CN114053893A - Pilot scale electrolyte mixing module - Google Patents
Pilot scale electrolyte mixing module Download PDFInfo
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- CN114053893A CN114053893A CN202111151371.6A CN202111151371A CN114053893A CN 114053893 A CN114053893 A CN 114053893A CN 202111151371 A CN202111151371 A CN 202111151371A CN 114053893 A CN114053893 A CN 114053893A
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- layer platform
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- 239000003792 electrolyte Substances 0.000 title claims abstract description 48
- 238000002156 mixing Methods 0.000 title claims abstract description 21
- 238000011020 pilot scale process Methods 0.000 title claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 61
- 238000001914 filtration Methods 0.000 abstract description 9
- 238000010276 construction Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 3
- 230000001681 protective effect Effects 0.000 description 10
- 230000009194 climbing Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000003990 capacitor Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000282326 Felis catus Species 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/058—Construction or manufacture
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0564—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
- H01M10/0566—Liquid materials
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Inorganic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a pilot-scale test electrolyte mixing module which comprises a module frame structure, wherein a two-layer platform is arranged at the top end of the module frame structure, a one-layer platform is arranged at the bottom end of the module frame structure, a second precision filter assembly is arranged on one side of the bottom of the one-layer platform, a first precision filter assembly is arranged at the top end of the one-layer platform on one side of the second precision filter assembly, a five-hundred-liter reaction kettle is arranged at the bottom end of the two-layer platform above the second precision filter assembly, the top end of the five-hundred-liter reaction kettle extends to the outside of the two-layer platform, a sixty-liter reaction kettle is arranged at the bottom end of the two-layer platform on one side of the five-hundred-liter reaction kettle, and a double-station glove box is arranged at the top end of the two-layer platform on one side of the five-hundred-liter reaction kettle. The invention not only achieves the purposes of convenient transportation and quick construction, improves the convenience of the pilot test module in use, but also improves the filtering effect of the pilot test module on the electrolyte in use.
Description
Technical Field
The invention relates to the technical field of modular device equipment, in particular to a pilot-scale test electrolyte mixing module.
Background
The electrolyte is a medium used by chemical batteries, electrolytic capacitors and the like, has certain corrosivity, can provide ions for normal work of the chemical batteries, ensures that chemical reactions generated in the work are reversible, and is mainly divided into the electrolyte in organisms, the electrolyte applied to the battery industry and the electrolyte in industries such as electrolytic capacitors, super capacitors and the like.
At present electrolyte need mix the technology processing to it in process of production, and in mixing process, need carry out the pilot scale mixing process to it, therefore need use corresponding pilot scale module, the structure of this type of pilot scale module is comparatively loose on the market today, leads to its area great, is difficult to be applicable to the factory building and uses, and be not convenient for transport, and is difficult to build the processing fast to it.
Disclosure of Invention
The invention aims to provide a pilot-scale test electrolyte mixing module, which solves the problems that the pilot-scale test module proposed in the background art has a loose structure, so that the pilot-scale test electrolyte mixing module occupies a large area, is difficult to be used in a factory building, is inconvenient to transport and is difficult to quickly build and treat.
In order to achieve the purpose, the invention provides the following technical scheme: the utility model provides a pilot scale electrolyte mixing module, includes module frame construction, module frame construction's top is equipped with the double-deck platform, module frame construction's bottom is equipped with the one deck platform, one side of one deck platform bottom is equipped with second precision filter subassembly, the one deck platform top of second precision filter subassembly one side is equipped with first precision filter subassembly, the double-deck platform bottom of second precision filter subassembly top is equipped with five hundred liters reation kettle, five hundred liters reation kettle's top extends to the outside of double-deck platform, the double-deck platform bottom of five hundred liters reation kettle one side is equipped with sixty liters reation kettle, sixty liters reation kettle's top extends to the outside of double-deck platform, the double-deck platform top of five hundred liters reation kettle one side is equipped with duplex position glove box.
Preferably, a first guard rail is installed at the edge position of the top end of the second-layer platform, and an opening is formed in one side of the surface of the first guard rail so as to protect workers at the top end of the second-layer platform.
Preferably, the two-layer platform and the one-layer platform are in a horizontal structure, and the length of the two-layer platform is equal to that of the one-layer platform, so that various components are mounted on the inner side of the module frame structure.
Preferably, one side on second floor platform surface is equipped with the cat ladder, the plane at cat ladder bottom place and the plane coplane at one deck platform bottom place to the staff climbs the top to second floor platform.
