CN105903254A - Multi-cone-shaped upender for filtering and washing powder - Google Patents
Multi-cone-shaped upender for filtering and washing powder Download PDFInfo
- Publication number
- CN105903254A CN105903254A CN201610392503.7A CN201610392503A CN105903254A CN 105903254 A CN105903254 A CN 105903254A CN 201610392503 A CN201610392503 A CN 201610392503A CN 105903254 A CN105903254 A CN 105903254A
- Authority
- CN
- China
- Prior art keywords
- cylinder
- tipper
- hollow
- powder body
- filtration washing
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/35—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element
- B01D33/68—Retarding cake deposition on the filter during the filtration period, e.g. using stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/80—Accessories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D33/00—Filters with filtering elements which move during the filtering operation
- B01D33/80—Accessories
- B01D33/801—Driving means, shaft packing systems or the like
Abstract
The invention discloses a multi-cone-shaped upender for filtering and washing powder. The upender comprises a support and a barrel. The two sides of the barrel are fixed to the support through a rotating shaft and a hollow extending shaft respectively. A power mechanism is arranged at the side of the support and connected with the rotating shaft. The hollow extending shaft is sleeved with an extending connection pipe through a fixing shaft. The barrel is provided with one or multiple conical barrel bodies through flanges. The enclosure areas between the conical barrel bodies and the barrel are internally provided with a filtering medium, and the filtering medium is connected with the extending connection pipe. By means of the multi-cone-shaped upender, the power can be filtered, washed and dried, and the filtering effect is high.
Description
Technical field
The present invention relates to a kind of powder body filtration washing tipper, particularly one be applicable to medicine or
The solid of the industries such as the crystalline solid of pesticide industry, the noble metal powder body of metallurgy industry, energy-conserving and environment-protective
Granule and gas and/or many tapers tipper of the filtration of liquid and washing.
Background technology
At present, conventional taper tipping arrangement is commercially a lot, such as: concrete mixer,
Flour mixing and blending machine.Its principle is to utilize motor to rotarily drive stirring vane to rotate, and makes
Article in agitator are driven to rotate, thus, reach the purpose of mixing.This kind of device structure
Simply, typically it is mainly used in mixing or is dried, it is impossible to filtering.
Summary of the invention
It is an object of the invention to, it is provided that a kind of powder body filtration washing many tapers tipper.This
The bright powder body that realizes filters, and filter effect is higher.
Technical scheme: a kind of powder body filtration washing many tapers tipper, its feature exists
In: including support and cylinder, cylinder both sides are fixed on through rotary shaft and hollow extraction axle respectively and prop up
On frame, stent side portion is provided with actuating unit, and actuating unit is connected with rotary shaft, hollow extraction axle
On through fixed hub be provided with extraction adapter；It is provided with one or more taper through flange on described cylinder
Cylinder, conical shell and cylinder enclose region in be provided with filter medium, filter medium and extraction
Adapter connects.
In aforesaid powder body filtration washing many tapers tipper, described actuating unit includes through slowing down
Support is fixed on the decelerator on support, and the output shaft of decelerator connects motor, and motor connects
Converter, the output shaft of described decelerator is had to be connected with rotary shaft through shaft coupling.
In aforesaid powder body filtration washing many tapers tipper, described filter medium is integrally fixed at the end
Flat board hollow filter plate on plate and/or the cylinder hollow filter plate being fixed on cylinder and/or
The tapered hollow screen plate being fixed on conical shell.
In aforesaid powder body filtration washing many tapers tipper, set in the hollow of described filter medium
There is ribs.
In aforesaid powder body filtration washing many tapers tipper, in described conical shell, it is provided with layout
Tapered filter tube.
In aforesaid powder body filtration washing many tapers tipper, it is provided with layout in described cylinder in circle
The filter tube of shape.
In aforesaid powder body filtration washing many tapers tipper, the bevel angle of described conical shell is
∠ β, (180 ° of-∠ β)/2 ＞ angles of repose.
