CN202309136U - Rapid charging device for lead acid storage battery - Google Patents
Rapid charging device for lead acid storage battery Download PDFInfo
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- CN202309136U CN202309136U CN201120412578XU CN201120412578U CN202309136U CN 202309136 U CN202309136 U CN 202309136U CN 201120412578X U CN201120412578X U CN 201120412578XU CN 201120412578 U CN201120412578 U CN 201120412578U CN 202309136 U CN202309136 U CN 202309136U
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Abstract
The utility model discloses a rapid charging device for a lead acid storage battery. The rapid charging device comprises an electrolyte input acid groove, an electrolyte output acid groove and a high-density electrolyte acid groove, wherein the high-density electrolyte acid groove is communicated with the electrolyte input acid groove and the electrolyte output acid groove through a first pipeline and a second pipeline respectively; an input pipeline and an output pipeline arranged on the electrolyte input acid groove and the electrolyte output acid groove are communicated with a battery respectively; the first pipeline, the second pipeline, the input pipeline and the output pipeline are provided with control valves respectively; the electrolyte input acid groove, the electrolyte output acid groove and the high-density electrolyte acid groove are provided with water injection pipelines respectively; and the high-density electrolyte acid groove is provided with an acid injection pipeline. The time consumption of the rapid charging device is 35-40 hours, the service life of the battery is not influenced while the charging efficiency of the battery is increased, the container formation production period of the battery is shortened greatly, and the production cost is saved.
Description
Technical field
The utility model relates to a kind of accumulator charging technology, is specifically related to a kind of quick charge acid circulation system of lead acid accumulator.
Background technology
Storage battery is internalized into charging technique, is that a kind of pole plate is internalized into charging at battery case, and cost is little, pollution is low, workman's health hazard ratio is changed into little technology outward.In being internalized into charging, temperature is wayward, and charge efficiency is low to be the problem that always exists, and most of producer solves this problem with prolongation charging interval, increase charge volume, but therefore brings the production cycle long, problems such as production cost increase; Also have part producer to attempt to increase the unit interval current charges, but battery meeting Yin Wendu is too high, and has a strong impact on its cycle life.Be difficult to accomplish the short time charging and do not influence battery performance in present technical merit.
Summary of the invention
The technical problem that the utility model will solve provides
OnePlant the lead acid accumulator quick charge device, provide simultaneously and utilize this device fast charge method, making it can reach higher charge efficiency does not at short notice influence battery performance again.
The utility model is realized through following technical scheme:
OnePlant the lead acid accumulator quick charge device; Comprise electrolyte input acid tank, electrolyte output acid tank, high density electrolyte acid tank; Said high density electrolyte acid tank is communicated with electrolyte input acid tank, electrolyte output acid tank respectively through first, second set pipeline, and said electrolyte input acid tank, electrolyte output acid tank are communicated with battery respectively through set input, output channel; First, second pipeline, and be respectively equipped with control valve in the input, output channel; Electrolyte input acid tank, electrolyte output acid tank, high density electrolyte acid tank are respectively equipped with filling pipe, and its middle-high density electrolyte acid tank also is provided with annotates the acid tube road.
The further improvement project of the utility model is that after electrolyte input acid tank, set input, the output channel of electrolyte output acid tank inserted battery container, the output channel insertion depth was deeper than input channel.The output channel insertion end is near the surface of the bus-bar in the housing.
The utility model further improvement project is, said control valve is an electronic valve, and said control valve is electrically connected with controller.Be provided with temperature, sulfuric acid density regulating apparatus in electrolyte input acid tank, electrolyte output acid tank, the high density electrolyte acid tank, said adjusting device is electrically connected with controller respectively.