Preferably, the two sides of the top end of the ladder stand are provided with second guard rails, and the second guard rails are symmetrical about the center line of the ladder stand so as to protect workers in climbing.
Preferably, sixty liters of kettle body circulating pump is installed on the top end of the platform on one side of the first precision filter assembly, one end of the sixty liters of kettle body circulating pump is communicated with the outer wall of the first precision filter assembly through a guide pipe, and the other end of the sixty liters of kettle body circulating pump is communicated with the outer wall of the sixty liters of reaction kettle through a guide pipe, so that the electrolyte in the sixty liters of reaction kettle is conveyed to the inside of the first precision filter assembly.
Preferably, a conduit is installed at one end of the first precision filter assembly, which is far away from the sixty-liter kettle body circulating pump, and one end of the conduit, which is far away from the first precision filter assembly, is communicated with the outer wall of the sixty-liter reaction kettle, so that the electrolyte circularly flows into the interior of the sixty-liter reaction kettle through the conduit.
Preferably, a five hundred liter kettle body circulating pump is installed at the top end of the platform on one side of the second precision filter assembly, one end of the five hundred liter kettle body circulating pump is communicated with one end of the second precision filter assembly through a guide pipe, and the other end of the five hundred liter kettle body circulating pump is communicated with the outer wall of the five hundred liter reaction kettle through a guide pipe, so that electrolyte in the five hundred liter reaction kettle is conveyed to the inside of the second precision filter assembly.
Preferably, a conduit is installed at one end of the second precision filter assembly, which is far away from the five hundred liter kettle body circulating pump, and one end of the conduit, which is far away from the second precision filter assembly, is communicated with the outer wall of the five hundred liter reaction kettle, so that the electrolyte circularly flows into the interior of the five hundred liter reaction kettle through the conduit.
Compared with the prior art, the invention has the beneficial effects that: the pilot-scale test electrolyte mixing module not only achieves the purposes of convenient transportation and quick construction, improves the convenience of the pilot-scale test module in use, but also improves the filtering effect of the pilot-scale test module on the electrolyte in use;
(1) the top and the bottom of the module frame structure are respectively provided with a two-layer platform and a one-layer platform, the first precision filter assembly, the second precision filter assembly, the five hundred liter kettle body circulating pump and the sixty liter kettle body circulating pump are arranged at the top end of the one-layer platform, and the five hundred liter reaction kettle and the sixty liter reaction kettle are arranged at the bottom end of the two-layer platform so as to be arranged at the inner side of the module frame structure, so that the pilot test module is compact in structure, small in occupied area and suitable for general plants, and the purposes of being convenient to transport and fast to build are achieved;
(2) the ladder stand is arranged on one side of the surface of the two-layer platform, the second protective guards are arranged on two sides of the top end of the ladder stand, so that a worker can climb to the top of the two-layer platform through the ladder stand and can be protected by the second protective guards, and meanwhile, the first protective guards are arranged at the edge position of the top end of the two-layer platform, so that the worker climbing to the top of the two-layer platform can be protected by the first protective guards, the middle test module can be safely maintained, and the convenience of the middle test module in use is improved;
(3) carry out the mixing reaction through five hundred liters reation kettle and sixty liters reation kettle to electrolyte and handle, carry the processing to the inside electrolyte of five hundred liters reation kettle by five hundred liters cauldron body circulating pump again, and carry out filtration treatment to this part electrolyte by second precision filter subassembly, flow in to the inside of five hundred liters reation kettle after the circulation, the inside electrolyte of sixty liters reation kettle is carried the processing to sixty liters reation kettle to rethread sixty liters cauldron body circulating pump, and carry out filtration treatment to this part electrolyte by first precision filter subassembly, flow in to the inside of sixty liters reation kettle after the circulation, in order to reach precision filtration's purpose, thereby the filter effect to electrolyte when having improved the pilot scale module and using.
Drawings
FIG. 1 is a schematic three-dimensional structure of the present invention;
FIG. 2 is a schematic front view of the present invention;
FIG. 3 is a left side view of the present invention;
FIG. 4 is a schematic diagram of the right view structure of the present invention;
FIG. 5 is a rear view of the present invention;
FIG. 6 is a schematic view of the process flow structure of the present invention.
