CN202297739U - Device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge - Google Patents
Device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge Download PDFInfo
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- CN202297739U CN202297739U CN2011203659366U CN201120365936U CN202297739U CN 202297739 U CN202297739 U CN 202297739U CN 2011203659366 U CN2011203659366 U CN 2011203659366U CN 201120365936 U CN201120365936 U CN 201120365936U CN 202297739 U CN202297739 U CN 202297739U
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- lead
- sludge
- antimony
- reaction kettle
- alkali lye
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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
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
A device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge relates to the technical field of lead ore smelting and comprises a reaction kettle. A stirring mechanism is arranged in the reaction kettle and connected with a speed regulation motor. The device is characterized in that an antimony sludge and alkali liquor discharging port is arranged on a lateral wall of the reaction kettle, a metal lead skim discharging port is arranged at the bottom of the reaction kettle and connected with a filtering groove, and the filtering groove is connected with a plate frame filtering machine through a pump. The device is mainly applied to waste refined lead sludge of derives in processes of lead ore smelting, waste lead recovery smelting regeneration reclamation smelting, extracts and separates lead, antimony sludge and alkali liquor in one-step method, is simple and convenient, makes comprehensive use of waste refined lead sludge produced in the waste lead smelting regeneration reclamation process, eliminates risk of polluting environment, and obtains better economical benefit.
Description
Technical field
The utility model relates to the lead ore technical field of smelting, is specifically related to the device of a kind of plumbous refining alkaline residue single stage method separation of lead, antimony slag and alkali lye.
Background technology
Lead is widely used in mainstay industries such as national defense construction, chemical industry, printing and dyeing, automobile, communication, is the closely-related base mateiral of industrial development and people's lives.Because the lead ore resource-constrained, each country more payes attention to the reclaiming recycling of leaded waste in the exploitation lead ore.But, no matter be that lead ore is smelted or the refining lead skim that derives in its smelting process is smelted in the recovery of scrap lead; The lead that generally contains 8%-10%; The antimony of 8%--18%, 20%--30% subtracts, for the refining lead skim of the qualified discharge standard that does not reach national environmental protection department regulation at present; Mostly enterprise is to concentrate stacks, and does not accomplish harmless treatment.
The utility model content
The utility model technical problem to be solved is to carry out autonomous innovation around plumbous separation and Extraction of smelting lead in the verivate refining lead skim; The new technology that obtains is implemented harmless treatment to it, the device of plumbous refining alkaline residue single stage method separation of lead, antimony slag and alkali lye that the refined lead slag for comprehensive during realization is derived to plumbous smelting process effectively utilizes.
The utility model technical problem to be solved adopts following technical scheme to realize,
The device of a kind of plumbous refining alkaline residue single stage method separation of lead, antimony slag and alkali lye; Comprise reaction kettle, be provided with stirring mechanism in the said reaction kettle, described stirring mechanism is connected with buncher; It is characterized in that: described reaction kettle sidewall is provided with antimony slag and alkali lye outlet; Said reaction kettle bottom is provided with the outlet of metal lead skim, and described metal lead skim outlet is connected with filter vat, and described filter vat is connected with flame filter press through pump.
Described antimony slag and alkali lye outlet are connected with filter vat through pipeline.
Be provided with dividing plate in the said filter vat, dividing plate is with the filter vat separated into two parts, and a part is communicated with antimony slag and alkali lye outlet, and another part is communicated with the outlet of metal lead skim.
Said metal lead skim outlet below is positioned at the filter vat level and is provided with screen plate.
The beneficial effect of the utility model is: the utility model mainly is to be applied to the waste refining lead skim that lead ore is smelted, scrap lead reclaims verivate in the smelting renewable resource smelting process; The lead that single stage method will wherein contain, antimony slag and alkali lye separation and Extraction are come out; Simple and convenient, the plumbous smelting in ore deposit, scrap lead are smelted the useless refining lead skim of generation danger in the renewable resource process, obtain fully utilizing; Eliminate the risk of contaminate environment, obtained good economic benefits.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose and be easy to understand understanding with effect, below in conjunction with concrete diagram, further set forth the utility model.