With above-mentioned
OnePlant lead acid accumulator and be internalized into the method that device is internalized into fast, comprise the following steps:
(1) electrolyte is imported input, the output channel of acid tank, electrolyte output acid tank; In the housing like claim 2 or 3 said insertion batteries; Under the control of controller, first pipeline control valve is opened, and the quantitative output density of high density electrolyte acid tank is 1.4 g/cm
3Electrolyte to electrolyte input acid tank in, carry finish after, first pipeline control valve is closed, to adjust to density be 1.1 g/cm to electrolyte input acid tank from being about to electrolyte
3, the input channel control valve is opened subsequently, quantitative be delivered to electrolyte in the battery after, left standstill 2 hours;
(2) with the current charges of 0.15-0.25C/n ampere/sheet at least 3 hours; Then with the current charges of 0.3-0.45C/n ampere/sheet at least 15 hours; Then the electric current with 0.23-0.32C/n ampere/sheet discharged 2 hours at least, again with the current charges of 0.25-0.4C/n ampere/sheet at least 8 hours; In this process, under the control of controller, input, output channel control valve are opened, and first, second pipeline control valve is closed, and carries out the cold and hot exchange of electrolyte, and the electrolyte temperature in the battery is controlled at about 40 ℃;
(3) with the current charges of 0.25-0.45C/n ampere/sheet at least 3 hours, then with the current charges of 0.15-0.25C/n ampere/sheet at least 7 hours; In this process, under the control of controller, input, output channel control valve, and first, second pipeline control valve all opens, it is 1.4 g/cm that high density electrolyte acid tank is carried density
3Electrolyte, electrolyte input acid tank, electrolyte output acid tank carry out exchange of electrolyte, and accomplish in preceding 0.5 hour in charging the density of electrolyte in the battery is adjusted to 1.280～1.300g/cm
3
Battery through the 3DBS210 of quick charge gained; Its 5 hour rate capacity, high-rate discharge ability, cycling durable experimental performance all are not less than national standard, and be as shown in the table:
The utility model compared with prior art; Advantage is: it is consuming time for more than (80～100) hour that conventional storage battery is internalized into charge technology; And the utility model consuming time be (35～40) hour, in the charge efficiency that has improved battery, do not influence battery life; Shorten being internalized into the production cycle of battery greatly, practiced thrift production cost.
Description of drawings
Fig. 1 is the device sketch map in the utility model.
Embodiment
It is as shown in Figure 1,
OnePlant the lead acid accumulator quick charge device; Comprise electrolyte input acid tank 1, electrolyte output acid tank 2, high density electrolyte acid tank 3; Said high density electrolyte acid tank 3 is communicated with electrolyte input acid tank 1, electrolyte output acid tank 2 respectively through first, second set pipeline, and said electrolyte input acid tank 1, electrolyte output acid tank 2 are communicated with battery 9 respectively through set input, output channel; First, second pipeline, and be respectively equipped with control valve (that is: input, output channel control valve 5,6, first, second pipeline control valve 4,7) in the input, output channel; Electrolyte input acid tank 1, high density electrolyte acid tank 3 are respectively equipped with filling pipe 10, and its middle-high density electrolyte acid tank also is provided with annotates acid tube road 11.Said filling pipe 10 is communicated with the pure water pipeline, and said notes acid tube road 11 is communicated with (diagram is not provided) with acid tank.
After electrolyte input acid tank 1, electrolyte output acid tank 2 set input, output channels inserted battery container, the output channel insertion depth was deeper than input channel, and the output channel insertion end is near the surface of the bus-bar in the housing.
Said control valve is an electronic valve, and said control valve is electrically connected with controller 8.
Be provided with temperature, sulfuric acid density regulating apparatus in electrolyte input acid tank, electrolyte output acid tank, the high density electrolyte acid tank, said adjusting device is electrically connected (diagram is not provided) respectively with controller.
