CN1748833A - Method for passing air flow through centrifugal separator and centrifugal separator - Google Patents

Abstract

The present invention relates to the method for making the surrounding atmosphere which is need to separate from the particle flowing through the centrifugal separator and the centrifugal separator using the method by aid of separated grills. According to the invention, the flowing wall bent by aid of the convexity is compelled to do an exceeding direction changing and these walls is constituted to the cavity collection zone which confront the zone including the recirculation zone, concretely speaking, is three particular flowing region which are situated on one special-shaped strip. Therefore, to realize the virtual vortex effect in the structure of the unified special-shaped strip, find out new flowing procedure following the method, wherein the separation of the particle existing with dust form must be especially high, scilicet reach one hundred percent actually.

Description

Be used to the method and the whizzer that make air flow through whizzer

The present invention relates to a kind of be used for making whizzer treat with particle for example dust and/or moisture from surrounding air flow through the method for whizzer, be that equipment carries the air that purifies, described equipment for example be ventilation, heating, air regulator and/or be used for to machinery, motor etc. such also at the device of the equipment air feed of vehicle.The invention still further relates to a kind of whizzer of this method of application, its flat construction unit by a three-dimensional constitutes, and this construction unit comprises inlet, through-flow mouth and outlet and the integrated through-flow and resolution element that separates grid form, is used for air flowing.

Such whizzer is known with simple structure and effect by DD214297.

According to according to the SGW Werder Co., Ltd further feature of the inside prior art of exploitation of the disclosed description of product formerly, such whizzer is known as follows:

The construction unit of the three-dimensional of-one formation whizzer starts in described equipment or the vehicle so that install or pack into as prefabricated installing component;

-in the internal structure by air inflow of the inside of this whizzer in order to guide air to be provided with, each vertical pipeline by the different section bar of cross section constitutes, it is made of the separation level that is used for particle to be separated in being provided with of its mutual zone, wherein each section bar is arranged the width as same grid that occupies a whizzer side by side, and the different cross section of section bar is provided with the mutual piecewise of the cross section that is used for the through-flow sky of air about separating level in a degree of depth of whizzer; And

The cross section of-each section bar has molding structure concave and/or convexity on the surface that is flowed into by air.

Each section bar is along the height of structure and installation unit generally, extended observation towards flow direction, constitute empty, at first diminishing cross section, so that quicken the air enter and the cross section that changes gradually, so that deflection is flowed and speed is reduced to the cross section of the air that stops guiding in the zone of the separation level that is used for particle to be separated and last sky in order to discharge the air of purification.

The machinery above-mentioned according to this design moulding separates grid, and it has:

-a plurality of becoming a mandarin of extending and separate section bar of being parallel to each other, wherein the section bar of two adjacency constitutes a flow gap that is used for air flowing respectively;

-the first section bar plane, its conglobate basically section bar that becomes a mandarin by sealing constitutes, and connects the section bar plane that two other streamwises are positioned at its back, and it is by constituting to the unlimited over there conglobate basically separation section bar of flow direction;

-each separates the back that section bar is positioned at a mobile gap on the section bar plane that is positioned at its front.

DE 100 42 443 A1 are from the prior art and notice such problem, that is, because little rigidity produces vibration, the less service life that it causes little separating degree and after this separates grid in long special-shaped bar.Derive its task thus, that is, make it not produce such vibration problem above-mentioned separation grid formation.Reasonably press the scheme proposals of DE 100 42 443 A1, the section bar that separates that become a mandarin section bar and streamwise is positioned at the 3rd section bar plane of its back connects bridge with one and interconnects.

This scheme be it seems at first function, although it no longer is new-type.What but should not ignore is wherein at first keep the second section bar plane constant, thereby it not to be taked such measure and does not eliminate in this section bar plane pipeline at least or reduction vibration best.

Except that this problem, can completely specifiedly be, according to the whizzer of described prior art because the separation that centrifugal force is used for particle has effectively had improved greatly characteristic.But it is not also optimized about the parameter with on the function on the technical pattern fully, for example

-favourable manufacturing;

The structure of the mechanically stable of-special-shaped bar and noncritical vibration characteristics;

-little constructional depth;

-high separating degree;

-minimum the pressure loss;

-big as far as possible centrifugal force and Gravity Separation;

-comprise little intrinsic noise; And

-bigger inflow velocity scope.

Quote as above, about determining by the scheme of DE 100 42 443 A1, Krapf and LEX Nachf. traffic technique Co., Ltd and limited partnership before this, ventilation and filtering technique about vehicle, by the company's description of product before 30 days Augusts in 2000 open so-called " a plurality of nozzle air grid ", by it as can be known, the section bar that separates that section bar and streamwise be positioned at the 3rd section bar plane of back that becomes a mandarin connects bar with one and interconnects.

In rolling stock was made, relevant professional domain had been devoted to separate at the machinery of the cooling air suction that is used for motor vehicles function, setting, structural design and the flow region in transverse section of section material of grid especially.Described and disclose this problem thus and be included in complexity among " Glaser yearbook " (ZEV+DET Glas.Ann.118 (1991) No.11/12) about following aspect:

The action principle of-current so-called centrifugal force precipitate and separate device;

The effort of the computer aided optimum of the grille-like of-separator;

-for performance parameter, the pressure loss and the sound pressure level of measuring dust and fluid separation applications and the experiment of audio spectrum; And

-performance test, practical application and other prospect.

Can determine that now what reached improves result who not only relies on experience under the result who utilizes economic flow optimized but also the mensuration that relies on relevant parameters.But also there is further improved possibility.

Scheme for the requirement of considering to accord with raising in more detail, except that here desk evaluation, for the form of implementation of the whizzer of up to the present describing, can further develop under the situation of decisive parameter about element and section bar as separating the structure of grid considering to improve.

Set out thus in the research here, that is, utilize strong acceleration effect and the interception before a mobile dead band to turn to, the particle that exists in air flows is produced strong centrifugal force.In view of this, the above-mentioned known whizzer with the setting of described separation grid is can be improved.Like this, for reaching the little progress of this whizzer, still must stand complicated form of implementation about many different special-shaped bars.The advantage of thin portion is being got in touch the deterioration to relevant parameters on the tolerance of shortcoming and reservation and the function all the time.

In such analysis and research, find, in " Aerosol Science andTechnology ", I.R.Torczynski and D.J.Rader two people in the 26:6 of in June, 1997 version and people such as Chih-Chieh Chen, Sheng-Hsin Huang, Wen-Yinn Lin, Tung-Sheng Shin and Fu-Tien Jeng in the 31:6 of in December, 1999 version, the simple model that may constitute away from this professional domain that is used for aerosol has also been described the cyclone effect (simplification) that comprises laminar flow and turbulent situation.

Definite by experiment in the evaluation of this publication, the centrifugation of known so far same a kind of whizzer is mainly concerned with the acceleration (deceleration) in interception section bar or the above-mentioned separation section bar.

Thus, the objective of the invention is, in this whizzer, according to the through-flow vertical or horizontal acceleration of method forced air, make particle going along with such as dust and/or water in its different state of aggregation because its higher density and inertia no longer can be followed air.In this case-be different from so far-also will by transverse acceleration (centrifugal acceleration) and by minimum deflection radius, very big steering angle and when turning to high flow velocity strengthen centrifugation so that

-realize the in fact higher inflow velocity scope of generation, but stand the little pressure loss;

-further improve little water droplet and the separating degree of particle from surrounding air;

-avoid the hydrodynamic noise that causes by the section bar that becomes a mandarin and critical vibration; And

-wherein also realize the super flow velocity of whizzer by the travel speed that for example reaches about 350km/h, and influence does not separate.

