CN203323522U - Rotary wheel type battery core baking system for battery pole piece - Google Patents
Rotary wheel type battery core baking system for battery pole piece Download PDFInfo
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- CN203323522U CN203323522U CN2013203324520U CN201320332452U CN203323522U CN 203323522 U CN203323522 U CN 203323522U CN 2013203324520 U CN2013203324520 U CN 2013203324520U CN 201320332452 U CN201320332452 U CN 201320332452U CN 203323522 U CN203323522 U CN 203323522U
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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
- 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
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
The utility model discloses a rotary wheel type battery core baking system for a battery pole piece. The rotary wheel type battery core baking system is characterized in that a rotary wheel is provided with a moisture absorption area, a residual heat recovery area and a regeneration area, wherein a fresh air inlet and a clean dry air outlet are respectively arranged at the left and right sides of the moisture absorption area, a filter, a primary surface cooler, a dehumanization fan and a secondary surface cooler are sequentially connected between the fresh air inlet and the moisture absorption area, the dehumidification fan is connected with a heat exchanger through a return air heat outlet exchanger pipeline, a regeneration air inlet pipeline and a regeneration air outlet pipeline are respectively arranged on the left and right sides of the residual heat recovery area, the regeneration air inlet pipeline is connected with the outlet of the secondary surface cooler, the regeneration air outlet pipeline is connected with an electrical heater, the outlet of the electrical heater is connected with the regeneration area through a pipeline, and the clean dry air outlet is connected with the heat exchanger through a clean dry air heat inlet exchanger pipeline. The rotary wheel type battery core baking system for the battery pole piece has the advantages of air drying and purification, environmental protection and energy conservation.
Description
Technical field
The utility model relates to the air dewetting technical field, relates in particular to a kind of rotary-type battery pole piece battery core baking system.
Background technology
Rotary dehumidifier belongs to an important branch of field of air conditioning, it is the Typical Representative that heats up and dehumidify, the rotary dehumidifier critical piece is runner, wheel surface is coated with hygroscopic agent, and surface is provided with cellular porous road, by the slow circumvolve runner, can adsorb the moisture in the humid air that flows through this runner, runner after moisture absorption dries and blows through the high temperature drying air-flow, can make hygroscopic agent dehydration regeneration, regenerated air heater in current rotary dehumidifier, all need lot of energy to carry out the thermal regeneration air, caused the wasting of resources, therefore current rotary dehumidifier exists the regeneration energy consumption high, the wasting of resources, the shortcoming of contaminated environment.
Summary of the invention
The utility model is high for traditional rotary dehumidifier regeneration energy consumption, the problem of the wasting of resources, contaminated environment; a kind of rotary-type battery pole piece battery core baking system is provided; return air advances heat-exchanger pipeline and return air goes out between heat-exchanger pipeline to be provided with heat exchanger; be used for heating clean dry air; make waste heat be recovered utilization; thereby saved the energy consumption that heats clean dry air with electric heater; this equipment utilization purge drying hot-air baking battery pole piece, battery core; protection of the environment, save the energy.