In aforesaid powder body filtration washing many tapers tipper, described ∠ β=60 ° or ∠ β=
90°。
In aforesaid powder body filtration washing many tapers tipper, described filter medium is once sintered
The sintered plate of molding.
In aforesaid powder body filtration washing many tapers tipper, described filter medium is at thickness direction
It is provided with the passage of stream cleaner liquid, the normal pressure of resistance to pressure reduction 0.6～1.6MPa or counter-pressure.
In aforesaid powder body filtration washing many tapers tipper, described actuating unit passes through touch screen
PLC system and/or DCS system and/or public control machine and/or mobile phone A PP software realized
Filter, wash, be dried, slagging tap runs without interruption continuously.
In aforesaid powder body filtration washing many tapers tipper, described cylinder body outer wall is provided with cold and hot matchmaker
Chuck.Enter heating agent when drying process in chuck and coordinate vacuum suction filter, doing of solid material particle
Dry speed will faster, in hgher efficiency.
Compared with prior art, the present invention drives barrel body rotation by actuating unit, makes conically shaped
Internal powder upset, is filtered by the filter medium in conical shell, after filtering
Cleaner liquid is through drawing adapter output, thus realizes the filtration washing of powder body, and efficiency is higher.
Ribs is set in the hollow of filter medium, reduces filter medium body thickness, reduce the energy
Consume cost-effective.The setting of multiple conical shells, can improve efficiency, convenient use.This
The bright powder body that realizes is filtered, washed and dried, and filter effect is higher.
Accompanying drawing explanation
The structural representation of Fig. 1 embodiment of the present invention 1；
The structural representation of Fig. 2 embodiment of the present invention 2；
The structural representation of Fig. 3 embodiment of the present invention 3；
The structural representation of Fig. 4 embodiment of the present invention 4；
The structural representation of Fig. 5 embodiment of the present invention 5；
The appearance schematic diagram of Fig. 6 embodiment of the present invention 6；
The appearance schematic diagram of Fig. 7 embodiment of the present invention 7；
The appearance schematic diagram of Fig. 8 embodiment of the present invention 8；
The appearance schematic diagram of Fig. 9 embodiment of the present invention 9；
The appearance schematic diagram of Figure 10 embodiment of the present invention 10；
The appearance schematic diagram of Figure 11 embodiment of the present invention 11.
1-support, 2-speed reducer base, 3-decelerator, 4-rotary shaft, 5-converter, 6-motor,
7-cylinder, 8-flange, 9-base plate, 10-support plate, 11-conical shell, 12-slags tap automatically
Valve, 13-feed pipe, 14-filter tube, 15-tapered hollow screen plate, 16-flat board hollow mistake
Filter plate, 17-cylinder hollow filter plate, 18-fairlead, 19-rotation axis support, 20-draws and connects
Pipe, 21-fixed hub, 22-hollow extraction axle.
Detailed description of the invention
The present invention is further illustrated with embodiment below in conjunction with the accompanying drawings, but be not intended as right
The foundation that the present invention limits.
Embodiment.A kind of powder body filtration washing many tapers tipper, as it is shown in figure 1, include propping up
Frame 1 and cylinder 7, cylinder 7 both sides are fixed on through rotary shaft 4 and hollow extraction axle 22 respectively
On support 1, support 1 sidepiece is provided with actuating unit, and actuating unit is connected with rotary shaft 4, empty
The heart is drawn and is provided with extraction adapter 20 through fixed hub 21 on axle 22；Through method on described cylinder 7
Blue 8 be provided with one or more conical shell 11, conical shell 11 and cylinder 7 enclose region
Inside being provided with filter medium, filter medium is connected with drawing adapter 20 through fairlead 18.Described dynamic
Force mechanisms includes being fixed on the decelerator 3 on support 1 through reducer pedestal 2, decelerator 3 defeated
Shaft connects motor 6, and motor 6 connects converter 5, the output shaft of described decelerator 3
It is connected with rotary shaft through shaft coupling.Described filter medium is integrally fixed at the flat board hollow on base plate 9
Screen plate 16 and/or the cylinder hollow filter plate 17 being fixed on cylinder 7 and/or be fixed on cone
Tapered hollow screen plate 15 on shape cylinder 11.Be provided with in described conical shell 11 layout in
The filter tube 14 of taper.It is provided with in described cylinder and arranges rounded filter tube.Described taper
The bevel angle of cylinder 11 is ∠ β, 180 ° of-∠ β/2 ＞ angles of repose.Described ∠ β=60 °
Or ∠ β=90 °.Described filter medium is the sintered plate of once sintered molding, not splice plate.
