CN209238153U - A kind of air dry sand Recognition Applied in Coal Preparation System - Google Patents

Abstract

The utility model discloses a kind of air dry sand Recognition Applied in Coal Preparation System, it is characterized by comprising bodies, separation system, arrange coal measures system, waste stone exhaust system, media processing system, electric-control system, dust pelletizing system, auxiliary system, the separation system, arrange coal measures system, waste stone exhaust system, media processing system is respectively positioned in body, row's coal measures system uses cooperation with spoil layer with the coal cinder layer on separation system respectively with waste stone exhaust system, the discharge gate on discharge gate and waste stone exhaust system on row's coal measures system is respectively communicated with the feed inlet on media processing system, the feed inlet on discharge port connection separation system on the media processing system, the dust pelletizing system dust removal port is connected to body, the feed inlet on discharge port connection separation system in the auxiliary system, the utility model compared with prior art the advantages of be: water law coal separation can be replaced completely With combined type selection by winnowing, coal separation cost is effectively reduced, coal separation efficiency is substantially improved.

Description

A kind of air dry sand Recognition Applied in Coal Preparation System

Technical field

The utility model relates to coal separation technical field, in particular to a kind of air dry sand Recognition Applied in Coal Preparation System.

Background technique

China is big coal country, with the rapid development of coal industry and the continuous improvement of mining mechanization level, raw coal Quality constantly decline, while coal consumers in order to increase economic efficiency and meet environmental protection needs, thus to coal product Quality constantly proposes requirements at the higher level, and not sorted raw coal cannot use, therefore coal separation has become coal production and utilizes process In essential important link.The essence of raw coal separation is the difference using the physicochemical properties of coal and other minerals It is different, the impurity in raw coal, such as spoil troilite are removed with machinery method, and raw coal is divided into the cleaned coal of different quality specification Product.

As coal preparation industry develops, the sorting process of raw coal can be divided into two kinds: wet concentration and dry method choosing, both techniques are all deposited In very big problem drawback.

Wet concentration: before eighties of last century, make a general survey of all coal preparation methods in the whole world all be unable to do without water --- coal separation is in water entirely It carries out in solution, using coal and the granular size difference of spoil and the difference of density, is sorted in the solution, it is most wide General method is jigging, dense media choosing and flotation.Because traditional coal preparation method must be sorted in aqueous solution, cause as Lower problem:

1. coal separation must use water and water consumption, 1 ton of raw coal average water consumption 0.2m is handled³, 3 tons of water are used when most, but The poor of water source has been doomed in the geologic structure in mining area and geographical location, even if on the earth being the ground that the non-coal-producing area also has 1/5 or more Area's serious water shortage, natural water source, which is not able to satisfy coal separation use or artificial water transfer or transports to have abundant water resources by raw coal, locates strange land Sorting is concentrated, it is at high cost and inconvenient.

2. the outflow of coal slime sewage not only causes Coal Loss, it also seriously polluted environment, lead to soil hardening, To reduce a large amount of outlet coal slime sewage, it is necessary to closed water circuit is realized, to realize that closed water circuit must carry out sewage Purified treatment, must set up dedicated sewage purification system equipment thus, at high cost and reduce coal separation efficiency.

3. the moisture in coal seriously affects or even decide the quality index of product, also increase ineffective traffic simultaneously, The wet coal winter transportation of extremely frigid zones also occurs that freezing vehicle rises vehicle phenomenon, for the moisture content for reducing product after choosing, it is necessary to set up dedicated Dewatering machine is dehydrated, but dehydration is only opposite rather than absolute, just current dehydration technique, after dehydration Product still contains certain moisture, is unfavorable for the direct utilization of coal cinder.

4. sorting is not thorough, there is cash in coal, there is coal in cash, because coal and spoil be not bright in assorting room in coal jigging True interface, when separation, are not thorough, and comprehensive dressing effect is no more than 80%, and sorting quality is lower, the dense-medium separation technology in China It starts from 1958, the coal separation process is complex, and equipment, pipeline are prone to wear, and maintains heavy workload, in operation, adjusts The requirement of aspect is more stringent, and the separating effect of heavy-media suspension coal separation is preferable, but it is still puzzlement China's dense medium that the consumption that is situated between is larger One main problem of coal separation, in coal separation production practices, the consumption that is situated between just belongs to fairly good level in 1.5kg/t or so, generally Medium consumption in preparation plant is in 3kg/t or so, and more slightly higher is 5~6kg/t, and it is even higher that some coal preparation plants have then reached 10kg/t.

5. coal preparation technique is many and diverse, a large amount of accessory machinery need to be set up, so as to cause investing to build or being transformed coal preparation plant's investment It is huge, it is easily exactly several ten million yuan or even several hundred million yuan.

Dry method choosing:

First stage, that is, Foundation stage: 1984, China Mining University took the lead in studying dry coal preparation in the world, complete At laboratory basic research, model investigation, the ore dressing for establishing " air dense medium stable state fluidisation " was theoretical, in 1987 " coal-selecting device in dry fluidized " application number was declared in China Intellectual Property Office May 28: 8710105, hereafter, Chinese Mining Industry University sets about implementing the project, carries out industrial test, and the Bai Jiazhuan coal mine in Taiyuan establishes First test in the world Base, but there are the following problems for the device:

1. discharge refuse mode is pushed using scraper plate strength, cause core component frequently by the blocking of the sundries such as spoil, coal slime, damage Badly cisco unity malfunction, it is rear several improved, using other schemes, it is not still able to satisfy normal requirement.

2. the medium used is that granular iron is husky, loss is too big, and several hundred tons are lost every year, on the one hand increases cost waste Resource, high temperature is red-hot when on the other hand these iron sand are mixed in burning in coal is easily damaged boiler.

3. whole cost is excessively high and production efficiency is low, industrial application cannot achieve.

Second stage, that is, exploratory stage: domestic existing combined type dry coal separation technology is also referred to as selection by winnowing, the basic principle is that logical Cross waving or vibrating for bed surface, make raw coal under the entrusting of little particle coal dust, dependent on the effect of external wind-force realize weight point to Flowing.This technology exists as following drawbacks:

1. separating effect is poor: such mode only belongs to " smut buddle " and just develops shaking table point early in China in 1956 Choosing, this technology only in separation by shaking table increases wind-force, slightly modified to separation by shaking table, because coal and spoil are in assorting room In without specific interface, bed surface the more shakes the more real, becomes dead bed, and when separation is not thorough, and comprehensive dressing effect is no more than 75%.

2. the efficiency of separation is low.

3. it is bulky that structure is complicated, cause cost of manufacture big, take up a large area, the volume that 100 ton/hours for the treatment of capacity is super 1000 cubic metres are crossed, causes investment newly-built and that coal preparation plant is transformed huge, is easily exactly millions of or even several ten million yuan.

4. energy consumption is high, the system power that 100 ton/hours for the treatment of capacity needs 300 kilowatts.

5. high production cost, maintenance cost is big.

6. dust is more, environment is polluted.

Phase III, that is, status: the country has scientific worker slightly to change in the scheme by China Mining University before this in 2008 Into: replace virgin metal air distribution plate with the polyethylene panel of gather aperture and blast cap, there are the following problems:

1. blocky and granular spoil still directly falls in vinyon plate surface, carries on as before and pushed using scraper plate strength, meeting Blockage and wear quickly lead to not work normally.

2. manufacturing process is complicated, manufacturing cost is excessively high, and structure is many and diverse and power consumption is huge, leads to coal separation higher cost, Close to wet concentration.

