CN2512508Y - Nickel tailings recovery device - Google Patents
Nickel tailings recovery device Download PDFInfo
- Publication number
- CN2512508Y CN2512508Y CN 01272074 CN01272074U CN2512508Y CN 2512508 Y CN2512508 Y CN 2512508Y CN 01272074 CN01272074 CN 01272074 CN 01272074 U CN01272074 U CN 01272074U CN 2512508 Y CN2512508 Y CN 2512508Y
- Authority
- CN
- China
- Prior art keywords
- sent
- concentrate
- pipeline
- slush pump
- chats
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model relates to a nickel tailings recovery device. Original ore slurry are sent into the sixteen Phi1200 quadruple screw downspoutings by 130m<3> per hour ore slurry pump, the screw downspoutings respectively get the gangues, the middling products and the ore concentrates, the gangues are discharged out by 130m<3> per hour ore slurry pump, the middling products are turned back to the original ore slurry by pipelines and the ore concentrates are sent into the six 1200 quadruple screw downspoutings by 40m<3> per hour ore slurry pump; the screw downspoutings respectively get the gangues, the middling products and the ore concentrates, the gangues are discharged out by 130 m<3> per hour ore slurry pump, the middling products are turned back to a first choosing pipeline by pipelines and the ore concentrates are sent into third choosing four Phi1200 quadruple screw downspoutings by 40m<3> per hour ore slurry pump, the screw downspoutings respectively get the gangues; the middling products and the ore concentrates, the middling products are sent to a second choosing pipeline by a pipeline 14, and the ore concentrates are discharged out by 15 m<3> per hour ore slurry pump. The utility model is characterized in reasonable design and high efficiency of the reclaimed nickel tailings and can reclaim the nickel concentrate with 3.26 to 3.4 percent.
Description
The utility model relates to a kind of refinement of nickel, particularly a kind of nickel mine tailing retracting device.At present, since nickel minerals is produced, nickeliferous 0.3% nickel mine tailing has been thought that therefore a large amount of for a long time nickel mine tailings are heaped, and cause the wasting of resources and environmental pollution without any utilizing the value of exploitation again.For addressing this problem, the utility model has designed a kind of nickel mine tailing retracting device, the reasonable use spiral chute, the particular processing technical process, recyclable nickel reaches 3.26～3.4% the smart powder of nickel, make the nickel mine tailing obtain abundant recovery, effectively utilized resource, solved environmental issue simultaneously again.
The technical solution of the utility model is: nickel mine tailing retracting device is to adopt to pass through 130m
3/ h slush pump is sent into raw ore slurry in 16 Φ, the 1200 four-start spiral chutes, and spiral chute obtains mine tailing, chats and concentrate respectively by sorting, and mine tailing passes through 130m
3/ h slush pump is discharged, and chats returns raw ore slurry by pipeline, and concentrate passes through 40m
3/ h slush pump is sent in 6 Φ, the 1200 four-start spiral chutes, and spiral chute obtains mine tailing, chats and concentrate respectively by sorting, and mine tailing passes through 130m
3/ h slush pump is discharged, and chats turns back to a concentrate selection pipeline by pipeline, and concentrate passes through 40m
3/ h slush pump is sent into three and is selected in 4 Φ, the 1200 four-start spiral chutes, and spiral chute obtains chats, concentrate respectively by sorting, and chats is sent into the two concentrate pipelines that select by pipeline, by 40m
3/ h slush pump is sent in the big mine distributor of three choosings, carries out final election again, the concentrate of resultant 3.26-3.4%, and concentrate passes through 15m
3/ h slush pump is discharged.
60M
3/ h clarified water pump 17 is connected on each slush pump by the pipeline connection, is used for making subsidy water to each slush pump and uses.
The equipment that the utlity model has is reasonable in design, reclaims the high characteristics of nickel mine tailing rate, and recyclable nickel reaches 3.26～3.4% the smart powder of nickel, makes the nickel mine tailing obtain abundant recovery, has effectively utilized resource, has solved environmental issue simultaneously again.