In the figure: 1. a modular frame structure; 2. a first guard rail; 3. a two-layer platform; 4. a five hundred liter reaction kettle; 5. a double-station glove box; 6. a second guard rail; 7. climbing a ladder; 8. a first precision filter assembly; 9. a second precision filter assembly; 10. a layer of platform; 11. sixty liters of reaction kettle; 12. five hundred liters of kettle body circulating pump; 13. sixty liters of kettle circulating pump.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-6, an embodiment of the present invention is shown: a pilot-scale test electrolyte mixing module comprises a module frame structure 1, wherein a two-layer platform 3 is arranged at the top end of the module frame structure 1, a first protective guard 2 is arranged at the edge position of the top end of the two-layer platform 3, and an opening is formed in one side of the surface of the first protective guard 2;
when the protective device is used, the first protective guard 2 is arranged at the edge position of the top end of the two-layer platform 3, so that protection treatment is carried out on workers at the top end of the two-layer platform 3;
the second-layer platform 3 and the first-layer platform 10 are in a horizontal structure, and the length of the second-layer platform 3 is equal to that of the first-layer platform 10;
when in use, the two-layer platform 3 and the one-layer platform 10 are horizontally arranged at the top and the bottom of the module frame structure 1, so that various components are all arranged at the inner side of the module frame structure 1;
a ladder stand 7 is arranged on one side of the surface of the second-layer platform 3, and the plane where the bottom end of the ladder stand 7 is located is coplanar with the plane where the bottom end of the first-layer platform 10 is located;
when in use, the ladder stand 7 is arranged on one side of the surface of the two-layer platform 3, so that a worker can conveniently climb to the top of the two-layer platform 3;
the two sides of the top end of the ladder stand 7 are provided with second guard rails 6, and the second guard rails 6 are symmetrical about the central line of the ladder stand 7;
when the ladder is used, two groups of second guard rails 6 are arranged on two sides of the top end of the ladder stand 7, so that protection treatment is performed on workers in climbing;
the bottom end of the module frame structure 1 is provided with a first-layer platform 10, one side of the bottom of the first-layer platform 10 is provided with a second precision filter assembly 9, the top end of the first-layer platform 10 at one side of the second precision filter assembly 9 is provided with a five-hundred-liter kettle body circulating pump 12, one end of the five-hundred-liter kettle body circulating pump 12 is communicated with one end of the second precision filter assembly 9 through a guide pipe, and the other end of the five-hundred-liter kettle body circulating pump 12 is communicated with the outer wall of the five-hundred-liter reaction kettle 4 through a guide pipe;
when in use, the five hundred liter kettle body circulating pump 12 is opened, so that the electrolyte in the five hundred liter reaction kettle 4 can be conveyed to the interior of the second precision filter assembly 9;
a conduit is arranged at one end of the second precision filter assembly 9, which is far away from the five hundred liter kettle body circulating pump 12, and one end of the conduit, which is far away from the second precision filter assembly 9, is communicated with the outer wall of the five hundred liter reaction kettle 4;
when in use, the electrolyte is filtered by the second precision filter assembly 9, so that the electrolyte circularly flows into the five hundred liters reaction kettle 4 through the guide pipe;
the top end of a layer of platform 10 at one side of the second precise filter assembly 9 is provided with a first precise filter assembly 8, the top end of a layer of platform 10 at one side of the first precise filter assembly 8 is provided with a sixty-liter kettle body circulating pump 13, one end of the sixty-liter kettle body circulating pump 13 is communicated with the outer wall of the first precise filter assembly 8 through a guide pipe, and the other end of the sixty-liter kettle body circulating pump 13 is communicated with the outer wall of the sixty-liter reaction kettle 11 through a guide pipe;
when in use, the sixty liters of the autoclave body circulating pump 13 is opened, so that the electrolyte in the sixty liters of the autoclave 11 can be conveyed to the interior of the first precision filter assembly 8;
a conduit is arranged at one end of the first precision filter assembly 8, which is far away from the sixty-liter kettle body circulating pump 13, and one end of the conduit, which is far away from the first precision filter assembly 8, is communicated with the outer wall of the sixty-liter reaction kettle 11;
when in use, the electrolyte is filtered by the first precision filter assembly 8, so that the electrolyte circularly flows into the sixty-liter reaction kettle 11 through the guide pipe;
five hundred liters of reation kettle 4 are equipped with to the 3 bottom ends of second layer platform above second precision filter subassembly 9, and the top of five hundred liters of reation kettle 4 extends to the outside of two layer platform 3, and the 3 bottom ends of two layer platform of 4 one sides of five hundred liters of reation kettle are equipped with sixty liters of reation kettle 11, and the top of sixty liters of reation kettle 11 extends to the outside of two layer platform 3, and the 3 tops of two layer platform of 4 one sides of five hundred liters of reation kettle are equipped with double-station glove box 5.
