CN107813444A - A kind of system and method using junked tire producing gelatine powder under normal temperature - Google Patents

A kind of system and method using junked tire producing gelatine powder under normal temperature Download PDF

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Publication number
CN107813444A
CN107813444A CN201711123481.5A CN201711123481A CN107813444A CN 107813444 A CN107813444 A CN 107813444A CN 201711123481 A CN201711123481 A CN 201711123481A CN 107813444 A CN107813444 A CN 107813444A
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CN
China
Prior art keywords
blob
viscose
rubber
rubber powder
feed bin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201711123481.5A
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Chinese (zh)
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CN107813444B (en
Inventor
张涛
刘晓龙
张飞
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Hebei Zeng Li Alwayseal Technology Ltd
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Hebei Zeng Li Alwayseal Technology Ltd
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Priority to CN201711123481.5A priority Critical patent/CN107813444B/en
Publication of CN107813444A publication Critical patent/CN107813444A/en
Application granted granted Critical
Publication of CN107813444B publication Critical patent/CN107813444B/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B17/0404Disintegrating plastics, e.g. by milling to powder
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/06Spray cleaning
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0268Separation of metals
    • B29B2017/0272Magnetic separation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0424Specific disintegrating techniques; devices therefor
    • B29B2017/044Knives
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Disintegrating Or Milling (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The present invention relates to a kind of system and method using junked tire producing gelatine powder under normal temperature, cut circle machine, shredder, butterfly that the system includes being sequentially connected according to material conveying direction select machine, some rubber breakers and its subsidiary engine, magnetic separator, Celloco fractionator Celloco, rubber powder feed bin and rubber powder grading plant.The present invention thoroughly solves the problems, such as that the existing power consumption during junked tire production rubber powder is high, dust pollution is serious and security incident is multiple, realize automation mechanized operation that is broken in whole broken, broken glue and being finely milled, energy-conserving and environment-protective, labo r usage and labor intensity are considerably reduced, and gained rubber powder quality is good.

Description

A kind of system and method using junked tire producing gelatine powder under normal temperature
Technical field
It is specifically a kind of to utilize junked tire ordinary temperature production the present invention relates to a kind of production system of rubber powder and method The system and method for rubber powder.
Background technology
With the improvement of people's life quality, automobile has enter into huge numbers of families, the thing followed is a large amount of junked tires Process problem.The quantity of China's junked tire is surged with the speed of about 65,000,000 every year, and its recovery utilization rate only has 30% left side It is right.The Year's consumption of Chinese rubber occupies first place in the world, and therein 60% comes from import.Rubber sources increasingly it is in short supply instantly, give up The regeneration of old tire has important social effect and economic implications.
At present, the method for producing rubber powder using junked tire mainly has two kinds, i.e. normal temperature roll-in shearing method and low-temperature grinding Method.Low-temperature grinding method is using liquid nitrogen as cooling agent, makes rubber after ultralow temperature cooling becomes fragile, then is crushed, due to liquid nitrogen Expensive, production cost is high and can not promote.Normal temperature roll-in shearing method is more universal production method, preceding working procedure, i.e., Tire crushes, using " small three "(Cut circle machine, cutting machine and dicer)To process, the production of intermediate step, i.e. rubber powder, Glue is carried out brokenly to blob of viscose using broken gluing equipment, follow-up retrofit uses flour mill.Tire blob of viscose is during broken glue, repeatedly The effect such as extruded, rubbed, being torn by from rubber breaker roll, decomposable process produces substantial amounts of heat energy, causes rubber powder temperature It is too high and burn, the quality of rubber powder is influenceed, thus the rubber powder produced using normal temperature roll-in shearing method is second-rate, application Limitation is big.Moreover, the power consumption of whole production process is high, noise is big, dust disperses seriously, the security incidents such as fire easily occur. For a long time, above mentioned problem turns into the bottleneck for suppressing industry development.
The content of the invention
An object of the present invention is just to provide a kind of system using junked tire producing gelatine powder under normal temperature, existing to solve Rubber powder obtained by production system is of poor quality, the safe thing such as serious, easy generation fire that production process power consumption is high, noise is big, dust disperses Therefore the problem of.
The second object of the present invention is just to provide a kind of method using junked tire producing gelatine powder under normal temperature, to improve rubber powder Quality, dust pollution is reduced, improve production security.
What an object of the present invention was realized in:A kind of system using junked tire producing gelatine powder under normal temperature, including Cut circle machine, shredder, the butterfly being sequentially connected according to material conveying direction select machine, some rubber breakers and its subsidiary engine, magnetic separator, fiber Separator, rubber powder feed bin and rubber powder grading plant;
The shredder includes frame and is arranged in frame to tear up storehouse, drive mechanism, spraying control device and hydraulic pressure pressure Trigger structure;Paired roll is provided with the inside for tearing up storehouse, the roll is connected with the drive mechanism;The spraying control Device processed, which includes being arranged on, tears up some atomizers inside storehouse, providing water tank and the spray at water source for the atomizer Fog pump, it is arranged on the photoelectric sensor that tears up Cang Jinliaokouchu and to control the sprayer controller of the spraying water pump; The hydraulic strip clamp includes the pressing plate for being arranged on the hydraulic cylinder torn up on storehouse and being hinged on hydraulic cylinder piston rod end, described Pressing plate can be stretched into through feedback outlet under the driving of hydraulic cylinder and torn up in storehouse;
The rubber breaker and its subsidiary engine include rubber breaker, the output belt feeder being arranged on below rubber breaker bottom discharge mouth, set Vibrations classifying screen in output belt feeder discharge end, with shake collecting bin and feed end that classifying screen lower floor feed opening is connected and Shake the connected return conveyer machine of classifying screen upper strata feed opening, the discharge end of the return conveyer machine and the charging of the rubber breaker Mouth is connected;The first temperature sensor and the first spray head, first spray head and the first spray are provided with the rubber breaker Sprinkling pump is connected, and first temperature sensor electrically connects with the input of the first spray controller, the first spray control The output end of device electrically connects with the driver of the first feeding spraying pump.
