision, big flux, corrosion resistant feature, obstruction in thickener is reduced, more conducively in thickener
Feed liquid is sufficiently mixed, and reduces buildup, improves finished product rate, TiAl or the intermetallic compound porous membrane material of NiAl or FeAl
Grain is completely embedded, and percent opening is high, and substrate pore size is big, and film layer aperture is small, and substrate is consistent with membrane material, PE, PA or ceramic material filter
Aging rupture will not occur for core, better mechanical property, acidproof, alkaline-resisting, resistance to aldehyde, resistance to aliphatic hydrocarbon, radioresistens irradiation and water-fast etc.
Chemical property is excellent, and the performance of organic solvent-resistant is also fine；Filter core adds deflector, can improve solid-liquid state, is uniformly mixed,
Be conducive to product particle uniformity, narrow PSD；Agitating paddle A7 is designed as fitting hypocentrum curve shape, by the easy jetsam in bottom
Stirring is reinforced in part to be influenced, and material waste is reduced；Back blow port 9 and purified liquor outlet 10, blowback are fixed on the side wall of cylinder A5
The side wall upper layer and lower layer of mouth 9 and purified liquor outlet 10 in cylinder A5 are distributed, and are connected to by connecting tube with the bottom of filter core 8, in mistake
During filter, blowback is carried out according to the parameters such as the break time of setting or filter pressure gradient or flow decline, it is more thorough
Removal filters the solid filter cake of pipe surface, and filtered clear liquid is discharged by connecting tube from purified liquor outlet 10；The side wall of cylinder A5
On be fixed with filtering and concentrating liquid outlet 6 and be located at the upper end of upper layer filter core 8 in cylinder A5, the outlet of filtering and concentrating liquid 6 passes through gas
Dynamic discharge valve and connecting tube are connect with main reaction kettle, so that automatic drain and level balance function are realized, for the flat of concentration
It weighs more accurate, while reducing the difficulty of whole flow balance adjustment, complexity and the operation for reducing robot control system(RCS) are difficult
Degree；The lower end cylinder A5 is equipped with the tapping valve A11 being connected to inside cylinder A5 and final concentrated product outlet A19；It is set on cylinder A5
It is equipped with manhole 21, equipment is facilitated to be overhauled；Rationally setting height, stirring cylinder A5 higher are conducive to stir on cylinder A5, if
Standby stable operation, swings small；By FEM calculation, end socket wall thickness is rationally designed, head wall is thicker can to ensure that equipment is highly concentrated
Stability when degree stirring；The liquidometer for detecting liquid level in cylinder A is provided on cylinder A, liquidometer can be with accurate measurements
Liquid level to realize automatic running, and reduces and leads to failure because liquid level is out of control, improves equipment continuous and steady operation.
On the top cylinder B14, the output shaft of decelerating motor B12 and the top of agitating paddle B15 are driven and connect decelerating motor B12
It connects for driving agitating paddle B15 axially to rotate；The top cylinder B14 is equipped with the stoste feed inlet 13 being connected to inside cylinder B14；It stirs
The bosom position that paddle B15 is located at cylinder B14 is mixed, the stoste in cylinder B14 is stirred；It is solid on the side wall of cylinder B14
Surely it is equipped with overflow port 16；Overflow port 16 connect by connecting tube with pans 18, pans 18 pass through diaphragm pump and connecting tube and
It is connected at the top of filtering-condensing apparatus, feed liquid is discharged into pans with overflow port in reaction kettle, is delivered to feed liquid by diaphragm pump
Thickener；The lower end cylinder B14 is equipped with the tapping valve B17 being connected to inside cylinder B14 and final concentrated product outlet B20.
