CN105498952B - Gold tailing processing system and method - Google Patents
Gold tailing processing system and method Download PDFInfo
- Publication number
- CN105498952B CN105498952B CN201610074307.5A CN201610074307A CN105498952B CN 105498952 B CN105498952 B CN 105498952B CN 201610074307 A CN201610074307 A CN 201610074307A CN 105498952 B CN105498952 B CN 105498952B
- Authority
- CN
- China
- Prior art keywords
- thickener
- mastic
- golden
- paste
- spiral chute
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
Abstract
The invention provides a gold tailing processing system and method. The gold tailing processing system comprises a feeding mechanism, a spiral chute connected to the feeding mechanism, a first paste thickener and a thickener connected to the spiral chute respectively, a tower mill connected to the thickener, a leaching adsorption device and a second paste thickener connected to the tower mill respectively, a paste filling system connected to the second paste thickener, and a high pond connected to the spiral chute, wherein the first paste thickener is connected to the paste filling system, and the high pond is connected to the first paste thickener and the thickener. The gold tailing processing system can be used for refining gold and other valuable elements from abandoned gold tailings, thereby improving the efficiency of utilization of resources and reaching the aim of eliminating tailing ponds.
Description
Technical field
The present invention relates to the system and method that a kind of mining tailing is utilized, more particularly to a kind of golden tailings glass system and place
Reason method.
Background technology
China's gold ore deposit species is various, and size mineral deposit spreads all over the country, and the development for Gold Mining Industry provides good money
Source basis.But golden production is due to being restricted by various factors such as industrial policy, technical equipment, dressing and smelting process and funds, resource
Producing level is generally low, serious waste phenomenon.
, more than 24,500,000 tons, current comprehensive utilization of tailing rate is very low, about for the mine tailing of China's gold system discharge every year
For 7%, typically still substantial amounts of soil is not only taken up, Tailings Dam ambient contamination, Er Qiexu is caused using stacked arrangement process
Input substantial contribution is used for Tailings Dam and builds and safeguard, therefore, for gold tailings comprehensive utilization has become gold mine resource
Comprehensive utilization and the important topic of aspect of preserving the ecological environment.
The content of the invention
The present invention proposes a kind of golden tailings glass system and processing method, and in solving prior art, mine tailing is piled up and polluted
The problems such as environment.
The technical scheme is that what is be achieved in that：
A kind of golden tailings glass system, including the spiral chute and spiral chute point of feeding mechanism and feeding mechanism connection
The leaching that the tower grinding machine and tower grinding machine that the first mastic thickener not connected is connected with thickener and thickener connects respectively is inhaled
The Paste-filling System that adsorption device is connected with the second mastic thickener and the second mastic thickener, the first mastic thickener
Also it is connected with Paste-filling System, the golden tailings glass system also includes a head-tank being connected with spiral chute, the high position
Pond is also connected with the first mastic thickener and thickener respectively.
Preferred version is that the spiral chute is for golden mine tailing is separated again, and coarse granule ore pulp is supplied to
Fine grained ore pulp is supplied to the first mastic thickener by thickener.
Preferred version is that the coarse granule ore pulp that the thickener is used to be introduced into enters the separation of water-filling ore deposit.
Preferred version is that the adsorbent equipment that leaches is for reclaiming to valuable element.
Preferred version is, the Paste-filling System is for the underflow of the second mastic thickener is backfilled.
A kind of golden tailings processing method：
First, golden mine tailing is entered by feeding mechanism；
2nd, golden mine tailing is separated again by spiral chute, after coarse granule ore pulp is reclaimed, is entered thickener, while
Fine grained ore pulp is introduced to the first mastic thickener carries out mastic concentration, and the overflow water produced in concentration process enters high-order water
Pond, returns again to spiral chute；
3rd, the underflow drawn by the first mastic thickener is backfilled into Paste-filling System；
4th, coarse granule ore pulp enters the separation of water-filling ore deposit by thickener, and its overflow water enters head-tank, returns again to spiral
Chute；
5th, tower grinding machine is entered by the underflow that thickener is drawn, fine grinding is carried out by tower grinding machine, the ore pulp after fine grinding enters leaching
Going out adsorbent equipment carries out the recovery of the valuable elements such as gold, and its tailings carries out mastic concentration into the second mastic thickener, by second
The overflow water produced in mastic thickener concentration process is back to tower grinding machine, and its underflow is backfilled into Paste-filling System.