The shredder is provided with two, and respectively the first shredder and the second shredder, the first shredder pass with tire Track is sent to be connected, the charging aperture of the second shredder is connected with the discharging opening of the first shredder, the discharging opening of the second shredder and butterfly The charging aperture of machine is selected to be connected, butterfly selects the unqualified rubber powder outlet of machine to be connected by feed back track with the feedback outlet of the first shredder; After tire is tentatively torn up into the first shredder, enter back into the second shredder carry out it is secondary tear up, obtained blob of viscose enter butterfly choosing In machine, the blob of viscose of size qualification enters in blob of viscose feed bin in case broken glue, out-of-size blob of viscose are back in the first shredder.
The rubber breaker is equipped with feeding device, and the feeding device includes blob of viscose feed bin, is arranged at the top of blob of viscose feed bin Feeding mouth, the vibrating feeder (conveyer), the charging belt feeder and use to be fed into rubber breaker that are arranged on blob of viscose bin bottom To control the vibrating controller of vibrating feeder (conveyer) discontinuous operation;The feed end of the charging belt feeder is located at the vibrating feeder (conveyer) Discharging opening below, it is described charging belt feeder discharge end be connected with the charging aperture of rubber breaker;
The distribution and conveying of blob of viscose, the distribution conveying are realized between the blob of viscose feed bin that each rubber breaker arranges by distribution conveyor Machine is that preceding belt conveyor and rear belt conveyor are provided with the top of blob of viscose feed bin, is set in the discharge end of preceding belt conveyor Two pieces of retractable valve plates are equipped with, one of valve plate is located at the top of the feeding mouth of blob of viscose feed bin, after another piece of valve plate is located at The top of the feed end of belt conveyor;The feed end of the preceding belt conveyor of blob of viscose feed bin corresponding to First rubber breaker and institute Stating butterfly selects the discharge end of machine to be connected.
Present invention additionally comprises the screen centrifuge for regrading rubber powder and by the levigate flour mill of rubber powder.By the rubber powder The rubber powder for the different stage that grading plant sorts out, centrifugation screening is carried out into screen centrifuge, qualified rubber powder is directly packed, no Qualified rubber powder enters in flour mill after milling, then sieved through screen centrifuge, so circulation.
The discharge end of the output belt feeder is provided with tripper, the tripper includes two conveyer belts and is arranged on Dam plate between two conveyer belts, the feed direction of two conveyer belts is opposite, and shake is provided with the discharging end of two conveyer belts Dynamic classifying screen.
The rubber breaker includes broken Jiao Cang, the two pairs of rollers being arranged on brokenly in glue storehouse and to drive the driver of two pairs of rollers, broken Jiao Cang top, the feed end for shaking classifying screen and discharge end are provided with dust gathering arrester, and dust gathering arrester passes through air inducing pipeline and dedusting The air inlet of device is connected, and second temperature sensor and the second spray head, second spray head and are provided with air inducing pipeline Two feeding spraying pumps are connected, and the second temperature sensor electrically connects with the input of the second spray controller, second spray The output end of controller electrically connects with the driver of the second feeding spraying pump.
The second object of the present invention is achieved in that a kind of method using junked tire producing gelatine powder under normal temperature, including Following steps:
A, tire is put into and cut in circle machine, mobile cutter, the tyre bead of tire both sides cut down, tyre bead centralized collection, cut away The tire of tyre bead is torn up in storehouse through tire transmission track feeding shredder;
B, the tire of tyre bead is cut away into after tearing up storehouse, and Driven by Hydraulic Cylinder pressing plate, which stretches into, tears up storehouse internal pressure ratch tire, photoelectric sensing Device detects signal and passes to sprayer controller, and sprayer controller control pump working, atomizer starts to storehouse internal spraying, At the same time, roll rotation cutting tire, cuts into blob of viscose, obtained blob of viscose selects machine to be screened into butterfly, size by tire Qualified blob of viscose enters blob of viscose feed bin in case broken glue, out-of-size blob of viscose are back to tear up in storehouse and torn up again;
C, blob of viscose is sent into rubber breaker through feeding device, and rubber powder is resolved under the friction, squeezing action in two pairs of rollers, and rubber powder passes through broken Glue motor spindle discharging opening is fallen on belt conveyer, through exporting Belt Conveying to vibrations classifying screen, in the vibration of vibrations classifying screen It is classified under sieving actoion, the rubber powder that particle diameter is less than the screen cloth mesh of vibrations classifying screen enters lower floor's slideway by screen cloth, and falls into In collecting bin, the rubber powder that particle diameter is more than the screen cloth mesh of vibrations classifying screen is stayed in above screen cloth, and is sent back to broken through return conveyer machine Continue brokenly glue in glue machine;During this, the first temperature sensor monitors rubber powder temperature in real time, when measured temperature is more than setting value When, the first spray head starts to spray water to rubber powder, after temperature is dropped to below setting value, stops water spray;
D, the rubber powder in collecting bin removes fiber into Celloco fractionator Celloco after magnetic separator removes steel wire, removes the rubber powder after fiber It is sent in rubber powder feed bin;
E, the rubber powder in rubber powder feed bin is discharged to rubber powder by the vibration discharger of rubber powder bin bottom according to setting time discontinuous operation On grading plant, the classification of rubber powder is realized.
Feeding device in the step c includes blob of viscose feed bin, the feeding mouth being arranged at the top of blob of viscose feed bin, is arranged on glue The vibrating feeder (conveyer) of block bin bottom, to the charging belt feeder that is fed into rubber breaker and to control between vibrating feeder (conveyer) Knock off the vibrating controller of work;The feed end of the charging belt feeder is located at below the discharging opening of the vibrating feeder (conveyer), described The discharge end of charging belt feeder is connected with the charging aperture of rubber breaker;The vibrating feeder (conveyer), will according to setting time discontinuous operation Blob of viscose in blob of viscose feed bin is discharged on charging belt feeder, charging belt feeder work, blob of viscose is transported in rubber breaker.
