CN103008241A

CN103008241A - Separator and wind power separation system

Info

Publication number: CN103008241A
Application number: CN2012105594312A
Authority: CN
Inventors: 高根树
Original assignee: Changsha Zoomlion Environmental Sanitation Machinery Co Ltd
Current assignee: Changsha Zoomlion Environmental Industry Co Ltd
Priority date: 2012-12-20
Filing date: 2012-12-20
Publication date: 2013-04-03
Anticipated expiration: 2032-12-20
Also published as: CN103008241B

Abstract

The invention discloses a separator, which comprises a shell (2), a pin wheel rotor (3), a centrifugal chamber (4), an air outlet fairing cone (5), a material falling hopper flange (7), a material falling hopper (9), an air inlet chamber (10) and an air outlet chamber (11), wherein the pin wheel rotor (3), the centrifugal chamber (4), the air outlet fairing cone (5), the material falling hopper flange (7), the material falling hopper (9), the air inlet chamber (10) and the air outlet chamber (11) are coaxially arranged in the shell; and the side wall of the centrifugal chamber (4) is provided with a plurality of holes. The invention also discloses a wind power separation system with the separator. Through the scheme, as the side wall of the centrifugal chamber (4) is provided with a plurality of holes, the separated small particles can timely reach the outer part of the centrifugal chamber, namely a space between the centrifugal chamber and the shell, through the holes; the condition that the small particles are separated from the gas is further realized; and the rotation speed of the small particles which are in high rotation speed can be obviously reduced after the small particles pass through the holes, so that the small particles outside the centrifugal chamber (4) can easily fall off in the material falling hopper at the action of gravity, and thereby the better separating effect can be reached.

Description

Seperator and wind sorting system

Technical field

The present invention relates to the pneumatic separating field of mixed material, such as chemical field and domestic waste sorting (such as separating plastic) field etc. particularly, relates to a kind of seperator, also relates to a kind of wind sorting system.

Background technology

Along with the raising of life of urban resident level, the content of plastics constantly increases in the house refuse.Plastics become garbage as resource, recycling emphasis point day by day.The plastics machinery sorting technology has generally adopted the pneumatic separating technology, namely realizes the sorting of plastic garbage in the house refuse by wind sorting system.Certainly, wind sorting system also can be applied to other field, for example chemical field.

Wind sorting system generally includes winnowing machine and seperator.

Winnowing machine for example can comprise blower fan, air register and selection by winnowing chamber, described selection by winnowing chamber comprises housing, this housing forms the entrance and exit of selection by winnowing chamber, one end of described air register is provided with air inlet, the other end forms tuyere, the outlet of described blower fan is connected with the air inlet of described air register, and the tuyere of described air register stretches into described selection by winnowing chamber from the entrance of described selection by winnowing chamber.The indoor cylinder that arranges of selection by winnowing is so that material is from the entrance of selection by winnowing chamber to the outlet migration.

The course of work of separator is: for example shed material by feeding machine to the entrance of selection by winnowing chamber, blower fan is blown by air register, blows to the selection by winnowing chamber.Material drops down onto on the indoor cylinder of selection by winnowing, heavy thing is wherein discharged by heavy thing blanking port under Action of Gravity Field, and can be delivered to assigned address by heavy thing conveyer, other light materials wind-engaging power effects and affix to and obtain migration agent on the cylinder move forward.Last these lightweight things are admitted to the inlet chamber of seperator as mentioned below, finish final sorting in seperator.

Seperator (for example integrated separation machine) then can comprise housing and essentially coaxially be arranged on this housing interior needle rotor, centrifugal chamber, exit cone, material-falling hopper flange, material-falling hopper, inlet chamber and outlet chamber; Centrifugal chamber roughly is cone barrel, and around the needle rotor setting; Exit cone roughly is cone barrel, is arranged in the centrifugal chamber and is positioned at the below of needle rotor; The material-falling hopper flange is fixed with respect to housing, and centrifugal chamber and exit cone are fixed on the top of material-falling hopper flange, and material-falling hopper is fixed on the below of material-falling hopper flange; Be formed with air inlet and gas outlet on the housing, inlet chamber extends in housing from the air inlet of housing, and outlet chamber side space under the exit cone extends to the gas outlet of housing.And in inlet chamber, be provided with the grid grate, be provided with the ring grate in periphery, centrifugal chamber.

The course of work of seperator can be divided into primary separation process and the second-order separation process.Primary separation process is: mixture to be separated (comprising larger pieces of material, bulky grain, granule and gas) enters the integrated separation machine from the air inlet of the inlet chamber of integrated separation machine.Larger pieces of material in the mixture (such as polybag, band etc.) is subject to the retardance of the ring grate of near the grid grate of air inlet and periphery, centrifugal chamber, or hits or be suspended on the grate bar, falls into the discharge bin of lower housing portion under Action of Gravity Field along the bar downslide.Bulky grain in the mixture also falls under gravity into discharge bin.Material in the discharge bin can be from the discharge port discharging, and is delivered to the precalculated position by the light material conveyer.The second-order separation process is: the gas of separating in primary separation process and short grained mixture enter the centrifugal chamber of seperator, under the needle rotor High Rotation Speed drives, High Rotation Speed thereupon, thus mixture is separated into granule and gas under centrifugal action.On the one hand, granule in the mixture (dust granule) is applied in larger centrifugal force, so that granule carries out outwards downward centrifugal motion, causes dust granule to arrive on the sidewall in centrifugal chamber, so dust granule moves downward along centrifugal chamber sidewall, falls in the material-falling hopper and discharges.On the other hand, the centrifugal force that the gas of relative clean is subject to is less, therefore enters the cavity center in centrifugal chamber, forms downward strong eddy flow.When arriving bottom, centrifugal chamber, enter exit cone inside, continue to do the high speed circumnutation, discharge by outlet chamber and outlet pipe at last.

There is the dissatisfactory shortcoming of separating effect in above-mentioned wind sorting system.

Summary of the invention

The purpose of this invention is to provide preferably seperator of a kind of separating effect.

To achieve these goals, the invention provides a kind of seperator, this seperator comprises housing and essentially coaxially is arranged on this housing interior needle rotor, centrifugal chamber, exit cone, material-falling hopper flange, material-falling hopper, inlet chamber and outlet chamber; Described centrifugal chamber roughly is cone barrel, and around described needle rotor setting; Described exit cone roughly is cone barrel, is arranged in the described centrifugal chamber and is positioned at the below of described needle rotor; Described material-falling hopper flange is fixed with respect to described housing, and described centrifugal chamber and exit cone are fixed on the top of described material-falling hopper flange, and described material-falling hopper is fixed on the below of described material-falling hopper flange; Be formed with air inlet and gas outlet on the described housing, described inlet chamber extends in described housing from the air inlet of described housing, and described outlet chamber side space under the described exit cone extends to the gas outlet of described housing; Wherein, be formed with a plurality of holes on the sidewall in described centrifugal chamber.

Preferably, described a plurality of hole is the cylindrical void that intermittently distributes ringwise.

Preferably, described a plurality of hole is formed at the bottom section of the sidewall in described centrifugal chamber.

Preferably, described material-falling hopper flange comprises the first annulus, the second annulus and a plurality of floor, and the radius of described the first annulus is less than the radius of the second annulus, and described floor radially is connected between described the first annulus and the second annulus.

Preferably, the bottom in described centrifugal chamber is fixed on described the second annulus, and described exit cone is fixed on described the first annulus.

Preferably, a plurality of floors below of described material-falling hopper flange is provided with a plurality of blades, and this blade roughly is the tabular of inclination, and incline direction is consistent with flow rotation direction in the described centrifugal chamber.

Preferably, described a plurality of blade pass are crossed annular slab connection, the first annulus arranged concentric of this annular slab and described material-falling hopper flange.

Preferably, this seperator comprises a plurality of described annular slab that diameter is different.

Preferably, described material-falling hopper flange top is coated with annular oriffice, and this annular oriffice comprises the plate body of annular, is formed with a plurality of holes on this plate body.

Preferably, described annular oriffice covers the first annulus of described material-falling hopper flange and the space between the second annulus at least.

Preferably, described exit cone surrounds hollow cavity by sidewall, and is formed with a plurality of holes on the sidewall of this exit cone.

