CN103691546A - Coarse coal slime sorting machine - Google Patents
Coarse coal slime sorting machine Download PDFInfo
- Publication number
- CN103691546A CN103691546A CN201310702163.XA CN201310702163A CN103691546A CN 103691546 A CN103691546 A CN 103691546A CN 201310702163 A CN201310702163 A CN 201310702163A CN 103691546 A CN103691546 A CN 103691546A
- Authority
- CN
- China
- Prior art keywords
- shunting
- cylindrical shell
- platform
- rotating shaft
- feeding
- 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.)
- Pending
Links
Images
Landscapes
- Centrifugal Separators (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The invention discloses a coarse coal slime sorting machine. The coarse coal slime sorting machine comprises a main engine barrel body, a platform, an electric actuator, a water tank, a water tank spraying device, a feeding bottom interfering device, a feeding device, a top cover, an overflow weir plate and a lower conical body, and is characterized in that a tapered diffusion platform is arranged on the upper end of the lower conical body; the big-diameter end of the tapered diffusion platform is fixedly connected to the lower conical body while the small-diameter end thereof corresponds to an outlet of a feeding barrel body and is in clearance fit with the feeding barrel body, so that a material is benefited to be diffused in an umbrella-shaped manner automatically along the periphery of the tapered diffusion platform without increasing a feeding pressure, and the diffused material is mixed with rising water flow sprayed by the water tank to generate a turbulent flow. The coarse coal slime sorting machine has the advantages of a novel structure, high sorting efficiency, no need of increasing the feeding pressure, low water content of the material when being discharged, high solid content, remarkable sorting effect, production cost reduction, process cost reduction and the like.
Description
Technical field
The present invention relates to colliery mechanical equipment technical field, specifically a kind of separation of coarse slime machine.
Background technology
As everyone knows, existing separation of coarse slime machine is that a kind of turbulent flow disturbs sink and emerge type separator, through retrieval, CN202700634 discloses a kind of utility model patent of separation of coarse slime machine, it comprises main frame cylindrical shell, platform, YE, water tank, water tank injection apparatus, pan feeding bottom countermeasure set, feeding device, top cover, overflow weir and hypocentrum, described a kind of separation of coarse slime machine, it is characterized in that: comprise cylindrical shell, differential adjustable downflow weir, feeding device, cone valve black box, YE, water tank and observation platform, the bottom of its middle cylinder body is provided with water tank, upper end is provided with differential adjustable downflow weir, the top of described differential adjustable downflow weir is provided with observation platform, the upper end of described cone valve black box is connected with YE by the support arm being arranged on observation platform, lower end is connected with the mine tailing exit seal that is arranged at cylinder body bottom, the inside of described cylindrical shell is provided with feeding device, described differential adjustable downflow weir comprises coaming plate, dividing plate and coaming plate support, wherein coaming plate is arranged at the inside of described cylindrical shell, and by a plurality of coaming plate supports, hang on the edge, upper end of cylindrical shell, the upper edge of described coaming plate is higher than the upper edge of cylindrical shell, the outer surface of described coaming plate is provided with a plurality of dividing plates that make to keep between coaming plate and cylindrical shell gap, described feeding device comprises feeding pipe for hindering the loose adjustable feeding device of formula, the loose arc plate of resistance and the loose arc board mount of resistance, wherein the upper end of feeding pipe is connected with observation platform, lower end is placed in cylindrical shell, the loose arc plate of described resistance is connected with the newel that is arranged on cylinder body bottom by hindering loose arc board mount, the lower port of the loose arc plate of described resistance and feeding pipe is corresponding and leave distance, the lower end of described feeding pipe is provided with by sliding up and down to adjust the lower port and the moving casing that hinders loose arc distance between plates of feeding pipe, on the tube wall of described moving casing, be provided with vertically bar shaped gap, at this bar shaped opening position, by screw bolt and nut, moving casing is fixedly connected with the lower end of feeding pipe, described cone valve black box adopts cone valve air tightness compensation arrangement to comprise pull bar, screw rod, Compress Spring, spring base, spring spool, nut and cone valve, wherein cone valve is connected with the valve base sealing of described cylinder body bottom mine tailing outlet, the upper end of described cone valve is connected with one end of pull bar, the other end of described pull bar is connected with one end of screw rod, another end of thread of described screw rod is through described support arm, and with described support arm can relative sliding, on another end of thread of described screw rod, the both sides up and down of described support arm are respectively equipped with positioning and locking nut, between the upside nut of described support arm and described support arm, be provided with successively from bottom to up spring base, Compress Spring