The distribution and conveying of blob of viscose, the distribution are realized between the supporting blob of viscose feed bin of each rubber breaker by distribution conveyor Conveyer is that preceding belt conveyor and rear belt conveyor are provided with the top of blob of viscose feed bin, in the discharging of preceding belt conveyor End is provided with two pieces of retractable valve plates, and one of valve plate is located at the top of the feeding mouth of blob of viscose feed bin, another piece of valve plate position In the top of the feed end of rear belt conveyor;The feed end of the preceding belt conveyor of the supporting blob of viscose feed bin of First rubber breaker The discharge end for selecting machine with the butterfly is connected;
Select preceding belt conveyor of the qualified blob of viscose of machine through blob of viscose feed bin corresponding to First rubber breaker outwards to convey from butterfly, beat Valve plate corresponding with the blob of viscose feed bin feeding mouth is opened, closes valve plate corresponding with rear belt conveyor, blob of viscose falls into the blob of viscose material In storehouse, when being fed intake into the blob of viscose feed bin of second rubber breaker, valve plate corresponding with rear belt conveyor is opened, is closed another Block valve plate, the subsequent belt conveyor of blob of viscose is conveyed backward, by that analogy, realize the feeding to each blob of viscose feed bin.
In step c, the rubber breaker includes broken Jiao Cang, the two pairs of rollers being arranged on brokenly in glue storehouse and to drive the driving of two pairs of rollers Device, dust gathering arrester is provided with broken Jiao Cang top, the feed end of vibrations classifying screen and discharge end, dust gathering arrester passes through air inducing pipeline It is connected with the air inlet of deduster, second temperature sensor and the second spray head, second spray is provided with air inducing pipeline Head is connected with the second feeding spraying pump, and the input that the second temperature sensor sprays controller with second electrically connects, and described the The output end of two spray controllers electrically connects with the driver of the second feeding spraying pump;
Second temperature sensor monitors air inducing pipeline internal temperature in real time, when measured temperature is more than setting value, the second spray head Start to spray water, after temperature is dropped to below setting value, stop water spray.
In the step e, the rubber powder of the different stage sorted out by the rubber powder grading plant, enter into screen centrifuge Row centrifugation screening, qualified rubber powder are directly packed, and underproof rubber powder enters in flour mill after milling, then sieved through screen centrifuge, So circulation.
The present invention is ingenious in design, and the links that junked tire is effectively broken into powder closely link up, automation Degree is high, considerably reduces labo r usage and hand labor intensity, saves production run cost, and energy-conserving and environment-protective, energy consumption is low, It is environment-friendly, it is easy to maintenance, it is adapted to popularization and application.The inventive method automaticity is high, and dump temperature is good, and rubber powder quality is good, The indices of gained rubber powder see the table below, from data in table, the remote superstate standard of rubber powder quality produced by the invention.
The present invention solves the problems, such as that tire caused dust during tearing up flies away, its structure low with security everywhere Simply, equipment cost and operating cost substantially reduce, and compared with underbalance pulse deduster, a set of underbalance pulse deduster takes More than tens of thousands of members, and the spraying control device used in the present invention only needs 5,000 yuan or so, equal type, is removed according to pulse Dirt uses the spraying control device of the present invention, it is necessary to configure the blower fan of 7.5kw power, only need to configure 0.75kw water pumps. Automaticity of the present invention is high, had both avoided dust and has dispersed, and will not produce in muddy water slave unit and discharge again, saves electric energy, avoids Secondary pollution and waste.
The present invention can effectively solve blob of viscose micelle caused by caused amount of heat in rubber breaker and subsidiary engine operation process With blob of viscose temperature it is too high the problem of, effectively reduce spontaneous combustion risk, suppress production process in produce dust recycling.It is of the invention with it is existing Natural cooling in broken gluing equipment is compared with air-cooled technology, can reduce temperature of charge to greatest extent, is reduced dedusting to greatest extent and is set Standby configuration power, realize that rubber powder breaks the environmental protection of rubber ring section, energy-conservation, the efficient, production process of zero spontaneous combustion risk.
Present system is ingenious in design, compact-sized, and belt conveyor is from the top of blob of viscose feed bin by saving equipment Space, optimize the attachment structure between belt conveyor, shorten the setting length of belt conveyor, saved equipment Cost, Devices in Workshop is rationally distributed, beneficial to safety in production.The vibrating feeder (conveyer) discontinuous operation of the present invention, both ensures rubber breaker In blob of viscose meet production requirement, the problems such as avoiding putty, flash caused by causing blob of viscose excessive again, kept an eye on without special messenger, Save manpower.
Brief description of the drawings
Fig. 1 is the schematic flow sheet of the present invention.
Fig. 2 is the structural representation of shredder.
Fig. 3 is the principle schematic diagram of shredder.
Fig. 4 is the structural representation of rubber breaker and its subsidiary engine.
Fig. 5 is the structural representation of tripper.
Fig. 6 is the structural representation of feeding device.
Fig. 7 is the structural representation of distribution conveyor.
Fig. 8 is the structural representation of vibrating feeder (conveyer).
In figure:1st, frame, 2, tear up storehouse, 3, drive mechanism, 4, framework platform, 5, roll, 6, tire transmission track, 7, return Expect track, 8, discharge gate, 9, atomizer, 10, water tank, 11, spraying water pump, 12, photoelectric sensor, 13, pressing plate, 14, piston Bar, 15, rubber breaker, 16, broken Jiao Cang, 17, two pairs of rollers, 18, output belt feeder, 19, conveyer belt, 20, dam plate, 21, vibrations classifying screen, 22nd, screen cloth, 23, return conveyer machine, 24, shirt rim, 25, cover plate, 26, dust gathering arrester, 27, blob of viscose feed bin, 28, preceding belt conveyor, 29th, rear belt conveyor, the 30, first valve plate, the 31, second valve plate, 32, vibrating feeder (conveyer), 33, hopper, 34, bearing, 35, vibration Motor, 36, buffer spring, 37, charging belt feeder, 38, butterfly select machine, 39, charging belt machine, 40, feeding mouth.
Embodiment
Embodiment 1:Utilize the system of junked tire producing gelatine powder under normal temperature.
The present invention mainly by cut circle machine, shredder, butterfly select machine 38, rubber breaker and its subsidiary engine, magnetic separator, Celloco fractionator Celloco, The part such as rubber powder feed bin, rubber powder grading plant, screen centrifuge and flour mill forms.
