CN201370068Y - Drying apparatus with a multiple impeller structure - Google Patents
Drying apparatus with a multiple impeller structure Download PDFInfo
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- CN201370068Y CN201370068Y CN200920066941U CN200920066941U CN201370068Y CN 201370068 Y CN201370068 Y CN 201370068Y CN 200920066941 U CN200920066941 U CN 200920066941U CN 200920066941 U CN200920066941 U CN 200920066941U CN 201370068 Y CN201370068 Y CN 201370068Y
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Abstract
The utility model discloses a drying apparatus with a multiple-impeller structure. The device comprises a casing, a rotating shaft device, an impeller rotating device and an impeller assembly. The rotating device is a vertical, hollow cylinder structure and comprises an upper rotating shaft connected with the impeller rotating device, a lower rotating shaft connected with the impeller assembly and a sealing device positioned therebetween. The impeller rotating device is a group of impellers regarding the rotating shaft as axle center and comprises a gradual change impeller assembly positioned inside a first conical part and a positive/reverse impeller assembly positioned inside a drying chamber. And the rotating shaft device, via a gearing, drives the impellers of the first impeller assembly and the second impeller assembly in the impeller assemblies to implement multidirectional rotation.
Description
Technical field
The utility model relates to a kind of drying plant, particularly a kind of drying plant with multi-impeller structure.
Background technology
In the reconstituted rice process, need dry cooling to the reconstituted rice particle after the extruding cutting.Yet the reconstituted rice particle water content after the extruding cutting is higher, temperature is higher, starch component wherein is under the big condition of temperature high humility, the gelatinization effect can take place, and makes the outer surface of reconstituted rice particle have higher viscosity, this also caused between the reconstituted rice particle to be stained with sticking degree bigger.
For the drying of solid particle material, often adopt tower drier, drum dryer etc., under the convection current or following current effect of hot-air, the moisture of solid particle material is taken away, thereby be dried.Yet because reconstituted rice particle outer surface has viscosity higher,, will very easily be stained with the group of sticking between the reconstituted rice particle, block drying device in case adopt baroque tower drying device to carry out large batch of drying.Be stained with coherent particle simultaneously and also can bring the situation of uneven drying.
Because the reconstituted rice water content is higher, in dry run, as carrying out drying fast, when reaching the water content requirement, the outer surface of reconstituted rice particle produces the crackle of be full of cracks through regular meeting.This is because when adopting heated-air drying in the dry run, hot-air is taken away the water of particle surface rapidly, and that the water of granule interior is not easy is volatilized, thereby make particle surface different with the evaporation rate of the water of inside, when the water content of granule interior reached requirement, particle surface was but because dehydration too much produces be full of cracks.Another causes the reason of above-mentioned situation to be, dry process is fierce too rapidly, there is not time enough to be diffused into particle surface by the water of granule interior, remedy surperficial different and water content difference that bring with the internal water evaporation rate, make granule interior and the surface the water content balance, avoid surface checking.
Simultaneously in the reconstituted rice dry run, because surface and inner water content inequality, even if dried particle surface is be full of cracks not, yet after placing a period of time, still can chap, and the situation of this water content inequality also caused boiling in the process in reconstituted rice, and the reconstituted rice particle is very easily damaged, causes nutriment that reconstituted rice adds etc. to run off along with water.
Yet existing drying device and method can't solve that reconstituted rice is intergranular is stained with sticking situation, and it is uneven and produce the situation of be full of cracks also can't to solve the volatilization of particle surface and internal moisture.
Chinese patent application 200510017417.X discloses a kind of drying means and dryer group thereof of high moisture material.This method is placed on high moisture material rapid draing in the rotary air-drying machine earlier then and continues drying in the fluid bed dryer with the lower particle of water content that obtains, obtain product.Though this method resolved into for two steps with dry run, avoid carrying out the too fast situation of high temperature drying dehydration always, yet how to avoid being stained with stickingly between the material particles, how to avoid high viscosity particulates plug drying device, how above-mentioned particle is carried out even drying, this patent application still just fails to solve.
Chinese patent application 200710023923.9,200510043078.2 and 200610160006.0 discloses a kind of micro-wave vacuum equipment.This equipment adopts microwave and vacuum equipment that materials inside is carried out drying.Because microwave drying, the material that is dried can carry out drying internally, and inner with surperficial water evaporation rate is identical, thereby can avoid the situation of dehydration inequality.Be stained with stickingly yet this equipment can't solve between granule materials, and can't carry out drying for large batch of material, dry speed is slow, cost is higher.
