CN105057125A - Hu's cyclone separation device - Google Patents
Hu's cyclone separation device Download PDFInfo
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- CN105057125A CN105057125A CN201510518473.5A CN201510518473A CN105057125A CN 105057125 A CN105057125 A CN 105057125A CN 201510518473 A CN201510518473 A CN 201510518473A CN 105057125 A CN105057125 A CN 105057125A
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Abstract
A Hu's cyclone separation device comprises a cylinder. The upper portion of the cylinder is provided with a feed chamber and a feed inlet, and the lower portion of the cylinder is provided with a slag storage chamber and a slag outlet. The feed chamber and the slag storage chamber are connected with the cylinder through flanges respectively. A plurality of outer cyclone guide plates are arranged on the upper portion of the inner wall of the cylinder. The upper end of a medium discharge pipe penetrates through an inner supporting pipe and is connected with the flanges, and the lower portion of the medium discharge pipe penetrates through a supporting pipe and the slag storage chamber. A plurality of inner cyclone guide plates are arranged on the periphery of the upper portion of the inner wall of the medium discharge pipe. A plurality of cyclone breaking plates are arranged at the bottom of the cylinder. The outer cyclone guide plates and the inner cyclone guide plates are opposite in rotation direction, so that cyclones in opposite directions are formed, and media are subjected to density difference separation under action of dual centrifugal force. The Hu's cyclone separation device is far superior to existing cyclone separation technologies, and has the characteristics of low resistance, good separation effect, convenient and rapid maintenance, small size and low cost. The Hu's cyclone separation device can be applied to various industries and is the most ideal device for solid-liquid separation, solid-gas separation and liquid-gas separation.
Description
Technical field
The present invention relates to Physical Separation Technology field, particularly cyclone separation process field, be mainly used in the three phase separation of material, Ru Shui is separated with sand, air and dust separation, and air is separated with water, and oil is separated etc. with gas.
Background technology
Environmental protection is attached great importance to, and the application of solid-liquid, solid and gas, liquid gas isolation technics is very extensive, ubiquity.There are some shortcomings, particularly cyclone separation process in existing Physical Separation Technology, some separating effects are bad, some separator complex structures.Although constantly there is new cyclonic separation patent to come out, all do not solve the puzzlement problem of cut diameter, when radial velocity increases, discharge pipe diameter reduces, good separating effect when grain density is large.But when grain density is constant, discharge pipe diameter reduces, and overall flow reduces, then radial velocity reduces, and at this moment resistance is large on the contrary, and separating effect is bad.This is the proposition of a contradiction; When the Disjoint Cone angle of separator becomes little, manufacture difficulty increases.So existing cyclone separation process is just used as first order primarily efficient filter, and because cyclone separation process is complicated, parameter is not right a little, and separating effect difference is just very large, the trend that cyclone separation process has the technology that is filtered to replace.
Summary of the invention
The technical problem to be solved in the present invention is the problem solving cut diameter, namely during cyclonic separation, when grain density is constant, discharge pipe enlarged diameter, during overall increased flow capacity, also can reach desirable separating effect, both retain the advantage of existing cyclone separation process, the shortcoming of existing cyclone separation process can be overcome again, a kind of brand-new Hu Shi cyclone separation device is provided.
Technical scheme of the present invention is, Hu Shi cyclone separation device, comprises cylinder, and cylinder top is provided with feed space, and dreg chamber is established in bottom, uses Flange joint cylinder respectively.Upper end inwall in cylinder is provided with several piece contour stealth deflector, and medium discharge duct upper end is through upper support short tube adpting flange, and its underpart is through lower support pipe and dreg chamber; Medium discharge duct upper inside wall week is along being provided with several inward eddy deflector; Be provided with several piece at cylinder bottom and break rotating plate; Contour stealth deflector is contrary with inward eddy deflector direction of rotation.Impeller guide plate forms the contrary eddy flow in direction with under the effect of inward eddy deflector outside, and medium carries out density contrast separation under the effect of dual centrifugal force.
