CN208161311U - Active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor - Google Patents
Active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor Download PDFInfo
- Publication number
- CN208161311U CN208161311U CN201820471551.XU CN201820471551U CN208161311U CN 208161311 U CN208161311 U CN 208161311U CN 201820471551 U CN201820471551 U CN 201820471551U CN 208161311 U CN208161311 U CN 208161311U
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- China
- Prior art keywords
- chamber
- processor
- exhaust
- vocs
- active carbon
- 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
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 68
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 58
- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 46
- 239000007921 spray Substances 0.000 claims abstract description 52
- 239000007788 liquid Substances 0.000 claims abstract description 37
- 239000003463 adsorbent Substances 0.000 claims abstract description 26
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 24
- 230000003647 oxidation Effects 0.000 claims abstract description 23
- 230000003197 catalytic effect Effects 0.000 claims abstract description 22
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 238000003860 storage Methods 0.000 claims abstract description 12
- 239000002699 waste material Substances 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 238000006243 chemical reaction Methods 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 19
- 230000004087 circulation Effects 0.000 claims description 18
- 239000003814 drug Substances 0.000 claims description 9
- 238000005086 pumping Methods 0.000 claims description 3
- 239000003610 charcoal Substances 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 239000002904 solvent Substances 0.000 abstract description 9
- 239000003344 environmental pollutant Substances 0.000 abstract description 6
- 231100000719 pollutant Toxicity 0.000 abstract description 6
- 238000004090 dissolution Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 47
- 150000002500 ions Chemical class 0.000 description 18
- 239000002156 adsorbate Substances 0.000 description 17
- 239000000126 substance Substances 0.000 description 11
- 229940079593 drug Drugs 0.000 description 8
- 238000012545 processing Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 230000001172 regenerating effect Effects 0.000 description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000007605 air drying Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000007146 photocatalysis Methods 0.000 description 2
- 230000001699 photocatalysis Effects 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000001994 activation Methods 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012806 monitoring device Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a kind of active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor, and VOCs processor includes adsorbent chamber.It is provided with active carbon storing frame in adsorbent chamber, is placed with active carbon in active carbon storing frame.The lower part of adsorbent chamber is connected with steam generator, and the steam generator includes liquid storage chamber, and heating device is provided in liquid storage chamber, and steam generator is also connected with the air blower by dry drum to active carbon.The utility model also provides a kind of exhaust-gas treatment line for being equipped with above-mentioned VOCs processor, including sequentially connected condenser, spray thrower and photochemical catalytic oxidation device；The air inlet of VOCs processor is connected with photochemical catalytic oxidation device, and gas returning port is connected to condenser.VOCs processor is in use, be not necessarily to move active carbon, the regenerated carbon in such a way that solvent dissolution, steam and hot gas are blown.Exhaust-gas treatment line is in use, each component cooperating, various pollutants in stepwise disposal exhaust gas, and treatment effect is more preferable.
Description
Technical field
The utility model relates to a kind of VOCs processors, and in particular to one kind can in-situ regeneration active carbon, and regenerate
This is low, and regenerative process damages small active carbon VOCs processor to active carbon and is equipped with the exhaust-gas treatment line of the processor.
Background technique
Existing active carbon is activated, and is carried out by way of heat baking.When the excessive particle of activated carbon adsorption
Or when exhaust gas, in order to make active carbon restore adsorption function, the frame equipped with active carbon is taken out first, then will have active carbon
Frame be put into oven and toasted, but baking process can generate reluctant secondary pollution, and pass through baking
Mode activated carbon process is complicated, and time-consuming, and energy consumption is high, and activation process can reduce the absorption property of active carbon.
Utility model content
In order to solve the activated carbon process complexity by way of baking in the prior art, time-consuming, and energy consumption is high, and meeting
The problem of reducing the absorption property of active carbon, the utility model provide a kind of active carbon VOCs processor and are equipped with the processor
Exhaust-gas treatment line.
A kind of VOCs processor provided by the utility model, including adsorbent chamber, the lower part of the adsorbent chamber are provided with air inlet
Mouthful, the top of adsorbent chamber is provided with exhaust outlet and gas returning port；The exhaust outlet for be discharged treated can discharge gas, it is described
Gas returning port is used to the exhaust gas during regenerated carbon importing other waste gas treatment equipments.Active carbon is provided in adsorbent chamber to deposit
Frame is put, is placed with active carbon in active carbon storing frame.The lower part of adsorbent chamber is connected with steam generator, the steam generator packet
Liquid storage chamber is included, heating device is provided in liquid storage chamber, the steam generator is also connected with the air blast by dry drum to active carbon
Machine.