When the device is used, firstly, a two-layer platform 3 and a one-layer platform 10 are respectively arranged at the top and the bottom of a module frame structure 1, a first precision filter component 8, a second precision filter component 9, a five hundred liter kettle body circulating pump 12 and a sixty liter kettle body circulating pump 13 are arranged at the top end of the one-layer platform 10, and a five hundred liter reaction kettle 4 and a sixty liter reaction kettle 11 are arranged at the bottom end of the two-layer platform 3 so as to be all arranged at the inner side of the module frame structure 1, so that the structure of the pilot scale module is compact, the occupied area is small, the pilot scale module is suitable for a general factory, the purposes of convenient transportation and quick building are achieved, then, a ladder stand 7 is arranged at one side of the surface of the two-layer platform 3, and second guard rails 6 are arranged at two sides of the top end of the ladder stand 7, so that a worker can climb to the top of the two-layer platform 3 through the ladder stand 7, the second guard rail 6 is used for protecting workers climbing the platform, the first guard rail 2 is arranged at the edge position of the top end of the second-layer platform 3, so that the workers climbing the top of the second-layer platform 3 are protected, finally, the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 are used for carrying out mixed reaction on the electrolyte, then, a five hundred liter kettle body circulating pump 12 is used for conveying the electrolyte in the five hundred liter reaction kettle 4, the second precise filter assembly 9 is used for filtering the part of the electrolyte, the part of the electrolyte flows into the five hundred liter reaction kettle 4 after circulation, then, a sixty liter kettle body circulating pump 13 is used for conveying the electrolyte in the sixty liter reaction kettle 11, the first precise filter assembly 8 is used for filtering the part of the electrolyte, and the part of the electrolyte flows into the sixty liter reaction kettle 11 after circulation, in order to achieve the purpose of precise filtration, a module frame structure 1 of the pilot test module is suitable for rolling door transportation of a common factory building, other auxiliary ultra-wide, ultra-high and other structural components are designed to be in bolted connection, a first protective guard 2, a second protective guard 6 and a ladder stand 7 are all detachable combined components, so that the pilot test module is convenient to assemble, disassemble and build, the pilot test module is mainly divided into two sets of mixed structures of a five hundred liter reaction kettle 4 and a sixty liter reaction kettle 11, the polishing degrees of the inner walls of the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 reach zero two microns, the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 are both provided with cold water jackets and are also provided with slow variable-frequency stirring, the five hundred liter reaction kettle body circulating pumps 12 and the sixty liter reaction kettle body 13 are mainly used for conveying treatment, and the precise filtration treatment is carried out through a first precise filter component 8 and a second precise filter component 9, and the system is provided with two sets, one set of the main system and the other set of the main system are standby so as to improve the running continuity of the system, powder additives are weighed and configured by the double-station glove box 5 and then are fed for use, when various liquid raw materials are fed, the weighed liquid raw materials are pressed into the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 by nitrogen, stirring is started again, the five hundred liter kettle body circulating pump 12 or the sixty liter kettle body circulating pump 13 is started, the purpose of self-circulation of the raw materials can be achieved, jacket freezing water valves arranged on the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 are also simultaneously opened, the temperature of media in the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11 is controlled, various powder additives are measured and configured by the double-station glove box 5, finished product filling is started after the system is configured, various cold source interfaces are designed at the tops of the five hundred liter reaction kettle 4 and the sixty liter reaction kettle 11, the device is characterized in that the device can be quickly butted with a factory energy system and can realize production, the total power of the pilot test module is thirty million, the electric cabinet is designed to be of a positive pressure explosion-proof type, motors equipped with a five hundred liter kettle body circulating pump 12, a sixty liter kettle body circulating pump 13, a five hundred liter reaction kettle 4 and a sixty liter reaction kettle 11 are all explosion-proof types, the electric cabinet is pneumatically operated in a frequency conversion control mode, the PLC instrument cabinet is also of a positive pressure explosion-proof type and is all explosion-proof instruments, a medium temperature adjusting control chilled water valve in a pressure transmitter is used for measuring the height limit of liquid level in the kettle, the system valve is automatically controlled by a PLC, and the combustible gas detection environment is leaked to danger linkage PLC linkage fire alarm, so that the pilot test module is used.
