CN110124429A - A kind of powder collecting vessel - Google Patents
A kind of powder collecting vessel Download PDFInfo
- Publication number
- CN110124429A CN110124429A CN201910424837.1A CN201910424837A CN110124429A CN 110124429 A CN110124429 A CN 110124429A CN 201910424837 A CN201910424837 A CN 201910424837A CN 110124429 A CN110124429 A CN 110124429A
- Authority
- CN
- China
- Prior art keywords
- outer cylinder
- powder collecting
- collecting vessel
- inner cylinder
- powder
- 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.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
- B01D45/16—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Cyclones (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
The invention discloses a kind of powder collecting vessels, it is poor to solve existing powder collection system there are effectiveness of classification, the problem of being difficult to effectively to collect Subnano-class superfine powder below, including outer cylinder, the powder collecting tank being connect with outer cylinder discharge port, to the closed cover board of progress at the top of outer cylinder, outer cylinder side is connected with feed pipe, the other side is connected with discharge pipe, the inner cylinder that sandwich is formed with outer cylinder is coaxially arranged in outer cylinder, inner cylinder is connected to feed pipe, inner cylinder is internally provided with blade group, blade group includes at least two grade blades, motor is provided with above cover board, with the sealing element of motor power output end transmission connection, sealing element extends to inner cylinder and is fixedly connected with blade group, setting is connected with vacuum elements between outer cylinder discharge port and powder collecting tank.The powder collecting vessel of the present invention using the above structure can be realized the classification to specified particle diameter and collect, do not need strainer and blowback system, be applicable to sealing and circulating or need the system of protective gas.
Description
Technical field
The invention belongs to powder collection devices, and in particular to a kind of powder collecting vessel.
Background technique
Powder classification collection mode is broadly divided into physics sedimentation, cyclonic separation at present, cloth bag is collected, strainer is collected etc..Object
Reason sedimentation is to carry powder by air-flow to follow the bulky grain of air motion first to settle due to the effect of gravity, is sunk after little particle
Drop, and then realize that the classification of powder is collected, but this method is very limited to the effectiveness of classification of powder, and it is larger out to be only capable of sub-argument
Particle；Cyclone collection is to utilize the cyclonic air flow formed in air-flow cyclone collector, by centrifugal force, settle bulky grain,
For little particle in vortex center as ascending air enters next stage collection device, cyclone classified device can distinguish physics sedimentation cannot
The fine powder of differentiation, but the precision of cyclone classified collection is controlled at most in micron dimension, can not achieve to superfine powder
Classification and collection；It is using the reticular structure of polymer fiber material itself formation as classification that cloth bag, which is collected, and strainer is collected
Collection device using the material of different mesh diameters, and then achievees the purpose that classification is collected according to the different partial size of powder, but
It is since dust can block mesh, it is therefore desirable to which blowback system will also regularly replace screen material, and current screen material
It is unsatisfactory to the collecting effect of superfine powder, the limit is collected in submicron order, and grading effect is bad, higher operating costs.
Summary of the invention
For existing powder collection system, that there are effectiveness of classification is poor, it is difficult to effectively collect Subnano-class superfine powder below
The problem of, the present invention provides a kind of powder collecting vessels.Sandwich is formed in collecting vessel by the way that inner cylinder is added, on inner cylinder top
Portion is formed different added with the blade for generating eddy airstream under the drive of speed regulating motor according to the shape of blade and revolving speed
Eddy airstream will make flow area and quiescent centre that vortex is formed in collecting vessel, powder due to the limitation of inner tube structure and shape
Feed pipe passes through quiescent centre and enters eddy airstream area, and under the drive of air-flow, dust-containing air stream is shrunk to the air column of rotation, and big
Grain is collided in collecting vessel inner cylinder inner wall due to the effect of centrifugal force, then falls into collecting tank along inner wall, little particle is with air-flow
Downward spiral movement.By adjusting the dimensional parameters of motor speed, blade construction and collecting vessel interior bucket, of collection can choose
Grain partial size.
