CN203256315U - Cyaniding leaching tank - Google Patents
Cyaniding leaching tank Download PDFInfo
- Publication number
- CN203256315U CN203256315U CN2013201955237U CN201320195523U CN203256315U CN 203256315 U CN203256315 U CN 203256315U CN 2013201955237 U CN2013201955237 U CN 2013201955237U CN 201320195523 U CN201320195523 U CN 201320195523U CN 203256315 U CN203256315 U CN 203256315U
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- Prior art keywords
- leaching
- cell body
- cyanide
- leaching tank
- cyanide leaching
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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 cyaniding leaching tank relates to a three-phase reaction device in the hydrometallurgy process, in particular to a leaching tank for cyaniding and leaching gold. The structure of the device comprises a leaching tank body, a driving motor and a speed reducer which are positioned above the leaching tank body, a speed reducer bracket, a stirring shaft which is connected with the speed reducer and is vertically positioned in the leaching tank body, and a stirring impeller which is fixed on the stirring shaft; the device is characterized in that the inflating device is a plurality of jetting inflators which are uniformly distributed in the horizontal circumferential direction and penetrate through the side wall of the lower part of the leaching tank body. The utility model discloses a cyanide leaching tank can effectively reduce the bubble diameter little, improves dissolved oxygen volume, and then improves the leaching rate of gold, reduces the consumption of cyanide, reduces the consumption of air, can maintain inflation system on line, reduces operation and maintenance cost.
Description
Technical field
A kind of Cyanide Leaching groove relates to the phase reaction equipment in a kind of hydrometallurgy process, especially for the leaching vat of gold Cyanide Leaching.
Background technology
It is main production gold method that Cyanide Leaching extracts gold from.Stirring cyanidation leaches and refers to levigate material and Cyanide Leaching agent are placed in the leaching steel basin, completes the process of leaching under the condition that stirs and inflate.
The electrochemical reaction that gold dissolves in the Cyanide Leaching steel basin is:
4Au+8CN
-+O
2+2H
2O=4Au(CN)
- 2+4OH
-
Prussiate and oxygen concentration are two topmost factors that determine golden dissolution rate.
At present, the Cyanide Leaching groove mainly is divided three classes: mechanical stirring Cyanide Leaching groove, pneumatic blending Cyanide Leaching groove, air and mechanically combining stirred leaching tank.China's gold mine Cyanide Leaching steel basin overwhelming majority used is the mechanical stirring leaching vat, this Cyanide Leaching steel basin is to transform a little to form on the basis of mining steel basin, mainly insert gas-filled valve or inflate by stirring in hollow axial groove at the periphery of flowsheet of slurry agitation groove, have the shortcomings such as energy consumption is high, easy deep gouge, air-dispersion is poor, dissolved oxygen amount is low, leaching efficiency is low, leaching cycle is long, the shortcoming of existing Cyanide Leaching steel basin has seriously restricted the production efficiency of gold mine.
Before 20 century 70s, China mainly adopts single impeller Cyanide Leaching steel basin.Along with developing rapidly of China's gold mine selecting and purchasing industry, the units such as the metallurgical design studies of China YouSe total institute have developed SJ type bilobed wheel Cyanide Leaching steel basin, and obtain widespread use.Its airing form mainly contains two kinds, and a kind of is quill shaft inflation (Fig. 1), and another kind is a steel pipe ring inflation (Fig. 2) that a lot of small sircle holes are arranged by the impeller below.No matter be quill shaft inflation or the inflation of bottom annulus, its shortcoming is mainly by the stirring action of impeller, airflow to be smashed to be small bubbles, bubble diameter is large, the air dispersion weak effect, dissolved oxygen content is low, and air utilization ratio is low, and most of air effusion ore pulp surface is returned in atmosphere, cause the gold cyanidation leaching rate slow, the Cyanide Leaching cycle is long.
Patent CN200720092935.2 changes the bottom inflation ring into the so-called microvesicle Inflatable dispenser (Fig. 3) that is formed and punched by up and down two block plates on the steel plate of upper strata, although can being distributed in groove even air, but the restriction that is subject to processing, bore dia on steel plate is still bigger than normal, cause bubble diameter bigger than normal, air utilization ratio is low; In addition, gold cyanidation leaches and all to carry out under alkaline environment, and on steel plate, the hole is easy to tie calcium and blocks.
Above-mentioned Cyanide Leaching steel basin is to transform a little to form on the basis of mining steel basin mostly, the shortcomings such as the ubiquity air dispersion is poor, air utilization ratio is low, dissolved oxygen amount is low, leaching efficiency is low, leaching cycle is long have seriously restricted the production efficiency of gold mine.
Summary of the invention
Purpose of the present invention is exactly the deficiency that exists for above-mentioned prior art, provides a kind of air dispersion good, and bubble diameter is little, the Cyanide Leaching groove that air utilization ratio and dissolved oxygen content are high.