PCT International Application PCT DE2006/000639 discloses a kind of drying device with demarcation strip, and korean patent application KR10-2006-0095243 also discloses a kind of air drier with compartment of some supporting plates formation simultaneously.Though above-mentioned patent application is separated into some parts by elements such as demarcation strips with material, carry out drying then, can less particle and particle between the situation of uneven drying, yet above-mentioned patent application can't solve the problem for its inside and outside dehydration inequality of particle, also can't avoid being stained with between particle sticking.
Chinese patent application 200710133825.0 discloses a kind of rotary drying machine.This dryer has the X-shaped lifting blade, material can be thrown repeatedly to fall, and makes the holdup time of material in dryer increase and makes material disperse, thereby allow between the material evenly dry.Yet this patent application still can't solve the situation of a granule interior and surperficial dehydration inequality.
Chinese patent application 200610062685.8 discloses a kind of drying machine.This drying machine is a kind of drying box, adopts the heating evaporation drying early stage, and the later stage is adopted the frequency electromagnetic waves heating, so that quick integral heating from inside to outside, and not damaged drying objects.Yet this device can't be avoided intergranular and be stained with stickingly, and adopts frequency electromagnetic waves to heat, and can't carry out the drying of a large amount of materials.
Chinese patent application 200410068779.7 based on Japanese patent application JP1919/2004 and JP53002/2004 discloses a kind of resin pellet dryer.But the purpose of this application is to provide a kind of drying device that prevents a mutual adhesion and efficient drying granule.This device is imported the pipeline that many inside have feeding screw with granule, carries out heat drying in pipeline, and utilizes the stirring action of feeding screw at pipe interior, disperses the granule that adheres to mutually.Yet for the big granule of surface viscosity, pipeline of the present utility model is blocked easily.This device construction complexity simultaneously can't be carried out the drying of material in enormous quantities, and this device also can't be avoided the situation of particle surface and inner dehydration inequality simultaneously.
PCT International Application PCT/JP2003/013360 discloses a kind of drying device of powder and granular material.This device at the built-in electric heater of central authorities, and have a plurality of partition walls be radial outstanding heat conducting and radiating sheet be housed in inside hopper.In the compartment that powder body material to be dried is distributed in and a plurality of partition wall constitutes, by the hot-air drying of convection current.Though powder body material is separated and is some groups, can promote the even drying of material, yet still can't avoid bonding and the inner and surperficial even drying of material between material particles.
Summary of the invention
The utility model discloses a kind of drying plant, comprise housing, turning gear, impeller rotating device, impeller sets.
Described housing is a kind of vertical structure, comprises charging aperture, first tapered portion, hothouse, second tapered portion, discharging opening from top to bottom successively.Described charging aperture is the cylindrical structure of hollow, is positioned at the first tapered portion top and is positioned at the center at this top.Described hothouse is the cylindrical structure of vertical hollow, and its top is provided with first tapered portion, and its bottom is provided with second tapered portion.Described discharging opening is the cylindrical structure of hollow, is positioned at second tapered portion bottom and is positioned at the center at this top.
Described turning gear is the cylindrical structure of vertical hollow, passes charging aperture, first tapered portion, hothouse, second tapered portion and discharging opening successively, and with the concyclic heart of said structure.Described turning gear comprises top rotating shaft that is connected with impeller rotating device and the bottom rotating shaft that is connected with impeller sets, and is positioned at the sealing device in the middle of both.The rotating shaft of described top is provided with gear.Rotating shaft of described top and bottom rotating shaft switched in opposite.
The axle housing of described top rotating shaft is provided with unidirectional hole, and the axocoel that described unidirectional hole and axle housing surround is interconnected, and passes the outside unidirectional discharge of axle housing to allow the axocoel gas inside by unidirectional hole.
It is the impeller in axle center with the rotating shaft that described impeller rotating device is one group, comprises the gradual change impeller sets that is positioned at the first tapered portion inside, the positive and negative impeller sets that is positioned at hothouse inside.Described gradual change impeller sets and positive and negative impeller sets comprise one group of impeller respectively.