Preferably, the described a plurality of pore size distributions that form on the sidewall of described exit cone are at the upper area of this sidewall.

Preferably, the roof of described outlet chamber is positioned at the below of described material-falling hopper flange, and with described material-falling hopper flange separately.

Preferably, this seperator comprises that also the ring of arranging around described centrifugal chamber combs, and this ring is combed and comprised and many ring comb bars from from the top cover of described housing to downward-extension be provided with the arc filter screen on the outer peripheral face of the close described inlet chamber of described ring comb.

Preferably, this seperator also comprises the stem stem that is arranged in the described exit cone, and this stem stem extends through described outlet chamber and described exit cone with the coaxial setting of described exit cone, described stem stem.

Preferably, described seperator is dust removal machine.

On the other hand, the present invention also provides a kind of wind sorting system, and wherein, this wind sorting system comprises seperator as indicated above.

Pass through technique scheme, sidewall by centrifugal chamber is formed with a plurality of holes, therefore the isolated granule outside that can be in time arrives centrifugal chamber by these holes is the space between centrifugal chamber and the housing, further realize with the separating of gas in, originally the granule of High Rotation Speed can reduce its rotary speed significantly through after these holes, thereby the granule that arrives outside, centrifugal chamber can easily be deposited in the material-falling hopper under Action of Gravity Field, thereby reaches preferably separating effect.

Other features and advantages of the present invention will partly be described in detail in the specific embodiment subsequently.

Description of drawings

Accompanying drawing is to be used to provide a further understanding of the present invention, and consists of the part of specification, is used from explanation the present invention with the following specific embodiment one, but is not construed as limiting the invention.In the accompanying drawings:

Fig. 1 is the structural representation of the winnowing machine that provides according to one embodiment of the present invention;

Fig. 2 is the schematic side view of winnowing machine as shown in Figure 1;

Fig. 3 is the schematic top plan view of winnowing machine as shown in Figure 1;

Fig. 4 is along the schematic cross-section of A-A line among Fig. 2;

Fig. 5 is the structural representation of the integrated separation machine that provides according to one embodiment of the present invention;

Fig. 6 is the internal structure schematic diagram of integrated separation machine as shown in Figure 1;

Fig. 7 is the local enlarged diagram of integrated separation machine shown in Figure 6;

Fig. 8 is the structural representation of the wind sorting system that provides according to one embodiment of the present invention;

Fig. 9 is the structural representation of the dust removal machine that provides according to one embodiment of the present invention;

Figure 10 is dust removal machine as shown in Figure 9

Figure 11 has shown the structure of blade, annular slab and the outlet chamber that can arrange for material-falling hopper flange and the below thereof of seperator provided by the invention;

Figure 12 has shown the structure that can be used for the annular oriffice of seperator provided by the invention, has wherein only shown half annular oriffice.

Description of reference numerals

The specific embodiment

Below in conjunction with accompanying drawing the specific embodiment of the present invention is elaborated.Should be understood that the specific embodiment described herein only is used for description and interpretation the present invention, is not limited to the present invention.

The below's minute two parts are described in detail wind sorting system and dust removal machine respectively, because the integrated separation machine in dust removal machine and the wind sorting system all belongs to seperator, a lot of features can be general, and text description and some accompanying drawings of therefore being used for these general features of explanation can cross-reference and references.

I, first: wind sorting system

The below describes the concrete structure of wind sorting system in detail, and wind sorting system mainly comprises winnowing machine and integrated separation machine.

One, winnowing machine

Winnowing machine mainly comprises blower fan 31, air register 32, selection by winnowing chamber 33, feeding machine and heavy thing conveyer.

Air register 32 is for roughly to be fan-shaped hollow housing, and housing one end is provided with air inlet, and the housing other end forms tuyere, and the shape of this housing broadens gradually from air inlet to tuyere and becomes flat.Air register 32 upwards stretches into separation chamber 33 from the side-lower inclined position of selection by winnowing chamber 33.The air inlet of air register 32 is connected with the outlet of blower fan 31, and the tuyere of air register 32 is positioned at the below of feeding conveyer 34.The tuyere width of air register 32 is suitable with the width of selection by winnowing chamber 33.Preferably, be provided with a plurality of deflectors 321 of arranging along the width parallel interval of tuyere in the tuyere of air register 32.

Selection by winnowing chamber 33 comprises housing 331 and the conveyer 332 that is arranged in this housing 331.Housing 331 forms the entrance and exit of selection by winnowing chamber.The porch of selection by winnowing chamber 33 can hang row's flexible plastic bar.Can form observation window on the sidewall of housing 331.The heavy thing blanking port of selection by winnowing chamber 33 is formed on the bottom of housing 331.Heavy thing conveyer is arranged on this heavy thing blanking port below, in order to when needed isolated heavy thing is delivered to assigned address.

Conveyer 332 can be the various suitable conveyers such as ribbon conveyer, chain transmission plate belt conveyor, as a kind of concrete embodiment, this conveyer 332 is belt feeder, comprise motor, decelerator, a roller, tail roller, bearing block, tensioning apparatus, framework and belt 3321, and be fixed on the support by framework.This conveyer 332 is in tilted layout, and the head of the entrance of close selection by winnowing chamber 33 is lower, and the afterbody of the outlet of close selection by winnowing chamber 33 is higher, and the angle of inclination is greater than 25 °, and afterbody surpasses the height of feeding machine.The head of conveyer 332 is positioned at the oblique below of air register 32, and stretches out the lower wall surface of selection by winnowing chamber 33, and the afterbody of conveyer 332 embeds inlet chamber 10 certain distances of integrated separation machine hereinafter described by the outlet of selection by winnowing chamber 33.The width of the belt 3321 of conveyer 332 is less than the width of the housing of selection by winnowing chamber 33.

The discharge end of feeding machine stretches into the entrance of selection by winnowing chamber 33, and is arranged in conveyer 332 tops.

Preferably, conveyer 332 can also comprise deviation correction mechanism.This deviation correction mechanism comprises the angle steel 333 on the both sides inwall of stationary housing 331, angle steel 333 bags of both sides are held the upper carrying breadth of the belt 3321 of conveyer 332, can either prevent belt deviation, can also play sealing function, prevent from the leakage of the space between belt and inner walls material.

Preferably, also be provided with wind deflector 334 in the housing 331 of selection by winnowing chamber 33, this wind deflector 334 is undulate tabular roughly, is arranged on conveyer 332 tops.Corrugated wind deflector 334 can be take the wave trough position of minimum point as boundary, is divided into gradually to the First of downward-extension and upwardly extending second one gradually.This wave trough position of corrugated wind deflector 334 can be arranged in the top in crosspoint of bearing of trend of the tuyere of the bearing of trend of discharge end of feeding machine and air register 32.Thereby wind deflector 334 form enlargings to the First of downward-extension and the conveyer 332 that is in tilted layout gradually, be convenient to material and shed on conveyer 332 and be convenient to the air-flow that the tuyere of air register 32 blows out from the discharge end of feeding machine and enter in the selection by winnowing chamber 33; Simultaneously, the cross-sectional sizes in the air current flow space that forms between upwardly extending second one and the conveyer 332 that is in tilted layout gradually of wind deflector 334 keeps basically identical, so that the wind speed maintenance is substantially even, improve whole wind speed, improve the migration force that the lightweight thing is subject to.

Preferably, winnowing machine also comprises for the governor motion of regulating the distance between conveyer 332 and the feeding machine.This governor motion for example can be the leading screw governor motion.

In sum, the invention provides a kind of winnowing machine, this winnowing machine comprises blower fan 31, air register 32 and selection by winnowing chamber 33, described selection by winnowing chamber 33 comprises housing 331, this housing 331 forms the entrance and exit of selection by winnowing chamber 33, one end of described air register 32 is provided with air inlet, the other end forms tuyere, the outlet of described blower fan 31 is connected with the air inlet of described air register 32, the tuyere of described air register 32 stretches into described selection by winnowing chamber 33 from the entrance of described selection by winnowing chamber 33, be provided with the mass transport part in the housing 331 of described selection by winnowing chamber 33, wherein, also be provided with wind deflector 334 in the housing 331 of described selection by winnowing chamber 33, the conveyor surface almost parallel ground of at least a portion plate face of this wind deflector 334 and described mass transport part arranges, and is arranged on the top of described mass transport part.