Purpose of the present invention is achieved through the following technical solutions:
A kind of Cyanide Leaching groove, its structure comprises: the leaching vat cell body, be positioned at drive-motor and the step-down gear of leaching vat cell body top, the step-down gear support, the stir shaft that is positioned at the leaching vat cell body that connect with step-down gear, vertical is fixed on the paddle wheel on stir shaft; It is characterized in that its inflation mechanism circumferentially evenly distributes, penetrates the injection aerator of leaching vat cell body lower sides for several levels.
A kind of Cyanide Leaching groove of the present invention is characterized in that described injection aerator in leaching vat cell body bottom, and the part of aerator is inserted in the leaching vat cell body, and level was arranged in centripetal minute.
A kind of Cyanide Leaching groove of the present invention is characterized in that described injection aerator is 3～10.
A kind of Cyanide Leaching groove of the present invention is characterized in that described aerator nozzle diameter is 0.5mm～6.0mm.
A kind of Cyanide Leaching groove of the present invention is characterized in that described several spray aerators and connect with leaching vat cell body steam line outward respectively, and this steam line is around the annular steel pipe that is arranged on the outer bottom of leaching vat cell body.
A kind of Cyanide Leaching groove of the present invention is characterized in that described steam line connects with air compressor machine by controlling pipeline, is provided with reducing valve, under meter, tensimeter on the control pipeline.
A kind of Cyanide Leaching groove of the present invention, high-pressure air can be sprayed by aerator and enter in ore pulp, can form a large amount of small bubbles in ore pulp, improve the gas-to-liquid contact area, improve the dissolved oxygen content in ore pulp, improve the gold cyanidation leaching rate, shorten the gold cyanidation extraction time, simplify the Cyanide Leaching flow process.
Description of drawings
Fig. 1 is a kind of leaching vat structural representation in prior art.
Fig. 2 is another kind of leaching vat structural representation in prior art.
Fig. 3 is another kind of leaching vat structural representation in prior art.
Fig. 4 is structural representation of the present utility model.
Fig. 5 is the part sectioned view of Fig. 4.
Embodiment
A kind of Cyanide Leaching groove, its structure comprises: leaching vat cell body 1 is positioned at drive-motor 2 and the step-down gear 3 of leaching vat cell body top, step-down gear support 4, the stir shaft 5 that is positioned at the leaching vat cell body that connect with step-down gear, vertical is fixed on the paddle wheel 6 on stir shaft; Its inflation mechanism circumferentially evenly distributes, penetrates the injection aerator 7 of leaching vat cell body lower sides for several levels; Its injection aerator bottom in the leaching vat cell body, level was arranged in centripetal minute; Spray quantity and the nozzle diameter of aerator and determine according to the designed capacity of leaching vat, be generally 3～10; Nozzle diameter is 0.5mm～6.0mm.
A kind of Cyanide Leaching groove of the present invention, described several spray aerators and connect with leaching vat cell body steam line 8 outward respectively, and this steam line is around the annular steel pipe that is arranged on the outer bottom of leaching vat cell body; Steam line connects with air compressor machine 10 by controlling pipeline 9, is provided with reducing valve 11, under meter 12, tensimeter 13 on the control pipeline.
Leaching vat of the present invention, it is even that its inflation system has air dispersion, and bubble diameter is little, and air utilization ratio is high, and dissolved oxygen content is high, the advantage such as can change online.During operation, motor reducer-stirring power is provided for the Cyanide Leaching steel basin; Step-down gear support-support motor step-down gear and stirring main shaft; Stir the transmission of power of main shaft-motor is produced to impeller, the impeller rotation; Cell body carrying Cyanide Leaching ore pulp; Impeller stirs ore pulp; The inflation main line is distributed to several aerators with the high pressure gas that air compressor machine produces; Gas-filled valve and injection nozzle are filled into the form of high pressure gas with micro-bubble in the Cyanide Leaching groove; The inflation pressure of the tensimeter on main pipe line-measurement Cyanide Leaching steel basin; The aeration quantity of flowmeter survey Cyanide Leaching steel basin; Reducing valve is regulated the inflation pressure of Cyanide Leaching steel basin; Air compressor machine produces high-pressure air; High-pressure air provides the pressure of source of the gas greater than 0.3MPa for gas-filled valve and injection nozzle; Nozzle diameter 0.5mm is to 6.0mm; High-pressure air enters in ore pulp by nozzle ejection; Can form a large amount of small bubbles in ore pulp; Improve the gas-to-liquid contact area; Improve the dissolved oxygen content in ore pulp; Gas-filled valve is arranged in the outside of reactor, if material or fouling cause aerator to stop up, can change online or keep in repair, and can not have any impact to normal production; Determine the quantity, nozzle diameter of aerator, decoration form and position on cell body according to the tolerance of industrial production needs.Can close separately certain or certain several aerators, also can change separately the nozzle of certain or certain several diameters, the convenient adjusting.
Claims (6)
1. Cyanide Leaching groove, its structure comprises: the leaching vat cell body, be positioned at drive-motor and the step-down gear of leaching vat cell body top, the step-down gear support, the stir shaft that is positioned at the leaching vat cell body that connect with step-down gear, vertical is fixed on the paddle wheel on stir shaft; It is characterized in that its inflation mechanism circumferentially evenly distributes, penetrates the injection aerator of leaching vat cell body lower sides for several levels.
