CN201823604U - Copper concentration production device utilizing flotation separation process - Google Patents
Copper concentration production device utilizing flotation separation process Download PDFInfo
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- CN201823604U CN201823604U CN2010205359376U CN201020535937U CN201823604U CN 201823604 U CN201823604 U CN 201823604U CN 2010205359376 U CN2010205359376 U CN 2010205359376U CN 201020535937 U CN201020535937 U CN 201020535937U CN 201823604 U CN201823604 U CN 201823604U
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- Prior art keywords
- separation
- tank
- copper concentration
- groove
- copper
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- 229910052802 copper Inorganic materials 0.000 title claims abstract description 55
- 239000010949 copper Substances 0.000 title claims abstract description 55
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 53
- 238000000926 separation method Methods 0.000 title claims abstract description 37
- 238000005188 flotation Methods 0.000 title claims abstract description 15
- 239000006260 foam Substances 0.000 claims abstract description 16
- 239000012141 concentrate Substances 0.000 claims description 41
- 238000011084 recovery Methods 0.000 abstract description 12
- 239000002184 metal Substances 0.000 abstract description 11
- 229910052751 metal Inorganic materials 0.000 abstract description 11
- 229910052725 zinc Inorganic materials 0.000 abstract description 7
- 239000011701 zinc Substances 0.000 abstract description 7
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 239000011133 lead Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 238000007667 floating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model relates to a device for separating metal from flowing liquid, in particular to a copper concentration production device utilizing the floatation separation process, which is capable of separating and producing copper concentration from polymetallic ore and aims to solve the technical problems of improving grade of copper concentration and increasing recovery rate of metal such as copper. The copper concentration production device comprises a first separation roughing tank, a second separation roughing tank, a third separation roughing tank, a fourth separation roughing tank, a fifth separation roughing tank, a separation concentrating tank and a copper concentration pump tank, wherein the separation concentrating tank is connected with the copper concentration pump tank via a concentration output pipe. The copper concentration production device is characterized in that a foam output pipe of the first separation roughing tank is connected with the copper concentration pump tank, foam output pipes of the second separation roughing tank, the third separation roughing tank, the fourth separation roughing tank and the fifth separation roughing tank are connected with a main output pipe, and an outlet of the main output pipe is connected with the separation concentrating tank. The copper concentration production device utilizing the flotation separation process improves grade of copper concentration by 2%, increases copper recovery rate by 1%, and increases lead recovery rate by 5% and zinc recovery rate by 5%, thereby achieving obvious economic and social benefits.
Description
Technical field the utility model relate to a kind of from working fluid the device of separating metal, particularly a kind of from the ore dressing of many metals the FLOTATION SEPARATION production of copper concentrate device of detached job output copper concentrate.
Background technology is present, for the polymetallic ore that contains these class original ore property complexity of multiple element such as Cu, Pb, Zn, S, Au, Ag, and the floating process using bulk flotation technology of ore-sorting system mill.In detached job, generally all adopt multiple-grooved to separate and roughly select the technology of foam through selected back output copper concentrate.In the ore-dressing technique of multi-metal complex sulfide ore, how to improve concentrate grade, it is the research direction that improves ore dressing plant technical indicator and economic benefit that the reduction concentrate contains mutually.
The applicant analyzes grade through long-term flow process examination separately to each flotation cell froth pulp of detached job and finds that it is best in quality that the first groove froth pulp is roughly selected in separation, is better than copper concentrate and other flotation cell froth pulps of selected operation output.From the examination result, separate and to roughly select the first groove foam cupric grade and be higher than the cleaner cell copper concentrate and contain copper grade, the former is generally of high grade about 3～4% than latter cupric, and leaded+zinc grade is low by about 4～6%, and the productive rate of roughly selecting the first groove foam cupric accounts for about 30% of whole copper concentrate productive rates.
