CN203967194U - A kind of nano-sized carbon and fumed silica battery process equipment - Google Patents
A kind of nano-sized carbon and fumed silica battery process equipment Download PDFInfo
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- CN203967194U CN203967194U CN201420438166.7U CN201420438166U CN203967194U CN 203967194 U CN203967194 U CN 203967194U CN 201420438166 U CN201420438166 U CN 201420438166U CN 203967194 U CN203967194 U CN 203967194U
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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
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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
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Filling, Topping-Up Batteries (AREA)
Abstract
The purpose of this utility model is to provide a kind of nano-sized carbon and fumed silica battery process equipment, this equipment has the functions such as the liquid of getting, mixing, quantitative quick filling, and the ectocine while reducing metering does not substantially have loss in filling process, easy to use.In order to reach described effect, the utility model adopts following technical scheme: a kind of nano-sized carbon and fumed silica battery process equipment, comprise a plurality of material storage tanks with temperature control system, described each material storage tank is connected to discharging hybrid electromagnetic valve by peristaltic pump, described a plurality of discharging hybrid electromagnetic valve is connected to same reaction vessel, and described reaction vessel is connected to multiposition valve by limited capacity electromagnetically operated valve, liquid level sensor.By such structure the utility model, by liquid level sensor with the triple valve of air pump, realized the liquid mode of getting of extraction unit volume, measured simply accurate, reproducible.
Description
Technical field
The utility model relates to a kind of battery processing device, especially a kind of nano-sized carbon and fumed silica battery process equipment.
Background technology
Along with the concept of energy-conserving and environment-protective deepens continuously, electric motor car is also more and more subject to liking of people.What meanwhile bring is exactly the use of large-scale storage battery.But more frequent owing to using, therefore also higher to the requirement in the capacity of storage battery, fail safe and useful life.In order to improve the performance of storage battery, best bet is the electrolyte of improveing wherein, for example, in the method for filling > > of the patent of invention < < colloidal electrolyte of lead acid accumulator that the patent No. is 200910097928.5, disclosed a kind of method for filling of colloidal electrolyte of lead acid accumulator, comprise the following steps: in dry battery, add sulfuric acid solution, after utmost point group sucks sulfuric acid solution, add the first colloidal electrolyte extremely group upper along and discharge, be discharged to when electric weight remains 30～50% and charge, after charging, with the second colloidal electrolyte, supply.Storage battery caloric value prepared by method for filling of the present invention is little, and battery life is long, and capacitance is reduced to 70%, and it discharges and recharges can be up to nearly 600 cycles, and the internal resistance of cell is lower, and self-discharge of battery speed is very little.
But along with electrolyte improvement, corresponding injected system also will improve, for example, in invention < < analysing valve control type lead-acid accumulator battery filling system > > that the patent No. is 201210087632.7, disclose a kind of analysing valve control type lead-acid accumulator battery filling system, comprise: device for casting, comprise acid-storing barrel and some quantitative measuring cups, quantitatively measuring cup is positioned in described acid-storing barrel, for analysing valve control type lead-acid accumulator battery is carried out to acid filling; Acid cooler, is connected with device for casting by acid inlet tube, for acid solution being cooled in valve-control type lead-acid accumulator threshold range; Take out sour device, by going out acid tube one end, be connected with device for casting, the other end is connected with acid cooler, for the acid solution in device for casting acid-storing barrel is withdrawn into described acid cooler.Compared with prior art, this inventive embodiments is by improving existing filling system, device for casting increases acid cooler and takes out sour device, acid cooler provides qualified cold acid to device for casting, taking out sour device is extracted in time acid cooler by the acid solution in device for casting acid-storing barrel and carries out cooling processing, keeping the acid solution being filled in analysing valve control type lead-acid accumulator battery is cold acid, thereby has improved the quality of analysing valve control type lead-acid accumulator battery.
Although such injected system can be guaranteed the temperature of injecting, except this advantage, do not have the quantitative anti-spilled setting that waits.The amount of perfusion sometimes still completes by original equipment such as measuring cups.So just there are the problems such as metering is inaccurate, and loss is large.
Utility model content
The purpose of this utility model is to provide a kind of nano-sized carbon and fumed silica battery process equipment, this equipment has the functions such as the liquid of getting, mixing, quantitative quick filling, and the ectocine while reducing metering does not substantially have loss in filling process, easy to use.
