CN104907191A - Rotary parallel dedusting device of cyclone separator - Google Patents
Rotary parallel dedusting device of cyclone separator Download PDFInfo
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- CN104907191A CN104907191A CN201510356212.8A CN201510356212A CN104907191A CN 104907191 A CN104907191 A CN 104907191A CN 201510356212 A CN201510356212 A CN 201510356212A CN 104907191 A CN104907191 A CN 104907191A
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- cyclone separator
- middle cylinder
- cylinder body
- parallel
- cylinder
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- 239000000428 dust Substances 0.000 claims description 27
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 9
- 238000002955 isolation Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 2
- 239000010865 sewage Substances 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims 1
- 239000003570 air Substances 0.000 description 19
- 239000010419 fine particle Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000003134 recirculating effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Cyclones (AREA)
Abstract
The invention discloses a rotary parallel dedusting device of a cyclone separator. The rotary parallel dedusting device mainly comprises a central cylinder body, a middle cylinder body and an outer cylinder body which are coaxially arranged and are insulated in a sealed mode from each other, wherein empty cavities are formed between every two of the three, the upper end of the empty cavity between the middle cylinder body and the outer cylinder body is provided with a tangential inlet; a plurality of small cyclone separators are uniformly connected in parallel to and fixed on the inner wall of the middle cylinder body by taking the centers of the three cylinder bodies as an axis. According to the invention, the problems that the plurality of cyclone dedusting devices in the existing boiler are low in dedusting efficiency, and are non-uniform in air quantity distribution are solved.
Description
Technical field
The present invention relates to a kind of cyclone separator and rotate dust arrester in parallel, particularly relate to the cyclone separator that one can trap fine particle (PM2.5) and rotate dust arrester in parallel.
Background technology
Atmosphere pollution is one of key factor affecting China's environment, and wherein dust pollution is the pith of atmosphere pollution.Research shows, the fine particle (PM2.5) in dust is easy to heavy metal in enriched air, acidic oxide, organic pollution, bacterium and virus etc., its to the harm of health far above coarseparticulate.Therefore, control dust pollution, the discharge especially controlling fine particle is significant.(magnifying year, the research of Inhalable Particulates in Urban Ambient Air, [J] Shanghai environmental science, 1999,18(4): 154-157).
Cyclone separator has the advantages such as structure is simple, small investment, operating cost are low because of it, and industrial dedusting is widely used.But single dust removal efficiency in cyclone cleaner is low, the dust removal requirement of large-sized boiler cannot be met.Numerous scholar's research, in CFBB, adopts the mode of multiple cyclone dust collectors parallel connection to carry out desulfurization and dedusting.Law of the country army of the Chinese Academy of Sciences, Liao Lei etc. ([1] law of the country army. the many cyclone separators of recirculating fluidized bed are arranged in parallel cold state experimental [D]. Postgraduate School, Chinese Academy of Sciences (Engineering Thermophysics research institute), 2014.; [2] Liao Lei. six cyclone separators are arranged in parallel experimental study and the numerical simulation [D] of recirculating fluidized bed. Postgraduate School, Chinese Academy of Sciences (Engineering Thermophysics research institute), 2011) have studied six cyclone dust collectors with the situation of the symmetrical H type distribution of furnace chamber central shaft.As shown in Figure 3.Experimental result shows, there is gas-solid and distribute uneven phenomenon between six cyclone separators; Under the same conditions, the cyclone separator pressure drop of diverse location and air quantity all have some differences.At burner hearth homonymy, the pressure drop being positioned at middle cyclone separator is lower than the pressure drop of cyclone separator being positioned at two ends; Side cyclone separator pressure drop near the female pipeline of afterbody is greater than the pressure drop away from the female pipeline side of afterbody, and middle position pressure drop size is between the two.When burner hearth wind speed 5 m/s, the pressure drop deviation of six cyclone separators is about 5.6%.Visible, six cyclone separators adopt central shaft to be arranged symmetrically with pattern, and two middle cyclone separators cannot reach gas-solid equilibrium all the time and particle phase volume fraction is even.
Studies have found that in addition, in high density multiphase flow, Gas-particle Flows is in two separators during impartial distribution, and separator pressure loss is maximum; In low-density multiphase flow, when especially density is very low, impartial distribution can make separator pressure loss reduction, and is unequally assigned the larger pressure loss.
Liao Lei and law of the country army analyze the reason of gas-particle two-phase uneven distribution between multiple cyclone separator, mainly contain two parts: a part is because the pulsating nature of aggregative fluidization and the multi-solution of symmetrical structure cause, and another part is because the non complete symmetry of structure causes.As can be seen here, the gas-particle two-phase realizing multiple cyclone separator is uniformly distributed raising efficiency of dust collection, to reduce energy loss significant.