Feed space is cone, is fixed on above flange; Feed space upper end connects a medium and enters pipe, and medium enters pipe upper end a flange, and impeller guide plate central upper is provided with a drag reduction cone and is placed in feed space middle and lower part outside.
Dreg chamber is cone, and dreg chamber center has a medium discharge duct to stretch out downwards, the end sealing of medium discharge duct, and dreg chamber upper end is provided with flange, with cylinder lower end Flange joint; Scum pipe and valve is provided with on the downside of dreg chamber.
The lower circle of drag reduction cone is connected with an inner support tube, and contour stealth deflector both sides are connected with the outer wall of inner support tube and the inwall of cylinder respectively; Broken rotating plate both sides are connected with the outer wall of support short tube of cylinder bottom and the inwall of cylinder respectively; Broken rotating plate stops eddy flow to the material after separation, prevents separator secondary from entering medium discharge duct.
The present invention has following good effect, and owing to adopting inside and outside incorgruous cyclone separation process, medium carries out density contrast separation under the effect of dual centrifugal force, and separating effect is very good.Contrast with existing filtering technique, without backwash, do not block.Contrast with existing cyclone separation process, separating effect is better, and particle separation diameter is less, and manufacture difficulty is lower, and consumptive material is few.
Accompanying drawing explanation
Fig. 1, Hu Shi cyclone separation device structural representation of the present invention.
Fig. 2, inside and outside incorgruous cyclonic separation schematic diagram.
Fig. 3, contour stealth deflector connection diagram.
Fig. 4, broken rotating plate connection diagram.
In figure: 1-main cylinder, 2-medium enters assembly, and 3-medium discharges assembly, 11-cylinder, 12-flange I, 13-drag reduction cone, 14-contour stealth deflector, 15-breaks rotating plate, 16-lower support short tube, 17-supports short tube, 21-feed space, and 22-medium enters pipe, 23 flange II, 24-flange I, 31-inward eddy deflectors, 32 flange I, 33 dreg chamber, 34-medium discharge duct, 35-flange II, 36-scum pipe, 37-residual cake valve.
Detailed description of the invention
Below by embodiment, and by reference to the accompanying drawings the present invention program is illustrated further:
The cyclone separation device of Hu Shi shown in Fig. 1, this device comprises a main cylinder 1, and main cylinder 1 top is provided with medium and enters assembly 2, and main cylinder 1 bottom is provided with medium and discharges assembly 3.Main cylinder 1 comprises a cylinder 11, cylinder 11 two ends are respectively provided with flange 12, contour stealth deflector 14 is provided with in cylinder 11 upper inside wall, impeller guide plate 14 central upper is provided with drag reduction cone 13 outside, the inner ring of impeller guide plate 14 is provided with support short tube 17 outside, the upper end of upper support short tube 17 and the lower lap welding of drag reduction cone 13 connect, and contour stealth deflector 14 is connected with the outer wall of upper support short tube 17 and the inwall of cylinder 11.Medium discharge duct 34 is positioned at dreg chamber 33 center, and medium discharge duct 34 epimere inwall is provided with plural block inward eddy deflector 31.Be provided with brokenly rotating plate 15 in cylinder 11 inwall lower end, be provided with lower support short tube 16 at the inner ring of broken rotating plate 15, medium discharge duct 34 passes dreg chamber 33 from lower support short tube 16, and broken rotating plate 15 welds with the outer wall of lower support short tube 16 and the inwall of cylinder 11.
Medium enters assembly 2 and comprises a medium and enter pipe 22, and medium enters pipe 22 upper end and is provided with flange 23, and it is taper feed space 21 that medium enters pipe 22 lower end, and feed space 21 lower end is provided with flange 24 and is connected with main cylinder 11.