Above each factor cause so far dry coal preparation still can not achieve industrial application.

In conclusion because of existing dry coal preparation technology, there are still many jejune problems, not perfect, only exist in spy The rope trial stage, so cannot promote and apply, at present or based on wet concentration.

The utility model people is further improved perfect, and develops a full set of anhydrous Recognition Applied in Coal Preparation System --- air dry sand coal separation System, thoroughly to solve many drawbacks of traditional coal separation.

Utility model content

The technical problems to be solved in the utility model is to overcome the above technological deficiency, is provided a kind of without water source, coal separation effect Rate height, air dry sand Recognition Applied in Coal Preparation System at low cost.

To achieve the goals above, the technical scheme adopted by the utility model is a kind of air dry sand Recognition Applied in Coal Preparation System, packet Include body, separation system, row coal measures system, waste stone exhaust system, media processing system, electric-control system, dust pelletizing system, auxiliary system, institute It states separation system, row's coal measures system, waste stone exhaust system, media processing system to be respectively positioned in body, row's coal measures system and waste stone exhaust system It uses and cooperates with spoil layer with the coal cinder layer on separation system respectively, on the discharge gate and waste stone exhaust system on row's coal measures system Discharge gate is respectively communicated with the feed inlet on media processing system, on the discharge port connection separation system on the media processing system Feed inlet, the electric-control system respectively with separation system, row coal measures system, waste stone exhaust system, media processing system, dust pelletizing system and Auxiliary system electrical connection, the dust pelletizing system dust removal port are connected to body, and the discharge port in the auxiliary system connects separation system On feed inlet.

The separation system is made of separation chamber, gas chamber, the first surge chamber, the second surge chamber and roots blower, and described point It selects room bottom to be connected to the air inlet on gas chamber and is fixed with pneumatic panel in its connectivity part, heating gas chamber is fixed in the gas chamber The heating net of interior air, the air inlet on the gas chamber is connected to the gas outlet on the first surge chamber, on first surge chamber Air inlet be connected to the gas outlet on the second surge chamber, the outlet air on air inlet and roots blower on second surge chamber Mouth connection.

The pneumatic panel is made of several fixed plates and several air-permeable elastic plates, the fixed plate and air-permeable elastic plate It is fixedly connected, and is alternatively arranged between it, integrally formed with several ventholes in the air-permeable elastic plate.

First surge chamber and the second surge chamber connectivity part are connected with gas flowmeter and flow control valve.

Row's coal measures system is made of rotation axis, row's screen, row's coal channel and motor driver, the rotation axis rotation The upper end of separation chamber is set, and described rotation axis one end and motor driver are sequentially connected, and row's screen is by several It arranges coal bar to constitute, row's coal bar is evenly distributed on rotation axis outer end face, feed inlet and separation chamber on row's coal channel Connection, and it uses cooperation with row's screen.

The motor driver includes first motor and the speed reducer with first motor transmission connection, the speed reducer It is sequentially connected with rotation axis.

The waste stone exhaust system includes spoil screening plant, spoil pushing meanss, the first spoil negative pressure device, spoil suction dress It sets, spoil crushing device and the second spoil negative pressure device, spoil screening plant and spoil pushing meanss use cooperation, spoil promotion Using cooperating, spoil pushing meanss and spoil suction device use cooperation, spoil suction dress for device and the first spoil negative pressure device It sets with spoil crushing device using cooperating, the second spoil negative pressure device and spoil suction device use cooperation.

The spoil screening plant is made of bottom sieve layer and side screen layers, and the bottom sieve layer is fixed in separation chamber, institute The one end for stating side screen layers is fixedly connected with the inner wall of separation chamber, and its other end is fixedly connected with bottom sieve layer, the side screen layers with Have gradient, the bottom sieve layer and side screen layers by bar construction is sieved between bottom sieve layer, there is blanking screen slot between adjacent sieve stick.

The spoil pushing meanss are made of mobile base, mandril and return pin, and the mandril, return pin are separately fixed at Separation chamber two sides of the bottom, the mobile base slide setting in separation chamber, and rotation is provided with swingle in the mobile base, Linkage board is fixedly connected on the swingle, the linkage board is used with mandril and return pin respectively to be cooperated, and linkage board Swingle rotation is driven after stress, discharge refuse pawl is fixedly connected on the swingle, and discharge refuse pawl end is exposed in bottom sieve layer Top.

The first spoil negative pressure device is by the first negative pressure chamber, the first double-gate, the first star of partition baiting valve, the second star Baiting valve, piano wire screen and the first air-introduced machine, feed inlet connection separation chamber and its connectivity part in first negative pressure chamber are located at Bottom sieve layer side end, first negative pressure chamber and separation chamber's connectivity part are provided with the first double-gate, and the partition is fixed at the In one negative pressure chamber, and it forms discharge refuse chamber and row's Jie's chamber, discharge port and the first star on the discharge refuse chamber in the first negative pressure chamber Feed inlet on shape baiting valve is connected to, and the discharge port on Jie's row chamber is connected to the feed inlet on the second star baiting valve, institute It states piano wire screen and is fixed at row's Jie's top of chamber, the feed inlet on the piano wire screen is connected to the first double-gate discharge port, and it is another It is fixedly connected at the top of one end and partition, the air inlet on first air-introduced machine is connected to the first negative pressure chamber, and is connected between it Place is provided with the first magnetic filtering sieve.

The spoil suction device is made of suction tube, feed pipe and mobile device, and the suction tube is located at separation chamber bottom It portion and is fixed in mobile base, and its bottom offers suction hole, on the feed inlet and suction tube on the feed pipe Discharge port connection, and discharge port thereon is connected to the feed inlet on the second spoil negative pressure device, the feed pipe and mobile dress It sets and connects and moved back and forth under the control of mobile device.

The mobile device includes the second motor, ball-screw and attachment base, and the ball-screw is connect with the second motor, Described attachment base one end is connect with ball-screw, and the other end is connect with feed pipe.

The spoil crushing device is made of rotating bar, the first rubble stick and rack gear, and the rotating bar is located in suction tube And be freely rotated in suction tube, the rack gear is fixed at separation chamber bottom, the both ends of the rotating bar and rack-driving Engagement, the first rubble stick are evenly distributed on rotating bar outer end face, and it is broken to be fixedly installed second on the suction inside pipe wall Stone stick, the second rubble stick and the first rubble stick staggeredly cooperate.

The second spoil negative pressure device is drawn by the second negative pressure chamber, the second double-gate, third star baiting valve, hose and second Blower is constituted, and the feed inlet in second negative pressure chamber is connected to the discharge port on the second double-gate, on second double-gate into Material mouth is connected to the discharge port on hose, and the feed inlet on the hose is connected to the discharge port on feed pipe, the third star Feed inlet on shape baiting valve is connected to the second negative pressure chamber, and the feed inlet on discharge port and media processing system thereon connects Logical, second air-introduced machine is connected to the second negative pressure chamber, and connectivity part is provided with the second magnetic filtering sieve between it.

The media processing system slightly takes off device by medium, medium essence takes off device, belt medium-separation device and medium storehouse and constitutes, The medium storehouse is fixed on organism bottom, with row coal measures system connection media processing system, in medium slightly take off device and row Coal measures system using cooperation, media processing system connect with waste stone exhaust system, in medium slightly take off device and waste stone exhaust system use Cooperation, the medium slightly take off the discharge port on device and are connected to the feed inlet on the de- device of medium essence, and the medium essence takes off device On discharge port be connected to the feed inlet on belt medium-separation device, on the discharge port on the belt medium-separation device and medium storehouse Feed inlet is connected to, and the discharge port on the medium storehouse is connected to the feed inlet on separation system.

