CN203737190U - Storage battery acid distribution system with cooling mechanism - Google Patents
Storage battery acid distribution system with cooling mechanism Download PDFInfo
- Publication number
- CN203737190U CN203737190U CN201320881603.8U CN201320881603U CN203737190U CN 203737190 U CN203737190 U CN 203737190U CN 201320881603 U CN201320881603 U CN 201320881603U CN 203737190 U CN203737190 U CN 203737190U
- Authority
- CN
- China
- Prior art keywords
- cooling
- shower
- acid distribution
- circulating pump
- tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 57
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000009826 distribution Methods 0.000 title abstract 9
- 238000003860 storage Methods 0.000 title abstract 4
- 239000002253 acid Substances 0.000 claims abstract description 53
- 239000012530 fluid Substances 0.000 claims description 25
- 241000196435 Prunus domestica subsp. insititia Species 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 10
- 239000007921 spray Substances 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000110 cooling liquid Substances 0.000 abstract 2
- 238000005086 pumping Methods 0.000 abstract 1
- 239000000498 cooling water Substances 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 2
- 239000004698 Polyethylene (PE) Substances 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000011260 aqueous acid Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- 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
Abstract
The utility model discloses a storage battery acid distribution system with a cooling mechanism. The storage battery acid distribution system comprises an acid distribution tank with a necking part, a spray pipe which annularly sleeves the necking part, a liquid inlet pipe, a collection tank and a circulating pump, wherein a water outlet facing the acid distribution tank is formed in the side wall of the spray pipe; two ends of the liquid inlet pipe are respectively connected with the spray pipe and the circulating pump; the collection tank is arranged below the acid distribution tank and is used for receiving cooling liquid sprayed by the spray pipe; the circulating pump is used for pumping the cooling liquid into the spray pipe through a circulating pipe. By adoption of the storage battery acid distribution system with the cooling mechanism, the temperature of a sulfuric acid solution in the acid distribution tank can be controlled to be 42 to 50 DEG C in the acid distribution process, and a cooling effect is good. Moreover, the sulfuric acid solution at the temperature of 42 to 50 DEG C is cooled to 30 DEG C or below in an acid cooling machine within only 0.5-1 hour, the time is greatly saved, and the production period is reduced.
Description
Technical field
The utility model belongs to battery production technical field, relates in particular to a kind of battery acid preparing system with cooling body.
Background technology
Lead-acid accumulator is widely used in all trades and professions with voltage stabilization, the advantage such as cheap.The electrolyte that lead-acid accumulator is used is sulphur aqueous acid, and therefore, in the production process of lead-acid accumulator, complex acid is very crucial step.
In complex acid process, conventionally need to use complex acid tank (battery complex acid tank), notification number is that the Chinese patent literature of CN203316077U discloses a kind of lead-acid accumulator acid preparing system complex acid tank, comprise complex acid tank body, on complex acid tank body, be provided with the liquid level gauge for the intrinsic liquid level of complex acid tank is shown, the bottom of this liquid level gauge body and top all with in complex acid tank body are connected, be communicated with on the pipeline of described complex acid tank body and described liquid level gauge bodies top and be provided with control valve, liquid level gauge body top is connected with by be filled with air in liquid level gauge body can all push back the pressure emptier in complex acid tank body by intrinsic liquid level gauge liquid.As above-mentioned patent, complex acid tank used does not all have cooling effect at present.
Because being added to the water, the concentrated sulfuric acid can produce a large amount of heats, in complex acid process, sulfuric acid solution temperature in battery complex acid tank reaches as high as 70 DEG C, and the reality of sulfuric acid solution can serviceability temperature below 30 DEG C, because existing battery complex acid tank is all without cooling effect, general way is the sulfuric acid solution of 70 DEG C of this kinds to be put into cold sour machine carry out cooling, and in cold sour machine, sulfuric acid solution is cooled to 30 DEG C at least need 3h below more than, in actual production process, take a large amount of time, the production cycle is very long.
Utility model content
The utility model provides the battery acid preparing system with cooling body, simple in structure, can in battery complex acid process, carry out complex acid tank cooling, and good cooling results.