Preferably, described wind deflector 334 roughly is corrugated tabular that outlet from from the entrance of described selection by winnowing chamber 33 to described selection by winnowing chamber 33 extends.

Preferably, described winnowing machine also comprises feeding machine, and the discharge end of this feeding machine stretches into the entrance of described selection by winnowing chamber 33, and is arranged in described conveyer 332 tops.

Preferably, corrugated described wind deflector 334 is take the wave trough position of minimum point as boundary, be divided into gradually to the First of downward-extension and upwardly extending second one gradually, described wave trough position is arranged in the top in crosspoint of bearing of trend of the tuyere of the bearing of trend of discharge end of described feeding machine and described air register 32.

Preferably, this winnowing machine also comprises be used to the governor motion of regulating the distance between described conveyer 332 and the described feeding machine.

Preferably, described governor motion is the leading screw governor motion.

Preferably, be provided with a plurality of deflectors 321 of arranging along the width parallel interval of tuyere in the tuyere of described air register 32.

The below describes the course of work of winnowing machine mentioned above.

The discharge end of feeding machine 34 is shed material to the head of the conveyer 332 of selection by winnowing chamber 33, and blower fan 31 is by air register 32 air-supplies, blows to selection by winnowing chamber 33 with obliquely direction.Material drops down onto on the conveyer 332, heavy thing is wherein upspring and is dropped to the discharge of heavy thing blanking port, and can be delivered to assigned address by heavy thing conveyer, other light materials wind-engaging power effects and obtain migration agent on the sluggish belt that affixes to conveyer 331 move forward.Last these lightweight things are admitted to the inlet chamber 10 of integrated separation machine as mentioned below, finish final sorting in the integrated separation machine.

Above-mentioned winnowing machine advantage structurally comprises:

(1), owing to be provided with the conveyer that is in tilted layout in the selection by winnowing chamber 33, therefore can improve sorting quality and the selection by winnowing efficient of winnowing machine.In the selection by winnowing process, all materials all drop on first on the conveyer 332, even the heavy thing can be along with conveyer 332 migrations one segment distance, in this transition process, also can under Action of Gravity Field, slide and discharge from heavy thing blanking port, only have the lightweight thing can be admitted to the inlet chamber 10 of integrated separation machine, even increase the feeding capacity of feeding machine 34, the heavy thing can not crossed conveyer 332 yet and sneak in the lightweight thing, therefore can improve sorting quality and the selection by winnowing efficient of winnowing machine.

(2), the corrugated wind deflector 334 of selection by winnowing chamber 33 interior layouts, thereby can reduce the area of section of wind-force effect, wind speed is increased, improve the migration force that the lightweight thing is subject to.

(3), a plurality of deflectors 321 of arranging along the width parallel interval of tuyere in the tuyere of air register 32, thereby can avoid dispersing of tuyere place air-flow, improve the uniformity of current rate.

(4), conveyer 332 can also comprise the deviation correction mechanism of angle steel form.This deviation correction mechanism can either prevent belt deviation, can also play sealing function, prevents from the leakage of the space between belt and inner walls material.

(5), winnowing machine also comprises for the governor motion of regulating the distance between conveyer 332 and the feeding machine.Thereby can come the flexible modulation should distance for the material situation of Various Seasonal, different material humidity, to reach the desirable efficiency of separation.

Two, integrated separation machine

The integrated separation owner will comprise: power set 1, housing 2, needle rotor 3, centrifugal chamber 4, exit cone 5, stem stem 6, material-falling hopper flange 7, annular oriffice 8, material-falling hopper 9, inlet chamber 10, outlet chamber 11, light material conveyer, the second collection ash can 15, grid grate 18 and ring grate 19.

Power set 1 are used for driving needle rotor 3 and rotate, and power set 1 can comprise motor, bearing housing and vertical pivot, and motor drives vertical pivot by bearing housing and rotates.

Housing 2 comprises top cover and sidewall, and top cover is roughly rectangular, and sidewall is extended straight down by the outer peripheral edges of top cover and forms, and top cover and sidewall surround the inner chamber of housing jointly.

Preferably, the top cover of housing 2 is stepped, and for example this top cover can comprise the first top cover 21, the second top cover 22 and the 3rd top cover 23.The first top cover 21 and the second top cover 22 are respectively tabular, the first top cover 21 is positioned at a side (right side for example of housing, namely be positioned at the top of inlet chamber 10), the second top cover 22 is positioned at the opposite side of housing (for example, namely be positioned at the top in needle rotor 3 and centrifugal chamber 4), the second top cover 22 is higher than the first top cover 21.The 3rd top cover 23 is connected between the first top cover 21 and the second top cover 22, and the angle of the 3rd top cover 23 and the first top cover 21 is the obtuse angle, thereby top cover integral body is stepped.

The sidewall of housing 2 can comprise the first side wall, the second sidewall, the 3rd sidewall and the 4th sidewall, and the first side wall and the second sidewall lay respectively at the both sides, front and back of housing, and the 3rd sidewall and the 4th sidewall lay respectively at the left and right sides of housing.The first side wall offers air inlet, gas outlet and blanking port, and air inlet is positioned at the right side of the first side wall, and gas outlet and blanking port are positioned at the left side of the second sidewall.Air inlet is higher than the gas outlet, and the gas outlet is positioned at the blanking port top.Preferably, can be provided with access panel on the sidewall of housing 2, thereby maintain easily the parts of housing 2 inside.Preferably, the second sidewall of housing 2 respectively and the junction between the 3rd sidewall and the 4th sidewall and the junction between the 3rd sidewall and the first side wall all be provided with the arc transition plate, so that the junction forms arc transition, thereby suppress the formation of the turbulent flow in housing 2 inner chambers, improve separating effect.The space of the first top cover 21 belows of housing 2 consists of inlet chamber 10, and the air inlet of offering on the first side wall consists of the entrance of this inlet chamber 10.

Be provided with grid grate 18 in the inlet chamber 10, grid grate 18 comprises many grid grate bars, the arranged direction of these grid grate bars and airintake direction intersect and are acute angle, intersect in obtuse angle with the blanking direction, insert with about equally spacing the first top cover 21 from housing 2, the top of grid grate bar is fixed on the first top cover 21 of housing 2, for example be fixed on the first top cover 21 arrange batten on.

Discharge bin is formed at the bottom of housing 2, and the discharge bin bottom is formed with discharge port, and the discharge port below is provided with the light material conveyer.Can be provided with gate on the discharge port, carry out discharging thereby can open the sluices when needed.

The vertical pivot of power set 1 stretches into the inner chamber of housing 2.

Needle rotor 3 comprises wheel hub and is fixed on to even intensive hierarchal arrangement radially wire pin seedling on this wheel hub.Needle rotor 3 is arranged at the below of the second top cover 22 in the inner chamber of housing 2, and is positioned at the bottom of power set 1.The wheel hub of needle rotor 3 is connected with the vertical pivot of power set 1 is coaxial.The integrated separation machine can arrange one or more needle rotors 3 as required.

Centrifugal chamber 4 is arranged at the below of the second top cover 22 in the housing 2, and is positioned at the periphery of needle rotor 3, has identical central axis with needle rotor 3.Centrifugal chamber 4 comprises roof, diapire and sidewall, is on the whole cone barrel.The roof in centrifugal chamber 4 is circular, sidewall from the outer peripheral edges of roof radially outwards and to downward-extension, it is circular that diapire also is, from radially outwards flatly (namely along the inwall of the direction vertical with the pivot center of needle rotor 3 towards housing 2) extension of bottom peripheral edge of sidewall, and can be fixed on the second annulus 72 of material-falling hopper flange 7 hereinafter described.That is to say that the outer peripheral edges of the roof in centrifugal chamber 4 are connected with the top of sidewall, the bottom of the sidewall of the inner peripheral of the diapire in centrifugal chamber 4 connects.Form the first opening on the roof in centrifugal chamber 4, form the second opening on the diapire, side wall ring surrounds cavity around this first opening and the second opening.Preferably, the roof in centrifugal chamber 4 is lower than the top certain altitude of needle rotor 3.That is to say that needle rotor 3 is not to be positioned at centrifugal chamber 4 fully, but part is stretched out from the roof in centrifugal chamber 4.Preferably, the bottom section of the sidewall in centrifugal chamber 4 is formed with the interrupted cylindrical void 41 that distributes of annular.

