CN204570002U - A kind of cupric refractory gold concentrate soaks golden system - Google Patents
A kind of cupric refractory gold concentrate soaks golden system Download PDFInfo
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- CN204570002U CN204570002U CN201520177867.4U CN201520177867U CN204570002U CN 204570002 U CN204570002 U CN 204570002U CN 201520177867 U CN201520177867 U CN 201520177867U CN 204570002 U CN204570002 U CN 204570002U
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- feeder
- leaching
- cupric
- storehouse
- gold concentrate
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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
The utility model discloses a kind of cupric refractory gold concentrate and soak golden system, comprise leaching plant, tailings glass equipment, medicament recovery system and replacing apparatus, it is characterized in that: described leaching plant comprises thiocarbamide feeder, oxide compound feeder, prussiate feeder, sulfuric acid feeder and leaching storehouse, described thiocarbamide feeder, oxide compound feeder, prussiate feeder and sulfuric acid feeder are all connected with leaching storehouse, described leaching plant and leach storehouse all with tailings glass equipment connection, described leaching storehouse is connected with medicament recovery system, described leaching storehouse is all connected with replacing apparatus with leaching plant, described tailings glass equipment is connected with replacing apparatus, constant temperature mechanism is provided with in described leaching storehouse, by each equipment reasonable coordination, it is rational in infrastructure to be that the utility model has, protection of the environment, improve leaching efficiency, energy circulating leaching, reduce and consume, and can will recycle with medicament, the cupric refractory gold concentrate reducing the advantages such as production cost soaks golden system.
Description
Technical field
The utility model relates to a kind of cupric refractory gold concentrate and soaks golden system.
Background technology
Adopt cyanide process mostly in a current method to kind of cupric refractory gold concentrate leaching gold, although the method soaks golden method the most widely at present, but because prussiate has severe toxicity, very big to environmental hazard, and the lysate of gold is slower, during to low grade ore or refractory ore, the reagent consumption of Cyanide Leaching and metallic element impact comparatively greatly, also cause leaching effect poor.
Therefore, need to provide a kind of new technical scheme to solve the problems referred to above.
Utility model content
(1) technical problem that will solve
For solving the problem, the utility model proposes a kind of rational in infrastructure, protection of the environment, improves leaching efficiency, and energy circulating leaching, reduces and consume, and can will recycle with medicament, and the cupric refractory gold concentrate reducing production cost soaks golden system.
(2) technical scheme
Cupric refractory gold concentrate of the present utility model soaks golden system, comprise leaching plant, tailings glass equipment, medicament recovery system and replacing apparatus, it is characterized in that: described leaching plant comprises thiocarbamide feeder, oxide compound feeder, prussiate feeder, sulfuric acid feeder and leaching storehouse, described thiocarbamide feeder, oxide compound feeder, prussiate feeder and sulfuric acid feeder are all connected with leaching storehouse, described leaching plant and leach storehouse all with tailings glass equipment connection, described leaching storehouse is connected with medicament recovery system, described leaching storehouse is all connected with replacing apparatus with leaching plant, described tailings glass equipment is connected with replacing apparatus, constant temperature mechanism is provided with in described leaching storehouse.
Further, described tailings glass equipment be provided with dense molten machine, thickener, pressure filter and filter between replacing apparatus and be connected.
Further, described medicament recovery system is connected with each feeder by pipeline.
Further, water conditioning mechanism is provided with in described medicament recovery system.
Further, described thickener and pressure filter are that three stage countercurrent vacuum type process.
Further, described replacing apparatus includes melting mechanism.
Further, described leaching storehouse is provided with more than five or five.
Further, iron trichloride is had in described oxide compound feeder.
(3) beneficial effect
Compared with prior art, it has following beneficial effect to the utility model:
Cupric refractory gold concentrate of the present utility model soaks golden system by each equipment reasonable coordination; it is rational in infrastructure to be that the utility model has; protection of the environment; improve leaching efficiency; energy circulating leaching; reduce and consume, and can will recycle with medicament, the cupric refractory gold concentrate reducing the advantages such as production cost soaks golden system.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
A kind of cupric refractory gold concentrate as shown in Figure 1 soaks golden system, comprise leaching plant, tailings glass equipment, medicament recovery system and replacing apparatus, the medicament of remnants can reclaim by medicament recovery system, reduce dosing, and reduce cost, described leaching plant comprises thiocarbamide feeder, oxide compound feeder, prussiate feeder, sulfuric acid feeder and leaching storehouse, described thiocarbamide feeder, oxide compound feeder, prussiate feeder and sulfuric acid feeder are all connected with leaching storehouse, iron trichloride in prussiate feeder, thiocarbamide feeder and sulfuric acid feeder are after the consumption of 1 to 1, the change of ore pulp can be made more stable, owing to being provided with constant temperature mechanism in described leaching storehouse, improve the stability of change, described leaching plant and leach storehouse all with tailings glass equipment connection, described leaching storehouse is connected with medicament recovery system, described leaching storehouse is all connected with replacing apparatus with leaching plant, described tailings glass equipment is connected with replacing apparatus, when running into different low grade ore, part can directly save leach storehouse part directly and tailings glass equipment leach, refractory ore leaching in storehouse the leaching carried out 20 to 24 hours, not only can improve gold leaching rate, also reducing the consumption of thiocarbamide, reducing cost, directly can add that the charging of thiocarbamide can allow the leaching yield of copper very steady, the effective severe toxicity harm reducing prussiate and bring leaching all sliming cyanidation in storehouse by prussiate feeder, and also reduce can subsequent recovery impact, raise the efficiency.