With a battery acid preparing system for cooling body, comprising:
With the complex acid tank of necking part;
Ring set is at the shower of necking part, and the sidewall of described shower is provided with the apopore towards complex acid tank;
Feed tube, two ends connect respectively shower and circulating pump;
Be located at the feeder of complex acid tank below, the cooling fluid of spilling for receiving shower;
Circulating pump, pumps into shower by cooling fluid by circulation pipe.
In the utility model, circulating pump pumps into cooling fluid feed tube and then enters into shower, and cooling fluid can be sprayed onto from the apopore of shower the outer wall of complex acid tank, and along the outer wall landing of complex acid tank, structure is very simple, and adopts the good cooling results of this spray type water-cooled.Secondly, the direct ring set of shower, at the necking part of shower, does not need extra fixture, and shower can firmly fix with the outer wall of complex acid tank, and installation and removal are all extremely convenient.In addition, feeder can also be collected the cooling fluid that shower spills, and makes cooling fluid can re-start utilization again, saves the energy.
As preferably, the described battery acid preparing system with cooling body also comprises that described import is communicated with feeder for allocating cooling fluid and the preparing pool with import and outlet, and described outlet connects described circulating pump.The coolant temperature of collecting due to feeder is higher, cooling fluid in feeder flow into preparing pool, can in preparing pool, allocate cooling fluid, make its requirement that meets cooling medium, it is cooling that then circulating pump can pump into deployed cooling fluid shower continuation.
As preferably, all apopores are uniformly distributed on shower.The cooling fluid spraying out from shower can get at the outer wall that is covered with uniformly complex acid tank, can be comprehensively, carry out cooling to the sulfuric acid solution in complex acid tank uniformly.
As preferably, the pore size of all apopores is identical.
As preferably, the aperture of described apopore is 0.3～1.5cm.Preferred, the aperture of described apopore is 0.5～1cm.The aperture of apopore is too small, the cooling water water yield spraying out from apopore is little, do not reach the effect of effective cooling sulfuric acid solution, if and the aperture of apopore is excessive, the current that apopore sprays out are too large, the flow velocity of cooling water is fast, and the time that causes cooling water to stop at the tank wall of battery complex acid tank is too short, and cooling water utilization rate is low.
Compared with prior art, the beneficial effects of the utility model are:
The battery acid preparing system that adopts the utility model band cooling body, can be controlled at 42 DEG C～50 DEG C by the sulfuric acid solution temperature in complex acid tank in complex acid process, good cooling results.Again the sulfuric acid solution of 42 DEG C～50 DEG C of this kinds is put into cold sour machine and be cooled to 30 DEG C and only need below 0.5h～1h, greatly save time and reduce the production cycle.
The battery acid preparing system of the utility model band cooling body is simple in structure, be convenient to produce and control, and cooling fluid can reuse, and cooling fluid utilization rate is high.
Brief description of the drawings
Fig. 1 is the structural representation of the battery acid preparing system of the utility model band cooling body.
Fig. 2 is the perspective view at complex acid tank position in the battery acid preparing system of the utility model band cooling body.
Fig. 3 is the perspective view at complex acid tank position while using the battery acid preparing system of the utility model band cooling body.
Reference numeral in figure is as follows:
1, complex acid tank; 2, necking part; 3, circulating pump; 4, shower; 5, feed tube;
6, apopore; 7, feeder; 8, preparing pool.
Detailed description of the invention
Below in conjunction with specific embodiment, the utility model is further explained.
As shown in Figure 1 and Figure 2, the battery acid preparing system of the utility model band cooling body comprises complex acid tank 1, shower 4, feed tube 5, circulating pump, feeder and preparing pool.
Complex acid tank 1 is with necking part 2.Shower 4 is for being coiled into the pipe of annular, and shower 4 is enclosed within the outer wall of necking part 2, and shower 4 can adopt polyethylene pipe to make.Shower 4 offers some apopores 6, and all apopores 6 are uniformly distributed on shower 4, and the size of all apopores is all consistent, and aperture is 0.5cm.In addition, the water outlet direction of all apopores 6 is all towards the outer wall of complex acid tank 1.
One end of feed tube 5 is connected with shower 4, and the other end is connected with circulating pump 3.
Feeder 7 is located at the below of complex acid tank 1, can collect the cooling fluid that shower spills.
