CN209663527U - For separating the cyclone separator and dip-tube of gas - Google Patents
For separating the cyclone separator and dip-tube of gas Download PDFInfo
- Publication number
- CN209663527U CN209663527U CN201790000817.6U CN201790000817U CN209663527U CN 209663527 U CN209663527 U CN 209663527U CN 201790000817 U CN201790000817 U CN 201790000817U CN 209663527 U CN209663527 U CN 209663527U
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- Prior art keywords
- dip
- tube
- nozzle
- shell
- cyclone separator
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C5/00—Apparatus in which the axial direction of the vortex is reversed
- B04C5/12—Construction of the overflow ducting, e.g. diffusing or spiral exits
- B04C5/13—Construction of the overflow ducting, e.g. diffusing or spiral exits formed as a vortex finder and extending into the vortex chamber; Discharge from vortex finder otherwise than at the top of the cyclone; Devices for controlling the overflow
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- Cyclones (AREA)
Abstract
The utility model relates to a kind of dip-tubes (2) and cyclone separator for the extraction air-flow from cyclone separator (1).During operation, gas is flowed into dip-tube (2) by gas access (8) and is flowed out again via gas vent (9).Dip-tube (2) includes the first area for being designed as nozzle, nozzle gradually becomes smaller to minimum diameter with assembling from nozzle inside diameter, and dip-tube (2) includes second area, gas flows through the second area positioned at first area downstream during operation, and second area is designed to diffuser, diffuser gradually become smaller directionally focusedly to the minimum diameter along first area from diffuser inside diameter.Nozzle has the geometry of the side surface in conical form, and side surface is relative to Axial-rotational Symmetry, and wherein the angle between side surface and axis is between 1 ° and 88 °.The purpose of the utility model is to provide a kind of novel dip-tubes for making cyclone separator that there is high separating efficiency and middle pressure to lose.
Description
Technical field
The utility model relates to a kind of dip-tubes for the gas bleeding from cyclone separator, wherein gas during operation
Dip-tube is flowed by gas access, and is flowed out again from dip-tube by gas vent.In addition, the utility model further relates to one
For kind for separating the cyclone separator of solid particle and/or at least one liquid from air-flow, the cyclone separator includes shell
The opening for air-flow and solid particle and/or at least one liquid to be concomitantly introduced into shell in body, shell is used for solid
The discharge port of particle and/or liquid and at least one it is according to the present utility model for from shell gas bleeding draw
Pipe.
Background technique
For most of different types of applications (such as round fluidized bed combustion (CFB burning), calcining, oil are recycled) and
For other processing, it is necessary to feed gas into next and/or last cleansing phase (such as electric precipitator
(ESP)) it removes from hot flue gases or product gas mixture containing solid before and/or separates solid, to meet environment
Or especially product specification.
In general, using gas cyclone separator is mixed from hot flue gases or product gas in the application field of these processing
Close the solid that particle form is filtered out in object.This cyclone separator is also used to steam power plant, in steam generator and whirlpool
From separation water in live steam or for the condensate separation in gas cooler between turbine.
Many functions and performance-relevant important ginseng with this cyclone separator have been had studied in enough degree
Number.These parameters include pressure, temperature, speed and the particulate load of gas and the geometry of cyclone separator.Here, special
Not, the corresponding cover board of cyclone separator or lid, the dip-tube of also referred to as vortex finder and discharge port and solid particle
Discharge is related.
Compared with other technologies for separating solid and gas, one of cyclone separator is the disadvantage is that this isolated effect
Rate is relatively low, especially in the case where fines of the size less than 10 μm.Efficiency about this sized particles is most
It is limited to 90 to 95% or even lower.
Since at the end of the 19th century, many investigation have had been carried out to determine single operation parameter and/or geometric parameter
Influence to the separative efficiency of gas cyclone.
This separative efficiency is influenced by series of parameters (such as particulate load and particle size).In addition, cyclonic separation
Gas velocity in device and its sub-component has decisive influence to the performance of cyclone separator.In the sub-component of cyclone separator
Pure gas speed directly influenced by the geometry of these components of cyclone separator.In addition, cyclone separator is interior
Parts (such as form of dip-tube (vortex finder), top (taper lower prong), inlet duct), ventilation etc. directly affect
Dust entrainment and separative efficiency.
In addition, in order to meet different industrial requirements, about the orientation (reversed and one-way flow) of entrance, there are different rotations
Wind separator designs (vertically or horizontally).Design for high yield is characterized in that shorter main body and furthermore allows big
The larger open of handling capacity.The pressure loss under this design conditions is usually relatively low, and wherein deposition rate is relatively low.With this
On the contrary, the design for higher efficiency is characterized in that long main body and small opening.On the one hand, this design leads to deposition speed
Rate is high, also leads to pressure loss height but then.
According to the high performance counter current cyclone separator including cylindrical vortex detector a kind of known to 0 972 572 A2 of EP.
