Wind power sieving apparatus
Technical field:
The present invention relates to a kind of solid particle material that is used to sieve, especially for the wind power sieving apparatus of solid particles such as screening coking coal.
Background technology:
Screening machine is that a kind of method with physics is separated into fine fraction and coarsely graded equipment with solid particle, is widely used in all fields such as metallurgy, chemical industry.Existing screening machine generally includes the electrodynamic type polytypes such as extension set and fluidized bed type screening machine, and wind power sieving apparatus that shake.
Motor-vibro screen formula screening machine is the equipment that generally adopts in the prior art, generally includes the unbalanced motor of finishing reciprocating motion or vibration in order to the drive screen cloth of screen cloth and rotation.This kind screening machine is in screening during solid particle material, is to rely on the reciprocating or vibration of the compass screen surface that tilts that fine grained in the solid particle on the screen cloth is spilt from screen cloth, and will discharges from the outlet on the sieve greater than the particle of mesh size.Though use this kind screening machine screening material efficient higher, but, because the quality of motor own and the volume that are adopted are all bigger, and need be equipped with heavy supporting member and moving parts, so, use this kind screening machine need relate to many equipment and roomy structures, also need more attendant and bigger maintenance cost simultaneously, and when work, can produce very big heat and noise; In addition; adopt the littler solid particle of screen cloth oscillatory type sieve diameter; be subjected to coating of particles and moisture in the material sometimes; and the restriction of viscosity; as easy bundle of the particle that has the tip makes sieve pore blockade on the mesh of screen cloth; and moisture is crossed conference and is made material produce the granulation tendency; making the particle that can be used as screenings originally go up outlet as oversize by sieve because of uniting discharges; even more serious is; the conference of solid particle material viscosity makes compass screen surface knot layer; and then cause screening machine can not normally finish the screening task, so, use the electrodynamic type screening machine can cause maintenance cost to improve and a large amount of production losses.
And the fluidized bed type screening machine comprises the gas distribution grid that has many holes, makes the fluidizing gas by the ejection of gas distribution grid below form fluid bed.This screening machine is to make classification of solid particles by the flow velocity of adjusting the gas that forms fluid bed, thereby solid particle is separated into coarse granule that is trapped in the fluid bed and the required fine grained that leaps out from fluid bed top.Pore stops up and gas distribution grid surface knot layer problem though this kind screening machine can solve, but this screening machine is had relatively high expectations to moisture content of material, as be used to sieve the used coking coal of coke oven, require the water content of coal not surpass 10%, when water content is higher than 10% in the coal, between the coal particle easily in conjunction with and form the bulky grain of bulk, at this moment, even if screening machine can be controlled the air quantity of fluidizing gas or the air quantity adjusting range of broad is arranged, also be difficult to make the bulk coal to be in the fluidisation attitude, it is trapped on the fluid bed, and under the more situation of bulk coal, the phenomenon that causes the fluidisation attitude to stop.
It is exactly a kind of improvement technology that proposes at the problems referred to above that the name of No. 1100112 Granted publications of Chinese patent is called " coking coal hot air blowing grading and moisture controlled coal preparation technology ".This coal preparation technology has disclosed a kind of fluidized bed drying technology, and making coal can be 200 ℃ in temperature--600 ℃ of atmosphere inner dryings and classification.Yet, with regard to regard to the screening machine of coke oven screening coking coal, require screening machine per hour can sieve out granularity 80 millimeters with 500 tons of interior coking coals to thousands of tons of, for the coal that is dried, if its fineness ratio is more even, in certain holdup time, may reach the desired aridity of fluidisation, but, under the big situation of the particle size distribution of coal, the bulky grain thing is because of can not get dry fully being trapped on the gas distribution grid, so it is very high to use this kind screening machine that the pulverizing program is required, and also needs to consume a large amount of heat energy and keep work; Simultaneously, high-temperature gas corrodes the gas distribution grid of fluid bed easily, needs expensive time and expense and change gas distribution grid; In addition, the quality of what and quality of coke oven output depends on the size of coking coal particle to a great extent, be that its particle diameter is more little, the interior coal dust of carbonization chamber of packing into is many more and careful, and its output is high more, and the quality of coke is good more, and this kind coal preparation technology must obtain fine grained by the winding-up mode highly that improves particle, but this mode not only improves energy consumption, but also can reduce output.