Exit cone 5 is arranged in the centrifugal chamber 4 and is positioned at the below of needle rotor 3, has identical central axis with centrifugal chamber 4.This exit cone 5 surrounds hollow cavity by sidewall, is on the whole the cone tubular.The first circular open is formed on the top of exit cone 5, and the second circular open is formed on the bottom, and the radius of this first circular open can be greater than the radius of needle rotor 3.There is certain distance in the bottom of the top of exit cone 5 and needle rotor 3, and the bottom of exit cone 5 is fixed on the material-falling hopper flange 7 described hereinafter.Preferably, the side wall ring week of exit cone 5 is provided with a plurality of holes 51, and this hole can be circular hole, and the aperture roughly can be 5～30mm.

Stem stem 6 is arranged in the cavity of exit cone 5, and has identical central axis with exit cone 5.The shape of stem stem 6 for example can comprise the frustum on top and the cylinder of bottom.The cylinder bottom surface of stem stem 6 is fixed on the outlet chamber 11 described hereinafter, and stem stem 6 extends through this outlet chamber and exit cone 5, and the end face of stem stem 6 can be concordant with the top of exit cone 5.

Material-falling hopper flange 7 comprises the first annulus 71, the second annulus 72 and some floors 73, the first annulus 71 and the second annulus 72 are concentric and coplanar, the radius of the first annulus 71 is less than the radius of the second annulus 72, some floors 73 equidistantly are periphery between the first annulus 71 and the second annulus 72, and each floor 73 radially is connected between the first annulus 71 and the second annulus 72.The bottom of exit cone 5 mentioned above is fixed on the first annulus 71 of this material-falling hopper flange 7.The second annulus 72 is fixing with respect to housing 2, for example can hang on by ring comb 19 hereinafter described the below of the second top cover 22 of housing 2.Material-falling hopper flange 7 and pinwheel turn from 3 and stem stem 6 have identical central axis.

Preferably, be coated with annular oriffice 8 on the material-falling hopper flange 7.More particularly, annular oriffice 8 can be covered on a plurality of floors 73 of material-falling hopper flange 7, thereby covers at least the first annulus 71 of material-falling hopper flange 7 and the space between the second annulus 72.

Material-falling hopper 9 comprises the cylindrical portion 91, the cone cylinder section 92 that is inverted cone barrel that are straight cylinder shape, be positioned at the annular canister section 93 of cylindrical portion 91 and be bonded on the oblique cone cylinder section 96 of cone cylinder section 92 belows.Pass the blanking port of the first side wall of housing 2 under the lower end cone mouth of oblique cone cylinder section 96 is oblique, and be connected with the second collection ash can 15.The upper peripheral edge of cylindrical portion 91 is fixed on the second annulus 72 of material-falling hopper flange 7, and the lower periphery of cylindrical portion 91 engages with the upper peripheral edge of cone cylinder section 92.The radius of annular canister section 93 is less than the radius of material-falling hopper flange 7 second annulus 72, greater than the radius of the first annulus 71.The upper peripheral edge of annular canister section 93 is fixed on the material-falling hopper flange 7, and lower periphery is lower than the roof certain distance of outlet chamber 11 described hereinafter.Be provided with some blades 94 on the outer peripheral face of this annular canister section 93, the shape of blade 94 is roughly the tabular of inclination, and incline direction is consistent with centrifugal chamber 4 interior flow rotation directions.Preferably, a plurality of blades 94 connect by annular slab 95, as shown in the figure, by three annular slabs 95 a plurality of blades 94 are linked together.Preferably, the top of the diapire in centrifugal chamber 4 and material-falling hopper 9 (being the upper peripheral edge of cylindrical portion 91) on the central axial direction in centrifugal chamber 4 at a distance of certain distance.Preferably, the open top of material-falling hopper 9 (being the open top of cylindrical portion 91) is greater than the bottom opening in centrifugal chamber 4 (being the second opening of the diapire in centrifugal chamber 4 mentioned above).

Outlet chamber 11 is arranged at the sidepiece (for example left side) of the cylindrical portion 91 of material-falling hopper 9, and this outlet chamber 11 is gone out from the left back sidewall quadrature tangential direction of cylindrical portion 91 by outlet pipe, passes through mutually with cylindrical portion 91 off-centre to form.Outlet chamber 11 is the rectangular-shaped tangential flat the first side wall that passes housing 2, comprise roof 111, left side wall, right side wall and diapire 112, the left side wall of this outlet chamber 11 comprises the circular ring plate that passes through mutually from cylindrical portion 91 and the left side wall of cuboid, the right side wall of outlet chamber 11 only is the right side wall of cuboid, and the diapire of outlet chamber 11 extends to the lower openings of closed cylinder section 91.Preferably, the roof 111 of outlet chamber 11 is lower than material-falling hopper flange 7 certain distances.

Ring grate 19 comprises many ring grate bars that extend towards the second annulus 72 of material-falling hopper flange 7 from the second top cover 22 of housing 2, and these many ring grate bars are circumferentially equidistantly arranged along the second annulus 72.Preferably, at least part of ring grate bar extends to the second annulus 72 of material-falling hopper flange 7 from the second top cover 22 of housing 2, and is fixed on this second annulus 72, thereby material-falling hopper flange 7 hangs on the second top cover 22 times.Preferably, be provided with arc filter screen 20 on the windward side of this ring grate 19 (i.e. the face of close inlet chamber 10).

Selectively, the integrated separation machine can also comprise that by liquid-jet device this liquid-jet device can comprise feed pipe 16 and atomizer 17, and as shown in the figure, feed pipe 16 can stretch in the material-falling hopper 9 from the cone cylinder section 92 of material-falling hopper 9, and extends through stem stem 6.Atomizer 17 is installed in the end of feed pipe 16, between the bottom of the top of stem stem 6 and needle rotor 3.

The below describes the course of work of integrated separation machine mentioned above.

1, primary separation process

Mixture to be separated (comprising larger pieces of material, bulky grain, granule and gas) enters the integrated separation machine from the air inlet of the inlet chamber 10 of integrated separation machine.Larger pieces of material in the mixture (such as polybag, band etc.) is subject to the retardance of the ring grate 19 of near the grid grate 18 of air inlet and 4 peripheries, centrifugal chamber, or hits or be suspended on the grate bar, falls into the discharge bin of housing 2 bottoms under Action of Gravity Field along the bar downslide.Bulky grain in the mixture also falls under gravity into discharge bin.Material in the discharge bin can be from the discharge port discharging, and is delivered to the precalculated position by the light material conveyer.

In this primary separation process, above-mentioned integrated separation machine advantage structurally comprises:

(1), because the roof in centrifugal chamber 4 is lower than the top certain altitude of needle rotor 3, so needle rotor 3 can decomposite a revolving force to centrifugal chamber 4 outside, aggravate the centrifugation of larger particles.

(2), because the top cover of housing 2 is stepped, therefore bulky grain just falls in the first top cover 21 lower zones, the mixture of granule and gas is then in the zone that further enters under the wind-force effect below the second top cover 22, and then enters in the centrifugal chamber 4 and separate.That is to say that mixture is in the climbing process, because the space becomes large and the abatement of wind, thereby being beneficial to bulky grain falls under Action of Gravity Field, thereby improves the separative efficiency of this primary separation process.

(3), the second sidewall of housing 2 respectively and the junction between the 3rd sidewall and the 4th sidewall and the junction between the 3rd sidewall and the first side wall all be provided with the arc transition plate, so that the junction forms arc transition, thereby suppress the formation of the turbulent flow in housing 2 inner chambers, improve separating effect.

(4), be provided with arc filter screen 20 on the windward side of ring grate 19 (i.e. the face of close inlet chamber 10), therefore when needle rotor 3 does not rotate, the local arc filter screen 20 of hanging up can stop light material (such as polybag, band etc.) to enter in the centrifugal chamber 3 on the ring grate 19, is convenient to the maintenance of needle rotor 3.

(5), the sidewall of housing 2 is provided with access panel, thereby maintains easily the parts of housing 2 inside.

