CN109004290A - A kind of heavy-duty battery constant temperature formation system and its use technique - Google Patents
A kind of heavy-duty battery constant temperature formation system and its use technique Download PDFInfo
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- CN109004290A CN109004290A CN201810907848.0A CN201810907848A CN109004290A CN 109004290 A CN109004290 A CN 109004290A CN 201810907848 A CN201810907848 A CN 201810907848A CN 109004290 A CN109004290 A CN 109004290A
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- 238000006243 chemical reaction Methods 0.000 claims abstract description 36
- 239000000126 substance Substances 0.000 claims abstract description 36
- 239000002253 acid Substances 0.000 claims abstract description 18
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims description 66
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000005192 partition Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- 239000011149 active material Substances 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000009529 body temperature measurement Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Classifications
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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
- H01M10/06—Lead-acid accumulators
- H01M10/12—Construction or manufacture
-
- 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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
- H01M10/613—Cooling or keeping cold
-
- 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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
- H01M10/615—Heating or keeping warm
-
- 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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/61—Types of temperature control
- H01M10/617—Types of temperature control for achieving uniformity or desired distribution of temperature
-
- 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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/63—Control systems
- H01M10/633—Control systems characterised by algorithms, flow charts, software details or the like
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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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/63—Control systems
- H01M10/637—Control systems characterised by the use of reversible temperature-sensitive devices, e.g. NTC, PTC or bimetal devices; characterised by control of the internal current flowing through the cells, e.g. by switching
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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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/65—Means for temperature control structurally associated with the cells
- H01M10/655—Solid structures for heat exchange or heat conduction
- H01M10/6556—Solid parts with flow channel passages or pipes for heat exchange
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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
- H01M10/60—Heating or cooling; Temperature control
- H01M10/65—Means for temperature control structurally associated with the cells
- H01M10/656—Means for temperature control structurally associated with the cells characterised by the type of heat-exchange fluid
- H01M10/6567—Liquids
- H01M10/6568—Liquids characterised by flow circuits, e.g. loops, located externally to the cells or cell casings
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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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Abstract
The invention discloses a kind of heavy-duty battery constant temperature formation system and its use technique, including battery conveying line, circulation, the chemical conversion sink with water circulatory function and the assembly line with water circulatory function, it is as follows using processing step: battery being subjected to acid adding first, battery is put into the assembly line with water circulatory function again, it is cooled down, then flow into battery restocking pipeline, battery is transferred to the chemical conversion sink with water circulatory function by battery restocking lift cart, battery is connected into charging cable, formation charging is carried out to battery according to technique in 1-2h.The invention has the advantages that by setting multisection type charge and discharge on charge technology, control the generation of cell heat in charge and discharge process, the temperature of control loop water water inlet and the flow of recirculated water, ensure that the temperature of Battery formation overall process is controlled at 35 ± 2 degrees Celsius, so that the pole plate upper, middle and lower active material chemical conversion for the battery being prepared is uniform, battery consistency is good, and performance is stablized.
Description
Technical field
The present invention relates to battery production equipment fields, and in particular to a kind of heavy-duty battery constant temperature formation system and its use
Technique.
Background technique
As country forbids the production containing cadmium cell and tank formation battery, power battery is all adjusted in recent years in no cadmium
It is melted into production technology, battery, in formation process, leads to battery mistake as the control of chemical conversion condition is bad using the key problem in technology being internalized into
It fills or charge less can seriously affect service life of battery.An essential condition in battery forming process is temperature, different temperature
The active material transformation efficiency and charge acceptance of lower battery are different, and China region extensively makes a clear distinction between the four seasons, and winter temperature is low, chemical conversion
Effect is poor, easily occurs being melted into impermeable phenomenon, summer temp is high, the phenomenon that overcharges easily occurs.It is sent out by research in recent years
Existing battery formation effect under conditions of 30-45 DEG C is more satisfactory, some producers pass through air-conditioning, ice cube, insulated wall, cooling water
Etc. modes cool down to chemical conversion environment, be not high expensive by the cooling of these modes be exactly that effect is undesirable, cannot be fine
The chemical conversion condition of ground control battery.
Summary of the invention
In order to solve the above technical problems, the present invention provides a kind of heavy-duty battery constant temperature formation system and its using work
Skill, it can be ensured that uniformly, battery consistency is good, and performance is stablized for the pole plate upper, middle and lower active material chemical conversion for the battery being prepared.
