CN102228872A - Cyclone water-powder-air separator - Google Patents
Cyclone water-powder-air separator Download PDFInfo
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- CN102228872A CN102228872A CN 201110141791 CN201110141791A CN102228872A CN 102228872 A CN102228872 A CN 102228872A CN 201110141791 CN201110141791 CN 201110141791 CN 201110141791 A CN201110141791 A CN 201110141791A CN 102228872 A CN102228872 A CN 102228872A
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Abstract
The invention discloses a cyclone water-powder-air separator. The separator comprises: a cylindrical outer cylinder; an air discharging port, a liquid discharging port, an air inlet port and a powder discharging port arranged on the cylinder; a swirl eliminating plate, a lower separating plate, a material collecting arc plate, a middle separating plate and an upper separating plate arranged in a chamber formed by the cylinder; a cone-shaped inner cylinder respectively connected to a lower separating plate central hole, a material collecting arc plate central hole and a middle separating plate central hole, wherein the cone-shaped inner cylinder is arranged above the swirl eliminating plate, and an annular chamber is formed between the external wall of the cone-shaped inner cylinder and the internal wall of the cylindrical outer cylinder; four reversed-cone-shaped cyclone separator and a round distributor with an X-shaped flow deflector arranged between and communicate with the middle separating plate and the upper separating plate; a secondary condensing plate arranged on the bottom of the X-shaped flow deflector; and an air discharging pipe arranged on the center of each reversed-cone-shaped cyclone separator, wherein the four air discharging pipes communicate with the upper separating plate. The invention is suitable for the separating of water-powder-air mixtures, and the separation efficiency of the separator is high.
Description
Technical field
The present invention relates to a kind of cyclone type pigment air separation.The water dust that it both can be used as complete sucking type sweeping car separates use, also can be used for the separation of industrial pigment gas mixture, and the pigment gas in for example industrial mill water powder gas separation and the medicine separates.
Background technology
At present, cyclone separator is to be well known, and has obtained extensive use in industrial gas solid separation and environmental protection dedusting field.In this device, have the inside that the air of powder is tangentially introduced the cyclonic separation body, the form circumferential flow is moving in the shape of a spiral around the inner surface of cyclonic separation body for air, powder is separated from primary air under action of centrifugal force, and fall into the bottom of cyclonic separation body, and the air of cleaning leaves separator by the central gas outlet of cyclonic separation body, as patent: ZL00817415.6, ZL02135539.8ZL97197594.9 etc., the characteristics of these cyclone separators are, under the effect of blower fan, it can (be called for short the powder that enters in the cyclone separator: dust) separate from air-flow.They are not suitable for the separation of moisture pigment gas mixture, in separation process, water, dust and air three can't be separated respectively.Yet, in the separation process of pigment gas mixture, water, powder and air need be separated respectively, especially water is to have certain recycling to be worth, if water, powder and air can be separated respectively, then water is recyclable, reaches the purpose of waste water recycling.
Summary of the invention
The objective of the invention is provides a kind of cyclone type pigment air separation in order to overcome the defective that above-mentioned existing separator can't separate water, powder and air respectively.This pigment air separation can farthest separate water, powder and air respectively efficiently, on the other hand, realizes waste water recycling.
In order to achieve the above object, the technical scheme that adopted of technical solution problem of the present invention is:
A kind of cyclone type pigment air separation, comprise cylindrical outer cylinder body 17, described cylindrical outer cylinder body 17 tops are provided with exhaust outlet 9, the bottom is provided with leakage fluid dram 16, the middle part is provided with air inlet 14 and powder outlet 5, be provided with in the wherein said air inlet 14 and once coagulate fishplate bar 18, air inlet 14 is installed in the tangential position on cylindrical outer cylinder body 17 cylindricals; Separate successively from bottom to top in described cylindrical outer cylinder body 17 inner chambers and be fixedly connected with the whirlpool plate 2 that disappears that has some holes, gather materials plate 13, middle division board 6 and last division board 10 of division board 4, arc down; Described whirlpool plate 2 tops that disappear are provided with respectively and following division board 4 centre bores, the arc taper inner sleeve 3 that plate 13 centre bores are connected with middle division board 6 centre bores that gathers materials, the axial line of the axial line of taper inner sleeve 3 and cylindrical outer cylinder body 17 coincides, and forms a toroidal cavity between taper inner sleeve 3 outer walls and cylindrical outer cylinder body 17 inwalls; Be provided with four the back taper cyclone separators 7 being connected with middle division board 6 and last division board 10 respectively and the rounded dispensers 11 of X-shaped deflector in described between division board 6 and the last division board 10; Rounded dispensers 11 lower ends of described X-shaped deflector are provided with secondary and coagulate fishplate bar 1, and dock with taper inner sleeve 3 upper port; The center, upper end of described four back taper cyclone separators 7 respectively is provided with the blast pipe 8 that is connected with last division board 10.
