CN106269199B - A kind of aqueous process of waste tire cracking residue - Google Patents

A kind of aqueous process of waste tire cracking residue Download PDF

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Publication number
CN106269199B
CN106269199B CN201510245965.1A CN201510245965A CN106269199B CN 106269199 B CN106269199 B CN 106269199B CN 201510245965 A CN201510245965 A CN 201510245965A CN 106269199 B CN106269199 B CN 106269199B
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seal box
spiral
waste tire
residue
water
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CN106269199A (en
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不公告发明人
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Shanghai Xinshiyuan Environmental Protection Technology Co Ltd
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Shanghai Xinshiyuan Environmental Protection Technology Co Ltd
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Abstract

The invention discloses a kind of aqueous process of waste tire cracking residue.The technique is comprised the steps of the seal box of waste tire cracking residue input inner filling water;Under the stirring propulsion for stirring propulsive mechanism;Carbon residue in the waste tire cracking residue to seal case end movement and exports;Steel wire in the waste tire cracking residue moves and assembles to seal box bottom, collects steel wire;Wherein, the operation inputted using feeding mechanism, the feeding mechanism are a binder spiral;The stirring propulsive mechanism is that a horizontally disposed stirring promotes spiral;It is full spiral, interrupted spiral or rake teeth spiral that the stirring, which promotes spiral,.Technique of the invention realizes waste tire cracking residue solid phase output and the two-phase of cracking gas phase output is effectively isolated blocking output;The totally-enclosed water law processing of automatic continuous waste tire cracking residue is realized simultaneously.

Description

A kind of aqueous process of waste tire cracking residue
Technical field
The present invention relates to a kind of aqueous process of waste tire cracking residue.
Background technique
With the continuous development of waste tire cracking process treatment process, treatment scale yield increasingly, but it is following Waste tire cracking residue output sealing and carbon residue steel wire separation problem still restrict industrialization standardization industry Development.
Since (wherein solid is residual for generation hydrocarbon gas and solid residue product after waste tire generation cracking reaction Slag product is also known as waste tire cracking residue), wherein hydrocarbon gas temperature is up to 400 DEG C or more and leaks to air It is inflammable and explosive when middle, therefore, in waste tire cracking residue output, it is necessary to stringent sealing, to prevent blocking hydrogen compound gas Body when solid residue exports " escape " to exterior space.Due to there is irregular steel wire to roll into a ball in waste tire cracking residue and Residue carbon of biomass pyrolysis, which intersects to exist, causes operating condition complicated, is different from single powder class pressing material and seals, it is difficult to pass through simple screw extrusion It realizes.And output, cooling, the separation of traditional waste tire cracking residue mostly use the single spiral equipment of septate heat transfer greatly, Such as the screw conveyor with cold water-cooling jacket, the extremely difficult waste tire cracking residue for making scale of equipment pass through single The extruding of helical blade forms closely knit material position sealing, cannot achieve waste tire cracking residue solid phase output and cracking gas phase The two of output isolate blocking output, also cannot achieve automatic continuous treatment process.Therefore present invention seek to address that tradition It is defeated to be effectively isolated blocking for the two-phase of solid phase output and cracking gas phase output after the waste tire cracking reaction that equipment cann't be solved Problem out;And traditional equipment cann't be solved waste tire cracking residue output, water-stop, cooling, washing, sieve The problem divide, being continuously conveyed.
Summary of the invention
The technical problem to be solved by the present invention is in order to overcome traditional waste tire to crack the output, cold of residue But, separation mostly uses greatly the single spiral equipment of septate heat transfer, and the extremely difficult cracking residue for making scale of equipment passes through single spiral shell The extruding of vane piece forms closely knit material sealing, cannot achieve waste tire cracking residue output and cracks gas phase output Two isolate the technical problems such as blocking output and automatic continuous treatment process, and provide a kind of waste tire cracking The aqueous process of residue.Technique of the invention realizes waste tire cracking residue solid phase output and cracking gas phase is defeated Two-phase out is effectively isolated blocking output;It is residual water-stop barrier cracking gas phase, the cracking of cooling high temperature waste tire have been completed at the same time It stays object, stirring water flotation sedimentation, material to fish for, water cycle temperature control, collect the function of handling product automatically, realizes automatically continuously Change the totally-enclosed water law processing of waste tire cracking residue.
Due to there is the steel wire of carbon residue powder and the similar knitting wool ball sample of a large amount of loose grafting in waste tire cracking residue Elastic irregular group, carbon residue have the characteristic of fluid during transportation, it is difficult to be fixed into regular shape movement.In waste tire In the input method for cracking residue, inventor is once attempted using single slow spin material envelope input method, high pressure water spray binder Method and reciprocating-piston method etc., but will form the density contrast and cavity of stock column using the envelope conveying of single slow spin material, it makes Leaked at not blanking, gas etc.;It will cause a large amount of fugitive dusts of carbon residue in waste tire cracking residue with high pressure water spray binder Water mist forms the sealing state of pipeline, causes pipeline blockage;Reciprocating-piston method is due to promoting cylinder body and conveying barrel must be there are Certain interval, the presence of steel wire keep reciprocating mechanism easily stuck by steel wire.After largely testing and studying, invent The last creative discovery of people, when the sealing that waste tire cracking residue is forced to indentation inner filling water using binder spiral After case, can be realized waste tire cracking residue output and cracking gas phase output two isolate blocking output, effectively solve The problems such as leakage of production process, completes cooling, serialization output, improves the quality of carbon residue and steel wire.