The technical solution adopted by the present invention is that:
A kind of heavy-duty battery constant temperature formation system, including battery conveying line, circulation, with the chemical conversion water of water circulatory function
Slot and assembly line with water circulatory function;
The battery conveying line includes battery restocking pipeline and battery undercarriage pipeline, the battery restocking pipeline and battery
Undercarriage pipeline is located at the chemical conversion sink both ends with water circulatory function, is additionally provided with battery by the battery restocking pipeline
Restocking lift cart is provided with battery undercarriage lift cart by battery undercarriage pipeline;
The circulation includes the cooling circulating water system and heated circulating water systems separated with partition wall, the cooling cycle
Water system includes water cooling pond and the cooling tower in cooling pond, and the heated circulating water systems include hot-tub and installation
Steam-heating system on hot-tub outer wall;
The assembly line with water circulatory function is connected by circulating water inlet road with circulation, and the band water follows
The assembly line side of ring function is provided with several acid adding machines;
The chemical conversion sink with water circulatory function passes through circulating water inlet road and circulating water outlet pipe road and recirculated water respectively
System is connected.
Further, it there are six the acid adding machine is total to, is arranged side by side in the assembly line side with water circulatory function, the band
There are six the chemical conversion sink of water circulatory function is total.
Further, recirculated water influent pressure is provided at close circulation position on the circulating water inlet road
Power surge tank.
Further, the hot-tub and water cooling pond pass through pipeline respectively and are connected with circulating water inlet road, hot-tub
It is connected with water cooling pond also by pipeline, is provided with hot water on the connecting pipe between the hot-tub and circulating water inlet road
Turn circulating water pressure pot valve and hot water intake pump, is provided on the connecting pipe between the water cooling pond and circulating water inlet road
Cold water intake pump is provided with hot water on the connecting pipe between the hot-tub and water cooling pond and turns cooling system valve.
Further, the battery restocking lift cart is located at battery restocking pipeline and the chemical conversion water with water circulatory function
Between slot, the battery undercarriage lift cart is located between battery undercarriage pipeline and chemical conversion sink with water circulatory function.
Further, sensor for measuring temperature A is installed in the hot-tub, temperature measurement sensing is installed in water cooling pond
Device B.
Further, further include power control cabinet, the sensor for measuring temperature A, sensor for measuring temperature B, hot water into
Water pump, cold water intake pump, steam-heating system, cooling tower, hot water turn circulating water pressure pot valve and hot water turns cooling system valve
It is connected respectively with power control cabinet.
A kind of use technique of heavy-duty battery constant temperature formation system, specific operation process are as follows:
Battery is put into acid adding machine first and carries out acid adding, battery is put into the assembly line with water circulatory function after acid adding,
Battery cooling 15min or more in the assembly line with water circulatory function, then flows into battery restocking pipeline, passes through battery restocking
Battery is transferred to the chemical conversion sink with water circulatory function by lift cart, battery is connected charging cable, according to as follows in 1-2h
Technique carries out formation charging to battery:
。
The beneficial effects of the present invention are: being controlled in charge and discharge process by multisection type charge and discharge are set on charge technology
The generation of cell heat, winter make full use of the heat that itself is generated in battery forming process, the temperature of control loop water water inlet
And the flow of recirculated water, it is ensured that the temperature of Battery formation overall process is controlled at 35 ± 2 degrees Celsius, so that the battery being prepared
Uniformly, battery consistency is good for the chemical conversion of pole plate upper, middle and lower active material, and performance is stablized.
Detailed description of the invention
Fig. 1 is the structural diagram of the present invention.
Fig. 2 is the structural schematic diagram of the chemical conversion sink in the present invention with water circulatory function.
Wherein: 1, battery conveying line, 2, circulation, 3, the chemical conversion sink with water circulatory function, 4, band water circulation function
Can assembly line, 5, battery restocking lift cart, 6, acid adding machine, 7, circulating water inlet road, 8, circulating water outlet pipe road, 9, follow
Ring water intake pressure surge tank, 10, power control cabinet, 11, battery restocking pipeline, 12, battery undercarriage pipeline, 13, battery
Decline lift cart, 21, cooling circulating water system, 22, heated circulating water systems, 23, hot water turn cooling system valve, 24, partition wall,
211, water cooling pond, 212, cooling tower, 213, cold water intake pump, 214, sensor for measuring temperature B, 221, hot-tub, 222, steaming
Vapour heating system, 223, hot water turn circulating water pressure pot valve, 224, hot water intake pump, 225, sensor for measuring temperature A.