Concrete structure of the present utility model and embodiment are provided by the following drawings.
What accompanying drawing was given is general structure schematic diagram of the present utility model.
Below in conjunction with accompanying drawing concrete structure of the present utility model and embodiment are described further.
Embodiment
See shown in the accompanying drawing: nickel mine tailing retracting device is to adopt to pass through 130m
3/ h slush pump 1 is sent raw ore slurry into big mine distributor 2, big mine distributor 2 is sent to 4,16 feed boxs 4 of 16 feed boxs again by pipeline 3 and respectively raw ore slurry is sent in 16 Φ, the 1200 four-start spiral chutes 5, and spiral chute 5 is by sorting, obtain mine tailing, chats and concentrate respectively, mine tailing passes through 130m
3/ h slush pump 16 is discharged, and chats returns raw ore slurry by pipeline 6, by 130m
3/ h slush pump 1 is sent into big mine distributor 2, carries out final election again, and concentrate passes through 40m
3/ h slush pump 7 is sent to two and selects big mine distributor 8, big mine distributor 8 is sent into 4,6 feed boxs 4 of 6 feed boxs respectively by pipeline 9 concentrate is sent in 6 Φ, the 1200 four-start spiral chutes 5, and spiral chute 5 is by sorting, obtain mine tailing, chats and concentrate respectively, mine tailing passes through 130m
3/ h slush pump 16 is discharged, and chats turns back to a concentrate selection pipeline by pipeline 19, by 40m
3/ h slush pump 7 is sent into two and is selected big mine distributor 8, carries out final election again, and concentrate passes through 40m
3/ h slush pump 11 is sent into three and is selected big mine distributor 12, big mine distributor 12 is sent into 4 feed boxs 4 respectively by pipeline 13,4 feed boxs 4 are sent into concentrate in 4 Φ, the 1200 four-start spiral chutes 5, spiral chute 5 is by sorting, obtain chats, concentrate respectively, chats is sent into the two concentrate pipelines that select by pipeline 14, by 40m
3/ h slush pump 11 send into three the choosing big mine distributors in 12, carry out final election again, obtain the concentrate of 3.26-3.4%, concentrate passes through 15m
3/ h slush pump 15 is discharged.
60M
3/ h clarified water pump 17 connects slush pump 1,7,11,15,16 by pipeline, is used for making subsidy water to each slush pump and uses.
Claims (1)
1, a kind of nickel mine tailing retracting device is characterized in that: pass through 130m
3/ h slush pump (1) is sent raw ore slurry into big mine distributor (2), big mine distributor (2) is sent to 16 feed boxs (4) again by pipeline (3), 16 feed boxs (4) are sent into raw ore slurry respectively in 16 Φ, the 1200 four-start spiral chutes (5), spiral chute (5) is by sorting, obtain mine tailing, chats and concentrate respectively, mine tailing passes through 130m
3/ h slush pump (16) is discharged, and chats returns raw ore slurry by pipeline (6), by 130m
3/ h slush pump (1) is sent into big mine distributor (2), and concentrate passes through 40m
3/ h slush pump (7) is sent to two and selects big mine distributor (8), big mine distributor (8) is sent into 6 feed boxs 4 respectively by pipeline (9), 6 feed boxs 4 are sent into concentrate in 6 Φ, the 1200 four-start spiral chutes (5), spiral chute (5) is by sorting, obtain mine tailing, chats and concentrate respectively, mine tailing passes through 130m
3/ h slush pump (16) is discharged, and chats turns back to a concentrate selection pipeline by pipeline (19), by 40m
3/ h slush pump (7) is sent into two and is selected big mine distributor (8), and concentrate passes through 40m
3/ h slush pump (11) is sent into three and is selected big mine distributor (12), big mine distributor (12) is sent into 4 feed boxs 4 respectively by pipeline (13), 4 feed boxs 4 are sent into concentrate in 4 Φ, the 1200 four-start spiral chutes (5), spiral chute (5) is by sorting, obtain chats, concentrate respectively, chats is sent into the two concentrate pipelines that select by pipeline (14), by 40m