The technical solution of the utility model is: a kind of rotary-type battery pole piece battery core baking system, comprise runner, and it is characterized in that: described runner is provided with the moisture absorption district, waste heat recovery district and renewing zone, described moisture absorption district the right and left is respectively arranged with outdoor fresh air import and the outlet of clean dry air, and filtering cartridge filter has been linked in sequence between described outdoor fresh air import and moisture absorption district, the one-level surface-cooler, the dehumidifying blower fan, the secondary surface cooler, described dehumidifying blower fan goes out heat-exchanger pipeline by return air and connects heat exchanger, described waste heat recovery district the right and left is respectively arranged with regeneration air inlet pipeline and regeneration air outlet conduit, described regeneration air inlet pipeline is connected with the secondary surface cooler outlet, described regeneration air outlet conduit is connected with electric heater, the electric heater outlet connects renewing zone by pipeline, and renewing zone connects the regeneration blower fan by pipeline, the regeneration air outlet, described clean dry air outlet is advanced heat-exchanger pipeline by clean dry air and is connected with heat exchanger, and heat exchanger goes out heat-exchanger pipeline and an electric heater by clean dry air, No. two electric heaters, No. three electric heater connects respectively, an electric heater, No. two electric heaters, No. three electric heaters more separately respectively with an imported valve, No. two imported valves, No. three imported valve connects, an imported valve, No. two imported valves, No. three imported valves more separately respectively with a high efficiency particulate air filter, No. two high efficiency particulate air filters, No. three high efficiency particulate air filter connects, a high efficiency particulate air filter, No. two high efficiency particulate air filters, No. three high efficiency particulate air filters more separately respectively with a battery pole piece battery core baking box, C-size battery pole piece battery core baking box, No. three battery pole piece battery core baking box connects, a battery pole piece battery core baking box, C-size battery pole piece battery core baking box, No. three battery pole piece battery core baking boxes more separately respectively with an outlet valve, No. two outlet valves, No. three outlet valve connects, an outlet valve, No. two outlet valves, No. three outlet valves jointly advance heat-exchanger pipeline by return air and are connected with heat exchanger.
The beneficial effects of the utility model are: by filtering cartridge filter, collect the fine solid particle in gas, purify air; At moisture absorption district the right and left, outdoor fresh air import and the outlet of clean dry air are set respectively, after the moisture absorption district absorbs, send indoor by clean dry air outlet by the moisture in outdoor fresh air; By regeneration air outlet and electric heater are set respectively at renewing zone the right and left, by the regeneration air heating is entered to renewing zone, and export discharged to atmosphere by regeneration air; Return air advances heat-exchanger pipeline and return air goes out between heat-exchanger pipeline to be provided with heat exchanger; be used for heating clean dry air; make waste heat be recovered utilization; thereby saved the energy consumption that heats clean dry air with heater; the contrast prior art; this equipment has the purge drying air, protection of the environment, the advantage of saving the energy.
The utility model has the advantage of:
1, by air cleaner, collect the fine solid particle in gas, purify air;
2, the inside of the heat exchange unit of heat exchanger does not exist solder joint and weld seam, and plate and the heat exchange unit thermal stress that the adaptive temperature gradient causes has effectively strengthened opposing thermal cycling fatigue ability greatly; Heat transference efficiency is high, and hot side liquid and cold-side fluid are via plate, directly carry out heat exchange, and hot transfer efficiency is high, and heat exchange efficiency can reach 92%;
3, the efficiency of waste heat recovery reaches 90%, saves the energy, has reduced the pollution to environment.
The accompanying drawing explanation
Fig. 1 is apparatus structure schematic diagram of the present utility model.
