CN202410265U - Multilevel integrated fluid power cyclone separator - Google Patents
Multilevel integrated fluid power cyclone separator Download PDFInfo
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- CN202410265U CN202410265U CN2011205368933U CN201120536893U CN202410265U CN 202410265 U CN202410265 U CN 202410265U CN 2011205368933 U CN2011205368933 U CN 2011205368933U CN 201120536893 U CN201120536893 U CN 201120536893U CN 202410265 U CN202410265 U CN 202410265U
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Abstract
The utility model provides a multilevel integrated fluid power cyclone separator comprising a columnar shell, a tangential water inlet pipe and a water outlet pipe, wherein the tangential water inlet pipe and the water outlet pipe are connected to the columnar shell; the columnar shell is formed by a top cover, a bottom plate and a side wall; the top cover is a detachable cover plate or a partially-opened cover plate; a columnar flow guide plate is arranged at the center of the upper part of the inner side of the columnar shell; the columnar flow guide plate is connected with the side wall of the columnar shell through a columnar flow guide plate supporting frame; the lower end of the columnar flow guide plate is connected with a tapered flow guide plate with a big top and a small bottom; a separation chamber inclined baffle is arranged in a hollow cavity between the tapered flow guide plate and the side wall; and deposited material storage chamber separation baffles are arranged below the tapered flow guide plate and on the side wall of the columnar shell. The cyclone separator is provided with three separation chambers which are integrated to a whole body; and compared with the existing fluid power cyclone separator, the removing effect and efficient treating capability of grains are obviously improved.
Description
Technical field
The utility model relates to a kind of fluid dynamic cyclone separator that rainwater is handled that is used for, the particularly a kind of purified treatment of rainfall runoff solid suspension and floating thing or preposition pretreated fluid dynamic cyclone separator of dirty combined drainage system solid suspension control of rain and sewage treatment process thereof of being used for.
Background technology
Fluid dynamic cyclone separator developing history abroad can be traced back to generation nineteen sixty, the effect that Bernard Smisson builds and tested the cyclonic separation facility at the Bristol of Britain, and be used to handle the pollution load of overflow control of combined system pipeline.The hydroseparator of the first generation can effectively be detained 70% pollution total amount (Smisson, 1967).Through development since the 1980's and commercialization, the fluid dynamic cyclone separator experimentizes in zones such as Europe, North America, Japan and uses.(Brombach,?1992;?Hedges?
et?al.,?1993;?Averill?
et?al.,?1997;?Arnett?and?Gurney,?1998;?and?Okamoto?
et?al.,?2002)。Its performance evaluation mainly comprises aspects such as the particle diameter, density, settling property of the particle that becomes a mandarin, and has stressed getting in touch and importance between sewage characteristic (especially the particle sinking speed distributes) and the facility treatment effect.At present, the range of application of fluid dynamic cyclone separator comprises water quality control measure, the wastewater treatment of collaborating pipeline, and rainwater is handled.Wherein, be applied in the fluid dynamic cyclone separation process of rainwater processing CDS and Vortechs
TMHas stronger representativeness.
CDS cyclone separator by the exploitation of Australian CDS company has added elliptical orifice-hoop screen cloth and has held back function, and adopted separation chamber's charging in the tangential, the mode of outer separation chamber discharging on the basis of conventional fluid power cyclone separator.This technological operation mechanism is that rainfall runoff or interflow system sewage water conservancy diversion are gone into the CDS cyclone separator, utilizes the acting in conjunction of eddy flow and circular screen, and realization is held back and cyclonic separation, and the water after the processing gets into outflow tube after through the grease baffle plate.This fluid dynamic cyclone separator mainly is made up of tangential water inlet pipe, downflow weir, hoop screen cloth, oil-shutting-off plate, sediment apotheca, tangential outlet pipe.The CDS cyclone separator has the particle of floating things such as polybag, cigarette end, leaf and greater particle size holds back effect preferably, and the setting of oil-shutting-off plate and grease sorbing material has also improved the removal effect of grease to a certain extent in addition.But,, can't guarantee fine grain removal effect because the screen size on the hoop screen cloth receives the influence of blockage problem.