2, the second-order separation process

The gas of separating in primary separation process and short grained mixture enter centrifugal chamber 4, under needle rotor 3 High Rotation Speeds drive, and High Rotation Speed thereupon, thus mixture is separated into granule and gas under centrifugal action.On the one hand, granule in the mixture (dust granule) is applied in larger centrifugal force, so that granule carries out outwards downward centrifugal motion, cause dust granule to arrive on the sidewall in centrifugal chamber 4, so dust granule moves downward along centrifugal chamber 4 sidewalls, fall in the material-falling hopper 9, thereby be disposed in the second collection ash can 15.On the other hand, the centrifugal force that the gas of relative clean is subject to is less, therefore enters the cavity center in centrifugal chamber 4, forms downward strong eddy flow.When arriving 4 bottom, centrifugal chamber, enter exit cone 5 inside, continue to do high speed circumnutation (effect at exit cone 5 and stem stem 6 is to reduce turbulent flow so that gas forms more regular eddy flow) around stem stem 6, discharge by outlet chamber 11 and outlet pipe at last.

It more than is the second-order separation process of dry dust removal mode.If as indicated above, the integrated separation machine also is provided with liquid-jet device, then can adopt preferred semi-wet dedusting method to carry out above-mentioned the second-order separation process.That is to say, after gas and short grained mixture enter centrifugal chamber 4, atomizer 17 ejection atomizing liquid grains (for example water), thus granule can be assembled liquid grain surface, so that particle increases, therefore can reduce it by the possibility of turbulent perturbation.

In this second-order separation process, above-mentioned integrated separation machine advantage structurally comprises:

(1), the bottom section by the sidewall in centrifugal chamber 4 is formed with the interrupted cylindrical void 41 that distributes of annular, therefore isolated granule can arrive the outside (being the space between centrifugal chamber and the housing 2) in centrifugal chamber 4 in time by these long and narrow cylindrical voids 41, further realize with the separating of gas in, originally the granule of High Rotation Speed can reduce its rotary speed significantly through after the cylindrical void 41, thereby the granule that arrives 4 outsides, centrifugal chamber can easily be deposited in the material-falling hopper 9 under Action of Gravity Field, thereby reaches preferably separating effect.

(2), because the top (being the upper peripheral edge of cylindrical portion 91) of the diapire in centrifugal chamber 4 and material-falling hopper 9 certain distance apart on the central axial direction in centrifugal chamber 4, therefore between the top of the diapire in centrifugal chamber 4 and material-falling hopper 9, constructed a longitudinal buffer district (namely the central axial direction in centrifugal chamber 4 has formed the slit buffer circle), further reduced the granule rotary speed, thereby under Action of Gravity Field, be deposited in the material-falling hopper 9 more easily, reach preferably separating effect.

(3), the open top of material-falling hopper 9 (being the open top of cylindrical portion 91) is greater than the bottom opening in centrifugal chamber 4 (being the second opening of the diapire in centrifugal chamber 4 mentioned above).Therefore, on the one hand, between the bottom opening in the open top of material-falling hopper 9 and centrifugal chamber 4, constructed a horizontal buffering area (namely having formed buffering area along the direction vertical with the central axis in centrifugal chamber 4), further reduced the granule rotary speed, thereby under Action of Gravity Field, be deposited in the material-falling hopper 9 more easily, reach preferably separating effect; On the other hand, because material-falling hopper 9 open tops are larger, therefore the granule from centrifugal chamber 4 can be received in the material-falling hopper 9 fully.

(4), be coated with annular oriffice 8 on the material-falling hopper flange 7.Annular oriffice 8 is fully ensureing under the condition that granule sees through, can reduce air-flow in the centrifugal chamber 4 to the probability of material-falling hopper 9 inner penetrations by forming resistance, thereby reduce air-flow to the disturbance of granule sedimentation, so that granule can be deposited in the material-falling hopper 9 more easily, reach preferably separating effect under Action of Gravity Field.

(5), be provided with some blades 94 on the outer peripheral face of annular canister section 93, the shape of blade 94 is roughly the tabular of inclination, and incline direction is consistent with centrifugal chamber 4 interior flow rotation directions.Preferably, a plurality of blades 94 connect by annular slab 95.Therefore, even some flows to material-falling hopper 9 from the air-flow in the centrifugal chamber 4 by annular oriffice 8, the blade 94 that arranges on the outer peripheral face of the annular canister section 93 of this material-falling hopper 9 can steering current swirl velocity transform to axial velocity, reduce air-flow to short grained disturbance, the short grained rotation that intercepts in the material-falling hopper 9 is risen.By annular slab 95 a plurality of blade 94 is interconnected along circular path, thereby annular slab 95 can form resistance, the outer shroud air-flow that stops relatively high pressure passes through and forms turbulent flow to the interior zone of relatively low pressure, thereby further reduces air-flow to short grained disturbance, improves separating effect.

(6), since exit cone 5 be provided with a plurality of holes 51 side wall ring week, therefore the gas of separating is when arriving 4 bottom, centrifugal chamber, be positioned at the air-flow of exit cone 5 outsides except the upper peripheral edge from exit cone 5 enters exit cone 5, most of air-flow can also enter exit cone 5 by a plurality of holes 51 on exit cone 5 sidewalls.If air-flow enters exit cone 5 from the upper peripheral edge of exit cone 5, then because the upper peripheral edge border of exit cone 5 can generate turbulent flow, therefore can produce disturbance to granule on every side; And if air-flow enters exit cone 5 by a plurality of holes 51 on exit cone 5 sidewalls, then air-flow can pass more lenitively hole 51 and enter exit cone 5 in rotary course, reduce the generation of turbulent flow, thereby reduce short grained disturbance on every side, reach better separating effect.More preferably, hole 51 is arranged on the upper area of the sidewall of exit cone 5.The gas of separating is when arriving 4 bottom, centrifugal chamber; the air-flow that is arranged in exit cone 5 outsides progressively enters exit cone 5 in the process that rotates up around exit cone 5; rotate up in the process at this; the granule that is mingled with in the air-flow can obtain sedimentation under Action of Gravity Field; therefore more near the top of exit cone 5, the granule that is mingled with in the air-flow is fewer.Therefore, hole 51 only is arranged on the upper area of the sidewall of exit cone 5, can prevent from being positioned at being mingled with of initial stage fiaring cone 5 lower areas more short grained air-flow and enter exit cone 5, further improves separating effect, purifies the gas of discharging from outlet chamber 11.

(7), the roof 111 of outlet chamber 11 is lower than material-falling hopper flange 7 certain distances.Therefore form the convolution zone between the roof of outlet chamber 11 and material-falling hopper flange 7, the air-flow that flows out from exit cone 5 convolutions can continue to circle round this circles round the zone.Because this convolution zone is comparatively regular substantial cylindrical, therefore air-flow can form regular eddy flow in this convolution process, thereby when entering in the not too regular outlet chamber 11, can reduce the generation of turbulent flow follow-up, reduce the possibility of altering on the air-flow, and then improve separating effect.

(8), at least part of ring grate bar of ring in the grate 19 extends to the second annulus 72 of material-falling hopper flange 7 from the second top cover 22 of housing 2, and is fixed on this second annulus 72.This part ring grate bar can be used for the welding location of the material-falling hopper 9 of material-falling hopper flange 7 belows, controls welding deformation, and can guarantee the axiality of centrifugal chamber 4, material-falling hopper flange 7 and material-falling hopper 9.

Three, wind sorting system

Wind sorting system mainly comprises above-mentioned winnowing machine and integrated separation machine.Winnowing machine and integrated separation machine are arranged on the frame.As indicated above, the afterbody of the conveyer 332 of winnowing machine embeds inlet chamber 10 certain distances of integrated separation machine by the outlet of selection by winnowing chamber 33, in order to the isolated lightweight thing of winnowing machine is delivered to further separation in the integrated separation machine.In addition, the outlet chamber 11 of integrated separation machine can be connected by the air intake vent of circulation airduct 37 with the blower fan 31 of winnowing machine, the outlet chamber 11 exhaust blast of integrated separation machine are offered blower fan 31, so that wind-force obtains is recycling, thereby the reduction system is to the blast requirement of blower fan 31.