For this purpose, with structurally design like this of whizzer, that is, can be not only separate in the unified special-shaped bar of grid but also separate in the different special-shaped bar of grid structure each become a mandarin section bar and they one one

-can flow into from front and side towards going into flow path direction;

-also utilize preposition thin plate to operate reliably with a plurality of holes or sieve aperture;

-with respect to vertical line+/-45 ° installation site can operate reliably; And

Even-bigger setting height(from bottom) can not have vibration problem yet, and as basic separating mechanism on function/structure in conjunction with one " virtual cyclone separator (virtuellenZyklon) ".

As a kind of scheme of the present invention, for separation grid with unified special-shaped bar, above-mentioned purpose according to be used for whizzer through-flow, comprise that the method by the method step of claim 1 to 22 reaches.

Mainly stipulate according to this: mobile wall by means of convex bending is compelled to carry out the direction variation of an extreme and these walls formations is faced the cavate capture zone that comprises the repetitive cycling district, specifically, is three distinctive flow regions that are positioned at a special-shaped bar.Whereby, structurally realize virtual whirlwind effect for unified special-shaped bar, find out the new flow process according to method, wherein the separation of the particle of dust form must be extra high, that is in fact reaches 100%.

Should emphasize that wherein principle of the present invention satisfies each actual condition aspect following, promptly

-method step and the method condition of utilizing claim 1 to determine separately, and

But-the measure that utilizes claim 2 to 22 of the present invention not only can single formation but also is utilized on its fullest ground generally.

In order to use this method, construct whizzer of the present invention according to the feature of claim 23 to 35.

Here also should emphasize, the section bar of the separation grid that the present invention determines can be realized by the architectural feature of claim 23, that is even do not constitute second and three-chamber capture zone S3, S6 yet, but utilize the design that is similar to Fig. 1 and 2 according to following claim, particularly claim 24 to 30 makes it perfect.

On this function of the special-shaped bar of unification of newly-designed whizzer and structure on and at first technical favourable possibility, flow by larger slot formula capture zone with the repetitive cycling by effect contact combination and can obtain a kind of especially in the unexpectedly high separative efficiency of solids, it did not also reach so far.

In addition, the big volume flow of liquid also can advantageously be separated and get rid of to the structural possibility of large scale capture zone, therefore obtains the advantage of constructing on the structure aspect application person, because can guarantee that higher through flow velocity is as core speed.

Purpose for proposing provides a kind of improved products greatly by means of unified special-shaped bar, and it is perfect and further developed the relevant pattern of the centrifugal force-virtual-cyclone separator that is used for a reality.

These advantages and improve and aspect the user, can help to improve serviceability, and needn't stand the pressure loss additional in through-flow and/or harmful vibration.

Also have technical advantages at last, that is, separating grid can also only be made of an independent extrudate, and this is conclusive and embodies special feature of the present invention for reducing cost and cost.

As second theme arranged side by side with first solution of the present invention, above-mentioned purpose is for the separation grid with different special-shaped bars, realizes according to the method by the method step of claim 36 to 51 that comprises that is used for whizzer.Provide the whizzer of this method of enforcement by feature according to claim 52 to 62.

For this scheme, the same following regulation of technical purpose, flowing is compelled to carry out the direction variation of an extreme by means of the wall of convex bending, and these walls are constituted each cavate capture zone that comprises the repetitive cycling district.This is made of three distinctive separated regions, and specifically, first and second separated regions are made of the second special-shaped bar and the 3rd separated region is made of the first special-shaped bar.Whereby, structurally realize virtual whirlwind effect for different special-shaped bars, can utilize the new flow process according to method, it is used for the separation of liquid particle is had the occasion of high request, because it reaches in fact 100% surprising separating degree, this was confirmed in experiment already.

Embodiment by two correspondence two invention schemes describes the present invention in more detail.In the accompanying drawings, Fig. 1 to 5 illustrates and comprises a mobility status and a whizzer that separates grid that is made of unified special-shaped bar, Fig. 6 illustrates the whizzer that comprises a separation grid that is made of two different special-shaped bars, and Fig. 7 illustrates the schematic diagram of the whizzer of two invention schemes.Wherein:

The perspective view of the special-shaped bar of the present invention that Fig. 1 extends at the height of its length upper edge whizzer constitutes the separation grid by it, and described whizzer comprises a separation grid that is made of unified special-shaped bar;

First scheme of Fig. 2 whizzer is by the signal partial graph by the cross section of each special-shaped bar that become a mandarin of Fig. 1, and comprises that the basic section bar of the present invention constitutes and flow region in the configuration of the principle of these special-shaped bars;

Fig. 3 press Fig. 1 that constitute with process each the special-shaped bar that is provided with similarly through-flow in according to the motion pattern of experiment;

Fig. 4 a) and b) in the process of pressing Fig. 3 is similarly through-flow according to the solids trajectory diagram of experiment;

Fig. 5 a) and b) in the process of pressing Fig. 3 is similarly through-flow according to the liquid particle trajectory diagram of experiment;

The signal partial graph in the cross section of the separation grid that the alternative plan of Fig. 6 whizzer constitutes by two different special-shaped bars, this separations grid comprises section bar formation and the separated region that the present invention is basic; And

The whizzer that Fig. 7 one schematically illustrates there is shown its front view, sectional view and vertical view.

Schematically illustrate a this principle structure with whizzer of a plurality of vertically extending special-shaped bars 1 by Fig. 7, it is held in the framework 2 and can connects as jockey 2.2 by means of for example tapping screw in this case and is fixed in the corresponding section bar structure 2.2.With the height of H mark whizzer, with its width of B mark and with the length of l mark abnormity bar 1.One degree of depth T is roughly taken by the width b (Fig. 1) of special-shaped bar.

A plurality of special-shaped bars 1 constitute described separation grid 3, and it flows into air by side Le along the direction of arrow, and wherein air is being cleaned later on by separating grid, and flows out at side La with along the direction of arrow, then it is defeated by the target that need supply gas.

Whizzer has a discharging area 6.In this zone, assemble solid and particle liquid that separates in the length of the special-shaped bar 1 in the textural edge of section bar with downward (arrow) shear flow owing to gravity with tackle, and do not remove via being shown in further detail there with unlabelled lines of orifices.

By such positive action, be in order to the section bar of mask work structure and from this zone, continue to get rid of among the particle that separates, and can freely be used for continuous separation again from leaked-in air.

As shown in fig. 1 and conspicuous by Fig. 2 to 5 equally, each special-shaped bar 1 can be made by an independent extrudate.Wherein the important section bar zone of its present invention or the structure of section bar also can be made of each special-shaped bar capable of being combined or can be arranged spaced apart, as it as shown in Fig. 6.

The air La that equally represents leaked-in air Le and outflow with arrow among Fig. 2 with and flow direction.

At first, as first scheme, the process of describing method of the present invention and the mode of action and to be incorporated into a whizzer in the grid 3 of separating with unified special-shaped bar on its function with on the structure.

Schematically illustrate the drawing in side sectional elevation of the separation grid 3 that constitutes by unified special-shaped bar 1.1 among Fig. 2.Marked region S0 to S9 represents flow region, below relates to them.Mark P0 to P5 sign is separated the relevant portion to functional description of section bar.The characteristics of separate particles describe in more detail by result and mensuration by experiment confirm in the section bar.

Each through-flow station of separation grid by special-shaped bar 1.1 is described with functional steps from air inflow side Le to air outflow side La.