and spring spool, the outer surface of described coaming plate is provided with the steady pin of a plurality of differing heights vertically, the steady pin of described a plurality of differing heights is many groups, and be distributed on the circumferencial direction of described coaming plate, the steady pin of described coaming plate by arbitrary height inserts the jack of offering on described coaming plate support and is connected with coaming plate support, between described coaming plate support and coaming plate, form gap, gap is stuck in to the upper along upper of cylindrical shell.It utilizes bottom water tank to eject the ascending current with certain pressure, in cylindrical shell, form sink and emerge type sorting turbulent and that carry out with the material flowing in cylindrical shell, material forms eddy flow under the effect of feeding device, and inject cylindrical shell, simultaneously, the rising mouth of a river six is ejected in cylindrical shell by the turbulent valve opening of pressure water tank turbulence plate with certain pressure and flow velocity uniformly, material forms the bed being comprised of the different suspended particulate of density under the effect of injection water, density is large is deposited in the bottom, the responsible upper strata that density is little, and flow out through the spout hole of cylindrical shell upper end, when the large spoil impurity sedimentation of density is in bottom and be stacked into the density detection timing of implanting in cylinder, its pressure has surpassed the controlling value density detection meter of setting and has outputed signal to PLC controller, PLC controller transfer instruction is to YE, by YE, open the cone valve in sealing state, the spoil impurity that is deposited in bottom is discharged from bed material mouth.After spoil impurity is discharged, the bed that bottom density is large declines, and material is reduced the pressure of surveymeter, and the density value of its output is less than setting value, PLC controller is that Sung Dynasty Village signal is to YE, and close cone valve, and reciprocal thus, make sorting in poised state, its deficiency is when feed pressure is not enough, material is easily deposited on the loose arc plate of resistance, makes the density that hinders loose arc plate periphery material be greater than the density that hinders loose arc plate peripheral space, causes separating effect undesirable.
The technical problem occurring in order to solve above-mentioned patent, CN103418487 discloses a kind of application for a patent for invention of separation of coarse slime machine, although this technical scheme arranges eddy flow countermeasure set on resistance is fallen apart, this eddy flow countermeasure set is to be provided with arc on the flat board of bullet upper end, so that the material that eddy flow gets off spreads apart by arc water conservancy diversion again, its deficiency is: because the pressure of convey materials is indefinite, the eddy flow angle of material is changed often, when the material of different angles eddy flow touches on flat board, arc on flat board and flat board has been offset the eddy flow dynamics of material, and then changed the eddy flow angle of material, make the diffusion of material in cylindrical shell change very micro-, and, also easily by solid accumulation on flat board, cause material not form eddy flow and scatter, affect separating effect, as can be seen here, the substance that this patent also can't resolve separator is not enough.
And the problem that existing separation of coarse slime owner will exist is because the material rising flows out naturally from downflow weir, because slightly overweighting water, material particles is difficult for discharging, and cause the water content overflowing large, solids content is few, and separating effect is undesirable; Secondly, because former pan feeding well is tangent line enter material way, because feed pressure is different, when pressure hour can not make material form eddy flow, material is scattered, affect separating effect.
Summary of the invention
The object of the invention is to solve above-mentioned the deficiencies in the prior art, provide that a kind of novel structure, the efficiency of separation are high, water content is little when strengthening feed pressure, material and discharge, solids content is high, separating effect is remarkable, reduce production costs and the separation of coarse slime machine of process costs.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of separation of coarse slime machine, comprise main frame cylindrical shell, platform, YE, water tank, water tank injection apparatus, pan feeding cylindrical shell, top cover and hypocentrum, described hypocentrum is fixedly connected with main frame cylinder body bottom through support, it is characterized in that described hypocentrum upper end is provided with taper diffusion platform, taper diffusion platform bigger diameter end is fixedly connected with hypocentrum, the corresponding pan feeding cylindrical shell outlet of miner diameter end, and coordinate with feeding cylinder body space, be beneficial to without increasing feed pressure in the situation that, make material automatically along taper diffusion platform periphery, be umbrella diffusion, material after diffusion mixes with the ascending current of water tank spray again, produce turbulent flow, material is different by density, be suspended in uniformly in cylindrical shell, guarantee density large be deposited in the bottom, what density was little floats over cylindrical shell upper end and flows out through downflow weir and discharging opening.