In figure: 1. regeneration air import, 2. regeneration blower fan, 3. renewing zone, 4. runner, 5. waste heat recovery district, 6. electric heater, 7. regeneration air inlet pipeline, 8. regeneration air outlet conduit, 9. outdoor fresh air import, 10. filtering cartridge filter, 11. one-level surface-cooler, 12. dehumidifying blower fan, 13. secondary surface cooler, 14. moisture absorption district, 15. clean dry air outlet, a 16. electric heater, a 17. imported valve, a 18. high efficiency particulate air filter, a 19. battery pole piece battery core baking box, a 20. outlet valve, 21. No. two electric heaters, 22. No. two imported valves, 23. No. two high efficiency particulate air filters, 24. C-size battery pole piece battery core baking box, 25. No. two outlet valves, 26. No. three electric heaters, 27. No. three imported valves, 28. No. three high efficiency particulate air filters, 29. No. three battery pole piece battery core baking boxes, 30. No. three outlet valves, 31. return air advances heat-exchanger pipeline, 32. return air goes out heat-exchanger pipeline, 33. clean dry air advances heat-exchanger pipeline, 34. heat exchanger, 35. clean dry air goes out heat-exchanger pipeline.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
In the utility model, a kind of rotary-type battery pole piece battery core baking system, comprise runner 4, and it is characterized in that: described runner 4 is provided with moisture absorption district 14, waste heat recovery district 5 and renewing zone 3, described moisture absorption district 14 the right and lefts are respectively arranged with outdoor fresh air import 9 and clean dry air outlet 15, and filtering cartridge filter 10 has been linked in sequence between described outdoor fresh air import 9 and moisture absorption district 14, one-level surface-cooler 11, dehumidifying blower fan 12, secondary surface cooler 13, described dehumidifying blower fan 12 goes out heat-exchanger pipeline 32 by return air and connects heat exchanger 34, described waste heat recovery district 5 the right and lefts are respectively arranged with regeneration air inlet pipeline 7 and regeneration air outlet conduit 8, described regeneration air inlet pipeline 7 is connected with 13 outlets of secondary surface cooler, described regeneration air outlet conduit 8 is connected with electric heater 6, electric heater 6 outlets connect renewing zone 3 by pipeline, and renewing zone 3 connects regeneration blower fan 2 by pipeline, regeneration air outlet 1, described clean dry air outlet 15 is advanced heat-exchanger pipeline 33 by clean dry air and is connected with heat exchanger 34, heat exchanger 34 by clean dry air go out heat-exchanger pipeline 35 respectively with an electric heater 16, No. two electric heaters 21, No. three electric heater 26 connects, an electric heater 16, No. two electric heaters 21, No. three electric heaters 26 separately respectively with an imported valve 17, No. two imported valves 22, No. three imported valve 27 connects, an imported valve 17, No. two imported valves 22, No. three imported valves 27 more separately respectively with a high efficiency particulate air filter 18, No. two high efficiency particulate air filters 23, No. three high efficiency particulate air filter 28 connects, a high efficiency particulate air filter 18, No. two high efficiency particulate air filters 23, No. three high efficiency particulate air filters 28 more separately respectively with a battery pole piece battery core baking box 19, C-size battery pole piece battery core baking box 24, No. three battery pole piece battery core baking box 29 connects, a battery pole piece battery core baking box 19, C-size battery pole piece battery core baking box 24, No. three battery pole piece battery core baking boxes 29 more separately respectively with an outlet valve 20, No. two outlet valves 25, No. three outlet valve 30 connects, an outlet valve 20, No. two outlet valves 25, No. three outlet valves 30 jointly advance heat-exchanger pipeline 31 by return air and are connected with heat exchanger 34.
The course of work of the present utility model: outdoor fresh air (air quantity 1000m
3/ h, 35 ℃ of temperature, humidity 70%, water capacity 25g/kg) by outdoor fresh air import 9, at first through filtering cartridge filter 10, filter, remove impurity, then through one-level surface-cooler 11, cooling rear (air quantity 1000m
3/ h, 13 ℃ of temperature, humidity 97%, water capacity 9g/kg), dehumidifying blower fan 12 is from return air inlet inspiration return air (air quantity 6000m
3/ h, 25 ℃ of temperature, humidity 0.57%, water capacity 0.11g/kg) mix (air quantity 7000m with one-level surface-cooler 12 humid air out