The present invention to achieve the above object, is achieved through the following technical solutions:
A kind of powder collecting vessel, including outer cylinder, the powder collecting tank being connect with outer cylinder discharge port, closed to carrying out at the top of outer cylinder
Cover board, the outer cylinder side are connected with feed pipe, and the other side is connected with discharge pipe, it is characterised in that coaxial arrangement in the outer cylinder
There is the inner cylinder that sandwich is formed with outer cylinder, the inner cylinder is connected to feed pipe, and the inner cylinder is internally provided with blade group, institute
Stating blade group includes at least two grade blades, motor is provided with above the cover board, be sequentially connected with motor power output end it is close
Sealing, the sealing element extend to inner cylinder and are fixedly connected with blade group, are arranged between the outer cylinder discharge port and powder collecting tank
It is connected with vacuum elements.
In the above-mentioned technical solutions, the inner cylinder includes upper straight tube, centrum and the lower straighttube for being sequentially connected sealing, it is described on
The caliber of straight tube is greater than the caliber of lower straighttube.
In the above-mentioned technical solutions, top setting of the blade group in upper straight tube, feed pipe pass through charging pipe fitting
It is connected to upper straight tube.
In the above-mentioned technical solutions, it is shifted to install up and down between every grade blade.
In the above-mentioned technical solutions, the gap settings such as flabellum of the flabellum of an every grade blade grade blade adjacent thereto.
In the above-mentioned technical solutions, the motor is adjustable speed motor.
In the above-mentioned technical solutions, the sealing element is magnetic fluid seal.
In the above-mentioned technical solutions, shaft one end in the magnetic fluid seal is connected to motor, and the other end passes through lid
Plate extends to inner cylinder and is fixedly connected with blade group.
In the above-mentioned technical solutions, the discharge port of the outer cylinder is conical opening.
In the above-mentioned technical solutions, the vacuum elements include the level-one Hygiene Ball Valve being successively tightly connected, the first pumping
Pipe, second level Hygiene Ball Valve, the second exhaust tube, outer cylinder discharge port are connect with level-one Hygiene Ball Valve, powder collecting tank and the second pumping
Pipe connection.
In conclusion by adopting the above-described technical solution, the present invention has the following advantages and beneficial effects:
Powder collecting vessel of the invention is novel in design, is skillfully constructed, can particle classifying to different-grain diameter and collection, it is especially right
The classification and collection of submicron order and nano level superfine powder.
Powder collecting vessel of the invention is not necessarily to strainer without vulnerable part, can be avoided and cloth bag or strainer collection occurs largely
The phenomenon that powder solid is adsorbed by strainer does not need to be equipped with many and diverse blowback system yet, is applicable to sealing circulation or needs
The system for wanting protective gas.
Detailed description of the invention
Fig. 1 is overall structure diagram of the invention.
Fig. 2 is inner tube structure schematic diagram of the invention.
Fig. 3 is the overlooking structure diagram that blade group of the present invention rotates under motor effect.
Fig. 4 is the wherein level-one blade side structure schematic view in the present invention.
Wherein: 1, outer cylinder, 2, inner cylinder, 2-1, upper straight tube, 2-2, centrum, 2-3, lower straighttube, 3, feed pipe, 4, discharge pipe,
5, cover board, 6, sealing element, 7, motor cabinet, 8, motor, 9, interior tube stent, 10, charging pipe fitting, 11, level-one Hygiene Ball Valve, 12,
Second level Hygiene Ball Valve, the 13, first exhaust tube, the 14, second exhaust tube, 15, powder collecting tank, 16, one grade blade, 17, second level leaf
Piece, 18, upper bolt hole, 19, lower bolt hole.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to the accompanying drawings and embodiments, right
The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and
It is not used in the restriction present invention.