The present invention can be provided with and help rotating feeding device in pan feeding cylindrical shell, it comprises rotating shaft and blade, described rotating shaft is located at the feeding cylinder axon heart, rotating shaft upper end and platform are hinged, lower end and taper diffusion platform are hinged, on described rotating shaft, interleaved is provided with blade vertically, when the mobile impulse force of material self promotes the blade rotary on rotating shaft, according to hydrodynamics eddy flow, produce centrifugal force, make the homodisperse principle of material, make to enter material in pan feeding cylindrical shell with no pressure flow and the turning effort of blade under produce centrifugal force and form eddy flow, material automatically sorts by density size in the dirty process of rotation, form better density stratification, by taper, spread again the secondary interference diffusion of platform and water tank injection apparatus, make oarse-grained material sink to rapidly main frame cylinder body bottom, short grained material suspends and main frame cylindrical shell top, reached the efficiency of separation high, separating effect acts on significantly.
The present invention can be arranged with pan feeding part flow arrangement in feeding cylinder external body, it comprises shunting top cover, shunting overflow weir and bridging tube body, described bridging tube body is back taper, bridging tube body is enclosed within pan feeding cylindrical shell middle and lower part, outer, bridging tube body upper end is provided with shunting overflow weir, below and taper diffusion platform outer rim matched in clearance, described shunting overflow weir top is provided with shunting top cover, shunting top cover is connected with shunting overflow weir through shunting support plate, so that form shunting overfall between described shunting overflow weir and shunting top cover, described shunting overfall is corresponding with the overfall of described main frame cylindrical shell upper end, when material is after helping the centrifugal layering of rotating feeding device, by the material in bridging tube body, form first sorting, the material particles that density is little is moved under the rotary centrifugal force effect of rotating shaft blade on bridging tube body inwall, shunting overfall through between shunting overflow weir and shunting top cover overflows, and overflow through the overfall of main frame cylindrical shell upper end, make the material moisture that overflows little, solids content is high, the gap that the material particles that density is large spreads between platform and bridging tube body along taper under the effect of self gravitation and eddy flow centrifugal force is discharged in main barrel body, and the while is through the effect of the injection water of the water tank injection apparatus of main frame cylinder body bottom, material is carried out to secondary again and disturb sorting, make it reach best separating effect.
Blade of the present invention comprises guide vane and centrifuge blade, described guide vane is provided with on the rotating shaft in pan feeding cylindrical shell, described centrifuge blade is provided with rotating shaft bottom, described guide vane and rotating shaft horizontal tilt 10-30 °, be beneficial to further material be carried out to water conservancy diversion, guarantee that guide vane plays to material the effect of revolving that helps, described centrifuge blade is connected with rotating shaft is vertical, is beneficial to strengthen the diffusance of bottom material.
The present invention also can be provided with slack adjuster between bridging tube body and taper diffusion platform, it comprises roll adjustment support, adjusting bolt and hold-down nut, described bridging tube body lower end exterior periphery is laid with at least three roll adjustment supports, the hole that adjusting bolt is provided with through roll adjustment support is connected with the screwed hole that the taper surface of taper diffusion platform is provided with, and fix through hold-down nut, be beneficial to adjust bridging tube body and taper diffusion platform underflow gap, control underflow size.
The present invention is owing to adopting said structure, has that novel structure, the efficiency of separation are high, water content is little when strengthening feed pressure, material and discharge, solids content is high, separating effect is remarkable, reduces production costs and the advantage such as process costs.
accompanying drawing explanation
Fig. 1 is the structural representation of prior art.
Fig. 2 is structural representation of the present invention.
Fig. 3 is that the present invention helps the master of rotating feeding device to look schematic diagram.
Fig. 4 is the top view of Fig. 3.