Specific embodiment
In order to deepen the understanding of the present invention, below in conjunction with embodiment and attached drawing, the invention will be further described, should
The examples are only for explaining the invention, does not restrict the protection scope of the present invention.
As depicted in figs. 1 and 2, a kind of heavy-duty battery constant temperature formation system, including battery conveying line 1, circulation
2, chemical conversion sink 3, power control cabinet 10 and the assembly line 4 with water circulatory function with water circulatory function;
Battery conveying line 1 includes battery restocking pipeline 11 and battery undercarriage pipeline 12, battery restocking pipeline 11 and battery
Undercarriage pipeline 12 is located at 3 both ends of chemical conversion sink with water circulatory function, is additionally provided with electricity by battery restocking pipeline 11
Pond restocking lift cart 5 is additionally provided with battery undercarriage lift cart 13, battery restocking lift cart by battery undercarriage pipeline 12
5 between battery restocking pipeline 11 and the chemical conversion sink 3 with water circulatory function, and battery undercarriage lift cart 13 is located at battery
Between undercarriage pipeline 12 and the chemical conversion sink 3 recycled with water;
Circulation 2 includes the cooling circulating water system 21 and heated circulating water systems 22 separated with partition wall 24, cooling cycle
Water system 21 includes water cooling pond 211 and the cooling tower 212 in cooling pond 211, and cooling tower 212 adds there are two being total to
Heat recirculated water system 22 includes hot-tub 221 and the steam-heating system 222 being mounted on 221 outer wall of hot-tub;
Assembly line 4 with water circulatory function is connected by circulating water inlet road 7 with circulation 2, and recycles function with water
There are six acid adding machine 6, six acid adding machines 6 are arranged side by side in 4 side of assembly line with water circulatory function for 4 side of the assembly line setting of energy
Side;
There are six chemical conversion sink 3 with water circulatory function is total, pass through circulating water inlet road 7 and circulating water outlet pipe road respectively
8 are connected with circulation 2;
Further, recirculated water intake pressure buffering is provided on circulating water inlet road 7 at close 2 position of circulation
Tank 9;
In present embodiment, recirculated water intake pressure is provided at close 2 position of circulation on circulating water inlet road 7
Surge tank 9, to cache the water in hot-tub 221 and water cooling pond 211;
Further, hot-tub 211 and water cooling pond 221 are connected by pipeline with circulating water inlet road 7 respectively, hot-tub
221 are connected with water cooling pond 211 also by pipeline, are arranged on the connecting pipe between hot-tub 221 and circulating water inlet road 7
There is hot water to turn circulating water pressure pot valve 223 and hot water intake pump 224, the connection between water cooling pond 211 and circulating water inlet road 7
It is provided with cold water intake pump 213 on pipeline, hot water is provided on the connecting pipe between hot-tub 221 and water cooling pond 211 and turns cold
But system valve 23;
In present embodiment, hot-tub 211 and water cooling pond 221 are connected by pipeline with circulating water inlet road 7 respectively, hot water
Pond 221 is connected with water cooling pond 211 also by pipeline, sets on the connecting pipe between hot-tub 221 and circulating water inlet road 7
It is equipped with hot water and turns circulating water pressure pot valve 223 and hot water intake pump 224, for controlling the discharge of water in hot-tub 221, water cooling pond
Cold water intake pump 213 is provided on connecting pipe between 211 and circulating water inlet road 7, for controlling water in water cooling pond 211
Discharge, be provided with hot water on the connecting pipe between hot-tub 221 and water cooling pond 211 and turn cooling system valve 23, for controlling
The circulation of water between water cooling pond 211 and hot-tub 221;
Further, sensor for measuring temperature A225 is installed in hot-tub 221, temperature measurement is installed in water cooling pond 211 and is passed
Sensor B214, sensor for measuring temperature A225, sensor for measuring temperature B214, hot water intake pump 224, cold water intake pump 213, heat