Beneficial effects of the present invention are：
The golden tailings glass system of the present invention can from discarded golden mine tailing the valuable element such as Extracting Gold again, raising resource
Utilization ratio, and realize anuryization process, reduce waste put, reach elimination Tailings Dam purpose.
Description of the drawings
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or existing
Accompanying drawing to be used needed for having technology description is briefly described, it should be apparent that, drawings in the following description are only this
Some embodiments of invention, for those of ordinary skill in the art, on the premise of not paying creative work, can be with
Other accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the functional block diagram of gold tailings glass system of the invention.
In figure：
10th, feeding mechanism；20th, spiral chute；30th, the first mastic thickener；40th, thickener；50th, tower grinding machine；60th, leach
Adsorbent equipment；70th, the second mastic thickener；80th, Paste-filling System；90th, head-tank.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than the embodiment of whole.It is based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
As shown in figure 1, the golden tailings glass system include feeding mechanism 10, and feeding mechanism 10 connection spiral chute
20th, and the first mastic thickener 30 that connects respectively of spiral chute 20 and thickener 40, and thickener 40 be connected tower grinding machine 50,
With tower grinding machine 40 be connected respectively leach adsorbent equipment 60 and the second mastic thickener 70, and the second mastic thickener 70 be connected
Paste-filling System 80, the first mastic thickener 30 are also connected with Paste-filling System 80.The golden tailings glass system is also
Including a head-tank 90 being connected with spiral chute 20, the head-tank 90 also respectively with the first mastic thickener 30 and concentration
Machine 40 connects.
The feeding mechanism 10 is used to introduce the materials such as golden mine tailing, and is supplied to spiral chute 20.The spiral chute 20
For golden mine tailing is separated again, and coarse granule ore pulp is supplied to into thickener 40, fine grained ore pulp is supplied to into first
Mastic thickener 30.The first mastic thickener 30 is for carrying out mastic concentration to fine grained ore pulp.The thickener 40 is used
Enter the separation of water-filling ore deposit in the coarse granule ore pulp being introduced into, and its underflow is supplied to into tower grinding machine 40.The tower grinding machine 40 is used for will
The underflow of introduction carries out fine grinding, and the slurry after fine grinding is supplied to leaching adsorbent equipment 60.The leaching adsorbent equipment 60 is used
In reclaiming to valuable element.The second mastic thickener 70 carries out cream for will leach the tailings that produces of adsorbent equipment 60
Body is concentrated, and the overflow water of generation is supplied to tower grinding machine 40.The Paste-filling System 80 is for by the second mastic thickener
70 underflow is backfilled.The head-tank 90 is for thickener 40 and the first mastic thickener 30 are distinguished in the course of work
The overflow water of generation is introduced, and is available to spiral chute 20.
The processing method of the golden tailings glass system is as follows：
First, golden mine tailing is entered by feeding mechanism 10；
2nd, golden mine tailing is separated again by spiral chute 20, after coarse granule ore pulp is reclaimed, is entered thickener 40,
Fine grained ore pulp is introduced to the first mastic thickener 30 carries out mastic concentration simultaneously, and the overflow water produced in concentration process is entered
Head-tank 90, returns again to spiral chute 20；
3rd, the underflow drawn by the first mastic thickener 30 is backfilled into Paste-filling System 80；
4th, coarse granule ore pulp by thickener 40 enter water-filling ore deposit separation, its overflow water enter head-tank 90, return again to
Spiral chute 20；
5th, tower grinding machine 40 is entered by the underflow that thickener 40 is drawn, fine grinding is carried out by tower grinding machine 40, the ore pulp after fine grinding
The recovery of the valuable elements such as gold is carried out into adsorbent equipment 60 is leached, it is dense that its tailings carries out mastic into the second mastic thickener 70
Contracting, is back to tower grinding machine 40 by the overflow water produced in 70 concentration process of the second mastic thickener, and its underflow enters paste body filling
System 80 is backfilled.