By the Vortechs rainwater treatment system of Polish Vortechnics manufactured, under high flow condition, be used for separating and being detained floating thing and sediment.This system as separating main body, promotes deposit fouling thing to migrate to sedimentation basin center and deposition through mild swirling motion by the cylindricality rotational flow grit chamber.Floating pollutants then floats on the liquid level, and is higher than vertical barricade bottom and is detained.Vortechs rainwater treatment system mainly is made up of tangential water inlet pipe, rotational flow grit chamber, oil storage storehouse, vertical barricade, downflow weir.Vortechs rainwater treatment system is when handling little rainfall incident, and the removal effect of sediment and suspension is very high.But in large and medium-sized rainfall incident, the clearance that sinks to the bottom thing and grease is very low, and suspending can appear in setting pot in the pollutant that before is trapped again.
The utility model content
The purpose of the utility model provides the multistage integrated fluid power cyclone separator of a kind of practicality and treatment effect optimization, solve the technical problem of traditional fluid dynamic cyclone separator inferior separating effect that is used for the rainwater processing.
For realizing above-mentioned purpose; The utility model adopts following technical scheme: a kind of multistage integrated fluid power cyclone separator; Comprise cylindrical shell and be connected tangential water inlet pipe, the outlet pipe on the cylindrical shell; It is characterized in that: said cylindrical shell is made up of top cover, base plate and sidewall, and wherein top cover is detachable cover plate or partially perforation cover plate; The inside upper part center of said cylindrical shell is provided with the cylindricality deflector and this cylindricality deflector is connected on the sidewall of cylindrical shell through cylindricality deflector bracing frame; The lower end of cylindricality deflector is connected with the up big and down small conical baffle of diameter; Be provided with separation chamber's sloping baffle in the cavity between conical baffle and the sidewall, the below of conical baffle, the sidewall of cylindrical shell are provided with deposit apotheca separation baffles; Said tangential water inlet pipe pass cylindrical shell sidewall, be connected on the cylindricality deflector, said outlet pipe is connected on the sidewall of cylindrical shell of separation chamber sloping baffle top.
Said deposit apotheca separation baffles comprises the Suspension Control cover again and partly isolates sloping baffle; The said cover of Suspension Control again be connected on the sidewall through Suspension Control cover bracing frame again and again the Suspension Control cover by downward-sloping around the middle mind-set, said partly isolate sloping baffle be connected on the sidewall and partly isolate sloping baffle by around downward-sloping to the center.
The angle of inclination of the said cover of Suspension Control again can be 15 °～45 °, and the angle of inclination that partly isolates sloping baffle can be 30 °～60 °.
Below the water inlet pipe of said tangential, can be provided with spiral deflector on the madial wall of said conical baffle.
The angle of inclination of said spiral deflector can be 5 °～15 °.
Said separation chamber sloping baffle can be connected on the sidewall of cylindrical shell, and sloping baffle is downward-sloping to the center by all around.
The lower end of said separation chamber sloping baffle can be provided with the shirt rim.
The angle of inclination of said separation chamber sloping baffle can be 15 °～30 °.
The horizontal level of the delivery port of said tangential water inlet pipe is lower than the horizontal level of the water inlet of outlet pipe.
The cone angle of said conical baffle can be 5 °～10 °.
Compared with prior art the utlity model has following characteristics and beneficial effect: the utility model is a kind of equipment that separates non-homogeneous mixture; Can realize the sedimentary separation of coarse granule in the rainfall runoff; And the delay of fine particle, grease and floating thing; Can be applicable to municipal storm sewer, combined system sewerage system, and the preliminary treatment of facilities such as wet land protection and filtration.