The document discloses the sizes and geometry of the extra high discrete component of efficiency for leading to cyclone separator of cyclone separator
Between relationship.
According to a kind of combustion apparatus known to 10 2,013 207724 A1 of document DE, wherein main burning is in cyclone separator shape
It is carried out in chamber.The dip-tube or vortex finder of this cyclone separator shape chamber have the form of venturi flume.
According to one kind dip-tube or vortex finder made of metal grate known to 0 447 802 A2 of document EP.Institute
It states dip-tube or vortex finder includes several honeycomb-like parts.
In general, the efficiency of well-designed cyclone separator can be improved by increasing tangential velocity, but this also causes
The pressure loss on cyclone separator increases.However, this higher pressure loss on cyclone separator is inevitably led
Cause the pressure loss in whole system higher, therefore the increase in demand to electric energy.Further, since the inner side and outer side of dip-tube it
Between subsequent high pressure gradients, the higher pressure loss also leads to the stronger stress of dip-tube.
Therefore, a purpose of the utility model is to provide one kind and cyclone separator can be made to have high separating efficiency and had
The novel dip-tube for thering is middle pressure to lose.The high loss of this dip-tube inlet by avoiding minor diameter and, is achieved.
However, realizing high tangential velocity by guiding the minor diameter in nozzle into.Due to this small cross section exist only in it is relatively short
Region on and guidance to it realized with the lesser pressure loss, therefore loss of total pressure reduces, while tangential velocity is several
It is identical.By adjusting flowing and subsequent diffuser on the same direction, a part of pressure loss is in addition also restored.
Utility model content
Above-mentioned purpose is addressed by the dip-tube and/or cyclone separator of the utility model.
Here, in order to extract air-flow out from cyclone separator, dip-tube includes gas access and gas vent.In the operation phase
Between, gas flows into dip-tube via gas access and flows out again from dip-tube via gas vent.Therefore, it is produced in dip-tube
The air-flow from gas access to gas vent direction is given birth to.
In addition, dip-tube according to the present utility model includes the first area for being designed as nozzle.The nozzle has at side
Have nozzle inside diameter, wherein the diameter of nozzle in the flowing direction from the nozzle inside diameter along gas vent directionally focusedly by
Gradually it is reduced to minimum diameter.
In addition, dip-tube includes second area, gas is flowed through positioned at secondth area at first area rear during operation
Domain.The second area is designed to diffuser, and wherein diffuser has at that side that it is distal side relative to first area and expands
Dissipate device internal diameter.The internal diameter of diffuser gradually decreases in minimum directionally focusedly from the diffuser inside diameter along first area
Diameter.
Nozzle is characterized in that the geometry of the side surface of truncated cone.Such side surface is relative to as the symmetrical of truncated cone
The Axial-rotational Symmetry of axis.The side surface can have relative to the angle of the axis value between 1 ° to 88 °,
Particularly between the value between 15 ° to 65 °.The design of this convergent nozzle is so that its production is extremely simple therefore especially cost-effective.
In addition, this is especially important for being attributed to the gas solid separation of opposite high gas flow this design reduces pressure drop.
Therefore, the cross section for the dip-tube that gas flows through is limited from the cross section limited by nozzle inside diameter to by minimum diameter
Minimum cross-section become smaller in a converging fashion.Since the neck part of dip-tube, dip-tube is swollen again along airflow direction
It is swollen to the bigger cross section limited by diffuser inside diameter.
When particle is dispersed phase, in order to separate particle from gas, the gas vent of cyclone separator must be about it
Diameter progress is appropriately designed, to avoid the high pressure loss while maintaining the major function of swirl stabilization and separative efficiency.
(wherein gas phase is dispersed phase to the hydrocyclone of separation gas and relative volumetric flow is small from the fluid with higher density
Much) it is not the case.Therefore, vortex finder can correspondingly be designed as having much smaller vortex finder diameter,
Or from rapidly (such as the index of the nozzle entrance shape (loudspeaker or Laval shape shape) relative to axis with very wide-angle
Ground, non-linearly) the vortex finder diameter that reduces.Due to very small volumetric flow of gas, this design still can
Middle pressure is caused to lose, because gas is dispersed phase.On the other hand, hydrocyclone is needed in eddy current probe inlet sometimes
Additional device (such as crash panel) enters vortex finder to avoid denser fluid.The whirlwind of particle is separated from gas
Separator does not need this device.In fact, such device is unfavorable, because particle may interact with them, this
It will lead to higher breakage of particles (such as due to particles hit).In addition, the non-linear reduction of vortex finder diameter will increase
The pressure loss of the cyclone separator of solid is separated from gas, because volumetric flow of gas is much larger than particle volume flow.