Determine as follows with reference to Fig. 2 to main points of the present invention:

-from S0 in the inflow region of S1, make by flowing into the mobile about 4 extraordinarily fast of forming part P0, this in Fig. 3 with shown in the streamline symbol describe;

-from S1 in first flow region of S4, make almost 45 ° of main flow deflections;

-be used for first and second cavate capture zone S2 and the S3 of particle, flowing is blocked and average speed is nearly reduced to zero;

-main flow is defeated by from S4 to second flow region of S8 and turned to about 90 ° consumingly along a moulding tongue piece P2 then.The in fact virtual cyclone separator that the common formation of this zone and the capture zone under it is made every effort to according to purpose;

-from S5 to the three-chamber capture zone of S6, flowing is blocked once more, wherein forms the recirculation zone (see figure 3) of slow rotation at position S5, it is by driving from the main flow of S4 to second flow region of S8;

-in this three-chamber capture zone S6, constitute dead (water) district (Fig. 4) of a secondary circulation, and flowing velocity drops to almost nil value in four barrel capture zone S7;

-the diffuser that constitutes by the first and second molded surface P5.1 and P5.2 once more partly expansion flow and, from separation grid of the present invention, discharge again at S9 hollow air-flow as recovering from the pressure of S8 to the 3rd flow region of S9.

From Le to La through-flow, the minimum total losses of gross pressure is allocated as follows by the present invention:

-in fact do not losing from the acceleration of S0 to the inflow region of S1;

-the pressure loss only occurs in separation level S1-S4-S8 through-flow of corresponding first and second flow regions, and this is not a shortcoming with respect to prior art at least;

-between the S8 of the 3rd flow region and S9, recover a part of power pressure, wherein on the whole by the profile that can freely separate optimal design abnormity bar 1.1 and make the mobile pressure loss reduce to minimum whereby by diffuser.

100% solids separation nearly reaches like this according to form of implementation of the present invention, promptly, force mobile (as by Fig. 4 a) and 4b) obviously easily see) in alignment with longitudinally or horizontal acceleration, make since the higher density of particle going along with (thereby and bigger inertia) it can not follow mobile.Wherein illustrate with the flow graph explanation.

-Fig. 4 a) be under the condition of parameter d dust≤10 μ m and speed U=5m/s the solids track and

-Fig. 4 b) is solids track under the condition of parameter d dust 〉=30 μ m and U=5m/s.

According to purpose, high flow velocity is strengthened the centrifugation of transverse acceleration (centrifugal acceleration) by little deflection radius, big steering angle and when turning to.Compare with the previous prior art of describing, for example according to DE 100 42 443 A1, its centrifugation is mainly concerned with the vertical acceleration (deceleration) of interception in the section bar, according to the major part of the effect of method of the present invention and whizzer from transverse acceleration.

The separating mechanism of solids at length is constructed as follows:

-be accelerated jointly and improving its momentum with flowing from S0 particle in the inflow region of S1;

-because to flow into the surface (as the bearing-surface profile of front) of forming part P0 be crooked, by its centrifugal acceleration that causes with particle going along with in the edge region with its transverse to the tendency leads of main flow direction to the centre that flows into cross section S1;

-particle, it can not be followed flow direction and carry out about 45 ° variation between the S1 of first flow region and S4, be dumped among the first cavate capture zone S2, in this region S 2 based on very low flow velocity;

-in the first cavate capture zone S2, the momentum of particle is owing to the collision on wall and reflection are lowered (Fig. 4 a) and 4b)), and the second cavate capture zone S3 improves the number of wall collision and captures some particles (Fig. 4 a) and 4b));

-by being changed by the minor radius of moulding tongue piece P2 guiding and high almost 90 ° the strong direction of speed current downflow between the second flow region S4 and S8, particle is thrown toward S5 and gets rid of among the three-chamber capture zone S6.In addition, particle trajectory is guided on the fixing border that is flowing among the passage area S4 into.Particle is by recirculation zone S5, partly losing its momentum (Fig. 4 a) and 4b) under the assistance of the reflection on the forming surface P4 and by the collision of the wall in three-chamber capture zone S6).

-secondary repetitive cycling in three-chamber capture zone S6 flows and to help at first to keep there the particle that is captured for the particle diameter of appointment and particle density (Fig. 4 a);

-the four barrel capture zone S7 supports the centrifugation of particle, it enters in this chamber (Fig. 4 a) and 4b) by wall reflection), wherein has only small particle, it is enough little of light, so that can follow transverse acceleration, or it is not separated and discharge because wall reflection is thrown away from capture zone in S9 from separate grid.

Therefore will make as follows according to splendid separation function of the present invention zone:

-the curved surface that flows into forming part P0 and moulding tongue piece P2 produces the centrifugal acceleration in through-flow, and it causes the throwing away of particle going along with of the density more higher than liquid component;

-first, second, third and four barrel capture zone S2 and S3 and S6 and S7 be used as interception and separated region the most efficiently.

According to the separation of droplet of the present invention from flow advantageously basically with suitable to the description that solids carried out.Difference between the behavior of little water droplet and the behavior of solids only is that its particle encounter just occurs on a profile wall.Though reflect from wall after the collision of solids in one elasticity/plasticity, a little water droplet forms a skin covering of the surface after wall collision, and it flows out under the influence of wall shearing stress and gravity.But when bouncing, a water droplet also may form satellite droplet.The diameter of this satellite droplet may be so little in this case, so that it can follow the outlet of flowing up to separating grid, but its quantity is less.

Below enumerate according to Fig. 5 a) and 5b) process, the separating mechanism of its small water droplets is different from the separating mechanism of solids, on function, also be applicable to the second invention scheme that to describe below other especially for this effect that reaches actual 100% fluid separation applications here, that is according to Fig. 6, having the separation grid 3 that is made of two different special-shaped bars 1.2,1.3 can realize.

Below illustrate with flow graph:

-Fig. 5 a) be parameter d water 〉=10 μ m and and the condition of U=5m/s under the liquid particle track and

-Fig. 5 b) is liquid particle track under the condition of parameter d water≤10 μ m and U=5m/s;

-at first, particularly big water droplet has been run into the section bar surface and has been flowed out (Fig. 5 b) as skin covering of the surface in the zone that flows into forming part P0);

-on the first and second separation edge P3.1 and P3.2 this film break away from surface and liquid be discharged into first and three-chamber capture zone S2 and S6 in;

-whole little water droplet, it collides on the section bar surface in the first cavate capture zone S2, as liquid film because gravity flows out and therefore separated;

-particle, it is dumped among the three-chamber capture zone S6 along recirculation zone S5 by passage area S4, bumps against on the inwall of catch tank of such formation and separated there;

-first, second, third and four barrel capture zone S2 and S3 and S6 and S7 not only be used as the capture chamber of flight water droplet but also be used as the eliminating of surface liquid film;

-removing little water droplet, it is enough little or light, consequently follows and flows beyond outlet, also has only amount of liquid not separated (Fig. 5 is a)) seldom, it falls to diffuser P5.1, in the zone of P5.2.

As for the difference between the characteristics that relate to characteristics on through-flow, separating mechanism and the structure two invention schemes, of the present invention, should emphasize:

Realize by " virtual cyclone separator " by making every effort to according to purpose for-one basic separating mechanism.Therefore emphasize relevant therewith flow region, wherein force to flow by means of the wall of convex bending basically and carry out strong direction and change.Capture the chamber in the face of this wall is provided with, in this captures chamber, constitute the repetitive cycling zone, form and flow tranquil space and guarantee the effective separation of particle;

-to pass through at region S 2 and S3 and S5, S6 and S7 (Fig. 2 and 3), big catch tank among similar 5.1,5.2,5.3 (Fig. 6) and repetitive cycling thereof flow, and separative efficiency also is high for solids:

If must separate big liquid capacity flow, then the capture chamber determined of large scale also is favourable, and this guarantees higher through flow velocity as core speed on function, and provides on the structure and the advantage on making for the user;

Wherein, do not strengthen the through-flow pressure loss with respect to prior art.