The medium slightly takes off device, and by first, slightly de- cylinder, outer reinforcement cylinder, aggregate bin, second slightly take off cylinder, interior reinforcement cylinder and spoke Item is constituted, described first slightly de- cylinder rotate setting in body, the described first thick take off offers material hole on cylinder barrel, and its two End is connected to the fixation of outer reinforcement cylinder, and the aggregate bin is fixed at the first slightly de- cylinder bottom, and discharge port and medium thereon Feed inlet connection on the de- device of essence, the interior reinforcement cylinder are fixed in outer reinforcement cylinder by spoke, the interior reinforcement cylinder and the Two slightly take off the fixed connection of cylinder, offer logical material strip on the described second thick de- cylinder barrel and stitch, the discharge port on the described second thick de- cylinder It is connected to the feed inlet on belt medium-separation device with the discharge port on the first thick de- cylinder, the media processing system and discharge refuse system When system connection, feed inlet on the described second thick de- cylinder with the discharge port and the second star baiting valve on the first star baiting valve On discharge port connection, feed inlet and row when the media processing system and row's coal measures system connect, on the described second thick de- cylinder Discharge port connection on coal channel.

The medium essence take off device by the de- pedestal of essence, the first dead axle, roller, first bearing, circular arc frame, the first material transfer cylinder, Discharge barrel and third motor are constituted, and the de- pedestal of essence is fixed in body, and it is de- that first dead axle is fixed at essence On pedestal, the roller is rotatably arranged on the first dead axle by first bearing, and it is located at immediately below aggregate bin, the circular arc Frame is fixed on the first dead axle, and is fixedly installed several permanent magnets thereon, magnetic of the adjacent permanent magnet block at outer surface of cylinder Power is different, and the discharge barrel is fixed on the de- pedestal of essence, and it is ipsilateral with circular arc frame, the discharge port on the discharge barrel with Feed inlet connection on belt medium-separation device, the first material transfer cylinder is fixed on the de- pedestal of essence, and it is located at circular arc frame The underface of end, the discharge port on the first material transfer cylinder are connected to medium storehouse, and the third motor is connect with drum drive.

The belt medium-separation device is by belt de-mediated pedestal, the second dead axle, second bearing, arc magnet ring, driving wheel, driven Wheel, conveyer belt, the second material transfer cylinder and the 4th motor are constituted, and the belt de-mediated pedestal is fixed in body, and described second Dead axle is fixed on belt de-mediated pedestal, and the driving wheel is rotatably arranged on the second dead axle by second bearing, described Arc magnet ring is fixed on the second dead axle, and the inner wall of itself and driving wheel has certain interval, and the driven wheel rotation is set It sets on belt de-mediated pedestal, by transmission V belt translation, the second material transfer cylinder is fixed at for the driving wheel and driven wheel On belt de-mediated pedestal, and its underface for being located at arc magnet ring end, the discharge port on the second material transfer cylinder is connected to medium Storehouse, the 4th motor are connected with capstan drive.

Medium delivery pump is fixedly installed in the body, the feed end on the medium delivery pump is connected to medium storehouse, And discharge port thereon is connected to separation chamber, and level sensor, the medium delivery pump and material are fixedly installed in the separation chamber Level sensor uses cooperation.

The electric-control system is made of control room and control host, and the control host is fixed in control room, institute It is electric with separation system, row's coal measures system, waste stone exhaust system, media processing system, dust pelletizing system and auxiliary system respectively to state control host Connection.

The dust pelletizing system is made of deduster and cleaning shaft, on the suction inlet and cleaning shaft on the deduster Dust mouth is connected to, and the dust mouth on the cleaning shaft is connected to internal body.

The auxiliary system is made of several belt conveyers, and the belt conveyer is respectively and on belt medium-separation device Discharge port and separation chamber on feed inlet using cooperation.

After adopting the above structure, the utility model is compared to the prior art advantageously:

1. entire assorting room carries out in air and dry solid dielectric completely, it is not necessarily to water source, also not needing will be former Sorting is concentrated in coal strange land, even if high and cold arid it is anhydrous it is regional also can normal coal separation on the spot, the requirement to ambient enviroment is extremely low, Its occupied area only has the 1/3 of traditional technology, and occupied area is small, greatly improves the scope of application of sorting, reduces sorting cost.

2. be not related to the dehydration problem after coal separation, also fundamentally solve the problems, such as in terms of sewage discharge pollution environment and The loss of coal caused by cost issues and sewage discharge in terms of the dirty water decontamination handles.

3. raw coal does not only contact water but also further reduced the water content of cleaned coal in assorting room, to both improve The quality index of product, effectively reduces ineffective traffic, rises the sorrow of vehicle there are no the jelly vehicle of extremely frigid zones coal winter transportation.

4. sorting quality is high, bed surface is sufficiently loosely sorted, and is had specific boundary line between cleaned coal and spoil, is completely separated, point Select rate close to 100%.

5. energy consumption very little, safe and environment-friendly, sorting process simplifies, high degree of automation, is not required to manpower participation, significantly The production cost of coal separation is reduced, the sorting cost of raw coal per ton only needs several yuans are more per ton than wet concentration to save dozens of yuan.

6. main machine structure is simple, it is easily installed and production management, manufacturing cost is lower than traditional coal preparation machine, is not required to civil engineering work Journey, a host are exactly a coal preparation plant, be mounted on level land can coal separation, be not required to other auxiliary equipment, under equal conditions 1/2 or more expense can be saved by building or be transformed coal preparation plant.

7. dielectric loss amount is small, when coal burning, does not damage boiler, effectively saving cost.

8. high production efficiency, overall mass is stablized, can round-the-clock continuous work, without frequent maintenance, long service life.

Detailed description of the invention

Fig. 1 is a kind of structural schematic diagram of air dry sand Recognition Applied in Coal Preparation System of the utility model.

Fig. 2 is the structural schematic diagram in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model at separation system.

Fig. 3 is that row's coal measures system shows with right at waste stone exhaust system depending on structure in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model It is intended to.

Fig. 4 is the partial elevational structural schematic diagram in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model at waste stone exhaust system.

Fig. 5 is that medium slightly takes off the structure of device in media processing system in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model Schematic diagram.

Fig. 6 is that medium essence takes off the structure of device in media processing system in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model Schematic diagram.

Fig. 7 is the structure of media processing system inner belt medium-separation device in a kind of air dry sand Recognition Applied in Coal Preparation System of the utility model Schematic diagram.