In the preferred embodiment of the utility model, the nozzle inside diameter of nozzle can be 1.2 to 8 times of minimum diameter, special
It is not 1.4 to 2.85 times.In addition, in a preferred embodiment, nozzle extends to tool from the region with the nozzle inside diameter
There is the length in the region of the minimum diameter to can be 0.14 to 4.0 times of minimum diameter.Otherwise length is according to selected
Angle and internal diameter generate.Using this geometry, effect according to the present utility model can be very strongly realized, so that
In the case where having existed middle pressure loss on cyclone separator, extraordinary separative efficiency is also realized.
In another preferred embodiment of the utility model, nozzle can have nozzle at the position of the nozzle inside diameter
Outer diameter, the nozzle od are less than the sum of nozzle inside diameter and 4 times of minimum diameters (Douter<Dinner+4×d).In other words, it is spraying
The end of mouth, thus at the position for being characterized in that the nozzle inside diameter, it is disposed with ring, wherein the width of the ring is less than minimum
4 times (< 4 × d) of internal diameter.The arrangement of ring with these sizes is used in particular for the nozzle of the side surface form in truncated cone.It utilizes
This ring, the geometry of dip-tube can adjust the geometry of Laval nozzle in a particularly simple way.This ring
It is adjusted particularly suitable for subsequent supplement, thus for example dip-tube can be adjusted according to modified operating parameter.
In another preferred embodiment of the utility model, nozzle od can be less than nozzle inside diameter and 4 times of minimum diameters
The sum of (Douter<Dinner+ 4 × d), and nozzle inside diameter can be 1.2 to 8 times of minimum diameter.It is particularly preferred that outside nozzle
Diameter can be less than the sum of nozzle inside diameter and 0.25 times of minimum diameter (Douter<Dinner+ 0.25 × d), nozzle inside diameter can be most
1.4 to 2.85 times of small internal diameter.The geometry is further characterized in that the form of ring, which is arranged in the end of nozzle
Place, therefore be arranged at the position of the nozzle inside diameter.This structure is also used for the nozzle that there is sonic nozzle to design.Same benefit
With the ring of this geometry, the air-flow by dip-tube especially can influenced in a particularly simple way later.
In a preferred embodiment of the utility model, diffuser is with the side surface for being respectively truncated cone or cylinder
Design.This geometry is relative to axis (being respectively the axis of symmetry of truncated cone or cylinder) rotational symmetry.In this feelings
Under condition, the angle between side surface and axis is preferably between 3 ° and 15 ° between 0 ° and 45 °.Truncated cone or cylinder
The axis of symmetry is also respectively the axis of symmetry of diffuser, and can also be the axis of symmetry of nozzle.Since diffuser is usually
King-sized component, therefore using this particularly simple structure of diffuser, the significant reduction of cost may be implemented.
In another preferred embodiment of the utility model, connection cylinder can be set between nozzle and diffuser.
Therefore, connection cylinder has the wherein diffuser that nozzle is connected to diffuser most at position of the nozzle with minimum diameter
At the position of small internal diameter.Therefore, it connects cylinder and/or has in connector identical with minimum diameter at connecting portion
Diameter.The length of the corresponding connection cylinder or truncated cone that extend to diffuser from nozzle be preferably smaller than minimum diameter 8 times (L < 8 ×
d).Connecting cylinder has very simple geometry, so that the channel from diffuser to nozzle is the logical of a milder
Road.Therefore, it is possible to further improve the flowing by dip-tube, therefore the especially low pressure loss may be implemented.In addition, from spray
The connection cylinder of mouth to diffuser can have different thickness, so as to due to nozzle and diffuser or cylinder itself not
Stack pile and provide more preferably connecting between nozzle and diffuser in the performance for wearability or any deformation and configuration aspects
It connects, usually that is, cylindrical profile has the curved profile of biconvex, concave-concave, plano-convex or plano-concave.
Another deformation scheme is characterized in that the front in nozzle and/or the rear in diffuser mention respectively in the flowing direction
For at least one additional nozzle or an additional diffuser.Design including several convergent nozzles being mutually adapted is very simple
It is single, therefore its production cost is low.When dip-tube should be optimally adjusted according to operating parameter, several nozzles for being mutually adapted
And/or diffuser provides high flexibility.In the case where this design, radius of curvature can be along the longitudinal direction of nozzle
Change, wherein the smallest radius of curvature is located at the position of highest curvature.
In another preferred embodiment, the connecting portion between nozzle and diffuser and/or single-nozzle and/or diffuser
It is smooth.For example, connecting portion can be polishing.By this smoothing, avoid to the negative of gas flow behavior
It influences.When between nozzle and diffuser setting connection cylinder when, when connection cylinder and nozzle between connecting portion and/
Or the connecting portion between connection cylinder and diffuser, when being smooth (such as being polished), by the same token, this is
It is advantageous.
In another preferred embodiment, at least part of dip-tube, such as connection cylinder, diffuser and/or nozzle
Negative profile (negative profile) separately constitute a device part or multiple devices.For the weight of alleviator,
They can be designed as hollow body.In other words, dip-tube includes facing device inside it, thus formed connection cylinder,
The negative profile of diffuser and/or nozzle.This geometry is relative to axis (axis of symmetry of i.e. negative profile) rotational symmetry.