Whirlpool plate 2 belows that disappear of the present invention also are provided with the whirlpool board mount 1 that disappears.
The whirlpool board mount 1 that disappears of the present invention is 45 degree and is connected with cylindrical outer cylinder body 17 inwalls with whirlpool plate 2 planes that disappear respectively.
The arc of the present invention plate 13 that gathers materials takes the form of inclined plane and is placed in down between division board 4 and the middle division board 6, and its inclined-plane low side docks with powder outlet 5.
Of the present invention being connected to is welded to connect.
The advantage and the beneficial effect of a kind of cyclone type pigment of the present invention air separation mainly are:
Because the air inlet (containing the plate that once condenses) of device, cylindrical outer cylinder body, tube taper inner sleeve and with holes disappearing form the structure of a whirlwind tube between the plate of whirlpool, the diameter of the taper inner sleeve in this whirlwind barrel structure is bigger, and then air-flow velocity is less.Therefore, in separation process, less to the centrifugal force that particle produces, have only the bigger particle of particle diameter just can be separated, and through after the plate that once condenses in the admission line, the small droplet major part of carrying in the air-flow can be agglomerated into big drop, along with second portion taper inner sleeve diameter diminishes gradually, and under the acting in conjunction of the plate that condenses of secondary, water will be separated, and drip along taper inner sleeve inwall, discharge from leakage fluid dram.
Along with air-flow continues to move upward,, tangentially enter four small-sized back taper cyclone separator inside arranging by circular symmetry through having the rounded dispensers of X-shaped deflector.Because the blast pipe diameter of these four small-sized cyclone separators is less, air velocity is accelerated, and wherein the suffered centrifugal force of particle is bigger, can isolate the particle diameter smaller particles.So powder remaining in can be with air-flow in this process is separated.
The present invention is applicable to the separation of moisture pigment gas mixture, water, powder and air can be separated respectively efficiently, and waste water is reclaimed, and reaches the effect of waste water recycling.
Description of drawings
Fig. 1 is the structural representation of cyclone type pigment air separation of the present invention.
Fig. 2 is the A-A view of Fig. 1.
Fig. 3 is the B-B view of Fig. 1.
Fig. 4 is that the C of Fig. 1 is to view.
Among the figure: 1, the whirlpool board mount that disappears; 2, the whirlpool plate that disappears; 3, taper inner sleeve; 4, following division board; 5, powder outlet; 6, middle division board; 7, back taper cyclone separator; 8, blast pipe; 9, exhaust outlet; 10, go up division board; 11, the rounded dispensers that has the X-shaped deflector; 12, the secondary plate that condenses; 13, the arc plate that gathers materials; 14, air inlet; 15, observation panel; 16, leakage fluid dram; 17, cylindrical outer cylinder body; 18, the plate that once condenses.
The specific embodiment
Below in conjunction with the drawings and specific embodiments cyclone type pigment air separation of the present invention is described further.