As shown in Figure 1, the device of a kind of plumbous refining alkaline residue single stage method separation of lead, antimony slag and alkali lye comprises reaction kettle 3; Be provided with stirring mechanism 2 in the reaction kettle 3, stirring mechanism 2 is connected with buncher 1, and reaction kettle 3 sidewalls are provided with antimony slag and alkali lye outlet 6; Reaction kettle 3 bottoms are provided with metal lead skim outlet 4; Metal lead skim outlet 4 is connected with filter vat 8, and filter vat 8 is connected with flame filter press 11 through pump 10, and antimony slag and alkali lye outlet 6 are connected with filter vat 8 through pipeline 7.Be provided with dividing plate 9 in the filter vat 8, dividing plate 9 is the filter vat separated into two parts, and a part is communicated with antimony slag and alkali lye outlet 6, and another part is communicated with metal lead skim outlet 4, and the metal lead skim exports 4 belows and is positioned at filter vat 8 levels and is provided with screen plate 5.
During work, at first alkaline residue and the water ratio in 4: 1 is added in the reaction kettle 3, the temperature in the reaction kettle 3 are controlled at 20-70 ℃; Stirred one hour; Antimony slag and alkali lye are isolated in antimony slag and alkali lye outlet 6 on reaction kettle 3 tops, and the metal lead skim is separated the metal lead button on the screen plate 5 that metal lead skim outlet 4 enters in the filter vat 8, and the metal lead button directly gets into the refining furnace refining; Antimony slag and alkali lye are sent into flame filter press 11 with pump 10; Isolate antimony slag and alkali lye, the antimony slag can be used as further antimony product raw material, and alkali lye can be used as sweetening agent.
More than show and described ultimate principle of the utility model and the advantage of principal character and the utility model.The technician of the industry should understand; The utility model is not restricted to the described embodiments; The principle of describing in the foregoing description and the specification sheets that the utility model just is described; Under the prerequisite that does not break away from the utility model spirit and scope, the utility model also has various changes and modifications, and these variations and improvement all fall in the utility model scope that requires protection.The utility model requires protection domain to be defined by appending claims and equivalent thereof.
Claims (4)
1. the device of plumbous refining alkaline residue single stage method separation of lead, antimony slag and alkali lye; Comprise reaction kettle, be provided with stirring mechanism in the said reaction kettle, described stirring mechanism is connected with buncher; It is characterized in that: described reaction kettle sidewall is provided with antimony slag and alkali lye outlet; Said reaction kettle bottom is provided with the outlet of metal lead skim, and described metal lead skim outlet is connected with filter vat, and described filter vat is connected with flame filter press through pump.
2. the device of plumbous refining alkaline residue single stage method separation of lead according to claim 1, antimony slag and alkali lye is characterized in that: described antimony slag and alkali lye outlet are connected with filter vat through pipeline.
3. the device of plumbous refining alkaline residue single stage method separation of lead according to claim 1, antimony slag and alkali lye; It is characterized in that: be provided with dividing plate in the said filter vat; Dividing plate is with the filter vat separated into two parts, and a part is communicated with antimony slag and alkali lye outlet, and another part is communicated with the outlet of metal lead skim.
4. the device of plumbous refining alkaline residue single stage method separation of lead according to claim 1, antimony slag and alkali lye is characterized in that: said metal lead skim outlet below is positioned at the filter vat level and is provided with screen plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203659366U CN202297739U (en) | 2011-09-28 | 2011-09-28 | Device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203659366U CN202297739U (en) | 2011-09-28 | 2011-09-28 | Device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202297739U true CN202297739U (en) | 2012-07-04 |
Family
ID=46366674
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203659366U Expired - Fee Related CN202297739U (en) | 2011-09-28 | 2011-09-28 | Device for separating lead, antimony sludge and alkali liquor in one-step method of lead refining caustic sludge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202297739U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102329965A (en) * | 2011-09-28 | 2012-01-25 | 界首市骏马工贸有限公司 | Device and method for separating lead, antimony slag and alkaline liquor from lead-refined alkali slag by using one-step method |
| CN106282588A (en) * | 2016-08-25 | 2017-01-04 | 安徽华铂再生资源科技有限公司 | Alkali regeneration method in reviver refine alkaline residue |
-
2011
- 2011-09-28 CN CN2011203659366U patent/CN202297739U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102329965A (en) * | 2011-09-28 | 2012-01-25 | 界首市骏马工贸有限公司 | Device and method for separating lead, antimony slag and alkaline liquor from lead-refined alkali slag by using one-step method |
| CN106282588A (en) * | 2016-08-25 | 2017-01-04 | 安徽华铂再生资源科技有限公司 | Alkali regeneration method in reviver refine alkaline residue |
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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: 20120928 |