Described each impeller comprises 4～16 at interval blades of equating of angles, and the angle that the blade of described each impeller is adjacent staggered angle between the blade of impeller is 10 °～25 °.Described each blade comprises central area and fringe region.Described central area is a sector structure, and its internal diameter equates that with the rotating shaft external diameter its center of circle angle is 10 °～35 °.Described fringe region is a sector structure, and its internal diameter equates that with the external diameter of central area its center of circle angle equates with the center of circle, central area angle.
The thickness of described central area is reducing to deviating from the rotor shaft direction gradually from rotating shaft, and is reduced to fringe region thickness and equates that the thickness of described fringe region is equal everywhere.
Described impeller has a horizontal surface that parallels with horizontal plane, and angle with horizontal plane is 5 °～15 ° a inclined surface.
The diameter of each impeller of described gradual change impeller sets successively decreases from top to bottom successively, and respectively and be provided with the safety clearance of 2mm～22mm between the first adjacent tapered portion inwall.The inclined surface of each impeller of described gradual change impeller sets is positioned at end face, horizontal surface is positioned at the bottom surface.
The equal diameters of each impeller 1035 of described positive and negative impeller sets 1032, and respectively and be provided with the safety clearance of 2mm～22mm between the adjacent hothouse inwall.Described positive and negative impeller sets comprises one group of inclined surface and is positioned at end face, horizontal surface and is positioned at the forward impeller of bottom surface and one group of horizontal surface and is positioned at the reverse impeller that end face, inclined surface are positioned at the bottom surface, and described forward impeller and reverse impeller are spaced apart.
Described impeller sets comprises first impeller sets and second impeller sets.Described first impeller sets comprise first rotating shaft with and a plurality of impellers of go up connecting.Described second impeller sets comprise second rotating shaft with and a plurality of impellers of go up connecting.Described impeller comprises 4～8 blades that equidistantly distribute, and described blade is in same plane or its top and bottom distortion.Each impeller of described first impeller sets equidistantly distributes, and each impeller of described second impeller sets equidistantly distributes, and the described second impeller sets impeller and the first impeller sets impeller are interspersed.
Be respectively equipped with first gear and second gear in described first rotating shaft and second rotating shaft, described gear, first gear, second gear are meshing with each other successively.Described top rotating shaft driven gear rotates, and gear driven first gear rotates, first gear driven, second gear, rotates by the engagement between said gear, and first rotating shaft to be himself being that rotate in the axle center, and second rotating shaft is himself being that rotate in the axle center.Described first rotating shaft and the second rotating shaft switched in opposite.
Described sealing device surrounds the gear of living, first gear and second gear, and said gear is sealed in sealing device inside.Described first rotating shaft is passed sealing device with second rotating shaft and is connected thereon.
On rotating shaft connection of described bottom and the supporting sealing device.Described bottom rotating shaft drives sealing device and rotates, and further drives first rotating shaft and second rotating shaft is that rotate in the axle center with the bottom rotating shaft.
By above-mentioned drying plant and method, can be so that the bigger reconstituted rice extruding of surface viscosity be cut the back particle before entering conventional large-scale drying devices such as tower drying device, each particle is disperseed and is not bondd mutually.
Because bonding mutually between the big particle of surface viscosity is so after entering predrying equipment, be positioned at the impeller rotating device dispersion under the charging aperture.Because impeller rotating device is provided with a plurality of impellers, impeller rotating device can be carried out fast dispersed with stirring fully to the particle that feeds intake in enormous quantities like this, makes that particle adhered to one another is disperseed.Top rotating shaft is simultaneously outwards sprayed high temperature air by the unidirectional hole on it, make the surface of the particle that is scattered here and there by impeller rotating device around it by dry rapidly, reduce its surperficial water content, and like this for the reconstituted rice particle, the reduction of its surperficial water content, can reduce the gelatinization effect of surface starch, avoid bonding thereby reduce viscosity.Herein, if large batch of feeding intake may exist particle to disperse to stir inequality, and just fall under the gravity effect under the situation about not stirring, and its surface can't be by the high temperature air drying.Yet in the utility model, spray the rotating shaft of high temperature air and just in time pass impeller rotating device, and, can fully stir the particle that is distributed in each space of enclosure interior because impeller rotating device has the different impeller of a plurality of diameters.Simultaneously the impeller of impeller rotating device has inclined surface and horizontal surface, thereby makes particle in the stressed difference on individual surface, can scatter with different directions, thereby degree of scatter strengthens.The distribution of the inclined surface of the positive and negative impeller of impeller rotating device and horizontal surface simultaneously is different, can make particle motion under agitation irregular, thereby avoid stirring in the same way the dispersion inequality that the movement of particles rule is brought always.