As shown in the figure: 2, body, 3, separation system, 301, separation chamber, 302, gas chamber, 303, pneumatic panel, 305, first is slow Rush room, the 306, second surge chamber, 307, roots blower, 308, fixed plate, 309, air-permeable elastic plate, 310, heating net, 311, gas Flowmeter body, 312, flow control valve, 4, row's coal measures system, 401, rotation axis, 402, row's screen, 403, row's coal channel, 404, row Coal bar, 405, first motor, 5, waste stone exhaust system, 501, spoil screening plant, 502, spoil pushing meanss, the 503, first spoil are negative Pressure device, 504, spoil suction device, 505, spoil crushing device, the 506, second spoil negative pressure device, 507, bottom sieve layer, 508, side screen layers, 509, sieve stick, 510, mobile base, 511, mandril, 512, return pin, 513, swingle, 514, linkage board, 515, discharge refuse pawl, the 516, first negative pressure chamber, the 517, first double-gate, 518, partition, 519, discharge refuse chamber, 520, row's Jie's chamber, 521, the One star baiting valve, the 522, second star baiting valve, 523, piano wire screen, the 524, first air-introduced machine, the 525, first magnetic filtering sieve, 526, suction tube, 527, suction hole, 528, feed pipe, the 529, second motor, 530, ball-screw, 531, attachment base, 532, turn Lever, 533, gear, 534, rack gear, the 535, first rubble stick, the 536, second rubble stick, the 537, second negative pressure chamber, 538, soft Pipe, the 539, second double-gate, 540, third star baiting valve, the 541, second air-introduced machine, the 542, second magnetic filtering sieve, 543, double-gate Room, the 544, first gate, the 545, second gate, 6, media processing system, 601, medium slightly take off device, 602, the de- dress of medium essence It sets, 603, belt medium-separation device, 604, medium storehouse, 605, first slightly takes off cylinder, 606, material hole, 607, outer reinforcement cylinder, 608, collection Hopper, the 609, second slightly de- cylinder, 610, logical material strip seam, 611, interior reinforcement cylinder, 612, spoke, 613, the de- pedestal of essence, 614, first Dead axle, 615, roller, 616, first bearing, 617, circular arc frame, 618, permanent magnets, 619, discharge barrel, the 620, first material transfer cylinder, 621, third motor, 622, belt de-mediated pedestal, the 623, second dead axle, 624, driving wheel, 625, second bearing, 626, arc magnetic Ring, 627, driven wheel, 628, conveyer belt, the 629, second material transfer cylinder, the 630, the 4th motor, 631, medium delivery pump, 632, material position Sensor, 7, electric-control system, 701, control room, 702, control host, 8, dust pelletizing system, 801, deduster, 9, auxiliary system, 901, belt conveyer.

Specific embodiment

The following describes the utility model in further detail with reference to the accompanying drawings.

A kind of air dry sand Recognition Applied in Coal Preparation System can select a certain number of air dry sand Recognition Applied in Coal Preparation System 1 according to coal separation amount, avoid A whole set of system does excessive idle work, improves coal separation efficiency, including body 2, separation system 3, row's coal measures system 4, waste stone exhaust system 5, Media processing system 6, electric-control system 7, dust pelletizing system 8, auxiliary system 9, the generally steel construction of body 2 have internal each component Support and protective effect well, separation system 3 is for separating coal with spoil, and row's coal measures system 4 is for the coal row after separating Out, the spoil discharge after waste stone exhaust system 5 is used to separate, media processing system 6 for by medium from the mixture of medium and coal It separates and then is again fed in separation system 3 in the mixed material of material or medium and spoil, control system 7 is for whole Automation control, convenient for operation, dust pelletizing system 8 is used to be sucked out and filter out dust for the air with dust in body 2, Prevent dust from damaging to whole intracorporal component and polluting to external environment, auxiliary system 9 is used for the conveying of material, The separation system 3, row's coal measures system 4, waste stone exhaust system 5, media processing system 6 are respectively positioned in body 2, row's coal measures system 4 with Waste stone exhaust system 5 respectively on separation system 3 coal cinder layer and spoil layer using cooperating, the discharge gate on row's coal measures system 4 with Discharge gate on waste stone exhaust system 5 is respectively communicated with the feed inlet on media processing system 6, the discharging on the media processing system 6 Mouthful connection separation system 3 on feed inlet, the electric-control system 7 respectively with separation system 3, row coal measures system 4, waste stone exhaust system 5, be situated between Matter processing system 6, dust pelletizing system 8 and auxiliary system 9 are electrically connected, and 8 dust removal port of dust pelletizing system is connected to body 2, the auxiliary The feed inlet on discharge port connection separation system 3 in system 9.

In order to keep the separating effect of coal and spoil more preferable, further, the separation system 3 is by separation chamber 301, gas chamber 302, the first surge chamber 305, the second surge chamber 306 and roots blower 307 are constituted, and separation chamber 301 is to form fluid as medium The effective carrier of form, 301 bottom of separation chamber are connected to the air inlet on gas chamber 302 and are fixed with distribution in its connectivity part Plate 303, pneumatic panel 303 can guarantee that the air entered in separation chamber 301 is more uniform, are fixed with and add in the gas chamber 302 The heating net 304 of hot gas room air, heating net 304 can guarantee the drying in separation chamber 301, be conducive to the better shape of medium At fluid form, the moisture content on coal cinder surface also can reduce, additionally it is possible to guarantee in extremely frigid zones without preheating all parts i.e. It can work, heating net 310 is fixed in gas chamber 302 with air inlet phase nearby, and 310 wire side of heating net is vertical with airintake direction, adds Heat supply network 310 is made of several heater strips with grid-like distribution, and heater strip heating speed is fast, high-efficient, while also can be selected The similar devices such as heating sheet, the air inlet on the gas chamber 302 are connected to the gas outlet on the first surge chamber 305, and described first Air inlet on surge chamber 305 is connected to the gas outlet on the second surge chamber 306, the air inlet on second surge chamber 306 It is connected to the air outlet on roots blower 307, the compressed air that Lodz blower 307 is blown out enters the first surge chamber 306 and mixes It is even then enter back into the first surge chamber 306 mix, guarantee separation chamber 301 in compressed air it is more uniform, further, institute It states pneumatic panel 303 to be made of several fixed plates 308 and several air-permeable elastic plates 309, the fixed plate 308 and air-permeable elastic Plate 309 is fixedly connected, and is alternatively arranged between it, integrally formed with several ventholes, bullet in the air-permeable elastic plate 309 Property air permeable plate 309 select felt plate, fixed plate 308 selects steel plate, guarantee to improve whole stability while ventilation is uniform, into One step, first surge chamber 305 and 306 connectivity part of the second surge chamber are connected with gas flowmeter 311 and flow control valve 312, whole automation control is improved, monitoring and maintenance are facilitated.

In order to guarantee that the coal after separation is preferably discharged from separation chamber 301, further, row's coal measures unites 4 by turning Moving axis 401, row's screen 402, row's coal channel 403 and motor driver are constituted, and the rotation axis 401 is rotatably arranged on sorting The upper end of room 301, described 401 one end of rotation axis and motor driver are sequentially connected, and row's screen 402 is by several rows Coal bar 404 is constituted, and row's coal bar 404 is evenly distributed on 401 outer end face of rotation axis, the charging on row's coal channel 403 Mouth is connected to separation chamber 301, and it uses with row's screen 402 and cooperates, and further, the motor driver includes first electric Machine 405 and the speed reducer being sequentially connected with first motor 405, the speed reducer and rotation axis 401 are sequentially connected, first motor 405 drive speed reducer rotation, and speed reducer drives rotation axis 401 to rotate, and row's screen 402 in rotation axis 401 rotates with it, and are arranging Under the stirring of screen 402, swim in the coal cinder of dielectric surface from separation chamber 301 by the row's of dialing out to coal channel 403, it is such Mode will not damage pneumatic panel 303, and row's coal is high-efficient, and dielectric loss is small.