Preparing pool 8 is for allocating cooling fluid, and this preparing pool 8 is with import and outlet, and wherein, import is connected with feeder 7 by pipeline, and outlet connects circulating pump 3, like this, enters in shower thereby circulating pump 3 can pump into feed tube by the cooling fluid in preparing pool.
In the time of complex acid, open circulating pump, the cooling fluid in preparing pool is pumped into feed tube by circulating pump, thus cooling fluid enters into shower, and discharge from delivery port; The cooling fluid of discharging from apopore 6, along the outer wall landing (as Fig. 3) of complex acid tank 1, is carried out cooling to sulfuric acid solution in complex acid tank; Fall into feeder from the cooling fluid of complex acid tank wall landing, the cooling fluid in feeder continues to flow in preparing pool; At preparing pool, can allocate the cooling medium that obtains suitable condition to cooling fluid.
The foregoing is only better implementation example of the present utility model, be not limited to the utility model, all within the utility model spirit and principle, any amendment of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (5)
1. the battery acid preparing system with cooling body, is characterized in that, comprising:
With the complex acid tank of necking part;
Ring set is at the shower of necking part, and the sidewall of described shower is provided with the apopore towards complex acid tank;
Feed tube, two ends connect respectively shower and circulating pump;
Be located at the feeder of complex acid tank below, the cooling fluid of spilling for receiving shower;
Circulating pump, pumps into shower by cooling fluid by circulation pipe.
2. the battery acid preparing system with cooling body as claimed in claim 1, is characterized in that, also comprises that described import is communicated with feeder for allocating cooling fluid and the preparing pool with import and outlet, and described outlet connects described circulating pump.
3. the battery acid preparing system with cooling body as claimed in claim 1, is characterized in that, all apopores are uniformly distributed on shower.
4. the battery acid preparing system with cooling body as claimed in claim 1, is characterized in that, the pore size of all apopores is identical.
5. the battery acid preparing system with cooling body as claimed in claim 4, is characterized in that, the aperture of described apopore is 0.3～1.5cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320881603.8U CN203737190U (en) | 2013-12-30 | 2013-12-30 | Storage battery acid distribution system with cooling mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320881603.8U CN203737190U (en) | 2013-12-30 | 2013-12-30 | Storage battery acid distribution system with cooling mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203737190U true CN203737190U (en) | 2014-07-30 |
Family
ID=51337055
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320881603.8U Active CN203737190U (en) | 2013-12-30 | 2013-12-30 | Storage battery acid distribution system with cooling mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203737190U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105374976A (en) * | 2015-10-30 | 2016-03-02 | 天能电池(芜湖)有限公司 | Acid return pipe of improved acid cooling machine |
| CN105375069A (en) * | 2015-11-16 | 2016-03-02 | 天能电池(芜湖)有限公司 | Cooling water bath used in acid filling process of accumulator battery |
| CN112555685A (en) * | 2020-12-02 | 2021-03-26 | 西安交通大学 | Neck-closing type micro-clearance pressurization system and method |
-
2013
- 2013-12-30 CN CN201320881603.8U patent/CN203737190U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105374976A (en) * | 2015-10-30 | 2016-03-02 | 天能电池(芜湖)有限公司 | Acid return pipe of improved acid cooling machine |
| CN105375069A (en) * | 2015-11-16 | 2016-03-02 | 天能电池(芜湖)有限公司 | Cooling water bath used in acid filling process of accumulator battery |
| CN105375069B (en) * | 2015-11-16 | 2018-06-22 | 天能电池(芜湖)有限公司 | Storage battery acidification bosh |
| CN112555685A (en) * | 2020-12-02 | 2021-03-26 | 西安交通大学 | Neck-closing type micro-clearance pressurization system and method |
| CN112555685B (en) * | 2020-12-02 | 2022-02-01 | 西安交通大学 | Neck-closing type micro-clearance pressurization system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 313100 Coal Mountain Industrial Park, Changxing County, Huzhou City, Zhejiang Province Patentee after: Tianneng Battery Group Co., Ltd. Address before: 313100 Coal Mountain Industrial Park, Changxing County, Huzhou City, Zhejiang Province Patentee before: Tianneng Battery Group Co., Ltd. |