CN105576316B - The retracting device of high-performance battery liquid - Google Patents
The retracting device of high-performance battery liquid Download PDFInfo
- Publication number
- CN105576316B CN105576316B CN201610054866.XA CN201610054866A CN105576316B CN 105576316 B CN105576316 B CN 105576316B CN 201610054866 A CN201610054866 A CN 201610054866A CN 105576316 B CN105576316 B CN 105576316B
- Authority
- CN
- China
- Prior art keywords
- battery liquid
- liquid
- filter
- tank
- sedimentation basin
- 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
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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/84—Recycling of batteries or fuel cells
Landscapes
- Battery Electrode And Active Subsutance (AREA)
- Secondary Cells (AREA)
- Hybrid Cells (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Filling, Topping-Up Batteries (AREA)
Abstract
The present invention relates to the retracting device of high-performance battery liquid, including sedimentation basin and the battery liquid tank for collecting battery liquid；Battery liquid tank is connected with sedimentation basin by centrifugal water pump；Sedimentation basin is connected with filter press and carries out press filtration to liquid, and gained liquid after press filtration is filtered using filter；Caused colloidal suspension particle after part filtering, is collected by crystallizing collecting tank, and another part adds pure water in the liquid after being filtered using filter, is entered by pipeline in fluid reservoir；Neutralisation treatment pond is connected with carbon group compound additive and bottom is provided with agitating device；Neutralisation treatment pond generates electric lead in the presence of electrolytic deposition device；After carrying out press filtration to the battery liquid of recovery, filtered after removing large volume of solid impurity particle, add after pure water dilution and then by multiple times of filtration, so as to ensure that being recycled for used and scrapped battery liquid, effectively improve productivity effect.
Description
Technical field
The present invention relates to a kind of high-performance battery technology field, and in particular to a kind of recovery of high-performance battery liquid
Device.
Background technology
The recovery and processing of waste and old lead acid accumulator must go, and mainly have following two reasons：First, avoid to environment
Pollution, second, old and useless battery recycling value it is at a relatively high.Due to the driving of economic benefit, small self-employed worker is in removal process
Middle shortage environmental consciousness, is arbitrarily disassembled, and poisonous spent acid is arbitrarily toppled over by personnel, causes waste and old lead acid accumulator to cause two to environment
Secondary pollution, and make waste and old lead acid accumulator that the mankind are caused with significant damage, these are in the treated of waste and old lead acid accumulator
It should be avoided in journey.
The composition of existing used and scrapped battery electrolyte is mainly sulfuric acid and metal ion；When battery can not in use,
In order to avoid the method that electrolyte causes serious pollution typically to be neutralized by lime to environment is handled；Above-mentioned processing mode is deposited
The wasting of resources, the processing cost increase the defects of, severe environmental pollution is also resulted in when serious, its serious influence and restriction
The survival and development of enterprise.
For above-mentioned technical problem, therefore need to be improved.
The content of the invention
The technical problem to be solved in the present invention is in view of the shortcomings of the prior art, to propose that one kind is simple in construction,
A kind of high-performance electric power storage easy to use, while effectively being reclaimed to the liquid of waste and old lead acid accumulator
The retracting device of pond liquid.
In order to reach object above, the technical solution adopted in the present invention is：The retracting device of high-performance battery liquid,
Including sedimentation basin and for collecting the battery liquid tank of battery liquid；Battery liquid tank and sedimentation basin pass through centrifugal water pump
It is connected；Sedimentation basin is connected with filter press and carries out press filtration to liquid, and gained liquid after press filtration is filtered using filter；
Caused colloidal suspension particle after part filtering, is collected, another part is entered using filter by crystallizing collecting tank
Pure water is added in liquid after row filtering, is entered by pipeline in fluid reservoir, fluid reservoir filters by centrifugal water pump and once
Device, secondary filter connect with neutralisation treatment pond；Neutralisation treatment pond is connected with carbon group compound additive and bottom is installed
There is agitating device；Neutralisation treatment pond generates electric lead in the presence of electrolytic deposition device.