The utlity model has three grades of separation chambers; And be integrated in one, have do not consume energy, floor space is little, be convenient to install and regulation and control, be convenient to concentrate characteristics such as desilting, simultaneously; Compare with existing fluid dynamic cyclone separator; Removal effect and effective processing capacity for particle are significantly improved, and specifically, have following characteristics: 1, owing to adopt the multistage design of segmentation; Each grade all has its removal target and the mechanism that are directed against specially; Prevented that secondary from carrying and the heterogeneity pollutant between interference effect, the removal efficient of the particle of each grade scope and floating thing has had the raising of globality, and on separation chambers at different levels configuration, size design, its reasonability is arranged also.2, the border configuration of one-level awl section separation chamber adopts the conical design of bottom reducing, and this configured has effectively reduced the loss of fluid energy, has guaranteed the adequacy of eddy flow; Simultaneously, the reducing of bottom has caused fine grained and has been mingled in the floating thing generation backflow in the fluid.3, with respect to one-level awl section separation chamber, the rotating fluid diameter in the secondary shell of column separation chamber is bigger, and the shell of column configured is easier to scattering and disappearing of fluid energy, thereby reduces the speed of secondary shell of column separation chamber inner fluid rotation, improves stability, prolongs the time of staying.4, three grades of shell of column separation chambers are that the fluid running space is maximum in all separation chambers, and the interference of high strength eddy flow in the one-level awl section separation chamber when effectively reducing high flow capacity, for thick, fine grain sedimentation again provides effective place.5, Suspension Control cover and partly isolate the collocation of sloping baffle has more effectively prevented the interference of powerful eddy flow to basic sediment.6, the setting of spiral deflector on the conical baffle sidewall, fluid stability of rotation when effectively having improved high flow capacity.
Description of drawings
Below in conjunction with accompanying drawing the utility model is done further detailed explanation.
Fig. 1 is the structural representation of the utility model.
Fig. 2 is the sketch map of A-A section among Fig. 1.
Fig. 3 is the sketch map of B-B section among Fig. 1.
Fig. 4 is the sketch map of C-C section among Fig. 1.
Fig. 5 is the sketch map of spiral deflector.
Fig. 6 is the sketch map of the top cover of cylindrical shell when opening.
Reference numeral: 1-floating thing apotheca; 2-one-level awl section separation chamber; 3-secondary shell of column separation chamber; Three grades of shell of column separation chambers of 4-; 5-deposit apotheca; The 6-cylindrical shell; 6.1-top cover; 6.2-base plate; 6.3-sidewall; 7-tangential water inlet pipe; The 8-outlet pipe; 9-cylindricality deflector; The 10-conical baffle; The 11-spiral deflector; 12-separation chamber sloping baffle; 12.1-shirt rim; 13-is the Suspension Control cover again; 14-partly isolates sloping baffle; 15-is Suspension Control cover bracing frame again; 16-cylindricality deflector bracing frame.
The specific embodiment
Embodiment is referring to shown in Fig. 1-6, and this multistage integrated fluid power cyclone separator comprises cylindrical shell 6 and is connected tangential water inlet pipe 7, the outlet pipe 8 on the cylindrical shell 6.Said cylindrical shell 6 is made up of top cover 6.1, base plate 6.2 and sidewall 6.3, wherein between base plate 6.2 and the sidewall 6.3 for being fixedly connected.
Said top cover 6.1 is detachable cover plate or partially perforation cover plate.Said detachable cover plate is meant between top cover 6.1 and the sidewall 6.3 to removably connecting, between promptly detachable cover plate and the sidewall 6.3 for removably connecting.Said partially perforation cover plate is meant and has maintenance desilting hole on the top cover 6.1 that open on the top cover above the floating thing apotheca in maintenance desilting hole, promptly has maintenance desilting hole on the partially perforation cover plate.Referring to Fig. 6, present embodiment has been selected detachable cover plate for use.
The purpose that top cover 6.1 is designed to detachable cover plate or partially perforation cover plate is installation, the maintenance of the utility model for ease and draws inner foreign material clearly.Specifically; Be exactly after operation after a while; Through disassembling the detachable cover plate of cylindrical shell 6, perhaps open the maintenance desilting hole on the partially perforation cover plate, just can overhaul the inside of cylindrical shell easily or clear up inner floating thing of cylindrical shell and deposit.