3/ h, 25 ℃ of temperature, humidity 7.2%, water capacity 1.4g/kg) enter secondary surface cooler 13, cooling after (air quantity 7000m
3/ h, 13 ℃ of temperature, humidity 15.2%, water capacity 1.4g/kg), then enter the moisture absorption district 14 that runner 4 arranges, by (the air quantity 5000m of the moisture absorption in outdoor fresh air
3/ h, 17 ℃ of temperature, humidity 0.2%, water capacity 0.012g/kg), become clean dry air (air quantity 5000m
3/ h, 17 ℃ of temperature, humidity 0.1%, water capacity 0.01g/kg) from clean dry air outlet 15, discharge, advance heat-exchanger pipeline 33 by clean dry air and enter heat exchanger 34, utilize the clean dry air of waste-heat low temperature in return air, make the clean drying-air temperature rising of low temperature (air quantity 5000m
3/ h, 25 ℃ of temperature, humidity 0.01%, water capacity 0.001g/kg), go out heat-exchanger pipeline 35 by clean dry air again and enter respectively electric heater 16 No. one, No. two electric heaters 21, No. three electric heater 26 heating, open imported valve 17 No. one, No. two imported valves 22, No. three imported valves 27, enter high efficiency particulate air filter 18 No. one, No. two high efficiency particulate air filters 23, No. three high efficiency particulate air filters 28 filter removes impurity, enter battery pole piece battery core baking box 19 No. one, C-size battery pole piece battery core baking box 24, No. three battery pole piece battery core baking box 29 air cooking battery pole pieces, battery core, return air is from an outlet valve 20, No. two outlet valves 25, No. three outlet valve 30 is discharged, advance heat-exchanger pipeline 31 by return air and enter heat exchanger 34, by the heat recovery in return air, go out heat-exchanger pipeline 32 from return air again and enter dehumidifying blower fan 12, another part air (regeneration air out from secondary surface cooler 13, air quantity 2000m
3/ h, 25 ℃ of temperature, humidity 12.3%, water capacity 2.4g/kg) by regeneration air inlet pipeline 7, enter waste heat recovery district 5, preheated (the air quantity 2000m of regeneration air
3/ h, temperature 45 C, humidity 8.3%, water capacity 1.4g/kg), then enter electric heater 6 by regeneration air outlet conduit 8, (air quantity 2000m after heating
3/ h, 140 ℃ of temperature, humidity 0.82%, water capacity 0.5g/kg), then enter renewing zone 3, make the moisture vaporization of runner 4 absorption, and export 1 (air quantity 2000m by regeneration blower fan 2 from regeneration air
3/ h, temperature 45 C, humidity 13.3%, water capacity 45.6g/kg) discharged to atmosphere.
The maximum characteristics of this equipment are by filtering cartridge filter, collect the fine solid particle in gas, purify air; At moisture absorption district the right and left, outdoor fresh air import and the outlet of clean dry air are set respectively, after the moisture absorption district absorbs, send indoor by clean dry air outlet by the moisture in outdoor fresh air; By regeneration air outlet and electric heater are set respectively at renewing zone the right and left, by the regeneration air heating is entered to renewing zone, and export discharged to atmosphere by regeneration air; Return air advances heat-exchanger pipeline and return air goes out between heat-exchanger pipeline to be provided with heat exchanger; be used for heating clean dry air; make waste heat be recovered utilization; thereby saved the energy consumption that heats clean dry air with heater; the contrast prior art; this equipment has the purge drying air, protection of the environment, the advantage of saving the energy.
With 1000m
3/ h air quantity outdoor fresh air runner equipment is example, and the utility model equipment and conventional equipment relatively, are described as follows:
The technical performance of a kind of rotary-type battery pole piece battery core baking system and rotary dehumidifier commonly used relatively
As can be seen here; maximum characteristics of the present utility model be by the moisture in outdoor fresh air after the moisture absorption district absorbs; by clean dry air outlet, send back to indoor; return air advances heat-exchanger pipeline and return air goes out between heat-exchanger pipeline to be provided with heat exchanger, is used for heating clean dry air, makes waste heat be recovered utilization; thereby saved the energy consumption that heats clean dry air with heater; this equipment has the purge drying air, protection of the environment, the advantage of saving the energy.