Working principle: stoste first continues into cylinder B14 by stoste feed inlet 13, passes through agitating paddle in cylinder B14
B15 stirring is reacted, and using the product of generation as nucleus, newly-generated product is agglomerated into particle, when the particle is with reaction
Between be gradually increased, ultimately form required product particle pattern.During long brilliant, since the required period is longer and reaction kettle holds
Product is limited, and it is long brilliant that intermediate product need to be continuously maintained under suitable reaction condition the reaction was continued.Feed liquid is with overflow in cylinder B14
Mouthfuls 16 are discharged into pans 18 feed liquid are delivered in filtering-condensing apparatus by diaphragm pump, continue under the action of stirring into
Row reaction.The intensity of stirring can adjust different revolving speeds (0-200r/min) by decelerating motor (frequency conversion), to meet reaction
It needs.Filter core 8 needed for being provided with filtering in filtering-condensing apparatus, filter core 8 filter, and will be free of the clear liquid discharge system of product slurry
Outside, it is used as other processes with water, due to the lasting discharge of clear liquid, realizes the gradually concentration to material slurry, led to simultaneously
That crosses thickener and reaction kettle realizes that the intracorporal material concentration of two tanks balances communicating pipe, filtration flux and reaction kettle inlet amount into
Row matching is increased or reduced by adjusting thickener top nitrogen (or other inert gases) pressure to realize to filtration flux
It adjusts.In process of production, reaction kettle, pans 18, the slurry concentration in thickener are gradually increasing, when grain diameter is with reaction
Between gradually grow up, after the period needed for reaching reaction, be discharged in products pot together, by the rings such as subsequent centrifuge separation, dry
Section, forms product ternary precursor.After the completion of work, regenerated liquid import 2 sprays chemical regeneration liquid and cleans to filter core 8
Regeneration, spray water inlet 3 spray liquid to cleaning inside cylinder A5, reduce fouling membrane, restore filtration flux, realize long-term
Stable operation.
The foregoing is merely a prefered embodiment of the invention, is not intended to limit the invention, all in the spirit and principles in the present invention
Within, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention.
Claims (6)
1. a kind of Novel filtration enrichment facility, it is characterised in that: including decelerating motor A (1), regenerated liquid import (2), shower water into
It is mouthful (3), nitrogen inlet (4), cylinder A (5), filtering and concentrating liquid outlet (6), agitating paddle A (7), filter core (8), back blow port (9), clear
Liquid exports (10), tapping valve A (11), final concentrated product outlet A (19) and manhole (21)；The decelerating motor A (1) is described
On cylinder A (5) top；(5) top cylinder A is equipped with the regenerated liquid import (2) being connected to inside the cylinder A (5), spray
Water inlet (3) and nitrogen inlet (4)；The agitating paddle A (7) and the filter core (8) are each provided at the inside of the cylinder A (5), and
The agitating paddle A (7) is located at the middle part of the filter core (8), and the periphery of the filter core (8) and the inner wall of the cylinder A (5) are fixed
Connection, the filter core (8) are distributed in the inner wall upper layer and lower layer of the cylinder A (5)；The output shaft of the decelerating motor A (1) and institute
The top transmission connection of agitating paddle A (7) is stated for driving the agitating paddle A (7) axially to rotate, the agitating paddle A (7) is designed as
It is bonded hypocentrum curve shape；The back blow port (9) and the purified liquor outlet are fixed on the side wall of the cylinder A (5)
(10), the back blow port (9) and the purified liquor outlet (10) are distributed in the side wall upper layer and lower layer of the cylinder A (5), pass through company
Adapter tube is connected to the bottom of the filter core (8)；The filtering and concentrating liquid outlet is fixed on the side wall for stating (5) cylinder A
(6) and positioned at the upper end of filter core (8) described in the interior upper layer of the cylinder A (5), the filtering and concentrating liquid outlet (6) is by pneumatically unloading
Material valve and connecting tube are connect with main reaction kettle；(5) lower end cylinder A is equipped with the row being connected to inside the cylinder A (5)
Liquid valve A (11) and final concentrated product outlet A (19)；Manhole (21) are set on the cylinder A (5).
2. a kind of Novel filtration enrichment facility according to claim 1, it is characterised in that: the filter core (8) uses screw thread
Connection.
3. a kind of Novel filtration enrichment facility according to claim 1, it is characterised in that: had additional on the filter core (8)
Deflector.
4. a kind of Novel filtration enrichment facility according to any one of claims 1 to 3, it is characterised in that: the filter core (8)
Annularly.
5. a kind of Novel filtration enrichment facility according to any one of claims 1 to 3, it is characterised in that: the cylinder A
(5) liquidometer for detecting the interior liquid level of the cylinder A (5) is provided on.