The inside upper part center of said cylindrical shell 6 is provided with cylindricality deflector 9 and this cylindricality deflector 9 is connected on the sidewall 6.3 of cylindrical shell through cylindricality deflector bracing frame 16; The lower end of cylindricality deflector 9 is connected with the up big and down small conical baffle of diameter 10; Be provided with separation chamber's sloping baffle 12 in the cavity between conical baffle 10 and the sidewall 6.3, the below of conical baffle 10, the sidewall of cylindrical shell 6.3 are provided with deposit apotheca separation baffles; Said tangential water inlet pipe 7 pass cylindrical shell sidewall 6.3, be connected on the cylindricality deflector 9, said outlet pipe 8 is connected on the sidewall 6.3 of cylindrical shell of separation chamber's sloping baffle 12 tops.The horizontal level of the delivery port of said tangential water inlet pipe 7 is lower than the horizontal level of the water inlet of outlet pipe 8.
As preferred embodiment, the cone angle of the conical baffle 10 in the present embodiment is 5 °～10 °.Below the said tangential water inlet pipe 7, be provided with spiral deflector 11 on the madial wall of said conical baffle 10, the angle of inclination of spiral deflector 11 is 5 °～15 °.
As preferred embodiment, the separation chamber's sloping baffle 12 in the present embodiment is connected on the sidewall 6.3 of cylindrical shell 6, and sloping baffle 12 is downward-sloping to the center by all around.The lower end of separation chamber's sloping baffle 12 is provided with shirt rim 12.1, and the angle of inclination of separation chamber's sloping baffle 12 is 15 °～30 °.
As preferred embodiment; Deposit apotheca separation baffles in the present embodiment comprises Suspension Control cover 13 again and partly isolates sloping baffle 14; The said cover of Suspension Control again 13 is connected on the sidewall 6.3 through Suspension Control cover bracing frame 15 again and Suspension Control cover 13 is by downward-sloping around the middle mind-set again, and the angle of inclination of Suspension Control cover 13 is 15 °～45 ° again.Said partly isolate sloping baffle 14 be connected on the sidewall 6.3 and partly isolate sloping baffle 14 by around downward-sloping to the center, the angle of inclination that partly isolates sloping baffle 14 is 30 °～60 °.
The inner space of said cylindricality deflector 9 is a floating thing apotheca 1; The inner space of the conical baffle 10 that is positioned at the below of floating thing apotheca 1 and is communicated with floating thing apotheca 1 is one-level awl section separation chamber 2; The outer space of the conical baffle 10 that is positioned at one-level awl section separation chamber's 2 bottom outside and is communicated with one-level awl section separation chamber 2 is secondary shell of column separation chamber 3; The space that is positioned at the top of separation chamber's sloping baffle 12 and is communicated with secondary shell of column separation chamber 3 is three grades of shell of column separation chambers 4, is positioned at Suspension Control cover 13 again and partly isolates the below of sloping baffle 14 and the space that is communicated with secondary shell of column separation chamber 3 is a deposit apotheca 5.Floating thing apotheca 1 is connected with one-level awl section separation chamber 2, and secondary shell of column separation chamber 3 is connected with one-level awl section separation chamber 2, and secondary shell of column separation chamber 3 is connected with three grades of shell of column separation chambers 4, deposit apotheca 5.Cylindricality deflector 9, conical baffle 10, sloping baffle 12, again Suspension Control cover 13, partly isolate sloping baffle 14 inside of whole cylindrical shell 6 be divided into three grades of separation chambers, floating thing apotheca 1 and deposit apotheca 5.The delivery port of 3 to three grades of shell of column separation chambers 4, said secondary shell of column separation chamber is positioned near the center of secondary shell of column separation chamber 3, can effectively control the sedimentary loss of coarse granule in the secondary shell of column separation chamber 3.Said floating thing apotheca 1 makes floating thing before getting into one-level awl section separation chamber 2, be trapped.
Said conical baffle 10 from its lateral its central authorities downward-sloping; Make that the space of the one-levels awl section separation chamber 2 that conical baffle 10 is inboard is up big and down small; Become a cone space, so not only can improve eddy flow effect and stability, can also guide to secondary shell of column separation chamber 3 flowing into cylindricality deflector 9 rainfall runofves inner and that spiral moves downward; Simultaneously; This configured when improving the eddy flow effect, has increased the separated space of secondary shell of column separation chamber 3, three grades of shell of column separation chambers 4.Also have, isolated floating thing is trapped in the top of one-level awl section separation chamber 2 in the rainwater, promptly in the inside of cylindricality deflector 9, the floating thing apotheca 1, can prevent that like this floating thing from impacting the eddy flow effect in the conical baffle 10.In addition; The design of closing up of the bottom of conical baffle 10 makes that floating thing and the fine grained in the rainfall runoff that spiral moves downward forms the backflow on the counter steer, the bottom in one-level awl section separation chamber 2; Promptly in the inboard of conical baffle 10; Fine grained and floating thing form when boring the outlet of section separation chamber 1 near one-level and reflux, and finally are trapped near the center of rotary fluid, have realized the delay of fine grained and floating thing thus.