Fig. 5 is that the present invention enters a kind of structural representation of material separating device.
Fig. 6 is the another kind of structural representation of pan feeding part flow arrangement of the present invention.
Fig. 7 is the top view of Fig. 5 or Fig. 6.
Reference numeral: main frame cylindrical shell 1, platform 2, YE 3, water tank 4, water tank injection apparatus 5, shunting top cover 6, pan feeding cylindrical shell 7, top cover 8, hypocentrum 10, taper diffusion platform 11, rotating shaft 12, blade 13,18, shunting overflow weir 14, bridging tube body 15, shunting overfall 16, overfall 17, centrifuge blade 18, roll adjustment support 19, adjusting bolt 20, hold-down nut 21.
The specific embodiment
Below in conjunction with accompanying drawing, the present invention is further described:
As shown in drawings, a kind of separation of coarse slime machine, comprises main frame cylindrical shell 1, platform 2, YE 3, water tank 4, water tank injection apparatus 5, pan feeding cylindrical shell 7, top cover 8 and hypocentrum 10, described hypocentrum is fixedly connected with main frame cylinder body bottom through support, main frame cylindrical shell 1, platform 2, YE 3, water tank 4, water tank injection apparatus 5, pan feeding cylindrical shell 7, structure and the annexation of top cover 8 and hypocentrum 10 are same as the prior art, this does not repeat, it is characterized in that described hypocentrum 10 upper ends are provided with taper diffusion platform 11, taper diffusion platform 11 bigger diameter ends are fixedly connected with hypocentrum 10, the corresponding pan feeding cylindrical shell outlet of miner diameter end, and with pan feeding cylindrical shell 7 matched in clearance, be beneficial to without increasing feed pressure in the situation that, make material automatically along taper diffusion platform 11 peripheries, be umbrella diffusion, the ascending current that material after diffusion sprays with water tank injection apparatus 5 again mixes, produce turbulent flow, material is different by density, be suspended in uniformly in cylindrical shell, guarantee density large be deposited in the bottom, what density was little floats over main frame cylindrical shell upper end and flows out through discharging opening.
The present invention can be provided with and help rotating feeding device in described pan feeding cylindrical shell 7, it comprises rotating shaft 12 and blade 13, described rotating shaft 12 is located at pan feeding cylindrical shell 7 axle center, rotating shaft 12 upper ends and platform 2 are hinged, lower end and taper diffusion platform 11 are hinged, on described rotating shaft 12, interleaved is provided with blade vertically, the impulse force mobile when material self promotes the blade 13 on rotating shaft 12, during 18 rotation, according to hydrodynamics eddy flow, produce centrifugal force, make the homodisperse principle of material, the material that makes to enter in pan feeding cylindrical shell 7 flows and blade 13 with no pressure, under 18 auxiliary pushing, produce centrifugal force and form eddy flow, material automatically sorts by density size in the dirty process of rotation, form better density stratification, by taper, spread again the secondary interference diffusion of platform 11 and water tank injection apparatus 7, make oarse-grained material sink to rapidly main frame cylindrical shell 1 bottom, short grained material suspends and main frame cylindrical shell 1 top, reached the efficiency of separation high, separating effect acts on significantly.
As accompanying drawing 2, 5, 6 the present invention can be provided with pan feeding part flow arrangement in pan feeding cylindrical shell 7 outer cover, it comprises shunting top cover 6, shunting overflow weir 14 and bridging tube body 15, described bridging tube body 15 is back taper, bridging tube body 15 is enclosed within pan feeding cylindrical shell 7 middle and lower parts, bridging tube body 15 outers, upper end are provided with shunting overflow weir 14, below and taper diffusion platform 11 outer rim matched in clearance, described shunting overflow weir 14 tops are provided with shunting top cover 6, shunting top cover 6 is connected with shunting overflow weir 14 through shunting support plate, so that described shunting overflow weir 14 and 6 of shunting top covers form shunting overfall 16, described shunting overfall 16 is corresponding with the overfall 17 of described main frame cylindrical shell 1 upper end, when material is after helping the centrifugal layering of rotating feeding device, by the material in bridging tube body 15, form first sorting, the material particles that density is little is moved under the rotary centrifugal force effect of rotating shaft 12 blades 13 on bridging tube body 15 inwalls, through shunting the shunting overfall 16 of 6 of overflow weir 14 and shunting top covers, overflow, and overflow through the overfall 17 of main frame cylindrical shell 1 upper end, make the material moisture that overflows little, solids content is high, the large material particles of density is discharged in main barrel body 1 along the gap of 15 of taper diffusion platform 11 and bridging tube bodies under the effect of self gravitation and eddy flow centrifugal force, and the while is through the effect of the injection water of the water tank injection apparatus of main frame cylindrical shell 1 bottom, material is carried out to secondary again and disturb sorting, make it reach best separating effect.