The present invention mainly solves above-mentioned technical problem by the following technical programs.
The present invention provides a kind of aqueous process of waste tire cracking residue, and it includes the following steps: will give up Old tire cracks the seal box of residue (comprising carbon residue and steel wire) input inner filling water;It is pushed away in the stirring of stirring propulsive mechanism Under;Carbon residue in the waste tire cracking residue to seal case end movement and exports;The waste tire Steel wire in cracking residue moves and assembles to seal box bottom, collects steel wire;Wherein, it is carried out using feeding mechanism The operation of input, the feeding mechanism are a binder spiral;The stirring propulsive mechanism is that a horizontally disposed stirring pushes away Into spiral;It is full spiral, interrupted spiral or rake teeth spiral that the stirring, which promotes spiral,.
The waste and old wheel that the waste tire cracking residue can obtain for the waste tire cleavage method of this field routine Tire cracks residue.The waste tire cracking residue includes carbon residue and steel wire (being made of carbon residue and steel wire).
The binder spiral can be the binder spiral of this field routine, for waste tire cracking residue to be forced pressure Enter the seal box of inner filling water, realizes the continuous input of waste tire cracking residue.The binder spiral is preferable Ground is set to one end (such as top) of the seal box.The binder spiral be preferably comprised one be fixed on it is described close Outer sleeve and one at the top of joint sealing are set to the helical blade in the outer sleeve.It will accumulation using the revolving speed pressurization of binder spiral Density is in 0.5kg/cm3The carbon residue that left and right cannot enter water sedimentation is forced in the seal box of indentation inner filling water.The binder The revolving speed of spiral is preferably greater than or is equal to 30 revs/min.The present invention is split the waste tire in a manner of forcing binder Residue is solved to force to completely attach to the waste tire cracking residue and water simultaneously It mixes rapidly.While the waste tire cracking residue and water are sufficiently mixed, water cracks high temperature waste tire residual Object is stayed to be cooled down in favor of present invention process subsequent operation.
Preferably, spiral shell can be continuously conveyed by waste tire cracking reaction equipment in the waste tire cracking residue Rotation is delivered to the feeding mechanism.
The seal box can be the seal box of this field routine, and preferably its section is rectangular or circular configuration, bottom Portion is U-type groove structure or oval type groove structure, and the U-type groove structure or oval type groove structure form a collecting tank.Described is close Joint sealing can pass through water cooling by recycling regulation of (the i.e. water internal circulation system) realization to the temperature of water in seal box in the extraction of pump The circulatory system carries out outer circulation cooling to realize the cooling and moisturizing to process water, and water temperature over-high is avoided to influence the effect of technical process Fruit.Temperature in water segregation cabin is generally required at 50 DEG C hereinafter, it is preferred that 0~50 DEG C.
Since the bulk density of carbon residue is less than 1, waste tire cracking residue is eventually suspended in the top in seal box, Therefore, the stirring propulsive mechanism is preferably located at the middle and upper part of the seal box.Preferably, the stirring propulsive mechanism Shaft be set to the seal box cabinet on, between the shaft and corresponding cabinet using sealing element seal.Described Waste tire cracking residue be entered seal box after, using stirring propulsive mechanism, break up, stir, push, further strengthen with The depth of water mixes dispersion effect;And the waste tire inside the seal box is cracked into residue from close to binder spiral sides It is transported to the screw mechanism.
The operation of the output can be the operation of this field routine, preferably be caught using discharging mechanism to carbon residue It obtains, fish for, with the operation exported.The discharging mechanism can be the discharging mechanism of undergraduate course field routine, as long as can catch It obtains, fish for carbon residue, the preferably screw mechanism of jacketed hydrophobic open cell thermo.The discharging mechanism is preferably provided In the top (i.e. the end top of seal box) of the seal box other end.In order to get rid of water as far as possible when capturing, fishing for Point, the discharging mechanism is preferably obliquely installed.The carbon residue capture through discharging mechanism, fished for, passes through the spiral shell of discharging mechanism Carbon residue is promoted to higher than other than seal case liquid level by vane piece, and water therein is then along helical blade and jacket structured outer Surface of cylinder's inboard wall clearance backflow is recycled into seal case, and the carbon residue after drainage can be used as primary cleaning product and be beaten Packet is collected and is delivered to finishing processing links.
The operation of the collection steel wire can be the operation of this field routine, as long as can collect steel wire. Waste tire cracks flotation sedimentation in water after residue input seal box, and the carbon residue that density is less than water is finally suspended in the water surface, Steel wire of the density greater than 1 sinks to seal box bottom.
Generally, the feeding mechanism, the discharging mechanism and the stirring propulsive mechanism drive preferably by one The work of motivation structure.The driving mechanism is preferably external electric motor.