As shown in Figure 1, a kind of cyclone type pigment air separation is made up of three parts, and first is cylindrical urceolus, second portion be whirlwind moisture from, third part is that the whirlwind powder separates.First: the cylindrical shell welded top of cylindrical outer cylinder body 17 has circular row gas port 9, and the bottom is welded with circular leakage fluid dram 16; Be welded with air inlet 14, arc gather materials plate 13 and powder outlet 5 respectively at cylindrical shell middle part.Wherein, air inlet 14 is aspect lower clapboard 4 following, along the tangential position welding of cylindrical outer cylinder body 17; Second portion: the whirlwind separator mainly is made up of cylindrical outer cylinder body 17 inwalls, taper inner sleeve 3, whirlpool plate 2 and the whirlpool board mount 1 that disappears of disappearing with holes, form an annular space between taper inner sleeve 3 outer walls and cylindrical outer cylinder body 17 inwalls, disappearing has circular port (as shown in Figure 4) on the whirlpool plate 2, and the water of separating can flow in the fluid reservoir from the hole on the whirlpool plate 2 that disappears.The whirlpool board mount 1 that disappears is 45 degree and welds together with the whirlpool plate 2 that disappears, cylindrical urceolus 17 inwalls respectively; Taper inner sleeve 3 welds together with following division board 4, middle division board 6 respectively, and division board 4, middle division board 6 weld together with cylindrical outer cylinder body 17 inwalls down; Third part (as shown in Figure 2): cyclone dust powder separator mainly is made up of four small-sized cyclone separators 7, the rounded dispensers 11 with X-shaped deflector and blast pipe 8; The secondary plate 12 that condenses is equipped with in rounded dispensers 11 bottoms with X-shaped deflector, rounded dispensers 11 its inside with X-shaped deflector are separated into four separate space under the effect of X-shaped deflector, communicate with four back taper cyclone separators 7 respectively in the upper edge tangential direction; Four back taper cyclone separators 7 arrange by circular symmetry, respectively with middle division board 6, go up division board 10 and weld together, and middle division board 6, go up division board 10 and weld together with cylindrical outer cylinder body 17 inwalls; The middle position and the last division board 10 of corresponding four back taper cyclone separators 7 weld together four blast pipes respectively.
During work, the mixture that has water and dust is under the effect of blower fan, at first by being installed in the plate 18 (as shown in Figure 3) that once condenses in the admission line 14, the effect of the plate 18 that once condenses is that the small droplet in the incoming flow is agglomerated into bigger drop, thereby increases drop group's diameter.Then, contain and form an outer eddy current that moves downward in the annular space of air-flow between cylindrical outer cylinder body 17 and taper inner sleeve 3 of drop and powder.Outer eddy current arrives after the whirlpool plate 2 that disappears, and just moves upward to form interior eddy current, enters into the inside of taper inner sleeve 3.In this process, the drop that particle diameter is bigger is separated and discharges by leakage fluid dram 16, the less powder of particle diameter is then distributed respectively by X-shaped deflector in the rounded dispensers 11 with X-shaped deflector with air-flow and enters into four small-sized back taper cyclone separator 7 inside, produce higher rotary speed, dust is separated, the powder of being separated by small-sized back taper cyclone separator 7 drops into by the storage powder that descends division board 4 and middle division board 6 to form indoor, can the powder that be scattered in down on the division board 4 be discharged by powder outlet 5 by the arc plate 13 that gathers materials; Air-flow after the separation is then discharged from exhaust outlet 9.
Claims (5)
1. cyclone type pigment air separation, comprise cylindrical outer cylinder body (17), described cylindrical outer cylinder body (17) top is provided with exhaust outlet (9), the bottom is provided with leakage fluid dram (16), the middle part is provided with air inlet (14) and powder outlet (5), it is characterized in that: be provided with in the described air inlet (14) and once coagulate fishplate bar (18), air inlet (14) is installed in the tangential position on cylindrical outer cylinder body (17) cylindrical; Separate successively from bottom to top in described cylindrical outer cylinder body (17) inner chamber and be fixedly connected with the whirlpool plate (2) that disappears that has some holes, gather materials plate (13), middle division board (6) and last division board (10) of division board (4), arc down; Described whirlpool plate (2) top of disappearing is provided with respectively and following division board (4) centre bore, the arc taper inner sleeve (3) that plate (13) centre bore is connected with middle division board (6) centre bore that gathers materials, the axial line of the axial line of taper inner sleeve (3) and cylindrical outer cylinder body (17) coincides, and forms a toroidal cavity between taper inner sleeve (3) outer wall and cylindrical outer cylinder body (17) inwall; Be provided with four the back taper cyclone separators (7) that are connected with middle division board (6) and last division board (10) respectively and the rounded dispensers (11) of X-shaped deflector in described between division board (6) and the last division board (10); The rounded dispensers of described X-shaped deflector (11) lower end is provided with secondary and coagulates fishplate bar (12), and docks with taper inner sleeve (3) upper port; The center, upper end of described four back taper cyclone separators (7) respectively is provided with the blast pipe (8) that is connected with last division board (10).