Circle machine is cut the tyre bead of tire both sides to be cut down, tyre bead is individually handled, avoids second-rate circle mouth Glue is mixed into tire glue powder, and the tire for cutting away tyre bead is sent in shredder through tire transmission track 6.
Shredder is the tire for cutting away tyre bead to be torn into 5cm × 8cm or so blob of viscose, in case broken glue, such as Fig. 2 and Fig. 3 Shown, shredder includes frame 1, tears up storehouse 2, drive mechanism 3, hydraulic strip clamp and spraying control device.
Storehouse 2 is torn up as the place for tearing up tire, a pair roller 5 is internally provided with warehouse, roll 5 include transfer roller and The cutter being arranged on transfer roller, transfer roller are connected with drive mechanism 3, and drive mechanism 3 is arranged on framework platform 4, and two are rolled Roller 5 relatively rotates, to carry out cutting and crushing to tire.Charging aperture, charging aperture and tire are provided with a side wall of warehouse Transmission track 6 is connected, and feedback outlet is provided with another side wall of warehouse, feedback outlet is connected with feed back track 7, in warehouse Bottom is provided with discharge gate 8, and charging aperture and feedback outlet are located at the top of framework platform 4, and discharge gate 8 is located at the lower section of framework platform 4.
Hydraulic strip clamp includes hydraulic cylinder and pressing plate 13, and pressing plate 13 is in " 7 " type, including supporting plate and cover clamp, support The bottom of plate is hinged on the warehouse outer wall below feedback outlet, and cover clamp passes through the feedback outlet for tearing up storehouse 2 to enter in warehouse, hydraulic pressure Cylinder is arranged on the warehouse outer wall above supporting plate, and the end of the piston rod 14 of hydraulic cylinder is be hinged on the supporting plate, piston rod 14 Reciprocating motion drive supporting plate around its jointed shaft rotate, and then drive cover clamp disengaging shredder feedback outlet.Tire enters After tearing up storehouse 2, hydraulic cylinder action, piston rod 14 bounces back, and pulls supporting plate to be rotated to close to warehouse direction, thus passes through cover clamp The feedback outlet for tearing up storehouse 2 enters in warehouse, pushes down tire, and tire forms the glue of bulk under the cutting and crushing effect of roll 5 Block, blob of viscose are discharged from discharge gate 8;After tearing up end-of-job, hydraulic cylinder acts again, and piston rod 14 is overhanging, promote supporting plate to Rotated away from warehouse direction, cover clamp is extracted out inside warehouse.
As shown in figure 3, spraying control device includes some atomizers 9, water tank 10, spraying water pump 11, photoelectric sensor 12 and sprayer controller, atomizer 9, which is arranged on, to be torn up in storehouse 2, and each atomizer 9 is connected by water supply line with water tank 10, Spraying water pump 11 is arranged on water supply line.Photoelectric sensor 12 is arranged at the charging aperture for tearing up storehouse 2, sprayer controller it is defeated Enter end to electrically connect with photoelectric sensor 12, the output end of sprayer controller electrically connects with spraying water pump 11.When photoelectric sensor 12 After detecting charging signal, signal is passed into sprayer controller, sprayer controller control spraying water pump 11 is opened, in water tank 10 Water enter atomizer 9 in, formed water smoke, water smoke will be torn up tire is torn up in storehouse 2 during caused dust settling get off, Avoid dust from flying and pollute environment, water smoke will mix after dust settling with the blob of viscose in storehouse, reduces blob of viscose temperature, avoids burning The generation of explosion accident.Also sprayer controller can be electrically connected with hydraulic cylinder, the dynamic of hydraulic cylinder is controlled by sprayer controller Make.
Due to dust yield and tire in feed bin to tear up the time proportional, in order to further improve dust settling Efficiency simultaneously avoids producing muddy water, frequency converter is connected in the output end of sprayer controller, by opening for Frequency Converter Control spraying water pump 11 Close and speed, the input of frequency converter electrically connect with the output end of sprayer controller, output end and the spraying water pump 11 of frequency converter Electronic mechatronics.Frequency converter enters the time of shredder feed bin according to tire, automatically adjusts the speed of spraying water pump 11, enters And the change of spraying size is realized, as tire enters the increase of the time of shredder feed bin, the speed of spraying water pump 11 is accelerated, After reaching setting and tearing up the time(After the completion of tearing up), Frequency Converter Control spraying water pump 11 close, spraying stop.
Shredder is provided with two, respectively the first shredder and the second shredder, the charging aperture and wheel of the first shredder Tire transmission track 6 is connected, and the charging aperture of the second shredder is connected with the discharging opening of the first shredder by delivery track, and second tears The discharging opening of broken machine selects the charging aperture of machine 38 to be connected with butterfly, and butterfly selects the unqualified material outlet of machine 38 to pass through feed back track 7 and first The feedback outlet of shredder is connected.After tire is tentatively torn up into the first shredder, enter back into the second shredder carry out it is secondary tear up, Obtained blob of viscose is selected in machine 38 into butterfly, and the blob of viscose of size qualification enters in blob of viscose feed bin 27 in case broken glue, out-of-size Blob of viscose is back in the first shredder.
Butterfly selects machine 38 to be sorted to blob of viscose, blob of viscose of the size no more than 5cm × 8cm is sorted out, by upper Material belt feeder 39 delivers to rubber breaker, in case broken glue, blob of viscose of the size more than 5cm × 8cm is transmitted back in shredder to be torn up again.
As shown in Figure 4 and Figure 5, rubber breaker and its subsidiary engine include rubber breaker 15, output belt feeder 18, tripper, vibrations point Level the sieve 21 and grade of return conveyer machine 23 part, by butterfly the blob of viscose of size qualification that machine 38 sorts out will be selected to carry out brokenly glue, Generate rubber powder.
Rubber breaker 15 includes broken glue storehouse 16, the two pairs of rollers 17 being arranged on brokenly inside glue storehouse 16 and to drive the drive of two pairs of rollers 17 Dynamic device, charge door, the bottom blanking that charge door passes through feed belt feeder 37 and blob of viscose feed bin 27 are provided with the top in broken glue storehouse 16 Mouth is connected, to launch blob of viscose into broken glue storehouse 16.The bottom in broken glue storehouse 16 is provided with discharging opening, to discharge through two pairs of rollers 17 The rubber powder obtained after extrusion friction.