Claims (1)
1. a rotary-type battery pole piece battery core baking system, comprise runner, and it is characterized in that: described runner is provided with the moisture absorption district, waste heat recovery district and renewing zone, described moisture absorption district the right and left is respectively arranged with outdoor fresh air import and the outlet of clean dry air, and filtering cartridge filter has been linked in sequence between described outdoor fresh air import and moisture absorption district, the one-level surface-cooler, the dehumidifying blower fan, the secondary surface cooler, described dehumidifying blower fan goes out heat-exchanger pipeline by return air and connects heat exchanger, described waste heat recovery district the right and left is respectively arranged with regeneration air inlet pipeline and regeneration air outlet conduit, described regeneration air inlet pipeline is connected with the secondary surface cooler outlet, described regeneration air outlet conduit is connected with electric heater, the electric heater outlet connects renewing zone by pipeline, and renewing zone connects the regeneration blower fan by pipeline, the regeneration air outlet, described clean dry air outlet is advanced heat-exchanger pipeline by clean dry air and is connected with heat exchanger, and heat exchanger goes out heat-exchanger pipeline and an electric heater by clean dry air, No. two electric heaters, No. three electric heater connects respectively, an electric heater, No. two electric heaters, No. three electric heaters more separately respectively with an imported valve, No. two imported valves, No. three imported valve connects, an imported valve, No. two imported valves, No. three imported valves more separately respectively with a high efficiency particulate air filter, No. two high efficiency particulate air filters, No. three high efficiency particulate air filter connects, a high efficiency particulate air filter, No. two high efficiency particulate air filters, No. three high efficiency particulate air filters more separately respectively with a battery pole piece battery core baking box, C-size battery pole piece battery core baking box, No. three battery pole piece battery core baking box connects, a battery pole piece battery core baking box, C-size battery pole piece battery core baking box, No. three battery pole piece battery core baking boxes more separately respectively with an outlet valve, No. two outlet valves, No. three outlet valve connects, an outlet valve, No. two outlet valves, No. three outlet valves jointly advance heat-exchanger pipeline by return air and are connected with heat exchanger.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203324520U CN203323522U (en) | 2013-05-31 | 2013-05-31 | Rotary wheel type battery core baking system for battery pole piece |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203324520U CN203323522U (en) | 2013-05-31 | 2013-05-31 | Rotary wheel type battery core baking system for battery pole piece |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203323522U true CN203323522U (en) | 2013-12-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013203324520U Expired - Fee Related CN203323522U (en) | 2013-05-31 | 2013-05-31 | Rotary wheel type battery core baking system for battery pole piece |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104061766A (en) * | 2014-03-27 | 2014-09-24 | 张建岗 | Drying equipment |
| CN104848673A (en) * | 2014-02-17 | 2015-08-19 | 张建岗 | Cell and pole piece drying device of rotating wheel type lithium ion battery |
| CN112138964A (en) * | 2020-10-24 | 2020-12-29 | 苏州兆和空调技术工程有限公司 | Air supply system used in battery electrode coating oven |
-
2013
- 2013-05-31 CN CN2013203324520U patent/CN203323522U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104848673A (en) * | 2014-02-17 | 2015-08-19 | 张建岗 | Cell and pole piece drying device of rotating wheel type lithium ion battery |
| CN104061766A (en) * | 2014-03-27 | 2014-09-24 | 张建岗 | Drying equipment |
| CN104061766B (en) * | 2014-03-27 | 2016-08-24 | 张建岗 | A kind of drying equipment |
| CN112138964A (en) * | 2020-10-24 | 2020-12-29 | 苏州兆和空调技术工程有限公司 | Air supply system used in battery electrode coating oven |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20171026 Address after: 214151 Jiangsu province Wuxi city Huishan District Qian Qiao Street Su Village (industrial concentration area) Patentee after: Wuxi Aobo Purifying & Dehumidifying Air Conditioner Co.,Ltd. Address before: 214151 358 Qian Qian Lu Village, Huishan District, Wuxi City, Jiangsu Patentee before: Zhang Jiangang |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 214151 Su Miao village, Qian Qiao street, Huishan District, Wuxi, Jiangsu (industrial concentration area) Patentee after: AOBO ENVIRONMENT NEW ENERGY (WUXI) Co.,Ltd. Address before: 214151 Su Miao village, Qian Qiao street, Huishan District, Wuxi, Jiangsu (industrial concentration area) Patentee before: Wuxi Aobo Purifying & Dehumidifying Air Conditioner Co.,Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131204 |