CN209060847U - Regnerated rubber powder processing vulcanizing treatment equipment - Google Patents
Regnerated rubber powder processing vulcanizing treatment equipment Download PDFInfo
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- CN209060847U CN209060847U CN201821598170.4U CN201821598170U CN209060847U CN 209060847 U CN209060847 U CN 209060847U CN 201821598170 U CN201821598170 U CN 201821598170U CN 209060847 U CN209060847 U CN 209060847U
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Abstract
The utility model relates to reclaimed rubber fields, in particular to regnerated rubber powder processing vulcanizing treatment equipment, including tower body, the intracorporal spray equipment of tower and packing layer, the spray equipment is located above packing layer, conical pipe is additionally provided in the tower body, the tower body bottom is equipped with air inlet, exhaust outlet is equipped at the top of the tower body, the taper bottom of the tube face air inlet, the tube wall of the conical pipe is equipped with mesh, the taper tube outer surface is fixed with helical blade, the helical blade is equipped with several through-holes, the spray equipment includes the hollow pipe of spray cylinder and rotation, the spray cylinder is fixedly connected on hollow pipe, the spray cylinder bottom is equipped with several weepers, the bottom of the spray cylinder is equipped with several stirring pipes.Inefficiency when the utility model is to solve the problems, such as to handle sulfide in the prior art.
Description
Technical field
The utility model relates to reclaimed rubber fields, specifically disclose regnerated rubber powder processing vulcanizing treatment equipment.
Background technique
In the treatment process of the reclaiming rubber powder of waste tire, the rubber after needing to vulcanize carries out desulfuration operations
Could normal use, but the flue gas containing a large amount of sulfide can be generated in sweetening process, if not to the flue gas of sulfur compound
It processing, then sulfide is dispersed into air, is on the one hand detrimental to health, pollution on the other hand is also resulted in atmospheric environment,
It thus needs to design a kind of vulcanizing treatment equipment, sulfide is absorbed and converted.
The prior art, which mostly uses, sprays filled mode progress sulphur removal operation, but due to the suction-operated of filler, often
The lye that will lead to a large amount of not desulphurations is adsorbed on filler outer surface, reduces sulfur removal effectiveness, or even due to sulfide, flue dust
Complexing action mechanism cause filler to agglomerate, gas treatment ability decline.
In addition, spray liquid is sprayed from top to bottom, and flue gas rises from the bottom up because density ratio air is small, and the two is mutual
When the harmful substances such as sulphide removal are gone in contact, because spray liquid directly falls under the effect of gravity, falling speed is fast, the speed of both
Spend contrary, thus the contact area of the two is small, handles the inefficiency of sulfide.
Utility model content
The utility model is intended to provide regnerated rubber powder processing vulcanizing treatment equipment, to solve to handle sulphur in the prior art
When compound the problem of inefficiency.
In order to achieve the above object, the embodiment of the utility model are as follows:
Regnerated rubber powder processing vulcanizing treatment equipment, including the intracorporal spray equipment of tower body, tower and packing layer, the spray
Shower device is located above packing layer, and conical pipe is additionally provided in the tower body, and the bottom of the tower body is equipped with air inlet, the tower body
Top be equipped with exhaust outlet, the taper bottom of the tube face air inlet, the tube wall of the conical pipe is equipped with mesh, the taper
The outer surface of pipe is fixed with helical blade, and the helical blade is equipped with several through-holes, and the spray equipment includes spray cylinder
With the hollow pipe of rotation, the spray cylinder is fixedly connected on hollow pipe, if the spray cylinder bottom be equipped with several weepers and
Dry stirring pipe.
Flue gas containing sulfide is entered in conical pipe by air inlet, because the tube wall of conical pipe is equipped with mesh, because
And flue gas is dispersed in inside tower body through mesh, and the helical blade being cased with outside conical pipe prevents flue gas from rising directly up,
And must be raised above along spiral-shaped, or rise through the big through-hole of helical blade, reduce the speed of flue gas rising.