As a preferred embodiment of the present invention, the carbon group compound additive includes coke, coal dust or other natural
Carbon.
As a preferred embodiment of the present invention, in the battery liquid tank, sedimentation basin, fluid reservoir and neutralisation treatment pond
It is mounted on the high and low liquid level detection device and alarm lamp for monitoring water level in tank.
As a preferred embodiment of the present invention, the colloidal suspension particle that the crystallization collecting tank is collected is burnt by boiler
Burn, discharge cleaning gas is produced after purified treatment.
As a preferred embodiment of the present invention, addition and the battery liquid in battery liquid tank of the pure water
Mass ratio be 0.5-3:90-110.
The beneficial effects of the invention are as follows：The present invention is simple in construction, easy to install and use, passes through the battery liquid to recovery
After carrying out press filtration, filtered after removing large volume of solid impurity particle, add after pure water dilution and then pass through multiple mistake
Filter, then adds carbon group compound, so as to ensure that being recycled for used and scrapped battery liquid, efficiently avoid battery
It is discarded caused by environmental pollution, effectively improve productivity effect.
Brief description of the drawings
Fig. 1 is the retracting device structural representation of high-performance battery liquid of the present invention.
Reference in figure：Battery liquid tank 1, centrifugal water pump 2, sedimentation basin 3, filter press 4, filter 5, crystallization are collected
Groove 6, boiler burn 7, discharge cleaning gas 8, pure water 9, fluid reservoir 10, a filter 11, secondary filter 12, neutralized
Processing pond 13, carbon group compound additive 14, agitating device 15, electrolytic deposition device 16, electric lead 17.
Embodiment
The embodiment of the present invention is elaborated below in conjunction with the accompanying drawings.
Embodiment：As shown in figure 1, the retracting device of high-performance battery liquid, including sedimentation basin 3 and for collecting electric power storage
The battery liquid tank 1 of pond liquid；Battery liquid tank 1 is connected with sedimentation basin 3 by centrifugal water pump 2；Sedimentation basin 3 and press filtration
Machine 4 is connected and carries out press filtration to liquid, and gained liquid after press filtration is filtered using filter 5；Produced after part filtering
Colloidal suspension particle, be collected by crystallizing collecting tank 6, liquid of the another part after being filtered using filter 5
Middle addition pure water 9, is entered by pipeline
In fluid reservoir 10, pass through the progress successively of filter press 4 and filter 5 so that each volume size in withdrawal liquid
Impurity be removed, so as to ensure the liquid carry out and pure water 9 dilute after it is i.e. recycling, ensure that the pure of the liquid
Degree；Fluid reservoir 10 is connected by centrifugal water pump 2 and a filter 11, secondary filter 12 with neutralisation treatment pond 13；It is logical
Multiple times of filtration is crossed, has further purified the purity of the liquid；Neutralisation treatment pond 13 is connected with carbon group compound additive 14 and bottom
Portion is provided with agitating device 15；It is mainly that the metallic compound in battery liquid is whole to add carbon group compound additive 14
It is reduced to metal or corresponding reduzate, such as lead；And carbon group compound additive 14 includes coke, coal dust or other natural
Carbon.
Neutralisation treatment pond 10, by separating out lead, and then founding door, generates electric lead in the presence of electrolytic deposition device 16
17。
It is mounted on being used to monitor water in tank in battery liquid tank 1, sedimentation basin 3, fluid reservoir 10 and neutralisation treatment pond 13
The high and low liquid level detection device and alarm lamp of position；The volume and size of aforesaid liquid just can be so monitored in real time, it is convenient
We operate.