Summary of the invention
The invention provides a kind of cyclone separator and rotate dust arrester in parallel, multiple dust removal efficiency in cyclone cleaner in existing boiler is low to solve, the problem of tolerance skewness.
For this reason, following technical scheme is adopted:
A kind of cyclone separator rotates dust arrester in parallel, primarily of the coaxial central cylinder, middle cylinder, the outer cylinder body composition that arrange, there is cavity, each other seal isolation each other, the bottom of this three cylindrical shell is cone structure and the cone distal end of middle cylinder and outer cylinder body is inside and outside underflow opening, and this inside and outside underflow opening is connected with ash exhauster by flange; Between described middle cylinder and outer cylinder body, the upper end of cavity is provided with tangential entry; Several small cyclones separators with the center of three cylindrical shells for axle is evenly fixed on the inwall of middle cylinder; The junction of middle cylinder and its underpart cone is connected with base plate, leaves air inlet annular distance between the outer rim of this base plate and the inwall of middle cylinder; The bottom discharge mouth of several small cyclones separators described to be fixed on base plate and and the cone of middle cylinder bottom through; The upper end of several small cyclones separators described has air inlet, and the inner chamber of this air inlet and middle cylinder is through; The outlet of these several small cyclones separator upper ends by bend pipe and central cylinder through; Described bend pipe is placed in the top seal at outer cylinder body top, and this top cover has outlet.
The cross section of described winding pipe exit and the angle of horizontal plane are 90
oto 180
o.
The present invention has considered that the efficiency of dust collection of multiple cyclone dust collectors is low, the reason of tolerance and pressure drop distribution inequality, by multiple cyclone dust collectors parallel configuration in a large cavity, be specially cyclone dust collectors coaxially to arrange, rotate arrangement one week around central axis, then dusty gas is directly sent into large cavity internal cyclone deduster with pipeline and carry out dedusting.
The contrast of the present invention and multiple cyclone separator H type in parallel layout as shown in Figures 2 and 3.Several cyclone separators of the present invention to rotate a circle layout around central shaft, and the parallel connection of multiple cyclone separator H type take furnace chamber as symmetry axis, and six cyclone separators divide equally layout in furnace chamber both sides.In laboratory, test the dust removing effects of the present invention and multiple cyclone separator H type in parallel layout, air quantity and pressure drop distribution uniformity, test air quantity is 10000m
3/ h.Test result as Figure 4-Figure 6.Fig. 4 is the change in pressure drop that two kinds of cyclone separator layouts cause.As can be seen from Figure 4, in the present invention, the pressure drop size of each cyclone separator is substantially identical, and the parallel connection of multiple cyclone separator H type causes the pressure drop difference of each cyclone separator larger.Fig. 5 is the air quantity change that two kinds of cyclone separator layouts cause, can find out, multiple cyclone separator H type layouts cause the gas-solid skewness of each cyclone separator, and air quantity is variant, and the air quantity difference of each cyclone separator of the present invention is little, achieve being uniformly distributed of air quantity.Fig. 6 is the separation efficiency comparative of two kinds of cyclone separator layouts, and the Effiency of whirlwind Separator of H type layout is variant, and B separative efficiency is minimum, and be that 60%, A is up to 80%, total separative efficiency is 79%; And the efficiency of dust collection of each cyclone separator is about 95% in the present invention, total efficiency of separation is 95%.Therefore, separative efficiency of the present invention, much larger than H type layout, efficiently can remove the fine particle in dusty gas.
In sum, compared with traditional multiple cyclone separator H type parallel configuration, the present invention can solve the shortcomings such as air quantity, pressure drop distribution is uneven, separative efficiency is low, each cyclone separator air quantity of coaxial layout is even, pressure drop is equal, separative efficiency is even, can collect dust in dusty gas efficiently.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the top view of Fig. 1;
Fig. 3 is the schematic diagram of cyclone separator H type parallel configuration in prior art;
Fig. 4 is the pressure drop comparison diagram of cyclone separator H type parallel configuration in the present invention and prior art;
Fig. 5 is the air quantity comparison diagram of cyclone separator H type parallel configuration in the present invention and prior art;
Fig. 6 is the separation efficiency comparative figure of cyclone separator H type parallel configuration in the present invention and prior art.
A to F in Fig. 4,5,6 represents cyclone separator of the prior art, and Y
1to Y
8for each small cyclones separator in the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further detail.