Water turns circulating water pressure pot valve 223 and hot water turns cooling system valve 23 and is connected respectively with power control cabinet 10;
In present embodiment, sensor for measuring temperature A225 is installed in hot-tub 221, temperature survey is installed in water cooling pond 211
Quantity sensor B214, sensor for measuring temperature A225, sensor for measuring temperature B214, hot water intake pump 224, cold water intake pump
213, steam-heating system 222, cooling tower 212, hot water turn circulating water pressure pot valve 223 and hot water turns cooling system valve 23 and divides
It is not connected with power control cabinet 10, it is sensor for measuring temperature A225, sensor for measuring temperature B214, hot water intake pump 224, cold
Water intake pump 213, hot water turn circulating water pressure pot valve 223 and hot water turns cooling system valve 23 and controlled by power control cabinet 10
System;
A kind of operation logic of above-mentioned heavy-duty battery constant temperature formation system is as follows: sensor for measuring temperature A225 and temperature measurement
Sensor B214 is respectively monitored the temperature in hot-tub 221 and water cooling pond 211, and sends monitoring result to power control
Cabinet 10 processed, power control cabinet 10 analyze the temperature monitoring result received:
When the temperature in hot-tub 221 is lower than 33 DEG C, power control cabinet 10 is issued to steam-heating system 222 and is instructed, steam
Heating system 222 heats the water in hot-tub 221, when the temperature in hot-tub 221 reaches 35 ± 2 DEG C, power control
Cabinet 10 processed starts hot water intake pump 224, opens hot water and turns circulating water pressure pot valve 223, recirculated water enters recirculated water along pipeline
Intake pressure surge tank 9 is then sent into recirculated water point of use by circulating water inlet road 7, including the change with water circulatory function
It is recycled respectively from the chemical conversion sink 3 with water circulatory function and with water at sink 3 with the assembly line with water circulatory function 4, recirculated water
The bottom of the assembly line 4 of function enters wherein, then flows out to circulating water outlet pipe road 8 from the overflow port on top, goes out through recirculated water
Waterpipe 8 is flow back into again in hot-tub 221, forms a closed loop;
When the temperature in hot-tub 221 is at 33--37 DEG C, start hot water intake pump 224, opens hot water and turn circulating water pressure tank
Valve 223, recirculated water enter recirculated water intake pressure surge tank 9, are then sent into recirculated water by circulating water inlet road 7 and use
Point, including the chemical conversion sink 3 with water circulatory function and the assembly line 4 with water circulatory function, recirculated water recycles function from band water respectively
The chemical conversion sink 3 of energy and the bottom of the assembly line 4 with water circulatory function enter wherein, then flow out to circulation from the overflow port on top
Water outlet conduit 8 is flow back into hot-tub 221 again through circulating water outlet pipe road 8, forms a closed loop;
When the temperature in hot-tub 221 is greater than 37 DEG C, starts hot water intake pump 224, open simultaneously hot water and turn cooling system valve
23, the hot water in hot-tub 221 enters in water cooling pond 211, and power control cabinet 10 is according in hot-tub 221 and water cooling pond 211
Temperature adjusts the cooling air quantity of the cooling tower 212 in water cooling pond 211, when the temperature in water cooling pond 211 reaches 35 ± 2 DEG C,
Start cold water intake pump 213, recirculated water enters in recirculated water intake pressure surge tank 9 from water cooling pond 211, then by circulation
Water water inlet line 7 is sent into recirculated water point of use, including the chemical conversion sink 3 with water circulatory function and the assembly line with water circulatory function
4, recirculated water enters wherein from the bottom of the chemical conversion sink 3 with water circulatory function and the assembly line 4 with water circulatory function respectively, then
Circulating water outlet pipe road 8 is flowed out to from the overflow port on top, is flow back into hot-tub 221 again through circulating water outlet pipe road 8, is formed
One closed loop.