3/ h slush pump (11) is sent into the big mine distributor (12) of three choosings, and concentrate passes through 15m
3/ h slush pump (15) is discharged, 60M
3/ h clarified water pump (17) connects slush pump (1), (7), (11), (15), (16) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01272074 CN2512508Y (en) | 2001-12-10 | 2001-12-10 | Nickel tailings recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01272074 CN2512508Y (en) | 2001-12-10 | 2001-12-10 | Nickel tailings recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2512508Y true CN2512508Y (en) | 2002-09-25 |
Family
ID=33677330
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01272074 Expired - Fee Related CN2512508Y (en) | 2001-12-10 | 2001-12-10 | Nickel tailings recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2512508Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527496A (en) * | 2011-12-13 | 2012-07-04 | 江西稀有稀土金属钨业集团有限公司 | System and method for power-free gravity mineral separation |
| CN103586125A (en) * | 2012-08-15 | 2014-02-19 | 临沂鲁兴钛业股份有限公司 | Tailing titanium selecting method through gravity |
-
2001
- 2001-12-10 CN CN 01272074 patent/CN2512508Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102527496A (en) * | 2011-12-13 | 2012-07-04 | 江西稀有稀土金属钨业集团有限公司 | System and method for power-free gravity mineral separation |
| CN102527496B (en) * | 2011-12-13 | 2015-05-20 | 江西稀有稀土金属钨业集团有限公司 | System and method for power-free gravity mineral separation |
| CN103586125A (en) * | 2012-08-15 | 2014-02-19 | 临沂鲁兴钛业股份有限公司 | Tailing titanium selecting method through gravity |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104888947B (en) | The magnetic separation of fine grain teeth cloth magnetic-red composite ore-centrifuge sorting process | |
| CN103567051B (en) | Small-scale lean hematite separation technology | |
| CN103071596B (en) | Method for recycling fine and superfine cassiterites from oxidized lode tin mud tailings | |
| CN101985113B (en) | Beneficiation method for copper nickel sulfide ore | |
| CN101850295A (en) | Beneficiation method for producing high-quality iron ore concentrate by low-grade magnetic iron ore | |
| CN102962123B (en) | Beneficiation process for low-grade copper-nickel ore | |
| CN103350027A (en) | Classified-desliming pressurized-feeding three-product dense medium cyclone coal preparation process | |
| CN104874459A (en) | Low-grade magnetite pre-selection and waste abandoning mineral separation process | |
| CN203061257U (en) | Production device for making sand by using river gravel | |
| CN203565193U (en) | Multifunctional sandstone mining device | |
| CN103381389A (en) | Production technology for improving secondary recovery rate of tailings | |
| CN105013603A (en) | Copper-nickel sulfide ore mineral separation method | |
| CN102764690A (en) | Separation method for treating low-grade refractory zinc lead oxide ores | |
| CN205323969U (en) | From selecting equipment of retrieving low -grade marmatite and tin quarry thing in copper tailing | |
| CN101612618A (en) | Process for discarding coarse tailings with primary sand return for ultralean magnetite ores | |
| CN103894283B (en) | A kind of ore-dressing technique of iron content height silicate-type iron ore | |
| CN201153145Y (en) | Separating and selecting apparatus used after crushing waste lead accumulators | |
| CN102430465B (en) | Method for selecting zinc oxide from muddy zinc oxide fine ore grains | |
| CN201543596U (en) | Copper scrap sorting device | |
| CN2512508Y (en) | Nickel tailings recovery device | |
| CN104785360A (en) | Dense medium separation method for recycling coarse fraction apatite from magnetite tailings | |
| CN105665124A (en) | High-intergrowth, high-ash and high-sulfur coal sorting and slurrying integrated process | |
| CN103447147B (en) | Novel low grade hematite ore concentration and water purification process | |
| CN104148187A (en) | Ore selection method for treating tin, lead and zinc polymetallic oxidized ore | |
| CN202516628U (en) | Ore sorting equipment |
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: 20020925 Termination date: 20100111 |