2. cyclone type pigment air separation according to claim 1 is characterized in that: described whirlpool plate (2) below that disappears is provided with the whirlpool board mount (1) that disappears.
3. cyclone type pigment air separation according to claim 2 is characterized in that: the described whirlpool board mount (1) that disappears is 45 degree and is connected with cylindrical outer cylinder body (17) inwall with whirlpool plate (2) lower plane that disappears respectively.
4. cyclone type pigment air separation according to claim 1 is characterized in that: the described arc plate (13) that gathers materials takes the form of inclined plane and is placed in down between division board (4) and the middle division board (6), and its inclined-plane low side docks with powder outlet (5).
5. cyclone type pigment air separation according to claim 1 is characterized in that: described connection is main for welding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101417916A CN102228872B (en) | 2011-05-30 | 2011-05-30 | Cyclone water-powder-air separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011101417916A CN102228872B (en) | 2011-05-30 | 2011-05-30 | Cyclone water-powder-air separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102228872A true CN102228872A (en) | 2011-11-02 |
| CN102228872B CN102228872B (en) | 2012-07-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011101417916A Expired - Fee Related CN102228872B (en) | 2011-05-30 | 2011-05-30 | Cyclone water-powder-air separator |
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| Country | Link |
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| CN (1) | CN102228872B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102728489A (en) * | 2012-06-12 | 2012-10-17 | 江苏科技大学 | Self-drive centrifugal cyclone wet/dry water-powder-air separator |
| CN108030633A (en) * | 2016-12-30 | 2018-05-15 | 3S医药有限公司 | Dental comprehensive therapeutic chair automatic water seal formula aspirator |
| CN109967271A (en) * | 2019-04-30 | 2019-07-05 | 兰州大学 | A kind of cyclone separator and Gas cleaning systems |
| CN110017673A (en) * | 2019-04-26 | 2019-07-16 | 河南工业大学 | A kind of pneumatic conveying drying separator |
| CN110017673B (en) * | 2019-04-26 | 2024-04-26 | 郑州精华实业有限公司 | Air flow drying and separating device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2047992U (en) * | 1989-04-28 | 1989-11-22 | 侯镜波 | Cyclonic dust removing clarifier with autowater lifting function for air purification |
| CN1104960C (en) * | 1996-09-02 | 2003-04-09 | 国际壳牌研究有限公司 | Cyclone separator |
| CN1187127C (en) * | 2002-09-17 | 2005-02-02 | 山东大学 | Cyclone separator |
| CN1247311C (en) * | 1999-12-22 | 2006-03-29 | 戴森技术有限公司 | Cyclonic separating apparatus |
| CN201295649Y (en) * | 2008-07-31 | 2009-08-26 | 中国石油大学(华东) | Gas-liquid whirlwind separator |
-
2011
- 2011-05-30 CN CN2011101417916A patent/CN102228872B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2047992U (en) * | 1989-04-28 | 1989-11-22 | 侯镜波 | Cyclonic dust removing clarifier with autowater lifting function for air purification |
| CN1104960C (en) * | 1996-09-02 | 2003-04-09 | 国际壳牌研究有限公司 | Cyclone separator |
| CN1247311C (en) * | 1999-12-22 | 2006-03-29 | 戴森技术有限公司 | Cyclonic separating apparatus |
| CN1187127C (en) * | 2002-09-17 | 2005-02-02 | 山东大学 | Cyclone separator |
| CN201295649Y (en) * | 2008-07-31 | 2009-08-26 | 中国石油大学(华东) | Gas-liquid whirlwind separator |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102728489A (en) * | 2012-06-12 | 2012-10-17 | 江苏科技大学 | Self-drive centrifugal cyclone wet/dry water-powder-air separator |
| CN108030633A (en) * | 2016-12-30 | 2018-05-15 | 3S医药有限公司 | Dental comprehensive therapeutic chair automatic water seal formula aspirator |
| CN110017673A (en) * | 2019-04-26 | 2019-07-16 | 河南工业大学 | A kind of pneumatic conveying drying separator |
| CN110017673B (en) * | 2019-04-26 | 2024-04-26 | 郑州精华实业有限公司 | Air flow drying and separating device |
| CN109967271A (en) * | 2019-04-30 | 2019-07-05 | 兰州大学 | A kind of cyclone separator and Gas cleaning systems |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102228872B (en) | 2012-07-18 |
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