Since the weight of device is usually less than the weight of steel, using weight saving and/or particularly simple structure (such as
The fixation of dip-tube), sizable cost, which may be implemented, to be reduced.Therefore, this causes in the feelings that extensive building change is not present
Cyclone separator and/or dip-tube under condition in improvement equipment it is extremely simple a possibility that.
In principle, it is preferably prepared by heat-resisting and/or corrosion-resistant material (such as ceramic fibre material, carbon fiber etc.)
At least some parts of dip-tube according to the present utility model, and/or at least some parts for being optionally the dip-tube mention
For preventing the surface corroded or coating.
In addition, the utility model includes the whirlwind point for separating solid particle and/or at least one liquid from air-flow
From device, the cyclone separator includes dip-tube defined above.
The air-flow of introducing can be also for example steam, only become to have by a kind of ingredient of subsequent condensation air-flow small
The air-flow of liquid particles.For example, this can only be realized by the successive cooling in cyclone separator.
Cyclone separator according to the present utility model includes shell, the opening for introducing air-flow in shell, for dividing
From solid or liquid discharge port and dip-tube for gas to be discharged.
In this case, in general, shell may include the cylindrical area for wherein arranging the opening for introducing air-flow.
In addition, shell may include the region conically assembled since cylindrical area along gravity direction.In the conical region
End, therefore discharge port is installed at the minimum point relative to gravity direction.In addition, cyclone separator includes dip-tube,
The dip-tube can be arranged at the side opposite with the discharge port at case lid of shell.According to the utility model, this is drawn
Take the feature of pipe as described above.
Opening in shell can be designed so that air-flow and the solid particle being contained therein and/or at least one liquid
Body is introduced into shell with tangential direction.Therefore, start circular motion in the housing.Then make air-flow together with particle with spiral shape
Formula is moved down on the direction of optional conical region.Since shell gradually becomes smaller, thus circular motion consumingly increases simultaneously
Therefore the strong centrifugal force having an impact to particle is formed.Therefore, particle moves in an outward direction, and locates particles hit on the outside
Onto the wall of shell.Fall to the direction of discharge port downwards in gravitational field from the particle separated in air-flow in this way
On.Being also with the liquid that air-flow separates, the liquid flows to the lowermost extent of shell, i.e. outlet side along the wall of shell
Mouthful, and can be taken out from shell at discharge port.Therefrom having extracted particle and/or the air-flow of liquid can then lead to
Dip-tube (vortex finder) is crossed further out cyclone separator.
In a preferred embodiment of the utility model, at least one dip-tube is arranged so that it is at least partly stretched
Into shell.In this case, dip-tube may be disposed so that its gas access is placed in shell, and its gas vent
It is placed in hull outside.Dip-tube can also be fully disposed in shell, so that the shell that gas vent is positioned directly in shell is opened
At mouthful.In addition, dip-tube can be arranged in shell and the entrance of dip-tube is positioned directly in the opening of shell from outside
Outside body.Therefore, equally by arranging dip-tube in cyclone separator, flow behavior can be influenced.Therefore, dip-tube is utilized
It, can be by dip-tube according to the present utility model in the intracorporal arrangement of the shell with the given geometry of cyclone separator shell
To adjust cyclone separator according to accurate operating parameter.
In another preferred embodiment of the utility model, several such dip-tubes can be provided, wherein drawing
The symmetrically or non-symmetrically arrangement of pipe is possible.For example, dip-tube can be relative to a plane or several planes with mirror image pair
The mode of title is arranged.Another possibility is the axial symmetry relative to mirror shaft.In this case, the also only position of dip-tube
It may be symmetrical for setting, and total symmetry is for example interrupted by different sizes, length or the insertion depth of dip-tube.It is logical
It crosses using several dip-tubes, the gas handling capacity of cyclone separator can be increased, without using single big dip-tube.Individually
The production and installation of big dip-tube are than using several small dip-tubes much more complex.Using symmetrically or non-symmetrically arranging, according to
Operating parameter, which adjusts cyclone separator, has many freedom degrees.
In a preferred embodiment of the utility model, at least one dip-tube is at least partly by cylinder collet.
In such a case, it is possible to adjust the diameter of cylinder according to dip-tube, and correspondingly the diameter of cylinder can be nozzle
Internal diameter or nozzle od.In this case, in addition cylinder can be more than nozzle inside diameter, be more than that wherein nozzle feature exists
It is protruded into shell in the position of nozzle inside diameter.This cylinder easily can be manufactured and be installed, and can be caused
The efficiency of cyclone separator further increases.
In another preferred embodiment of the utility model, cylinder can extend to the inside of shell from shell, wherein
Several dip-tubes are arranged in cylinder.Therefore, single dip-tube can be by a cylinder encirclement or whole group dip-tube quilt
One single cylinder surrounds.When using several dip-tubes, the arrangement around a single cylinder of several dip-tubes can also be with
Improve the efficiency of cyclone separator.
