CN206996270U - A kind of curing fume gathers cleaning system - Google Patents
A kind of curing fume gathers cleaning system Download PDFInfo
- Publication number
- CN206996270U CN206996270U CN201720486964.0U CN201720486964U CN206996270U CN 206996270 U CN206996270 U CN 206996270U CN 201720486964 U CN201720486964 U CN 201720486964U CN 206996270 U CN206996270 U CN 206996270U
- Authority
- CN
- China
- Prior art keywords
- air
- cleaning system
- curing
- collecting hood
- exhaust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
It the utility model is related to a kind of curing fume collection cleaning system, including exhaust fume collecting hood, air collector, pulse type reactor and photooxidation catalytic cleaner, the exhaust fume collecting hood includes the color steel perpendicular to roof installation, color steel forms closed area and vulcanizer is covered in into inside, and color steel bottom is fixedly connected with the soft curtain of plastics;Exhaust fume collecting hood is connected by airduct with air collector, and air-introduced machine is provided between exhaust fume collecting hood and air collector;Air collector is connected by the exhaust gas entrance of pipeline and pulse type reactor, the gas vent of pulse type reactor is connected by airduct with photooxidation catalytic cleaner, the airduct that the air outlet of photooxidation catalytic cleaner is connected is provided with air-introduced machine, and outdoor is discharged into from the waste gas of photooxidation catalytic cleaner air outlet discharge.The utility model ensure that workshop is pollution-free, and the pollutant removing rate in flue gas can be made to make curing fume qualified discharge up to more than 96%.
Description
Technical field
A kind of curing fume collection cleaning system is the utility model is related to, belongs to technical field of environment protection equipment.
Background technology
The vulcanization of rubber is last important flow of rubber manufacturing process, in sulfidation, portions additive
Volatilization turns into curing fume from rubber.Contained pollutant smell is big in curing fume, carcinogenicity is strong, the health hazard to worker
Huge, traditional approach is to add force ventilation mode to cause to dislike to environment by outside the direct drain chamber of curing fume using gravity-flow ventilation
Bad influence.With Environmental protection work pay attention to day by day, study to curing fume be collected processing it is extremely urgent.
Inventor is based on above-mentioned consideration, devises a kind of curing fume collection cleaning system, had both avoided vulcanization cigarette
Harm of the gas to indoor workers ' health, also reduce the influence of waste gas discharge environmental pollution.
Utility model content
To achieve these goals, technical scheme is used by the utility model:
A kind of curing fume gathers cleaning system, including exhaust fume collecting hood, air collector, pulse type reactor and photooxidation catalytic purification
Device, the exhaust fume collecting hood include the color steel perpendicular to roof installation, and color steel forms closed area and vulcanizer is covered in into inside, color
Steel plate bottom is fixedly connected with the soft curtain of plastics;Exhaust fume collecting hood is connected by airduct with air collector, is provided with and is drawn between exhaust fume collecting hood and air collector
Blower fan;Air collector is connected by the exhaust gas entrance of pipeline and pulse type reactor, the gas vent of pulse type reactor by airduct with
Photooxidation catalytic cleaner connects, and the airduct that the air outlet of photooxidation catalytic cleaner is connected is provided with air-introduced machine, is catalyzed from photooxidation
The waste gas of clarifier air outlet discharge is discharged into outdoor.
The pulse type reactor includes housing, and housing central section is provided with circulating absorption solution entrance and the waste gas tangent with housing
Entrance, housing bottom are cone settling tank, and cone settling tank is provided with particulate emission mouth, and the lower section of circulating absorption solution entrance is provided with
Circulating absorption solution exports, and case top is provided with upper end cover, and upper end cover is provided with gas vent, and the bottom of upper end cover is provided with circular keep off
Plate, carbon fiber adsorption and catalytic combustion layer is provided between upper end cover and circular baffle plate;Enclosure interior is located at the top of exhaust gas entrance provided with upper
Dividing plate, upper spacer middle part are provided with nozzle, guide vane are provided with exhaust gas entrance.
The lower section that the enclosure interior is located at exhaust gas entrance is provided with lower clapboard, and lower clapboard is provided with nozzle, on upper spacer
Nozzle and the nozzle consistency from top to bottom on lower clapboard.
The diameter of the circular baffle plate is more than 3 times of gases exit line.
The circular baffle plate rear is additionally provided with gas-liquid separation net.
The nozzle is La Geer nozzles.
The circulating absorption solution use mass fraction for 8% sodium hydrate aqueous solution.