Utility model content the technical problems to be solved in the utility model is to provide a kind of easy realization, improves the FLOTATION SEPARATION production of copper concentrate device of metal recovery rates such as copper concentrate grade and raising copper.
It is as follows that the utility model solves the problems of the technologies described above the technical scheme of taking: a kind of FLOTATION SEPARATION production of copper concentrate device, comprise separating and roughly select first groove, separate and roughly select second groove, separate and roughly select three-flute, separate and roughly select the 4th groove, separate and roughly select the 5th groove, separate cleaner cell and copper concentrate pump pond, separate cleaner cell and be connected with copper concentrate pump pond through the concentrate efferent duct; It is characterized in that: separate the foam efferent duct of roughly selecting first groove and be connected with copper concentrate pump pond; Separate and to roughly select second groove, separate and roughly select three-flute, separate and roughly select the 4th groove and separate the foam efferent duct of roughly selecting the 5th groove and be connected with delivery trunk, delivery trunk exports and separates cleaner cell and be connected.
The foam efferent duct that first groove is roughly selected in separation of the present utility model directly is connected with copper concentrate pump pond; Utilize in the polymetallic ore valuable metal and contain assorted high characteristics, separate the direct output copper concentrate of foam of roughly selecting first groove, improved the grade of copper concentrate on the one hand, metal recovery rates such as copper, lead, zinc have been improved on the other hand, not only simplified the subsequent technique of flotation, and shortened the flotation time of copper concentrate, prevent copper concentrate part loss in subsequent technique, and created the good condition that sorts for subsequent technique.
The utility model is roughly selected the first groove froth pulp to existing separation and is entered and separate the cleaner cell operation and change direct output copper concentrate into, can improve copper concentrate grade 2%, improve copper recovery 1%, improve lead recovery 0.5%, improve zinc recovery 0.5%, economic benefit and obvious social benefit.
Description of drawings Fig. 1 is a structural representation of the present utility model,
Fig. 2 is the structural representation of existing FLOTATION SEPARATION production of copper concentrate device.
Among the figure: the-groove is roughly selected in the 1-separation, and second groove is roughly selected in the 2-separation, and three-flute is roughly selected in the 3-separation, and the 4th groove is roughly selected in the 4-separation, the 5th groove is roughly selected in the 5-separation, and 6-separates cleaner cell, 7-copper concentrate pump pond, 8-concentrate efferent duct, the 9-first groove foam efferent duct, 10-delivery trunk, 11-mineral-feeding pipe.
The specific embodiment is as shown in Figure 2: a kind of FLOTATION SEPARATION production of copper concentrate device, comprise separating and roughly select first groove 1, separate and roughly select second groove 2, separate and roughly select three-flute 3, separate and roughly select the 4th groove 4, separate and roughly select the 5th groove 5, separate cleaner cell 6 and copper concentrate pump pond 7, separate cleaner cell 6 and be connected with copper concentrate pump pond 7 through concentrate efferent duct 8; Mineral-feeding pipe 11 is roughly selected first groove, 1 input raw ore to separation; Separating the first groove foam efferent duct 9 of roughly selecting first groove 1 is connected with copper concentrate pump pond 7; Separate and to roughly select second groove 2, separate and roughly select three-flute 3, separate and roughly select the 4th groove 4 and separate the foam efferent duct of roughly selecting the 5th groove 5 and be connected with delivery trunk 10, delivery trunk 10 exports and separates cleaner cell 6 and be connected.
The utility model is roughly selected the direct output copper concentrate of the first groove foam at detached job, has prevented copper concentrate part loss in subsequent technique, and has created the good condition that sorts for subsequent technique.