Impeller rotating device makes particle constantly be kicked up, rotate between each impeller, thereby has increased near the holdup time of particle impeller rotating device, with the high temperature air drying that is sprayed by the top rotating shaft fully.
Disperse and high temperature air dried granules whereabouts through impeller rotating device, in order further to avoid boning once more between the dispersed particle, the impeller unit that is provided with by the drying plant bottom further disperses it.
Utility model content simultaneously is described, and each impeller of first impeller sets is that vertical rotation is done in the axle center with first rotating shaft under the effect of each gear and each rotating shaft, is that the axle center is done and horizontally rotated with the bottom rotating shaft simultaneously.And each impeller of second impeller sets is that vertical rotation is done in the axle center with second rotating shaft under the effect of each gear and each rotating shaft, is that the axle center is done and horizontally rotated with the bottom rotating shaft simultaneously.So first impeller sets and second impeller sets can provide multidirectional rotation, thereby can carry out multidirectional dispersed with stirring to particle.Meanwhile, the switched in opposite of the switched in opposite of top rotating shaft and bottom rotating shaft, first rotating shaft and second rotating shaft, different like this turning to can further promote the degree of scatter of particle, thereby avoids disperseing dried particle to bond once more.
The utility model is a kind of dry apparatus and method that pre-dried adopted before of handling of carrying out, thereby it focuses on the particle that surface viscosity is big and carries out sufficient multidirectional stirring dispersion, and fast drying is carried out on its surface simultaneously, disperse, each other inadherent particle that surface viscosity reduces subsequently once more to obtain.It is emphasized that, described drying is a kind of high temperature drying fast, and its purpose only is to take away the water of particle surface, thereby reduces viscosity, this drying is not to particle drying truly, can not solve the real reduction of granule interior and surface water content.This drying also is the rapid drying of carrying out in the particle dropping process simultaneously, and the time is shorter, to avoid the long too much situation of being brought of surperficial dehydration drying time.The utility model can solve the big particle of surface viscosity in entering dry run such as tower drying device, because obstruction drying device and the even phenomenon of uneven drying brought of bonding mutually.Non-caked mutually through the particle that device of the present utility model was handled owing to surface viscosity reduces, can in dry run subsequently, obtain drying effect preferably.
Description of drawings
Fig. 1 is the overall structure schematic diagram of the predrying system of the utility model.
Fig. 2 is the detailed view of the top rotating shaft of the predrying system of the utility model.
Fig. 3 is the viewgraph of cross-section of the top rotating shaft of the predrying system of the utility model.
Fig. 4 a is the viewgraph of cross-section along the utility model impeller rotating device of the A1-A1 ' of Fig. 1.
Fig. 4 b is the viewgraph of cross-section along the utility model impeller rotating device of the A2-A2 ' of Fig. 1.
Fig. 4 c is the viewgraph of cross-section along the utility model impeller rotating device of the A3-A3 ' of Fig. 1.
Fig. 4 d is the viewgraph of cross-section along the utility model impeller rotating device of the A4-A4 ' of Fig. 1.
Fig. 4 e is the longitudinal profile view of the impeller of the utility model impeller rotating device.
Fig. 5 a is the front view of the impeller of the utility model impeller sets.
Fig. 5 b is the side view of the impeller of the utility model impeller sets.
The specific embodiment
According to claim of the present utility model and the disclosed content of utility model content, the technical solution of the utility model is specific as follows described.
Embodiment one:
A kind of drying plant comprises as the lower part:
According to Fig. 1:
A kind of drying plant comprises housing 101, turning gear 102, impeller rotating device 103, impeller sets 104.
Described housing 101 is a kind of vertical structures, comprises charging aperture 1011, first tapered portion 1012, hothouse 1013, second tapered portion 1014, discharging opening 1015 from top to bottom successively.Described charging aperture 1011 is cylindrical structures of hollow, is positioned at first tapered portion, 1012 tops and is positioned at the center at this top.
Described hothouse 1013 is cylindrical structures of vertical hollow, and its top is provided with first tapered portion 1012, and its bottom is provided with second tapered portion 1014.Described discharging opening 1015 is cylindrical structures of hollow, is positioned at second tapered portion, 1014 bottoms and is positioned at the center at this top.