Medium is discharged assembly 3 and is comprised a taper dreg chamber 33, medium discharge duct 34 is positioned at dreg chamber 33 center, medium discharge duct 34 epimere inwall is provided with plural block inward eddy deflector 31, the exit, lower end of medium discharge duct 34 is provided with flange 35, and dreg chamber 33 upper end flange 32 is connected with the flange 12 of main cylinder 11.Be provided with scum pipe 36 in the side of dreg chamber 33, scum pipe 36 lower end is provided with residual cake valve 37.
Fig. 2 represents that inside and outside eddy flow direction is contrary.Contour stealth deflector 14 rotates clockwise, and inward eddy deflector 31 counter-clockwise direction is rotated, and produces the contrary incorgruous eddy flow in direction in cylinder 11.
Fig. 3, Fig. 4 can find out, contour stealth deflector 14 both sides are connected with the outer wall of upper support short tube 17 and the inwall of cylinder 11 respectively; Broken rotating plate 15 both sides are connected with the outer wall of the lower support short tube 16 of cylinder bottom and the inwall of cylinder (11) respectively.
The course of work
Medium for being separated enters pipe 22 by medium and enters feed space 21, evenly enter contour stealth deflector 14 by drag reduction cone 13 and form contour stealth, enter cylinder 11 again, force under inward eddy deflector 31 on medium discharge duct 34 top acts on to form the contrary inward eddy in direction, interior, the operation of Hu Shi cyclonic separation is carried out under outer incorgruous cyclonic action, due to interior, contour stealth direction is contrary, form one and be separated enveloping surface, the material that medium Midst density is larger can only flow through brokenly downwards rotating plate 15 along cylinder 11 inwall, no longer form eddy flow, be deposited on dreg chamber 33, discharge through residual cake valve 37 timing again, the material that density is less is then discharged from medium discharge duct 34 lower end, thus form a continuous print Hu Shi cyclonic separation process.
The application employs main cylinder assembly, medium enters assembly, medium discharges the terms such as assembly, use these terms to be only used to describe more easily and explain the flesh and blood of the application, they are construed to the restriction that any one adds is all contrary with the spirit of this patent.Described specific embodiment, be only illustrating this patent, do not limit the scope of present patent application, those skilled in the art does various Revision and supplement to described specific embodiment, or adopt similar mode substitute, all contain by present techniques.
Claims (4)
1. Hu Shi cyclone separation device, comprise cylinder (11), cylinder top is provided with feed space (21) and charging aperture, dreg chamber (33) and slag notch are established in bottom, be connected with cylinder (11) with flange respectively, it is characterized in that: be provided with several piece contour stealth deflector (14) in cylinder (11) upper inside wall, medium discharge duct (34) upper end is through inner support tube (17) adpting flange (12), and its underpart is through stay pipe (16) and dreg chamber (33); Medium discharge duct (34) upper inside wall week is along being provided with several inward eddy deflector (31); Be provided with several piece in cylinder (11) bottom and break rotating plate (15); Contour stealth deflector (14) is contrary with inward eddy deflector (31) direction of rotation; Impeller guide plate forms the contrary eddy flow in direction with under the effect of inward eddy deflector outside, and medium carries out density contrast separation under the effect of dual centrifugal force.
2. Hu Shi cyclone separation device according to claim 1, is characterized in that: feed space (21) is cone, is fixed on above flange (24); Feed space (21) upper end connects a medium and enters pipe (22), and medium enters pipe (22) upper end a flange (23); Contour stealth deflector (14) central upper is provided with a drag reduction cone (13) and is placed in feed space (21) middle and lower part.
3. Hu Shi cyclone separation process device according to claim 1, it is characterized in that, dreg chamber (33) is cone, dreg chamber (33) center has a medium discharge duct (34) to stretch out downwards, the end sealing of medium discharge duct (34) connects cylinder (11) upper flanges, and dreg chamber (33) lower end is provided with flange (35); Dreg chamber (33) side is provided with scum pipe (36) and valve (37).