As shown in Figure 4, blade of the present invention comprises guide vane 13 and centrifuge blade 18, described guide vane 13 is provided with on the rotating shaft 12 in pan feeding cylindrical shell 7, described centrifuge blade 18 is provided with rotating shaft 12 bottoms, described guide vane 13 is 10-30 ° with rotating shaft 12 horizontal tilt a, be beneficial to further material be carried out to water conservancy diversion, guarantee that 13 pairs of materials of guide vane play the effect that helps to revolve, described centrifuge blade 18 is connected with rotating shaft 12 is vertical, the diffusance that is beneficial to strengthen bottom material, has significantly improved the efficiency of separation.
As shown in Figure 2, the present invention also can be provided with slack adjuster between bridging tube body 15 and taper diffusion platform 11, it comprises roll adjustment support 19, adjusting bolt 20 and hold-down nut 21, described bridging tube body 15 lower end exterior periphery are laid with at least three roll adjustment supports 19, the hole that adjusting bolt 20 is provided with through roll adjustment support 19 is connected with the screwed hole that the taper surface of taper diffusion platform 11 is provided with, and fixing through hold-down nut 21, be beneficial to adjust bridging tube body 15 and taper diffusion platform 11 underflow gaps, control underflow size.
The present invention is when work: first, according to the material of sorting, by adjusting bolt, adjust the gap of bridging tube body and taper diffusion platform underflow, material inlet is connected feed pipe, material injects from the feeding mouth of pan feeding cylindrical shell 7, while entering in pan feeding cylindrical shell 7 by feeding mouth, material promotes guide vane 13 rotations on rotating shaft 12 through self mobile impulse force, according to hydrodynamics eddy flow, produce centrifugal force, make to enter material in pan feeding cylindrical shell 7 with no pressure flow and the auxiliary water conservancy diversion of guide vane 13 under produce centrifugal force and form eddy flow, material in the process of eddy flow automatically according to density size auto-sequencing, make it to form better density stratification, simultaneously, material particles after layering is under the centrifugal action of the centrifuge blade of rotating shaft bottom, the material particles that density is little is moved under the augmented thrust effect of rotating shaft 12 bottom centrifuge blades 13 on bridging tube body 15 inwalls, through shunting the shunting overfall 16 of 6 of overflow weir 14 and shunting top covers, overflow, and flow out through overfall 17 and the discharging opening of main frame cylindrical shell 1 upper end, material after further separated layering, make it to form first sorting, make the material moisture that overflows little, solids content is high, the large material particles of density flows out through the gap of 15 of taper diffusion platform 11 and bridging tube bodies under the centrifugal action of self gravitation and eddy flow centrifuge blade, and be discharged in main frame cylindrical shell 1 along the taper outer rim of taper diffusion platform 11, and the while is in the effect of the injection water of the water tank injection apparatus 5 of main frame cylindrical shell 1 bottom, material is carried out to secondary again and disturb sorting, make material form gradually particle layers by density size, the concentrate material of underwater certain depth is overflowed again by the gap between overflow weir 9 and main frame cylindrical shell 1, and while being deposited in density larger solid accumulation in bottom to density sensor, make density sensor pressurized reach the density value of setting, to YE 3, send signal, opening cone valve discharges bottom material.After material is discharged, density sensor is stressed and reduces to issue a signal to YE 3 and close cone valve.
The present invention is owing to adopting said structure, has that novel structure, the efficiency of separation are high, water content is little when strengthening feed pressure, material and discharge, solids content is high, separating effect is remarkable, reduces production costs and the advantage such as process costs.