As shown in Figure 1, a kind of powder collecting vessel, including outer cylinder, it is arranged in outer cylinder and is formed in sandwich with outer cylinder
Cylinder.Inner barrel and outer barrel is prepared using stainless steel material.
The top opening of outer cylinder, is closed by cover board, and cover board is connect by ring flange with outer cylinder, is sealed with O-ring.
The side of outer cylinder is welded with the feed pipe extended in outer cylinder, and feed pipe is connected to by feeding pipe connector with inner cylinder, feed pipe
Connector can be to be flexible coupling (hose adds anchor ear) or Hard link (clip).The outer cylinder other side is welded with discharge pipe.Outer cylinder goes out
Material mouth is connected to powder collecting tank, is slid for convenience of powder particle into powder collecting tank, discharge port uses vertebral body structure, centrum knot
Structure is connect by ring flange with outer cylinder, is sealed by O-ring.
Setting is connected with vacuum elements between outer cylinder discharge port and powder collecting tank, and vacuum elements include passing through clip successively
Level-one Hygiene Ball Valve, the first exhaust tube, second level Hygiene Ball Valve, the second exhaust tube being connected and fixed, it is close with silicagel pad between clip
Envelope.First exhaust tube and the second exhaust tube have the small ball of trachea, and discharge port is connect with level-one Hygiene Ball Valve, and powder is collected
Tank is connect with the second exhaust tube.
Motor cabinet and adjustable speed motor are provided with above outer cylinder, motor cabinet, which is fixed by screws in, to be collected on cover plate,
Motor is fixed by screws on motor cabinet.
As shown in Fig. 2, inner cylinder is tertiary structure, upper straight tube, centrum and lower straighttube including successively welded seal, inner cylinder is logical
It crosses interior tube stent and is arranged in outer cylinder, fixation is bolted.Upper straight tube inner top position is provided with blade group, blade group
For multilevel structure, including at least two grade blades, the series of blade can be adjusted as needed.The type of blade can be axis stream
One of formula, centrifugal, mixed-flow, vortex.As shown in figure 3, second level leaf may be selected in blade group using axial--flow blading
Piece, inferior clearance dislocation installation on the flabellum in two grade blades, a grade blade are located at two grade blades top, and the fan of a grade blade
Leaf diameter is greater than the flabellum diameter of two grade blades.One grade blade mainly generates downward spiral thrust, and two grade blades mainly generate
Eddy airstream.
Motor power output end is provided with sealing element, and shaft one end in sealing element is connect with motor drive, and the other end is worn
It crosses collection cover plate and stretches to inner cylinder, be fixedly connected with blade group, such sealing element is same by the power transmission of motor to inner cylinder
When outer cylinder is sealed, magnetic fluid seal can be used in sealing element.If dust collection bucket is it is not necessary that when sealing, sealing element can be used instead
Thrust bearing.As shown in figure 4, being provided with upper bolt hole and lower bolt hole in the vertical direction of blade axle sleeve, upper bolt hole is under
Bolt hole runs through axle sleeve in the horizontal direction, and corresponding bolt hole is provided in the shaft of sealing element, by bolt by blade and
Sealing element is fixedly connected, and guarantees that blade center is overlapped with the center of gravity of sealing element.
When motor works, inner cylinder provides fixed boundary condition to the air-flow that blade generates, and plays the role of duct, passes through
The dimensional parameters of inner cylinder are adjusted, can control the granularity of dust collected and quality.If a is the upper straight tube height of inner cylinder, b is inner cylinder
Upper straight tube diameter, c are the cone height of inner cylinder, and d is the diameter of inner cylinder lower straighttube, and e is inner cylinder lower straighttube height.The value of a is bigger,
Collision probability is bigger between dust, and the time of coarse powder centrifugation is bigger, is conducive to collect bulky grain；The value of d is smaller, and the value of c gets over senior general
The collision for reducing aggregate and barrel, increases the precision of classification；The value of e gets over senior general and to segment aggregate in eddy airstream tail portion
Residence time is longer, more grows up conducive to aggregate, and then collects the superfine powder of low-density.