It is provided with ribs in the hollow of described filter medium.Small end at described conical shell 11 sets
There is automatic valve 12 of slagging tap, the outer wall of conical shell 11 is additionally provided with feed pipe 13.Described sky
The heart is drawn axle 22 and is fixed on support 1 by rotation axis support 19.Fairlead 18 can not
Pass through in hollow extraction axle, directly utilize flexible pipe and connect, reduce manufacturing cost, and overturn
Angle need be restricted.
The present invention arranges flange 8 between cylinder 7 and conical shell 11, can be used for installing energy mutually
The filter medium changed；Base plate 9 is set in cylinder, for reducing base plate 9 thickness and proof strength,
Can arrange support plate 10 under base plate, automatic valve 12 of slagging tap is arranged on the osculum of conical shell
End, cylinder both sides arrange rotary shaft 4 and hollow extraction axle 22, and rotation axis support 19 is arranged on
On support 1, decelerator 3 is arranged on speed reducer base 2 and is connected with rotary shaft, converter 5
Controlling motor 6 drives decelerator 3 to make tipper overturn.
The flip angle of the present invention 360 ° just overturns, instead overturns or/and the unrestricted number of turns is the most single
To upset without anti-upset.
The present invention enter mother solution, go out cleaner liquid, blowback, malleation, go out solid slag, washings enter
Pipe with go out pipe etc. and always drawn by 22 hollow extraction axis congruences, extraction adapter 20 is welded on fixing axle
On set 21, prevent technique adapter from interfering with equipment upset.
The present invention each area filter medium fairlead is drawn respectively or/and draw together after collecting；
Draw respectively and facilitate the physics pulse cleaning of each area filter medium more thoroughly, extend filter medium
Service life, it is ensured that stablizing of cleaner liquid flow；Draw together after collecting, can reduce
The quantity of technique adapter, reduces hollow and draws the processing cost of axle and simplify the complexity of robot control system(RCS)
Degree, reduction equipment dispatches from the factory cost profit in using enterprise.
The present invention arranges tapered hollow screen plate 15 on conical shell 11 or/and filter tube
14, tapered hollow screen plate is or/and the angle of taper of angle of taper and conical shell of filter tube
Unanimously, filter tube arranges multiple structure increases filter area.
The present invention flat board hollow filter plate 16 is set on base plate 9 or/and horizontal filtering pipe or
/ and handstand filter tube.
The present invention cylinder hollow filter plate 17 is set at cylinder 7 or/and horizontal filtering pipe or
/ and handstand filter tube or/and hang filter tube from above.
Setting is feed pipe 13 and the fairlead of powder body filtration washing many tapers tipper further
18 are connected to hollow extraction axle 22 collects, together with conical shell 11 and hollow extraction axle 22
Upset, on fixed hub 21, connection extraction adapter 20 is fixed on support 1 and does not overturns, technique
Adapter is fixing draws convenient layout.
The bevel angle ∠ β of the conical shell 11 of the present invention, carries out simulation by computer software
Computing, is adjusted by factors such as the particle diameter of solid particle, shape, water content in filtrated stock, makes
The bevel angle ∠ β of conical shell meets formula: (180 ° of-∠ β)/2 ＞ angles of repose, preferably
Bevel angle ∠ β=60 °, or ∠ β=90 °；In tapping process, the cone of conical shell
The correct design of shape angle make solid particle without noresidue in the emptying at dead angle, beneficially equipment and
Not mixed batch of material.
The present invention arranges 1 conical shell, or 2 conical shells, or 3 conical shells,
Or 4 conical shells, or 5 conical shells, or 6 conical shells, or more than 6 cones
Shape cylinder.