2. a kind of Cyanide Leaching groove according to claim 1 is characterized in that described injection aerator bottom in the leaching vat cell body, and level was arranged in centripetal minute.
3. a kind of Cyanide Leaching groove according to claim 1, is characterized in that described injection aerator is 3～10.
4. a kind of Cyanide Leaching groove according to claim 1, is characterized in that described aerator nozzle diameter is 0.5mm～6.0mm.
5. a kind of Cyanide Leaching groove according to claim 1, is characterized in that described several spray aerators and connect with leaching vat cell body steam line outward respectively, and this steam line is around being arranged on bottom circulating line outside the leaching vat cell body.
6. a kind of Cyanide Leaching groove according to claim 5, is characterized in that described steam line connects with air compressor machine by controlling pipeline, is provided with reducing valve, under meter, tensimeter on the control pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201955237U CN203256315U (en) | 2013-04-18 | 2013-04-18 | Cyaniding leaching tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201955237U CN203256315U (en) | 2013-04-18 | 2013-04-18 | Cyaniding leaching tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203256315U true CN203256315U (en) | 2013-10-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013201955237U Expired - Lifetime CN203256315U (en) | 2013-04-18 | 2013-04-18 | Cyaniding leaching tank |
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| CN (1) | CN203256315U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103602809A (en) * | 2013-11-29 | 2014-02-26 | 中南大学 | Stirring reaction tank used for amplified culturing of mineral-leaching microorganism |
| CN103695642A (en) * | 2013-12-10 | 2014-04-02 | 王安劳 | Dual-impeller hollow-shaft inflated stirred leaching tank |
| EA025097B1 (en) * | 2014-02-04 | 2016-11-30 | Открытое Акционерное Общество "Научно-Исследовательский Институт Металлургической Теплотехники" Оао "Вниимт" | Apparatus for executing technological processes in two-phase system "liquid-solid" |
| CN106269294A (en) * | 2016-08-17 | 2017-01-04 | 北矿机电科技有限责任公司 | A kind of aerating device of agitation impeller flotator |
| CN110331277A (en) * | 2019-07-02 | 2019-10-15 | 长春黄金研究院有限公司 | A method of oxidation carries golden sulfide mineral |
| CN118499691A (en) * | 2024-07-18 | 2024-08-16 | 山东华东风机有限公司 | Air supply system and control method applied to mineral separation and gold extraction and nonferrous metal separation and smelting |
-
2013
- 2013-04-18 CN CN2013201955237U patent/CN203256315U/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103602809A (en) * | 2013-11-29 | 2014-02-26 | 中南大学 | Stirring reaction tank used for amplified culturing of mineral-leaching microorganism |
| CN103602809B (en) * | 2013-11-29 | 2015-09-02 | 中南大学 | A kind of stirred tank for leaching microbacteria amplification culture |
| CN103695642A (en) * | 2013-12-10 | 2014-04-02 | 王安劳 | Dual-impeller hollow-shaft inflated stirred leaching tank |
| EA025097B1 (en) * | 2014-02-04 | 2016-11-30 | Открытое Акционерное Общество "Научно-Исследовательский Институт Металлургической Теплотехники" Оао "Вниимт" | Apparatus for executing technological processes in two-phase system "liquid-solid" |
| CN106269294A (en) * | 2016-08-17 | 2017-01-04 | 北矿机电科技有限责任公司 | A kind of aerating device of agitation impeller flotator |
| CN110331277A (en) * | 2019-07-02 | 2019-10-15 | 长春黄金研究院有限公司 | A method of oxidation carries golden sulfide mineral |
| CN118499691A (en) * | 2024-07-18 | 2024-08-16 | 山东华东风机有限公司 | Air supply system and control method applied to mineral separation and gold extraction and nonferrous metal separation and smelting |
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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: 100070, No. 23, building 18, 188, base station, South Fourth Ring Road West, Beijing, Fengtai District Co-patentee after: Mining and Metallurgical Technology Group Co.,Ltd. Patentee after: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. Address before: 100070, No. 23, building 18, 188, base station, South Fourth Ring Road West, Beijing, Fengtai District Co-patentee before: Bgrimm Technology Group Patentee before: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. Address after: 100070, No. 23, building 18, 188, base station, South Fourth Ring Road West, Beijing, Fengtai District Co-patentee after: Bgrimm Technology Group Patentee after: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. Address before: 100070, No. 23, building 18, 188, base station, South Fourth Ring Road West, Beijing, Fengtai District Co-patentee before: Beijing General Research Institute of Mining and Metallurgy Patentee before: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200522 Address after: No.23, 18th District, No.188, nansihuan West Road, Fengtai District, Beijing 100160 Patentee after: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. Address before: 100070, No. 23, building 18, 188, base station, South Fourth Ring Road West, Beijing, Fengtai District Co-patentee before: Mining and Metallurgical Technology Group Co.,Ltd. Patentee before: BGRIMM MACHINERY & AUTOMATION TECHNOLOGY Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131030 |