The course of work of powder collecting vessel are as follows: driven by the motor, multistage blade high speed rotation is formed inside inner cylinder
Eddy airstream, the inside of inner cylinder are eddy airstream area, and the interlayer between collecting vessel outer cylinder and collecting vessel inner cylinder is quiescent centre, contain powder
Last air-flow enters eddy airstream area, the distance of charging tube hub line a to grade blade by feed pipe under the effect of external circulating fan
Greater than feed tube diameter, but again as close as possible to a grade blade, eddy airstream band that the air-flow containing dust is formed in level-one blade
It is dynamic lower to enter eddy airstream area, and downward spiral is shrunk to the air column of rotation, bulky grain due to the effect of centrifugal force with inner cylinder
Inner wall collision, then fall into collecting tank along inner wall, little particle is moved downward with flow spiral, by adjust motor speed,
The dimensional parameters of blade construction and collecting vessel inner cylinder can choose the grain diameter of collection, and the powder without being collected is gone out
The negative pressure in air port sucks next stage collecting vessel, and in nano level superfine powder, air-flow containing powder enters eddy airstream area, and is formed
Air column is rotated, nano level superfine powder collides in air column, reunites, and air column bottom is contacted with collecting vessel inner cylinder cone discharge port mouth
Afterwards, eddy airstream periphery blocked rotation, aggregate in peripheral air stream with after the collision of collecting vessel inner cylinder inner wall because gravitational settling arrives
In collecting tank, eddy airstream center fine particle is moved along collecting vessel inner cylinder lower straighttube, after collecting vessel inner cylinder lower straighttube, by
Do not constrained by pipeline in air-flow, in downwardly direction gradually radial diffusion, to lose the constraint to powder, will height according to not
Partial size together, current density, the adjustment of powder density, cooperation adjustment air outlet diameter, so that circulating fan was formed in air outlet
Negative pressure is insufficiently resistant to the gravity of powder reuniting body itself, and the powder for losing constraint will be in air outlet quiescent centre below with gravity
Sedimentation, cleaning gas tream will enter quiescent centre at air outlet, return in circulating system from discharge pipe.
When powder is collected, level-one Hygiene Ball Valve and second level Hygiene Ball Valve are first closed, the first exhaust tube and second level are then unclamped
Clip between Hygiene Ball Valve, and second level Hygiene Ball Valve, the second exhaust tube, powder collecting tank are integrally moved into packing case.Installation
When collecting tank, if system needs inert gas or vacuum protection, needs first to extract the air in the first exhaust tube out, then open
Level-one Hygiene Ball Valve and second level Hygiene Ball Valve.The use of powder collecting tank is threadedly coupled, and other component is all using snapping connection, just
Just it dismantles.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within mind and principle.
Claims (10)
1. a kind of powder collecting vessel including outer cylinder, the powder collecting tank connecting with outer cylinder discharge port, is closed outer cylinder top
Cover board, the outer cylinder side is connected with feed pipe, and the other side is connected with discharge pipe, it is characterised in that coaxially sets in the outer cylinder
It is equipped with the inner cylinder that sandwich is formed with outer cylinder, the inner cylinder is connected to feed pipe, and the inner cylinder is internally provided with blade group,
The blade group includes at least two grade blades, be provided with above the cover board motor, with the transmission connection of motor power output end
Sealing element, the sealing element extend to inner cylinder and are fixedly connected with blade group, set between the outer cylinder discharge port and powder collecting tank
It sets and is connected with vacuum elements.
2. a kind of powder collecting vessel according to claim 1, it is characterised in that the inner cylinder includes being sequentially connected sealing
Upper straight tube, centrum and lower straighttube, the caliber of the upper straight tube are greater than the caliber of lower straighttube.
