CN203304062U - Device for automatic beneficiation by gravity - Google Patents
Device for automatic beneficiation by gravity Download PDFInfo
- Publication number
- CN203304062U CN203304062U CN2013203471479U CN201320347147U CN203304062U CN 203304062 U CN203304062 U CN 203304062U CN 2013203471479 U CN2013203471479 U CN 2013203471479U CN 201320347147 U CN201320347147 U CN 201320347147U CN 203304062 U CN203304062 U CN 203304062U
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- CN
- China
- Prior art keywords
- ore
- tilting section
- ore discharge
- chute
- concentrate
- 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
- 230000005484 gravity Effects 0.000 title claims abstract description 14
- 239000012141 concentrate Substances 0.000 claims abstract description 26
- 238000011010 flushing procedure Methods 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 241000209094 Oryza Species 0.000 claims description 4
- 235000007164 Oryza sativa Nutrition 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 235000009566 rice Nutrition 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 13
- 239000011707 mineral Substances 0.000 abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000004033 plastic Substances 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 241000196324 Embryophyta Species 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000004568 cement Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
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Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The utility model discloses a device for automatic beneficiation by gravity. A concentrate discharge tube, a tailings discharge tube and an ore discharge inserting tube are arranged at the ore discharge end of a chute; the concentrate discharge tube is communicated with a concentrate groove; the tailings discharge tube is communicated with a tailings groove; the chute orderly comprises a first inclination section and a second inclination section which is joined with the first inclination section from the ore supply end to the ore discharge end; the width of the second inclination section is reduced along the ore discharge direction; the slope of the second inclination section is greater than that of the first inclination section; ore discharge protecting plates are respectively arranged at two transverse sides of the first inclination section and the second inclination section; dredge change-over plugs are arranged on the concentrate discharge tube and the tailings discharge tube. The device disclosed by the utility model is convenient to maintain and simple to operate; the comprehensive utilization rate of mineral resources can be improved.
Description
Technical field
The utility model relates to a kind of by the device of gravity automatic ore dressing, belongs to the technique of preparing field.
Background technology
The main beneficiation method in the heavy metal mines such as now a lot of tungsten, tin is gravity separation, the main gravity beneficiation equipment adopted is jigging machine, shaking table, spiral concentrator, centrifugal ore separator etc., different in kind according to ore, its recovery rate in ore-dressing is greatly about the 65-80% left and right, and the metal loss major part in this class mill tailings concentrates in the fine fraction product.
According to comprehensive utilization of resources and energy-saving and cost-reducing needs, wish the loss metal recovery in mill tailings is recycled.
The utility model content
The purpose of this utility model is to provide a kind of by the device of gravity automatic ore dressing, and it is easy to maintenance, side is simple to operate, can improve the mineral resources comprehensive utilization rate.
For this reason; it is a kind of by the device of gravity automatic ore dressing that the utility model provides; this device comprises the enrichment conical surface of mineral-feeding pipe, mine distributor and mine distributor below of chute, flannelette blanket concentrate hopper, the inclination of flushing type hydrocyclone, feed launder, at least one inclination successively, it is characterized in that: each chute to the ore deposit end be provided with a total feed launder and mineral-feeding pipe, minute ore deposit groove and a plurality of side by side divide pipe; Mine-discharging terminal at chute is provided with concentrate ore discharge pipe, mine tailing ore discharge pipe and ore discharge intubate, and concentrate ore discharge pipe is communicated with the concentrate ditch, and mine tailing ore discharge pipe is communicated with the mine tailing ditch; Chute is from comprising successively the first tilting section and the second tilting section be connected with the first tilting section to the ore deposit end to mine-discharging terminal, and the width of the second tilting section dwindles along the ore discharge direction, and the gradient of the second tilting section is greater than the gradient of the first tilting section; The horizontal both sides of the first tilting section and the second tilting section are respectively equipped with the ore discharge backplate; Concentrate ore discharge pipe and mine tailing ore discharge pipe are provided with opens the conversion plug.
Preferably, described flushing type hydrocyclone comprises sieve-board type classification case and the hydrocyclone of mutual linking from top to bottom successively, hydrocyclone is provided with the mineral-feeding pipe be communicated with the hydrocyclone inner chamber in its tangential direction, above this mineral-feeding pipe, be provided with the ore pulp overflow pipe, ore pulp overflow pipe opening up; Sieve-board type classification case is back taper, foot be provided with sieve plate and below developing room, the side of this developing room is provided with high-pressure intake pipe, below is provided with the ore discharge pipe.