Therefore pass through the method for the present invention and the structure of whizzer, in two kinds of schemes, for relevant application person or operator, in the finished product of favourable technology manufacturing, improve the efficient and the serviceability of centrifugal separator of the present invention greatly as centrifugal force-virtual-cyclone separator.

In this respect, technically in the first invention scheme particularly advantageously be, only 3 extrudates 1.1 being determined by unique a kind of number are formed, thereby this can reduce manufacturing expense and also reduces cost.Still should emphasize that the separation grid 3 with unified special-shaped bar 1.1 can be applicable to whole particles, the important optimal separation of preferred solids.

If but in the scope that requires, also to separate in fact 100% the liquid particle or the liquable particle of any state of aggregation, the second method scheme described below would then be adopted and according to the form of implementation of Fig. 6.

Prerequisite to this is that mobility status in each flow region that describes in detail among the embodiment in front and mobilization here also are like this.But because geometry different configuration or the distribution of each capture zone that is used for particle to be separated on two different special-shaped bars, here also will be by its mark and structural design each specific separated region of invention programme definition with respect to the front, and the flow region of lay special stress on same purpose no longer.

Through-flow method according to the whizzer of the second invention scheme, wherein have with different special-shaped bars 1.2,1.3 the grating type section bar that is provided with by the air inflow, make leaked-in air by means of the first special-shaped bar 1.2 become the forming part 1.2.1 that becomes a mandarin of convex bending at first to quicken to enter the cross section 4.1 of the diminishing sky of a nozzle-type to flow direction, wherein different special-shaped bars 1.2,1.3 is configured for particle to be separated equally mutually in it is provided with capture also is configured for the cross section that gradually changes 4 that air can flow through simultaneously with separated regions.

After this on the one hand air flows to the first section bar part 1.3.1 that the streamwise into the second special-shaped bar 1.3 opens wide, therein separating solid particles to a considerable extent in having first separated region 5.1 of the first resolution element 5.1.1.

Make the deflection of air stream on the other hand and continue to turn to and enter among the second section bar part 1.3.4 that the vane type of the second special-shaped bar 1.3 opens wide.Special here also unprecipitated moist particle is almost completely separated in having second separated region 5.2 of the second resolution element 5.2.1, because form dead (water) district (being similar to the description to the first invention scheme of Fig. 4) of a secondary circulation there by the special geometrical construction of second separated region 5.2, it guarantees actual 100% fluid separation applications prerequisite.

At last, make air stream turn to the 3rd section bar part 1.2.2 that opens wide of the first special-shaped bar 1.2 on the one hand, its formation has the 3rd separated region 5.3 of the 3rd resolution element 5.3.1, be used for the particularly separation completely of reality liquid or liquable particle, and on the other hand in the cross section 4.2 that enlarges gradually of the air stream of discharging, in second zone that connects between the outer wall of bar 1.3.3 and the 3rd section bar part 1.2.2 that opens wide, guarantee the pressure recovery.

At described separated region 5.1,5.2,5.3 middle flow velocity can drop to zero nearly, make and wherein partly form the tranquil dead band of flowing, thereby the particle that separates is constantly along special-shaped bar 1.2,1.3 length because downward shear flow and the gravity effect addressed in first embodiment are gathered in the discharging area 2.1, and can be excluded by the there.

According to method, (being similar to the first invention scheme) flowed to be intercepted at and is positioned at separated region 5.1,5.2, in the recirculation zone in 5.3 the zone and make its rotation lentamente therein.Flow therein and can carry out off-load by main flow driving and the diffusion effect that constitutes by means of the wall between the section bar surface of the first special-shaped bar 1.2 and the second special-shaped bar 1.3 then.In fact after this air do not have particle and flow to application places.

In this respect,, can tackle mobilely in the capture zone that 1.3.4 constitutes, wherein in these capture zones, can form (extremely) zone of the conclusive secondary circulation of function at the section bar part 1.3.1 that opens wide by at least one.

Generally, in fact air will be the no pressure loss from entering (Le) up to discharging the through-flow of (La) whizzer.

The pressure loss of main portions is limited to the wall of first cross section 4.1 that opens wide of the second special-shaped bar 1.3 and first flow region that connects between the bar 1.2.4 of the first special-shaped bar 1.2.

This method keeps recovering the power pressure of a part by means of diffusion effect.

In this invention scheme, the method uniqueness also be, the curved surface and/or the second special-shaped bar 1.3 by means of the inflow section bar 1.2.1 of the first special-shaped bar 1.2 produce such centrifugal acceleration in through-flow, it causes throwing away the particle that density going along with in the air is higher than liquid particle, as solids, wherein the solids of indication are reflected from profile wall after the collision of elasticity/plasticity.

Equally, the solids that comprise in flowing into air quicken to enter each inflow region with flowing and obtain a momentum simultaneously to improve.

The characteristics of the inventive method are, flow into the solids that comprise in the air because crooked inflow surface is subjected to a centrifugal acceleration, wherein especially at the fringe region that flows particle going along with about transverse to the trend of main flow direction intermediary movements to a corresponding inflow cross section.

In order to realize 100% fluid separation applications, conclusively be, the liquid component of particle such as water droplet/little water droplet with the wall collision of section bar after form a skin covering of the surface, it flows out under the influence of wall shearing stress and gravity.

Wherein at first bigger liquid particle drops in the section bar that becomes a mandarin and for example flows into and collided its surface in the zone of forming part 1.2.1 and flow out as skin covering of the surface.

In this method scheme, the skin covering of the surface of liquid particle is at the first and/or second separation edge 1.3.2 of the second special-shaped bar 1.3, and 1.3.5 is last separated and be discharged from as liquid.

Water droplet/little water droplet, it runs into the surface of special-shaped bar 1.2,1.3 in capture zone, also separated thus owing to gravity flows out as liquid film.

The liquid particle that is thrown out of is run into the inwall of the second section bar part 1.3.4 that the vane type of the second special-shaped bar 1.3 that constitutes catch tank opens wide equally, and finally separated there, also interception flight water droplet simultaneously, and it flows out as the surface liquid film.

The combination of these method steps guarantees to get rid of fully liquid component, wherein, generally at the textural and same particle to be separated in these flow regions of different section bars because shear stress and/or gravity effect are moved to the discharging area 2.1 of whizzer also is excluded there.

Have special-shaped bar 1.2, the 1.3 method schemes that constitute separation grid 3 for using this, the cross section 4 of the sky that flows through by air of the whizzer that will design and the first special-shaped bar 1.2 that constitutes for the separating particles continuous dislocation and the separated region 5.1 of the second special-shaped bar 1.3 according to this, 5.2,5.3 constitute, section bar part 1.3.1,1.3.4,1.2.2 that these special-shaped bars utilize its streamwise to open wide comprise the resolution element 5.1.1 with corresponding formation, 5.2.1,5.3.1 first, second and the 3rd separated region 5.1,5.2,5.3.

The first special-shaped bar 1.2, it at first has comprising of streamwise convex bending of about 45 ° of forming part 1.2.1 that become a mandarin to the upper surface of intrinsic deflection, it connects first and meets bar 1.2.4 and last the 3rd section bar part 1.2.2 that opens wide with the 3rd resolution element 5.3.1 that connects, these resolution elements 5.3.1 by rounding open wide forward and connect a pair of blade that bar 1.2.4 separates by first and constitute with flange of indentation on the 3rd separation edge 1.2.3, and constitute two cavate catch tanks that separate like this, the second special-shaped bar 1.3 of setting in parallel, it at first has the first section bar part 1.3.1 that opens wide that (towards flow direction) flows into, its blade with flange of indentation on the first separation edge 1.3.2 by each rounding constitutes, and surrounds the cavate catch tank thus.Connect a pair of cavate catch tank that separates again, its formation has the second section bar part 1.3.4 that opens wide of the second separation edge 1.3.5, and each second separation edge 1.3.5 makes the second section bar part 1.3.4 change second over to and meets bar 1.3.3.