In a preferred embodiment of the present invention, a water segregation cabin can be also connected on the side wall of the seal box exit side; The seal box and the top in the water segregation cabin are mutually isolated, and bottom passes through a connection mouth connection.Therefore, described Seal box and the water segregation cabin are generally the Communicating device structure of bottom connection, to strengthen the isolation of purified effect of carbon residue and steel wire Fruit.The water segregation cabin is preferably single wall incline structure.
Preferably, the side wall of the exit side of the seal box is by the top of the seal box and the water segregation cabin Isolation, the connection mouth are set to the bottom of the side wall of the seal box exit side.Using the exit side side wall of seal box as The mechanism on obstruction seals case and water compartment top can effectively simplify the structure that separating device is selected in entire washing, be allowed to more compact, The effective length for reducing connection mouth simultaneously, avoids steel wire from blocking.
Preferably, the top of the seal box is lower than the opening in the water segregation cabin, the water in the water segregation cabin Water surface elevation in face height and the seal box maintains an equal level.
Preferably, the waste tire cracks the steel wire in residue from seal box bottom under the push of delivery device Portion enters water segregation cabin;The delivery device is located in the U-type groove or oval type groove of seal box bottom.The delivery device It can be the delivery device of this field routine, preferably one is horizontally set on the push spiral of the seal box bottom.It is described Push spiral be preferably full spiral or shaftless screw.The starting point of the delivery device is located at the pressure of the seal box Expect the side wall of spiral sides, the end end of the delivery device is located at the side wall of the exit side of the seal box, and close to the connection At mouthful.The delivery device is preferably located in the collecting tank, and collecting tank collects the steel wire for being sunken to seal box bottom To delivery device, the transport rate of delivery device is improved.
Preferably, the steel wire is lifted out water segregation cabin using discharging hoisting mechanism.The discharging hoisting mechanism Preferably jacket structured spiral or belt elevator.The operation for being lifted out water segregation cabin can be the behaviour of this field routine Make, the steel wire is preferably lifted out water segregation using jacket structured spiral or belt lifting drainage mechanism, and portion is i.e. out of my cabin It can.The water segregation cabin can be realized by recycling (i.e. water internal circulation system) in the extraction of pump to the temperature of water segregation cabin water Regulation carries out outer circulation cooling by water-cooling circulating system to realize the cooling and moisturizing to process water, avoids water temperature over-high shadow Ring the effect of technical process.Temperature in water segregation cabin is generally required at 50 DEG C hereinafter, it is preferred that 0~50 DEG C.
Preferably, the starting point of the discharging hoisting mechanism is located at the connection passage port, the discharging elevator The end end of structure is located at the outlet in the water segregation cabin.The starting point, which is located at connection passage port, will can be pushed in time to water compartment Steel wire transport, avoid steel wire connection passage port obstruction, hinder the output of subsequent steel wire.
The discharging hoisting mechanism is preferably a material copy belt.Preferably, the starting point of the material copy belt is set to institute The exit side in the water segregation cabin stated is simultaneously adjacent with the connection mouth, and the end end of the material copy belt is set to opening for the water segregation cabin At mouthful.
It is driven preferably, the delivery device and the discharging hoisting mechanism pass through an external driving mechanism respectively It is dynamic.The driving mechanism is preferably external electric motor.
Preferably, the stirring propulsive mechanism, the discharging mechanism, the propulsive mechanism, the discharging mention The revolving speed for rising mechanism can be not especially limited, but material accumulation in order to prevent, revolving speed are typically greater than or equal to binder spiral Revolving speed, i.e., the revolving speed of above-mentioned each mechanism is typically greater than or equal to 30 revs/min.
In a preferred embodiment of the present invention, the feeding mechanism, the seal box, the stirring propulsive mechanism A waste tire, which is formed, with the discharging mechanism cracks residue sealed conveying device.Residue is cracked according to waste tire Sealed conveying device carries out aqueous process of the invention, when the height that the steel wire of seal box bottom is assembled is promoted close to stirring When mechanism, steel wire is collected in the operation of arrestment.
In a preferred embodiment of the present invention, the seal box, the delivery device, the discharging hoisting mechanism Separating device is selected in the washing for forming waste tire cracking residue with the water segregation cabin.
Preferably, the waste tire cracking residue sealed conveying device and the waste tire crack residue Washing select separating device to collectively constitute device used in the aqueous process of waste tire of the present invention cracking residue.
In the present invention, the feeding mechanism, the seal box, the stirring propulsive mechanism, the discharging machine Structure, the delivery device, the discharging hoisting mechanism and the water segregation cabin model, size and specification can be according to need The amount of waste tire cracking residue to be processed carries out conventional selection.In treatment process of the invention, waste tire cracking is residual Stay the treating capacity of object generally in 500kg/h~600kg/h.