In another preferred embodiment of the utility model, the region of shell (at least one dip-tube by the region into
Enter in shell or in which at least one dip-tube be positioned directly on shell) there is circular form.Then, dip-tube can phase
For the regional center or prejudicially arrange.In the case where several dip-tubes have the arrangement of the axis of symmetry, the symmetry axis
Line with center or can be eccentrically located on the area.Center arrangement allows the particularly simple installation of cyclone separator, because
Such as the orientation of lid is unrelated, and eccentric and/or unsymmetrical arrangement for example considers the position of the opening for introducing air-flow
It sets.
Detailed description of the invention
Hereinafter, by embodiment and the utility model is explained with reference to the accompanying drawings.Here, it is described and/or describes
Feature independently or in any combination form this reality independently of its general introduction in Patent right requirement or its backward reference
With novel theme.
Fig. 1 schematically shows the structure of cyclone separator,
Fig. 2 a schematically shows dip-tube,
Fig. 2 b schematically shows the dip-tube with connector,
Fig. 3 a is schematically shown with the dip-tube for drawing angle,
Fig. 3 b schematically shows the nozzle with ring,
Fig. 4 schematically shows have band drafting angle diffuser dip-tube,
Fig. 5 a shows the arrangement of the dip-tube in cyclone separator,
Figure 5b shows that another arrangement of the dip-tube in cyclone separator,
Fig. 5 c shows another arrangement of the dip-tube in cyclone separator,
Fig. 5 d shows another arrangement of the dip-tube in cyclone separator,
Fig. 6 a shows the arrangement of dip-tube, wherein there is cylinder at cap,
Fig. 6 b shows another arrangement of dip-tube, wherein there is cylinder at cap,
Fig. 6 c shows another arrangement of dip-tube, wherein there is cylinder at cap,
FIG. 6d shows that the arrangement positioned at cylinder intracorporal several dip-tubes,
Fig. 7 a shows being arranged symmetrically for dip-tube,
Fig. 7 b shows the unsymmetrical arrangement of dip-tube,
Fig. 8 a shows the cyclone separator with the dip-tube being arranged symmetrically, and
Fig. 8 b shows the cyclone separator of the dip-tube with arranged off-centre.
Specific embodiment
For being shown schematically in Fig. 1 from the basic structure for the cyclone separator 1 for separating solid or liquid in air-flow.
Cyclone separator 1 includes shell 3, and the shell includes cylindrical area 5 and conical region or conical area 6.In cylindrical shape
Locating gas service 4 in region 5, air-flow pass through the gas service injection together with particle.Cyclone separator 1 is logical
Often it is arranged so that the direction of the downwardly directed gravitational field of conical section 6.Discharge port 7 is positioned at the minimum point of conical section,
The particle and/or liquid extracted from air-flow can be discharged by the discharge port.
During operation, air-flow passes through gas service 4 together with particle and is introduced into shell 3.This generally tangential side
To realization, to directly generate the circular motion of air-flow.Air-flow is moved to conical region from gas service 4 in a spiral form
On 6 direction.Particle is transported to the outer wall of cyclone separator 1 by centrifugal force, and particle passes through at the outer wall
The influence of gravity and be moved on the direction of discharge port 7.Then, gas is moved upwards to enter by gas access 8 and be drawn
Pipe 2, and come out by gas vent 9 from dip-tube 2 as the gas of purification.
Fig. 2 a shows the basic structure of dip-tube 2, and the dip-tube has the diffuser 12 being located in second area 11
With the nozzle 13 being located in first area 10, diffuser and nozzle are connected with each other at connecting portion 14.Nozzle 13 includes having
Nozzle inside diameter DinnerWide opening and the narrow opening with small internal diameter d.Diffuser is at its connecting portion 14 with nozzle 13
It is further characterized in that minimum diameter d, and the diameter of the direction upper diffuser in the other end towards diffuser is become greater to more again
Wide internal diameter.
Fig. 2 b shows the basic structure of the dip-tube 2 including diffuser 12, nozzle 13 and connector 15, the connector
It is connected at connecting portion 14 with diffuser 12 and nozzle 13.Connector 15 is characterized in that diameter corresponds to minimum diameter d.
In Fig. 2 a and 2b, the gas access 8 of dip-tube and one end of nozzle 13 and/or the position of nozzle inside diameter weight
It closes.But this is not necessarily such case.But can also be arranged at nozzle other components (such as cylinder), wherein it is described its
One end of its component rather than nozzle forms gas access.
Fig. 3 a shows the dip-tube 2 with Fig. 2 a for drawing size.Interconnecting piece between diffuser 12 and nozzle 13
At position, dip-tube is characterized in that the minimum diameter d.Nozzle 13 is designed as the side surface of frustum of a cone, and in modification side
In the case where case, nozzle is plotted as dotted line, and nozzle can have length or height H.Have height lesser with depicted as solid lines
Very flat structures, i.e. short structure nozzle 13.The nozzle of conical form is characterized in that the axis of symmetry 20, wherein truncated cone phase
For 20 rotational symmetry of the axis of symmetry.In addition, the nozzle of conical form has small for the variant schemes for being plotted as dotted line
Angle α.In the variant schemes for being plotted as solid line, angle is bigger.