According to Fig. 1:
Described turning gear 102 is cylindrical structures of vertical hollow, passes charging aperture 1011, first tapered portion 1012, hothouse 1013, second tapered portion 1014 and discharging opening 1015 successively, and with the concyclic heart of said structure.Described turning gear 102 comprises the top rotating shaft 1024 that is connected with impeller rotating device 103 and is connected with the bottom rotating shaft 1025 of impeller sets 104, and is positioned at the sealing device 1026 in the middle of both.Described top rotating shaft 1024 is provided with gear 1027.Described top rotating shaft 1024 and bottom rotating shaft 1025 switched in opposite.
According to Fig. 2 and Fig. 3:
The axle housing 1022 of described top rotating shaft 1024 is provided with unidirectional hole 1023, and described unidirectional hole 1023 is interconnected with the axocoel 1021 that axle housing 1022 surrounds, and passes axle housing 1022 outside unidirectional discharges to allow axocoel 1021 gas inside by unidirectional hole 1023.
Industrial check valve commonly used can be adopted in described unidirectional hole.
According to Fig. 1 and Fig. 4 a, 4b, 4c, 4d, 4e:
It is the impeller in axle center with rotating shaft 102 that described impeller rotating device 103 is one group, comprises the gradual change impeller sets 1031 that is positioned at first tapered portion, 1012 inside, the positive and negative impeller sets 1032 that is positioned at hothouse 1013 inside.Described gradual change impeller sets 1031 and positive and negative impeller sets 1032 comprise one group of impeller 1035 respectively.
Described each impeller 1035 comprises 4～16 at interval blades of equating of angle a2, and the blade of described each impeller is adjacent that staggered angle a4 is 10 °～25 ° between the blade of impeller.Described each blade comprises central area 1036 and fringe region 1037.Described central area 1036 is sector structures, and its internal diameter equates that with rotating shaft 102 external diameters its center of circle angle a1 is 10 °～35 °.Described fringe region 1037 is sector structures, and its internal diameter equates that with the external diameter of central area 1036 its center of circle angle equates with central area 1036 center of circle angles.
According to Fig. 1 and Fig. 4 a, 4e:
The thickness of described central area 1036 is reducing to deviating from rotating shaft 102 directions gradually from rotating shaft 102, and is reduced to fringe region 1037 thickness and equates that the thickness of described fringe region 1037 is equal everywhere.
It is 5 °～15 ° inclined surface 10352 that described impeller 1035 has 10351, one angle a3 with horizontal plane of a horizontal surface that parallels with horizontal plane.
The diameter of each impeller 1035 of described gradual change impeller sets 1031 successively decreases from top to bottom successively, and respectively and be provided with the safety clearance of 2mm～22mm between adjacent first tapered portion, 1012 inwalls.The inclined surface 10352 of each impeller 1035 of described gradual change impeller sets 1031 is positioned at end face, horizontal surface 10351 is positioned at the bottom surface.
The equal diameters of each impeller 1035 of described positive and negative impeller sets 1032, and respectively and be provided with the safety clearance of 2mm～22mm between adjacent hothouse 1013 inwalls.Described positive and negative impeller sets 1032 comprises one group of inclined surface 10352 and is positioned at end face, horizontal surface 10351 and is positioned at the forward impeller of bottom surface and one group of horizontal surface 10351 and is positioned at the reverse impeller that end face, inclined surface 10352 are positioned at the bottom surface, and described forward impeller and reverse impeller are spaced apart.
According to Fig. 1 and Fig. 5 a, 5b:
Described impeller sets 104 comprises first impeller sets 1041 and second impeller sets 1042.Described first impeller sets 1041 comprise first rotating shaft 1043 with and a plurality of impellers 1047 of go up connecting.Described second impeller sets 1042 comprise second rotating shaft 1044 with and a plurality of impellers 1047 of go up connecting.Described impeller 1047 comprises 4～8 blades 1047 that equidistantly distribute, and described blade 1047 is in same plane or its top and bottom distortion.Each impeller 1047 of described first impeller sets 1041 equidistantly distributes, and each impeller 1047 of described second impeller sets 1042 equidistantly distributes, and described second impeller sets impeller 1047 and first impeller sets, 1041 impellers 1047 are interspersed.
