CN204017625U - Dual Battery formation purifying processor - Google Patents
Dual Battery formation purifying processor Download PDFInfo
- Publication number
- CN204017625U CN204017625U CN201420425479.9U CN201420425479U CN204017625U CN 204017625 U CN204017625 U CN 204017625U CN 201420425479 U CN201420425479 U CN 201420425479U CN 204017625 U CN204017625 U CN 204017625U
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- CN
- China
- Prior art keywords
- condenser
- balls
- buffer channel
- mozzle
- layers
- Prior art date
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- Expired - Fee Related
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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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- Battery Electrode And Active Subsutance (AREA)
Abstract
The utility model belongs to a kind of dual Battery formation purifying processor, and forming primarily of mozzle and condenser, this processor comprises condenser, mozzle, buffer channel and cover plate, wherein descends the interior bottom of the buffer channel of filter upper end to be provided with separation layers of balls.The utility model can carry out double filtration purification to acid mist, effectively can solve the acid mist pollution environmental problem in battery charged process, the problem of battery with two side terminals and acid deficient when battery negative pressure vacuumizes can also be solved simultaneously, there is purification cost low, on acid adding and negative pressure vacuum pumping without impact, good purification and safe and reliable advantage.
Description
Technical field
The utility model belongs to a kind of dual Battery formation purifying processor.
Background technology
In the production process of lead-acid accumulator, have a procedure to be Charging Techniques, Charging Techniques is exactly charge to battery by certain technological requirement with direct current after battery acid filling liquid.Battery its terminal voltage in charging process can raise gradually, and when positive pole input electricity reaches 70% of battery capacity, terminal voltage reaches water decomposition voltage, and the water decomposition in electrolyte separates out O at positive pole
2, when negative pole input electricity reaches 90% of battery capacity, terminal voltage reaches water decomposition voltage, and the water decomposition in electrolyte separates out H at negative pole
2, O
2and H
2h can be taken out of during precipitation
2sO
4, this H
2sO
4in vaporific, i.e. acid mist, acid mist enters in air and pollutes the environment.Battery formation acid mist amount of precipitation and formation process, overcharge current, change into tank liquor or battery temperature and overcharge electricity relevant.Change into the later stage, overcharge electric current larger, change into tank liquor or battery temperature is higher, acid mist amount of precipitation is also more.
Simultaneously, battery is in charging process, because pole plate generation chemical reaction causes porosity to change, the change of pole plate also can produce extruding to dividing plate, thus also result in the change of separator porosity, so, acid solution in battery can be extruded, the amount of inside battery acid solution will be caused like this to reduce, and the chemical reaction of battery in formation process causes the acid solution density in inside battery and outside batteries acid kettle inconsistent simultaneously, thus causes the difference of battery acid content and voltage.
Current domestic battery industry generally uses opened type acid solution kettle, as the H that charging produces
2and O
2when directly separating out, the H taken out of
2sO
4also more, therefore the workshop even acid mist concentration of surrounding enviroment are also higher, and acid mist not only stimulates the respiratory tract of people, produce injury to the respiratory apparatus of people, digestion, internal system, also affect the environment of periphery and the growth of plant, existing domestic regulation the highest permission H
2sO
4gas discharging concentration is 45mg/m
3, but above-mentioned standard is rare reaches.Domestic battery industry adopts complexity mostly to the process of acid mist and the larger Acid fog purification equipment of volume, and collection and purification cost is large, and costly, also unfavorable actual acid adding operation, result of use is poor.At present, process adopts complicated and that volume is larger Acid fog purification equipment mostly, and collection and purification cost is large, and costly, also unfavorable actual acid adding operation, clean-up effect is poor.
Summary of the invention
The purpose of this utility model is a kind of dual Battery formation purifying processor of design, double filtration purification can be carried out to acid mist, effectively can solve the acid mist pollution environmental problem in battery charged process, the problem of battery with two side terminals and acid deficient when battery negative pressure vacuumizes can also be solved simultaneously, there is purification cost low, on acid adding and negative pressure vacuum pumping without impact, good purification and safe and reliable advantage.