Due to different manufacturers or the tire of different model, containGlueAmount and steel wire amount also can be different, therefore, this hair The carbon left and steel wire amount that bright treatment process finally obtains can not also be characterized with specific numberical range.If waste tire In, the mass ratio of gel content and steel wire amount is 7:3, then the useless wheel tire pyrolysis residue obtained after cracking is through technique of the invention After processing, the mass ratio of obtained carbon residue and steel wire is 7:1;If gel content and steel wire amount are 6.5:3.5 in waste tire, split After process of the invention, the mass ratio of obtained carbon residue and steel wire is the useless wheel tire pyrolysis residue obtained after solution 6.5:3.5, it is seen that technique of the invention can be realized 100% separation of carbon residue and steel wire.
The present invention also provides a kind of device for the waste tire cracking residue aqueous process, packets It has included:
The seal box of one inner filling water;
One is set to described seal box one end, for inputting the feeding mechanism of waste tire cracking residue;
One is set to the top of the seal box other end, for exporting carbon residue in the waste tire cracking residue Discharging mechanism;
One is set to inside the seal box, for by the carbon residue in the solution residue inside the seal box from close The feeding mechanism side is transported to the stirring propulsive mechanism of the discharging mechanism;And at least one is described for driving The driving mechanism of feeding mechanism, the discharging mechanism and the stirring propulsive mechanism work.
In the present invention one preferably embodiment, it is adjacent in the exit side of the seal box equipped with a water segregation cabin, And the seal box and the top in the water segregation cabin are mutually isolated;The bottom in the water segregation cabin and the sealing The bottom of case passes through a connection mouth connection;
A delivery device for being located at bottom is additionally provided in the seal box, the starting point of the delivery device is located at institute The side wall of the feed side for the seal box stated, the end end of the delivery device are located at the side of the exit side of the seal box Wall, and close to the connection passage port;
A discharging hoisting mechanism is equipped in the water segregation cabin;The top of the seal box is lower than the water segregation The opening in cabin, the water surface elevation in water surface elevation and the seal box in the water segregation cabin maintain an equal level;And
At least one is used to drive the driving mechanism of the propulsive mechanism and the discharging hoisting mechanism work.
Wherein, the section of the seal box is preferably rectangular or circular configuration, and bottom is preferably U-type groove structure Or oval type groove structure, so as to form a collecting tank.
Wherein, the feeding mechanism is preferably a binder spiral.It is fixed that the binder spiral is preferably comprised one Outer sleeve and one at the top of the seal box are set to the helical blade in the outer sleeve.Spiral can be utilized using binder spiral Revolving speed pressurization overcomes water to the buoyancy of waste tire cracking residue, and waste tire cracking residue is made to be forced into water In.The revolving speed of the binder spiral is typically greater than or equal to 30 revs/min.
Wherein, the discharging mechanism is preferably a screw mechanism, the more preferably spiral shell for jacketed hydrophobic open cell thermo Revolve mechanism.The screw mechanism is preferably obliquely installed.
Wherein, the stirring propulsive mechanism is preferably a horizontally disposed stirring and promotes spiral.It is promoted using stirring Spiral can play the role of breaing up waste tire cracking residue, can substantially more cool down in water, then Xiang Mi again The output mechanism of joint sealing transports.On the cabinet that the stirring promotes the shaft of spiral to be preferably set to the seal box, institute It states and is sealed between shaft and corresponding cabinet using sealing element.The stirring promotes spiral to be preferably located at the seal box Middle and upper part.The stirring promotes spiral to be preferably full spiral, interrupted spiral or rake teeth spiral.The discharging mechanism Preferably it is set to the side that the stirring promotes spiral.
Wherein, the delivery device is preferably a push spiral for being horizontally set on the seal box bottom.Compared with Goodly, the starting point of the push spiral is set to the side wall of the feed side of the seal box, and it is close that the end end of the push spiral is set to this The side wall of the exit side of joint sealing is simultaneously adjacent with the connection mouth.The delivery device is preferably located in the collecting tank, is received Collection slot collects the steel wire for being sunken to seal box bottom to delivery device, improves the transport rate of delivery device.
Wherein, described preferably, the side wall of the exit side of the seal box is by the upper isolation of the seal box and the water compartment Connection mouth is set to the bottom of the side wall of the seal box exit side.Using the exit side side wall of seal box as obstruction seals case and water The mechanism on compartment top can effectively simplify the structure that separating device is selected in entire washing, be allowed to more compact, that completes seal box has Effect sealing.
Wherein, preferably, the starting point of the discharging hoisting mechanism is located at the connection passage port, the discharging is mentioned The end end for rising mechanism is located at the outlet in the water segregation cabin.The starting point, which is located at connection passage port, will to be pushed in time to water The steel wire of compartment is transported, and is avoided steel wire in connection passage port obstruction, is hindered the output of subsequent steel wire.Wherein, the discharging hoisting mechanism A preferably material copy belt.Preferably, the starting point of the material copy belt be set to the seal box exit side and with the connection mouth Adjacent, the end end of the material copy belt is set to the exit in the water segregation cabin.
Wherein, the driving mechanism is preferably external electric motor.
Without prejudice to the field on the basis of common sense, above-mentioned each optimum condition, can any combination to get the present invention it is each preferably Example.