The utility model using exhaust fume collecting hood by gas sampling caused by vulcanizer to air collector, and by air collector
It is delivered to after waste gas pressurization in pulse type reactor and carries out desulfurizing and purifying processing, is gone by photooxidation catalytic cleaner in removing exhaust gas
Peculiar smell, finally the waste gas after processing is discharged into air.Whole smoke collecting cleaning system ensure that workshop is pollution-free,
The pollutant removing rate in flue gas can be made to make curing fume qualified discharge up to more than 96%.
The utility model is further elaborated below by way of the drawings and specific embodiments.
Brief description of the drawings:
Fig. 1 is overall structure diagram of the present utility model;
Fig. 2 is the internal structure schematic diagram of vortex pulse reactor;
Fig. 3 is A-A sectional views in Fig. 2.
Embodiment:
As shown in figure 1, a kind of curing fume collection cleaning system, including the collection waste gas produced for collecting vulcanizer 3
Petticoat pipe, by the air collector 5 of waste gas pressurized storage, in air collector 5 waste gas carry out desulfurizing and purifying processing the and of pulse type reactor 6
Remove the photooxidation catalytic cleaner 7 to eliminate the unusual smell.Exhaust fume collecting hood can be installed vertically on the roof in workshop using color steel 1, made more
Block color steel 1 is surrounded by the space of a closing and all vulcanizers 3 is enclosed in closing space, in every piece of color steel 1
The soft curtain 2 of plastics is fixedly mounted in bottom, and the soft curtain 2 of plastics both can facilitate the disengaging of worker again with printing opacity.Formed using aforesaid way
Exhaust fume collecting hood installation is simple, and the change to existing workshop is smaller, and does not influence the daylighting of curing department.Exhaust fume collecting hood is by airduct by sulphur
Change fume collection in air collector 5, in order to make the waste gas of the discharge of vulcanizer 3 not spread in workshop, increase air inducing on airduct
Machine 4.
The curing fume being stored in air collector 5 need to carry out pressurized treatments, then pass through pipeline to pulse type reactor 6
On exhaust gas entrance 615 in.Pulse type reactor 6 used herein above is using vortex structural principle using gas-liquid mass transfer come to useless
Gas carries out purified treatment, therefore the gas entered in pulse type reactor 6 need to be made to rotate in a circumferential direction at a high speed, therefore curing fume is shifted to an earlier date
Pressurizeed very necessary, and the exhaust gas entrance pipeline 615 on pulse type reactor 6 need to be designed to and the outer surface phase of housing 606
Cut.To fully ensure that gas produces vortex in the internal rotation of housing 606, guide vane 604 is installed at exhaust gas entrance pipeline 615,
The spacing of guide vane 604 and housing 606 should not be too big and guide vane 604 is possessed streamlined contour, is circulated to prevent stopping
The splash of absorbing liquid and the rotation for destroying air-flow.The upper and lower of exhaust gas entrance pipeline 615 is internally located in housing 606 to set respectively
One piece of upper spacer 605 and lower clapboard 602, in the center of upper and lower dividing plate installation La Geer nozzles 603 symmetrical above and below.The nozzle
603 effect is to make to come two strands of circulating absorption solutions up and down of self-circulating pump to clash at a high speed, to produce small uniform splash drop,
So as to obtain higher gas-liquid mass transfer efficiency.To produce symmetrical droplets, it is right above and below strict centering that upper and lower nozzle 603 is answered
Together.The pressure energy that can guarantee that liquid from La Geer nozzles is fully changed into kinetic energy.Nozzle 603 is connected to housing by pipeline
606 outside simultaneously forms circulating absorption solution entrance 612 on housing 606.The bottom of housing 606 is cone settling tank 601, taper
The middle part of subsider 601 is provided with particulate emission mouth 611, is additionally provided with and follows on the housing 606 of the lower section of circulating absorption solution entrance 612
Ring absorbing liquid outlet 613.The top of housing 606 is provided with upper end cover 609, and gases exit line is provided with the center of upper end cover 609
614, the lower section of upper end cover 609 is additionally provided with a circular baffle plate 608, and the diameter of baffle plate 608 need to be straight more than gases exit line 614
More than 3 times of footpath, it is the rotation situation for maintaining near exit gas that it, which is acted on, increases residence time of the gas in reactor,
Reduce drop entrainment.When designed waste gas gas velocity is higher, also gas-liquid separation net should be set at the rear of circular baffle plate 608
607.Carbon fiber adsorption and catalytic combustion layer 610 is provided between upper end cover 609 and circular baffle plate 608, waste gas can be further handled and inhale
The component that solubility is relatively low in liquid is received, the adsorbing fiber improves the robustness under gas shock using braiding structure.This implementation
Circulating absorption solution used in example is the sodium hydrate aqueous solution that mass fraction is 8%.