With above-mentioned
OnePlant the lead acid accumulator quick charge device and carry out quick charge method, comprise the following steps:
(1) electrolyte is imported input, the output channel of acid tank 1, electrolyte output acid tank 2; Insert as stated in the housing of battery 9; Under the control of controller 8, first pipeline control valve 4 is opened, and high density electrolyte acid tank 3 quantitative output densities are 1.4 g/cm
3Electrolyte to electrolyte input acid tank 1 in, carry finish after, first pipeline control valve 4 is closed, electrolyte is imported sour 1 groove, and to adjust to density be 1.1 g/cm from being about to electrolyte
3, input channel control valve 5 is opened subsequently, quantitative electrolyte is delivered in the battery 9 after, left standstill 2 hours;
(2) with the current charges of 0.15C/n ampere/sheet 3 hours, with the current charges of 0.35C/n ampere/sheet 17 hours, then the electric current with 0.23C/n ampere/sheet discharged 3 hours then, again with the current charges of 0.25C/n ampere/sheet 9 hours; In this process, under the control of controller, input, output channel control valve 5,6 are opened, and first, second pipeline control valve 4,7 is closed, and carries out the cold and hot exchange of electrolyte, and the electrolyte temperature in the battery is controlled at about 40 ℃;
(3) with the current charges of 0.25C/n ampere/sheet 4 hours, then with the current charges of 0.25C/n ampere/sheet 7 hours; In this process, under the control of controller 8, input, output channel control valve 5,6, and first, second pipeline control valve 4,7 all opens, it is 1.4 g/cm that high density electrolyte acid tank 3 is carried density
3Electrolyte, electrolyte input acid tank 1, electrolyte output acid tank 2 carry out exchange of electrolyte, and accomplish in preceding 0.5 hour in charging the density of electrolyte in the battery is adjusted to 1.280～1.300g/cm
3
Fast charge method comprises the following steps:
(1) electrolyte is imported input, the output channel of acid tank 1, electrolyte output acid tank 2; Insert as stated in the housing of battery 9; Under the control of controller 8, first pipeline control valve 4 is opened, and high density electrolyte acid tank 3 quantitative output densities are 1.4 g/cm
3Electrolyte to electrolyte input acid tank 1 in, carry finish after, first pipeline control valve 4 is closed, electrolyte is imported sour 1 groove, and to adjust to density be 1.1 g/cm from being about to electrolyte
3, input channel control valve 5 is opened subsequently, quantitative electrolyte is delivered in the battery 9 after, left standstill 2 hours;
(2) with the current charges of 0.20C/n ampere/sheet 3 hours, with the current charges of 0.30C/n ampere/sheet 18 hours, then the electric current with 0.20C/n ampere/sheet discharged 4 hours then, again with the current charges of 0.30C/n ampere/sheet 8 hours; In this process, under the control of controller, input, output channel control valve 5,6 are opened, and first, second pipeline control valve 4,7 is closed, and carries out the cold and hot exchange of electrolyte, and the electrolyte temperature in the battery is controlled at about 40 ℃;
(3) with the current charges of 0.35C/n ampere/sheet 3 hours, then with the current charges of 0.20C/n ampere/sheet 8 hours; In this process, under the control of controller 8, input, output channel control valve 5,6, and first, second pipeline control valve 4,7 all opens, it is 1.4 g/cm that high density electrolyte acid tank 3 is carried density
3Electrolyte, electrolyte input acid tank 1, electrolyte output acid tank 2 carry out exchange of electrolyte, and accomplish in preceding 0.5 hour in charging the density of electrolyte in the battery is adjusted to 1.280～1.300g/cm
3
All the other are implemented like embodiment 1.
Fast charge method comprises the following steps:
(1) electrolyte is imported input, the output channel of acid tank 1, electrolyte output acid tank 2; Insert as stated in the housing of battery 9; Under the control of controller 8, first pipeline control valve 4 is opened, and high density electrolyte acid tank 3 quantitative output densities are 1.4 g/cm
3Electrolyte to electrolyte input acid tank 1 in, carry finish after, first pipeline control valve 4 is closed, electrolyte is imported sour 1 groove, and to adjust to density be 1.1 g/cm from being about to electrolyte
3, input channel control valve 5 is opened subsequently, quantitative electrolyte is delivered in the battery 9 after, left standstill 2 hours;
(2) with the current charges of 0.22C/n ampere/sheet 3 hours, with the current charges of 0.40C/n ampere/sheet 15 hours, then the electric current with 0.30C/n ampere/sheet discharged 2 hours then, again with the current charges of 0.40C/n ampere/sheet 8 hours; In this process, under the control of controller, input, output channel control valve 5,6 are opened, and first, second pipeline control valve 4,7 is closed, and carries out the cold and hot exchange of electrolyte, and the electrolyte temperature in the battery is controlled at about 40 ℃;
(3) with the current charges of 0.40C/n ampere/sheet 3 hours, then with the current charges of 0.15C/n ampere/sheet 8 hours; In this process, under the control of controller 8, input, output channel control valve 5,6, and first, second pipeline control valve 4,7 all opens, it is 1.4 g/cm that high density electrolyte acid tank 3 is carried density
3Electrolyte, electrolyte input acid tank 1, electrolyte output acid tank 2 carry out exchange of electrolyte, and accomplish in preceding 0.5 hour in charging the density of electrolyte in the battery is adjusted to 1.280～1.300g/cm
3
All the other are implemented like embodiment 1.