The present invention at 3 or/and 3 with in upper conical tipper, it is achieved the 1st conically shaped
Body is at fed filtration, and the 2nd conical shell in washing and press dry, and the 3rd conical shell is carried out
Deslagging goes out dry solid；Fed filtration operation is entered after the 3rd conical shell deslagging terminates, the
1 conical shell then fed filtration terminates enter washing and press dry operation, and the 2nd conically shaped
Body washs and press dry end entrance deslagging and goes out dry solid operation；It is circulated and so forth, and leads to
Cross touch screen/PLC or/and DCS system is or/and public control machine is or/and mobile phone realizes filtering, washing
Wash, be dried, slagging tap runs without interruption continuously；
The present invention filtering, wash, stop upset or/and continuous overturning runs when slagging tap.
The present invention, when upset runs, can form upset and stir the work of material filter progress
With, reduce the resistivity of mother solution cake layer and reduce energy consumption；Washing procedure can be formed solid particle
Contact with washings more fully, more thoroughly, shorten the time of washing procedure；To muck discharging process meeting
Form upset solid particle, loosen and break up solid block, more conducively the continuous row of solid particle
Go out.Deadweight is utilized or/and pull of vacuum is or/and solid slag is arranged by gas positive pressure power when slagging tap
Go out.Pull of vacuum is utilized or/and gas positive pressure power is or/and cleaner liquid is arranged by pump pressurization during filtration
Go out.
Described filter medium and filter tube, be provided with the logical of stream cleaner liquid at thickness direction
Road, the normal pressure of resistance to pressure reduction 0.6～1.6MPa is or/and counter-pressure, and filter media material is poly-
Tetrafluoroethene or/ultra-high molecular weight polyethylene are or/and titanium is or/and S31603 is or/and poly-third
Alkene, simple material is or/and add heatproof component or/and add resistance to oxidation component or/and add
The component of resistance to aging resistance, filter medium union joint and this body by integral forming.
Described tapered hollow screen plate divide in conical centre's axle vertical direction 2nd district or/
More than 2nd district, and the fairlead after subregion is each independently drawn respectively.
Embodiment 1.When having two conical shells, as it is shown in figure 1, cylinder 7 and taper
Flange 8 is set between cylinder 11, under flat board hollow filter plate 16, base plate 9 is set, for reducing
Base plate 9 thickness and proof strength arrange support plate 10 under base plate, automatic valve 12 of slagging tap
It is arranged on the osculum end of conical shell.
Tapered hollow screen plate 15 and filter tube 14, tapered hollow are set on conical shell 11
Screen plate 15 is consistent with the angle of taper of conical shell with the angle of taper of filter tube 14, makes cone
The bevel angle ∠ β of shape cylinder meets formula: (180 ° of-∠ β)/2 ＞ angles of repose；Cylinder 7
Arranging cylinder hollow filter plate 17 and filter tube, filter tube can arrange multiple structure increases filtration
Area.
Feed pipe 13 and fairlead 18 are connected to hollow extraction axle 22 and collect, with conical shell
11 overturn together with hollow extraction axle 22, fixed hub 21 connects and draws adapter 20 and consolidate
Being scheduled on support 1 not overturn, technique adapter is fixing draws convenient layout.
Cylinder both sides arrange rotary shaft 4 and hollow extraction axle 22, and rotation axis support 19 is arranged on
On support 1, decelerator 3 is arranged on speed reducer base 2 and is connected with rotary shaft 4, converter 5
Controlling motor 6 drives decelerator 3 to make tipper overturn.
This structure i.e. has flat board hollow filter plate 16, has again tapered hollow screen plate 15, also has
Cylinder hollow filter plate 17 and filter tube 14；And filter tube 14 is i.e. arranged in tapered hollow mistake
Filter plate side, is further placed in cylinder hollow filter plate side, various filter medium reasonable combination,
Significantly increase the filter area in single filtration zone and can discharge again solid slag smoothly.
Shaft coupling, convenient installation are set between power source motor 6 and decelerator 3 and rotary shaft 4；
Turbine worm decelerator preferentially selected by decelerator, possesses locked and energy positioning turning angle.