Vulcanization waste gas through over pressurizeed enters in housing 606 along exhaust gas entrance pipeline 615, in the effect of guide vane 604
Lower formation cyclone, to the central motion of housing 606 while gas rotating.At the same time, circulating pump supercharging divides circulating absorption solution
Do not sprayed into 2 stocks from upper and lower nozzle 603, form the drop of splash and contacted with rotary gas, realized between gas-liquid two-phase
Mass transport process.During gas makees eddying motion, due to the conservation of momentum, gas circumferential speed gradually increases so that gas-liquid two
Alternate shear rate gradually increases, and this is highly beneficial to mass-transfer progress, and the liquid of two bursts of relative injections is with certain arteries and veins
Frequencies flow is rushed, the flow of two nozzles 603 is also changed with certain frequency.Therefore the diameter of the drop zone sprayed is by small
To great achievement cyclically-varying, this promotes liquid to form less drop, adds the specific surface area of drop, enhances gas-liquid
Mass transport process, and the periodic splash of liquid can also effectively prevent that gas is short-circuit.Solid particle after gas-liquid mass transfer
Thing falls into cone settling tank 601 and discharged from particulate emission mouth 611, and waste liquid is from the discharge of circulating absorption solution outlet 613, and waste gas is from gas
The discharge of body outlet 614.Vulcanization waste gas after above-mentioned purified treatment, the removal efficiency of its pollutant are up to more than 96%.
It is still remaining unavoidably although the exhaust emission after the above-mentioned desulfurization of pulse type reactor 6 is removed totally substantially
Certain peculiar smell, therefore the gas vent 614 of pulse type reactor 6 is connected by the air inlet of airduct and photooxidation catalytic cleaner 7
Connect, carrying out oxidation to the organic molecule in waste gas using UV lamp removes peculiar odor treatment, in air-introduced machine(It is not drawn into figure)Effect
Under, it can be directly discharged to outdoor from the waste gas of the air outlet of photooxidation catalytic cleaner 7 discharge.
Above example only to illustrate the technical solution of the utility model and unrestricted, those of ordinary skill in the art couple
Other modifications or equivalent substitution that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope, it all should cover in right of the present utility model.
Claims (7)
1. a kind of curing fume gathers cleaning system, it is characterised in that:Including exhaust fume collecting hood, air collector, pulse type reactor and photooxidation
Catalytic cleaner, the exhaust fume collecting hood include the color steel perpendicular to roof installation, and color steel, which forms closed area, will vulcanize hood
In inside, color steel bottom is fixedly connected with the soft curtain of plastics;Exhaust fume collecting hood is connected by airduct with air collector, exhaust fume collecting hood and air collector it
Between be provided with air-introduced machine;Air collector is connected by the exhaust gas entrance of pipeline and pulse type reactor, and the gas vent of pulse type reactor leads to
Airduct to be crossed to be connected with photooxidation catalytic cleaner, the airduct that the air outlet of photooxidation catalytic cleaner is connected is provided with air-introduced machine, from
The waste gas of photooxidation catalytic cleaner air outlet discharge is discharged into outdoor.
A kind of 2. curing fume collection cleaning system according to claim 1, it is characterised in that:The pulse type reactor bag
Housing is included, housing central section is provided with circulating absorption solution entrance and the exhaust gas entrance tangent with housing, and housing bottom settles for taper
Groove, cone settling tank are provided with particulate emission mouth, and the lower section of circulating absorption solution entrance exports provided with circulating absorption solution, case top
Provided with upper end cover, upper end cover is provided with gas vent, and the bottom of upper end cover is provided with circular baffle plate, between upper end cover and circular baffle plate
Provided with carbon fiber adsorption and catalytic combustion layer;The top that enclosure interior is located at exhaust gas entrance is provided with upper spacer, and nozzle is provided with the middle part of upper spacer,
Guide vane is provided with exhaust gas entrance.
A kind of 3. curing fume collection cleaning system according to claim 2, it is characterised in that:The enclosure interior is located at
The lower section of exhaust gas entrance is provided with lower clapboard, and lower clapboard is provided with nozzle, above and below the nozzle on nozzle and lower clapboard on upper spacer
Alignment.
A kind of 4. curing fume collection cleaning system according to claim 2, it is characterised in that:The circular baffle plate it is straight
Footpath is more than 3 times of gases exit line.
A kind of 5. curing fume collection cleaning system according to claim 2, it is characterised in that:The circular baffle plate rear
It is additionally provided with gas-liquid separation net.