Be respectively equipped with first gear 1045 and second gear 1046 in described first rotating shaft 1043 and second rotating shaft 1044, described gear 1027, first gear 1045, second gear 1046 are meshing with each other successively.Rotating shaft 1024 driven gears 1027 in described top rotate, gear 1027 drives 1045 rotations of first gear, first gear 1045 drives second gear 1046, rotate by the engagement between said gear, first rotating shaft 1043 to be himself being that rotate in the axle center, and second rotating shaft 1044 is himself being that rotate in the axle center.Described first rotating shaft 1043 and second rotating shaft, 1044 switched in opposite.
Described sealing device 1026 surround the gear of living 1027, first gear 1045 and second gear 1046, and said gear is sealed in sealing device 1026 inside.Described first rotating shaft 1043 is passed sealing device 1026 with second rotating shaft 1044 and is connected thereon.
On described bottom rotating shaft 1025 connections and the supporting sealing device 1026.Described bottom rotating shaft 1025 drives sealing devices 1026 and rotates, and further drives first rotating shaft 1043 and second rotating shaft 1044 is that rotate in the axle center with bottom rotating shaft 1025.
Adopt drying plant to carry out pre-dried process and comprise following steps:
According to Fig. 1:
Step 11: from charging aperture 1011 input material particles, described material particles enters first tapered portion 1012 under the gravity effect.
According to Fig. 1, Fig. 4 a, 4b, 4c, 4d, 4e:
Step 12: top rotating shaft 1024 drives impeller rotating device 103 rotations that connect on it, each impeller of this impeller rotating device 103 is in the process of rotation, with being distributed in the material particles dispersion of first tapered portion 1012 and whereabouts and kicking up, make material particles be well dispersed in hothouse 1013 inside.
According to Fig. 1, Fig. 2 and Fig. 3:
Step 13: the gas that input has uniform temperature humidity in axocoel 1021, the unidirectional hole 1023 that this gas passes on the axle housing 1022 outwards sprays, mix mutually with the material particles that are dispersed in hothouse 1013 inside and kicked up, make material particles under the effect of this gas, its surface is by rapidly dry, with avoid between material particles be stained with sticking.
According to Fig. 1:
Step 14: the gear 1027 that top rotating shaft 1024 drives on it is that rotate in the axle center with top rotating shaft 1024, and gear 1027 drives 1045 rotations of first gear, first gear 1045 drives second gear 1046 and rotates.
The rotation of first gear 1045 further drives first rotating shaft 1043 himself be that rotate in the axle center, the rotation of second gear 1046 further drive second rotating shaft 1044 himself being that rotate in the axle center, and switched in opposite.
Bottom rotating shaft 1025 to be rotating with the direction of top rotating shaft 1024 switched in opposite, and to drive sealing device 1025, first rotating shaft 1043 and second rotating shaft 1044 successively be that rotate in the axle center with bottom rotating shaft 1025.
Step 15: the impeller 1047 that first rotating shaft 1043 drives on it is that rotate in the axle center with first rotating shaft 1043, and impeller 1047 is realized multidirectional rotation along with first rotating shaft 1043 is that rotate in the axle center with bottom rotating shaft 1025 simultaneously.
The impeller 1047 that second rotating shaft 1044 drives on it is that rotate in the axle center with second rotating shaft 1044, and impeller 1047 is realized multidirectional rotation along with second rotating shaft 1044 is that rotate in the axle center with bottom rotating shaft 1025 simultaneously.
According to Fig. 1, Fig. 5 a, 5b:
Step 16: the material particles that passes impeller rotating device 103 whereabouts is further disperseed under the multidirectional rotation of each impeller 1047 of first impeller sets 1041 and second impeller sets 1042 is stirred, to avoid intergranular bonding.
Step 17: the material particles that passes first impeller sets 1041 and second impeller sets 1042 is assembled in second tapered portion, 1014 bottoms, and by discharging opening 1015 outputs.
Embodiment two:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 4 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 34 °.
The inclined surface 10352 of described impeller 1035 is 14 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 24 ° between the blade of impeller.
Be provided with the safety clearance of 3mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment three:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 4 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 32 °.
The inclined surface 10352 of described impeller 1035 is 13 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 22 ° between the blade of impeller.
Be provided with the safety clearance of 5mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment four:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 8 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 29 °.
The inclined surface 10352 of described impeller 1035 is 12 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 19 ° between the blade of impeller.
Be provided with the safety clearance of 7mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment five:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 8 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 26 °.
The inclined surface 10352 of described impeller 1035 is 11 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 19 ° between the blade of impeller.
Be provided with the safety clearance of 9mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment six:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 9 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 23 °.