Fig. 3 b shows single-nozzle 13, wherein additional ring 18 is arranged in the end of nozzle.Utilize the ring 18, nozzle 13
There is internal diameter D in its endinnerAnd outer diameter Douter, outer diameter DouterExpand due to ring 18.
Fig. 4 shows the dip-tube 2 with the diffuser 12 with drafting angle β of Fig. 2 a.The diffuser 12 of dip-tube 2 is set
It is calculated as truncated cone and there is rotation axis 21.
Fig. 5 a to 5d shows different insertion depths of the dip-tube 2 in the shell 3 of cyclone separator.
In fig 5 a, dip-tube 2 is arranged so that it is fully inserted into shell 3, thus 8 cloth of gas access of dip-tube 2
It sets in the lower section of the lower edge of gas service 4.The gas access 8 of dip-tube 2 is placed in shell 3.
In figure 5b, dip-tube 2 only partially protrudes into shell 3 so that the gas access 8 of dip-tube 2 be located in
At the identical height of the lower edge of gas service 4.
Fig. 5 c shows a variant schemes, wherein only the approximately half of of dip-tube 2 protrudes into shell 3, so that drawing
The gas access 8 of pipe 2 is arranged in the top of the lower edge of gas service 4.
In figure 5d, entire dip-tube 2 is arranged in the outside of shell 3.From the outside of dip-tube 2 by the gas of dip-tube 2
Entrance 8 is directly arranged at the lid 17 of shell 3.
Fig. 6 a shows the dip-tube 2 surrounded completely by cylinder 19.Cylinder and dip-tube are arranged in the lid 17 of shell 3
Place.The each a part with lid 17 for illustrating only shell 3 of Fig. 6 a to 6d.In this case, the region of 17 lower section of lid is
The inside of shell.Therefore, cylinder and dip-tube 2 are fully inserted into shell 3.
Fig. 6 b shows one embodiment, and wherein dip-tube 2 only partially protrudes into shell 3, so that dip-tube 2
Gas vent 9 is arranged in outside shell 3, and gas access 8 is arranged in shell 3.Cylinder 19 is fully located in shell 3
Inside interior and that shell 3 is reached more than dip-tube 2.
Fig. 6 c shows one embodiment, and wherein dip-tube 2 is directly installed on from lid 17 from the outside of shell 3.Cylinder
19 are located at same position in shell 3, at the opposite side of dip-tube 2.
FIG. 6d shows that several dip-tubes 2 to be arranged in the top view on lid 17, and shows together in lower area
It is fully located in the side view of the identical set of the dip-tube 2 in the cylinder 19 in shell 3.The arrangement of dip-tube can be as above
Change describedly, referring to 6b and 6c.
Fig. 7 a shows the arrangement of several dip-tubes in the shell 3 of cyclone separator 1, these dip-tubes are arranged in whirlwind
At the lid 17 of the shell 3 of separator 1.In this case, the arrangement of dip-tube 2 is symmetrical relative to the axis of symmetry, described
The axis of symmetry passes through centrally located dip-tube 2.
Fig. 7 b shows the arrangement also with Fig. 7 a for the two additional dip-tubes 2 arranged in an asymmetrical fashion.In addition,
Fig. 7 b shows the dip-tube 2 in the shell 3 for not being fully inserted into cyclone separator 1 at the center of being arranged in, therefore some draws
Pipe is taken to be can be positioned at different height relative to the gas access of nozzle.
Fig. 8 a and 8b show the center arrangement of dip-tube 2 and the difference of arranged off-centre.In Fig. 8 a, dip-tube 2 is opposite
It is disposed concentrically upon in lid 17, and dip-tube 2 is arranged in the outside at the center in figure 8b.Therefore, it is drawing for arranged off-centre
Pipe 2.In addition, in figure 8b, referring to eccentricity and direction by arrow.