Claims (5)
1. a separation of coarse slime machine, comprise main frame cylindrical shell, platform, YE, water tank, water tank injection apparatus, pan feeding cylindrical shell, top cover and hypocentrum, described hypocentrum is fixedly connected with main frame cylinder body bottom through support, it is characterized in that described hypocentrum upper end is provided with taper diffusion platform, taper diffusion platform bigger diameter end is fixedly connected with hypocentrum, the corresponding pan feeding cylindrical shell outlet of miner diameter end, and coordinate with feeding cylinder body space.
2. a kind of separation of coarse slime machine according to claim 1, it is characterized in that being provided with and helping rotating feeding device in described pan feeding cylindrical shell, it comprises rotating shaft and blade, described rotating shaft is located at the feeding cylinder axon heart, rotating shaft upper end and platform are hinged, lower end and taper diffusion platform are hinged, and on described rotating shaft, interleaved is provided with blade vertically.
3. a kind of separation of coarse slime machine according to claim 1, it is characterized in that described feeding cylinder external body is arranged with pan feeding part flow arrangement, it comprises shunting top cover, shunting overflow weir and bridging tube body, described bridging tube body is back taper, bridging tube body is enclosed within pan feeding cylindrical shell middle and lower part, outer, bridging tube body upper end is provided with shunting overflow weir, below and taper diffusion platform outer rim matched in clearance, described shunting overflow weir top is provided with shunting top cover, shunting top cover is fixedly connected with shunting overflow weir through shunting support plate, so that form shunting overfall between described shunting overflow weir and shunting top cover, described shunting overfall is corresponding with the overfall of described main frame cylindrical shell upper end.
4. a kind of separation of coarse slime machine according to claim 1, it is characterized in that described blade comprises guide vane and centrifuge blade, described guide vane is provided with on the rotating shaft in pan feeding cylindrical shell, described centrifuge blade is provided with rotating shaft bottom, and described guide vane and rotating shaft horizontal tilt a are 10-30 °.
5. a kind of separation of coarse slime machine according to claim 1, it is characterized in that being provided with slack adjuster between described bridging tube body and taper diffusion platform, it comprises roll adjustment support, adjusting bolt and hold-down nut, described bridging tube body lower end exterior periphery is laid with at least three roll adjustment supports, the hole that adjusting bolt is provided with through roll adjustment support is connected with the screwed hole that the taper surface of taper diffusion platform is provided with, and fixes through hold-down nut.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310702163.XA CN103691546A (en) | 2013-12-19 | 2013-12-19 | Coarse coal slime sorting machine |
| CN201410144939.5A CN103878059B (en) | 2013-12-19 | 2014-04-13 | Separation of coarse slime machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310702163.XA CN103691546A (en) | 2013-12-19 | 2013-12-19 | Coarse coal slime sorting machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103691546A true CN103691546A (en) | 2014-04-02 |
Family
ID=50353304
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310702163.XA Pending CN103691546A (en) | 2013-12-19 | 2013-12-19 | Coarse coal slime sorting machine |
| CN201410144939.5A Active CN103878059B (en) | 2013-12-19 | 2014-04-13 | Separation of coarse slime machine |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410144939.5A Active CN103878059B (en) | 2013-12-19 | 2014-04-13 | Separation of coarse slime machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN103691546A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104226457A (en) * | 2014-06-30 | 2014-12-24 | 江苏恒荣矿山机械有限公司 | Flow-stabilizing hydraulic classifier |
| CN105435951A (en) * | 2015-12-22 | 2016-03-30 | 大同煤矿集团有限责任公司 | Coarse slime separation machine |
| CN105521878A (en) * | 2015-11-25 | 2016-04-27 | 山东科技大学 | Hydrocyclone with teeter bed separator (TBS) cyclone water curtain separation tank |
| CN110882824A (en) * | 2019-11-07 | 2020-03-17 | 王平武 | Interference bed separator |
| CN111111904A (en) * | 2019-12-31 | 2020-05-08 | 河南理工大学 | Device and method capable of adapting to regulation and control of different fine-grained minerals interference settling separation flow fields |
| CN111804587A (en) * | 2020-06-22 | 2020-10-23 | 江苏华宏科技股份有限公司 | Aortic aerodynamic flow sorting system |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1095999A2 (en) * | 1983-04-29 | 1984-06-07 | Институт ядерной энергетики АН БССР | Centrifugal apparatus for slime thickening |
| CN2795164Y (en) * | 2005-07-30 | 2006-07-12 | 马钢(集团)控股有限公司 | Full automatic uniform material distributor for top storehouse |
| CN201482250U (en) * | 2009-07-17 | 2010-05-26 | 淮北矿山机器制造有限公司 | Automatic diluting distribution device of thickener |
| CN202700634U (en) * | 2012-06-08 | 2013-01-30 | 柳建志 | Coarse slime sorting machine |
| CN203764390U (en) * | 2013-12-19 | 2014-08-13 | 威海顺宝金属制品有限公司 | Coarse slime sorting machine |
-
2013
- 2013-12-19 CN CN201310702163.XA patent/CN103691546A/en active Pending
-
2014
- 2014-04-13 CN CN201410144939.5A patent/CN103878059B/en active Active
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104226457A (en) * | 2014-06-30 | 2014-12-24 | 江苏恒荣矿山机械有限公司 | Flow-stabilizing hydraulic classifier |
| CN105521878A (en) * | 2015-11-25 | 2016-04-27 | 山东科技大学 | Hydrocyclone with teeter bed separator (TBS) cyclone water curtain separation tank |
| CN105435951A (en) * | 2015-12-22 | 2016-03-30 | 大同煤矿集团有限责任公司 | Coarse slime separation machine |
| CN110882824A (en) * | 2019-11-07 | 2020-03-17 | 王平武 | Interference bed separator |
| CN110882824B (en) * | 2019-11-07 | 2021-11-30 | 石门宝丰机械制造有限公司 | Interference bed separator |
| CN111111904A (en) * | 2019-12-31 | 2020-05-08 | 河南理工大学 | Device and method capable of adapting to regulation and control of different fine-grained minerals interference settling separation flow fields |
| CN111804587A (en) * | 2020-06-22 | 2020-10-23 | 江苏华宏科技股份有限公司 | Aortic aerodynamic flow sorting system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103878059A (en) | 2014-06-25 |
| CN103878059B (en) | 2016-05-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103878059B (en) | Separation of coarse slime machine | |
| CN202700634U (en) | Coarse slime sorting machine | |
| CN200998694Y (en) | Short column jet flow floatation machine | |
| CN107649287B (en) | Magnetic micro-fluidic concentrator and complete mineral processing equipment thereof | |
| CN102240610B (en) | Self-gas supply mixed fly ash multistage flotation separation system | |
| CN201052473Y (en) | Coal slurry separator | |
| CN104437834A (en) | Centrifugal ore-dressing device and ore-dressing method thereof | |
| CN203124084U (en) | Tri-product coal slime sorter | |
| CN203764390U (en) | Coarse slime sorting machine | |
| CN104907184B (en) | Pre-desliming and microbubble static-modularity flotation system | |
| CN101947500B (en) | Separator integrated with cyclonic separation and cyclonic flotation | |
| CN107127048B (en) | Magnetic micro-fluidic concentrator and complete magnetic separation equipment thereof | |
| CN103418487B (en) | A kind of separation of coarse slime machine | |
| CN102327807A (en) | Three-product teetered bed separator | |
| CN102311158B (en) | Tilted plate separator with variable inclination | |
| CN202015517U (en) | Composite high-efficiency phase separator | |
| CN102218231B (en) | Oil-water separator | |
| CN211099540U (en) | Ore pulp ore separation box with steady flow ore feeding device | |
| CN200995166Y (en) | Separator of interferent bed | |
| CN202173998U (en) | Combined fly ash floatation separation system with self-air supply | |
| CN203508184U (en) | Coarse slime sorting machine | |
| CN201023062Y (en) | Hydraulic classifier | |
| CN102441479B (en) | Liquid and solid fluidized bed sorting machine for three products and working method thereof | |
| CN103120986A (en) | Flotation tank | |
| CN106570298B (en) | Construction method and application of continuous high-concentration steady-state sand discharging model of superfine tailing vertical sand silo |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140402 |