Claims (9)
1. The pilot scale electrolyte mixing module is characterized by comprising a module frame structure (1), wherein a two-layer platform (3) is arranged at the top end of the module frame structure (1), a layer platform (10) is arranged at the bottom end of the module frame structure (1), a second precision filter component (9) is arranged at one side of the bottom of the layer platform (10), a first precision filter component (8) is arranged at the top end of the layer platform (10) at one side of the second precision filter component (9), a five-hundred-liter reaction kettle (4) is arranged at the bottom end of the two-layer platform (3) above the second precision filter component (9), the top end of the five-hundred-liter reaction kettle (4) extends to the outside of the two-layer platform (3), a sixty-liter reaction kettle (11) is arranged at the bottom end of the two-layer platform (3) at one side of the five-hundred-liter reaction kettle (4), and the top end of the sixty-liter reaction kettle (11) extends to the outside of the two-layer platform (3), and a double-station glove box (5) is arranged at the top end of the two-layer platform (3) on one side of the five hundred liters reaction kettle (4).
2. The pilot electrolyte mixing module of claim 1, wherein: the edge position of the top end of the two-layer platform (3) is provided with a first guard rail (2), and one side of the surface of the first guard rail (2) is provided with an opening.
3. The pilot electrolyte mixing module of claim 1, wherein: the two-layer platform (3) and the one-layer platform (10) are of a horizontal structure, and the length of the two-layer platform (3) is equal to that of the one-layer platform (10).
4. The pilot electrolyte mixing module of claim 1, wherein: one side on the surface of the two-layer platform (3) is provided with a ladder (7), and the plane where the bottom end of the ladder (7) is located is coplanar with the plane where the bottom end of the one-layer platform (10) is located.
5. The pilot electrolyte mixing module of claim 4, wherein: and second guard rails (6) are arranged on two sides of the top end of the ladder stand (7), and the second guard rails (6) are symmetrical about the center line of the ladder stand (7).
6. The pilot electrolyte mixing module of claim 1, wherein: sixty liters of kettle body circulating pump (13) are installed on one deck platform (10) top of first precision filter subassembly (8) one side, the one end of sixty liters of kettle body circulating pump (13) is linked together through the outer wall of pipe with first precision filter subassembly (8), the other end of sixty liters of kettle body circulating pump (13) is linked together through the outer wall of pipe with sixty liters of reation kettle (11).
7. The pilot electrolyte mixing module of claim 6, wherein: the one end that sixty liters cauldron body circulating pump (13) were kept away from in first precision filter subassembly (8) is installed the pipe, the one end that first precision filter subassembly (8) were kept away from to the pipe is linked together with the outer wall of sixty liters reation kettle (11).
8. The pilot electrolyte mixing module of claim 1, wherein: five hundred liters of kettle body circulating pump (12) are installed on one deck platform (10) top of second precision filter subassembly (9) one side, the one end of five hundred liters of kettle body circulating pump (12) is linked together through the one end of pipe with second precision filter subassembly (9), the other end of five hundred liters of kettle body circulating pump (12) is linked together through the outer wall of pipe with five hundred liters of reation kettle (4).
9. The pilot electrolyte mixing module of claim 8, wherein: and a guide pipe is installed at one end, far away from the five hundred liter kettle body circulating pump (12), of the second precision filter assembly (9), and one end, far away from the second precision filter assembly (9), of the guide pipe is communicated with the outer wall of the five hundred liter reaction kettle (4).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111151371.6A CN114053893A (en) | 2021-09-29 | 2021-09-29 | Pilot scale electrolyte mixing module |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111151371.6A CN114053893A (en) | 2021-09-29 | 2021-09-29 | Pilot scale electrolyte mixing module |
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| CN114053893A true CN114053893A (en) | 2022-02-18 |
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| CN208554025U (en) * | 2018-07-12 | 2019-03-01 | 福建省农业科学院土壤肥料研究所 | A kind of fully automatic culculating reaction liquid fertilizer production equipment |
| CN209061050U (en) * | 2018-10-31 | 2019-07-05 | 嘉兴耐源电器有限公司 | A kind of Full-automatic electrolytic liquid configuration equipment |
| CN209271346U (en) * | 2018-12-05 | 2019-08-20 | 山东兰桥医学科技有限公司 | A kind of large capacity deployment platform |
| CN209828953U (en) * | 2019-04-11 | 2019-12-24 | 河南华瑞高新材料有限公司 | Filter equipment of high-efficient circulation of electrolyte |
| CN211585311U (en) * | 2019-12-25 | 2020-09-29 | 四川星明能源环保科技有限公司 | Low-cost vanadium electrolyte production system |
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