The positive effect of the present invention is that:
1, material position can not be formed when treatment process of the invention solves original screw conveyor steel conveying carbon residue The problem of sealing blocks the connection of Pintsch process reaction unit and air by seal box, completes waste tire cracking residual The purpose that object stirs in water-filled seal box, cools down, transports, efficiently solves the leakage problem of production process, completes Cooling, serialization output, improves the quality of carbon residue and steel wire.
2, technique of the invention utilizes the close of two kinds of different materials of carbon residue and steel wire by the method for automation washing sedimentation Waste tire is cracked the steel wire of carbon residue of the residue flotation settled density less than 1 and density greater than 1 in water by degree difference, in order to Effectively recycling steel wire, reduces equipment cost, improves product yield, protects environment.
3, technique of the invention completes water-stop barrier cracking gas phase, cooling high temperature waste tire cracking residue, stirs Mix water flotation sedimentation, material is fished for, water cycle temperature control, the automatic function of collecting processing product.
4, in the steel wire that technique of the invention obtains without carbon residue, without steel wire in carbon residue, the separation rate of steel wire and carbon residue is reachable To 100%.
Detailed description of the invention
Fig. 1 is the partial sectional view that waste tire cracks residue sealed conveying device in embodiment 1.
Fig. 2 is that separating device schematic diagram of internal structure is selected in the washing that waste tire cracks residue in embodiment 2.
Fig. 3 is the structure of the exit side for the seal box that separating device is selected in the washing that waste tire cracks residue in embodiment 2 Schematic diagram.
Fig. 4 is the schematic diagram of internal structure that waste tire cracks residue water law processing unit in embodiment 3.
Fig. 5 is the process flow chart of embodiment 3.
Specific embodiment
The present invention is further illustrated below by the mode of embodiment, but does not therefore limit the present invention to the reality It applies among a range.In the following examples, the experimental methods for specific conditions are not specified, according to conventional methods and conditions, or according to quotient The selection of product specification.
Embodiment 1
As shown in Figure 1, the waste tire cracking residue sealed conveying device in the present embodiment includes a seal box 1, Water (not shown) is filled in the inside of seal box 1.
The front end of the seal box 1 is equipped with a binder spiral 2 as feeding mechanism, which includes an outer sleeve 21 and blade 22.Wherein one end of outer sleeve 21 is fixed on the top of seal box 1, the discharge port of the other end and cracking reaction device Connect (not shown).The binder spiral 2 passes through external electrical motor driven.Due to the weight of waste tire cracking residue Relatively light, in order to effectively be pressed into seal box, the revolving speed of the binder spiral 2 is greater than or equal to 30 revs/min.
It is equipped with a discharging mechanism, the i.e. screw mechanism 4 of jacketed hydrophobic open cell thermo in the tail end of seal box 1, for catching Obtain, fish for waste tire cracking residue in carbon residue;One end of the outer sleeve of the screw mechanism 4 is fixed on the tail of seal box 1 Portion.Wherein, in order to get rid of moisture as far as possible when capturing, fishing for, the shaft of the screw mechanism 4 is tilted relative to the seal box 1 Setting, i.e. the outer sleeve opposing seal case 1 of screw mechanism 4 are inclined to set, thus when screw mechanism 4 comes up carbon residue extraction When, moisture is then out of, clearance backflow to seal box 1 between the outer sleeve and blade of screw mechanism 4.
In the inside of seal box 1, setting one is for the waste tire cracking residue entered inside seal box 1 to be transported to Stirring propulsive mechanism at screw mechanism 4.It is sufficiently cold in water body in order to reach waste tire cracking residue in the present embodiment But purpose promotes spiral 3 as the stirring propulsive mechanism using stirring.As shown in Figure 1, stirring promotes turning for spiral 3 Axis is horizontally placed on inside seal box 1, and the both ends of shaft wear out the cabinet of seal box 1.It is arranged between shaft and cabinet There is sealing mechanism (not shown).One end of shaft is connect with another electric motor (not shown).
Since the bulk density of carbon residue is less than 1, waste tire cracking residue is eventually suspended in the top in seal box 1 Portion, therefore stirring propulsion spiral 3 is set to the middle and upper part of the seal box 1.And it more smooth can be obtained for the ease of screw mechanism 4 Carbon residue is fished for into out seal box 1, the side that stirring promotes 3 one end of spiral is arranged in screw mechanism 4.
The sealed conveying device can not form material position sealing when solving original screw conveyor steel conveying carbon residue Problem, by seal box block Pintsch process reaction unit and air connection, complete waste tire cracking residue exist It is stirred in the seal box of inner filling water, is cooling, transport purpose, efficiently solved the leakage problem of production process, complete Cooling, serialization output, improves the quality of carbon residue and steel wire.
Embodiment 2
As shown in Figures 2 and 3, it includes a seal box that separating device is selected in the washing of the waste tire cracking residue in the present embodiment 1, binder spiral 2 of the top setting one of the feed side of seal box 1 as feeding mechanism.The binder spiral 2 includes an outer sleeve 21 and blade 22.Wherein one end of outer sleeve 21 is fixed on the top of seal box 1, the discharge port of the other end and cracking reaction device Connect (not shown).A water segregation cabin 5 is equipped in the exit side of seal box 1.Water segregation cabin 5 is adjacent with seal box 1, the sealing The side plate of the exit side of case 1 plays compartmentation, by the upper isolation in water segregation cabin 5 and seal box 1.In the bottom of the side plate 51 Equipped with a connection mouth 6, so that seal box 1 and water segregation cabin 5 become a Communicating device.Wherein, the top of seal box 1 is lower than water The opening of cofferdam 5.