Output belt feeder 18 is arranged on brokenly the lower section of the discharging opening in glue storehouse 16, rubber powder to be transported out, including output Belt and driver.Tripper is arranged on the discharge end of output belt, and tripper includes two conveyer belts 19 and is arranged on two Dam plate 20 between conveyer belt 19, the transmission direction of two conveyer belts 19 are reversely transmitted with dam plate 20 for boundary, i.e. conveyer belt 19 One end away from dam plate 20 is discharge end.The end face of dam plate 20 is triangular in shape, and the top of dam plate 20 is along positioned at output belt discharge end Lower section, thus will export the rubber powder that falls on belt and be divided into two parts, to improve follow-up shaking-sieving efficiency.
Vibrations classifying screen 21 is respectively arranged with the discharging end of every conveyer belt 19, vibrations classifying screen 21 includes slideway, set Screen cloth 22 and shaking device on slideway are put, slideway is separated into two layers up and down by screen cloth 22, the feed opening and collecting bin of lower floor It is connected, the feed opening on upper strata and the bottom of return conveyer machine 23(Feed end)It is connected.After rubber powder enters vibrations classifying screen 21, particle diameter Less than the mesh of screen cloth 22 micelle by screen cloth 22, fall on slideway bottom plate, and slid under the collective effect of vibrations and gravity Into collecting bin;The micelle that particle diameter is more than the mesh of screen cloth 22 stays in the top of screen cloth 22, and under the collective effect of vibrations and gravity It is slipped on return conveyer machine 23.
Return conveyer machine 23 includes return conveyer and the drive device being obliquely installed, the top of return conveyer(Discharge end)With The charging aperture in broken glue storehouse 16 is connected, and the larger micelle foldback of particle diameter is returned in rubber breaker 15, carries out breaking glue again.Returning charge skin Discharge end with machine 23 is provided with positioned at the surface of output belt feeder 18 between return conveyer machine 23 and output belt feeder 18 PVC window shades, it can effectively obstruct dust and leak, it is necessary to when observing the micelle on output belt, window shade is lifted up.In returning charge The both sides of belt are respectively arranged with shirt rim 24, to reduce dropping for micelle in course of conveying or blob of viscose, avoid belt both sides from penetrating Steel wire causes belt to wear sideslip, reduces blanking around machine, extends belt service life, reduces the replacing of belt and conveying axis Frequency.Cover plate 25 is respectively equipped with the top of return conveyer and bottom, to prevent discharging airborne dust.
The first temperature sensor and the first spray head, the first temperature sensor and spray are internally provided with broken glue storehouse 16 The input electrical connection of controller, the first spray head are connected by water supply line with water tank 10, and spray is provided with water supply line Sprinkling pump, feeding spraying pump are provided with variable frequency drives, and variable frequency drives electrically connect with spraying the output end of controller.When the first temperature Sensor measured temperature is higher than setting value(70℃)When, signal is sent to spray controller, spray controller receives temperature letter Number it is rear send drive signal to variable frequency drives, and according to setting value, adjust variable frequency drives working frequency, control shower water Revolution speed, so as to adjust spray flow, finally realize the reasonable control of temperature of charge.
Dust gathering arrester 26 is provided with respectively at the positions such as the feed end in broken glue storehouse 16, tripper and return conveyer, to Dust caused by collection, dust gathering arrester 26 are connected by air inducing pipeline with the air inlet of deduster.Is provided with air inducing pipeline Two temperature sensors and the second spray head, both sprays and control principle same first temperature sensor and the first spray head, this Place repeats no more.
Because the broken glue speed of rubber breaker 15 tears up speed less than shredder, in order to improve production efficiency, it is commonly provided with More set rubber breakers and its subsidiary engine.Every rubber breaker 15 is equipped with feeding device, as shown in fig. 6, feeding device includes blob of viscose material Storehouse 27, vibrating feeder (conveyer) 32, charging belt feeder 37 and vibrating controller.Blob of viscose feed bin 27 tears up and passed through through shredder to store Butterfly selects machine 38 to sort the obtained blob of viscose of size qualification, and its top warehouse is in the form of a column, and bottom warehouse is in back taper.On the top of warehouse Portion is provided with feeding mouth 40, and discharging opening is provided with the bottom of warehouse, and vibrating feeder (conveyer) 32 is arranged on the discharge outlet.Such as figure Shown in 8, vibrating feeder (conveyer) 32 includes bearing 34, hopper 33, buffer spring 36 and vibrating motor 35, and hopper 33 is arranged on feed bin Discharge outlet, bearing 34 are located at the lower section of hopper 33, to support hopper 33, buffer spring 36 be arranged on the bottom surface of hopper 33 with Between the top surface of bearing 34, to buffer the vibration transmitted to the direction of bearing 34, vibrating motor 35 is arranged on the outside of hopper 33 On wall.
Vibrating controller is provided with two delay circuits controlling the discontinuous operation of vibrating motor 35 in vibrating controller, One controlling the feed time of vibrating motor 35(That is single time of vibration), another to control vibrating motor 35 plus Expect interval time(Interval time i.e. between two-time vibration).The blob of viscose of size qualification is stored in blob of viscose feed bin 27, and root Feed time and feeding interval time are set according to the demand of actual production, had thus both ensured that the blob of viscose in rubber breaker 15 met production Demand, the problems such as avoiding putty, flash caused by causing blob of viscose excessive again.
Belt feeder 37 feed blob of viscose is transported in rubber breaker 15, its bottom(That is feed end)Positioned at vibrating feeder (conveyer) The lower section of 32 discharging opening, its top(That is discharge end)It is connected with the charging aperture of rubber breaker 15.It is provided with charging belt feeder 37 Sensor, when having detected that blob of viscose falls when on belt, its supporting electric motor starting, driving charging belt feeder 37 works, by glue Block is sent into rubber breaker 15, and when no blob of viscose falls when on belt feeder, its supporting motor is closed, and belt feeder is stopped.