6. a kind of main reaction kettle device, it is characterised in that: including Novel filtration concentration such as described in any one of claim 1 to 5
Device and decelerating motor B (12), stoste feed inlet (13), cylinder B (14), agitating paddle B (15), overflow port (16), tapping valve B
(17), pans (18), final concentrated product outlet B (20)；The filtering and concentrating liquid outlet (6) passes through pipeline and the cylinder
The lower end of B (14) is connected to, and the decelerating motor B (12) is on cylinder B (14) top；Cylinder B (14) top is equipped with
The stoste feed inlet (13) being connected to inside the cylinder B (14)；The agitating paddle B (15) is located at the interior of the cylinder B (14)
Portion middle position；The top of the output shaft of the decelerating motor B (12) and the agitating paddle B (15) is sequentially connected for driving
Agitating paddle B (15) is stated axially to rotate；The overflow port (16) are fixed on the side wall of the cylinder B (14)；The overflow port
(16) it is connect by connecting tube with the pans (18), the pans (18) pass through diaphragm pump and connecting tube and filtering and concentrating
Connection at the top of device；(14) lower end cylinder B be equipped with the tapping valve B (17) being connected to inside the cylinder B (14) and
Final concentrated product outlet B (20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811302242.0A CN109382058A (en) | 2018-11-02 | 2018-11-02 | A kind of Novel filtration enrichment facility and main reaction kettle device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811302242.0A CN109382058A (en) | 2018-11-02 | 2018-11-02 | A kind of Novel filtration enrichment facility and main reaction kettle device |
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| CN109382058A true CN109382058A (en) | 2019-02-26 |
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| CN110102232A (en) * | 2019-05-23 | 2019-08-09 | 傅荣华 | Concentration systems are used in a kind of production of lithium battery persursor material |
| CN110681313A (en) * | 2019-09-30 | 2020-01-14 | 成都思达能环保设备有限公司 | Continuous filtering and separating device |
| CN113262533A (en) * | 2020-02-14 | 2021-08-17 | 杉杉能源（宁夏）有限公司 | Unpowered concentrator and ternary precursor production device |
| CN114100494A (en) * | 2021-11-08 | 2022-03-01 | 江西睿达新能源科技有限公司 | Production equipment and production process of ternary precursor |
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| CN114931802A (en) * | 2022-05-31 | 2022-08-23 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and outlet system thereof |
| CN114931910A (en) * | 2022-04-18 | 2022-08-23 | 成都思达能环保设备有限公司 | Equipment for coprecipitation reaction of anode material precursor and filter assembly |
| CN114931918A (en) * | 2022-04-08 | 2022-08-23 | 成都思达能环保设备有限公司 | Positive electrode material precursor coprecipitation reaction equipment |
| CN115054986A (en) * | 2022-06-27 | 2022-09-16 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and filtering and concentrating device thereof |
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| CN115193368B (en) * | 2022-04-08 | 2024-03-22 | 成都思达能环保设备有限公司 | Positive electrode material precursor coprecipitation reaction equipment |
| CN115193368A (en) * | 2022-04-08 | 2022-10-18 | 成都思达能环保设备有限公司 | Positive electrode material precursor coprecipitation reaction equipment |
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| CN114931910A (en) * | 2022-04-18 | 2022-08-23 | 成都思达能环保设备有限公司 | Equipment for coprecipitation reaction of anode material precursor and filter assembly |
| CN114931910B (en) * | 2022-04-18 | 2024-03-22 | 成都思达能环保设备有限公司 | Equipment and filter assembly for coprecipitation reaction of precursors of positive electrode material |
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| CN114733463B (en) * | 2022-04-18 | 2024-04-12 | 成都思达能环保设备有限公司 | Positive electrode material precursor coprecipitation reaction equipment |
| CN114931802A (en) * | 2022-05-31 | 2022-08-23 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and outlet system thereof |
| CN114931804A (en) * | 2022-05-31 | 2022-08-23 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and clear system thereof |
| CN114931805A (en) * | 2022-05-31 | 2022-08-23 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and outlet system thereof |
| CN115054986A (en) * | 2022-06-27 | 2022-09-16 | 成都思达能环保设备有限公司 | Coprecipitation reaction system and filtering and concentrating device thereof |
| CN115672236A (en) * | 2022-11-01 | 2023-02-03 | 成都思达能环保设备有限公司 | Battery anode material precursor coprecipitation reaction equipment and system |
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Application publication date: 20190226 |