In order to guarantee that the spoil after separation is preferably discharged from separation chamber 301, further, the waste stone exhaust system 5 is wrapped It is broken to include spoil screening plant 501, spoil pushing meanss 502, the first spoil negative pressure device 503, spoil suction device 504, spoil Crushing device 505 and the second spoil negative pressure device 506, spoil screening plant 501 and spoil pushing meanss 502 use cooperation, spoil Using cooperating, spoil pushing meanss 502 and spoil suction device 504 are used for pushing meanss 502 and the first spoil negative pressure device 503 Cooperation, spoil suction device 504 and spoil crushing device 505 use cooperation, the second spoil negative pressure device 506 and spoil suction Device 504 is using cooperation, and further, the spoil screening plant 501 is made of bottom sieve layer 507 and side screen layers 508, the bottom Screen layers 507 are fixed in separation chamber 301, and one end of the side screen layers 508 is fixedly connected with the inner wall of separation chamber 301, and Its other end is fixedly connected with bottom sieve layer 507, has gradient, the bottom sieve layer between the side screen layers 508 and bottom sieve layer 507 507 and side screen layers 508 is made of sieve stick 509, it is heavy above medium in spoil with blanking screen slot between adjacent sieve stick 509 When entering to dielectric substrates, biggish spoil can be dropped on bottom sieve layer 507, lesser, and medium bottom can be sunk to from screen slot Layer, spoil is effectively sieved, greatly alleviate follow-up work amount, further, the spoil pushing meanss 502 It is made of mobile base 510, mandril 511 and return pin 512, the mandril 511, return pin 512 are separately fixed at separation chamber 301 Two sides of the bottom, the mobile base 510 slide setting in separation chamber 301, and rotation is provided with rotation in the mobile base 510 Bar 513, is fixedly connected with linkage board 514 on the swingle 513, the linkage board 514 respectively with mandril 511 and return pin 512 using cooperation, and drives swingle 513 to rotate after 514 stress of linkage board, the row of being fixedly connected on the swingle 513 Cash pawl 515,515 end of discharge refuse pawl are exposed on the top of bottom sieve layer 507, to prevent discharge refuse pawl 515 from rotating larger angle, also The limit that positioning baffle is used as discharge refuse pawl 515 should be set, and when work, the movement of mobile base 510 is able to drive the shifting of discharge refuse pawl 515 Dynamic, discharge refuse pawl 515 is abutted with positioning baffle at this time, and to have the function that limit, discharge refuse pawl 515 can push bottom sieve layer 507 to fall The bulky grain spoil that material screen is sewed on is mobile, and bulky grain spoil can be discharged when reaching the outlet of separatory vessel end face spoil；And this When mandril 511 can withstand linkage board 514 and allow its rotate, the rotation of linkage board 514 will drive swingle 513 rotation, swingle 513 rotation will drive discharge refuse pawl 515 and rotate down, and be located at the lower part of bottom sieve layer 507, in this way when mobile base 510 is returned Return can be made more smooth when position；When mobile base 510 returns in situ, return pin 512 can withstand linkage board 514, allow Linkage board 514 drives swingle 513 to rotate backward so that the upper end of discharge refuse pawl 515 returns to the top of bottom sieve layer 507, with into Spoil pushes operation to row next time, and further, the first spoil negative pressure device 503 is by the first negative pressure chamber 516, the first double-gate 517,518 first star baiting valve 521 of partition, the second star baiting valve 522, piano wire screen 523 and the first air-introduced machine 524, it is described Feed inlet connection separation chamber 301 and its connectivity part in first negative pressure chamber 516 are located at 507 side end of bottom sieve layer, and described first Negative pressure chamber 516 and 301 connectivity part of separation chamber are provided with the first double-gate 517, and the partition 518 is fixed at the first negative pressure chamber In 516, and it forms discharge refuse chamber 519 and row's Jie's chamber 520 in the first negative pressure chamber 516, the discharge port on the discharge refuse chamber 519 with Feed inlet on first star baiting valve 521 is connected to, on the discharge port and the second star baiting valve 522 on Jie's row chamber 520 Feed inlet connection, at the top of 523 row of being fixed at Jie's chamber of piano wire screen 520, feed inlet on the piano wire screen 523 and the The connection of one double-gate, 517 discharge port, and be fixedly connected at the top of its other end and partition 518, the air inlet on first air-introduced machine 524 It mouthful is connected to the first negative pressure chamber 516, and connectivity part is provided with the first magnetic filtering sieve 525 between it, when work, the first air-introduced machine Air suction in first negative pressure chamber 516 is formed vacuum by 524 in the first negative pressure chamber 516, and the first negative pressure chamber 516 is in the first double-gate The mixed material sucking for the spoil and medium that mechanism 517 can release spoil moving system 502 when opening, mixed material are first Piano wire screen 523 is first passed through, piano wire screen 523 can pass through medium but can not arbitrarily roll into discharge refuse chamber 520 simultaneously by spoil, spoil By dischargeing subsequent processing in the first star baiting valve 521, medium is fallen in row's Jie's chamber 520 and by the second star blowing Valve 522 is discharged to subsequent processing, and since mixed material can generate dust during exercise, these dusts are entering the first air-introduced machine Before 524 can be filtered in the first magnetic filtering sieve 525, filtered medium with can at immediately be discharged, further, institute It states spoil suction device 504 to be made of suction tube 526, feed pipe 528 and mobile device, the suction tube 526 is located at separation chamber It 301 bottoms and is fixed in mobile base 510, and its bottom offers suction hole 527, the charging on the feed pipe 528 Mouth is connected to the discharge port on suction tube 526, and the feed inlet on discharge port and the second spoil negative pressure device 506 thereon connects Logical, the feed pipe 528 connect with mobile device and moves back and forth under the control of mobile device, further, the movement Device includes the second motor 529, ball-screw 530 and attachment base 531, and the ball-screw 530 is connect with the second motor 529, Described 531 one end of attachment base is connect with ball-screw 530, and the other end is connect with feed pipe 528, when work, the second motor 529 Ball-screw 530 is driven to rotate, ball-screw 530 drives attachment base 531 mobile, meanwhile, the feed pipe being connect with attachment base 531 528 will do it movement, and drive suction tube 526 mobile, and suction tube 526 absorbs little particle spoil by suction hole 527 on one side And medium, it is mobile to be able to drive mobile base 510 on one side, and further, the spoil crushing device 505 is by rotating bar 532, the One rubble stick 535 and rack gear 534 are constituted, and the rotating bar 532 is located in suction tube 526 and freely turns in suction tube 526 Dynamic, the rack gear 534 is fixed at 301 bottom of separation chamber, and the both ends of the rotating bar 532 are engaged with the transmission of rack gear 534, 532 both ends of rotating bar are fixedly connected with the gear 533 coaxial with rotating bar 532, gear 533 and rack gear through suction tube 526 is gone out 534 using cooperation, and the first rubble stick 535 is evenly distributed on 532 outer end face of rotating bar, on 526 inner wall of suction tube It is fixedly installed the second rubble stick 536, the second rubble stick 536 and the first rubble stick 535 staggeredly cooperate, and suction tube 526 exists Move back and forth carry out suction in 301 bottom of separation chamber under the drive of feed pipe 528, in 526 moving process of suction tube, suction tube Rotating bar 532 in 526 is since gear 533 and the cooperation of rack gear 534 are rotated, the first rubble stick in rotating bar 532 535 rotate with it, and the first rubble stick 535 in rotation forms shearing to spoil with the second rubble stick 536 in suction tube 526 and breaks It is broken, leptosomatic spoil fragment is directly converted into granular spoil fragment, avoids blockage problem, it is further, described Second spoil negative pressure device 506 is by the second negative pressure chamber 537, the second double-gate 539, third star baiting valve 540, hose 538 and Two air-introduced machines 541 are constituted, and the feed inlet in second negative pressure chamber 537 is connected to the discharge port on the second double-gate 539, and described the Feed inlet on two double-gates 539 is connected to the discharge port on hose 538, the feed inlet on the hose 538 and feed pipe 528 On discharge port connection, the feed inlet on the third star baiting valve 540 is connected to the second negative pressure chamber 537, and thereon out Material mouth is connected to the feed inlet on media processing system 6, and second air-introduced machine 541 is connected to the second negative pressure chamber 537, and its it Between connectivity part be provided with the second magnetic filtering sieve 542, when work, air in the second negative pressure chamber 537 is sucked out the second air-introduced machine 541 Vacuum is formed in the second negative pressure chamber 537, the second air-introduced machine 541 can be by feed pipe 528 when the second double-gate mechanism 539 opens The mixed material of interior spoil and medium sucks, and is then discharged to subsequent processing by third star baiting valve 540, due to mixed Dust can be generated during exercise by closing material, these dusts can be in the second magnetic filtering sieve 542 before entering the second air-introduced machine 541 Middle filtering, filtered medium with can be at being discharged immediately, the first double-gate mechanism 517 and 539 structure phase of the second double-gate mechanism Together, it is made of double-gate room 543, the first valve 544, the second valve 545, the first valve 544, the second valve 545 are located at The feed end of the feed end and discharge end of double-gate room 543, the double-gate room 543 of the first double-gate mechanism 517 is connected to separation chamber 301, Its discharge end is connected to the first negative pressure chamber 516, and the feed end of the double-gate room 543 of the second double-gate mechanism 539 is connected to hose 538, goes out Expect that end is connected to the second negative pressure chamber 537, first valve 544 is in off state when idle, and the second valve 545 is in an open state, work When, it, due to vacuum action, is vacuum state in double-gate room 543 that the first valve 544, which is in off state, and the second valve 545 is closed, Then the first valve 544 is opened, and the second valve 545 is in off state, and mixed material is inhaled into double-gate room 543, and then the One valve 544 is closed, and then the second valve 545 is opened, and completes charging, and whole process can guarantee the first negative pressure chamber 516 or the second Vacuum in negative pressure chamber 537 is stablized.