The golden tailings glass system can from discarded golden mine tailing the valuable element such as Extracting Gold again, improve the utilization of resource
Efficiency, and realize that anuryization is processed, reduce waste and put, reach elimination Tailings Dam purpose.
Presently preferred embodiments of the present invention is the foregoing is only, not to limit the present invention, all essences in the present invention
Within god and principle, any modification, equivalent substitution and improvements made etc. should be included within the scope of the present invention.
Claims (6)
1. a kind of golden tailings glass system, it is characterised in that：Including feeding mechanism and feeding mechanism connection spiral chute and
The tower grinding machine and tower grinding machine that the first mastic thickener that spiral chute connects respectively is connected with thickener and thickener connects respectively
The Paste-filling System that the leaching adsorbent equipment for connecing is connected with the second mastic thickener and the second mastic thickener, described first
Mastic thickener is also connected with Paste-filling System, and the golden tailings glass system also includes the high-order water being connected with spiral chute
Pond, the head-tank are also connected with the first mastic thickener and thickener respectively.
2. gold tailings glass system as claimed in claim 1, it is characterised in that：The spiral chute is for golden mine tailing is carried out
Again separate, and coarse granule ore pulp is supplied to into thickener, fine grained ore pulp is supplied to into the first mastic thickener.
3. gold tailings glass system as claimed in claim 1, it is characterised in that：The thickener is used for the coarse granule being introduced into
Ore pulp enters the separation of water-filling ore deposit.
4. gold tailings glass system as claimed in claim 1, it is characterised in that：The leaching adsorbent equipment is for valuable unit
Element is reclaimed.
5. gold tailings glass system as claimed in claim 1, it is characterised in that：The Paste-filling System is for by the second cream
The underflow of body thickener is backfilled.
6. a kind of golden tailings processing method, it is characterised in that：A kind of golden tailings glass system is provided, the golden tailings glass system is
Golden tailings glass system described in claim 1, its processing method are as follows：
First, golden mine tailing is entered by feeding mechanism；
2nd, golden mine tailing is separated again by spiral chute, after coarse granule ore pulp is reclaimed, is entered thickener, while will be thin
Granule ore pulp is introduced to the first mastic thickener and carries out mastic concentration, and the overflow water produced in concentration process enters head-tank,
Return again to spiral chute；
3rd, the underflow drawn by the first mastic thickener is backfilled into Paste-filling System；
4th, coarse granule ore pulp enters the separation of water-filling ore deposit by thickener, and its overflow water enters head-tank, returns again to spiral slip
Groove；
5th, tower grinding machine is entered by the underflow that thickener is drawn, fine grinding is carried out by tower grinding machine, the ore pulp after fine grinding enters to leach to be inhaled
Adsorption device carries out the recovery of the valuable elements such as gold, and its tailings carries out mastic concentration into the second mastic thickener, by the second mastic
The overflow water produced in thickener concentration process is back to tower grinding machine, and its underflow is backfilled into Paste-filling System.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610074307.5A CN105498952B (en) | 2016-02-02 | 2016-02-02 | Gold tailing processing system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610074307.5A CN105498952B (en) | 2016-02-02 | 2016-02-02 | Gold tailing processing system and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105498952A CN105498952A (en) | 2016-04-20 |
| CN105498952B true CN105498952B (en) | 2017-05-03 |
Family
ID=55707483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610074307.5A Active CN105498952B (en) | 2016-02-02 | 2016-02-02 | Gold tailing processing system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105498952B (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106223347B (en) * | 2016-08-15 | 2018-07-03 | 大连地拓环境科技有限公司 | A kind of method for extending the in-service Tailings Dam length of service |