The inclined surface 10352 of described impeller 1035 is 10 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 17 ° between the blade of impeller.
Be provided with the safety clearance of 11mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment seven:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 9 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 20 °.
The inclined surface 10352 of described impeller 1035 is 9 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 17 ° between the blade of impeller.
Be provided with the safety clearance of 13mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment eight:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 12 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 17 °.
The inclined surface 10352 of described impeller 1035 is 8 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 15 ° between the blade of impeller.
Be provided with the safety clearance of 15mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment nine:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 12 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 14 °.
The inclined surface 10352 of described impeller 1035 is 7 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 15 ° between the blade of impeller.
Be provided with the safety clearance of 17mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment ten:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 16 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 12 °.
The inclined surface 10352 of described impeller 1035 is 6 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 13 ° between the blade of impeller.
Be provided with the safety clearance of 19mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Embodiment 11:
Adopt following technical parameter to improve embodiment one:
Each impeller 1035 of described impeller rotating device 103 comprises 16 blades.
The center of circle angle a1 of the central area 1036 of described impeller 1035 is 11 °.
The inclined surface 10352 of described impeller 1035 is 5 ° with the angle a3 of horizontal plane.
The blade of described each impeller is adjacent that staggered angle a4 is 12 ° between the blade of impeller.
Be provided with the safety clearance of 20mm between described impeller 1035 and adjacent first tapered portion, 1012 inwalls or the hothouse 1013.
Claims (10)
1, a kind of drying plant with multi-impeller structure is characterized in that, comprises housing (101), turning gear (102), impeller rotating device (103), impeller sets (104);
Described turning gear (102) comprises top rotating shaft (1024) that is connected with impeller rotating device (103) and the bottom rotating shaft (1025) that is connected with impeller sets (104), and is positioned at the sealing device (1026) in the middle of both;
Described impeller rotating device (103) is made up of the impeller that with rotating shaft (102) is the axle center;
Described housing (101) is a kind of vertical structure, comprises charging aperture (1011), first tapered portion (1012), hothouse (1013), second tapered portion (1014), discharging opening (1015) from top to bottom successively;
Described charging aperture (1011) is the cylindrical structure of hollow, is positioned at first tapered portion (1012) top and is positioned at the center at this top;
Described hothouse (1013) is the cylindrical structure of vertical hollow, and its top is provided with first tapered portion (1012), and its bottom is provided with second tapered portion (1014);
Described discharging opening (1015) is the cylindrical structure of hollow, is positioned at second tapered portion (1014) bottom and is positioned at the center at this top;
Described turning gear (102) is the cylindrical structure of vertical hollow, passes charging aperture (1011), first tapered portion (1012), hothouse (1013), second tapered portion (1014) and discharging opening (1015) successively, and with the concyclic heart of said structure.
2, a kind of drying plant with multi-impeller structure as claimed in claim 1, it is characterized in that, it is the impeller in axle center with rotating shaft (102) that described impeller rotating device (103) is one group, comprises the positive and negative impeller sets (1032) that is positioned at the inner gradual change impeller sets (1031) of first tapered portion (1012), is positioned at hothouse (1013) inside;
Described gradual change impeller sets (1031) and positive and negative impeller sets (1032) comprise one group of impeller (1035) respectively; Described each impeller (1035) comprises 4～16 at interval blades of equating of angles, and the angle that the blade of described each impeller is adjacent staggered angle between the blade of impeller is 10 °～25 °;
Described each blade comprises central area (1036) and fringe region (1037);
Described central area (1036) is a sector structure, and its internal diameter equates that with rotating shaft (102) external diameter its center of circle angle is 10 °～35 °;
Described fringe region (1037) is a sector structure, and its internal diameter equates that with the external diameter of central area (1036) its center of circle angle equates with the center of circle, central area (1036) angle.
3, a kind of drying plant with multi-impeller structure as claimed in claim 2, it is characterized in that, the thickness of described central area (1036) is reducing to deviating from rotating shaft (102) direction gradually from rotating shaft (102), and be reduced to fringe region (1037) thickness and equate, the thickness of described fringe region (1037) equates everywhere;
Described impeller (1035) has a horizontal surface that parallels with horizontal plane (10351), and angle with horizontal plane is 5 °～15 ° a inclined surface (10352).