Embodiment 2.As in figure 2 it is shown, the difference of embodiment 2 and embodiment 1 is:
Cancel in the middle of flat board hollow filter plate 16 and tapered hollow screen plate 15 cylinder hollow filter plate,
Cancel filter tube；For some solid particle material, may adhere between filter tube, make
Discharging is the most thorough；Between flat board hollow filter plate and tapered hollow screen plate, gapless is set, and
Accumulate solid particle in anti-space here or product is impacted by long bacterium.
Embodiment 3.As it is shown on figure 3, the difference of embodiment 3 and embodiment 1 is:
Only retain flat board hollow filter plate 16.
Embodiment 4.As shown in Figure 4, embodiment 3 is with the difference of embodiment 1:
Only retain flat board hollow filter plate 16, and for embodiment 3, due to two pieces of base plates
Setting space is less, and many straight tubes region, territory, slag storage region than Fig. 3, the territory, slag storage region, relative deposits slag
Amount can be more.
Embodiment 5.As it is shown in figure 5, the difference of the present embodiment and embodiment 1 is:
Only 1 filtration zone, and only 1 block flat board hollow filter plate 16, one of them taper
Cylinder as filtration zone, another one only as counterweight or/and outer rule symmetry is used.
Embodiment 6.As shown in Figure 6, the present embodiment is dissymmetrical structure, and conical shell is only
1, and only 1 filtration zone in conical shell, opposed configuration is simple, manufacturing cost
Minimum, configuration rotary shaft and hollow extraction axle and support, motor, decelerator etc..With embodiment
The shape differentiation of 5 is less 1 conical shell.And filter and can configure flat board hollow as required
Screen plate and/or tapered hollow screen plate and/or cylinder hollow filter plate and/or filter tube.
Embodiment 7.As it is shown in fig. 7, the present embodiment is symmetrical structure, conical shell 2,
Can be 1 filtration zone or 2 filtration zones, configure rotary shaft and hollow extraction axle and prop up
Frame, motor, decelerator etc..It is many 1 conical shells with the shape differentiation of embodiment 6.And
Filtration can configure as required flat board hollow filter plate and/or tapered hollow screen plate and/or
Cylinder hollow filter plate and/or filter tube.
Embodiment 8.As shown in Figure 8, the present embodiment is dissymmetrical structure, conical shell 3,
Can be 1 filtration zone or 2 filtration zones or 3 filtration zones, configuration rotary shaft and
Hollow extraction axle and support, motor, decelerator etc..It is many 1 with the shape differentiation of embodiment 7
Individual conical shell.Filter progress, washing procedure, muck discharging process can be entered by control program
Full-automatic continual continuous operation of row controls.And filter and can configure flat board hollow mistake as required
Filter plate and/or tapered hollow screen plate and/or cylinder hollow filter plate and/or filter tube.
Embodiment 9.As it is shown in figure 9, the present embodiment is symmetrical structure, conical shell 4,
Can be 1 filtration zone or 2 filtration zones or 3 filtration zones or 4 filtration zones,
Configuration rotary shaft and hollow extraction axle and support, motor, decelerator etc. share, integration process
Height, equipment service efficiency is more preferably.It is many 1 pair of conical shells with the shape differentiation of embodiment 7.
Between filter progress, washing procedure, muck discharging process can being carried out the most not by control program
Disconnected runs control continuously.And filter and can configure flat board hollow filter plate and/or cone as required
Shape hollow filter plate and/or cylinder hollow filter plate and/or filter tube.
Embodiment 10.As shown in Figure 10, the present embodiment is dissymmetrical structure, conical shell 5
Part, can be 1 filtration zone or 2 filtration zones or 3 filtration zones or 4 filtrations
Region or 5 filtration zones, configuration rotary shaft and hollow extraction axle and support, motor, deceleration
Devices etc. share, and integration process is high, and equipment service efficiency is more preferably.Profile district with embodiment 8
It not many 1 pair of conical shells.By control program can to filter progress, washing procedure, go out
Slag operation carries out full-automatic continual continuous operation and controls.And filtration can configure flat as required
Plate hollow filter plate and/or tapered hollow screen plate and/or cylinder hollow filter plate and/or
Filter tube.