Preferably, this wind sorting system also comprises overflow blower fan 38, and this overflow blower fan 38 is communicated with the outlet chamber 11 of integrated separation machine by overflow airduct 39.More specifically, overflow airduct 39 and circulation airduct 37 are communicated with the outlet chamber 11 of integrated separation machine, and overflow airduct 39 is positioned at top, are cattle horn shape and turn out, the lower overflow blower fan 38 that connects; Below overflow airduct 39, circulation airduct 37 stretches out, through being connected with the air intake vent of the blower fan 31 of winnowing machine behind two sections elbows.

The course of work of this wind sorting system is: treat that sorting material is separated into heavy thing and lightweight thing by winnowing machine first, the heavy thing is delivered to assigned address by heavy thing conveyer, and the lightweight thing is then sent in the integrated separation machine and further separated.In the integrated separation machine, the lightweight thing is through primary separation and the second-order separation, in primary separation process, wherein isolated larger pieces of material and bulky grain are delivered to the precalculated position by the light material conveyer, rest materials is separated into granule and gas by the second-order separation process, its small particles is disposed in the second collection ash can 15, the gas of relative clean is then discharged from the outlet chamber 11 of integrated separation machine, a part is circulated to the air intake vent of the blower fan 31 of winnowing machine, another part by the overflow of overflow blower fan to external environment condition.

This wind sorting system is except the structural advantage separately with above-mentioned winnowing machine and integrated separation machine, also has following structural advantage: owing to be provided with overflow blower fan 38, therefore can be so that keep little negative pressure in the system, reduce windage, and owing to overflow blower fan 38 is connected with the outlet chamber 11 of integrated separation machine, so overflow route is shorter, and without blower fan 31, thereby further reduce windage, reduce ineffective energy consumption.

II, second portion: dust removal machine

The below specifies the structure of seperator provided by the invention mainly take dust removal machine as example.

Dust removal machine mainly comprises: power set 1, housing 2, needle rotor 3, centrifugal chamber 4, exit cone 5, stem stem 6, material-falling hopper flange 7, annular oriffice 8, material-falling hopper 9, inlet chamber 10, outlet chamber 11, elementary material blanking tube 12, the first collection ash can 13, guided plate 14 and the second collection ash can 15.

Housing 2 comprises top cover and sidewall, and top cover is roughly rounded, and sidewall is extended straight down by the outer peripheral edges of top cover and forms, and top cover and sidewall surround the inner chamber of housing jointly, and this housing is round straight tube shape on the whole.The vertical pivot of power set 1 stretches into the inner chamber of housing 2, and the symmetrical centre dead in line of the top cover of the axis of vertical pivot and housing 2.

Needle rotor 3 comprises wheel hub and is fixed on to even intensive hierarchal arrangement radially wire pin seedling on this wheel hub.Needle rotor 3 is arranged in the inner chamber of housing 2, and is positioned at the bottom of power set 1.The wheel hub of needle rotor 3 is connected with the vertical pivot of power set 1 is coaxial.Dust removal machine can arrange one or more needle rotors 3 as required.

Centrifugal chamber 4 is arranged in the housing 2 and is positioned at the periphery of needle rotor 3, has identical central axis with needle rotor 3.Centrifugal chamber 4 comprises roof, diapire and sidewall, is on the whole cone barrel.The roof in centrifugal chamber 4 is circular, sidewall from the outer peripheral edges of roof radially outwards and to downward-extension, it is circular that diapire also is, from the bottom peripheral edge of sidewall radially outwards flatly (namely along the inwall of the direction vertical with the pivot center of needle rotor 3 towards housing 2) extend, and be fixed in the bottom of the sidewall of housing 2.That is to say that the outer peripheral edges of the roof in centrifugal chamber 4 are connected with the top of sidewall, the bottom of the sidewall of the inner peripheral of the diapire in centrifugal chamber 4 connects.Form the first opening on the roof in centrifugal chamber 4, form the second opening on the diapire, side wall ring surrounds cavity around this first opening and the second opening.Preferably, the roof in centrifugal chamber 4 is lower than the top certain altitude of needle rotor 3.That is to say that needle rotor 3 is not to be positioned at centrifugal chamber 4 fully, but part is stretched out from the roof in centrifugal chamber 4.Preferably, the bottom section of the sidewall in centrifugal chamber 4 is formed with the interrupted cylindrical void 41 that distributes of annular.

Exit cone 5 is arranged in the centrifugal chamber 4 and is positioned at the below of needle rotor 3, has identical central axis with centrifugal chamber 4.This exit cone 5 surrounds hollow cavity by sidewall, is on the whole the cone tubular.The first circular open is formed on the top of exit cone 5, and the second circular open is formed on the bottom.There is certain distance in the bottom of the top of exit cone 5 and needle rotor 3, and the bottom of exit cone 5 is fixed on the material-falling hopper flange 7 described hereinafter.Preferably, the side wall ring week of exit cone 5 is provided with a plurality of holes 51, and this hole can be circular hole, and the aperture roughly can be 5～30mm.More preferably, hole 51 is arranged on the upper area of the sidewall of exit cone 5.

Stem stem 6 is arranged in the cavity of exit cone 5, and has identical central axis with exit cone 5.The shape of stem stem 6 for example can comprise the frustum on top and the cylinder of bottom.The cylinder bottom surface of stem stem 6 is fixed on the outlet chamber 11 described hereinafter, and stem stem 6 extends through this outlet chamber and exit cone 5, and stretches out certain altitude from exit cone 5, but apart from the bottom certain distance of needle rotor 3.

Material-falling hopper flange 7 comprises the first annulus 71, the second annulus 72 and some floors 73, the first annulus 71 and the second annulus 72 are concentric and coplanar, the radius of the first annulus 71 is less than the radius of the second annulus 72, some floors 73 equidistantly are periphery between the first annulus 71 and the second annulus 72, and each floor 73 radially is connected between the first annulus 71 and the second annulus 72.The bottom of exit cone 5 mentioned above is fixed on the first annulus 71 of this material-falling hopper flange 7.72 bottoms of being fixed in housing 2 of the second annulus.Material-falling hopper flange 7 has identical central axis with housing 2.

Material-falling hopper 9 comprises the cylindrical portion 91 that is straight cylinder shape, the cone cylinder section 92 that is inverted cone barrel and the annular canister section 93 that is positioned at cylindrical portion 91.The upper peripheral edge of cylindrical portion 91 is fixed on the second annulus 72 of material-falling hopper flange 7, and the lower periphery of cylindrical portion 91 engages with the upper peripheral edge of cone cylinder section 92.The radius of annular canister section 93 is less than the radius of material-falling hopper flange 7 second annulus 72, greater than the radius of the first annulus 71.The upper peripheral edge of annular canister section 93 is fixed on the material-falling hopper flange 7, and lower periphery is lower than the roof certain distance of outlet chamber 11 described hereinafter.Be provided with some blades 94 on the outer peripheral face of this annular canister section 93, the shape of blade 94 is roughly the tabular of inclination, and incline direction is consistent with centrifugal chamber 4 interior flow rotation directions.Preferably, a plurality of blades 94 connect by annular slab 95, as shown in the figure, by three annular slabs 95 a plurality of blades 94 are linked together.Preferably, the top of the diapire in centrifugal chamber 4 and material-falling hopper 9 (being the upper peripheral edge of cylindrical portion 91) on the central axial direction in centrifugal chamber 4 at a distance of certain distance.Preferably, the open top of material-falling hopper 9 (being the open top of cylindrical portion 91) is greater than the bottom opening in centrifugal chamber 4 (being the second opening of the diapire in centrifugal chamber 4 mentioned above).As shown in the figure, the radius of the cylindrical portion 91 of material-falling hopper 9 equates substantially with the radius of the sidewall of housing 2, and the radius of the second opening of the diapire in centrifugal chamber 4 is then less than the radius of the sidewall of housing.The lower end of the cone cylinder section 92 of material-falling hopper 9 is the secondary blanking port, and this secondary blanking port is connected with the second collection ash can 15.