Preferably, the quantity of chute is 2-8, and width is 0.8 meter, and length is 10 meters.
Preferably, the gradient of the first tilting section of chute is 9-11%, and the gradient of the second tilting section (36) is 20-30%.
Preferably, the gradient of the enrichment conical surface is between the 24-27 degree.
Preferably, the described conversion plug opened is intubate, and the external diameter of this intubate is less than or equal to the internal diameter of concentrate ore discharge pipe and mine tailing ore discharge pipe.
Preferably, mine distributor is the conical galvanized iron sheet of thickness 0.5mm, and the diameter of mine distributor bottom circumference is 0.52-0.55 rice, and cone angle is controlled at the 34-37 degree, and the above is evenly equipped with 10-20 bar involute groove.
Preferably, the groove that the taper seat that the described enrichment conical surface is mongolia yurt type, polygonal pyramid face, hemisphere face or spirality descend, consist of cement;
Preferably, the situation lower bottom part circle diameter that is the yurt shape is controlled at 2.8-3.1 rice.
The beneficial effects of the utility model are: the comprehensive utilization ratio of unpowered raising mineral resources, facts have proved, and comprehensive recovery can improve 5-8%.
The accompanying drawing explanation
Fig. 1 is the schematic diagram according to Unpowered gravity ore-dressing plant of the present utility model;
Fig. 2 is device floor map as shown in Figure 1;
Fig. 3 is the enrichment conical surface schematic diagram in device as shown in Figure 1;
Fig. 4 is the structure schematic top plan view according to flannelette blanket formula chute of the present utility model and two ends thereof;
Fig. 5 is the structure schematic side view according to flannelette blanket formula chute of the present utility model and two ends thereof;
Fig. 6 is the side-looking structural representation according to flushing type hydrocyclone of the present utility model; With
Fig. 7 is the plan structure schematic diagram according to flushing type hydrocyclone of the present utility model.
Specific embodiment
Below in conjunction with specific embodiment, further set forth the technical solution of the utility model.
In accompanying drawing 1-3, Reference numeral 1 means that flushing type hydrocyclone, Reference numeral 2 mean that feed launder, Reference numeral 3 mean that flannelette blanket formula chute, Reference numeral 4 mean that flannelette blanket concentrate hopper, Reference numeral 5 mean that mineral-feeding pipe, Reference numeral 6 mean that mine distributor, Reference numeral 7 mean the enrichment conical surface (being commonly called as yurt).
As shown in Figure 1, enforcement comprises the steps: that according to the method for Unpowered gravity ore dressing of the present utility model the mine tailing in ore dressing plant is through 1 classification of Simple flushing formula hydrocyclone, overflow after classification is given to ore pulp respectively in the chute 3 of certain slope and width through feed launder 2, the surface of chute 3 is covered with one deck flannelette blanket, ore pulp forms the film that slips of uniform and stable on the surface of flannelette blanket, poor according to the sinking speed that the density variation of different minerals causes, the heavy mineral preferential deposition is in the fine hair formula gap of flannelette blanket, gangue mineral is along with flow of slurry is brought in mine tailing, like this after enrichment after a while, stop to ore deposit, the heavy mineral that adopts water under high pressure will be attached on flannelette blanket is flushed in flannelette blanket concentrate hopper 4, ore deposit is given in flushing again after finishing, so go round and begin again.
The heavy mineral rough concentrate of flannelette blanket output adds water move to certain pulp density, through mineral-feeding pipe 5, evenly be given in the mine distributor on the enrichment conical surface 7 (yurt) in 6, mine distributor is fast rotational under the impact of flow of slurry, simultaneously ore pulp evenly is sprinkling upon on the yurt 7 of cement, on the slope of yurt 7, form moisture film, heavy mineral is attached to the slope (smooth taper cement surface) of yurt 7, and gangue is domatic away from the slope of yurt 7.After enrichment after a while, stop to ore deposit, in one embodiment, the time of enrichment, on the slope of yurt 7, high-grade heavy mineral concentrate product in enrichment generally at 30-40 minute.