Embodiment 11.As shown in figure 11, the present embodiment is symmetrical structure, conical shell 6,
Can be 1 filtration zone or 2 filtration zones or 3 filtration zones or 4 filtration zones
Or 5 filtration zones or 6 filtration zones, configuration rotary shaft and hollow extraction axle and support,
Motor, decelerator etc. share, and integration process is high, and equipment service efficiency is more preferably.With embodiment
The shape differentiation of 9 is many 1 pair of conical shells.By control program can to filter progress, wash
Wash operation, muck discharging process carries out full-automatic continual continuous operation and controls.And filtration can basis
Need to configure flat board hollow filter plate and/or tapered hollow screen plate and/or cylinder hollow mistake
Filter plate and/or filter tube.
Claims (10)
1. powder body filtration washing many tapers tipper, it is characterised in that: include support (1)
With cylinder (7), cylinder (7) both sides are respectively through rotary shaft (4) and hollow extraction axle (22)
Being fixed on support (1), support (1) sidepiece is provided with actuating unit, actuating unit and rotation
Axle (4) connects, and hollow extraction axle (22) is provided with extraction adapter through fixed hub (21)
(20)；It is provided with one or more conical shell (11) through flange (8) on described cylinder (7),
Conical shell (11) and cylinder (7) enclose region in be provided with filter medium, filter medium
It is connected with drawing adapter (20).
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
It is: described actuating unit includes being fixed on the deceleration on support (1) through reducer pedestal (2)
Device (3), the output shaft of decelerator (3) connects motor (6), and motor (6) connects change
Frequently device (5), the output shaft of described decelerator (3) is connected with rotary shaft through shaft coupling.
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
It is: described filter medium is integrally fixed at flat board hollow filter plate (16) on base plate (9)
And/or cylinder hollow filter plate (17) that is fixed on cylinder (7) and/or be fixed on taper
Tapered hollow screen plate (15) on cylinder (11).
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
It is: be provided with in described conical shell (11) and arrange tapered filter tube (14).
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
It is: be provided with in described cylinder and arrange rounded filter tube.
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
Being: the bevel angle of described conical shell (11) is ∠ β, (180 ° of-∠ β)/2 ＞ pacifies
Breath angle.
Powder body filtration washing many tapers tipper the most according to claim 6, its feature
It is: described ∠ β=60 ° or ∠ β=90 °.
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
It is: described filter medium is the sintered plate of once sintered molding.
Powder body filtration washing many tapers tipper the most according to claim 1, its feature
Be: described filter medium thickness direction be provided with stream cleaner liquid passage, resistance to pressure reduction 0.6～
The normal pressure of 1.6MPa or counter-pressure.