Wherein, described tailings glass equipment be provided with dense molten machine, thickener, pressure filter and filter between replacing apparatus and be connected; Described medicament recovery system is connected with each feeder by pipeline; Be provided with water conditioning mechanism in described medicament recovery system, can recycle protection support; Described thickener and pressure filter are that three stage countercurrent vacuum type process; Described replacing apparatus includes melting mechanism; Described leaching storehouse is provided with more than five or five; Iron trichloride is had in described oxide compound feeder.
Cupric refractory gold concentrate of the present utility model soaks golden system; its advantage is: by each equipment reasonable coordination; it is rational in infrastructure to be that the utility model has; protection of the environment; improve leaching efficiency, energy circulating leaching, reduces and consumes; and can will recycle with medicament, the cupric refractory gold concentrate reducing the advantages such as production cost soaks golden system.
Embodiment recited above is only be described preferred implementation of the present utility model, not limits design of the present utility model and scope.Under the prerequisite not departing from the utility model design concept; the various modification that this area ordinary person makes the technical solution of the utility model and improvement; protection domain of the present utility model all should be dropped into; the technology contents of the utility model request protection, all records in detail in the claims.
Claims (8)
1. a cupric refractory gold concentrate soaks golden system, comprise leaching plant, tailings glass equipment, medicament recovery system and replacing apparatus, it is characterized in that: described leaching plant comprises thiocarbamide feeder, oxide compound feeder, prussiate feeder, sulfuric acid feeder and leaching storehouse, described thiocarbamide feeder, oxide compound feeder, prussiate feeder and sulfuric acid feeder are all connected with leaching storehouse, described leaching plant and leach storehouse all with tailings glass equipment connection, described leaching storehouse is connected with medicament recovery system, described leaching storehouse is all connected with replacing apparatus with leaching plant, described tailings glass equipment is connected with replacing apparatus, constant temperature mechanism is provided with in described leaching storehouse.
2. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: described tailings glass equipment be provided with dense molten machine, thickener, pressure filter and filter between replacing apparatus and be connected.
3. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: described medicament recovery system is connected with each feeder by pipeline.
4. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: be provided with water conditioning mechanism in described medicament recovery system.
5. cupric refractory gold concentrate according to claim 2 soaks golden system, it is characterized in that: described thickener and pressure filter are that three stage countercurrent vacuum type process.
6. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: described replacing apparatus includes melting mechanism.
7. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: described leaching storehouse is provided with more than five or five.
8. cupric refractory gold concentrate according to claim 1 soaks golden system, it is characterized in that: have iron trichloride in described oxide compound feeder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520177867.4U CN204570002U (en) | 2015-03-27 | 2015-03-27 | A kind of cupric refractory gold concentrate soaks golden system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520177867.4U CN204570002U (en) | 2015-03-27 | 2015-03-27 | A kind of cupric refractory gold concentrate soaks golden system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204570002U true CN204570002U (en) | 2015-08-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201520177867.4U Active CN204570002U (en) | 2015-03-27 | 2015-03-27 | A kind of cupric refractory gold concentrate soaks golden system |
Country Status (1)
| Country | Link |
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| CN (1) | CN204570002U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115961143A (en) * | 2022-12-24 | 2023-04-14 | 涉县宝轩机械设备有限公司 | Efficient energy-saving leaching tank for argillized ores |
-
2015
- 2015-03-27 CN CN201520177867.4U patent/CN204570002U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115961143A (en) * | 2022-12-24 | 2023-04-14 | 涉县宝轩机械设备有限公司 | Efficient energy-saving leaching tank for argillized ores |
| CN115961143B (en) * | 2022-12-24 | 2023-10-17 | 山西建兴机械设备有限公司 | High-efficiency energy-saving leaching tank for mud mine |
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