In the inside of seal box 1 by having a push spiral 7 as delivery device, the shaft 71 of the push spiral 7 Starting point the feed side of seal box 1 is set, end end is arranged on the side plate 51 of 1 exit side of seal box and close to connection mouth 6.The push spiral 7 passes through external electrical motor driven.
A material copy belt 8 as discharging mechanism is equipped in water segregation cabin 5.The starting point of the material copy belt 8 and connection Mouth 6 is adjacent, and the end end of material copy belt 8 is set to the opening in water segregation cabin 5.In order to further be separated when transporting steel wire Steel wire and moisture, 8 relative level of material copy belt is at being obliquely installed.The material copy belt 8 passes through external electrical motor driven.
In addition, the top of seal box 1 is rectangle, the collecting tank for the U-shaped that one inwardly collapses is formed at the lower part of seal box 1, To which the steel wire that guidance is sunken to 1 bottom of seal box is gathered to push spiral 7, it is readily transported.May be used also the cross section of the collecting tank For semiellipse type.
The material of the steel wire containing residue carbon of biomass pyrolysis is admitted to after seal box 1 sedimentation of flotation in water by binder spiral 2, and density is small It is finally suspended in the water surface in the carbon residue of water, steel wire of the density greater than 1 sinks to 1 bottom of seal box, collects aggregation by push spiral 7 Steel wire in collecting tank and 6 water segregation cabin of connection mouth, 5 direction for crossing 51 bottom of side wall pushes, side plate 51 blocks seal box 1 With the connection on 5 top of water segregation cabin, the carbon residue positioned at 1 top of seal box will not enter in water segregation cabin 5, to make water segregation cabin Water purification state is kept in 5, avoids carbon residue pollution.The steel wire for being gathered in water segregation cabin 5 is promoted by the revolution of material copy belt 8, The separation output that output to water compartment 5 completes steel wire is promoted after filtering out moisture.
The wet concentration selects separating device that can act on by the flotation of water and is automatically separated residue carbon of biomass pyrolysis and steel wire, has prevented traditional magnetic Optional equipment separation is not thorough and the problem of dust pollution.In addition, the washing selects separating device to pass through the method for automation washing sedimentation Using the density contrast of two kinds of different materials of carbon residue and steel wire in water by waste tire cracking residue flotation settled density less than 1 Carbon residue and density be greater than 1 steel wire and reduce equipment cost in order to effectively recycle steel wire, improve product yield, protection ring Border.
Embodiment 3
Examples 1 and 2 collectively constitute 3 waste tire of embodiment cracking residue aqueous process use device, specifically Fig. 4 is seen, wherein the meaning that each appended drawing reference indicates is identical as Examples 1 and 2.Water law processing of the invention is carried out using the device Technique.Concrete technology flow process is as follows:
The waste tire cracking residue that cracking reaction equipment continuously exports is delivered to feeder by the way that spiral is continuously conveyed Structure is pressurizeed by the revolving speed of binder spiral, and waste tire cracking residue is forced indentation 1L or more in a manner of forcing binder Complete water-filled seal box, wherein the revolving speed of binder spiral is 30 revs/min.Waste tire cracks residue and enters full of water Airtight water tank after, under the action of water, cooling, the stirring propulsive mechanism of feeding mechanism side-lower cracks waste tire at this time (stirring conveying) is broken up, stirred, being pushed to residue, is further strengthened and is mixed dispersion effect with the depth of water.Waste tire The carbon residue in residue is cracked to seal case end movement, the discharging mechanism capture of seal case end is arranged at, fishes for, By being promoted to higher than other than seal case liquid level for the helical blade of discharging mechanism, the water in carbon residue is then along helical blade It is recycled with cylinder clearance backflow into seal case, the carbon residue after drainage is exported and produced outside apparatus of the present invention as primary washing Product carry out collecting and baling and are delivered to finishing processing links, remain in the carbon residue finally obtained without steel wire.Waste tire cracking is residual It stays the steel wire in object gradually to collect to seal box sedimentation under mechanical stirring and waterpower settlement action, is being located at seal box bottom U Delivery device in type groove enters water segregation cabin under pushing, and steel wire is gone out by the discharging hoisting mechanism continuance lifting in water segregation cabin Water segregation portion and is collected out of my cabin, and gained steel wire is remained without carbon residue.
Wherein, stir propulsive mechanism, discharging mechanism, propulsive mechanism, discharge hoisting mechanism revolving speed can be not especially limited, But material accumulation, revolving speed are typically equal to or greater than the revolving speed of binder spiral, i.e., the revolving speed one of above-mentioned each mechanism in order to prevent As be greater than or equal to 30 revs/min.