Embodiment example:
Operation data:
The geometry of cyclone separator:
As a result:
It is expected that separative efficiency η :~96% (conservative) in the case where the preferred embodiment of the utility model is simultaneously > 96%
It is expected that P :~22 millibars of pressure loss Δ in the case where the preferred embodiment of the utility model when 100m/s (is protected
Keep) and < 25 millibars
Reference signs list
1 cyclone separator
2 dip-tubes
3 shells
4 gas services
5 cylindrical areas
6 conical regions
7 discharge ports
8 gas accesses
9 gas vents
10 first areas
11 second areas
12 diffusers
13 nozzles
14 connecting portions
15 connection cylinders
17 lids
18 rings
19 cylinders
The axis of symmetry of 20 nozzles
The axis of symmetry of 21 diffusers
D minimum diameter
DinnerNozzle inside diameter
DouterNozzle od
The height of H nozzle
Claims (14)
1. a kind of dip-tube (2) is used for the gas bleeding from cyclone separator (1), wherein gas is via gas during operation
Entrance (8) flows into dip-tube (2) and flows out again via gas vent (9), which is characterized in that dip-tube (2) includes being designed as spraying
The first area (10) of mouth (13), the nozzle is from nozzle inside diameter (Dinner) gradually become smaller minimum diameter (d) with assembling, and
Dip-tube (2) includes second area (11), and gas flows through described second positioned at first area (10) downstream during operation
Region, and the second area is designed to diffuser (12), and the diffuser is from diffuser inside diameter along first area
The minimum diameter (d) is gradually become smaller directionally focusedly, and nozzle (13) has the geometry of the side surface in conical form
Shape, the axis of symmetry (20) rotational symmetry of the side surface of nozzle relative to nozzle, wherein the side surface of nozzle with
Angle (α) between the axis of symmetry (20) is arranged between 1 ° and 88 °, and wherein in the upstream of the nozzle (13)
At least one other nozzle and/or other diffusers are set in the downstream of the diffuser (12).
2. dip-tube according to claim 1, which is characterized in that the side surface and the axis of symmetry (20) of nozzle
Between angle (α) between 15 ° and 65 °.
3. dip-tube according to claim 1, which is characterized in that the nozzle inside diameter (D of nozzle (13)inner) it is described
1.2 to 8 times of minimum diameter (d) and/or nozzle (13) from the nozzle inside diameter (Dinner) arrive the minimum diameter (d) length
Degree (H) is 0.2 to 4 times of the minimum diameter (d).
4. dip-tube described in any one of -3 according to claim 1, which is characterized in that nozzle (13) is in the nozzle inside diameter
(Dinner) position at have be less than the nozzle inside diameter (Dinner) nozzle od with the sum of 4 times of minimum diameters (d)
(Douter)。
5. dip-tube described in any one of -3 according to claim 1, which is characterized in that nozzle od meets nozzle od
(Douter) < nozzle inside diameter (Dinner)+4 × minimum diameter (d), and the nozzle inside diameter (Dinner) it is in the minimum
1.2 to 8 times of diameter (d).
6. dip-tube described in any one of -3 according to claim 1, which is characterized in that it is in cut that the diffuser (12), which has,
The geometry of the side surface of tapered, the axis of symmetry (21) rotational symmetry of the side surface of diffuser relative to diffuser,
Angle (β) between the side surface and the axis of symmetry (21) of middle diffuser is between 0 ° and 45 °.
7. dip-tube described in any one of -3 according to claim 1, which is characterized in that in the nozzle (13) and the expansion
Arrangement connection cylinder (15) between device (12) is dissipated, wherein the connector internal diameter and the minimum diameter of the connection cylinder
(d) identical.
8. dip-tube according to claim 7, which is characterized in that the connection cylinder (15) is than the minimum diameter
(d) diffuser (12) are extended to from nozzle (13) in 8 times of shorter length.
9. a kind of cyclone separator, for separating solid particle and/or at least one liquid, the cyclone separator from air-flow
Including being used to air-flow and solid particle and/or at least one liquid being concomitantly introduced into shell in shell (3), shell (3)
(3) opening in, for the discharge port (7) of solid particle and/or liquid and for gas bleeding to be extremely from shell (3)
A few dip-tube (2), which is characterized in that dip-tube (2) is dip-tube according to claim 1.
10. cyclone separator according to claim 9, which is characterized in that at least one described dip-tube (2) is arranged to make
It is at least partly reached in the shell (3) or at least one described dip-tube (2) is arranged in the outer of the shell (3)
The portion and gas access (8) of dip-tube (2) is positioned directly in another opening of shell (3).
11. cyclone separator according to claim 9, which is characterized in that multiple dip-tubes (2) are provided with, wherein described
The arrangement of multiple dip-tubes (2) designs in a manner of symmetrically or non-symmetrically.
12. cyclone separator according to any of claims 9 to 11, which is characterized in that it is described at least one draw
Pipe (2) is taken at least partly to be surrounded by cylinder (19), wherein the diameter of the cylinder (19) can be greater than in the minimum
Diameter (d) is simultaneously less than or equal to the nozzle od (Douter) and/or the cylinder (19) protrude past the nozzle inside diameter
(Dinner) and enter in shell (3).
13. cyclone separator according to any of claims 9 to 11, which is characterized in that cylinder (19) is from shell
Body (3) extends to the inside of shell (3), and plurality of dip-tube (2) is arranged in the cylinder (19).