From the point of view of energy-conserving and environment-protective and the utilization of resources, the colloidal suspension particle that crystallization collecting tank 6 is collected passes through boiler
7 are burned, discharge cleaning gas 8 is produced after purified treatment；
The addition of pure water 9 and the mass ratio of battery liquid in battery liquid tank 1 are 0.5-3:90-110；This
The utilization rate for the battery liquid that sample is reclaimed is high, so as to ensure that being recycled for used and scrapped battery liquid, effectively keeps away
Environmental pollution caused by used and scrapped battery abandons is exempted from, and being recycled for scrap battery liquid can effectively improve production
Benefit.
The foregoing description of the disclosed embodiments, professional and technical personnel in the field are enable to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention.Therefore, it is of the invention
The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one
The most wide scope caused.
Although reference in figure has more been used herein：Battery liquid tank 1, centrifugal water pump 2, sedimentation basin 3, press filtration
Machine 4, filter 5, collecting tank 6 is crystallized, boiler burns 7, and gas 8, pure water 9, fluid reservoir 10, a filter are cleaned in discharge
11, secondary filter 12, neutralisation treatment pond 13, carbon group compound additive 14, agitating device 15, electrolytic deposition device 16,
The electric grade of lead 17 term, but it is not precluded from the possibility using other terms.It is used for the purpose of more easily retouching using these terms
State and explain the essence of the present invention；Any additional limitation is construed as all to disagree with spirit of the present invention.
Claims (5)
1. the retracting device of high-performance battery liquid, it is characterised in that：Including sedimentation basin（3）With for collecting battery liquid
Battery liquid tank（1）；Battery liquid tank（1）And sedimentation basin（3）Pass through centrifugal water pump（2）It is connected；Sedimentation basin（3）With
Filter press（4）Connect and press filtration is carried out to liquid, filter is used to gained liquid after press filtration（5）Filtered；A part of mistake
Caused colloidal suspension particle after filter, by crystallizing collecting tank（6）It is collected, another part is using filter（5）Carry out
Pure water is added in liquid after filtering（9）, fluid reservoir is entered by pipeline（10）In, fluid reservoir（10）Pass through centrifugal water pump
（2）With a filter（11）, secondary filter（12）With neutralisation treatment pond（13）Connection；Neutralisation treatment pond（13）With carbon
Based compound additive（14）Connect and bottom is provided with agitating device（15）；Neutralisation treatment pond（13）In electrolytic deposition device
（16）In the presence of generate electric lead（17）.
2. the retracting device of high-performance battery liquid according to claim 1, it is characterised in that：The carbon group compound
Additive（14）Including coke, coal dust or other natural carbon.
3. the retracting device of high-performance battery liquid according to claim 1, it is characterised in that：The battery liquid
Tank（1）, sedimentation basin（3）, fluid reservoir（10）With neutralisation treatment pond（13）In be mounted on high and low liquid for monitoring water level in tank
Level detecting apparatus and alarm lamp.
4. the retracting device of high-performance battery liquid according to claim 1, it is characterised in that：The crystallization collecting tank
（6）The colloidal suspension particle of collection is burned by boiler（7）, discharge cleaning gas is produced after purified treatment（8）.