It is as follows to use the economic benefit estimation that the utility model brought:
Raw ore calculates according to copper grade 0.8%, plumbous grade 2.45%, zinc grade 4.05, handle the ore deposit amount year by 300,000 tons of calculating, metal price (5 years average prices) is 37350 yuan/ton by copper. metal, lead are 5405 yuan/ton. and metal, zinc is 5617 yuan/ton. metal calculates, and a year increase economic benefit is:
Copper recovery is increased the benefit: ten thousand yuan of 0.8% * 300000 * 1% * 37350=89.64
Lead recovery is increased the benefit: ten thousand yuan of 2.45% * 300000 * 0.5% * 5405=19.86
Lead recovery is increased the benefit: ten thousand yuan of 4.05% * 300000 * 0.5% * 5617=34.12
Increase by ten thousand yuan of economic total benefit: 89.64+19.86+34.12=143.12
And the structure of existing FLOTATION SEPARATION production of copper concentrate device as shown in Figure 1: separate and to roughly select first groove 1, separate and roughly select second groove 2, separate and roughly select three-flute 3, separate to roughly select the 4th groove 4 and separate the foam efferent duct of roughly selecting the 5th groove 5 and all is connected with delivery trunk 10, delivery trunk 10 exports and separates cleaner cell 6 and be connected; Separating cleaner cell 6 is connected with copper concentrate pump pond 7 through concentrate efferent duct 8.
Claims (1)
1. FLOTATION SEPARATION production of copper concentrate device, comprise separating and roughly select first groove, separate and roughly select second groove, separate and roughly select three-flute, separate and roughly select the 4th groove, separate and roughly select the 5th groove, separate cleaner cell and copper concentrate pump pond, separate cleaner cell and be connected with copper concentrate pump pond through the concentrate efferent duct; It is characterized in that: the first groove foam efferent duct (9) that first groove (1) is roughly selected in described separation is connected with described copper concentrate pump pond (7); Described separation roughly selects that second groove (2), described separation are roughly selected three-flute (3), described separation is roughly selected the 4th groove (4) and is connected with described delivery trunk (10) with the described foam efferent duct of roughly selecting the 5th groove (5) that separates, and described delivery trunk (10) outlet is connected with the described cleaner cell (6) that separates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205359376U CN201823604U (en) | 2010-09-17 | 2010-09-17 | Copper concentration production device utilizing flotation separation process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205359376U CN201823604U (en) | 2010-09-17 | 2010-09-17 | Copper concentration production device utilizing flotation separation process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201823604U true CN201823604U (en) | 2011-05-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205359376U Expired - Fee Related CN201823604U (en) | 2010-09-17 | 2010-09-17 | Copper concentration production device utilizing flotation separation process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201823604U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103433146A (en) * | 2013-08-20 | 2013-12-11 | 长沙有色冶金设计研究院有限公司 | Booze flotation method and system capable of improving rougher flotation effect |
| CN107597448A (en) * | 2017-10-25 | 2018-01-19 | 湖南水口山有色金属集团有限公司 | A kind of sorting process for improving the non-ferrous metal ore rate of recovery |
| CN110300628A (en) * | 2017-02-15 | 2019-10-01 | 奥图泰(芬兰)公司 | Flotation device, its use, equipment and method |
-
2010
- 2010-09-17 CN CN2010205359376U patent/CN201823604U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103433146A (en) * | 2013-08-20 | 2013-12-11 | 长沙有色冶金设计研究院有限公司 | Booze flotation method and system capable of improving rougher flotation effect |
| CN103433146B (en) * | 2013-08-20 | 2015-06-10 | 长沙有色冶金设计研究院有限公司 | Booze flotation method and system capable of improving rougher flotation effect |
| CN110300628A (en) * | 2017-02-15 | 2019-10-01 | 奥图泰(芬兰)公司 | Flotation device, its use, equipment and method |
| US11548013B2 (en) | 2017-02-15 | 2023-01-10 | Metso Outotec Finland Oy | Flotation arrangement, its use, a plant and a method |
| CN107597448A (en) * | 2017-10-25 | 2018-01-19 | 湖南水口山有色金属集团有限公司 | A kind of sorting process for improving the non-ferrous metal ore rate of recovery |
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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: 20110511 Termination date: 20130917 |