Therefore separate grid 3 important cross-sectional configurations function aspects with it as follows for whizzer:

A) cross section of one first special-shaped bar 1.2, it at first has the forming part of becoming a mandarin 1.2.1 along the air feed direction, has first the 3rd section bar part 1.2.2 that meets bar 1.2.4 and open wide then;

B) cross section of one second special-shaped bar 1.3, it has the first unlimited section bar part 1.3.1 along the air feed direction as the section bar that becomes a mandarin, and has the second unlimited section bar part 1.3.4 then; And

C) setting that replaces mutually of special-shaped bar 1.2,1.3, it constitutes the cross section 4 of the sky that can flow through along the degree of depth T of whizzer, its along the air feed direction

Have on the one hand the cross section 41 that is the diminishing sky of nozzle-type, so that quicken the speed of leaked-in air, it connects the cross section 4.2 of the sky that strengthens gradually, so that reduce air velocity stopping and reduce the pressure loss up to its part;

And have first separated region 5.1, second separated region 5.2 and the 3rd separated region 5.3 that is used for particle on the other hand, they have resolution element 5.1.1 respectively, 5.2.1 and 5.3.1, this resolution element is respectively formed at the cross section 4 of the sky between the special-shaped bar 1.2,1.3.

Advantageously, whizzer is designed to for special-shaped bar 1.2, meet bar 1.3.3 1.3 have first 1.2.5 and second that meets bar 1.2.4 and connect the bar formula, not only in order to stable air stream but also be used for special-shaped bar 1.2,1.3 being fixed in the framework 2 by means of Connection Element 2.2.

Its section bar part 1.3.1 affiliated or that connected cavate opens wide at least one separated region 5.1,5.2,5.3 and at least one function, 1.3.4,1.2.2 common constitute " virtual cyclone separator ", in order to separating particles, and as described in the first invention scheme.Therefore, in general, whizzer has the partial function feature of a centrifugal force-virtual-cyclone separator in separating grid 3.

The make of whizzer designs like this, promptly

A) framework 2 is contained in the first and second special-shaped bars 1.2,1.3 wherein vertical and that be parallel to each other and extend.

B) special-shaped bar 1.2,1.3 length (l) in the height (H) of whizzer, extend as separating grid, abnormity bar 1.2,1.3 roughly takes the degree of depth (T) of whizzer, and a plurality of special-shaped bars 1.2, the 1.3 vertical and extension that is parallel to each other are arranged in the width B of whizzer 1, and the width B 1 of form separating grid 3 thus, and

C) be provided for getting rid of the discharging area 2.1 of the particle of separation.

Whizzer can suitably cover with unshowned multihole lamina or sieve formula body on the surface that is flowed into air and/or the surface of the air that flowed out.

In addition, might in the sealed hollow that flows into section bar such as 1.2.1, heating element heater be set, so that for example run into the ice/snow load of the extreme that flows into air.

Whizzer can depart from its installation site vertical line up to+/-45 °, and have such external styling, its profile is determined all can be matched with the relevant moulding of equipment, machinery, vehicle etc. with size, and does not reduce according to function of the present invention.

At preferential application places (optimal separation/alternative plan of first scheme=all particles=liquid particle 100% separation), and on the function with use in combination and implement each relevant claim to a method and whole feature of requiring of the respective right of whizzer corresponding to each scheme on the structure, the present invention is used for the actual maximum use of schemes performance at two kinds thus.

Therefore, can realize a kind of through-flow and method whizzer of being used for, according to this based on following primary condition:

A) speed of inflow air is favourable in the scope of 6-8m/s in the scope of 0.5-1, so that it can be accelerated to 4 times;

B) liquid particle can separate to reach 100% separating degree it when the drop size is 20 μ m from air;

C) solids are that 60 μ m and density are 2.66kg/m in granular size ³The time it can be separated from air with 100% separating degree almost and/or

D) at diffuser P5.1, the back of the suitable cross section of P5.2 or alternative plan, the outflow air of off-load has the insignificant pressure loss on less and the function.

For the application of the present invention in rolling stock, make whizzer can realize reaching the super flow velocity of 350km/h and do not stand so far shortcoming functional lesion for example.Even serious so far and disadvantageous work noise, thereby in according to form of implementation of the present invention, also be lowered unimportant in practice to a great extent.

The assembling of each required extrudate and fixing can the connection by removable or non-disconnectable formula simply thereof realize.

List of numerals

Le flows into a side and the direction of air

La flows out a side and the direction of air

The S0-S1 inflow region

S1 flows into cross section

S1-S4 first flow region

The S2 first cavate capture zone

The S3 second cavate capture zone

The S4 passage area

S4-S8 second flow region

The S5 recirculation zone

S6 three-chamber capture zone comprises (extremely) zone of secondary cycles

S7 four barrel capture zone

S8-S9 the 3rd flow region

P0 flows into forming part

P2 moulding tongue piece

P3.1 flows into first separation edge on forming part surface

P3.2 flows into second separation edge on forming part surface

P4 section bar surface

The P5.1 first section bar surface

The P5.2 second section bar surface

The P5.3 connecting wall

1 special-shaped bar

1.1 unified special-shaped bar

1.2 the first special-shaped bar

The forming part 1.2.1 become a mandarin

1.2.2 the 3rd section bar part of opening wide

1.2.3 the 3rd separation edge

1.2.4 first connects bar

1.2.5 connect bar formula protuberance

1.3 the second special-shaped bar

1.3.1 the first section bar part of opening wide

1.3.2 first separation edge

1.3.3 second connects bar

1.3.4 the second section bar part of opening wide

1.3.5 second separation edge

2 frameworks

2.1 discharging area

2.2 jockey

3 separate grid

Air feed shown in the cross section of 4 skies comprises

4.1 be the diminishing cross section of nozzle-type

4.2 the cross section of Kuo Daing gradually

5.1 first separated region

5.1.1 first resolution element

5.2 second separated region

5.2.1 second resolution element

5.3 the 3rd separated region

5.3.1 the 3rd resolution element

The length of l abnormity bar

The width of b abnormity bar

The height of H whizzer

The width of B whizzer

B1 separates the width of grid

The degree of depth of T whizzer

Claims (62)

1. be used for making whizzer treat with particle for example dust and/or moisture from surrounding air flow through the method for whizzer, by means of one is the inflow of air, the structure and the installation unit of the three-dimensional of transmitting and flowing out and constitute, carry the air that purifies for equipment, described equipment for example is to ventilate, heating, air regulator and/or be used for to machinery, the device of air feed such as motor, also has the equipment in the vehicle, machinery etc., the structure of described three-dimensional and installation unit have and become grating type to be provided with therein, special-shaped bar (1.1) section bar that becomes a mandarin by air, each special-shaped bar (1.1) is provided with mutually and is configured for the capture and/or the separated region of particle to be separated, and constitute simultaneously and can flow through air, the cross section (S1-S9) that changes, it is characterized in that

A) flow into the air of inflow region (S0-S1) along the direction of arrow by means of inflow forming part (P0) acceleration from one first side (Le) against the flow direction convex bending, and the main flow that makes air about 45 ° of deflection in first flow region (S1-S4), wherein, flow velocity drops to zero nearly in four barrel capture zone (S7);

B) main flow of air changes second flow region (S4-S8) over to for about 90 ° along moulding tongue piece (P2) then;

C) be flowing in the recirculation zone (S5) and be blocked and make it to rotate lentamente therein, should flow is therein driven by the main flow in second flow region (S4-S8); And

D) flow then by means of by the first and second section bar surfaces (P5.1, P5.2) diffuser of Gou Chenging by off-load, after this flows out along the direction of arrow in one second side (La) in the 3rd flow region (S8-S9);

Thereby the particle of separation is gone up because downward shear flow and gravity effect are gathered in the discharging area (2.1) also is excluded therefrom in the length (l) of special-shaped bar (1.1) continuously.