For this reason, the utility model formed primarily of mozzle and condenser, and this processor comprises:
Condenser, condenser is U-shaped, and condenser lower end is provided with the body socket with the exhaust outlet grafting of acid filling device upper end, is provided with reservoir chamber in condenser, and condenser internal upper part is provided with the lower filter in this condenser internal upper part space of transverse seal.Mozzle, mozzle is hollow tubular, the upper end of mozzle communicates with the reservoir chamber in condenser, and the lower end of mozzle passes from the middle part of body socket and is positioned at body socket outer end, and the tube wall being positioned at the mozzle of body socket lower end is the tube wall of side band open seam.Buffer channel, buffer channel is the tubular body of band convex edge, middle part edge, the buffer channel of edge bottom, convex edge is plugged in the upper port of condenser, the lower surface of buffer channel is positioned in the upper periphery portion of filter on condenser, it is seal cavity between the bottom perisporium of buffer channel and the condenser inner wall of grafting, be provided with the upper filter in this buffer channel internal upper part space of transverse seal in the buffer channel of edge upper end, convex edge, the interior bottom of the buffer channel of lower filter upper end is provided with separation layers of balls.Cover plate, cover plate is positioned at and capping buffer channel upper surface, is provided with steam vent in the middle part of cover plate.
Described separation layers of balls is made up of the spheroid of four layers of three kinds of different-diameter from the bottom to top, and wherein upper to be separated layers of balls be two layers, middle separation layers of balls with under to be separated layers of balls be one deck.The diameter of each spheroid in lower separation layers of balls: the diameter of each spheroid in middle separation layers of balls: diameter=4 being above separated each spheroid in layers of balls: 2: 1.Each spheroid in described separation layers of balls is made up of polytetrafluoroethylene (PTFE), spheroid is at least provided with two through diameter holes.Described upper and lower filter be through over-richness be the cellular polyurethane foamed sheet that 10 ~ 20% sodium hydroxide solutions soaked.Described cover plate bottom eye-splice is in upper end of condenser mouth.Said structure design reaches the purpose of this utility model.
The utility model can carry out double filtration purification to acid mist, effectively can solve the acid mist pollution environmental problem in battery charged process, the problem of battery with two side terminals and acid deficient when battery negative pressure vacuumizes can also be solved simultaneously, there is purification cost low, on acid adding and negative pressure vacuum pumping without impact, good purification and safe and reliable advantage.The utility model is that the acid gas concentration of emission of separating out from steam vent of the present utility model in battery forming process is lower than 0.03mg/m through testing inspection data
3.The utility model is combined inserting formula, and replacing filter and parts conveniently, operate practical and convenient, cheap for manufacturing cost, are beneficial to and promote the use of.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is buffer channel partial structurtes schematic diagram of the present utility model.
Fig. 3 is the structural representation of spheroid in each separation layers of balls of the present utility model.
Specific embodiments
As shown in Figure 1 to Figure 3, a kind of dual Battery formation purifying processor, formed primarily of mozzle 10 and condenser 7.This processor comprises:
Condenser, condenser is U-shaped, and condenser lower end is provided with the body socket 9 with the exhaust outlet grafting of acid filling device upper end, is provided with reservoir chamber 8 in condenser, and condenser internal upper part is provided with the lower filter 6 in this condenser internal upper part space of transverse seal.
Mozzle 10, mozzle is hollow tubular, the upper end of mozzle communicates with the reservoir chamber in condenser, and the lower end of mozzle passes from the middle part of body socket and is positioned at body socket outer end, and the tube wall being positioned at the mozzle of body socket lower end is the tube wall of side band open seam 11.
Buffer channel 5, buffer channel is the tubular body of band convex edge, middle part edge 51, and the buffer channel of edge bottom, convex edge is plugged in the upper port of condenser.The lower surface of buffer channel is positioned in the upper periphery portion of filter on condenser.It is seal cavity between the bottom perisporium of buffer channel and the condenser inner wall of grafting.The upper filter 2 in this buffer channel internal upper part space of transverse seal is provided with in the buffer channel of edge upper end, convex edge.The interior bottom of the buffer channel of lower filter upper end is provided with and is separated layers of balls 4; Described separation layers of balls is made up of the spheroid of four layers of three kinds of different-diameter from the bottom to top, and wherein upper to be separated layers of balls 41 be two layers, middle separation layers of balls 42 with under be separated layers of balls 43 for one deck; The diameter of each spheroid in lower separation layers of balls: the diameter of each spheroid in middle separation layers of balls: diameter=4 being above separated each spheroid in layers of balls: 2: 1.Each spheroid in described separation layers of balls is made up of polytetrafluoroethylene (PTFE), spheroid is at least provided with two through diameter holes 44, is beneficial to adsorb acid mist.
Cover plate 1, cover plate is positioned at and capping buffer channel upper surface, is provided with steam vent 2 in the middle part of cover plate.
Described upper and lower filter be through over-richness be the cellular polyurethane foamed sheet that 10 ~ 20% sodium hydroxide solutions soaked.Described cover plate bottom eye-splice is in upper end of condenser mouth.