While flue gas rises, spray liquid passes through hollow pipe and spray cylinder, then equably by the weeper on spray cylinder
It trickles down on packing layer.
Under the through-hole for equably falling on helical blade down through the spray liquid of packing layer, and passing through helical blade continues
It falls, the flue gas in spray liquid dropping process between helical blade is in contact, and spray liquid inhales the sulfide in flue gas
It receives, realizes to the initial absorption of sulfide, and when flue gas continues to rise to packing layer, the sulfide in flue gas is again by packing layer
Filler material, which absorbs, carries out double absorption.
The case where being sprayed in compared with the prior art only with spray equipment has the advantages that
First, when flue gas passes through conical pipe, flue gas reaches between helical blade through mesh, the ascending path of flue gas by into
Ramping when entering conical pipe becomes the rising of spiraling along helical blade, while flue gas ascending path changes, cigarette
The speed that gas rises slows down, and increases the time of contact of flue gas and packing layer and spray liquid, thus the contact area of the two obtains
It improves.
Second, spray liquid does primary absorption to flue gas, and packing layer does double absorption to flue gas, and classification absorbs so that in flue gas
Sulfide more fully absorbed, further improve the absorbed ratio of sulfide in flue gas.
The presence of stirring pipe rotates stirring pipe with the rotation of spray cylinder, on the one hand, stirring pipe is rotated filler
Layer carries out constantly overturning agitation, so that not being able to give full play to the absorption to sulfide in flue gas with the packing layer of smoke contacts
Effect；On the other hand, the presence of stirring, but also the lye that filler layer surface is adsorbed is removed, compared with the prior art
Middle filler is easy the case where agglomeration, and the packing layer for being constantly reversed stirring avoids agglomeration and causes to absorb the reduction of sulfide function
The case where.
It further, further include atomising device, the atomising device includes several water vats being obliquely installed, and the water vat is located at
Between helical blade, the water vat bottom is equipped with several reverse taper holes, and the water vat inner wall slidably connects piston, far from water vat
Piston rod is fixedly connected on the piston of bottom side.
In water vat be equipped with spray liquid, when being compressed by piston and piston rod to the volume in water vat, spray liquid from
Sprayed in the reverse taper hole of water vat bottom, because the pyramidal structure of reverse taper hole makes spray liquid in high speed ejection, spray liquid with
Mist sprays, and parabolically type falls the spray liquid of ejection.
On the one hand, the spray liquid of aerosol type compared with the prior art in drops spray liquid, spraying spray liquid and flue gas
Contact area it is bigger, be more advantageous to the absorption of sulfide in flue gas；On the other hand, the water vat being obliquely installed, so that spray
The fall trajectory of misty spray liquid be parabola fall, compared with the prior art in by gravity fall the case where, parabolic
Spray liquid and flue gas ascending path formation intersects, further increase the two contact area, be conducive to sulfide in flue gas
It absorbs.
Further, the stirring pipe side wall is provided with several water dumping holes.So that spray liquid is entered by the water dumping hole of stirring pipe
Into packing layer, and the stirring pipe rotated, so that radial spray of the spray liquid come out from water dumping hole along rotation hollow pipe, it should
The spray liquid path that jet path comes out with the weeper being equipped with from spray cylinder bottom is intersected, so that packing layer is uniform by spray liquid
It drenches.
The presence of stirring pipe rotates stirring pipe with the rotation of spray cylinder, on the one hand, stirring pipe is rotated filler
Layer carries out constantly overturning agitation, so that not being able to give full play to the absorption to sulfide in flue gas with the packing layer of smoke contacts
Effect；On the other hand, the presence of stirring, but also the lye that filler layer surface is adsorbed is removed, compared with the prior art
Middle filler is easy the case where agglomeration, and the packing layer for being constantly reversed stirring avoids agglomeration and causes to absorb the reduction of sulfide function
The case where.
