CN206597434U - The total system of rubber waste gas - Google Patents
The total system of rubber waste gas Download PDFInfo
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- CN206597434U CN206597434U CN201621200135.3U CN201621200135U CN206597434U CN 206597434 U CN206597434 U CN 206597434U CN 201621200135 U CN201621200135 U CN 201621200135U CN 206597434 U CN206597434 U CN 206597434U
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- waste gas
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- total system
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- 239000002912 waste gas Substances 0.000 title claims abstract description 26
- 230000007246 mechanism Effects 0.000 claims abstract description 71
- 239000007789 gas Substances 0.000 claims abstract description 45
- 238000005507 spraying Methods 0.000 claims abstract description 27
- 238000010521 absorption reaction Methods 0.000 claims abstract description 10
- 238000001816 cooling Methods 0.000 claims abstract description 10
- 238000005070 sampling Methods 0.000 claims abstract description 10
- 239000007921 spray Substances 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 238000010438 heat treatment Methods 0.000 claims description 17
- 239000000446 fuel Substances 0.000 claims description 9
- 238000000889 atomisation Methods 0.000 claims description 7
- 230000006835 compression Effects 0.000 claims description 4
- 238000007906 compression Methods 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 25
- 239000003546 flue gas Substances 0.000 abstract description 24
- 230000000694 effects Effects 0.000 abstract description 9
- 239000003921 oil Substances 0.000 description 22
- 239000010426 asphalt Substances 0.000 description 19
- 238000012545 processing Methods 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000011295 pitch Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000000295 fuel oil Substances 0.000 description 4
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 230000001976 improved effect Effects 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000008034 disappearance Effects 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 210000004072 lung Anatomy 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- 206010058467 Lung neoplasm malignant Diseases 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
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- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011294 coal tar pitch Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000005474 detonation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
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- 239000003822 epoxy resin Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
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- 231100000053 low toxicity Toxicity 0.000 description 1
- 201000005202 lung cancer Diseases 0.000 description 1
- 208000020816 lung neoplasm Diseases 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
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- 231100000252 nontoxic Toxicity 0.000 description 1
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- 125000005575 polycyclic aromatic hydrocarbon group Chemical group 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000011387 rubberized asphalt concrete Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of total system of rubber waste gas, including gas sampling mechanism, and the filter mechanism connected by the road with described gas sampling mechanism successively, spraying cooling mechanism, spray-absorption mechanism, DDBD mechanisms, air-introduced machine and burner, described burner includes cylinder, is arranged on cylinder anterior steady wind disk and atomising mechanism, is arranged on the air inlet mechanism at cylinder rear portion.Using axle stream integral blower, overall volume is small, and structure is more compact, and air intake direct current arrives at supplying air disc, windage is small, air quantity is big, and the waste gas blast pipe and gas sampling mechanism connection at center, and flue gas is aspirated using middle part, because flue gas amount fluctuation ratio is larger, extraneous air is directly supplemented by air inlet gap, the overall air-supply effect of air supply motor is can effectively ensure that, it is ensured that burner normal work.
Description
Technical field
The present invention relates to industrial waste smoke gas disposal technical field, more particularly to a kind of integrated treatment system of rubber waste gas
System.
Background technology
Rubber powder modified asphalt lays urban road expressway and bridge floor, can reduce and absorption of noise, improve wheel with
Road adherence, improving frictional force makes brake much sooner, effectively, and frost-cracking-preventing antiageing effect good winter does not ftracture, and hot day is not
It is soft viscous, and a large amount of junked tires is recycled utilization.But rubber powder under 185 DEG C~195 DEG C states with asphalt mixing when,
Have largely containing the vicious flue gas effusion such as ether, hydrogen cyanide, sulfur dioxide, wherein the BaP contained is polycyclic aromatic hydrocarbon Poisoning
A kind of maximum strong carcinogenic substance, is combined together with the aerosol of all kinds particulate formation in air, can below 8 microns
Suck in grit, the ratio for being directly sucked in lung is higher, lung is sucked through respiratory tract, into alveolar even blood, cause lung cancer
And angiocardiopathy.