10. overturn according to the many tapers of powder body filtration washing described in any one of claim 1-9
Machine, it is characterised in that: described actuating unit passes through touch screen/PLC system and/or DCS system
And/or public control machine and/or mobile phone A PP software realize filtering, wash, be dried, slag tap continuous
Run without interruption.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610392503.7A CN105903254B (en) | 2016-06-03 | 2016-06-03 | A kind of more taper tippers of powder filtration washing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610392503.7A CN105903254B (en) | 2016-06-03 | 2016-06-03 | A kind of more taper tippers of powder filtration washing |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105903254A true CN105903254A (en) | 2016-08-31 |
| CN105903254B CN105903254B (en) | 2018-01-05 |
Family
ID=56743283
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610392503.7A Active CN105903254B (en) | 2016-06-03 | 2016-06-03 | A kind of more taper tippers of powder filtration washing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105903254B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0372203A1 (en) * | 1988-12-05 | 1990-06-13 | Kreyenborg Verwaltungen Und Beteiligungen Kg | Filtration device for extrusion presses and injection moulds |
| CN2058619U (en) * | 1989-04-27 | 1990-06-27 | 上海华元干燥技术工程公司 | Turning-over tank filter with sealing cap |
| CN1442230A (en) * | 2002-03-01 | 2003-09-17 | 过志昌 | Horizontal reacting filtering drying machine and its method |
| CN101385962A (en) * | 2008-10-07 | 2009-03-18 | 浙江大学 | Reaction filter drying apparatus with compression membrane |
| CN202538452U (en) * | 2012-02-28 | 2012-11-21 | 福建省长汀金龙稀土有限公司 | Positive pressure filter device applied to rare-earth powder washing |
| CN205659475U (en) * | 2016-06-03 | 2016-10-26 | 浙江东瓯过滤机制造有限公司 | Many topers of powder filtration washing upset machine |
-
2016
- 2016-06-03 CN CN201610392503.7A patent/CN105903254B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0372203A1 (en) * | 1988-12-05 | 1990-06-13 | Kreyenborg Verwaltungen Und Beteiligungen Kg | Filtration device for extrusion presses and injection moulds |
| CN2058619U (en) * | 1989-04-27 | 1990-06-27 | 上海华元干燥技术工程公司 | Turning-over tank filter with sealing cap |
| CN1442230A (en) * | 2002-03-01 | 2003-09-17 | 过志昌 | Horizontal reacting filtering drying machine and its method |
| CN101385962A (en) * | 2008-10-07 | 2009-03-18 | 浙江大学 | Reaction filter drying apparatus with compression membrane |
| CN202538452U (en) * | 2012-02-28 | 2012-11-21 | 福建省长汀金龙稀土有限公司 | Positive pressure filter device applied to rare-earth powder washing |
| CN205659475U (en) * | 2016-06-03 | 2016-10-26 | 浙江东瓯过滤机制造有限公司 | Many topers of powder filtration washing upset machine |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105903254B (en) | 2018-01-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108479609A (en) | Curing molding equipment material stirring device | |
| CN208728159U (en) | A kind of quartz sand automatic pickling system | |
| CN104096405B (en) | A kind of effective filter for steel rolling Treatment of Sludge | |
| CN106799351A (en) | A kind of dehumidifying dedusting device for myotonin processing | |
| CN205659475U (en) | Many topers of powder filtration washing upset machine | |
| CN206569526U (en) | A kind of material anti-caking homogenizer | |
| CN109747038A (en) | Batch mixer | |
| CN109650619A (en) | A kind of centrifugal chemical engineering sewage recycling and reusing device | |
| CN105903254A (en) | Multi-cone-shaped upender for filtering and washing powder | |
| CN206287350U (en) | A kind of non-baking brick machine agitating device | |
| CN108543464A (en) | A kind of bi-motor mixed stirring device | |
| CN206168420U (en) | Reaction unit for chemical production | |
| CN205815535U (en) | A kind of scalable chemical material stirring device | |
| CN209679926U (en) | A kind of agitator of medicine company | |
| CN216604198U (en) | Feeding device of filter press | |
| CN204338070U (en) | A kind of efficient planet-style wheel roller mixer | |
| CN110000014A (en) | A kind of heavy duty detergent hydrocyclone with anti-blockage function | |
| CN211384093U (en) | Printing ink production is with filter screen of multilayer adsorbed impurity | |
| CN209141130U (en) | A kind of novel single horizontal axis pressure concrete mixer | |
| CN211782624U (en) | Multilayer vibration dryer | |
| CN213918874U (en) | Honeycomb ceramic pug vacuum pug mill | |
| CN209668942U (en) | A kind of sewage-treatment plant | |
| CN207412893U (en) | For the agitating device in sewage disposal | |
| CN207221795U (en) | A kind of veterinary drug special efficient mixing arrangement | |
| CN209792130U (en) | Washing machine for post-treatment of cobaltosic oxide synthetic material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: A kind of powder filtering washing multi cone turnover machine Effective date of registration: 20221213 Granted publication date: 20180105 Pledgee: Agricultural Bank of China Limited Lishui Development Zone Sub branch Pledgor: ZHEJIANG DONGOU FILTER MANUFACTURING Co.,Ltd. Registration number: Y2022330003660 |