Claims (5)
1.
OnePlant the lead acid accumulator quick charge device; It is characterized in that: comprise electrolyte input acid tank, electrolyte output acid tank, high density electrolyte acid tank; Said high density electrolyte acid tank is communicated with electrolyte input acid tank, electrolyte output acid tank respectively through first, second set pipeline, and said electrolyte input acid tank, electrolyte output acid tank are communicated with battery respectively through set input, output channel; First, second pipeline, and be respectively equipped with control valve in the input, output channel; Electrolyte input acid tank, high density electrolyte acid tank are respectively equipped with filling pipe, and its middle-high density electrolyte acid tank also is provided with annotates the acid tube road.
2. as claimed in claim 1
OnePlant the lead acid accumulator quick charge device, it is characterized in that: after electrolyte input acid tank, set input, the output channel of electrolyte output acid tank inserted battery container, the output channel insertion depth was deeper than input channel.
3. as claimed in claim 2
OnePlant the lead acid accumulator quick charge device, it is characterized in that: the output channel insertion end is near the surface of the bus-bar in the housing.
4. as claimed in claim 1
OnePlant the lead acid accumulator quick charge device, it is characterized in that: said control valve is an electronic valve, and said control valve is electrically connected with controller.
5. as claimed in claim 1
OnePlant the lead acid accumulator quick charge device, it is characterized in that: be provided with temperature, sulfuric acid density regulating apparatus in electrolyte input acid tank, electrolyte output acid tank, the high density electrolyte acid tank, said adjusting device is electrically connected with controller respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120412578XU CN202309136U (en) | 2011-10-26 | 2011-10-26 | Rapid charging device for lead acid storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120412578XU CN202309136U (en) | 2011-10-26 | 2011-10-26 | Rapid charging device for lead acid storage battery |
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| CN202309136U true CN202309136U (en) | 2012-07-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201120412578XU Expired - Fee Related CN202309136U (en) | 2011-10-26 | 2011-10-26 | Rapid charging device for lead acid storage battery |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102354771A (en) * | 2011-10-26 | 2012-02-15 | 浙江天能电池江苏新能源有限公司 | Quick charging device for lead-acid storage battery and quick charging method |
| RU2722439C1 (en) * | 2019-08-16 | 2020-06-01 | Федеральное государственное казенное военное образовательное учреждение высшего образования "Рязанское гвардейское высшее воздушно-десантное ордена Суворова дважды Краснознаменное командное училище имени генерала армии В.Ф. Маргелова" Министерства обороны Российской Федерации | Low-maintenance lead-acid accumulator battery |
| CN113394523A (en) * | 2021-05-21 | 2021-09-14 | 天能电池集团股份有限公司 | Acid adding and formation method for lead storage battery |
-
2011
- 2011-10-26 CN CN201120412578XU patent/CN202309136U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102354771A (en) * | 2011-10-26 | 2012-02-15 | 浙江天能电池江苏新能源有限公司 | Quick charging device for lead-acid storage battery and quick charging method |
| CN102354771B (en) * | 2011-10-26 | 2014-01-22 | 浙江天能电池江苏新能源有限公司 | Quick charging device for lead-acid storage battery and quick charging method |
| RU2722439C1 (en) * | 2019-08-16 | 2020-06-01 | Федеральное государственное казенное военное образовательное учреждение высшего образования "Рязанское гвардейское высшее воздушно-десантное ордена Суворова дважды Краснознаменное командное училище имени генерала армии В.Ф. Маргелова" Министерства обороны Российской Федерации | Low-maintenance lead-acid accumulator battery |
| CN113394523A (en) * | 2021-05-21 | 2021-09-14 | 天能电池集团股份有限公司 | Acid adding and formation method for lead storage battery |
| CN113394523B (en) * | 2021-05-21 | 2022-09-20 | 天能电池集团股份有限公司 | Acid adding and formation method for lead storage battery |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120704 Termination date: 20121026 |