Said spiral deflector 11 is arranged on the below of the tangential interface of tangential water inlet pipe 7 and cylindricality deflector 9; Be connected with the inwall of conical baffle 10; But the constrain fluids track, improve the eddy current flow pattern, reduce the flow field disturbance, the steady flow of guiding fluid, so fluid stability of rotation when having improved high flow capacity.
The 3 main sedimentary removals of accomplishing in the rainfall runoff of coarse granule of said secondary shell of column separation chamber, the shell of column configured of secondary shell of column separation chamber 3 has reduced the speed of fluid rotation, prolongs the time of staying.
In addition; Under high flow capacity, secondary shell of column separation chamber 3 is easy to generate runs thick phenomenon, and three grades of shell of column separation chambers 4 are set; The main thick phenomenon of the race that forms because of flow is excessive that can prevent exactly; The interference of the high strength eddy flow when promptly three grades of shell of column separation chambers 4 can resist high flow capacity in the one-level awl section separation chamber 2, three grades of shell of column separation chambers 4 are cushion spaces of bigger a, fluid stable, the rainwater that can be high flow capacity provides the sufficient time of staying.
Said sloping baffle 12 is positioned at the top of the outlet at bottom of said conical baffle 10; Can prevent the generation of short flow phenomenon, sloping baffle 12 from its lateral its central authorities downward-sloping, and be provided with shirt rim 12.1 in the bottom; Can control in the two stage column section separation chamber 3 liquid to the outflow of three grades of shell of column separation chambers 4; Delay effect once more can be played to floating thing in the shirt rim 12.1 of sloping baffle 12 bottoms, can effectively prevent to run thick simultaneously.
The said cover 13 of Suspension Control again is downward-sloping laterally from central authorities, and seal at the top, bottom opening; Be positioned at the below of the outlet at bottom of conical baffle 10; And, can prevent that the strong eddy flow of one-level awl section separation chamber 2 from causing disturbance to basic sediment by bracing frame 15 supports, effective control suspends again; In addition, the bottom opening of Suspension Control cover 13 design again can be played certain delay effect to floating thing in the deposit apotheca 5 and particle.Said isolation sloping baffle 14 is arranged on the below of Suspension Control cover 13 again, can sediment be guided in the deposit apotheca 5, and can unite the control disturbance with Suspension Control cover 13 again and suspend.Suspension Control cover 13 and partly isolate the collocation of sloping baffle 14 again; Can prevent of the interference of powerful eddy flow to basic sediment, and, the sediment in the deposit apotheca 5; Through Suspension Control cover 13 again with partly isolate the measure of blocking of sloping baffle 14, can prevent the suspension again under the high flow capacity.
Said cylindrical shell 6 can be used for the fixing internal member.Said tangential water inlet pipe 7 is connected to cylindricality deflector 9 and extends to cylindrical shell 6 outsides, and rainfall runoff flow into cylindricality deflector 9 inside through tangential water inlet pipe 7; Because tangential water inlet pipe 7 is tangentially to be connected to said cylindricality deflector 9, institute so that rainwater to flow into cylindricality deflector 9 inner and rotate around the central axis of one-level awl section separation chamber 2.Said outlet pipe 8 is connected to cylindrical shell 6 and extends to the outside of cylindrical shell 6, and rainwater is discharged through outlet pipe 8.