In one embodiment, the concentration that the heavy mineral in flannelette blanket concentrate hopper 4 is added to the secondary ore pulp that water concocting becomes is 10-12%; The pressure 2-3kg/cm of high-pressure washing water
2, the quantity of chute will be determined according to disposal ability, 10 meters of general flute length, wide 0.8 meter, the chute of gradient 9-11% disposal ability hourly per hour is about 1-1.5 ton (dry ore deposit amount), and after needing ore deposit to be processed amount to determine, the quantity of chute has also just calculated.The slope control of " yurt " is between 24 to 27 degree, and yurt bottom circle diameter is controlled at 3 meters left and right, and at the bottom of mine distributor, circular diameter is controlled at 0.54 meter left and right, and cone angle is controlled at 35 degree left and right.
As Figure 2-3, in the device of Unpowered gravity ore dressing of the present utility model, the parameter of " yurt " is as follows: d
1=130mm, H=891mm, h
1=100mm, h
2=400mm, h
3=267mm, D
1=3000mm, D
2=4500mm, D
3=4800mm, D
4=5200mm, D
5=5500mm.
In the device according to Unpowered gravity ore dressing of the present utility model, designed the mine distributor on a kind of flannelette blanket formula chute, yurt and yurt.After the mine tailing in ore dressing plant is carried out to classification, overflow flows into flannelette blanket formula chute automatically, through flannelette blanket formula chute, roughly select enrichment, to improve the grade of product, the rough concentrate of flannelette blanket formula chute feeds the mine distributor on yurt (the enrichment conical surface), and on mine distributor 20 gradually are recessed at fast rotational under the dynamic action of current (being flow of slurry), ore pulp are evenly spread on the slope of yurt, heavy mineral is enrichment again on slope, and the grade of product is further improved.
According to the utility model, if necessary, further yurt, like this, through the enrichment of two to three times, just can obtain the product requirement of final sales.
As shown in Fig. 4-5, in an embodiment of the present utility model, woollen blanket chute 3 to ore deposit end 12, be provided with feed launder 23 and DN80 plastics mineral-feeding pipe 11, minute ore deposit groove 24 and DN20 plastics divide pipe 10, can make mine-supplying quantity evenly be covered with whole groove 3 surfaces, be conducive to the sorting of weight mineral.
In addition on the one hand, the utility model is provided with DN80 plastics concentrate ore discharge pipe 31, DN80 plastics mine tailing ore discharge pipe 32 and DN65 plastics ore discharge intubate 33 at the mine-discharging terminal 34 of woollen blanket chute 3, operating personnel can discharge concentrate to concentrate ditch 41 by the position of adjusting intubate 33 very easily easily, discharge mine tailing to mine tailing ditch 42.
The utility model adopts the high pressure water washing flannelette blanket, has saved the operation of " put-down blanket, wash flannelette blanket and flocking blanket " of the prior art, greatly reduces employee's labour intensity.
The utility model is provided with " flushing type waterpower revolve slip device classification ", can improve the recovering effect of flannelette blanket.
As shown in Fig. 6-7, " flushing type hydrocyclone " also claims " flushing type waterpower revolve slip device " to comprise sieve-board type classification case 100 and hydrocyclone 101, can be welded also and can be built into common brick with iron plate.
The mine tailing in ore dressing plant is raised the mineral-feeding pipe 102 (for example selecting DN200) of delivering to the tangential direction that is arranged on hydrocyclone 101 by sand pump, thereby feeds in hydrocyclone 101.Because ore pulp has certain pressure and flow velocity, in mine tailing the coarse fraction tailings under centrifugal force and Action of Gravity Field wall 103 spirals along cyclone 101 move downward, when the sieve plate 105 on developing room 104 tops that approach the cone end, again under the flushing action of the water under high pressure in high-pressure intake pipe 106, only have the coarse granule tailings just can overcome the effect of ascending current and enter ore discharge pipe 107 and discharge.Remaining fine grained tailings, under the effect of ascending current, moves upward, and for example, from ore pulp overflow pipe 108 (selecting DN150), discharging, and enter blanket sluice 3, carries out ore-dressing practice, thereby has completed classification process.