Further, the stirring pipe is S-shaped.The stirring pipe of S-shaped makes the contact area of stirring pipe and packing layer bigger, more
Be conducive to the stirring to packing layer.
Further, the piston rod and hollow pipe are driven by a motor.
Motor drives so that whole equipment realizes automation, advantageously reduces artificial investment, raising working efficiency.
Detailed description of the invention
Fig. 1 is the shaft section view of the utility model embodiment.
Specific embodiment
It is further described below by specific embodiment:
Appended drawing reference in Figure of description includes: tower body 1, air inlet 11, exhaust outlet 12, packing layer 2, conical pipe 3, net
Hole 31, helical blade 4, through-hole 41, spray cylinder 51, hollow pipe 52, stirring pipe 53, water vat 6, reverse taper hole 61, piston 7, piston
Bar 8.
The present embodiment is substantially as shown in Figure 1:
Regnerated rubber powder processing vulcanizing treatment equipment, including spray equipment, the packing layer 2, taper in tower body 1, tower body 1
Pipe 3 and atomising device, spray equipment are located at 2 top of packing layer, and 1 bottom of tower body is equipped with air inlet 11, is equipped with exhaust at the top of tower body 1
The tube wall of mouth 12,3 bottom face air inlet 11 of conical pipe, conical pipe 3 is equipped with mesh 31, and 3 outer surface of conical pipe is fixed with
Helical blade 4, helical blade 4 are equipped with several through-holes 41；Ceramic corrugated filler is filled in packing layer 2.
Spray equipment includes the hollow pipe 52 of spray cylinder 51 and rotation, and spray cylinder 51 is fixedly connected on hollow pipe 52, is sprayed
It drenches 51 bottom of cylinder and is equipped with several weepers and several stirring pipes 53,53 side wall of stirring pipe is provided with several water dumping holes, and stirring pipe 53
It is S-shaped.
Atomising device includes several water vats 6 being obliquely installed, and water vat 6 is located between the blade of helical blade 4,6 bottom of water vat
Portion is equipped with several reverse taper holes 61, and 6 inner wall of water vat slidably connects piston 7, fixed on the piston 7 far from 6 bottom side of water vat
It is connected with piston rod 8.
Piston rod 8 and hollow pipe 52 are driven by a motor.
Specific implementation process is as follows:
Motor drives hollow pipe 52 to rotate, and while hollow pipe 52 rotates, the spray cylinder 51 being fixedly connected is driven to rotate, spray
The stirring pipe 53 that leaching 51 bottom of cylinder is fixedly connected is entered in spray cylinder 51 also with rotation, spray liquid by hollow pipe 52, then
It is entered in packing layer 2 by the water dumping hole in the weeper and hollow pipe 52 of 51 bottom of spray cylinder, spray liquid penetrates packing layer 2
It falls.
In spraying device, motor drives piston rod 8 and piston 7 to compress water vat 6 and is provided in the spray cylinder 51 of spray liquid
Volume, so that spray liquid is squeezed and sprays from reverse taper hole 61, the spray liquid of ejection forms mist and under parabola
It falls.
Flue gas containing a large amount of sulfide enters in conical pipe 3 from air inlet 11, then penetrates the mesh 31 of conical pipe 3
It enters between helical blade 4, the ramping when ascending path of flue gas is from entering conical pipe 3 becomes along helical blade 4
Rising of spiraling, while flue gas ascending path changes, flue gas rise speed slow down.
Spiralling flue gas spray liquid spraying with formation first between helical blade 4 contacts, through under packing layer 2
The spray liquid fallen is also contacted between helical blade 4 with flue gas, and the contact of spray liquid, spray mist with flue gas forms primary suction
It receives；The axial direction with gravity along conical pipe 3 of spray liquid falls, and sprays mist descent path parabolically, thus spray liquid, spray
Contact of the mist with flue gas is formed in space to intersect, so that the liquid of spray and the contact surface of flue gas greatly improve, is conducive to improve
Handle the efficiency of sulfide.
Spiralling flue gas continues to rise to packing layer 2, and packing layer 2 adsorbs flue gas, is formed to sulfide
Double absorption.
The primary classification absorpting form absorbed with double absorption, so that the sulfide in flue gas is more fully inhaled
It receives, improves the absorbed ratio of sulfide in flue gas into one.
Stirring pipe 53 is rotated with the rotation of spray cylinder 51, on the one hand, the rotation of stirring pipe 53 carries out packing layer 2 constantly
Ground overturning agitation, so that not being able to give full play to the absorption to sulfide in flue gas with the packing layer of smoke contacts 2；It is another
Aspect, the presence of stirring avoid the agglomeration of packing layer 2 and cause but also the lye that 2 surface of packing layer is adsorbed is removed
Absorb the case where sulfide function reduces.
Above-described is only the embodiments of the present invention, and the common sense such as well known specific structure and characteristic are herein in scheme
It does not describe excessively.It should be pointed out that for those skilled in the art, in the premise for not departing from the utility model structure
Under, several modifications and improvements can also be made, these also should be considered as the protection scope of the utility model, these all will not influence
The effect and patent practicability that the utility model is implemented.
Claims (5)
1. regnerated rubber powder processing vulcanizing treatment equipment, including the intracorporal spray equipment of tower body, tower and packing layer, the spray
Device is located above packing layer, it is characterised in that: conical pipe is additionally provided in the tower body, the bottom of the tower body is equipped with air inlet
Mouthful, the top of the tower body is equipped with exhaust outlet, and the tube wall of the taper bottom of the tube face air inlet, the conical pipe is equipped with net
Hole, the taper tube outer surface are fixed with helical blade, and the helical blade is equipped with several through-holes, the spray equipment packet
The hollow pipe of spray cylinder and rotation is included, the spray cylinder is fixedly connected on hollow pipe, and the spray cylinder bottom is equipped with several drops
Water hole and several stirring pipes.
2. regnerated rubber powder processing vulcanizing treatment equipment according to claim 1, it is characterised in that: further include atomization dress
It sets, the atomising device includes several water vats being obliquely installed, and between helical blade, the water vat bottom is set the water vat
There are several reverse taper holes, the water vat inner wall slidably connects piston, fixed on the piston far from water vat bottom side to connect
It is connected to piston rod.
3. regnerated rubber powder processing vulcanizing treatment equipment according to claim 2, it is characterised in that: the stirring pipe
Side wall is provided with several water dumping holes.
4. regnerated rubber powder according to claim 3 processing vulcanizing treatment equipment, it is characterised in that: the stirring pipe is in
S-shaped.
5. being existed according to regnerated rubber powder processing vulcanizing treatment equipment, feature described in claim 2-4 any claim
In: the piston rod and hollow pipe are driven by a motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821598170.4U CN209060847U (en) | 2018-09-28 | 2018-09-28 | Regnerated rubber powder processing vulcanizing treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821598170.4U CN209060847U (en) | 2018-09-28 | 2018-09-28 | Regnerated rubber powder processing vulcanizing treatment equipment |
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| Publication Number | Publication Date |
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| CN209060847U true CN209060847U (en) | 2019-07-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821598170.4U Active CN209060847U (en) | 2018-09-28 | 2018-09-28 | Regnerated rubber powder processing vulcanizing treatment equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110548376A (en) * | 2019-09-25 | 2019-12-10 | 安徽国能亿盛环保科技有限公司 | Desulfurization and denitrification's boiler waste heat recovery device |
-
2018
- 2018-09-28 CN CN201821598170.4U patent/CN209060847U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110548376A (en) * | 2019-09-25 | 2019-12-10 | 安徽国能亿盛环保科技有限公司 | Desulfurization and denitrification's boiler waste heat recovery device |
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