Embodiment 1, with reference to Fig. 1,2, a kind of cyclone separator rotates dust arrester in parallel, form primarily of coaxial setting, the central cylinder 14 each other with cavity, each other seal isolation, middle cylinder 27, outer cylinder body 23, the bottom of this three cylindrical shell is cone structure, and the cone distal end of middle cylinder 27 and outer cylinder body 23 is inside and outside underflow opening 10,24, this inside and outside underflow opening 10,24 is connected with ash exhauster by flange; Cavity upper end between described middle cylinder 27 and outer cylinder body 23 is provided with tangential entry 22; Several small cyclones separators 28 with the center of three cylindrical shells for axle is evenly fixed on the inwall of middle cylinder 27; The junction of middle cylinder 27 and its underpart cone is connected with base plate 11, leaves air inlet annular distance 26 between the outer rim of this base plate 11 and the inwall of middle cylinder 27; The bottom discharge mouth 9 of several small cyclones separators 28 described to be fixed on base plate 11 and and the cone of middle cylinder 27 bottom through; The upper end of several small cyclones separators 28 described has air inlet 29, and the inner chamber of this air inlet 29 and middle cylinder 27 is through; The outlet of these several small cyclones separator 28 upper ends by bend pipe 12 and central cylinder 14 through; The top cover 13 that described bend pipe 12 is placed in outer cylinder body top seals, and this top cover 13 has outlet 15.
The angle of the cross section that described bend pipe 12 exports and horizontal plane is 90
oto 180
o, make pressure drop even.
Described ash exhauster 6 is made up of bed material groove 17, connection valve 19, U-shaped pipe 20; Described bed material groove 17 one end is connected by flange 16 with described inside and outside underflow opening 10,24, and the other end is connected with U-shaped pipe 20 by flange, and the other end of U-shaped pipe 20 is sewage draining exit 21; The bottom of bed material groove 17 is provided with blowoff valve 18.
Embodiment 2, with reference to Fig. 1, the bed material groove 17 of described ash exhauster 6 is communicated with central cylinder 14 by drainpipe 30, solves the laying dust problem in central cylinder 14.Remaining with embodiment 1.
The course of work of the present invention: dust-contained airflow tangentially enters the upper end of cavity between outer cylinder body 23 and middle cylinder 27 by tangential entry 22, produces rotating flow, under centrifugal action, carries out first order separation.Isolated coarse granule or drop will fall the cone inwall of outer cylinder body 23 lower end, discharge through outer underflow opening 24.The air-flow be separated through the first order to enter the bottom of middle cylinder 27 through air inlet annular distance 26, then rotate into each cyclone separator 28 respectively from the air inlet 29 of some cyclone separator 28 upper ends simultaneously, in cyclone separator 28, produce rotating flow, carry out second level separation.Air-flow after the second level is separated is discharged to central tube 14 through bend pipe 12, and air-flow carries out colliding, reuniting in central tube 14, and the fine particle that part is not trapped is grown up again, realizes the third level and is separated.Be provided with blow-off pipe 30 in central tube 14 bottom, the drop generated after the third level is separated is discharged to bed material groove 17 by blow-off pipe 30.Finally, under the suction function that outside applies, the air-flow in central tube 14 can enter discharge duct below by outlet 15.
Claims (4)
1. a cyclone separator rotates dust arrester in parallel, it is characterized in that: primarily of the coaxial central cylinder (14), middle cylinder (27), outer cylinder body (23) composition that arrange, there is cavity, each other seal isolation each other, the bottom of this three cylindrical shell is cone structure and the cone distal end of middle cylinder (27) and outer cylinder body (23) is inside and outside underflow opening (10,24), and this inside and outside underflow opening (10,24) is connected with ash exhauster by flange; Between described middle cylinder (27) and outer cylinder body (23), the upper end of cavity is provided with tangential entry (22); Several small cyclones separators (28) with the center of three cylindrical shells for axle is evenly fixed on the inwall of middle cylinder (27); The junction of middle cylinder (27) and its underpart cone is connected with base plate (11), leaves air inlet annular distance (26) between the outer rim of this base plate (11) and the inwall of middle cylinder (27); The bottom discharge mouth (9) of several small cyclones separators (28) described be fixed on base plate (11) upper and and the cone of middle cylinder (27) bottom through; The upper end of several small cyclones separators (28) described has air inlet (29), and the inner chamber of this air inlet (29) and middle cylinder (27) is through; The outlet of these several small cyclones separator (28) upper ends by bend pipe (12) and central cylinder (14) through; Described bend pipe (12) is placed in top cover (13) sealing at outer cylinder body top, this top cover (13) has outlet (15).
2. a kind of cyclone separator according to claim 1 rotates dust arrester in parallel, it is characterized in that: the angle of the cross section that described bend pipe (12) exports and horizontal plane is 90
oto 180
o.