The distribution and conveying of blob of viscose are realized between the supporting blob of viscose feed bin 27 of each rubber breaker 15 by distribution conveyor, is such as schemed Shown in 7, distribution conveyor is that preceding belt conveyor 28 and rear belt conveyor 29 are provided with the top of blob of viscose feed bin 27, preceding The discharge end of belt conveyor 28 is provided with two pieces of retractable valve plates, and the discharge end of belt conveyor 28 leads before valve plate is hinged on On trackside wall, the width of two pieces of valve plates is equal to the belt width of preceding belt conveyor 28, is referred to as the first valve plate 30 and second Valve plate 31, wherein, the first valve plate 30 is located at the top of the feeding mouth 40 of blob of viscose feed bin 27, and the second valve plate 31 is located at rear Belt Conveying The top of the feed end of machine 29.When two pieces of valve plates close, the discharge end of preceding belt conveyor 28 is blocked, when the first valve plate 30 are opened, and when the second valve plate 31 closes, blob of viscose is fallen into current blob of viscose feed bin 27, when the first valve plate 30 closes, the second valve plate 31 During opening, blob of viscose falls on rear belt conveyor 29, is delivered to next blob of viscose feed bin 27.The supporting blob of viscose of First rubber breaker 15 The feed end of the preceding belt conveyor 28 of feed bin 27 selects the discharge end of machine 38 to be connected with butterfly, the supporting glue of last rubber breaker 15 Rear belt conveyor 29 can be not provided with block storehouse 27.Between two adjacent blob of viscose feed bins 27, after previous blob of viscose feed bin The preceding belt conveyor 28 of belt conveyor 29 and latter blob of viscose feed bin is seamlessly connected, or same belt conveyor.
Magnetic separator removes steel wire to carry out magnetic separation to the rubber powder in collecting bin;Celloco fractionator Celloco is removing in rubber powder Fiber.The rubber powder of removing steel wire and fiber is delivered in rubber powder feed bin by bucket elevator to be stored, and according to different purposes, utilizes glue Powder grading plant is classified to rubber powder, isolates the rubber powder of different meshes.Part rubber powder is directly sent to packing by wind-force Machine, packed;Remaining rubber powder enters screen centrifuge through helix transporting device, and after centrifugation is sieved, qualified rubber powder packing is unqualified Rubber powder enter flour mill in be milled, the rubber powder after milling, which is entered back into screen centrifuge, to be sieved, so circulation.
Embodiment 2:Utilize the method for junked tire producing gelatine powder under normal temperature.
The method using junked tire producing gelatine powder under normal temperature of the present invention comprises the following steps:
1)The system using junked tire producing gelatine powder under normal temperature described in a set of embodiment 1 is set, during original state, shredder Pressing plate 13 is being torn up outside storehouse 2.
2)Tire is put into and cut in circle machine, mobile cutter, the tyre bead of tire both sides is cut down, tyre bead can be straight after collecting Pin is sold, also can through grinding silk process for producing circle mouth steel wire and circle mouth glue, circle mouth steel wire can direct marketing, circle mouth glue can be sharp again With broken glue milling.
3)The tire for cutting away tyre bead is sent into tire transmission track 6, completes to enter after weighing on tire transmission track 6 and tears up Machine is torn up in storehouse 2.
4)For tire into after tearing up in storehouse 2, photoelectric sensor 12 detects tire signal, and signal is passed into control Device, controller control hydraulic cylinder action, piston rod 14 bounce back, pull supporting plate to be rotated to close to warehouse direction, thus make gland Plate enters in warehouse through tearing up storehouse feedback outlet, and tire is pushed down, and simultaneously, spraying water pump 11 is started working, and atomizer 9 is opened Beginning to storehouse internal spraying, roll 5 starts simultaneously at rotation, cuts tire, when reaching setting time, spray water pump 11 and drive mechanism 3 are stopped, and the piston rod 14 of hydraulic cylinder is overhanging, and cover clamp is extracted out inside warehouse, prepares the cutting of next tire, obtains To blob of viscose discharged through tearing up the discharge gate 8 of the bottom of storehouse 2, select in machine 38, screened into butterfly, the blob of viscose of size qualification enters Blob of viscose feed bin 27 is in case broken glue, out-of-size blob of viscose are back to tear up in storehouse 2 through feed back track 7 and torn up again.
Preceding belt conveyor 28 of the qualified blob of viscose of machine 38 through blob of viscose feed bin corresponding to First rubber breaker 15 is selected from butterfly Outwards conveying, open and the 40 corresponding valve plate of blob of viscose feed bin feeding mouth, closing and rear 29 corresponding valve plate of belt conveyor, glue Block is fallen into the blob of viscose feed bin, when needing to feed intake into the blob of viscose feed bin of second rubber breaker 15, is opened and rear Belt Conveying Valve plate corresponding to machine 29, another piece of valve plate is closed, the subsequent belt conveyor 29 of blob of viscose is conveyed backward, by that analogy, realization pair The feeding of the blob of viscose feed bin 27 of each rubber breaker 15.
5)Vibrating controller, will according to the feed time and the discontinuous operation of feeding interval time control vibrating motor 35 of setting Blob of viscose in blob of viscose feed bin 27 is discharged on charging belt feeder 37, and charging belt feeder 37 is worked, and blob of viscose is transported into rubber breaker 15 In broken glue storehouse 16;
6)After blob of viscose enters in broken glue storehouse 16, two pairs of rollers 17 start to rotate, and extrude, rub blob of viscose, it is resolved into rubber powder, and rubber powder leads to Cross the bottom discharge mouth of rubber breaker 15 to fall on belt conveyer, punish into two parts, two parts rubber powder and respectively enter to tripper Sieve classification on corresponding vibrations classifying screen 21, the small rubber powder of particle diameter enter lower floor's cunning by shaking the screen cloth 22 of classifying screen 21 Road, and falling into collecting bin, the big rubber powder of particle diameter stay in the top of screen cloth 22, and through return conveyer machine 23 send back in rubber breaker 15 after Continuous broken glue;During this, the first temperature sensor monitors rubber powder temperature in real time, when measured temperature is more than setting value(70℃)When, First spray head starts to spray water to rubber powder, after temperature is dropped to below setting value, stops water spray.