A kind of 6. curing fume collection cleaning system according to claim 2, it is characterised in that:The nozzle is La Geer
Nozzle.
A kind of 7. curing fume collection cleaning system according to claim 2, it is characterised in that:The circulating absorption solution is adopted
With the sodium hydrate aqueous solution that mass fraction is 8%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720486964.0U CN206996270U (en) | 2017-05-04 | 2017-05-04 | A kind of curing fume gathers cleaning system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720486964.0U CN206996270U (en) | 2017-05-04 | 2017-05-04 | A kind of curing fume gathers cleaning system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206996270U true CN206996270U (en) | 2018-02-13 |
Family
ID=61442926
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720486964.0U Expired - Fee Related CN206996270U (en) | 2017-05-04 | 2017-05-04 | A kind of curing fume gathers cleaning system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206996270U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107349731A (en) * | 2017-07-11 | 2017-11-17 | 郑堂勇 | A kind of air dedusting and nitrogen dioxide recycling and processing device |
CN108246070A (en) * | 2018-03-02 | 2018-07-06 | 广州紫科环保科技股份有限公司 | A kind of integration post-cure emission-control equipment and method |
CN108655146A (en) * | 2018-05-09 | 2018-10-16 | 三角轮胎股份有限公司 | The method of closed tyre vulcanization |
CN109827442A (en) * | 2019-02-28 | 2019-05-31 | 中卫市茂烨冶金有限责任公司 | Multistation flue gas and surplus heat collection device for ferrosilicon casting |
-
2017
- 2017-05-04 CN CN201720486964.0U patent/CN206996270U/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107349731A (en) * | 2017-07-11 | 2017-11-17 | 郑堂勇 | A kind of air dedusting and nitrogen dioxide recycling and processing device |
CN108246070A (en) * | 2018-03-02 | 2018-07-06 | 广州紫科环保科技股份有限公司 | A kind of integration post-cure emission-control equipment and method |
CN108655146A (en) * | 2018-05-09 | 2018-10-16 | 三角轮胎股份有限公司 | The method of closed tyre vulcanization |
CN109827442A (en) * | 2019-02-28 | 2019-05-31 | 中卫市茂烨冶金有限责任公司 | Multistation flue gas and surplus heat collection device for ferrosilicon casting |
CN109827442B (en) * | 2019-02-28 | 2023-08-29 | 中卫市茂烨冶金有限责任公司 | Multi-station flue gas and waste heat collecting device for ferrosilicon pouring |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN206996270U (en) | A kind of curing fume gathers cleaning system | |
CN103203170B (en) | Flue-gas cleaner | |
CN103933832B (en) | A kind of device for removing haze and atmosphere pollution | |
CN201894904U (en) | Dual-cylinder rotational-flow bubbling dust removal and desulfurization gas cleaning device | |
CN207401353U (en) | A kind of spray painting and drying tunnel waste gas treatment equipment | |
CN203123767U (en) | Composite type dust collector | |
CN211098372U (en) | Efficient flue gas desulfurization tower | |
CN201988299U (en) | Waste gas purifying device | |
CN204051344U (en) | A kind of dusting desulfurizing integrated machine | |
CN104190190A (en) | Dedusting and desulfurization integrated machine | |
CN210356536U (en) | Gum dipping waste gas treatment device | |
CN206996240U (en) | A kind of vortex pulse type reactor | |
CN116688689B (en) | A high-efficient dust removal spray column for exhaust-gas treatment | |
CN206508686U (en) | A kind of flue gas ash removal denitrification apparatus for environmental protection | |
CN210495866U (en) | Environment-friendly exhaust gas purification device for granulating chemical fiber friction material | |
CN203355583U (en) | Flue gas purifier | |
CN215138194U (en) | Dust removal tail gas purification treatment equipment for finished product treatment section of cigarette factory | |
CN2376989Y (en) | Combined smoke-eliminating dust-collecting purifying device | |
CN210448538U (en) | Waste gas treatment device in high-efficient burning of coke oven gas | |
CN205269374U (en) | Exhaust gas treating device | |
CN210546932U (en) | Modified asphalt waterproofing membrane exhaust-gas treatment system | |
CN208465601U (en) | A kind of desulfurizing tower | |
CN207153465U (en) | A kind of phenolic resin waste gas treatment equipment | |
CN205667783U (en) | For printing the environment-friendly disposal system of waste gas | |
CN205886494U (en) | Flue gas degree of depth dust removal defogging water conservation unit reaches by its device of constituteing |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180213 Termination date: 20190504 |