| CN106285774A (en) * | 2016-08-15 | 2017-01-04 | 大连地拓重工有限公司 | A kind of cyanogen-containing tailing innoxious paste body filling method |
| CN106334621A (en) * | 2016-08-24 | 2017-01-18 | 大连地拓重工有限公司 | Beneficiation method for tailing-free pond |
| CN109701725B (en) * | 2019-01-16 | 2020-07-28 | 中冶北方（大连）工程技术有限公司 | Method for balancing underground tailing filling amount and tailing amount in mineral separation production |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4643059B2 (en) * | 2001-05-31 | 2011-03-02 | Ｊｘ日鉱日石金属株式会社 | Method of recovering metal from electronic / electric parts with resin |
| CN102600964B (en) * | 2012-03-15 | 2013-06-05 | 江西稀有金属钨业控股集团有限公司 | Method and system for recovering tailing resources |
| CN103816990B (en) * | 2014-02-19 | 2016-06-29 | 哈巴河金坝矿业有限公司 | A kind of gold flotation tailing comprehensive recovering process and device thereof |
| CN203916868U (en) * | 2014-06-14 | 2014-11-05 | 江西一元再生资源有限公司 | A kind ofly improve the ore-sorting system that slag gold recovery is soaked in arsenic-containing gold concentrate cyaniding |
| CN105080706B (en) * | 2015-08-18 | 2017-07-21 | 卯伟伟 | A kind of low grade gold ore recovery process |
-
2016
- 2016-02-02 CN CN201610074307.5A patent/CN105498952B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN105498952A (en) | 2016-04-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105498952B (en) | Gold tailing processing system and method | |
| CN101451192B (en) | Comprehensive recovery method for directly cyanating and intensified leaching multi-metal gold ore concentrate | |
| CN103555938B (en) | A kind of high flotation and metallurgy method containing mud copper oxide ore | |
| CN106378254A (en) | Method for removing magnetic impurities from tantalum-niobium waste ores by utilizing combined magnetic separation | |
| CN102228762A (en) | Dehydration method and device of tailings | |
| CN106242109A (en) | A kind of phosphorus ore direct reverse flotation produces waste water segmentation and utilizes technique | |
| CN103801450A (en) | Process for recovering tungsten from very low grade tungstenic tailings | |
| CN104846195A (en) | Method for recovering low-grade precious metal from mineral dressing tailings | |
| CN207119448U (en) | A kind of golden mine tailing pretreatment system | |
| CN103805775B (en) | Cupric low-grade gold resource comprehensive utilization process | |
| CN106636614A (en) | Method for leaching niobium, scandium and rare earth elements from tailings | |
| CN103480495B (en) | A kind of method selecting smelting to combine recovery copper cobalt from copper cobalt ore acidleach metallurgical slag | |
| CN104342186A (en) | Water washing separation method and water washing separation system for oil sand | |
| CN206965907U (en) | A kind of golden mine tailing haydite production system | |
| CN104745833B (en) | A kind of handling process for high golden paint ore | |
| CN104745811A (en) | Acid ore washing biological leaching process used for high mud alkaline uranium ore | |
| CN106669963A (en) | Pre-concentration method for ore separation of gold tailings | |
| CN109355498B (en) | Process method for recovering copper from low-grade copper oxide ore | |
| CN104607305A (en) | Niobium-zirconium ore mineral separation method | |
| CN106480311A (en) | A kind of Uranium extraction solid-liquid separation on ore pulp method | |
| CN206965906U (en) | A kind of iron tailings recycling treatment system | |
| CN104531987A (en) | Method for lowering leaching alkali consumption of alkaline uranium ore rich in gypsum | |
| CN104258977A (en) | Regrinding and rescreening method and device of gold floating tailings | |
| CN103157560B (en) | Flotation method of vulcanizing lead and zinc by weak acid full pulp | |
| CN103817011B (en) | A kind of carbonaceous thing inhibitor and the application in high charcoal molybdenum nickel minerals flotation molybdenum nickel thereof |
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 | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180105 Address after: Dalian high tech Industrial Park in Liaoning province 116023 Guang Xian Lu No. 133 building 21 room 2014, Cerberus Patentee after: Dalian Earth Environment Technology Co., Ltd. Address before: No. 16, revitalization Road, Bay Industrial Zone, Pu Wan New District, Dalian, Liaoning Patentee before: DALIAN DITUO HEAVY INDUSTRY CO., LTD. |
|
| TR01 | Transfer of patent right |