During use, the utility model is plugged on by the body socket of condenser lower end on the exhaust outlet of each acid filling device list lattice upper end, the acid mist produced in battery charging process can enter in condenser by mozzle, because the temperature of outside air is always lower than the temperature of rechargeable battery, the acid mist of separating out becomes the globule due to condensation, can be attached on the reservoir chamber inwall in condenser, (containing acid) water of generation flows back to inside battery again by mozzle.After condensation process, the acid mist of a small amount of volatilization, carry out first time by the lower filter of upper end of condenser to filter, the each separation layers of balls of acid mist again in buffer channel of discharging carries out a degree of depth absorption, further acid mist condensation is become the globule by each spheroid in each separation layers of balls, progressively the integrated sour water that contains also flows back to inside battery by mozzle.The acid mist of a small amount of precipitation carries out second time by upper filter again and filters, and eventually passes the clean air after twice filtration and a degree of depth absorption by the steam vent volatilization on cover plate, thus reaches the object eliminated acid mist and separate out.The utility model is taken off after having operated.
In a word, the utility model can carry out double filtration purification to acid mist, effectively can solve the acid mist pollution environmental problem in battery charged process, the problem of battery with two side terminals and acid deficient when battery negative pressure vacuumizes can also be solved simultaneously, there is purification cost low, on acid adding and negative pressure vacuum pumping without impact, good purification and safe and reliable advantage.
Claims (5)
1. a dual Battery formation purifying processor, formed primarily of mozzle and condenser, it is characterized in that: this processor comprises,
Condenser, condenser is U-shaped, and condenser lower end is provided with the body socket with the exhaust outlet grafting of acid filling device upper end, is provided with reservoir chamber in condenser, and condenser internal upper part is provided with the lower filter in this condenser internal upper part space of transverse seal;
Mozzle, mozzle is hollow tubular, the upper end of mozzle communicates with the reservoir chamber in condenser, and the lower end of mozzle passes from the middle part of body socket and is positioned at body socket outer end, and the tube wall being positioned at the mozzle of body socket lower end is the tube wall of side band open seam;
Buffer channel, buffer channel is the tubular body of band convex edge, middle part edge, the buffer channel of edge bottom, convex edge is plugged in the upper port of condenser, the lower surface of buffer channel is positioned in the upper periphery portion of filter on condenser, it is seal cavity between the bottom perisporium of buffer channel and the condenser inner wall of grafting, be provided with the upper filter in this buffer channel internal upper part space of transverse seal in the buffer channel of edge upper end, convex edge, the interior bottom of the buffer channel of lower filter upper end is provided with separation layers of balls;
Cover plate, cover plate is positioned at and capping buffer channel upper surface, is provided with steam vent in the middle part of cover plate.
2., by dual Battery formation purifying processor according to claim 1, it is characterized in that:
Described separation layers of balls is made up of the spheroid of four layers of three kinds of different-diameter from the bottom to top, and wherein upper to be separated layers of balls be two layers, middle separation layers of balls with under to be separated layers of balls be one deck;
The diameter of each spheroid in lower separation layers of balls: the diameter of each spheroid in middle separation layers of balls: diameter=4 being above separated each spheroid in layers of balls: 2: 1.
3., by the dual Battery formation purifying processor described in claim 1 or 2, it is characterized in that: each spheroid in described separation layers of balls is made up of polytetrafluoroethylene (PTFE), spheroid is at least provided with two through diameter holes.
4., by dual Battery formation purifying processor according to claim 1, it is characterized in that: described upper and lower filter be through over-richness be the cellular polyurethane foamed sheet that 10 ~ 20% sodium hydroxide solutions soaked.
5., by dual Battery formation purifying processor according to claim 1, it is characterized in that: described cover plate bottom eye-splice is in upper end of condenser mouth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420425479.9U CN204017625U (en) | 2014-07-28 | 2014-07-28 | Dual Battery formation purifying processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420425479.9U CN204017625U (en) | 2014-07-28 | 2014-07-28 | Dual Battery formation purifying processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204017625U true CN204017625U (en) | 2014-12-17 |
Family
ID=52057539
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420425479.9U Expired - Fee Related CN204017625U (en) | 2014-07-28 | 2014-07-28 | Dual Battery formation purifying processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204017625U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109037580A (en) * | 2018-07-25 | 2018-12-18 | 江苏永达电源股份有限公司 | A kind of container formation technique |
-
2014
- 2014-07-28 CN CN201420425479.9U patent/CN204017625U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109037580A (en) * | 2018-07-25 | 2018-12-18 | 江苏永达电源股份有限公司 | A kind of container formation technique |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20141217 Termination date: 20190728 |