3. a kind of cyclone separator according to claim 1 rotates dust arrester in parallel, it is characterized in that: described ash exhauster is made up of bed material groove (17), connection valve (19), U-shaped pipe (20); Described bed material groove (17) one end is connected by flange (16) with described inside and outside underflow opening (10,24), and the other end is connected with U-shaped pipe (20) by connection valve (19), and the other end of this U-shaped pipe (20) is sewage draining exit (21); The bottom of bed material groove (17) is provided with blowoff valve (18).
4. a kind of cyclone separator according to claim 3 rotates dust arrester in parallel, it is characterized in that: the bed material groove (17) of described ash exhauster is communicated with central cylinder (14) by drainpipe (30).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510356212.8A CN104907191B (en) | 2015-06-25 | 2015-06-25 | Cyclone separator rotation dust arrester in parallel |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510356212.8A CN104907191B (en) | 2015-06-25 | 2015-06-25 | Cyclone separator rotation dust arrester in parallel |
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| Publication Number | Publication Date |
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| CN104907191A true CN104907191A (en) | 2015-09-16 |
| CN104907191B CN104907191B (en) | 2017-08-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510356212.8A Active CN104907191B (en) | 2015-06-25 | 2015-06-25 | Cyclone separator rotation dust arrester in parallel |
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| Country | Link |
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| CN (1) | CN104907191B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106166519A (en) * | 2016-08-30 | 2016-11-30 | 江苏天鹏石化科技股份有限公司 | A kind of continuous discharge gas-solid separator |
| CN109589045A (en) * | 2019-01-29 | 2019-04-09 | 品孚罗特过滤设备（北京）有限公司 | Rotary fluid, cyclonic separation tree and high effect dust cleaner |
| CN114752421A (en) * | 2021-01-08 | 2022-07-15 | 中国石油天然气集团有限公司 | Natural gas pipeline filtering system and method |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2138525Y (en) * | 1992-09-23 | 1993-07-21 | 东北电力学院 | Multi-stage vortex duster |
| CN2536307Y (en) * | 2002-04-29 | 2003-02-19 | 张桂才 | Vortex powder separators |
| CN1422187A (en) * | 2000-03-31 | 2003-06-04 | 戴森有限公司 | Apparatus for separating particles from a fluid flow |
| CN1751800A (en) * | 2005-09-20 | 2006-03-29 | 泰怡凯电器(苏州)有限公司 | Cyclone separator |
| CN202061725U (en) * | 2011-05-12 | 2011-12-07 | 信阳市四通机械制造有限公司 | Cyclone dust collector and composite cyclone dust collector |
| CN205008123U (en) * | 2015-06-25 | 2016-02-03 | 王博 | Rotatory parallelly connected dust collector of cyclone |
-
2015
- 2015-06-25 CN CN201510356212.8A patent/CN104907191B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2138525Y (en) * | 1992-09-23 | 1993-07-21 | 东北电力学院 | Multi-stage vortex duster |
| CN1422187A (en) * | 2000-03-31 | 2003-06-04 | 戴森有限公司 | Apparatus for separating particles from a fluid flow |
| CN2536307Y (en) * | 2002-04-29 | 2003-02-19 | 张桂才 | Vortex powder separators |
| CN1751800A (en) * | 2005-09-20 | 2006-03-29 | 泰怡凯电器(苏州)有限公司 | Cyclone separator |
| CN202061725U (en) * | 2011-05-12 | 2011-12-07 | 信阳市四通机械制造有限公司 | Cyclone dust collector and composite cyclone dust collector |
| CN205008123U (en) * | 2015-06-25 | 2016-02-03 | 王博 | Rotatory parallelly connected dust collector of cyclone |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106166519A (en) * | 2016-08-30 | 2016-11-30 | 江苏天鹏石化科技股份有限公司 | A kind of continuous discharge gas-solid separator |
| CN109589045A (en) * | 2019-01-29 | 2019-04-09 | 品孚罗特过滤设备（北京）有限公司 | Rotary fluid, cyclonic separation tree and high effect dust cleaner |
| CN109589045B (en) * | 2019-01-29 | 2023-10-20 | 品孚罗特过滤设备（北京）有限公司 | Cyclone body, cyclone separation tree and high-efficiency dust removing device |
| CN114752421A (en) * | 2021-01-08 | 2022-07-15 | 中国石油天然气集团有限公司 | Natural gas pipeline filtering system and method |
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| Publication number | Publication date |
|---|---|
| CN104907191B (en) | 2017-08-15 |
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Effective date of registration: 20180427 Address after: 730000 room 315-13, 249 Donggang West Road, Chengguan District, Lanzhou, Gansu Patentee after: Lanzhou cloud Environment Technology Co., Ltd. Address before: 730000 room 2502, 15 building, two division, Lanzhou University, Lanzhou, Gansu. Patentee before: Wang Bo |