Claims (9)
1. one kind is passed through the device of gravity automatic ore dressing, this device comprises the enrichment conical surface (7) of the chute (3), flannelette blanket concentrate hopper (4) of flushing type hydrocyclone (1), feed launder (2), at least one inclination, the mineral-feeding pipe (5) tilted, mine distributor (6) and mine distributor (6) below successively, it is characterized in that: each chute (3) to ore deposit end (12) be provided with a total feed launder (23) and mineral-feeding pipe (11), minute ore deposit groove (24) and a plurality of side by side divide pipe (10); Mine-discharging terminal (34) in chute (3) is provided with concentrate ore discharge pipe (31), mine tailing ore discharge pipe (32) and ore discharge intubate (33), concentrate ore discharge pipe (31) is communicated with concentrate ditch (41), and mine tailing ore discharge pipe (32) is communicated with mine tailing ditch (42); Chute (3) is from comprising successively the first tilting section (35) and the second tilting section (36) be connected with the first tilting section (35) to ore deposit end (12) to mine-discharging terminal (34); the width of the second tilting section (36) dwindles along the ore discharge direction, and the gradient of the second tilting section (36) is greater than the gradient of the first tilting section (35); The horizontal both sides of the first tilting section (35) and the second tilting section (36) are respectively equipped with ore discharge backplate (35 ', 36 '); Concentrate ore discharge pipe (31) and mine tailing ore discharge pipe (32) are provided with opens the conversion plug.
2. device according to claim 1, it is characterized in that: described flushing type hydrocyclone comprises sieve-board type classification case and the hydrocyclone of mutual linking from top to bottom successively, hydrocyclone is provided with the mineral-feeding pipe be communicated with the hydrocyclone inner chamber in its tangential direction, above this mineral-feeding pipe, be provided with the ore pulp overflow pipe, ore pulp overflow pipe opening up; Sieve-board type classification case is back taper, foot be provided with sieve plate and below developing room, the side of this developing room is provided with high-pressure intake pipe, below is provided with the ore discharge pipe.
3. device according to claim 1 is characterized in that: the quantity of chute (3) is 2-8, and width is 0.8 meter, and length is 10 meters.
4. according to the described device of claim 1 or 3, it is characterized in that: the gradient of first tilting section (35) of chute (3) is 9-11%, and the gradient of the second tilting section (36) is 20-30%.
5. device according to claim 1, it is characterized in that: the gradient of the enrichment conical surface is between the 24-27 degree.
6. device according to claim 1 is characterized in that: described to open the conversion plug be intubate (33), and the external diameter of this intubate (33) is less than or equal to the internal diameter of concentrate ore discharge pipe (31) and mine tailing ore discharge pipe (32).
7. device according to claim 1, it is characterized in that: mine distributor (6) is the conical galvanized iron sheet of thickness 0.5mm, the diameter of mine distributor (6) bottom circumference is 0.52-0.55 rice, and cone angle is controlled at the 34-37 degree, and the above is evenly equipped with 10-20 bar involute groove.
8. device according to claim 1, is characterized in that: the groove that the taper seat that the described enrichment conical surface is mongolia yurt type, polygonal pyramid face, hemisphere face or spirality descend.
9. device according to claim 8, it is characterized in that: the situation lower bottom part circle diameter that is the yurt shape is 2.8-3.1 rice.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2013203471479U CN203304062U (en) | 2013-06-18 | 2013-06-18 | Device for automatic beneficiation by gravity |
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CN2013203471479U CN203304062U (en) | 2013-06-18 | 2013-06-18 | Device for automatic beneficiation by gravity |
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CN203304062U true CN203304062U (en) | 2013-11-27 |
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CN2013203471479U Expired - Fee Related CN203304062U (en) | 2013-06-18 | 2013-06-18 | Device for automatic beneficiation by gravity |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103657824A (en) * | 2013-12-16 | 2014-03-26 | 裴寿益 | Ore grinding method |
CN105921254A (en) * | 2016-06-22 | 2016-09-07 | 江西稀有稀土金属钨业集团有限公司 | Full-automatic tailing pile blanket recycling device |
-
2013
- 2013-06-18 CN CN2013203471479U patent/CN203304062U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103657824A (en) * | 2013-12-16 | 2014-03-26 | 裴寿益 | Ore grinding method |
CN105921254A (en) * | 2016-06-22 | 2016-09-07 | 江西稀有稀土金属钨业集团有限公司 | Full-automatic tailing pile blanket recycling device |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20131127 |
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CU01 | Correction of utility model | ||
CU01 | Correction of utility model |
Correction item: Termination upon expiration of patent Correct: Revocation of Patent Expiration and Termination False: On July 4, 2023, the expiration and termination of the 39 volume 2701 patent Number: 27-01 Volume: 39 |
|
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131127 |