7)Rubber powder in collecting bin removes fiber into Celloco fractionator Celloco after magnetic separator removes steel wire, after removing fiber Rubber powder is promoted in rubber powder feed bin by bucket elevator.
8)Rubber powder in rubber powder feed bin is discharged to by the vibration discharger of rubber powder bin bottom according to setting time discontinuous operation On rubber powder grading plant, the classification of rubber powder is realized.The rubber powder of the different stage sorted out by rubber powder grading plant, part glue Powder is directly packed, and remaining rubber powder carries out centrifugation screening into screen centrifuge, and qualified rubber powder is directly packed, and underproof rubber powder enters It is milled in flour mill, then is sieved through screen centrifuge, so circulation.
In said process, air inducing pipeline takes issuable dust at rubber breaker and its subsidiary engine away, second temperature sensing Device monitors air inducing pipeline internal temperature in real time, and when measured temperature is more than setting value, the second spray head starts to spray water, at a temperature of After being down to below setting value, stop water spray.

Claims (10)

1. a kind of system using junked tire producing gelatine powder under normal temperature, it is characterized in that, including according to material conveying direction successively phase Cut circle machine, shredder, butterfly even selects machine, some rubber breakers and its subsidiary engine, magnetic separator, Celloco fractionator Celloco, rubber powder feed bin and rubber powder Grading plant;
The shredder includes frame and is arranged in frame to tear up storehouse, drive mechanism, spraying control device and hydraulic pressure pressure Trigger structure;Paired roll is provided with the inside for tearing up storehouse, the roll is connected with the drive mechanism;The spraying control Device processed, which includes being arranged on, tears up some atomizers inside storehouse, providing water tank and the spray at water source for the atomizer Fog pump, it is arranged on the photoelectric sensor that tears up Cang Jinliaokouchu and to control the sprayer controller of the spraying water pump; The hydraulic strip clamp includes the pressing plate for being arranged on the hydraulic cylinder torn up on storehouse and being hinged on hydraulic cylinder piston rod end, described Pressing plate can be stretched into through feedback outlet under the driving of hydraulic cylinder and torn up in storehouse;
The rubber breaker and its subsidiary engine include rubber breaker, the output belt feeder being arranged on below rubber breaker bottom discharge mouth, set Vibrations classifying screen in output belt feeder discharge end, with shake collecting bin and feed end that classifying screen lower floor feed opening is connected and Shake the connected return conveyer machine of classifying screen upper strata feed opening, the discharge end of the return conveyer machine and the charging of the rubber breaker Mouth is connected;The first temperature sensor and the first spray head, first spray head and the first spray are provided with the rubber breaker Sprinkling pump is connected, and first temperature sensor electrically connects with the input of the first spray controller, the first spray control The output end of device electrically connects with the driver of the first feeding spraying pump.
2. system according to claim 1, it is characterized in that, the rubber breaker is equipped with feeding device, the feeding device Including blob of viscose feed bin, the feeding mouth being arranged at the top of blob of viscose feed bin, the vibrating feeder (conveyer) for being arranged on blob of viscose bin bottom, to The charging belt feeder that is fed in rubber breaker and to control the vibrating controller of vibrating feeder (conveyer) discontinuous operation;The charging skin Feed end with machine is located at below the discharging opening of the vibrating feeder (conveyer), the charging discharge end of belt feeder and entering for rubber breaker Material mouth is connected;
The distribution and conveying of blob of viscose, the distribution conveying are realized between the blob of viscose feed bin that each rubber breaker arranges by distribution conveyor Machine is that preceding belt conveyor and rear belt conveyor are provided with the top of blob of viscose feed bin, is set in the discharge end of preceding belt conveyor Two pieces of retractable valve plates are equipped with, one of valve plate is located at the top of the feeding mouth of blob of viscose feed bin, after another piece of valve plate is located at The top of the feed end of belt conveyor;The feed end of the preceding belt conveyor of blob of viscose feed bin corresponding to First rubber breaker and institute Stating butterfly selects the discharge end of machine to be connected.
3. system according to claim 1, it is characterized in that, in addition to screen centrifuge for regrading rubber powder and by rubber powder Levigate flour mill.
4. system according to claim 1, it is characterized in that, the discharge end of the output belt feeder is provided with tripper, The tripper includes two conveyer belts and the dam plate being arranged between two conveyer belts, the feed direction phase of two conveyer belts The back of the body, vibrations classifying screen is provided with the discharging end of two conveyer belts.
5. system according to claim 1, it is characterized in that, the rubber breaker includes broken Jiao Cang, is arranged on brokenly in glue storehouse Two pairs of rollers and to drive the driver of two pairs of rollers, at broken Jiao Cang top, shake the feed end of classifying screen and discharge end is provided with Dust gathering arrester, dust gathering arrester are connected by air inducing pipeline with the air inlet of deduster, and second temperature sensor is provided with air inducing pipeline With the second spray head, second spray head is connected with the second feeding spraying pump, and the second temperature sensor is controlled with the second spray The input electrical connection of device processed, the output end of the second spray controller electrically connect with the driver of the second feeding spraying pump.
6. a kind of method using junked tire producing gelatine powder under normal temperature, it is characterized in that, comprise the following steps:
A, tire is put into and cut in circle machine, mobile cutter, the tyre bead of tire both sides cut down, tyre bead centralized collection, cut away The tire of tyre bead is torn up in storehouse through tire transmission track feeding shredder;
B, the tire of tyre bead is cut away into after tearing up storehouse, and Driven by Hydraulic Cylinder pressing plate, which stretches into, tears up storehouse internal pressure ratch tire, photoelectric sensing Device detects signal and passes to sprayer controller, and sprayer controller control pump working, atomizer starts to storehouse internal spraying, At the same time, roll rotation cutting tire, cuts into blob of viscose, obtained blob of viscose selects machine to be screened into butterfly, size by tire Qualified blob of viscose enters blob of viscose feed bin in case broken glue, out-of-size blob of viscose are back to tear up in storehouse and torn up again;
C, blob of viscose is sent into rubber breaker through feeding device, and rubber powder is resolved under the friction, squeezing action in two pairs of rollers, and rubber powder passes through broken Glue motor spindle discharging opening is fallen on belt conveyer, through exporting Belt Conveying to vibrations classifying screen, in the vibration of vibrations classifying screen It is classified under sieving actoion, the rubber powder that particle diameter is less than the screen cloth mesh of vibrations classifying screen enters lower floor's slideway by screen cloth, and falls into In collecting bin, the rubber powder that particle diameter is more than the screen cloth mesh of vibrations classifying screen is stayed in above screen cloth, and is sent back to broken through return conveyer machine Continue brokenly glue in glue machine;During this, the first temperature sensor monitors rubber powder temperature in real time, when measured temperature is more than setting value When, the first spray head starts to spray water to rubber powder, after temperature is dropped to below setting value, stops water spray;
D, the rubber powder in collecting bin removes fiber into Celloco fractionator Celloco after magnetic separator removes steel wire, removes the rubber powder after fiber It is sent in rubber powder feed bin;
E, the rubber powder in rubber powder feed bin is discharged to rubber powder by the vibration discharger of rubber powder bin bottom according to setting time discontinuous operation On grading plant, the classification of rubber powder is realized.