In order to guarantee that medium is preferably detached from from spoil or coal, further, the media processing system 6 is thick by medium De- device 601, medium essence take off device 602, belt medium-separation device 603 and medium storehouse 604 and constitute, and the medium storehouse 604 is fixed on 2 bottom of body, and 4 media processing systems 6 that connects of row's coal measures system, in medium slightly take off device 601 and 4 uses of row's coal measures system Cooperation, the media processing system 6 connect with waste stone exhaust system 5, in medium slightly take off device 601 and waste stone exhaust system 5 using cooperation, The medium slightly takes off the discharge port on device 601 and is connected to the feed inlet on the de- device 602 of medium essence, the de- dress of the medium essence The discharge port set on 602 is connected to the feed inlet on belt medium-separation device 603, the discharge port on the belt medium-separation device 603 It being connected to the feed inlet on medium storehouse 604, the discharge port on the medium storehouse 604 is connected to the feed inlet on separation system 3, into One step, the medium slightly takes off device 601, and by first, slightly de- cylinder 605, outer reinforcement cylinder 607, aggregate bin 608, second slightly take off cylinder 609, interior reinforcement cylinder 611 and spoke 612 are constituted, and described first slightly takes off cylinder 605 rotates setting in body 2, and described first is thick de- Material hole 606 is offered on 605 barrels of cylinder, and its both ends is connected to the fixation of outer reinforcement cylinder 607, the fixation of aggregate bin 608 is set It sets in the first slightly de- 605 bottom of cylinder, and discharge port thereon takes off the feed inlet on device 602 with medium essence and be connected to, it is described interior to add Strong cylinder 611 is fixed in outer reinforcement cylinder 607 by spoke 612, and the interior reinforcement cylinder 611 and the second thick de- cylinder 609 are fixed and connected Logical, described second slightly offers logical material strip seam 610 on de- 609 barrel of cylinder, discharge port on the described second thick de- cylinder 609 and the Discharge port on one thick de- cylinder 605 is connected to the feed inlet on belt medium-separation device 603, the media processing system 6 and row When cash system 5 connects, feed inlet on the described second thick de- cylinder 609 with the discharge port and the on the first star baiting valve 521 Discharge port connection on two star baiting valves 522, when the media processing system 6 is connect with row's coal measures system 4, described second is thick de- Feed inlet on cylinder 609 is connected to the discharge port on row's coal channel 403, when work, the mixed material or medium of medium and coal and The mixed material of spoil slightly takes off 609 one end of cylinder from second first and enters in the second thick de- cylinder 609, due to the second star baiting valve 522 drive, second slightly takes off cylinder 609 and the first thick de- synchronous rotation of cylinder 605, and second slightly takes off cylinder 609 in the process constantly rotated Middle medium and lesser spoil or coal cinder are from abjection in logical material strip seam 610 into first slightly de- cylinder 605, and then medium is from material hole Abjection is into aggregate bin 608 in 606, and slightly de- 609 other end of cylinder and first thick de- 605 one end of cylinder are discharged from second for coal or spoil To subsequent processing, overall structure, which can effectively avoid at material hole 606 or logical material strip seam 610, there is stuck problem, and de-mediated is high-quality And it is high-efficient, further, the belt medium-separation device 603 is by belt de-mediated pedestal 622, the second dead axle 623, second bearing 625, arc magnet ring 626, driving wheel 624, driven wheel 627, conveyer belt 628, the second material transfer cylinder 629 and the 4th motor 630 are constituted, The belt de-mediated pedestal 622 is fixed in body 2, and second dead axle 623 is fixed at belt de-mediated pedestal On 622, the driving wheel 624 is rotatably arranged on the second dead axle 623 by second bearing 625, and the arc magnet ring 626 is fixed It is arranged on the second dead axle 623, and the inner wall of itself and driving wheel 624 has certain interval, the driven wheel 627 is rotatably arranged on On belt de-mediated pedestal 622, the driving wheel 624 is driven with driven wheel 627 by conveyer belt 628, the second material transfer cylinder 629 are fixed on belt de-mediated pedestal 622, and its underface for being located at 626 end of arc magnet ring, second material transfer Discharge port on cylinder 629 is connected to medium storehouse 604, and the 4th motor 630 is sequentially connected with driving wheel 624, further, institute It states and is fixedly installed medium delivery pump 631 in body 2, the feed end on the medium delivery pump 631 is connected to medium storehouse 604, And discharge port thereon is connected to separation chamber 301, is fixedly installed level sensor 632 in the separation chamber 301, the medium is defeated Send pump 631 with level sensor 632 using cooperating, when work, the 4th motor 630 drives the rotation of the first driving wheel 624, transmission Band 628 is rotated with it with the second driving wheel 627, to form the transmission of material, is moved under the drive that material passes through conveyer belt 628 When at arc magnet ring 626, since medium contains a large amount of ferro elements, medium is just adsorbed on conveyer belt 628, coal cinder, cash The materials such as stone are discharged when being sent to integral outer, and medium still follows conveyer belt 628 mobile at this time, when medium is far from arc It is just voluntarily fallen in the second material transfer cylinder 629 when shape magnet ring 626, spoil or coal cinder are further taken off in transmission process It is situated between, improves the reuse ratio of medium.