Summary of the invention:
The purpose of this invention is to provide and a kind ofly utilize pneumatic power that the mode of free-falling solid particle winding-up is sieved with solution to yield poorly and the wind power sieving apparatus of problem such as energy consumption height.
Wind power sieving apparatus proposed by the invention comprises that the upper end is respectively equipped with feed(raw material)inlet and waste gas outlet, hollow container that the lower end is respectively equipped with coarse granule outlet and fine grained outlet and the distribution device that is installed in the material that is used in this hollow container to receive and disperses to fall into from the feed(raw material)inlet, and be arranged on the air jet system that the hollow container side is used for the material gas jet that distributes to distribution device, described air jet system comprises that one has the housing of air intake and is installed in the interior air distributor that is connected with hollow container of this housing, described air distributor is made of the flat pieces of vertically disposed one group of level or inclination, and each flat pieces is provided with groove along the direction of gas communication.
Described distribution device comprises last distribution device that is installed in the below, feed(raw material)inlet successively and the following distribution device that keeps at a certain distance away with described upward distribution device.Described distribution device down comprises 1 to 6 layer of axially spaced-apart apart from the comb teeth shape sieve of arranging, and the tooth on the adjacent two layers comb teeth shape sieve is arranged along vertical alternating expression, described go up distributing device comprise one group of vertical plate that arrange the lateral separation and be installed in close waste gas outlet one side of vertical plate and lower area to the arc striker plate of opposite side smooth curved.Described distribution device also comprises gravity distribution device that is installed in the distribution device top successively and the bar shaped sieve that is made of the rod member group that keeps at a certain distance away.
The below of described waste gas outlet also is equipped with and is used for the arc deflector that steering current is discharged by predetermined way.
The bottom of described hollow container and between coarse granule outlet and fine grained outlet, the sub-material plate that can sway is installed also.
Wind power sieving apparatus proposed by the invention only adopts a hollow container and installation distribution device within it, and air jet system just can realize the screening task, so the structure of this screening machine and production technology are quite simple, its volume is also very little, has very low cost of manufacture; Simultaneously, when the screening material, distribution device can disperse material and pulverize, and the air jet system utilization directly realizes screening to the material winding-up that disperses and pulverize, not only disposal ability is big for this screening mode, and does not have blockage problem, and moisture content of material and viscosity are not had higher requirement, and then can save the auxiliary device of heated air, its cost is further reduced; In addition, the direction that the direction of air jet system blowing gas and material fall is provided with suitable angle, and it can increase gas-solid phase relative moving speed, and then realizes screening efficiency and screening quality preferably.
Description of drawings:
Accompanying drawing 1 is the surface structure schematic diagram of an embodiment of wind power sieving apparatus;
Accompanying drawing 2 is cross-sectional view of wind power sieving apparatus shown in Figure 1.
The specific embodiment:
Referring to Fig. 1 and Fig. 2, these two accompanying drawings provide the overall appearance structure of an embodiment of wind power sieving apparatus proposed by the invention.This screening machine comprises air jet system 1 and distribution device 2, and hollow container 3 these three parts.
Described hollow container 3 is to be made of rectangular case basically, be provided with a feed(raw material)inlet 31 and waste gas outlet 32 at an upper portion thereof, and large granule outlet 33, and thereunder and near a side of feed(raw material)inlet 31 or air jet system 1 be provided with coarse granule outlet 34, be provided with fine grained outlet 35 at the opposite side of length direction.Waste gas outlet 32 is the parts that are used for the discharge of the gas in 1 spirt hollow container of air jet system 3, because in some occasion, as when sieving coking coal, its needed particle is very little, for the granule that prevents to be sized flows out outside the hollow container 3 with gas, an arc deflector 36 is installed below waste gas outlet 32, the lower area of arc deflector 36 is towards the direction bending of air jet system 1, the gas that air jet system 1 is sprayed arrives the Background Region of arc deflector 36 earlier, and then flows out through waste gas outlet 32 by circuitous mode.The below of coarse granule outlet 34 and fine grained outlet 35 is separately installed with the discharge valve of opening by the weight of material 37, discharge valve 37 is to be made of the moving runner of being with blade, when coarse granule material and fine granular materials respectively when coarse granule outlet 34 and fine grained outlet 35 are fallen, lean on the blade rotation of the gravitation energy of himself with moving runner, thereby material is discharged, and another function of discharge valve 37 is to prevent that outside gas from entering in the hollow container 3.