7. according to the method for claim 6, it is characterized in that, the feeding device in the step c includes blob of viscose feed bin, set Feeding mouth at the top of blob of viscose feed bin, the vibrating feeder (conveyer) for being arranged on blob of viscose bin bottom, to being fed into rubber breaker plus Expect belt feeder and to control the vibrating controller of vibrating feeder (conveyer) discontinuous operation;The feed end of the charging belt feeder is located at Below the discharging opening of the vibrating feeder (conveyer), the discharge end of the charging belt feeder is connected with the charging aperture of rubber breaker;It is described to shake Blob of viscose in blob of viscose feed bin is discharged on charging belt feeder, feed belt feeder work by dynamic feeder according to setting time discontinuous operation Make, blob of viscose is transported in rubber breaker.
8. according to the method for claim 7, it is characterized in that, conveyed between the supporting blob of viscose feed bin of each rubber breaker by distributing Machine realizes the distribution and conveying of blob of viscose, the distribution conveyor be before being provided with the top of blob of viscose feed bin belt conveyor and after Belt conveyor, the discharge end of preceding belt conveyor is provided with two pieces of retractable valve plates, one of valve plate is located at blob of viscose The top of the feeding mouth of feed bin, another piece of valve plate are located at the top of the feed end of rear belt conveyor;First rubber breaker is supporting The feed end of preceding belt conveyor of blob of viscose feed bin select the discharge end of machine to be connected with the butterfly;
Select preceding belt conveyor of the qualified blob of viscose of machine through blob of viscose feed bin corresponding to First rubber breaker outwards to convey from butterfly, beat Valve plate corresponding with the blob of viscose feed bin feeding mouth is opened, closes valve plate corresponding with rear belt conveyor, blob of viscose falls into the blob of viscose material In storehouse, when being fed intake into the blob of viscose feed bin of second rubber breaker, valve plate corresponding with rear belt conveyor is opened, is closed another Block valve plate, the subsequent belt conveyor of blob of viscose is conveyed backward, by that analogy, realize the feeding to each blob of viscose feed bin.
9. according to the method for claim 6, it is characterized in that, in step c, the rubber breaker includes broken Jiao Cang, is arranged on brokenly Two pairs of rollers in glue storehouse and to drive the driver of two pairs of rollers, at broken Jiao Cang top, shake the feed end and discharge end of classifying screen Dust gathering arrester is provided with, dust gathering arrester is connected by air inducing pipeline with the air inlet of deduster, and the second temperature is provided with air inducing pipeline Degree sensor and the second spray head, second spray head are connected with the second feeding spraying pump, the second temperature sensor and the The input electrical connection of two spray controllers, the output end of the second spray controller and the driver electricity of the second feeding spraying pump Connection;
Second temperature sensor monitors air inducing pipeline internal temperature in real time, when measured temperature is more than setting value, the second spray head Start to spray water, after temperature is dropped to below setting value, stop water spray.
10. according to the method for claim 6, it is characterized in that, in the step e, sorted by the rubber powder grading plant The rubber powder of different stage out, centrifugation screening is carried out into screen centrifuge, qualified rubber powder is directly packed, and underproof rubber powder enters Enter after being milled in flour mill, then sieved through screen centrifuge, so circulation.
CN201711123481.5A 2017-11-14 2017-11-14 System and method for producing rubber powder at normal temperature by using waste tires Expired - Fee Related CN107813444B (en)

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Publication number Priority date Publication date Assignee Title
CN108772982A (en) * 2018-06-08 2018-11-09 国宏中晶(北京)科技发展有限公司 A kind of waste tire fine glue powder preparation facilities that granularity is controllable and method
CN109531879A (en) * 2018-12-29 2019-03-29 广州市联冠机械有限公司 A kind of broken colloid system
CN109940785A (en) * 2018-09-20 2019-06-28 湖北耐特胶业有限公司 A kind of waste tire recycling oil refining production line
CN111688070A (en) * 2020-06-30 2020-09-22 朱涛 Tire automatic processing grinds reducing mechanism

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CN204222012U (en) * 2014-10-28 2015-03-25 天津三雄科技有限公司 A kind of process units of vulcanized rubber powder
CN104526911A (en) * 2013-08-14 2015-04-22 宁夏亿能橡塑有限公司 System and method for producing environment-friendly rubber powder

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CN2721230Y (en) * 2004-08-26 2005-08-31 刘清俊 Breaker of waste tyre
CN101670625A (en) * 2009-09-28 2010-03-17 四川乐山亚联机械有限责任公司 Method for producing gelatine powder under normal temperature by using waste tires
CN104526911A (en) * 2013-08-14 2015-04-22 宁夏亿能橡塑有限公司 System and method for producing environment-friendly rubber powder
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CN108772982A (en) * 2018-06-08 2018-11-09 国宏中晶(北京)科技发展有限公司 A kind of waste tire fine glue powder preparation facilities that granularity is controllable and method
CN109940785A (en) * 2018-09-20 2019-06-28 湖北耐特胶业有限公司 A kind of waste tire recycling oil refining production line
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CN111688070A (en) * 2020-06-30 2020-09-22 朱涛 Tire automatic processing grinds reducing mechanism

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