Wherein, circulation in the extraction that seal box and water segregation cabin pass through pump, i.e. water internal circulation system are realized in seal box Water in the regulation of coolant-temperature gage, seal box or water segregation cabin carries out outer circulation cooling by water-cooling circulating system to realize to technique The cooling and moisturizing of water avoid water temperature over-high from influencing the effect of technical process, generally, it is desirable that seal box and water segregation cabin Zhong Shui Temperature at 50 DEG C or less.
The technique of the present embodiment, which realizes waste tire cracking residue solid phase output and the two-phase of cracking gas phase output, to be had Effect isolation blocks output, prevents gas from escaping, highly-safe;It is useless water-stop barrier cracking gas phase, cooling high temperature have been completed at the same time Old tire cracking residue, stirring water flotation sedimentation, material are fished for, water cycle temperature control, collect the function of handling product automatically.
The device as used in aqueous process in this present embodiment can realize the requirement of continuous production, can be to useless Old tire cracks residue and carries out batch processing, and the waste tire cracking residue inlet amount process range into seal box can be with FromFeather weight is clipped to tonne not.For the present embodiment by adjusting to each mechanism model, specification and size, waste tire cracks residue Treating capacity be generally 600kg/h.
Embodiment 4
Aqueous process of the invention is carried out using the waste tire cracking residue sealed conveying device of embodiment 1. Concrete technology flow process is as follows:
The waste tire cracking residue that cracking reaction equipment continuously exports is delivered to feeder by the way that spiral is continuously conveyed Structure is pressurizeed by the revolving speed of binder spiral, and waste tire cracking residue is forced indentation 1L or more in a manner of forcing binder Complete water-filled seal box, wherein the revolving speed of binder spiral be 30 revs/min.Waste tire cracking residue, which enters, to be full of After the airtight water tank of water, under the action of water, cooling, the stirring propulsive mechanism of feeding mechanism side-lower splits waste tire at this time (stirring conveying) is broken up, stirred, being pushed to solution residue, is further strengthened and is mixed dispersion effect with the depth of water.Waste and old wheel Tire cracks the carbon residue in residue to seal case end movement, is arranged at discharging mechanism capture, the fishing of seal case end It takes, by being promoted to higher than other than seal case liquid level for the helical blade of discharging mechanism, the water in carbon residue is then along spiral Blade is recycled with cylinder clearance backflow into seal case, and the carbon residue after drainage, which exports, to be washed outside apparatus of the present invention as primary It washs product progress collecting and baling and is delivered to finishing processing links.Waste tire crack the steel wire in residue in mechanical stirring and Gradually collect to seal box sedimentation under waterpower settlement action, when the close stirring pusher of height that the steel wire of seal box bottom is assembled When structure, steel wire is collected in the operation of arrestment.
Wherein, stir propulsive mechanism, the revolving speed of discharging mechanism can be not especially limited, but material accumulation in order to prevent, Its revolving speed is typically greater than or equal to the revolving speed of binder spiral, i.e., the revolving speed of above-mentioned each mechanism is typically greater than or equal to 30 revs/min.
Wherein, circulation in the extraction that seal box passes through pump, i.e. water internal circulation system realize the tune to coolant-temperature gage in seal box It controls, the water in seal box carries out outer circulation cooling by water-cooling circulating system to realize the cooling and moisturizing to process water, avoids Water temperature over-high influences the effect of technical process, generally, it is desirable that the temperature of water is at 50 DEG C or less in seal box.
The treatment process of the present embodiment can not form material position when solving original screw conveyor steel conveying carbon residue The problem of sealing blocks the connection of Pintsch process reaction unit and air by seal box, completes waste tire cracking residual Object stirring, cooling, transport purpose in internal water-filled seal box, efficiently solve the leakage problem of production process, complete It is exported at cooling, serialization, obtained steel wire without steel wire in carbon residue, improves the quality of carbon residue and steel wire without carbon residue.
For the present embodiment by adjusting to each mechanism model, specification and size, waste tire cracks the treating capacity one of residue As be 500kg/h.

Claims (10)

1. a kind of aqueous process of waste tire cracking residue, which is characterized in that it includes the following steps: by waste and old wheel Tire cracks the seal box of residue input inner filling water;In the case where the stirring of stirring propulsive mechanism promotes;The waste tire Carbon residue in cracking residue to seal case end movement and exports;Steel wire in the described waste tire cracking residue to Seal box bottom moves and assembles, and collects steel wire;Wherein, the operation inputted using feeding mechanism, the feeding Mechanism is a binder spiral;The stirring propulsive mechanism is that a horizontally disposed stirring promotes spiral;The stirring promotes Spiral is full spiral, interrupted spiral or rake teeth spiral;A water segregation can be also connected on the side wall of the seal box exit side Cabin;The seal box and the top in the water segregation cabin are mutually isolated, and bottom passes through a connection mouth connection;In pusher Under the push of structure, the steel wire in the waste tire cracking residue enters water segregation cabin from seal box bottom;Described pushes away Mechanism is sent to be located in the U-type groove or oval type groove of seal box bottom;The starting point of the delivery device is located at the sealing The side wall of the binder spiral sides of case, the end end of the delivery device are located at the side wall of the exit side of the seal box, and close The connection passage port.