The course of work of the utility model is following: mix the sedimentary rainwater of suspension, floating thing and coarse granule and get into cylindricality deflector 9 inside by tangential water inlet pipe 7; And formation eddy flow; At centrifugal force, entad under the acting in conjunction of buoyancy and fluid drag force; Density mixes suspension and floating thing less than water, will move towards the center of rotational flow field in the horizontal direction, finally before getting into one-level awl section separation chamber 2, is trapped to floating thing apotheca 1.In addition, in the position that vertically will rotate down to conical baffle 10 outlet at bottoms, segment fluid flow is carried under one's arms to mix and is done the reciprocation cycle motion on suspension and the floating thing counter steer.
Said coarse granule sediment is then carried under one's arms by residual fluid and is got into secondary shell of column separation chamber 3; In secondary shell of column separation chamber 3; The inertia strength that the dynamics that rainwater upwards flows out flows out downwards from conical baffle 10 bottoms less than the coarse granule sediment; Make most coarse granule sediment do 180 ° driving in the wrong direction, and finally be sink to deposit apotheca 5, promptly be mixed with of the outlet of the sedimentary runoff of coarse granule through one-level awl section separation chamber 2; And secondary shell of column separation chamber 3 stable, at a slow speed rotation down, in the deposit apotheca 5 bottom being precipitated to.
Rainwater through after 3 processing of secondary shell of column separation chamber is then crossed sloping baffle 12, gets into three grades of shell of column separation chambers 4 and carries out the end reason, and the outlet pipe 8 through cylindrical shell top effluxes at last.
The utility model pollutes the application example in the current control of footpath at the simulation heavy rain: the cylindricality deflector internal diameter in the utility model is 250mm, highly is 250mm; The conical baffle cone angle is 7 °, highly is 500mm, back cut diameter 250mm; The spiral deflector angle of inclination is 11 °, and width is 60mm, highly is 250mm; Partly isolating the sloping baffle angle of inclination is 45 °, highly is 150mm, and back cut diameter is 450mm; Suspension Control cover angle of inclination is 30 ° again, highly is 50mm, and back cut diameter is 50mm; The sloping baffle angle of inclination is 23 °, highly is 50mm, and back cut diameter is 550mm, and shirt rim, bottom diameter is 220mm, highly is 30mm; Tangential water inlet pipe diameter is 65mm, and diameter of outflow tube is 100mm.Separating effect: when inlet meso-position radius D50 excursion is within 45～61 μ m; Is 25.79～38.66% to particle diameter in the removal efficient of the solid particle of 0～45 μ m; Is 48.41～69.18% to particle diameter in the removal efficient of the solid particle of 45～125 μ m, and the removal efficient of the solid particle of particle diameter more than 125 μ m has been reached 86.31～96.80%.
Claims (10)
1. multistage integrated fluid power cyclone separator; Comprise cylindrical shell (6) and be connected tangential water inlet pipe (7), the outlet pipe (8) on the cylindrical shell (6); It is characterized in that: said cylindrical shell (6) is made up of top cover (6.1), base plate (6.2) and sidewall (6.3), and wherein top cover (6.1) is detachable cover plate or partially perforation cover plate; The inside upper part center of said cylindrical shell (6) is provided with cylindricality deflector (9) and this cylindricality deflector (9) is connected on the sidewall (6.3) of cylindrical shell through cylindricality deflector bracing frame (16); The lower end of cylindricality deflector (9) is connected with the up big and down small conical baffle of diameter (10); Be provided with separation chamber's sloping baffle (12) in the cavity between conical baffle (10) and the sidewall (6.3), the sidewall (6.3) of the below of conical baffle (10), cylindrical shell is provided with deposit apotheca separation baffles; Said tangential water inlet pipe (7) pass cylindrical shell sidewall (6.3), be connected on the cylindricality deflector (9), said outlet pipe (8) is connected on the sidewall (6.3) of cylindrical shell of separation chamber's sloping baffle (12) top.
2. multistage integrated fluid power cyclone separator according to claim 1; It is characterized in that: said deposit apotheca separation baffles comprises Suspension Control cover (13) again and partly isolates sloping baffle (14); The said cover of Suspension Control again (13) be connected through Suspension Control cover bracing frame (15) again that sidewall (6.3) is gone up and again Suspension Control cover (13) by downward-sloping around the middle mind-set, said partly isolate sloping baffle (14) be connected sidewall (6.3) go up and partly isolate sloping baffle (14) by around downward-sloping to the center.