4, a kind of drying plant with multi-impeller structure as claimed in claim 3, it is characterized in that, the diameter of each impeller (1035) of described gradual change impeller sets (1031) successively decreases from top to bottom successively, and respectively and be provided with the safety clearance of 2mm～22mm between adjacent first tapered portion (1012) inwall;
The inclined surface (10352) of each impeller (1035) of described gradual change impeller sets (1031) is positioned at end face, horizontal surface (10351) is positioned at the bottom surface.
5, a kind of drying plant with multi-impeller structure as claimed in claim 4, it is characterized in that, the equal diameters of each impeller (1035) of described positive and negative impeller sets (1032), and respectively and be provided with the safety clearance of 2mm～22mm between adjacent hothouse (1013) inwall;
Described positive and negative impeller sets (1032) comprises one group of inclined surface (10352) and is positioned at end face, horizontal surface (10351) and is positioned at the forward impeller of bottom surface and one group of horizontal surface (10351) and is positioned at the reverse impeller that end face, inclined surface (10352) are positioned at the bottom surface, and described forward impeller and reverse impeller are spaced apart.
6, a kind of drying plant with multi-impeller structure as claimed in claim 5, it is characterized in that, the axle housing (1022) of described top rotating shaft (1024) is provided with unidirectional hole (1023), described unidirectional hole (1023) is interconnected with the axocoel (1021) that axle housing (1022) surrounds, and passes the outside unidirectional discharge of axle housing (1022) to allow axocoel (1021) gas inside by unidirectional hole (1023);
Described top rotating shaft (1024) is provided with gear (1027);
Described top rotating shaft (1024) and bottom rotating shaft (1025) switched in opposite.
7, a kind of drying plant with multi-impeller structure as claimed in claim 6 is characterized in that, described impeller sets (104) comprises first impeller sets (1041) and second impeller sets (1042);
Described first impeller sets (1041) comprise first rotating shaft (1043) with and a plurality of impellers (1047) of go up connecting;
Described second impeller sets (1042) comprise second rotating shaft (1044) with and a plurality of impellers (1047) of go up connecting;
Described impeller (1047) comprises 4～8 blades (1047) that equidistantly distribute, and described blade (1047) is in same plane or its top and bottom distortion.
8, a kind of drying plant with multi-impeller structure as claimed in claim 7, it is characterized in that, each impeller (1047) of described first impeller sets (1041) equidistantly distributes, each impeller (1047) of described second impeller sets (1042) equidistantly distributes, and the described second impeller sets impeller (1047) is interspersed with first impeller sets (1041) impeller (1047).
9, a kind of drying plant with multi-impeller structure as claimed in claim 8, it is characterized in that, be respectively equipped with first gear (1045) and second gear (1046) in described first rotating shaft (1043) and second rotating shaft (1044), described gear (1027), first gear (1045), second gear (1046) are meshing with each other successively;
Described top rotating shaft (1024) driven gear (1027) rotates, gear (1027) drives first gear (1045) rotation, first gear (1045) drives second gear (1046), rotate by the engagement between said gear, first rotating shaft (1043) to be himself being that rotate in the axle center, and second rotating shaft (1044) is himself being that rotate in the axle center;
Described first rotating shaft (1043) and second rotating shaft (1044) switched in opposite.
10, a kind of drying plant with multi-impeller structure as claimed in claim 9, it is characterized in that, described sealing device (1026) surround the gear of living (1027), first gear (1045) and second gear (1046), and said gear is sealed in sealing device (1026) inside;
Described first rotating shaft (1043) is passed sealing device (1026) with second rotating shaft (1044) and is connected thereon;
On described bottom rotating shaft (1025) connection and the supporting sealing device (1026);
Described bottom rotating shaft (1025) drives sealing device (1026) and rotates, and further drives first rotating shaft (1043) and second rotating shaft (1044) is that rotate in the axle center with bottom rotating shaft (1025).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920066941U CN201370068Y (en) | 2009-01-15 | 2009-01-15 | Drying apparatus with a multiple impeller structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920066941U CN201370068Y (en) | 2009-01-15 | 2009-01-15 | Drying apparatus with a multiple impeller structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201370068Y true CN201370068Y (en) | 2009-12-30 |
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ID=41496148
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920066941U Expired - Fee Related CN201370068Y (en) | 2009-01-15 | 2009-01-15 | Drying apparatus with a multiple impeller structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201370068Y (en) |
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2009
- 2009-01-15 CN CN200920066941U patent/CN201370068Y/en not_active Expired - Fee Related
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20091230 Termination date: 20110115 |