2. in accordance with the method for claim 1, it is characterized in that (S2 is blocked in S3) and its average speed is dropped to almost zero to be flowing in the first and second cavate capture zones.

3. according to claim 1 or 2 described methods, it is characterized in that, be flowing in three-chamber capture zone (S6) and be blocked, wherein in this three-chamber capture zone (S6), constitute (extremely) zone of secondary repetitive cycling.

4. according to one of claim 1 to 3 described method, it is characterized in that air is actually the no pressure loss in the acceleration of inflow region (S0-S1).

5. according to one of claim 1 to 3 described method, it is characterized in that the main pressure loss is limited to first flow region (S1-S4) and/or second flow region (S4-S8).

6. according to one of claim 1 to 3 described method, it is characterized in that, in the 3rd flow region (S8-S9) by means of (P5.1, P5.2) diffuser of Gou Chenging recovers a part of power pressure by the first and second section bar surfaces.

7. according to one of claim 1 to 6 described method, it is characterized in that, in through-flow, produce such centrifugal force acceleration by means of the curved surface that flows into forming part (P0) and moulding tongue piece (P2), it causes throwing away density going along with in the air particle such as the solids higher than liquid particle, and wherein said solids wall from section bar after the collision of elasticity/plasticity is reflected.

8. according to one of claim 1 to 7 described method, it is characterized in that the solids that contain are accelerated and are able to simultaneously momentum together with flowing and improve in each inflow region (S0-S1) in leaked-in air.

9. according to one of claim 1 to 8 described method, it is characterized in that, the solids that contain in leaked-in air are owing to the bending that flows into forming part (P0) surface that becomes a mandarin obtains a centrifugal acceleration, wherein especially in the fringe region that flows particle going along with just transverse to the trend of main flow direction intermediary movements toward inflow cross section (S1).

10. according to one of claim 1 to 9 described method, it is characterized in that, those can not be followed the about 45 ° solids of air main flow deflection in first flow region (S1-S4) and be got rid of in the first cavate capture zone (S2) under very low relatively flow velocity, this moment is therein by colliding the momentum that for example collision on inwall and reflection have reduced solids, number that the second cavate capture zone (S3) raising is simultaneously collided and the solids that capture other.

11. according to one of claim 1 to 10 described method, it is characterized in that, because having about 90 ° strong direction in second flow region (S4-S8) under less radius changes and high speed, (P2) guides to by the moulding tongue piece, solids are tangential to recirculation zone (S5) and are dumped in the 3rd capture zone (S6), and, be flowing in the track of fixed boundary control (guiding) particle in the passage area (S4), wherein solids are by recirculation zone (S5), and partly given to support by the reflection on section bar surface (P4), thereby solids are lost its momentum owing to wall collides in three-chamber capture zone (S6).

12. according to one of claim 1 to 11 described method, it is characterized in that, in three-chamber capture zone (S6), on the meaning of circulation, play the mobile of secondary action and help to make the particle of certain granules size and density to be retained in the capture zone (S6).

13., it is characterized in that four barrel capture zone (S7) helps to keep because the wall reflection enters particle wherein according to one of claim 1 to 12 described method.

14., it is characterized in that said particle has than higher density of liquid particle and solids normally according to one of claim 8 to 13 described method.

15., it is characterized in that the liquid component of particle such as water droplet/little water droplet forms a skin covering of the surface later in the wall collision with section bar according to one of claim 1 to 6 described method, it flows out under the effect of wall shearing stress and gravity.

16., it is characterized in that at first bigger liquid particle drops in to be run into the surface in the zone that flows into forming part (P0) and flow out as skin covering of the surface according to one of claim 1 to 6 and 15 described method.

17. according to one of claim 1 to 6 and 15 or 16 described method, it is characterized in that, (P3.1 P3.2) goes up separated and is discharged in the first cavate capture zone (S2) and/or the three-chamber capture zone (S6) as liquid the skin covering of the surface of liquid particle in first and second separation edge that flow into forming part (P0).

18. in accordance with the method for claim 17, it is characterized in that those run into the water droplet/little water droplet on section bar surface in the first cavate capture zone (S2), as liquid owing to gravity flow out and thereby separated.

19. according to one of claim 1 to 6 and 15 described method, it is characterized in that those are got rid of to three-chamber capture zone (S5, liquid particle S6) by passage area (S4), the inwall of running into the 3rd capture zone (S6) is also separated there, and described the 3rd capture zone constitutes catch tank.

20., it is characterized in that the flight water droplet is trapped in first, second, third and four barrel capture zone (S2 according to one of claim 1 to 6 and 15 or 16 described method, S3, S6, S7) in, it is excluded as the surface liquid film in these capture zones.

21., it is characterized in that section bar is used like this according to one of claim 1 to 20 described method, promptly, at different section bar structure (P0, P2, P3.1, P3.2, P4, P5, P5.1, P5.2 P3) goes up and makes particle to be separated because shear stress and/or gravity effect also are excluded there to discharging area (2.1) motion of whizzer in described flow region (S0 to S9).

22. according to one of claim 1 to 21 described method, it is characterized in that, have only solids too little and/or too light, that can follow transverse acceleration and/or because the solids that wall reflection is thrown away from capture zone, and have only too little and/or too light as little water droplet, can follow to flow and arrive the liquid particle of outlet, and/or at diffuser (P5.1, P5.2) amount of liquid seldom of sedimentation just in the zone is still the insignificant part of the air of outflow.

23. use according to claim 1 to 22 is described and separate the whizzer of the method for grid (3) by means of one, in order to separating particles from the air that flows through whizzer, for example dust and/or water, described whizzer has a kind of flat structure of three-dimensional and the form of installation unit, be used for equipment as ventilating, heating, air regulator and/or mechanical in order to give, the device of air feed such as motor, the equipment that also is used for vehicle, machinery etc., be included in that in the whizzer vertical and parallel dislocation is provided with, constitute the special-shaped bar (1.1) that separates grid (3), these special-shaped bars are flowed into by air and are through-flow in the cross section of sky, and has the separated region that is used for separating particles, it is characterized in that

A) each special-shaped bar (1.1) (streamwise) of meeting stream at its cross section at first has comprising of a convex bending of about 45 ° of upper faces to intrinsic deflection, this upper face ends at one first separation edge (P3.1), and the section bar surface (P4) of a slight vane type camber arch is extended in the centre of that open wide at such streamwise or the inflow forming part (P0) that the one-tenth convex surface constitutes in the bottom, downward on the one hand and moulding tongue piece (P2) termination of oppositely extending in this section bar surface, and like upwards feeding one the case on the other hand in the forming part, this forming part comprises one first and one second section bar surface (P5.1, P5.2) and therebetween connecting wall (P5.3), wherein, in transverse section of section material, constitute a four barrel capture zone (S7) on the whole, its streamwise opens wide or concave surface ground extends, and constituting one first cavate capture zone (S2), it opens wide against flow direction or concave surface ground extends;

B) have the inflow region with inflow cross section (S1) (S0-S1) that in cross section, reduces at first gradually and the passage area (S4) of and then about 45 ° of deflections for the special-shaped bar of through-flow each that is arranged in parallel of air (1) streamwise, this passage area is along moulding tongue piece (P2) and first separation edge (P3.1) guiding, and turn to diffuser again and derive, described diffuser have gradually enlarge by the first and second section bar surface (P5.1, P5.2) cross section of Xian Dinging, and

C) mating reaction that flow into, the through-flow and air that flows out and these section bars is configured in the whizzer constitutes first flow region (S1-S4), the main flow of Jia Suing is by about 45 ° of deflections therein, main flow is changed over to second flow region (S4-S8) by about 90 ° again along moulding tongue piece (P2) then, and in the 3rd flow region (S8-S9), the main flow that be purified this moment to a large extent is at diffuser (P5.1, P5.2) expansion in, wherein

D) each several part of second flow region (S4-S8) together with at least the four and first cavate capture zone under it or that connect on the function (S7 S2) constitutes " virtual cyclone separator " together, in order to separating particles and

E) whizzer comprises the functional character of a centrifugal force-virtual-cyclone separator on the whole.