Side in hollow container 3 and close large granule outlet 33 is equipped with air jet system 1, this air jet system 1 comprises the housing 11 and the air distributor 13 that is connected with hollow container 3 that is installed in this housing 11 that have air intake 12, air distributor 13 is to be used to the gas that disperses and quicken to spray into from air intake 12, it can adopt multiple structure, as adopt structures such as guide vane, and the air distributor 13 that provides in the present embodiment is to constitute in the housing 11 and along vertically disposed one group of flat pieces by being installed in, and each flat pieces is provided with groove 131 along the direction of gas communication.Flat pieces can be along the direction horizontal positioned of air-flow, the placement that also can be inclined upwardly along the direction of air-flow, and tilted-putted flat pieces more helps material is carried out the dusting cover branch.
The distribution device 2 that provides in the present embodiment comprises bar shaped sieve 21, gravity distribution device 22, goes up distribution device 23 and following distribution device 24 these four parts.Wherein, bar shaped sieve 21 is to be made of the rod member group that keeps at a certain distance away and be mounted obliquely within the feed(raw material)inlet 31, and the lower end that makes the rod member group is extended feed(raw material)inlet 31 and is overlapped on the upper edge of large granule outlet 33, after material that coal etc. is sized is in feed(raw material)inlet 31, relatively the particle of super large or other foreign material can be sieved 21 by bar shaped and stop and discharge outside the hollow containers 3 from large granule outlet 33, and thin relatively particle is entered in the hollow container 3; Gravity distribution device 22 is installed in the below of bar shaped sieve 21, it is to be made of blade-carrying the wheel, gravity distribution device 22 has two kinds of functions: the first leans on the gravity of the material self that falls into from feed(raw material)inlet 31 that material is imported in the hollow container 3, it two is to prevent that gas in the hollow container 3 from 31 flowing out from the feed(raw material)inlet, and the particle that is sized is flowed out outside the hollow container 3 with gas; Last distribution device 23 is installed in the below of gravity distribution device 22, it comprises one group of vertical plate 231 that arrange the lateral separation and is installed in vertical plate 231 near waste gas outlet one sides and the lower area arc striker plate 232 to the opposite side smooth curved, the material that last distribution device 23 can fall gravity distribution device 22 scatters basically equably along the perpendicular direction of the gas that is sprayed with air jet system 1, is beneficial to material screening; Following distribution device 24 is installed in the below of distribution device 23, it is to be made of three layers or 1 to 6 layer of comb teeth shape sieve, tooth 241 on the adjacent two layers comb teeth shape sieve is arranged along vertical alternating expression, and make distance between adjacent two rooted teeth in upper strata less than the distance between adjacent two rooted teeth of lower floor, heap to avoid being sized material effectively, following distribution device 24 functions are further dispersed materials, so, it can adopt multiple structure, as adopting screen cloth or cutting plate etc., the following distribution device 24 of these structures all can be finished task of the present invention.
Described distribution device 2 also can directly adopt down distribution device 24 or go up distribution device 23 this single structures, perhaps adopt and go up distribution device 23 and following distribution device 24 structure combining, perhaps adopt gravity distribution device 22 and last distribution device 23 and/or following distribution device 24 structure combining.
The bottom of described hollow container 3 and the section between coarse granule outlet 34 and fine grained outlet 35 are triangular in shape, also being equipped with at the vertex of a triangle position can be around the sub-material plate 39 of axle 38 rotations, rotate along with sub-material plate 39 exports 35 directions to fine grained gradually, the particle that flows out material from fine grained outlet 35 is tapered.The mode that control sub-material plate 39 rotates can adopt manually or mechanical rotation or various ways such as electronic, because these rotating manners can adopt prior art to finish, so, do not provide concrete structure in the accompanying drawing.