14. cyclone separator according to any of claims 9 to 11, which is characterized in that shell (3) it is described extremely
A few dip-tube (2) enters in shell (3) through it or in which at least one described dip-tube (2) is positioned directly in shell (3)
On that panel region (17) there is circular form, and at least one described dip-tube (2) central place or be prejudicially arranged in shell
On the region (17) of body.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE202016102385.8U DE202016102385U1 (en) | 2016-05-04 | 2016-05-04 | Cyclone and dip tube for the separation of particles from a gas |
| DE202016102385.8 | 2016-05-04 | ||
| PCT/EP2017/060624 WO2017191242A1 (en) | 2016-05-04 | 2017-05-04 | Cyclone and dip tube for separating a gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209663527U true CN209663527U (en) | 2019-11-22 |
Family
ID=56117087
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201790000817.6U Active CN209663527U (en) | 2016-05-04 | 2017-05-04 | For separating the cyclone separator and dip-tube of gas |
Country Status (7)
| Country | Link |
|---|---|
| CN (1) | CN209663527U (en) |
| AU (2) | AU2017101842A4 (en) |
| BR (1) | BR212018072086U2 (en) |
| DE (1) | DE202016102385U1 (en) |
| RU (1) | RU191344U1 (en) |
| UA (1) | UA138563U (en) |
| WO (1) | WO2017191242A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113198624A (en) * | 2021-05-08 | 2021-08-03 | 华东理工大学 | Method and device for strong mass transfer countercurrent contact of two-phase fluid |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2567866B (en) * | 2017-10-27 | 2020-04-15 | Dyson Technology Ltd | Cyclonic separator |
| BR112021005160A2 (en) | 2018-09-19 | 2021-06-15 | Haven Technology Solutions Llc | fluid separation apparatus and method for removing lighter density fluid from a liquid; and, liquid processing apparatus |
| DE102019121373B4 (en) * | 2019-08-07 | 2022-03-10 | Netzsch Trockenmahltechnik Gmbh | SEPARATORS WITH PARTIAL FILTRATION |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH484686A (en) * | 1967-06-16 | 1970-01-31 | Escher Wyss Ag | Cyclone for cutting off gases from liquid-gas mixtures |
| FI54436C (en) * | 1976-05-14 | 1978-12-11 | Enso Gutzeit Oy | HYDROCYCLON |
| AT364303B (en) * | 1980-04-10 | 1981-10-12 | Voest Alpine Ag | HEAT EXCHANGER UNIT FOR PREHEATING CEMENT FLOUR |
| US4692311A (en) * | 1982-12-23 | 1987-09-08 | Shell Oil Company | Apparatus for the separation of fluid cracking catalyst particles from gaseous hydrocarbons |
| DE4009004A1 (en) | 1990-03-21 | 1991-09-26 | Didier Werke Ag | SUBMERSIBLE TUBE AND METHOD FOR THE PRODUCTION THEREOF |
| AT395385B (en) * | 1990-12-13 | 1992-12-10 | Voest Alpine Krems | SUBMERSIBLE TUBE FOR DEVICES FOR SEPARATING AMOUNTS |
| PT102166B (en) | 1998-06-08 | 2000-03-31 | Romualdo Luis Ribera Salcedo | HIGH EFFICIENCY CYCLES |
| DE10038282C2 (en) * | 2000-08-04 | 2003-04-17 | Voith Paper Patent Gmbh | Hydrocyclone and its use |
| WO2011002373A1 (en) * | 2009-07-03 | 2011-01-06 | Glv Finance Hungary Kft., Luxembourg Branch | Hydrocyclone, system and method for cleaning cellulose suspensions |
| DE102013207724A1 (en) | 2013-04-26 | 2014-10-30 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Combustion plant with improved ventilation and cyclonic combustion chamber |
-
2016
- 2016-05-04 DE DE202016102385.8U patent/DE202016102385U1/en active Active
-
2017
- 2017-05-04 RU RU2018138983U patent/RU191344U1/en active
- 2017-05-04 AU AU2017101842A patent/AU2017101842A4/en active Active
- 2017-05-04 AU AU2017260663A patent/AU2017260663A1/en active Pending
- 2017-05-04 WO PCT/EP2017/060624 patent/WO2017191242A1/en active Application Filing
- 2017-05-04 UA UAU201810967U patent/UA138563U/en unknown
- 2017-05-04 BR BR212018072086-6U patent/BR212018072086U2/en not_active Application Discontinuation
- 2017-05-04 CN CN201790000817.6U patent/CN209663527U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113198624A (en) * | 2021-05-08 | 2021-08-03 | 华东理工大学 | Method and device for strong mass transfer countercurrent contact of two-phase fluid |
Also Published As
| Publication number | Publication date |
|---|---|
| AU2017260663A1 (en) | 2018-11-22 |
| UA138563U (en) | 2019-12-10 |
| AU2017101842A4 (en) | 2019-05-02 |
| AU2017260663A2 (en) | 2018-12-13 |
| WO2017191242A1 (en) | 2017-11-09 |
| RU191344U1 (en) | 2019-08-01 |
| BR212018072086U2 (en) | 2019-03-06 |
| DE202016102385U1 (en) | 2016-05-24 |
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