24. separate the whizzer of the method for grid (3) by means of one according to the described application of claim 23, it is characterized in that, the surface that special-shaped bar (1.1) has the plane of a bottom to extend, it ends at short second separation edge (P3.2) to intrinsic deflection.

25. separate the whizzer of the method for grid (3) by means of one, it is characterized in that special-shaped bar (1) has one to open wide the moulding tongue piece (P2) of ground, slightly overlapping separation edge (P3.2) according to the described application of claim 23.

26. separate the whizzer of the method for grid by means of one according to the described application of claim 23, it is characterized in that, abnormity bar (1.1) has forming part like the case that opens wide in contrast to flow direction, it comprise the section bar surface (P5.1, P5.2) and connecting wall (P5.3).

27. separate the whizzer of the method for grid (3) by means of one according to the described application of claim 23, it is characterized in that special-shaped bar (1.1) has one second cavate capture zone (S3), its streamwise opens wide or concave surface ground extends.

28. separate the whizzer of the method for grid (3) by means of one according to the described application of claim 23, it is characterized in that special-shaped bar (1.1) has a three-chamber capture zone (S6), it opens wide or the extension of concave surface ground in contrast to flow direction.

29. separate the whizzer of the method for grid (3) according to the described application of claim 23 by means of one, it is characterized in that second section bar surface (P5.2) termination is to projecting inward edge.

30. according to one of claim 23 to 29 described whizzer, it is characterized in that, the moulding bar of the streamwise design of section bar structure comprises an independent extrudate as special-shaped bar (1.1), and it can have in order to set up a structure or a device (2.2) that connects flowing into forming part (P0) inside.

31. according to one of claim 23 to 30 described whizzer, it is characterized in that,

A) framework (2) is provided with special-shaped bar (1.1) vertical therein and that be parallel to each other and extend;

B) length (l) of special-shaped bar (1.1) is extended in the height (H) of whizzer (1), the width (b) of abnormity bar (1.1) roughly takes the degree of depth (T) of whizzer, and a plurality of vertical and special-shaped bars (1.1) of being parallel to each other and extending are set in the width (B) of whizzer (1), and formation is separated grid (3) thus, and

C) be provided with a discharging area (2.1) that is used to get rid of the particle of separation.

32., it is characterized in that each special-shaped bar (1.1) is fixed in the framework (2) by the removable or non-disconnectable formula of device (2.2) according to one of claim 23 to 31 described whizzer.

33. according to one of claim 23 to 32 described whizzer, it is characterized in that, bear surface that flows into air and the surface of bearing the outflow air and cover by unshowned multihole lamina or diagrid.

34., it is characterized in that according to one of claim 23 to 33 described whizzer, take an installation site, its can depart from vertical line up to+/-45 °.

35. according to one of claim 23 to 34 described whizzer, it is characterized in that having a kind of like this external styling, its profile and size all can be matched with the corresponding moulding of equipment, machinery, vehicle etc.

36. be used for making whizzer treat with particle for example dust and/or moisture from surrounding air flow through the method for whizzer, by means of one is the inflow of air, the structure and the installation unit of the three-dimensional of transmitting and flowing out and constitute, carry the air that purifies for equipment, described equipment for example is to ventilate, heating, air regulator and/or be used for to machinery, the device of air feed such as motor, also has the equipment in the vehicle, machinery etc., the structure of described three-dimensional and installation unit have and become grating type to be provided with therein, the special-shaped bar (1.2 that becomes a mandarin by air, 1.3) section bar, each special-shaped bar is provided with mutually and is configured for the capture and/or the separated region of particle to be separated, and constitute simultaneously and can flow through air, the cross section (4) that changes, it is characterized in that

A) leaked-in air is quickened by means of at first being in the cross section (4.1) of the diminishing sky of nozzle-type one against the forming part that becomes a mandarin (1.2.1) of flow direction convex bending of the first special-shaped bar (1.2);

B) air is flow to into unlimited first section bar part (1.3.1) of the streamwise of the second special-shaped bar (1.3), separating solid particles to a considerable extent in having first separated region (5.1) of first resolution element (5.1.1) therein, and make the deflection of air stream on the other hand and continue to turn to and enter second section bar part (1.3.4) that the vane type of the second special-shaped bar (1.3) opens wide, special therein also not humidity/the liquid particle of deposition have in second separated region (5.2) of second resolution element (5.2.1) almost completely separated one;

C) last, air stream enters the 3rd section bar that the opens wide part (1.2.2) of the first special-shaped bar (1.2) on the one hand, its formation one has the 3rd separated region (5.3) of the 3rd resolution element (5.3.1), be used for the separation fully of the reality of particle, and on the other hand in the cross section (4.2) that enlarges gradually of the air stream of discharging, second connect bar (1.3.3) and the outer wall of the 3rd section bar part (1.2.2) of opening wide between the zone in produce the pressure recovery, and

D) at said separated region (5.1,5.2,5.3) in, flow velocity can drop to zero nearly, and the mobile tranquil dead band of formation therein, thereby the particle of separation constantly is being gathered in the discharging area (2.1) owing to downward shear flow and gravity effect on the length of special-shaped bar (1.2,1.3) and can be excluded therefrom.

37. according to the described method of claim 36, it is characterized in that, be flowing in and be positioned at separated region (5.1,5.2,5.3) be blocked in the recirculation zone in the scope and can rotate lentamente therein, should flow therein and can drive, and the diffusion effect that constitutes by means of the wall between the section bar surface of the first special-shaped bar (1.2) and the second special-shaped bar (1.3) that flows then can not flowed to application places by off-load with after this in fact having particle by main flow.

38. according to claim 36 or 37 described methods, it is characterized in that flowing can be by at least one section bar that opens wide part (3.2.1,3.2.3,3.1.2) be blocked in the capture zone that constitutes, and in this capture zone, can form secondary circulation (extremely) zone.

39., it is characterized in that air through-flowly is actually the no pressure loss from entering until what discharge whizzer according to one of claim 36 to 38 described method.

40. according to one of claim 36 to 39 described method, it is characterized in that the pressure loss of main portions is limited to the wall of first section bar that opens wide part (1.3.1) of the second special-shaped bar (1.2) and first flow region that connects between the bar (1.2.4) of the first special-shaped bar (1.2).

41. according to one of claim 36 to 40 described method, it is characterized in that, can recover a part of power pressure by means of diffusion effect.

42. according to one of claim 36 to 41 described method, it is characterized in that, the curved surface and/or the second special-shaped bar (1.3) by means of the forming part that becomes a mandarin (1.2.1) of the first special-shaped bar (1.2) produce such centrifugal acceleration in through-flow, it causes throwing away the particle that density going along with in the air is higher than liquid particle, as solids, wherein said solids are reflected from profile wall after the collision of elasticity/plasticity.