4. Hu Shi cyclone separation process device according to claim 1, it is characterized in that: the lower circle of drag reduction cone (13) is connected with an inner support tube (17), contour stealth deflector (14) both sides are connected with the outer wall of inner support tube (17) and the inwall of cylinder (11) respectively; Broken rotating plate (15) both sides are connected with the outer wall of the support short tube (16) of cylinder bottom and the inwall of cylinder (11) respectively; Broken rotating plate stops eddy flow to the material after separation, prevents separator secondary from entering medium discharge duct (34).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510518473.5A CN105057125A (en) | 2015-08-21 | 2015-08-21 | Hu's cyclone separation device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510518473.5A CN105057125A (en) | 2015-08-21 | 2015-08-21 | Hu's cyclone separation device |
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| CN105057125A true CN105057125A (en) | 2015-11-18 |
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| CN201510518473.5A Pending CN105057125A (en) | 2015-08-21 | 2015-08-21 | Hu's cyclone separation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828429A (en) * | 2021-09-18 | 2021-12-24 | 浙江工业大学 | System and process for deacidifying superfine powder |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2037264U (en) * | 1988-03-30 | 1989-05-10 | 刘中铭 | Bag type axial flow cyclone duster |
| JP2000140708A (en) * | 1998-08-31 | 2000-05-23 | Mazda Motor Corp | Separator for turbid material |
| CN1513575A (en) * | 2003-07-28 | 2004-07-21 | 西南石油学院 | Vertical eyclone filtering dust collector |
| CN201366381Y (en) * | 2009-01-13 | 2009-12-23 | 中国石油大学(华东) | Combined type cyclone separator for purifying natural gas |
| CN201516416U (en) * | 2009-10-23 | 2010-06-30 | 山东青州微粉有限公司 | Inverted airflow seal device used for airflow classer |
| CN102343310A (en) * | 2011-08-17 | 2012-02-08 | 中国石油大学(北京) | Shunting core pipe and single-pipe cyclone separator with same |
| CN204247404U (en) * | 2014-11-18 | 2015-04-08 | 李焱 | Double rotational directions cyclone dust collectors |
| CN205236214U (en) * | 2015-08-21 | 2016-05-18 | 胡建军 | Hu shi hydrocyclone separation device |
-
2015
- 2015-08-21 CN CN201510518473.5A patent/CN105057125A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2037264U (en) * | 1988-03-30 | 1989-05-10 | 刘中铭 | Bag type axial flow cyclone duster |
| JP2000140708A (en) * | 1998-08-31 | 2000-05-23 | Mazda Motor Corp | Separator for turbid material |
| CN1513575A (en) * | 2003-07-28 | 2004-07-21 | 西南石油学院 | Vertical eyclone filtering dust collector |
| CN201366381Y (en) * | 2009-01-13 | 2009-12-23 | 中国石油大学(华东) | Combined type cyclone separator for purifying natural gas |
| CN201516416U (en) * | 2009-10-23 | 2010-06-30 | 山东青州微粉有限公司 | Inverted airflow seal device used for airflow classer |
| CN102343310A (en) * | 2011-08-17 | 2012-02-08 | 中国石油大学(北京) | Shunting core pipe and single-pipe cyclone separator with same |
| CN204247404U (en) * | 2014-11-18 | 2015-04-08 | 李焱 | Double rotational directions cyclone dust collectors |
| CN205236214U (en) * | 2015-08-21 | 2016-05-18 | 胡建军 | Hu shi hydrocyclone separation device |
Non-Patent Citations (2)
| Title |
|---|
| 张裕萍: "《流体输送与过滤操作实训》", 31 March 2006, 化学工业出版社 * |
| 邱明等: "《摩擦学原理与设计》", 31 August 2013, 国防工业出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828429A (en) * | 2021-09-18 | 2021-12-24 | 浙江工业大学 | System and process for deacidifying superfine powder |
| CN113828429B (en) * | 2021-09-18 | 2024-03-19 | 浙江工业大学 | System and process for deacidifying ultrafine powder |
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Application publication date: 20151118 |