For whole better automation control, further, the electric-control system 7 is by control room 701 and control host 702 are constituted, and control host 702 is for receiving each sensor signal and instructing to each electric component sending action, the control Host 702 processed is fixed in control room 701, the control host 702 respectively with separation system 3, row coal measures unite 4, discharge refuse System 5, media processing system 6, dust pelletizing system 8 and auxiliary system 9 are electrically connected.

In order to avoid dust is more in body 2, further, the dust pelletizing system 8 is by deduster 801 and cleaning shaft structure At the suction inlet on the deduster 801 is connected to the dust mouth on cleaning shaft, dust mouth and machine on the cleaning shaft It is connected to inside body 2, the air that dust is had in body 2 is sucked out and is filtered by deduster 801, avoids dust in body 2 The damage of each component and destruction to ambient enviroment.

In order to guarantee effective transmission of material, further, the auxiliary system 9 is by several 901 structures of belt conveyer At the belt conveyer 901 is used with the discharge port on belt medium-separation device 603 and the feed inlet in separation chamber 301 respectively Cooperation.

Claims (22)

1. a kind of air dry sand Recognition Applied in Coal Preparation System, it is characterised in that: including body (2), separation system (3), row's coal measures system (4), row Cash system (5), media processing system (6), electric-control system (7), dust pelletizing system (8), auxiliary system (9), the separation system (3), row's coal measures system (4), waste stone exhaust system (5), media processing system (6) are respectively positioned in body (2), row's coal measures system (4) with The row that waste stone exhaust system (5) is united on (4) with spoil layer using cooperation, row's coal measures with the coal cinder layer on separation system (3) respectively Discharge gate in material mouth and waste stone exhaust system (5) is respectively communicated with the feed inlet on media processing system (6), the media processing system (6) on discharge port connection separation system (3) on feed inlet, the electric-control system (7) respectively with separation system (3), row coal System (4), waste stone exhaust system (5), media processing system (6), dust pelletizing system (8) and auxiliary system (9) electrical connection, the dedusting system (8) dust removal port of uniting is connected to body (2), the feed inlet in discharge port connection separation system (3) on the auxiliary system (9).

2. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 1, it is characterised in that: the separation system (3) is by sorting Room (301), gas chamber (302), the first surge chamber (305), the second surge chamber (306) and roots blower (307) are constituted, the sorting Room (301) bottom is connected to the air inlet on gas chamber (302) and is fixed with pneumatic panel (303), the gas chamber in its connectivity part (302) heating net (304) of heating gas chamber (302) interior air is fixed in, the air inlet and first on the gas chamber (302) are slow Rush the connection of the gas outlet on room (305), going out on the air inlet and the second surge chamber (306) on first surge chamber (305) Port is connected to, and the air inlet on second surge chamber (306) is connected to the air outlet on roots blower (307).

3. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: the pneumatic panel (303) is by several A fixed plate (308) and several air-permeable elastic plates (309) are constituted, and the fixed plate (308) and air-permeable elastic plate (309) are fixed Connection, and be alternatively arranged between it, integrally formed with several ventholes in the air-permeable elastic plate (309).

4. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: first surge chamber (305) with Second surge chamber (306) connectivity part is connected with gas flowmeter (311) and flow control valve (312).

5. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: row's coal measures system (4) is by rotating Axis (401), row screen (402), row coal channel (403) and motor driver are constituted, and the rotation axis (401) is rotatably arranged on The upper end of separation chamber (301), described rotation axis (401) one end and motor driver are sequentially connected, row's screen (402) It is made of several rows coal bar (404), row's coal bar (404) is evenly distributed on rotation axis (401) outer end face, row's coal Feed inlet on channel (403) is connected to separation chamber (301), and it uses cooperation with row screen (402).

6. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 5, it is characterised in that: the motor driver includes the One motor (405) and the speed reducer being sequentially connected with first motor (405), the speed reducer and rotation axis (401) transmission connect It connects.

7. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: the waste stone exhaust system (5) includes cash Stone screening plant (501), spoil pushing meanss (502), the first spoil negative pressure device (503), spoil suction device (504), cash Stone crushing device (505) and the second spoil negative pressure device (506), spoil screening plant (501) make with spoil pushing meanss (502) With cooperation, spoil pushing meanss (502) and the first spoil negative pressure device (503) use cooperation, spoil pushing meanss (502) and cash Stone suction device (504) uses cooperation, the second spoil using cooperation, spoil suction device (504) and spoil crushing device (505) Negative pressure device (506) and spoil suction device (504) use cooperation.

8. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 7, it is characterised in that: the spoil screening plant (501) It is made of bottom sieve layer (507) and side screen layers (508), the bottom sieve layer (507) is fixed in separation chamber (301), the side One end of screen layers (508) is fixedly connected with the inner wall of separation chamber (301), and its other end is fixedly connected with bottom sieve layer (507), institute Stating between side screen layers (508) and bottom sieve layer (507) has gradient, the bottom sieve layer (507) and side screen layers (508) by sieve stick (509) it constitutes, there is blanking screen slot between adjacent sieve stick (509).

9. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 8, it is characterised in that: the spoil pushing meanss (502) It is made of mobile base (510), mandril (511) and return pin (512), the mandril (511), return pin (512) are fixed respectively In separation chamber (301) two sides of the bottom, the mobile base (510) sliding setting, mobile base in separation chamber (301) (510) rotation is provided with swingle (513) on, is fixedly connected with linkage board (514), the linkage on the swingle (513) Plate (514) drives swingle after linkage board (514) stress respectively with mandril (511) and return pin (512) using cooperation (513) it rotates, is fixedly connected with discharge refuse pawl (515) on the swingle (513), discharge refuse pawl (515) end is exposed the bottom of at The top of screen layers (507).

10. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 7, it is characterised in that: the first spoil negative pressure device (503) it is put by the first negative pressure chamber (516), the first double-gate (517), (518) first star baiting valve (521) of partition, the second star Expect valve (522), piano wire screen (523) and the first air-introduced machine (524), the feed inlet on first negative pressure chamber (516) is connected to sorting Room (301) and its connectivity part are located at bottom sieve floor (507) side end, and first negative pressure chamber (516) is connected to separation chamber (301) Place is provided with the first double-gate (517), and the partition (518) is fixed in the first negative pressure chamber (516), and it is in the first negative pressure Discharge refuse chamber (519) and row Jie's chamber (520), discharge port and the first star blowing on the discharge refuse chamber (519) are formed in room (516) Feed inlet on valve (521) is connected to, the charging on discharge port and the second star baiting valve (522) on Jie's row chamber (520) Mouthful connection, piano wire screen (523) row of being fixed at Jie's chamber (520) top, feed inlet on the piano wire screen (523) and the The connection of one double-gate (517) discharge port, and be fixedly connected at the top of its other end and partition (518), on first air-introduced machine (524) Air inlet be connected to the first negative pressure chamber (516), and connectivity part is provided with the first magnetic filtering sieve (525) between it.

11. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 10, it is characterised in that: the spoil suction device (504) it is made of suction tube (526), feed pipe (528) and mobile device, the suction tube (526) is located at separation chamber (301) bottom It portion and is fixed on mobile base (510), and its bottom offers suction hole (527), the charging on the feed pipe (528) Mouth is connected to the discharge port on suction tube (526), and the feed inlet on discharge port and the second spoil negative pressure device (506) thereon Connection, the feed pipe (528) connect with mobile device and move back and forth under the control of mobile device.

12. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 11, it is characterised in that: the mobile device includes second Motor (529), ball-screw (530) and attachment base (531), the ball-screw (530) connect with the second motor (529), institute It states attachment base (531) one end to connect with ball-screw (530), the other end is connect with feed pipe (528).

13. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 11, it is characterised in that: the spoil crushing device (505) it is made of rotating bar (532), the first rubble stick (535) and rack gear (534), the rotating bar (532) is located at suction tube (526) it is freely rotated in and in suction tube (526), the rack gear (534) is fixed at separation chamber (301) bottom, described The both ends of rotating bar (532) are engaged with rack gear (534) transmission, and the first rubble stick (535) is evenly distributed on rotating bar (532) On outer end face, be fixedly installed the second rubble stick (536) on suction tube (526) inner wall, the second rubble stick (536) with First rubble stick (535) staggeredly cooperates.

14. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 11, it is characterised in that: the second spoil negative pressure device (506) by the second negative pressure chamber (537), the second double-gate (539), third star baiting valve (540), hose (538) and the second air inducing Machine (541) is constituted, and the feed inlet on second negative pressure chamber (537) is connected to the discharge port on the second double-gate (539), and described the Feed inlet on two double-gates (539) is connected to the discharge port on hose (538), feed inlet and feeding on the hose (538) The discharge port connection on (528) is managed, the feed inlet on the third star baiting valve (540) is connected to the second negative pressure chamber (537), And discharge port thereon is connected to the feed inlet on media processing system (6), second air-introduced machine (541) and the second negative pressure chamber (537) it is connected to, and connectivity part is provided with the second magnetic filtering sieve (542) between it.

15. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 7, it is characterised in that: the media processing system (6) by Medium slightly takes off device (601), medium essence takes off device (602), belt medium-separation device (603) and medium storehouse (604) and constitutes, and is given an account of Matter storehouse (604) is fixed on body (2) bottom, and row's coal measures system (4) media processing system (6) that connect, in medium slightly take off Device (601) and row coal measures system (4) using cooperate, the media processing system (6) being connect with waste stone exhaust system (5), in medium Device (601) are slightly taken off with waste stone exhaust system (5) using cooperating, and the medium slightly takes off the discharge port on device (601) and takes off with medium essence Feed inlet connection on device (602), the medium essence take off on discharge port and belt medium-separation device (603) on device (602) Feed inlet connection, the discharge port on the belt medium-separation device (603) is connected to the feed inlet on medium storehouse (604), described Discharge port on medium storehouse (604) is connected to the feed inlet on separation system (3).

16. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 15, it is characterised in that: the medium slightly takes off device (601) by first, slightly de- cylinder (605), outer reinforcement cylinder (607), aggregate bin (608), second slightly take off cylinder (609), interior reinforcement cylinder (611) and spoke (612) is constituted, and described first slightly takes off cylinder (605) rotation setting in body (2), and described first slightly takes off cylinder (605) it is offered on barrel material hole (606), and its both ends is connected to the fixation of outer reinforcement cylinder (607), the aggregate bin (608) It is fixed at first slightly de- cylinder (605) bottom, and the feed inlet company on discharge port thereon and medium essence de- device (602) Logical, it is interior that interior the reinforcements cylinder (611) by spoke (612) is fixed on outer reinforcements cylinder (607), the interior reinforcement cylinder (611) and the Two slightly take off cylinder (609) fixed connection, offer logical material strip on described second thick de- cylinder (609) barrel and stitch (610), described second is thick Discharge port on de- cylinder (609) with first slightly take off discharge port on cylinder (605) with the feed inlet on belt medium-separation device (603) Connection, when the media processing system (6) connect with waste stone exhaust system (5), described second slightly take off cylinder (609) on feed inlet with Discharge port connection on discharge port and the second star baiting valve (522) on first star baiting valve (521), the media processes When system (6) is connect with row's coal measures system (4), going out on the feed inlet and row coal channel (403) on described second thick de- cylinder (609) Material mouth connection.

17. 6 a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 1, it is characterised in that: the medium essence takes off device (602) it is passed by essence de- pedestal (613), the first dead axle (614), roller (615), first bearing (616), circular arc frame (617), first Barrel (620), discharge barrel (619) and third motor (621) are constituted, and the essence de- pedestal (613) is fixed at body (2) Interior, first dead axle (614) is fixed on essence de- pedestal (613), and the roller (615) passes through first bearing (616) It is rotatably arranged on the first dead axle (614), and it is located at immediately below aggregate bin (608), the circular arc frame (617) is fixed on first On dead axle (614), and it is fixedly installed several permanent magnets (618) thereon, adjacent permanent magnet block (618) is in roller (615) appearance Magnetic force at face is different, and the discharge barrel (619) is fixed on essence de- pedestal (613), and it is same with circular arc frame (617) Side, the discharge port on the discharge barrel (619) are connected to the feed inlet on belt medium-separation device (603), the first material transfer cylinder (620) it is fixed on essence de- pedestal (613), and its underface for being located at circular arc frame (617) end, the first material transfer cylinder (620) discharge port on is connected to medium storehouse (604), and the third motor (621) and roller (615) are sequentially connected.

18. 7 a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 1, it is characterised in that: the belt medium-separation device (603) by belt de-mediated pedestal (622), the second dead axle (623), second bearing (625), arc magnet ring (626), driving wheel (624), driven wheel (627), conveyer belt (628), the second material transfer cylinder (629) and the 4th motor (630) are constituted, the belt de-mediated Pedestal (622) is fixed in body (2), and second dead axle (623) is fixed on belt de-mediated pedestal (622), The driving wheel (624) is rotatably arranged on the second dead axle (623) by second bearing (625), and the arc magnet ring (626) is solid It is fixed to be arranged on the second dead axle (623), and the inner wall of itself and driving wheel (624) has certain interval, the driven wheel (627) turns Dynamic to be arranged on belt de-mediated pedestal (622), the driving wheel (624) and driven wheel (627) are driven by conveyer belt (628), The second material transfer cylinder (629) is fixed on belt de-mediated pedestal (622), and it is located at arc magnet ring (626) end Underface, the discharge port on the second material transfer cylinder (629) are connected to medium storehouse (604), the 4th motor (630) and driving wheel (624) it is sequentially connected with.

19. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: fixed setting in the body (2) Have medium delivery pump (631), the feed end on the medium delivery pump (631) is connected to medium storehouse (604), and discharging thereon Mouth connection separation chamber (301), the separation chamber (301) is interior to be fixedly installed level sensor (632), the medium delivery pump (631) cooperation is used with level sensor (632).

20. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 1, it is characterised in that: the electric-control system (7) is by controlling Room (701) and control host (702) are constituted, and the control host (702) is fixed in control room (701), the control Host (702) respectively with separation system (3), row coal measures unite (4), waste stone exhaust system (5), media processing system (6), dust pelletizing system (8) and auxiliary system (9) is electrically connected.

21. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 1, it is characterised in that: the dust pelletizing system (8) is by dedusting Device (801) and cleaning shaft are constituted, and the suction inlet on the deduster (801) is connected to the dust mouth on cleaning shaft, described It is connected to inside dust mouth and body (2) on cleaning shaft.

22. a kind of air dry sand Recognition Applied in Coal Preparation System according to claim 2, it is characterised in that: the auxiliary system (9) is by several A belt conveyer (901) is constituted, the belt conveyer (901) respectively on belt medium-separation device (603) discharge port and Feed inlet in separation chamber (301) uses cooperation.