43., it is characterized in that the solids that contain are accelerated and are able to simultaneously momentum with flowing and improve according to one of claim 36 to 42 described method in each inflow region in flowing into air.

44. according to one of claim 36 to 43 described method, it is characterized in that, the solids that contain in flowing into air are because the crooked surface that becomes a mandarin is subjected to a centrifugal acceleration, wherein especially at mobile edge particle going along with regard to transverse to the trend of main flow direction to an intermediary movements that becomes a mandarin cross section accordingly.

45., it is characterized in that the liquid component of particle such as water droplet/little water droplet forms a skin covering of the surface later in the wall collision with section bar according to one of claim 36 to 44 described method, it flows out under the effect of wall shearing stress and gravity.

46., it is characterized in that at first bigger liquid particle drops in its surface of interior collision, zone of the forming part that becomes a mandarin and flows out as skin covering of the surface according to one of claim 36 to 45 described method.

47., it is characterized in that (1.3.2 1.3.5) goes up separated and is discharged from as liquid the skin covering of the surface of liquid particle in first and/or second separation edge of the second special-shaped bar (1.3) according to one of claim 36 to 46 described method.

48., it is characterized in that those run into the water droplet/little water droplet on special-shaped bar (1.2,1.3) surface according to one of claim 36 to 47 described method in capture zone, flow out owing to gravity and separated thus as liquid film.

49., it is characterized in that the liquid particle that is thrown out of is run into the inwall of second section bar part (1.3.4) that the vane type of the second special-shaped bar (1.3) opens wide according to one of claim 36 to 48 described method, it constitutes catch tank, and mainly separated there.

50., it is characterized in that capture the flight water droplet, it is excluded as the surface liquid film according to one of claim 36 to 49 described method.

51. according to one of claim 36 to 50 described method, it is characterized in that, at different section bars textural and in these flow regions particle to be separated since shear stress and/or gravity effect to discharging area (2.1) motion of whizzer and be excluded there.

52. use whizzer according to one of claim 36 to 51 described method, it separates grid (3) separating particles from the air that flows through whizzer by means of one, for example dust and/or water, described whizzer has a kind of flat structure of three-dimensional and the form of installation unit, be used for equipment as ventilating, heating, air regulator and/or mechanical in order to give, the device of air feed such as motor, the equipment that also is used for vehicle, machinery etc., be included in the whizzer vertical and be arranged in parallel, constitute the special-shaped bar that separates grid (3), these special-shaped bars are flowed into by air and are through-flow in the cross section (4) of sky, and separated region with the priority dislocation formation that is used for separating particles, it is characterized in that, be provided with the first special-shaped bar (1.2) and the second special-shaped bar (1.3), section bar part (the 1.3.1 that these special-shaped bars open wide with its streamwise, 1.3.4,1.2.2) constitute resolution element (5.1.1 with relative configurations, 5.2.1,5.3.1) first, the second and the 3rd separated region (5.1,5.2,5.3).

53. according to the described whizzer of claim 52, it is characterized in that,

A) first irregular strip (1.2); Its at first have (streamwise) convex bending, comprise about 45 ° of forming parts that become a mandarin (1.2.1) to the upper surface of intrinsic deflection; It connects first and connects bar (1.2.4) and last the 3rd section bar that the opens wide part (1.2.2) with the 3rd resolution element (5.3.1) that connects; These resolution elements by rounding open wide forward and consisted of by the first a pair of blade that has at the flange of the upper indentation of the 3rd separation edge (1.2.3) that connects that bar (1.2.4) separates; Consist of thus two cavate catch tanks that separate

B) be parallel to the second special-shaped bar (1.3) that the first special-shaped bar is provided with, it at first has streamwise) meet first section bar part stream, that open wide (1.3.1), it is by the blade formation that goes up the flange of indentation in first separation edge (1.3.2) that has of rounding, and constitute the cavate catch tank thus, connect a pair of cavate catch tank that separates again, its formation has second section bar that the opens wide part (1.3.4) of second separation edge (1.3.5), and each second separation edge (1.3.5) makes second section bar part (1.3.4) carry out the transition to second and connects bar (1.3.3).

54. according to claim 52 or 53 described whizzers, it is characterized in that,

A) cross section of one first special-shaped bar (1.2), it at first has the forming part of becoming a mandarin (1.2.1) along the air feed direction, has first the 3rd section bar part (1.2.2) that connects bar (1.2.4) and open wide then;

B) cross section of one second special-shaped bar (1.3), it has unlimited first section bar part (1.3.1) and has unlimited second section bar part (1.3.4) then as the forming part that becomes a mandarin along the air feed direction; And

C) setting that replaces mutually of special-shaped bar (1.2,1.3), it constitutes the cross section (4) that can go up through-flow sky in the degree of depth (T) of whizzer, this cross section along the air feed direction

-have the cross section (4.1) that is the diminishing sky of nozzle-type on the one hand, so that quicken the speed of leaked-in air, it connects the cross section (4.2) of the sky that strengthens gradually, so that reduce air velocity up to the interception of its part and in order to reduce the pressure loss;

-and have first separated region (5.1), second separated region (5.2) and the 3rd separated region (5.3) that is used for particle on the other hand, they have resolution element (5.1.1 respectively, 5.2.1,5.3.1), these resolution elements form the cross section (4) that is in the sky between the special-shaped bar (1.2,1.3) respectively.

55. according to one of claim 52 to 54 described whizzer, it is characterized in that, abnormity bar (1.2,1.3) have first and connect bar (1.2.4) and connect bar formula protuberance (1.2.5) and second and connect bar (1.3.3), not only in order to steady air flow but also be used for special-shaped bar (1.2,1.3) fixing on a framework (2).

56. according to one of claim 52 to 55 described whizzer, it is characterized in that, at least one separated region (5.1,5.2,5.3) (1.3.1,1.3.4 1.2.2) constitute " virtual cyclone separator " together for the section bar part of opening wide together with cavate under it or that connect at least one function, in order to separating particles, the perhaps whizzer functional character that in separating grid (3), has the part of a centrifugal force-virtual-cyclone separator.

57. according to one of claim 52 to 56 described whizzer, it is characterized in that, be provided with the device (2.2) that is connected with framework (2) in order to set up.

58. according to one of claim 52 to 57 described whizzer, it is characterized in that,

A) framework (2) is provided with the first and second special-shaped bars (1.2,1.3) vertical therein and that be parallel to each other and extend;

B) special-shaped bar (1.2,1.3) length (l) in the height (H) of whizzer, extend as separating grid (3), abnormity bar (1.2,1.3) roughly take the degree of depth (T) of whizzer, and a plurality of vertical and special-shaped bars (1.2 of being parallel to each other and extending, 1.3) be arranged in the width (B) of whizzer, form thus and separate grid (3), and

C) be provided for getting rid of the discharging area (2.1) of the particle of separation.

59., it is characterized in that special-shaped bar (1.2,1.3) is fixed in the framework (2) by the removable or non-disconnectable formula of device (2.2) according to one of claim 52 to 58 described whizzer.

60. according to one of claim 52 to 59 described whizzer, it is characterized in that, bear the surface that flows into the surperficial of air and/or bear the outflow air and cover by unshowned multihole lamina or diagrid.

61., it is characterized in that according to one of claim 52 to 60 described whizzer, take an installation site, its depart from vertical line until+/-45 °.

62. according to one of claim 52 to 61 described whizzer, it is characterized in that having a kind of like this external styling, its profile and size all can be matched with the corresponding moulding of equipment, machinery, vehicle etc.

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