Inlet chamber 10 is arranged at a side (for example left side) of housing 2, and this inlet chamber 10 is tangentially entered by admission line, passes through mutually with the inner chamber off-centre of housing 2 to form, and inlet chamber 10 integral body are the snail annular.Inlet chamber 10 comprises roof 101, diapire 102 and sidewall 103.Roof 101 is concordant with the top cover of housing 2, and the inner chamber of diapire 102 from the diapire of admission line to housing 2 is around extension, until surround the sidewall in centrifugal chamber 4.Preferably, the diapire 102 of inlet chamber 10 is lower than the roof certain distance in centrifugal chamber 4.Diapire 102 is positioned at the snail ring of the part formation inlet chamber 10 of housing 2 inner chambers.Be formed with a plurality of holes on the snail ring, and be provided with sideboard, in order to operationally block or expose hole on the snail ring.Preferably, the hole on this snail ring is arcuate socket 1021, and this arcuate socket 1021 extends and forms around the central axis in centrifugal chamber 4.

Outlet chamber 11 is arranged at the sidepiece (for example right side) of the cylindrical portion 91 of material-falling hopper 9, and this outlet chamber 11 is gone out from the right back sidewall quadrature tangential direction of cylindrical portion 91 by outlet pipe, passes through mutually with cylindrical portion 91 off-centre to form.These outlet chamber 11 integral body are the snail annular, comprise roof 111, diapire 112 and sidewall (not shown), and diapire 112 is concordant with the lower periphery of the cylindrical portion 91 of material-falling hopper 9.Preferably, the roof 111 of outlet chamber 11 is lower than material-falling hopper flange 7 certain distances.

The lower sidewall of housing 2 is provided with elementary blanking port, and this elementary blanking port is connected with an end of elementary material blanking tube 12, and the other end of elementary material blanking tube 12 is connected with the first collection ash can 13.Preferably, be provided with the guided plate 14 of inclination in the inner chamber of housing 2, these guided plate 14 spiral surroundings extend to the elementary blanking port of bottom of the inner chamber of housing 2 along spiral path from the inner chamber top of housing 2 outside the sidewall in centrifugal chamber 4.

Selectively, dust removal machine can also comprise that by liquid-jet device this liquid-jet device can comprise feed pipe 16 and atomizer 17, and as shown in the figure, feed pipe 16 can stretch in the material-falling hopper 9 from the cone cylinder section 92 of material-falling hopper 9, and extends through stem stem 6.Atomizer 17 is installed in the end of feed pipe 16, between the bottom of the top of stem stem 16 and needle rotor 3.

In sum, the invention provides a kind of seperator, this seperator comprises housing 2 and essentially coaxially is arranged on needle rotor 3, centrifugal chamber 4, exit cone 5, material-falling hopper flange 7, material-falling hopper 9, inlet chamber 10 and outlet chamber 11 in this housing 2; Described centrifugal chamber 4 roughly is cone barrel, and arranges around described needle rotor 3; Described exit cone 5 roughly is cone barrel, is arranged in the described centrifugal chamber 4 and is positioned at the below of described needle rotor 3; Described material-falling hopper flange 7 is fixed with respect to described housing 2, and described centrifugal chamber 4 and exit cone 5 are fixed on the top of described material-falling hopper flange 7, and described material-falling hopper 9 is fixed on the below of described material-falling hopper flange 7; Be formed with air inlet and gas outlet on the described housing 2, towards described housing 2 interior extensions, described outlet chamber 11 extends to the gas outlet of described housing 2 to described inlet chamber 10 from 5 times side spaces of described exit cone from the air inlet of described housing 2; Wherein, the below of described material-falling hopper flange 7 is provided with a plurality of blades 94, this blade 94 roughly is the tabular of inclination, and incline direction is consistent with described centrifugal chamber 4 interior flow rotation directions, and described a plurality of blade 94 connects by annular slab 95, this annular slab 95 and described material-falling hopper flange 7 arranged concentric.

Preferably, this seperator comprises a plurality of described annular slab 95 that diameter is different.

Preferably, described material-falling hopper flange 7 comprises the first annulus 71, the second annulus 72 and a plurality of floor 73, and the radius of described the first annulus 71 is less than the radius of the second annulus 72, and described floor 73 radially is connected between described the first annulus 71 and the second annulus 72.

Preferably, described a plurality of blade 94 is arranged on the below of the floor 73 of described material-falling hopper flange 7.

Preferably, the bottom in described centrifugal chamber 4 is fixed on described the second annulus 72, and described exit cone 5 is fixed on described the first annulus 71.

On the other hand, the present invention also provides a kind of seperator, and this seperator comprises housing 2 and essentially coaxially is arranged on needle rotor 3, centrifugal chamber 4, exit cone 5, material-falling hopper flange 7, material-falling hopper 9, inlet chamber 10 and outlet chamber 11 in this housing 2; Described centrifugal chamber 4 roughly is cone barrel, fixes with respect to described housing 2, and arranges around described needle rotor 3; Described exit cone 5 roughly is cone barrel, is arranged in the described centrifugal chamber 4 and is positioned at the below of described needle rotor 3; Described material-falling hopper flange 7 is fixed with respect to described housing 2, and described exit cone 5 is fixed on the top of described material-falling hopper flange 7, and described material-falling hopper 9 is fixed on the below of described material-falling hopper flange 7; Be formed with air inlet and gas outlet on the described housing 2, described inlet chamber 10 extends from 4 tops, centrifugal chamber of air inlet in described housing 2 of described housing 2, and described outlet chamber 11 extends to the gas outlet of described housing 2 from 5 times side spaces of described exit cone; Wherein, the top of the bottom in described centrifugal chamber 4 and described material-falling hopper 9 on the central axial direction in described centrifugal chamber 4 separately.

Preferably, the open top of described material-falling hopper 9 is greater than the bottom opening in described centrifugal chamber 4.

Preferably, the lower sidewall of described housing 2 is provided with elementary blanking port, be provided with the guided plate 14 of inclination in the inner chamber of described housing 2, these guided plate 14 spiral surroundings extend to the described elementary blanking port of described housing 2 along spiral path from the inner chamber top of described housing 2 outside the sidewall in described centrifugal chamber 4.

Also on the other hand, the present invention also provides a kind of seperator, and this seperator comprises housing 2 and essentially coaxially is arranged on needle rotor 3, centrifugal chamber 4, exit cone 5, material-falling hopper flange 7, material-falling hopper 9, inlet chamber 10 and outlet chamber 11 in this housing 2; Described centrifugal chamber 4 roughly is cone barrel, fixes with respect to described housing 2, and arranges around described needle rotor 3; Described exit cone 5 roughly is cone barrel, is arranged in the described centrifugal chamber 4 and is positioned at the below of described needle rotor 3; Described material-falling hopper flange 7 is fixed with respect to described housing 2, and described exit cone 5 is fixed on the top of described material-falling hopper flange 7, and described material-falling hopper 9 is fixed on the below of described material-falling hopper flange 7; Be formed with air inlet and gas outlet on the described housing 2, described inlet chamber 10 extends from 4 tops, centrifugal chamber of air inlet in described housing 2 of described housing 2, and described outlet chamber 11 extends to the gas outlet of described housing 2 from 5 times side spaces of described exit cone; Wherein, be formed with a plurality of arcuate sockets 1021 on the diapire 102 of described inlet chamber 10, this arcuate socket 1021 extends around the central axis in described centrifugal chamber 4.

Preferably, described inlet chamber 10 is arranged at a side of described housing 2, pass through mutually with the inner chamber off-centre of described housing 2 and to be the snail annular, described inlet chamber 10 comprises roof 101, diapire 102 and two sidewalls 103, described diapire 102 to the inner chamber of housing 2 around extension, until surround the sidewall in described centrifugal chamber 4.

Preferably, the top of the bottom in described centrifugal chamber 4 and described material-falling hopper 9 on the central axial direction in described centrifugal chamber 4 separately.

The below describes the course of work of dust removal machine mentioned above.

1, primary separation process

Mixture to be separated (comprising bulky grain, granule and gas) tangentially enters inlet chamber 10 from the admission line on dust removal machine top; form whirlwind; under the effect of inertia and centrifugal force; the gas that centrifugal force is less and granule mixture are positioned at the center; the bulky grain that centrifugal force is larger then is positioned at periphery, thereby realizes primary separation.Bulky grain is deposited under Action of Gravity Field on the snail ring of inlet chamber 10 diapires 102, and the hole on the snail ring is blocked by baffle plate at this moment, thereby bulky grain is gathered on this snail ring.During discharging, this baffle plate is removed, isolated bulky grain falls into the periphery of housing 2 inner chambers by the arcuate socket 1021 on the snail ring, is deposited at last the bottom of housing 2, and the elementary blanking port by housing 2 bottoms enters the first collection ash can 13 through elementary material blanking tube 12.