3. a kind of powder collecting vessel according to claim 2, it is characterised in that top of the blade group in upper straight tube
Setting, feed pipe are connected to by feeding pipe fitting with upper straight tube.
4. a kind of powder collecting vessel according to claim 1, it is characterised in that shifted to install up and down between every grade blade.
5. according to right want 4 described in a kind of powder collecting vessel, it is characterised in that the flabellum of every grade blade level-one leaf adjacent thereto
The gap settings such as the flabellum of piece.
6. a kind of powder collecting vessel according to claim 1, it is characterised in that the motor is adjustable speed motor.
7. a kind of powder collecting vessel according to claim 1, it is characterised in that the sealing element is magnetic fluid seal.
8. a kind of powder collecting vessel according to claim 7, it is characterised in that the shaft one in the magnetic fluid seal
End is connected to motor, and the other end extends to inner cylinder across cover board and is fixedly connected with blade group.
9. a kind of powder collecting vessel according to claim 1, it is characterised in that the discharge port of the outer cylinder is conical opening.
10. a kind of powder collecting vessel according to claim 1, it is characterised in that the vacuum elements include that successively sealing connects
Level-one Hygiene Ball Valve, the first exhaust tube, second level Hygiene Ball Valve, the second exhaust tube connect, outer cylinder discharge port and level-one Hygiene Ball Valve
Connection, powder collecting tank are connect with the second exhaust tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910424837.1A CN110124429B (en) | 2019-05-21 | 2019-05-21 | Powder collecting barrel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910424837.1A CN110124429B (en) | 2019-05-21 | 2019-05-21 | Powder collecting barrel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110124429A true CN110124429A (en) | 2019-08-16 |
| CN110124429B CN110124429B (en) | 2022-02-08 |
Family
ID=67572021
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910424837.1A Active CN110124429B (en) | 2019-05-21 | 2019-05-21 | Powder collecting barrel |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110124429B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114858967A (en) * | 2022-05-05 | 2022-08-05 | 殷柳 | Aluminum powder stability performance measuring device and method |
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| CN101541394A (en) * | 2006-11-30 | 2009-09-23 | 西湖朗维尤公司 | High-pressure separator |
| CN103987436A (en) * | 2011-10-06 | 2014-08-13 | 胡斯华纳有限公司 | Dust collector with constant suction force |
| CN104703706A (en) * | 2012-10-09 | 2015-06-10 | 纳诺控制股份公司 | Device for separation of particles from gas flow |
| CN106807310A (en) * | 2017-02-24 | 2017-06-09 | 绵阳市宏扬科技有限公司 | The equipment that a kind of discharge-induced explosion legal system takes nanometer powder |
-
2019
- 2019-05-21 CN CN201910424837.1A patent/CN110124429B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2920422Y (en) * | 2006-05-19 | 2007-07-11 | 金苗兴 | Dust eliminator set |
| CN101541394A (en) * | 2006-11-30 | 2009-09-23 | 西湖朗维尤公司 | High-pressure separator |
| CN103987436A (en) * | 2011-10-06 | 2014-08-13 | 胡斯华纳有限公司 | Dust collector with constant suction force |
| CN104703706A (en) * | 2012-10-09 | 2015-06-10 | 纳诺控制股份公司 | Device for separation of particles from gas flow |
| CN106807310A (en) * | 2017-02-24 | 2017-06-09 | 绵阳市宏扬科技有限公司 | The equipment that a kind of discharge-induced explosion legal system takes nanometer powder |
Non-Patent Citations (2)
| Title |
|---|
| 宋晓辉等编著: "《铝合金粉材生产技术》", 31 August 2008, 冶金工业出版社 * |
| 袁惠新主编: "《分离工程》", 31 January 2002, 中国石化出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114858967A (en) * | 2022-05-05 | 2022-08-05 | 殷柳 | Aluminum powder stability performance measuring device and method |
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| Publication number | Publication date |
|---|---|
| CN110124429B (en) | 2022-02-08 |
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