5. the retracting device of high-performance battery liquid according to claim 1, it is characterised in that：The pure water（9）
Addition and battery liquid tank（1）The mass ratio of middle battery liquid is 0.5-3:90-110.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610054866.XA CN105576316B (en) | 2016-01-26 | 2016-01-26 | The retracting device of high-performance battery liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610054866.XA CN105576316B (en) | 2016-01-26 | 2016-01-26 | The retracting device of high-performance battery liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105576316A CN105576316A (en) | 2016-05-11 |
| CN105576316B true CN105576316B (en) | 2018-01-23 |
Family
ID=55886198
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610054866.XA Active CN105576316B (en) | 2016-01-26 | 2016-01-26 | The retracting device of high-performance battery liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105576316B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1248801A (en) * | 1999-08-31 | 2000-03-29 | 沈阳环境科学研究所 | Technology for cleaning and recovering lead from waste accumulator |
| CN101244831A (en) * | 2008-03-18 | 2008-08-20 | 华中科技大学 | Method and device for recycling anhydrous sodium sulfate from desulfurization lead plaster filter liquor |
| CN103936190A (en) * | 2014-04-02 | 2014-07-23 | 超威电源有限公司 | Barium hydroxide treatment method with zero discharging of lead-acid storage battery wastewater |
| CN104183884A (en) * | 2013-07-31 | 2014-12-03 | 天能电池(芜湖)有限公司 | Lead acid storage battery waste acid recycling technology |
| CN205376680U (en) * | 2016-01-26 | 2016-07-06 | 浙江平湖华龙实业股份有限公司 | Recovery unit of high performance battery liquid |
-
2016
- 2016-01-26 CN CN201610054866.XA patent/CN105576316B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1248801A (en) * | 1999-08-31 | 2000-03-29 | 沈阳环境科学研究所 | Technology for cleaning and recovering lead from waste accumulator |
| CN101244831A (en) * | 2008-03-18 | 2008-08-20 | 华中科技大学 | Method and device for recycling anhydrous sodium sulfate from desulfurization lead plaster filter liquor |
| CN104183884A (en) * | 2013-07-31 | 2014-12-03 | 天能电池(芜湖)有限公司 | Lead acid storage battery waste acid recycling technology |
| CN103936190A (en) * | 2014-04-02 | 2014-07-23 | 超威电源有限公司 | Barium hydroxide treatment method with zero discharging of lead-acid storage battery wastewater |
| CN205376680U (en) * | 2016-01-26 | 2016-07-06 | 浙江平湖华龙实业股份有限公司 | Recovery unit of high performance battery liquid |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105576316A (en) | 2016-05-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104282962B (en) | The recovery method of waste and old lithium ionic cell electrolyte | |
| US10340561B2 (en) | Devices and method for smelterless recycling of lead acid batteries | |
| CN102453931A (en) | Technology for treating and purifying copper electrolyte by vortex electrolysis | |
| CA3121766C (en) | Improved devices and method for smelterless recycling of lead acid batteries | |
| CN102496752A (en) | Method for recycling electrolyte of waste lithium ion battery | |
| CN105439356A (en) | Method and device for synchronously recycling sulfuric acid and fluorine and chlorine from polluted acid | |
| CN205528100U (en) | Blue charcoal waste water utilization device | |
| CN101759158A (en) | Method for regenerating and recovering sulfuric acid from waste acid | |
| CN104841691B (en) | A kind of restorative procedure of heavy metal nickel contaminated soil | |
| CN104009269B (en) | The recovery and treatment method of waste and old lithium ion battery | |
| CN102655248B (en) | Battery waste acid recycling device | |
| CN107196005A (en) | Method for recovering waste lead storage battery | |
| CN201038237Y (en) | Selective volatilization recovery system for waste zinc-manganese battery | |
| CN202246872U (en) | System for recycling printed board acid etching waste solution and copper | |
| CN101219946A (en) | Method for recycling waste liquor of ammonium hexanedioic acid and recycling system thereof | |
| CN106025421A (en) | Electroplating peeling recovery technology of lithium battery electrode | |
| CN202610337U (en) | Resourceful treatment device for metal pickling waste liquor | |
| CN206424964U (en) | Regenerating active carbon system | |
| CN106756010A (en) | The method that fluorine in solution of zinc sulfate is removed after the roasting of zinc metallurgy white residue | |
| CN105576316B (en) | The retracting device of high-performance battery liquid | |
| CN104183884A (en) | Lead acid storage battery waste acid recycling technology | |
| CN205376680U (en) | Recovery unit of high performance battery liquid | |
| CN102660751B (en) | Resourceful treating method and resourceful treating device for metal pickling effluent | |
| CN102851730A (en) | Method for recycling waste acid etching solution of printed circuit board and recovering copper | |
| CN104726866A (en) | Acidic etching waste liquid regeneration and copper recovery device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |