CN203955302U - The filtration of zirconium ball and retracting device - Google Patents
The filtration of zirconium ball and retracting device Download PDFInfo
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- CN203955302U CN203955302U CN201420326193.5U CN201420326193U CN203955302U CN 203955302 U CN203955302 U CN 203955302U CN 201420326193 U CN201420326193 U CN 201420326193U CN 203955302 U CN203955302 U CN 203955302U
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- zirconium ball
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Abstract
The utility model discloses a kind of filtration and retracting device of zirconium ball, comprise separator for filtering zirconium ball and be arranged on separator near the side on ground for collecting the recovery frame of zirconium ball, separator offers the charging aperture being communicated with the slurry outlet of grinder, the discharging opening being communicated with the Buffer Pool of finished product slurry and the slag-drip opening that is arranged on bottom, the inside of separator is detachably provided with screen pack, screen pack has two openings, screen pack is communicated with slag-drip opening near the opening of one end, bottom of separator, slag-drip opening is provided with slag charge switch valve away from a side of screen pack, the other end opening of screen pack is communicated with charging aperture, slag-drip opening is communicated with recovery frame away from one end of separator.A kind of filtration and retracting device of zirconium ball are provided, realize separating of zirconium ball and slurry by separator is set, reclaim frame and realize screening and the recovery to zirconium ball by arranging, both ensured the quality of finished product slurry, make again zirconium ball be recycled utilization, save production cost.
Description
Technical field
The utility model relates to the technical field that calcium carbonate is produced, and relates in particular to a kind of filtration and retracting device of zirconium ball.
Background technology
In paper industry, calcium carbonate is a kind of conventional rapidoprint, and calcium carbonate is widely used in applying glue coating and calcium carbonate and adds and the processing procedure such as fill out.At present, most of papermaking producer has all been equipped with calcium carbonate grinding shop, and utilizes grinder to produce to meet the powdered whiting product of oneself needs.Wherein, the powdered whiting of high fineness is subject to favor and the extensive use of most of producer because it is with low cost, the powdered whiting of high fineness requires the particle diameter of more than 90% particle to be less than 2 microns conventionally, needs three or three above grinder series connection productions.In addition, when the powdered whiting of high fineness is produced by grinder, need in grinder, add particle diameter is the zirconium ball between 0.6-1.0mm, but along with the lengthening of milling time, zirconium club diminishes gradually, and flow out and enter finished product slurry from the discharging opening of grinder, affect the quality of finished product slurry.Simultaneously, because the lifting of the solid content of the impact of viscosity control, dispersant and calcium carbonate mud, the zirconium ball that particle diameter is qualified also can flow out and enter finished product slurry from the discharging opening of grinder, not only affect the quality of finished product slurry, the equipment of postorder workshop section is produced to adverse influence, as zirconium ball destroys valve, increases wearing and tearing, the wearing and tearing of increase to screen cylinder etc. to screw pump, and cause a large amount of wastes of zirconium ball, production cost is raise.
Chinese patent literature CN201988422U discloses a kind of superfine-powder calcium carbonate grinder, comprise cylindrical shell, in described cylindrical shell, be provided with the agitating device being driven by power set, the top of described cylindrical shell is provided with charging import, is provided with slurry outlet and abrasive media outlet on the sidewall of the bottom of described cylindrical shell.But above-mentioned grinder does not arrange corresponding abrasive media filtration, and abrasive media is easily followed slurry and escaped and enter finished product slurry from described slurry outlet, affects the quality of finished product slurry.
Based on above-mentioned situation, producer proposes a kind of filtration and retracting device, and abrasive media is effectively filtered and reclaimed, and improves the cleanliness factor of finished product slurry and reduces production costs.
Utility model content
The purpose of this utility model is: a kind of filtration and retracting device of zirconium ball are provided, realize separating of zirconium ball and slurry by separator is set, reclaim frame and realize screening and the recovery to zirconium ball by arranging.
For reaching this object, the utility model by the following technical solutions:
A kind of filtration of zirconium ball and retracting device, comprise separator for filtering zirconium ball and be arranged on described separator near the side on ground for collecting the recovery frame of described zirconium ball, described separator offers the charging aperture being communicated with the slurry outlet of grinder, the discharging opening being communicated with the Buffer Pool of finished product slurry and the slag-drip opening that is arranged on bottom, the inside of described separator is detachably provided with screen pack, the two ends of described screen pack have two openings, described screen pack is communicated with described slag-drip opening near the opening of one end, bottom of described separator, described slag-drip opening is provided with slag charge switch valve away from a side of described screen pack, the other end opening of described screen pack is communicated with described charging aperture, described slag-drip opening is communicated with described recovery frame away from one end of described separator.
Particularly, while using described separator to filter zirconium ball, described slag charge switch valve must be in closed condition.Slurry after grinder grinds is discharged and enters in described screen pack by described charging aperture from described slurry outlet, described zirconium ball cannot pass through described screen pack, described zirconium ball is stopped by described slag charge switch valve and in the internal precipitate of described screen pack, and described slurry can pass through described screen pack, described slurry enters the Buffer Pool of finished product slurry from described discharging opening after by described screen pack.In addition, in the time that described separator stops filtering, when described grinder is no longer carried slurry to described separator, open described slag charge switch valve, the zirconium ball that makes to be deposited in described screen pack falls in described recovery frame automatically, realizes the recovery of zirconium ball.
Preferably, described charging aperture is opened in the sidewall of described separator near the position at top.
Preferably, described screen pack is made up of nylon material.
Preferably, the aperture of described screen pack is between 0.2mm-0.8mm.Concrete aperture can need to be selected according to the grinding precision of grinder with to the fineness of slurry.
As the preferred technical scheme of one, described recovery frame comprises and reclaims support and be detachably arranged on the screen frame on described recovery support, and the inside of described screen frame is detachably provided with the screen cloth for screening zirconium ball.The mesh of described screen cloth can be according to producer the needs of the particle diameter to zirconium ball select and change, described screen cloth can filter and screen described zirconium ball, the described zirconium ball that is less than the mesh of described screen cloth enters trench through described screen cloth, and the described zirconium ball that is greater than the mesh of described screen cloth is deposited in described screen cloth and is recovered utilization.
Preferably, described recovery support comprises the support platform for holding described screen frame, in described support platform, offer the opening of stepping down of U-shaped, the top of described screen frame is provided with support lugn, described screen frame from the described opening of stepping down enter described support platform and make described support lugn and described support platform near the surperficial butt of described separator one side.
Preferably, on described support lugn, be relatively set with two for carrying the handle of described screen frame.
Preferably, described screen frame entirety is cylindric.
As the preferred technical scheme of one, the top of described screen frame is provided with top cover, on described top cover, offer the slag inlet that is communicated with described slag-drip opening and for rinsing the mouth spray of described zirconium ball, described mouth spray is selectively connected with water pipe and realizes the flushing to described zirconium ball.
As the preferred technical scheme of one, described screen pack is provided with the next retainer plate near the opening sleeve of one end, bottom of described separator, described the next retainer plate is detachably arranged in described slag-drip opening, described screen pack is provided with upper retainer plate away from the opening sleeve of one end, bottom of described separator, and described upper retainer plate is detachably arranged on the first pipeline being communicated with described charging aperture.
Preferably, the external diameter of described upper retainer plate is less than the external diameter of described the next retainer plate.
Particularly, the slurry that described grinder is carried enters described screen pack by described upper retainer plate, and the described zirconium ball being deposited in described screen pack is discharged described screen pack by described the next retainer plate.
Particularly, in the time that needs are changed described screen pack, first described upper retainer plate is pulled down from described the first pipeline, described the next retainer plate is pulled down from described slag-drip opening, and by described upper retainer plate, the next retainer plate and screen pack take out from described slag-drip opening, then described screen pack is separated with described the next retainer plate dismounting from described upper retainer plate, and described upper retainer plate and described the next retainer plate are arranged on to the both ends open of new described screen pack, finally by described upper retainer plate, the next retainer plate and screen pack pack described separator into from described slag-drip opening, and described the next retainer plate is arranged in described slag-drip opening, described upper retainer plate is arranged on described the first pipeline.
As the preferred technical scheme of one, described the next retainer plate is fixedly installed second pipe away from a side of described screen pack, described slag charge switch valve is fixedly mounted on described second pipe, and described second pipe is communicated with described slag inlet by pipeline away from one end of described the next retainer plate.
Particularly, need described slag charge switch valve to close before using described separator to filter described zirconium ball.
As the preferred technical scheme of one, described the first pipeline runs through described charging aperture away from one end of described upper retainer plate and extends to the outside of described separator, described the first pipeline is communicated with the slurry outlet of grinder by pipeline away from one end of described upper retainer plate, on described the first pipeline and the outer setting that is positioned at described separator be useful on the charging control valve of controlling slurry flow.
As the preferred technical scheme of one, the bottom of described separator is taper, and described slag-drip opening is arranged on the tip of the bottom of taper, and the top of described separator is provided with able to turn on or off seal cover.Particularly, in the time that described separator is cleaned, the sewage after cleaning can flow down and directly discharge from described slag-drip opening along the inclined-plane of taper bottom, has reduced the difficulty of cleaning.
Particularly, while changing described screen pack, need to open described seal cover, and described upper retainer plate be loaded and unloaded near a side of described seal cover from described separator.
Preferably, described separator comprises body and be fixed on the described bottom of described body near described recovery frame one side, and described seal cover is arranged on the side of described body away from described bottom, and described body is cylindric, and described bottom is coniform.
Preferably, described separator comprises body and be fixed on the described bottom of described body near described recovery frame one side, and described seal cover is arranged on the side of described body away from described bottom, and described body is rectangular-shaped, and described bottom is cubic taper.
As the preferred technical scheme of one, described discharging opening is opened on described seal cover, described discharging opening is provided with the 3rd pipeline away from a side of described separator, described the 3rd pipeline is communicated with the Buffer Pool of finished product slurry by pipeline away from one end of described separator, on described the 3rd pipeline, is provided with the discharging switch valve for opening and closing described the 3rd pipeline.
As the preferred technical scheme of one, on described the 3rd pipeline and between described discharging opening and described discharging switch valve, be provided with and wash away pipeline, described in wash away on pipeline and be fixedly installed and wash away switch valve.
Particularly, in the time that described separator is in running order, described in wash away switch valve must be in closed condition.In the time that needs clean described separator, first close described charging control valve and described discharging switch valve, then open described slag charge switch valve and described in wash away switch valve, and by described wash away pipeline be connected with water pipe realization washing away and cleaning described separator.
As the preferred technical scheme of one, on described seal cover and a side that is positioned at described discharging opening offer swash, described swash is provided with and washes away pipeline away from a side of described separator, described in wash away on pipeline and be fixedly installed and wash away switch valve.
Particularly, in the time that described separator is in running order, described in wash away switch valve must be in closed condition.In the time that needs clean described separator, first close described charging control valve and described discharging switch valve, then open described slag charge switch valve and described in wash away switch valve, and by described wash away pipeline be connected with water pipe realization washing away and cleaning described separator.
The beneficial effects of the utility model are: filtration and retracting device that a kind of zirconium ball is provided, by being set, separator realizes separating of zirconium ball and slurry, by being set, recovery frame realizes screening and the recovery to zirconium ball, both ensured the quality of finished product slurry, make again zirconium ball be recycled utilization, save production cost.
Brief description of the drawings
According to drawings and embodiments the utility model is described in further detail below.
Fig. 1 is the filtration of zirconium ball and the structural representation of retracting device described in embodiment mono-;
Fig. 2 is the filtration of zirconium ball and the structural representation of retracting device described in embodiment bis-;
Fig. 3 is the filtration of zirconium ball and the structural representation of retracting device described in embodiment tri-.
In Fig. 1 to Fig. 3:
1, separator; 11, charging aperture; 12, discharging opening; 13, slag-drip opening; 14, seal cover;
2, screen pack; 21, upper retainer plate; 22, the next retainer plate;
3, reclaim frame; 31, reclaim support; 311, support platform; 32, screen frame; 321, screen cloth; 322, support lugn; 323, handle; 33, top cover; 331, slag inlet; 332, mouth spray;
4, the first pipeline; 41, charging control valve;
5, second pipe; 51, slag charge switch valve;
6, the 3rd pipeline; 61, discharging switch valve;
7, wash away pipeline; 71, wash away switch valve; 72, swash;
8, spray piping; 81, spray switch valve.
Detailed description of the invention
Further illustrate the technical solution of the utility model below in conjunction with accompanying drawing and by detailed description of the invention.
Embodiment mono-:
As shown in Figure 1, a kind of filtration of zirconium ball and retracting device, comprise separator for filtering zirconium ball 1 and be arranged on separator 1 near the side on ground for collecting the recovery frame 3 of described zirconium ball, separator 1 offer charging aperture 11, the discharging opening 12 being communicated with the Buffer Pool of finished product slurry being communicated with the slurry outlet of grinder and be arranged on bottom slag-drip opening 13.Particularly, separator 1 comprises body and is fixed on described body near the described bottom of reclaiming frame 3 one sides, described body is provided with able to turn on or off seal cover 14 away from a side of described bottom, described body is cylindric, described bottom is coniform, slag-drip opening 13 is arranged on the tip of cone shape described bottom, and discharging opening 12 is opened in the center of seal cover 14, and charging aperture 11 is opened in the sidewall of separator 1 near the position at top.
The inside of separator 1 is detachably provided with screen pack 2, screen pack 2 is screen packs of being made up of nylon, the aperture of screen pack 2 is 0.2mm, screen pack 2 has the upper opening of top one side of close separator 1 and the next opening of bottom one side of close separator 1, described the next opening sleeve is provided with the next retainer plate 22, the next retainer plate 22 is detachably arranged in slag-drip opening 13, described upper opening sleeve is provided with upper retainer plate 21, and upper retainer plate 21 is detachably arranged on the first pipeline 4 being communicated with charging aperture 11.The external diameter of upper retainer plate 21 is less than the external diameter of the next retainer plate 22.
Particularly, in the time that needs are changed screen pack 2, first opening encapsulation lid 14, upper retainer plate 21 is pulled down from the first pipeline 4, the next retainer plate 22 is pulled down from slag-drip opening 13, and by upper retainer plate 21, the next retainer plate 22 and screen pack 2 take out from slag-drip opening 13, then screen pack 2 is separated with the next retainer plate 22 dismountings from upper retainer plate 21, and upper retainer plate 21 and the next retainer plate 22 are arranged on to the both ends open of new screen pack 2, finally by upper retainer plate 21, the next retainer plate 22 and screen pack 2 pack separator 1 into from slag-drip opening 13, and the next retainer plate 22 is arranged in slag-drip opening 13, upper retainer plate 21 is arranged on the first pipeline 4.
The first pipeline 4 runs through charging aperture 11 away from one end of upper retainer plate 21 and extends to the outside of separator 1, the first pipeline 4 is communicated with the slurry outlet of grinder by pipeline away from one end of upper retainer plate 21, on the first pipeline 4 and the outer setting that is positioned at separator 1 be useful on the charging control valve 41 of controlling slurry flow.
The next retainer plate 22 is fixedly installed second pipe 5 away from a side of screen pack 2, is provided with the slag charge switch valve 51 for opening and closing second pipe 5 on second pipe 5, and second pipe 5 is communicated with recovery frame 3 by pipeline away from one end of the next retainer plate 22.Particularly, use separator 1 before described zirconium ball is filtered needs slag charge switch valve 51 to close.
Discharging opening 12 is provided with the 3rd pipeline 6, the three pipelines 6 away from a side of separator 1 and is communicated with the Buffer Pool of finished product slurry by pipeline away from one end of separator 1, is provided with the discharging switch valve 61 for opening and closing the 3rd pipeline 6 on the 3rd pipeline 6.
On the 3rd pipeline 6 and between discharging opening 12 and discharging switch valve 61, be provided with and wash away pipeline 7, wash away on pipeline 7 and be fixedly installed and wash away switch valve 71.Particularly, in the time that separator 1 is in running order, washing away switch valve 71 must be in closed condition; In the time of needs cleaning separator 1, first close charging control valve 41 and discharging switch valve 61, then open slag charge switch valve 51 and wash away switch valve 71, and being connected realization washing away and cleaning separator 1 with water pipe by washing away pipeline 7.
Reclaiming frame 3 comprises recovery support 31 and is detachably arranged on the screen frame 32 reclaiming on support 31, screen frame 32 entirety are cylindric, the inside of screen frame 32 is detachably provided with the screen cloth 321 for screening zirconium ball, screen cloth 321 can filter and screen described zirconium ball, the described zirconium ball that is less than the mesh of screen cloth 321 enters trench through screen cloth 321, and the described zirconium ball that is greater than the mesh of screen cloth 321 is deposited in screen cloth 321 and is recovered utilization.
Reclaim support 31 and comprise the support platform 311 for holding screen frame 32, in support platform 311, offer the opening of stepping down of U-shaped, the top of screen frame 32 is provided with support lugn 322, and screen frame 32 enters support platform 311 and makes support lugn 322 and the surperficial butt of support platform 311 near separator 1 one sides from the described opening of stepping down.On support lugn 322, be relatively set with two for carrying the handle 323 of screen frame 32.
The top of screen frame 32 is provided with top cover 33, on top cover 33, offer the slag inlet 331 that is communicated with slag-drip opening 13 and for rinsing the mouth spray 332 of described zirconium ball, mouth spray 332 is fixedly installed spray piping 8 away from a side of screen frame 32, on spray piping 8, be provided with the spray switch valve 81 for opening and closing spray piping 8, spray piping 8 is communicated with water pump by water pipe away from one end of screen frame 32.
Operation principle:
Use separator 1 when zirconium ball is filtered, slag charge switch valve 51 and wash away switch valve 71 must be in closed condition.Open charging control valve 41 and discharging switch valve 61, the inside of separator 1 discharged and enters by the first pipeline 4 and charging aperture 11 by slurry after described grinder grinds from described slurry outlet, and middle through entering in screen pack 2 from upper retainer plate 21, described zirconium ball cannot pass through screen pack 2, described zirconium ball is stopped by slag charge switch valve 51 and in the internal precipitate of screen pack 2, and described slurry can pass through screen pack 2, the Buffer Pool of finished product slurry is discharged and entered by the 3rd pipeline 6 to described slurry from discharging opening 12 after by screen pack 2.In addition, in the time that separator 1 stops filtering, be that charging control valve 41 is while cutting out, open slag charge switch valve 51, the zirconium ball that makes to be deposited in screen pack 2 falls into automatically by second pipe 5 and slag inlet 331 in the screen frame 32 that reclaims frame 3, and by screen frame 32, described zirconium ball is screened, realize the recovery to qualified zirconium ball.
Embodiment bis-:
The difference of the present embodiment and embodiment mono-is:
As shown in Figure 2, the described body of separator 1 is rectangular-shaped, and the described bottom of separator 1 is cubic taper.Screen pack 2 is screen packs of being made up of nylon, and the aperture of screen pack 2 is 0.8mm.Discharging opening 12 is opened on seal cover 14, but non-central location, on seal cover 14 and a side that is positioned at discharging opening 12 offer swash 72, swash 72 is provided with and washes away pipeline 7 away from a side of separator 1, washes away on pipeline 7 and is fixedly installed and washes away switch valve 71.Particularly, in the time that separator 1 is in running order, washing away switch valve 71 must be in closed condition.In the time of needs cleaning separator 1, first close charging control valve 41 and discharging switch valve 61, then open slag charge switch valve 51 and wash away switch valve 71, and being connected realization washing away and cleaning separator 1 with water pipe by washing away pipeline 7.
Embodiment tri-:
The difference of the present embodiment and embodiment bis-is:
As shown in Figure 3, the described body of separator 1 is cylindric, and the described bottom of separator 1 is coniform.Screen pack 2 is screen packs of being made up of nylon, and the aperture of screen pack 2 is 0.5mm.Discharging opening 12 is opened in the sidewall of separator 1 near the position of seal cover 14, discharging opening 12 is oppositely arranged with charging aperture 11, discharging opening 12 is fixedly installed the 3rd pipeline 6 away from a side of separator 1, the 3rd pipeline 6 is communicated with the Buffer Pool of finished product slurry by pipeline away from one end of separator 1, is provided with the discharging switch valve 61 for opening and closing the 3rd pipeline 6 on the 3rd pipeline 6.
The center of seal cover 14 offers swash 72, and swash 72 is provided with and washes away pipeline 7 away from a side of separator 1, washes away on pipeline 7 and is fixedly installed and washes away switch valve 71.Particularly, in the time that separator 1 is in running order, washing away switch valve 71 must be in closed condition.In the time of needs cleaning separator 1, first close charging control valve 41 and discharging switch valve 61, then open slag charge switch valve 51 and wash away switch valve 71, and being connected realization washing away and cleaning separator 1 with water pipe by washing away pipeline 7.
" first ", " second " herein, " the 3rd " are only used to be distinguished on describing, and do not have special implication.
What need statement is; above-mentioned detailed description of the invention is only preferred embodiment of the present utility model and institute's application technology principle; in technical scope disclosed in the utility model; the variation that any those skilled in the art of being familiar with easily expect or replacement, all should be encompassed in protection domain of the present utility model.
Claims (10)
1. the filtration of a zirconium ball and retracting device, it is characterized in that, comprise separator for filtering zirconium ball and be arranged on described separator near the side on ground for collecting the recovery frame of described zirconium ball, described separator offers the charging aperture being communicated with the slurry outlet of grinder, the discharging opening being communicated with the Buffer Pool of finished product slurry and the slag-drip opening that is arranged on bottom, the inside of described separator is detachably provided with screen pack, the two ends of described screen pack have two openings, described screen pack is communicated with described slag-drip opening near the opening of one end, bottom of described separator, described slag-drip opening is provided with slag charge switch valve away from a side of described screen pack, the other end opening of described screen pack is communicated with described charging aperture, described slag-drip opening is communicated with described recovery frame away from one end of described separator.
2. the filtration of zirconium ball according to claim 1 and retracting device, is characterized in that, described recovery frame comprises and reclaim support and be detachably arranged on the screen frame on described recovery support, and the inside of described screen frame is detachably provided with the screen cloth for screening zirconium ball.
3. the filtration of zirconium ball according to claim 2 and retracting device, is characterized in that, the top of described screen frame is provided with top cover, offers the slag inlet that is communicated with described slag-drip opening and for rinsing the mouth spray of described zirconium ball on described top cover.
4. the filtration of zirconium ball according to claim 3 and retracting device, it is characterized in that, described screen pack is provided with the next retainer plate near the opening sleeve of one end, bottom of described separator, described the next retainer plate is detachably arranged in described slag-drip opening, described screen pack is provided with upper retainer plate away from the opening sleeve of one end, bottom of described separator, and described upper retainer plate is detachably arranged on the first pipeline being communicated with described charging aperture.
5. the filtration of zirconium ball according to claim 4 and retracting device, it is characterized in that, described the next retainer plate is fixedly installed second pipe away from a side of described screen pack, described slag charge switch valve is fixedly mounted on described second pipe, and described second pipe is communicated with described slag inlet by pipeline away from one end of described the next retainer plate.
6. the filtration of zirconium ball according to claim 5 and retracting device, it is characterized in that, described the first pipeline runs through described charging aperture away from one end of described upper retainer plate and extends to the outside of described separator, described the first pipeline is communicated with the slurry outlet of grinder by pipeline away from one end of described upper retainer plate, on described the first pipeline and the outer setting that is positioned at described separator be useful on the charging control valve of controlling slurry flow.
7. the filtration of zirconium ball according to claim 6 and retracting device, is characterized in that, the bottom of described separator is taper, and described slag-drip opening is arranged on the tip of the bottom of taper, and the top of described separator is provided with able to turn on or off seal cover.
8. the filtration of zirconium ball according to claim 7 and retracting device, it is characterized in that, described discharging opening is opened on described seal cover, described discharging opening is provided with the 3rd pipeline away from a side of described separator, described the 3rd pipeline is communicated with the Buffer Pool of finished product slurry by pipeline away from one end of described separator, on described the 3rd pipeline, is provided with the discharging switch valve for opening and closing described the 3rd pipeline.
9. the filtration of zirconium ball according to claim 8 and retracting device, is characterized in that, on described the 3rd pipeline and between described discharging opening and described discharging switch valve, be provided with and wash away pipeline, described in wash away on pipeline and be fixedly installed and wash away switch valve.
10. the filtration of zirconium ball according to claim 8 and retracting device, it is characterized in that, on described seal cover and a side that is positioned at described discharging opening offer swash, described swash is provided with and washes away pipeline away from a side of described separator, described in wash away on pipeline and be fixedly installed and wash away switch valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420326193.5U CN203955302U (en) | 2014-06-18 | 2014-06-18 | The filtration of zirconium ball and retracting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420326193.5U CN203955302U (en) | 2014-06-18 | 2014-06-18 | The filtration of zirconium ball and retracting device |
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| Publication Number | Publication Date |
|---|---|
| CN203955302U true CN203955302U (en) | 2014-11-26 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420326193.5U Expired - Fee Related CN203955302U (en) | 2014-06-18 | 2014-06-18 | The filtration of zirconium ball and retracting device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109482572A (en) * | 2018-12-28 | 2019-03-19 | 北方奥钛纳米技术有限公司 | Zirconium ball cleaning device |
| CN112604781A (en) * | 2020-11-26 | 2021-04-06 | 湖南新威凌新材料有限公司 | Superfine grinder and ball material separator thereof |
-
2014
- 2014-06-18 CN CN201420326193.5U patent/CN203955302U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109482572A (en) * | 2018-12-28 | 2019-03-19 | 北方奥钛纳米技术有限公司 | Zirconium ball cleaning device |
| CN112604781A (en) * | 2020-11-26 | 2021-04-06 | 湖南新威凌新材料有限公司 | Superfine grinder and ball material separator thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141126 Termination date: 20180618 |