2. treatment process as described in claim 1, which is characterized in that the binder spiral is set to the seal box One end, for waste tire cracking residue to be forced to the seal box of indentation inner filling water;The binder spiral includes one It is fixed on the outer sleeve at the top of the seal box and a helical blade in the outer sleeve;And/or the pressure Expect that the revolving speed of spiral is greater than or equal to 30 revs/min.
3. treatment process as described in claim 1, which is characterized in that the section of the seal box is rectangular or round knot Structure.
4. treatment process as described in claim 1, which is characterized in that the stirring propulsive mechanism is located at the seal box Middle and upper part;And/or the shaft of the described stirring propulsive mechanism is set on the cabinet of the seal box, the shaft with it is right It is sealed between the cabinet answered using sealing element.
5. treatment process as described in claim 1, which is characterized in that carbon residue is captured using discharging mechanism, is fished for, with The operation exported;The discharging mechanism is the screw mechanism of jacketed hydrophobic open cell thermo;The discharging mechanism is set It is placed in the top of the seal box other end;And/or the discharging mechanism is to be obliquely installed.
6. treatment process as claimed in claim 5, which is characterized in that the water segregation cabin is single wall incline structure;It is described Seal box exit side side wall by the upper isolation of the seal box and the water segregation cabin, the connection mouth is set to The bottom of the side wall of the seal box exit side;The top of the seal box is lower than the opening in the water segregation cabin, institute Water surface elevation in the water surface elevation in the water segregation cabin stated and the seal box maintains an equal level.
7. treatment process as claimed in claim 6, which is characterized in that the delivery device be one be horizontally set on it is described The push spiral of seal box bottom;The push spiral is full spiral or shaftless screw.
8. treatment process as claimed in claim 7, which is characterized in that be lifted out the steel wire using discharging hoisting mechanism The operation of water segregation cabin progress steel wire collection;The starting point of the discharging hoisting mechanism is located at the connection passage port, described The end end of discharging hoisting mechanism be located at the outlet in the water segregation cabin;The discharging hoisting mechanism is jacket structured spiral shell Rotation or belt elevator.
9. treatment process as claimed in claim 8, which is characterized in that the discharging hoisting mechanism is a material copy belt, institute The starting point for the material copy belt stated is set to the exit side in the water segregation cabin and the material copy adjacent, described with the connection mouth The end end of belt is set to the opening in the water segregation cabin.
10. treatment process as claimed in claim 8, which is characterized in that the feeding mechanism, the discharging mechanism, described Stirring propulsive mechanism, the delivery device and the discharging hoisting mechanism pass through an external driving mechanism driving respectively; The driving mechanism is external electric motor.
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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11253833A (en) * 1998-03-12 1999-09-21 Shimizu Corp Separation of contaminant and washing device
CN2887444Y (en) * 2005-11-07 2007-04-11 黄琼瑶 Floatation tank for plastic sheet recovery
JP2008012528A (en) * 2006-06-05 2008-01-24 Santekku:Kk Gravity separation type waste recovery apparatus and gravity separation type waste recovery method
CN201094927Y (en) * 2007-07-30 2008-08-06 欧哲文 Flotation washer
CN201260983Y (en) * 2008-09-17 2009-06-24 北京德通化纤工业有限公司 Flotation machine for waste plastic sheet material
TW201043338A (en) * 2009-06-03 2010-12-16 Jia-Shin Chen Density sieve machine for waste articles
CN201873554U (en) * 2010-11-23 2011-06-22 浙江省环境保护科学设计研究院 Air stripping-type oil-water separation device
CN203409919U (en) * 2013-07-22 2014-01-29 厦门绿洲环保产业股份有限公司 Hydraulic cleaning and sorting machine for plastic garbage
CN104552659A (en) * 2015-01-13 2015-04-29 宁波市阳光汽车配件有限公司 Buoyancy separation device for automobile non-metal smashed waste

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11253833A (en) * 1998-03-12 1999-09-21 Shimizu Corp Separation of contaminant and washing device
CN2887444Y (en) * 2005-11-07 2007-04-11 黄琼瑶 Floatation tank for plastic sheet recovery
JP2008012528A (en) * 2006-06-05 2008-01-24 Santekku:Kk Gravity separation type waste recovery apparatus and gravity separation type waste recovery method
CN201094927Y (en) * 2007-07-30 2008-08-06 欧哲文 Flotation washer
CN201260983Y (en) * 2008-09-17 2009-06-24 北京德通化纤工业有限公司 Flotation machine for waste plastic sheet material
TW201043338A (en) * 2009-06-03 2010-12-16 Jia-Shin Chen Density sieve machine for waste articles
CN201873554U (en) * 2010-11-23 2011-06-22 浙江省环境保护科学设计研究院 Air stripping-type oil-water separation device
CN203409919U (en) * 2013-07-22 2014-01-29 厦门绿洲环保产业股份有限公司 Hydraulic cleaning and sorting machine for plastic garbage
CN104552659A (en) * 2015-01-13 2015-04-29 宁波市阳光汽车配件有限公司 Buoyancy separation device for automobile non-metal smashed waste

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