A kind of use technique of above-mentioned heavy-duty battery constant temperature formation system, specific operation process are as follows: first by battery
It is put into acid adding machine 6 and carries out acid adding, because active material in battery and acid can react and generate a large amount of heat moment, after acid adding
Battery is put into the assembly line 4 with water circulatory function, battery cooling 15min in the assembly line 4 with water circulatory function in 2min
More than, battery restocking pipeline 11 is then flowed into, battery is transferred to by the change with water circulatory function by battery restocking lift cart 5
At sink 3, battery is connected into charging cable, formation charging is carried out (with 12V20Ah electricity to battery according to following technique in 1-2h
For pool process):
,
Charging is finished to go on battery undercarriage pipeline 12 by battery undercarriage lift cart 13 and be exported;
The battery performance comparison for battery and the conventional method production prepared using the present invention is as shown in the table:
The present invention is by controlling the generation of cell heat in charge and discharge process, winter to multisection type charge and discharge are set on charge technology
Make full use of the heat that itself is generated in battery forming process, the temperature of control loop water water inlet and the flow of recirculated water season, really
The temperature for protecting Battery formation overall process is controlled at 35 ± 2 degrees Celsius, so that the pole plate upper, middle and lower active matter for the battery being prepared
Uniformly, battery consistency is good for matter chemical conversion, and performance is stablized.
Claims (8)
1. a kind of heavy-duty battery constant temperature formation system, which is characterized in that followed including battery conveying line, circulation, band water
The chemical conversion sink of ring function and the assembly line with water circulatory function;
The battery conveying line includes battery restocking pipeline and battery undercarriage pipeline, the battery restocking pipeline and battery
Undercarriage pipeline is located at the chemical conversion sink both ends with water circulatory function, is additionally provided with battery by the battery restocking pipeline
Restocking lift cart is provided with battery undercarriage lift cart by battery undercarriage pipeline;
The circulation includes the cooling circulating water system and heated circulating water systems separated with partition wall, the cooling cycle
Water system includes water cooling pond and the cooling tower in cooling pond, and the heated circulating water systems include hot-tub and installation
Steam-heating system on hot-tub outer wall;
The assembly line with water circulatory function is connected by circulating water inlet road with circulation, and the band water follows
The assembly line side of ring function is provided with several acid adding machines;
The chemical conversion sink with water circulatory function passes through circulating water inlet road and circulating water outlet pipe road and recirculated water respectively
System is connected.
2. a kind of heavy-duty battery constant temperature formation system according to claim 1, which is characterized in that the acid adding machine is shared
Six, be arranged side by side in the assembly line side with water circulatory function, the chemical conversion sink with water circulatory function altogether there are six.
3. a kind of heavy-duty battery constant temperature formation system according to claim 1, which is characterized in that the recirculated water water inlet
Recirculated water intake pressure surge tank is provided at close circulation position on pipeline.
4. a kind of heavy-duty battery constant temperature formation system according to claim 1, which is characterized in that the hot-tub and cold
Pond passes through pipeline respectively and is connected with circulating water inlet road, and hot-tub is connected with water cooling pond also by pipeline, the heat
It is provided with hot water on connecting pipe between pond and circulating water inlet road and turns circulating water pressure pot valve and hot water intake pump, institute
State and be provided with cold water intake pump on the connecting pipe between water cooling pond and circulating water inlet road, the hot-tub and water cooling pond it
Between connecting pipe on be provided with hot water and turn cooling system valve.
5. a kind of heavy-duty battery constant temperature formation system according to claim 1, which is characterized in that the battery restocking liter
Drop trolley is located between battery restocking pipeline and chemical conversion sink with water circulatory function, and the battery undercarriage lift cart is located at
Between battery undercarriage pipeline and chemical conversion sink with water circulatory function.
6. a kind of heavy-duty battery constant temperature formation system according to claim 1, which is characterized in that peace in the hot-tub
Equipped with sensor for measuring temperature A, sensor for measuring temperature B is installed in water cooling pond.
7. according to claim 1 to a kind of heavy-duty battery constant temperature formation system described in 6, which is characterized in that further include power
Control cabinet, the sensor for measuring temperature A, sensor for measuring temperature B, hot water intake pump, cold water intake pump, steam heating system
System, cooling tower, hot water turn circulating water pressure pot valve and hot water turns cooling system valve and is connected respectively with power control cabinet.
8. special according to claim 1 to a kind of use technique of heavy-duty battery constant temperature formation system described in 6 any one
Sign is that specific operation process is as follows:
Battery is put into acid adding machine first and carries out acid adding, battery is put into the assembly line with water circulatory function after acid adding,
Battery cooling 15min or more in the assembly line with water circulatory function, then flows into battery restocking pipeline, passes through battery restocking
Battery is transferred to the chemical conversion sink with water circulatory function by lift cart, battery is connected charging cable, according to as follows in 1-2h
Technique carries out formation charging to battery:
。
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