Conventional rubber powder at high operating temperatures with asphalt mixing when, effusion it is vicious containing ether, hydrogen cyanide, sulfur dioxide etc.
Flue gas is directly discharged into air, at its malicious smelly flue gas after heat exchanger cooling in exhaust gas cooling device after being handled into oil-washing apparatus
Manage effect not ideal.
Although can effectively remove flue gas produced during rubber powder modified asphalt etc. using a variety of chemically and physically methods
The smelly composition of poison, but use cost is high, and the component in flue gas is result in as waste disposal, fail to give full play to its work
With the flue gas that produces in rubber powder modified asphalt production being not only, in SBS modified pitch, SBR modified pitch, epoxy resin modification
Pitch, color asphalt, heavy traffic paving asphalt, coal tar pitch etc. production prepare when can also produce similar malicious smelly flue gas, by above-mentioned flue gas
Bitumen flue gas is referred to as, is paying attention to environmental protection instantly, effective processing of bitumen flue gas directly concerns asphalt rubber row
Industry existence is basic.
The U of Chinese patent 201815218 discloses a kind of processing method of bitumen flue gas, by the bitumen flue gas of generation by pre-
Constant flow is sprayed to production heating burner hearth by proportion-controllable and bitumen flue gas is burnt at high temperature.Also disclose one simultaneously
Processing unit is planted, the bitumen flue gas produced in production after simple process, is sent directly into burner hearth and it is burnt by it, burner hearth
It can be dispensing reactor or the burner hearth of Asphaltum heating pot, be so just consumed while production, reduce processing pressure, and
And, bitumen flue gas burning is handled, flammable component is taken full advantage of in bitumen flue gas, only produced after processing carbon dioxide and
Water, pollutes small, processing cost is low, effectively protects external environment condition.
But, the processing unit in above-mentioned patent is directly injected directly into the flame envelope of burner flame using bitumen flue gas
Part, because bitumen flue gas yield is unstable, causes burning treatment effect undesirable, while at flame envelope, easily causing
Part bitumen flue gas causes burning processing insufficient away from flame.
The content of the invention
In view of the technical drawbacks of the prior art, it is an object of the present invention to provide a kind of General Office of rubber waste gas
Reason system.
To realize that the technical scheme that the purpose of the present invention is used is：
A kind of total system of rubber waste gas, including gas sampling mechanism, and successively with described gas sampling
The filter mechanism that mechanism is connected by the road, spraying cooling mechanism, spray-absorption mechanism, DDBD mechanisms, air-introduced machine and burner, institute
The burner stated includes cylinder, is arranged on cylinder anterior steady wind disk and atomising mechanism, is arranged on the air inlet mechanism at cylinder rear portion,
Described atomising mechanism includes front end and is formed with spray chamber and and is positioned at the shower nozzle and oil gas input mechanism of Wen Feng disk center, institute
The air inlet mechanism stated includes the axial flow blower for being arranged on cylinder lumen rear portion, is centrally positioned in described axial flow blower air intake surface
The exhaust inlet pipe connected with the air outlet of air-introduced machine, is formed with air inlet passage between described exhaust inlet pipe and cylinder.
Be provided with described spray chamber spray chamber is divided into front and rear two sections and only allow it is right after to preceding circulation list
To valve system, orifice is formed with the leading flank of described spray chamber.
Described one-way valve mechanism includes the baffle ring being fixedly connected with described atomization chamber interior walls, by the compression of front side spring
Hold on described baffle ring trailing flank to realize sealed valve plate.
It is axially fixed in the middle part of described leading flank and is provided with sleeve pipe, pluggable institute is formed with the middle part of described valve plate
The connecting rod in sleeve pipe stated, described spring is set on described sleeve pipe and holds described valve plate backward.
Described oil gas input mechanism includes the cyclone connected respectively with compressed air feeding pipe and fuel supply pipe
Tube and oil rotation pipe, and to the heater block to compressed air and fuel Heating.
Also include heater block, it includes outer cylinder body, is placed coaxially on the heating rod in outer cylinder body, outside described
Cylinder is interior and is arranged on the spiral oil circuit coil pipe of heating rod periphery, and described oil circuit coil pipe is serially connected in described fuel delivery pipe
Lu Shang, air inlet and gas outlet, described compressed air feeding pipe correspondence have been correspondingly formed at described outer cylinder body two ends
Ground connects to realize the heating of compressed air with described air inlet and gas outlet.
Described cooling water tower includes tower body, is arranged on the air inlet of tower body bottom, is arranged on the gas outlet at the top of tower body,
Two spraying layers in the middle part of tower body and top are spaced apart and arranged in, and are arranged on the demisting layer on the spraying layer top at top.
Spray-absorption mechanism includes tower body, is arranged on the air inlet of tower body bottom, is arranged on the gas outlet at the top of tower body,
Two spraying layers in the middle part of tower body and top are arranged on every ground, the packing layer below spraying layer are correspondingly arranged at, and be arranged on
The demisting layer on the spraying layer top at top.Described spraying layer includes the water inlet supervisor connected with circulating water line, multiple and institute
Multiple water inlet pipes that the water inlet supervisor stated is vertically arranged and connected, are corresponded to respectively on described water inlet supervisor and water inlet pipe
The spray head that ground is provided with spray head, described water inlet pipe is staggered front to back distribution.
Compared with prior art, the beneficial effects of the invention are as follows：
Using axle stream integral blower, overall volume is small, and structure is more compact, and air intake direct current arrives at supplying air disc, wind
Resistance is small, and air quantity is big, and the waste gas blast pipe and gas sampling mechanism connection at center, flue gas is aspirated using middle part, because useless
Exhaust gas volumn fluctuation ratio is larger, and extraneous air is directly supplemented by air inlet gap, can effectively ensure that the overall air-supply effect of air supply motor
Really, it is ensured that burner normal work.
Brief description of the drawings
Fig. 1 show the structural representation of the total system of the rubber waste gas of the present invention.
Fig. 2 show the structural representation of the burner of the present invention.
Fig. 3 show the structural representation of shower nozzle；
Fig. 4 show spraying cooling structural scheme of mechanism；
Fig. 5 show spraying layer structural representation；
Fig. 6 show heater block structural representation.
Embodiment
The present invention is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that described herein
Specific embodiment only to explain the present invention, be not intended to limit the present invention.
As shown in figures 1 to 6, the total system of rubber waste gas of the invention include gas sampling mechanism, and successively with
The filter mechanism that described gas sampling mechanism is connected by the road, spraying cooling mechanism, draws at spray-absorption mechanism, DDBD mechanisms
Blower fan, the exhaust outlet of described air-introduced machine accesses burner, i.e., carry out burning processing herein to the gas after processing.Described is useless
Gas collecting mechanism is multiple gas skirts being correspondingly arranged above waste gas generating mechanism.Described waste gas generating mechanism includes reaction
The high temperature such as kettle, finished pot, agitator tank and the mechanism that pitch waste gas can be produced.Wherein, described burner includes cylinder 40, sets
In the steady wind disk 47 and atomising mechanism that cylinder is anterior, the air inlet mechanism at cylinder rear portion is arranged on, before described atomising mechanism includes
End be formed with spray chamber and and be positioned at the shower nozzle 46 and oil gas input mechanism of Wen Feng disk center, described air inlet mechanism includes setting
The axial flow blower (not shown) at cylinder lumen rear portion is put, described axial flow blower air intake surface and air inducing is centrally positioned in
The exhaust inlet pipe 43 of the air outlet connection of machine, is formed with air inlet passage between described exhaust inlet pipe and cylinder.
Present invention introduces DDBD mechanisms, the recovery of large granular materials is carried out using filter mechanism in early stage, material is realized
Recycle, for waste gas cooled and absorption processing after, in entrance DDBD mechanisms, utilize produced high energy electron, freedom
Each component in base isoreactivity particle irradiation, ionization, cracking industrial waste gas, is allowed to decompose, and some row such as oxidation are complicated
Chemical reaction, so as to eliminate the peculiar smell of various discharge of pollutant sources, stink pollutant, finally in conjunction with high-temp combustion, make poisonous
Pernicious gas reaches low toxicity, Non-toxic, protects environment for human survival.And axle stream integral blower is used, overall volume is small,
Structure is more compact, and air intake direct current arrives at supplying air disc, and windage is small, and air quantity is big, and the waste gas blast pipe and waste gas at center
Collecting mechanism is connected, and flue gas is aspirated using middle part, because flue gas amount fluctuation ratio is larger, directly supplements outer by air inlet gap
Portion's air, can effectively ensure that the overall air-supply effect of air supply motor, it is ensured that burner normal work.
To realize the automatically cleaning of pipeline, it is provided with described spray chamber and spray chamber is divided into front and rear two sections and only permitted
Perhaps the one-way valve mechanism of right backward preceding circulation, orifice is formed with the leading flank of described spray chamber.The present invention's is certainly clear
Clean burner, front and rear two parts are divided into by spray chamber by one-way valve mechanism, operationally, and oil pressure and air pressure collective effect can be by
One-way valve mechanism is opened and realizes that fogging oil gas blowout goes out, when being stopped, and oil pump stops, and oil pressure is reduced to disappearance, continues to provide
Air pressure first can by the oil gas in spray chamber, all blowout carries out the burnings of salvage stores, and with the disappearance of oil pressure, pressure
Contracting gas can be cleaned, the problems such as preventing from blocking caused by remaining from blowback oil circuit to the remnants in oil circuit.
Moreover, spray chamber is divided into two parts, it is real again after the gas of initial atomization is by narrow one-way valve mechanism
Now expansion atomization, improves atomized particle size, further lifts combustion efficiency.
Wherein, described one-way valve mechanism includes the baffle ring being fixedly connected with described atomization chamber interior walls, by front side spring
24 compression holds on described baffle ring trailing flank to realize sealed valve plate 29.Specifically, to realize the axial direction of valve plate
Move back and forth, be axially fixed in the middle part of described leading flank and be provided with sleeve pipe, be formed with the middle part of described valve plate pluggable
Connecting rod in described sleeve pipe, described spring is set on described sleeve pipe and holds described valve plate backward.
Formula one-way valve mechanism is held using spring, it is simple in construction, it is swift in response, can realizes that atomization indoor gas all sprays
Go out, meanwhile, from the beginning oil circuit cleans, it is ensured that without remnants greases in shower nozzle, is prevented effectively from detonation or oil circuit is blocked.
Described oil gas input mechanism includes what is connected respectively with compressed air feeding pipe 45 and fuel supply pipe 44
Cyclone tube 41 and oil rotation pipe 42, described spray chamber formation is in rotation pipe, oil gas rotation tube end, it is preferable that described
Spray chamber in be additionally provided with impeller.Also include to the heater block to compressed air and fuel Heating.
Using rotation mixing, fuel oil combustion efficiency can be improved, exhaust-gas treatment effect is then improved, it is preferable that be useless to ensure
The suction dynamics of gas, described the inner of exhaust inlet pipe 43 is tapered to be expanded outwardly to form extension diameter section.
Meanwhile, to ensure that burner normal work, by compressed air and fuel oil or the corresponding heating of combustion gas, is heated to 80-
100 degrees Celsius, improve atomizing effect and efficiency of combustion.Specifically, described heater block 200 includes outer cylinder body 210, together
The heating rod 220 in outer cylinder body is arranged on axle, in described outer cylinder body and is arranged on the spiral type oil of heating rod periphery
Road coil pipe 230, described oil circuit coil pipe is serially connected on described fuel supply pipe, in described outer cylinder body two ends correspondence landform
Into having air inlet and gas outlet, described compressed air feeding pipe is accordingly connected with reality with described air inlet and gas outlet
The heating of existing compressed air, it is preferable that described heating rod ring week is provided with radiating fin, meanwhile, in described outer cylinder body
Spiral wind deflector is formed with internal face to increase the traveling distance of compressed air, improves heat exchange effect, and and spiral shell
Rotating oil circuit coil pipe correspondence spiral is advanced, it is to avoid wind is maked a whistling sound.
Compressed air and fuel oil are heated using electrically heated mode, 80-100 degrees Celsius is heated to, atomization is improved
Effect, and electrical heating speed is fast, thermal-stable, meanwhile, set using spiral is overlapping, realize compressed air and fuel oil plus
Thermal source is shared, and reduces equipment cost, and reduces volume, is easily installed maintenance.
To realize the recycling of bulky grain rubber grain, described filter mechanism includes casing, is fixed in casing
Multiple orifice plates, the aperture of described orifice plate is 40-80 mesh.
Specifically, described spraying cooling mechanism is taken the photograph for cooling water tower so that flue-gas temperature is down into 60 from 150 DEG C or so
Family name's degree, described cooling water tower includes tower body 31, is arranged on the air inlet 32 of tower body bottom, is arranged on the gas outlet at the top of tower body
33, two spraying layers 34 in the middle part of tower body and top are spaced apart and arranged in, and be arranged on the demisting on the spraying layer top at top
Layer 35.
Equally, spray-absorption mechanism includes tower body, is arranged on the air inlet of tower body bottom, is arranged on the outlet at the top of tower body
Mouthful, two spraying layers in the middle part of tower body and top are spaced apart and arranged in, the packing layer below spraying layer, Yi Jishe is correspondingly arranged at
Put the demisting layer on the spraying layer top at top.
Wherein, described spraying layer includes the water inlet supervisor 36 connected with circulating water line, multiple and described water inlet masters
Multiple water inlet pipes 37 that pipe is vertically arranged and connected, are respectively correspondingly provided with described water inlet supervisor and water inlet pipe
Spray head on spray head 38, described water inlet pipe is staggered front to back distribution.Preferably, described spray head is in concentric circles cloth
Office, the spray head on water inlet supervisor is the center of circle, and each spray head can use prior art, will not be repeated here.
The present invention carries out spraying cooling and absorption using void tower, and processing cost is low, realizes material in waste gas more and returns
Receive, DDBD abundant processing, efficiently solves the problems, such as pitch vent gas treatment in addition.Void tower mechanism end air-introduced machine in addition, it is overall
Gas circuit windage is small, reduces motor and uses, energy-saving and emission-reduction.
Described above is only the preferred embodiment of the present invention, it is noted that for the common skill of the art
For art personnel, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications
Also it should be regarded as protection scope of the present invention.
Claims (9)
1. a kind of total system of rubber waste gas, it is characterised in that including gas sampling mechanism, and successively with it is described
The filter mechanism that gas sampling mechanism is connected by the road, spraying cooling mechanism, spray-absorption mechanism, DDBD mechanisms, air-introduced machine and
Burner, described burner includes cylinder, is arranged on cylinder anterior steady wind disk and atomising mechanism, is arranged on cylinder rear portion
Air inlet mechanism, described atomising mechanism include front end be formed with spray chamber and and be positioned at Wen Feng disk center shower nozzle and oil gas it is defeated
Enter mechanism, described air inlet mechanism includes the axial flow blower for being arranged on cylinder lumen rear portion, is centrally positioned in described axle stream wind
The exhaust inlet pipe connected with the air outlet of air-introduced machine of machine air intake surface, air is formed between described exhaust inlet pipe and cylinder
Inlet channel.
2. the total system of rubber waste gas as claimed in claim 1, it is characterised in that set in described spray chamber
Have and spray chamber is divided into front and rear two sections and only allows the one-way valve mechanism of right backward preceding circulation, in the front side of described spray chamber
Orifice is formed with face.
3. the total system of rubber waste gas as claimed in claim 2, it is characterised in that described one-way valve mechanism includes
The baffle ring being fixedly connected with described atomization chamber interior walls, is held on described baffle ring trailing flank with reality by the compression of front side spring
Existing sealed valve plate.
4. the total system of rubber waste gas as claimed in claim 3, it is characterised in that the edge in the middle part of described leading flank
Axial restraint is provided with sleeve pipe, and the connecting rod that can be inserted into described sleeve pipe, described spring are formed with the middle part of described valve plate
It is set on described sleeve pipe and holds described valve plate backward.
5. the total system of rubber waste gas as claimed in claim 1, it is characterised in that described oil gas input mechanism bag
The cyclone tube connected respectively with compressed air feeding pipe and fuel supply pipe and oil rotation pipe are included, and to compression
The heater block of air and fuel Heating.
6. the total system of rubber waste gas as claimed in claim 5, it is characterised in that also including heater block, it is wrapped
Outer cylinder body is included, the heating rod in outer cylinder body is placed coaxially on, in described outer cylinder body and heating rod periphery is arranged on
Spiral oil circuit coil pipe, described oil circuit coil pipe is serially connected on described fuel supply pipe, at described outer cylinder body two ends pair
It is formed with air inlet and gas outlet with answering, described compressed air feeding pipe accordingly connects with described air inlet and gas outlet
Pass to the heating for realizing compressed air.
7. the total system of rubber waste gas as claimed in claim 1, it is characterised in that described spraying cooling mechanism bag
Tower body is included, the air inlet of tower body bottom is arranged on, the gas outlet at the top of tower body is arranged on, is spaced apart and arranged in the middle part of tower body and top
Two spraying layers in portion, and it is arranged on the demisting layer on the spraying layer top at top.
8. the total system of rubber waste gas as claimed in claim 1, it is characterised in that described spray-absorption mechanism bag
Tower body is included, the air inlet of tower body bottom is arranged on, the gas outlet at the top of tower body is arranged on, is spaced apart and arranged in the middle part of tower body and top
Two spraying layers in portion, are correspondingly arranged at the packing layer below spraying layer, and be arranged on the demisting on the spraying layer top at top
Layer.
9. the total system of rubber waste gas as claimed in claim 7 or 8, it is characterised in that described spraying layer includes
The water inlet supervisor connected with circulating water line, multiple multiple water inlet pipes for being vertically arranged and connecting with described water inlet supervisor,
Respectively correspondingly it is provided with described water inlet supervisor and water inlet pipe before the spray head on spray head, described water inlet pipe
After be interspersed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621200135.3U CN206597434U (en) | 2016-11-07 | 2016-11-07 | The total system of rubber waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621200135.3U CN206597434U (en) | 2016-11-07 | 2016-11-07 | The total system of rubber waste gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206597434U true CN206597434U (en) | 2017-10-31 |
Family
ID=60148208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621200135.3U Expired - Fee Related CN206597434U (en) | 2016-11-07 | 2016-11-07 | The total system of rubber waste gas |
Country Status (1)
| Country | Link |
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| CN (1) | CN206597434U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106377978A (en) * | 2016-11-07 | 2017-02-08 | 天津海泰环保科技发展股份有限公司 | Comprehensive processing system for rubber waste gas |
-
2016
- 2016-11-07 CN CN201621200135.3U patent/CN206597434U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106377978A (en) * | 2016-11-07 | 2017-02-08 | 天津海泰环保科技发展股份有限公司 | Comprehensive processing system for rubber waste gas |
| CN106377978B (en) * | 2016-11-07 | 2022-07-12 | 天津海泰环保科技发展股份有限公司 | Comprehensive treatment system for rubber waste gas |
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