3. multistage integrated fluid power cyclone separator according to claim 2, it is characterized in that: the angle of inclination of the said cover of Suspension Control again (13) is 15 °～45 °, the angle of inclination that partly isolates sloping baffle (14) is 30 °～60 °.
4. multistage integrated fluid power cyclone separator according to claim 1 is characterized in that: on the madial wall of the below of said tangential water inlet pipe (7), said conical baffle (10), be provided with spiral deflector (11).
5. multistage integrated fluid power cyclone separator according to claim 4 is characterized in that: the angle of inclination of said spiral deflector (11) is 5 °～15 °.
6. multistage integrated fluid power cyclone separator according to claim 1; It is characterized in that: said separation chamber sloping baffle (12) is connected on the sidewall (6.3) of cylindrical shell (6), and sloping baffle (12) is downward-sloping to the center by all around.
7. multistage integrated fluid power cyclone separator according to claim 6, it is characterized in that: the lower end of said separation chamber sloping baffle (12) is provided with shirt rim (12.1).
8. multistage integrated fluid power cyclone separator according to claim 6 is characterized in that: the angle of inclination of said separation chamber sloping baffle (12) is 15 °～30 °.
9. multistage integrated fluid power cyclone separator according to claim 1, it is characterized in that: the horizontal level of the delivery port of said tangential water inlet pipe (7) is lower than the horizontal level of the water inlet of outlet pipe (8).
10. multistage integrated fluid power cyclone separator according to claim 1 is characterized in that: the cone angle of said conical baffle (10) is 5 °～10 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205368933U CN202410265U (en) | 2011-12-20 | 2011-12-20 | Multilevel integrated fluid power cyclone separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205368933U CN202410265U (en) | 2011-12-20 | 2011-12-20 | Multilevel integrated fluid power cyclone separator |
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| Publication Number | Publication Date |
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| CN202410265U true CN202410265U (en) | 2012-09-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011205368933U Expired - Fee Related CN202410265U (en) | 2011-12-20 | 2011-12-20 | Multilevel integrated fluid power cyclone separator |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102512857A (en) * | 2011-12-20 | 2012-06-27 | 北京建筑工程学院 | Multistage integrated hydrodynamic cyclone separator |
| CN104338346A (en) * | 2014-04-18 | 2015-02-11 | 总装备部工程设计研究总院 | Fluid distributing system and multiphase separator thereof |
| CN104906835A (en) * | 2015-05-19 | 2015-09-16 | 郑小青 | Mud-water separation device and slurry mud-water separation method |
| CN104998445A (en) * | 2015-07-31 | 2015-10-28 | 江苏楷益智能科技有限公司 | Settler |
| CN105457352A (en) * | 2014-09-09 | 2016-04-06 | 宜兴市天马环保工程有限公司 | Internal cyclone structure of novel cyclone precipitator |
-
2011
- 2011-12-20 CN CN2011205368933U patent/CN202410265U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102512857A (en) * | 2011-12-20 | 2012-06-27 | 北京建筑工程学院 | Multistage integrated hydrodynamic cyclone separator |
| CN102512857B (en) * | 2011-12-20 | 2014-05-28 | 北京建筑工程学院 | Multistage integrated hydrodynamic cyclone separator |
| CN104338346A (en) * | 2014-04-18 | 2015-02-11 | 总装备部工程设计研究总院 | Fluid distributing system and multiphase separator thereof |
| CN104338346B (en) * | 2014-04-18 | 2016-01-06 | 总装备部工程设计研究总院 | Fluid supply system and multiphase separator thereof |
| CN105457352A (en) * | 2014-09-09 | 2016-04-06 | 宜兴市天马环保工程有限公司 | Internal cyclone structure of novel cyclone precipitator |
| CN104906835A (en) * | 2015-05-19 | 2015-09-16 | 郑小青 | Mud-water separation device and slurry mud-water separation method |
| CN104998445A (en) * | 2015-07-31 | 2015-10-28 | 江苏楷益智能科技有限公司 | Settler |
| CN104998445B (en) * | 2015-07-31 | 2016-09-07 | 江苏楷益智能科技有限公司 | A kind of settler |
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