In order to reach described effect, the utility model adopts following technical scheme: a kind of nano-sized carbon and fumed silica battery process equipment, comprise a plurality of material storage tanks with temperature control system, described each material storage tank is connected to discharging hybrid electromagnetic valve by peristaltic pump, described a plurality of discharging hybrid electromagnetic valve is connected to same reaction vessel, described reaction vessel is by limited capacity electromagnetically operated valve, liquid level sensor is connected to multiposition valve, described multiposition valve is provided with one and detects mouth, a leakage fluid dram, an air scoop and a plurality of constant volume filling exit, described air scoop connects a triple valve, another interface of described triple valve is connected to outside air by air pump, described a plurality of constant volume filling exit is connected respectively in a plurality of storage battery encapsulation, described leakage fluid dram is connected with waste liquid storage device.
Preferably, described constant volume filling exit quantity is no more than 6.Because reaction vessel volume is limited, too many constant volume filling exit arranges not only bad for the mixing of materials in reaction vessel, is also unfavorable for the installation of filling storage battery encapsulation simultaneously.
Preferably, described constant volume filling exit surface is provided with cleaning doctor.Scraper can scrape some residual electrolyte in leakage fluid dram, guarantees multiposition valve surface cleaning.
Preferably, liquid level sensor is any one isolated liquid level sensor in photoelectric sensor, electromagnetic sensor, capacitance sensor.
Preferably, material storage tank quantity is 2-4.This actual proportioning according to electrolyte is selected.
The utlity model has following beneficial effect:
1,, by liquid level sensor with realized the liquid mode of getting of extraction unit volume with the triple valve of air pump, measure simply accurate, reproducible.
2, the whole filling link of liquid of getting substantially in closed system, has reduced external pollution, has improved the quality of product.
3, whole liquid-way system can be realized unmanned operation, as long as staff handles the placement of storage battery well, saves manually, and has guaranteed that operating personnel's is healthy.
Accompanying drawing explanation:
Fig. 1 is the structural representation of a kind of nano-sized carbon of the utility model and fumed silica battery process equipment.
Embodiment:
As shown in Figure 1, a kind of nano-sized carbon of the utility model and fumed silica battery process equipment, comprise a plurality of material storage tanks 1 with temperature control system, depositing different raw materials in material storage tank 1.According to actual product, select the quantity of material storage tank 1.Described each material storage tank 1 is connected to discharging hybrid electromagnetic valve 3 by peristaltic pump 2, described a plurality of discharging hybrid electromagnetic valve 3 is connected to same reaction vessel 4, described reaction vessel 4 is by limited capacity electromagnetically operated valve 5, liquid level sensor 6 is connected to multiposition valve 7, described multiposition valve 7 is provided with one and detects mouth 71, a leakage fluid dram 72, an air scoop 73 and a plurality of constant volume filling exit 74, described air scoop 73 connects a triple valve 8, described triple valve 8 another interfaces are connected to outside air by air pump, described a plurality of constant volume filling exit 74 is connected respectively in a plurality of storage battery encapsulation, described leakage fluid dram 72 is connected with waste liquid storage device.Consider storage battery exhaust position, no more than 6 of described constant volume filling exit 74 quantity.Described constant volume filling exit 74 surfaces are provided with cleaning doctor.Liquid level sensor 6 is any one isolated liquid level sensor in photoelectric sensor, electromagnetic sensor, capacitance sensor.Material storage tank 1 quantity is 2-4.Described reaction vessel 4 is quartz container.Described whole equipment place ambient temperature is 5-15 degree Celsius, guarantees that electrolyte can sex change at such temperature.
During the utility model work, open discharging hybrid electromagnetic valve 3, by peristaltic pump 2, from each material storage tank 1, take out batching.Peristaltic pump 2 has pollution-free: fluid only contacts pump line, does not contact the pump housing; Precision is high: repeatable accuracy, and steady state accuracy is high and can produce the vacuum degree that reaches 98%; There is no valve, mechanical seal and stuffing seal, just do not have these to produce the factor of revealing and safeguarding yet; Therefore can carry easily the features such as solid, liquid or gas-liquid mixed phase fluid, the valuable raw material such as the most suitable conveying nano-sized carbon and fumed silica.Until close discharging hybrid electromagnetic valve 3 after specifying the material of proportioning to enter into reaction vessel 4.Now limited capacity electromagnetically operated valve 5 cuts out always.In reaction vessel 4, various materials carry out mix and blend, according to technique, process.After completion of processing, opening limited capacity electromagnetically operated valve 5 carries out filling.In pouring process, limited capacity electromagnetically operated valve 5 is opened always.Filling front first have specify the electrolyte of unit volume to be transported to detect mouthfuls 71 to detect.After liquid level sensor 6 senses the electrolyte stream of specified amount, the air pump exhaust of triple valve 8 stops the electrolyte in pipeline to continue to enter into multiposition valve 7.Operating personnel inspect by random samples in this step, and be not all needs to implement at every turn.