In this primary separation process, above-mentioned dust removal machine advantage structurally comprises:

(2), because the diapire 102 of inlet chamber 10 is lower than the roof certain distance in centrifugal chamber 4, therefore make the bulky grain of the High Rotation Speed of separating in infall process, reduce rotary speed, the bulky grain of separating is densification progressively if having time, can accumulate on the diapire 102 of inlet chamber 10, flow in the centrifugal chamber 4 but be unlikely to enter, thereby also can reduce bulky grain to the wearing and tearing in centrifugal chamber 4.

(3), the hole on the snail ring is arcuate socket 1021, arcuate socket 1021 is compared with existing circular hole and is had the following advantages.The aperture of circular hole can not be too large (comparing with the size of snail ring), so the delay area between the circular hole is larger, thereby also has more bulky grain can be trapped on the snail ring between the circular hole, is difficult to fall into the periphery of housing 2 inner chambers.The arc radius of arcuate socket 1021 then can be large (even can be suitable with the size of snail ring), so the delay area between the arcuate socket 1021 is then less, thereby only has a small amount of bulky grain to be trapped on the snail ring between the arcuate socket 1021.Because bulky grain major part under centrifugal action is gathered in the position near the outer peripheral edges of snail ring, and arcuate socket 1021 can be pressed close to the outer peripheral edges setting of snail ring, thereby further impels most of bulky grain to waltz through the periphery that arcuate socket 1021 falls into housing 2 inner chambers.

(4), owing to be provided with the guided plate 14 of inclination in the inner chamber of housing 2, the bulky grain that therefore falls in the inner chamber of housing 2 can slide to elementary blanking port along guided plate 14, thereby accelerates the velocity of discharge of bulky grain thing.

2, the second-order separation process

The gas that is positioned at the center of separating in primary separation process and short grained mixture enter centrifugal chamber 4, under needle rotor 3 High Rotation Speeds drive, and High Rotation Speed thereupon, thus mixture is separated into granule and gas under centrifugal action.On the one hand, granule in the mixture (dust granule) is applied in larger centrifugal force, so that granule carries out outwards downward centrifugal motion, cause dust granule to arrive on the sidewall in centrifugal chamber 4, so dust granule moves downward along centrifugal chamber 4 sidewalls, fall in the material-falling hopper 9, thereby be disposed in the second collection ash can 15.On the other hand, the centrifugal force that the gas of relative clean is subject to is less, therefore enters the cavity center in centrifugal chamber 4, forms downward strong eddy flow.When arriving 4 bottom, centrifugal chamber, enter exit cone 5 inside, continue to do high speed circumnutation (effect at exit cone 5 and stem stem 6 is to reduce turbulent flow so that gas forms more regular eddy flow) around stem stem 6, discharge by outlet chamber 11 and outlet pipe at last.

It more than is the second-order separation process of dry dust removal mode.If as indicated above, dust removal machine also is provided with liquid-jet device, then can adopt preferred semi-wet dedusting method to carry out above-mentioned the second-order separation process.That is to say, after gas and short grained mixture enter centrifugal chamber 4, atomizer 17 ejection atomizing liquid grains (for example water), thus granule can be assembled liquid grain surface, so that particle increases, therefore can reduce it by the possibility of turbulent perturbation.

In this second-order separation process, above-mentioned dust removal machine advantage structurally comprises:

Below describe by reference to the accompanying drawings preferred embodiment of the present invention in detail; but; the present invention is not limited to the detail in the above-mentioned embodiment; in technical conceive scope of the present invention; can carry out multiple simple variant to technical scheme of the present invention, these simple variant all belong to protection scope of the present invention.

Need to prove that in addition each the concrete technical characterictic described in the above-mentioned specific embodiment in reconcilable situation, can make up by any suitable mode.For fear of unnecessary repetition, the present invention is to the no longer separately explanation of various possible combinations.

In addition, also can carry out any combination between the various embodiment of the present invention, as long as it is without prejudice to thought of the present invention, it should be considered as content disclosed in this invention equally.

Claims

1. seperator, this seperator comprise housing (2) and essentially coaxially are arranged on needle rotor (3), centrifugal chamber (4), exit cone (5), material-falling hopper flange (7), material-falling hopper (9), inlet chamber (10) and outlet chamber (11) in this housing (2); Described centrifugal chamber (4) roughly is cone barrel, and arranges around described needle rotor (3); Described exit cone (5) roughly is cone barrel, is arranged in the described centrifugal chamber (4) and is positioned at the below of described needle rotor (3); Described material-falling hopper flange (7) is fixing with respect to described housing (2), and described centrifugal chamber (4) and exit cone (5) are fixed on the top of described material-falling hopper flange (7), and described material-falling hopper (9) is fixed on the below of described material-falling hopper flange (7); Described housing is formed with air inlet and gas outlet on (2), described inlet chamber (10) extends in described housing (2) from the air inlet of described housing (2), and described outlet chamber (11) extends to the gas outlet of described housing (2) from the lower side space of described exit cone (5); It is characterized in that, be formed with a plurality of holes on the sidewall in described centrifugal chamber (4).

2. seperator according to claim 1 is characterized in that, described a plurality of holes are the cylindrical void (41) that intermittently distributes ringwise.

3. seperator according to claim 1 is characterized in that, described a plurality of holes are formed at the bottom section of the sidewall in described centrifugal chamber (4).

4. seperator according to claim 1, it is characterized in that, described material-falling hopper flange (7) comprises the first annulus (71), the second annulus (72) and a plurality of floor (73), the radius of described the first annulus (71) is less than the radius of the second annulus (72), and described floor (73) radially is connected between described the first annulus (71) and the second annulus (72).

5. seperator according to claim 4 is characterized in that, the bottom in described centrifugal chamber (4) is fixed on described the second annulus (72), and described exit cone (5) is fixed on described the first annulus (71).

6. seperator according to claim 4, it is characterized in that, a plurality of floors (73) below of described material-falling hopper flange (7) is provided with a plurality of blades (94), and this blade (94) roughly is the tabular of inclination, and incline direction is consistent with the interior flow rotation direction in described centrifugal chamber (4).

7. seperator according to claim 6 is characterized in that, described a plurality of blades (94) connect by annular slab (95), the first annulus (71) arranged concentric of this annular slab (95) and described material-falling hopper flange (7).

8. seperator according to claim 7 is characterized in that, this seperator comprises a plurality of described annular slab (95) that diameter is different.

9. seperator according to claim 4 is characterized in that, described material-falling hopper flange (7) top is coated with annular oriffice (8), and this annular oriffice (8) comprises the plate body of annular, is formed with a plurality of holes on this plate body.

10. seperator according to claim 9 is characterized in that, described annular oriffice (8) covers first annulus (71) of described material-falling hopper flange (7) and the space between the second annulus (72) at least.

11. seperator according to claim 1 is characterized in that, described exit cone (5) surrounds hollow cavity by sidewall, and is formed with a plurality of holes (51) on the sidewall of this exit cone (5).

12. seperator according to claim 11 is characterized in that, the described a plurality of holes (51) that form on the sidewall of described exit cone (5) are distributed in the upper area of this sidewall.

13. seperator according to claim 1 is characterized in that, the roof of described outlet chamber (11) is positioned at the below of described material-falling hopper flange (7), and with described material-falling hopper flange (7) separately.

14. described seperator according to claim 1, it is characterized in that, this seperator also comprises the ring comb (19) of arranging around described centrifugal chamber (2), this ring comb (19) comprise that many ring comb bars from from the top cover of described housing (2) to downward-extension, described ring are combed and be provided with arc filter screen (20) on the outer peripheral face of close described inlet chamber (10) of (19).

15. seperator according to claim 1, it is characterized in that, this seperator also comprises the stem stem (6) that is arranged in the described exit cone (5), this stem stem (6) extends through described outlet chamber (11) and described exit cone (5) with the coaxial setting of described exit cone (5), described stem stem (6).

16. the described seperator of any one in 15 is characterized in that described seperator is dust removal machine according to claim 1.

17. a wind sorting system is characterized in that, this wind sorting system comprises the described seperator of any one in the claim 1 to 16.