Detect that to carry out normally filling, filling process after qualified be exactly to specify the electrolyte of unit volume to be transported to constant volume filling exit 74, except the amount of carrying is different, other process is identical with testing process.Common one group of constant volume filling exit 74 quantity are 6.Consider the loss of pipeline and detect requiredly, in reaction vessel 4, the amount of material is slightly more than the filling amount of 6 group storage batteries.Unnecessary electrolyte is discharged in leakage fluid dram 72.Because air pump stops carrying air, also have a gap, the unnecessary gas that now triple valve 8 brings is discharged by air scoop 73.
After filling, limited capacity electromagnetically operated valve 5 cuts out, and according to actual conditions cleaning reaction vessel 4, operating personnel put into next flow process by filling complete storage battery, again lay out and need to carry out filling storage battery.
By above-mentioned liquid dataway operation order, liquid-way system of the present utility model is got to the measurement of liquid precision, in unit volume, be set as under the condition of 1mL, the error of getting a filling storage battery is no more than 5 unit volume.Should and in pouring process whole electrolyte pollution-free, can not bring harm to operating personnel yet.Material is considerably less at whole equipment internal consumption.In fact common storage battery is filling does not need so accurate equipment, but nano-sized carbon and fumed silica Material Cost are higher, and comparatively harsh to environmental requirement.And adopting useful life that the utility model can effectively improve battery in the situation that of identical proportioning more than 15%, identical raw material can be produced storage battery 4% more, and pollutes less.For large enterprise, reached very surprising effects of energy saving and emission reduction.
The above embodiment has only expressed and has explained to of the present utility model, is not to restriction of the present utility model.Protection range of the present utility model contain with good grounds the utility model equivalent transformation, improvement and the expansion done.
Claims (5)
1. a nano-sized carbon and fumed silica battery process equipment, it is characterized in that: comprise a plurality of material storage tanks with temperature control system (1), described each material storage tank (1) is connected to discharging hybrid electromagnetic valve (3) by peristaltic pump (2), described a plurality of discharging hybrid electromagnetic valves (3) are connected to same reaction vessel (4), described reaction vessel (4) is by limited capacity electromagnetically operated valve (5), liquid level sensor (6) is connected to multiposition valve (7), described multiposition valve (7) is provided with one and detects mouthful (71), a leakage fluid dram (72), an air scoop (73) and a plurality of constant volume filling exit (74), described air scoop (73) connects a triple valve (8), another interface of described triple valve (8) is connected to outside air by air pump, described a plurality of constant volume filling exits (74) are connected respectively in a plurality of storage battery encapsulation, described leakage fluid dram (72) is connected with waste liquid storage device.
2. a kind of nano-sized carbon according to claim 1 and fumed silica battery process equipment, is characterized in that: no more than 6 of described constant volume filling exit (74) quantity.
3. a kind of nano-sized carbon according to claim 2 and fumed silica battery process equipment, is characterized in that: described constant volume filling exit (74) surface is provided with cleaning doctor.
4. a kind of nano-sized carbon according to claim 1 and fumed silica battery process equipment, is characterized in that: liquid level sensor (6) is any one isolated liquid level sensor in photoelectric sensor, electromagnetic sensor, capacitance sensor.
5. a kind of nano-sized carbon according to claim 1 and fumed silica battery process equipment, is characterized in that: material storage tank (1) quantity is 2-4.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420438166.7U CN203967194U (en) | 2014-08-05 | 2014-08-05 | A kind of nano-sized carbon and fumed silica battery process equipment |
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| CN201420438166.7U CN203967194U (en) | 2014-08-05 | 2014-08-05 | A kind of nano-sized carbon and fumed silica battery process equipment |
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| CN203967194U true CN203967194U (en) | 2014-11-26 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104157897A (en) * | 2014-08-05 | 2014-11-19 | 浙江长兴金太阳电源有限公司 | Silicon dioxide battery processing device adopting nanocarbon and gas phase method |
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2014
- 2014-08-05 CN CN201420438166.7U patent/CN203967194U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104157897A (en) * | 2014-08-05 | 2014-11-19 | 浙江长兴金太阳电源有限公司 | Silicon dioxide battery processing device adopting nanocarbon and gas phase method |
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