Preferably, first circulation pump is additionally provided in the adsorbent chamber, adsorbent chamber top is provided with spray head, first circulation
The water inlet pipe of pump extends to spray liquid case or liquid storage chamber, and the water pumping pipe of first circulation pump is connected to spray head.The first circulation
Adsorbate in active carbon can be dissolved removal by the solvent of liquid, while can also scrub and glue on active carbon by the setting of pump
Attached undissolvable pollutant.
Preferably, it is additionally provided in the adsorbent chamber for the drier that active carbon is dry.The drier can be
The device of similar hair dryer, drier may include air heating chamber, and heating member is arranged in heating chamber, then will be hot by blower
Wind goes out；Hot gas is blown to active carbon by drier, it can be by active carbon Zhong Shui, easily evaporation organic liquor equal solvent evaporative removal.
The utility model compared with prior art, has the advantages that：
In the prior art, active carbon need to be generally taken out, then the high-temperature baking in particular device, and then by activated carbon adsorption
Substance removal, operating process is complicated, time-consuming, energy consumption is big, loss is big, and is also easy to produce secondary pollution.In the present invention, without moving
Active carbon in dynamic adsorbing regenerator removes adsorbate according to the physicochemical properties difference of adsorbate.Steam generator generates
Solvent vapo(u)r is blown three kinds of modes and is removed adsorbate in active carbon using solvent vapour heating, solvent vapo(u)r dissolution and solvent vapo(u)r.
Solvent vapo(u)r can uniformly be circulated to each aperture of active carbon, and the adsorbate in aperture is dissolved and blown out, and remove active carbon
In adsorbate, regenerating active carbon can be realized.
The utility model also provides a kind of exhaust-gas treatment line for being equipped with above-mentioned VOCs processor, including sequentially connected cold
The air inlet of condenser, spray thrower and photochemical catalytic oxidation device, the VOCs processor is connected with the exhaust pipe of photochemical catalytic oxidation device,
The gas returning port of VOCs processor is connected to condenser.
Preferably, the VOCs processor and photochemical catalytic oxidation device are respectively provided with two, between VOCs processor and photocatalysis
It is connected by way of in parallel between oxidator.The VOCs processor and photochemical catalytic oxidation device are respectively provided with two, at VOCs
Reason device and photochemical catalytic oxidation device using when can select a use as needed, also can be used simultaneously；Also facilitate and do not stopping at exhaust gas
Science and engineering carries out maintenance processing to VOCs processor and photochemical catalytic oxidation device in the case where making.
Preferably, the spray thrower lower part is provided with the first concentration drying equipment, and the first concentration drying equipment includes first
The inlet of waste collection chamber, the first waste collection chamber is connected with spray thrower and condenser；First waste collection chamber top is set
It is equipped with the first dosing mouth and the first steam outlet, the first waste collection is intracavitary to be additionally provided with primary heater.Described first is dense
The setting of contracting drying equipment can carry out subsequent processing to condensate liquid and highly concentrated spray liquid, drug is added by dosing mouth
Make volatile matter qualitative response in condensate liquid and spray liquid, moisture removal is then gone by primary heater heating.
Preferably, exhaust-gas treatment all-in-one machine is additionally provided between the photochemical catalytic oxidation device and VOCs processor, it is described useless
Gas disposal all-in-one machine includes tower body, and energetic ion reaction chamber and spray chamber are provided in tower body.The lower part of the tower body is connected with
Air inlet pipe, air inlet pipe are connected with energetic ion reaction chamber, are provided with energetic ion pipe in the energetic ion reaction chamber.It is described
Energetic ion reaction chamber top is additionally provided with gas outlet, and gas outlet is connected to the lower part of spray chamber by gas transport pipe.Spray
Chamber is connected with second circulation pump, and the water inlet of the second circulation pump passes through two water inlet pipes respectively and is connected with chemical tank and spray
The collecting tank of chamber lower part, two water inlet pipes are mounted on the second valve, and the top of the spray chamber is also connected with escape pipe.At one
Setting energetic ion reaction chamber and spray chamber in tower body can save emission-control equipment effectively using space in tower body
Cost, also reduce occupied area.Exhaust gas is able to carry out energetic ion reaction in tower body, then removes energetic ion through spray
Remaining chemical substance after reaction prevents the substances such as the ozone added during energetic ion reaction or photocatalysis oxidation reaction etc.
Not reaction completely, prevents the substances such as ozone from remaining, reduces secondary pollution；It also can further go simultaneously readily soluble in removing exhaust gas
Object further improves exhaust-gas treatment ability.
Further preferably, the liquid collecting bottom of pond portion is also connected with outlet tube, and outlet tube is connected with the second concentration drying equipment, the
Two concentration drying equipments include the second waste collection chamber, and the inlet of the second waste collection chamber is connected with outlet tube；Second is useless
Liquid collecting chamber top is provided with the second dosing mouth and the second steam outlet, and the second waste collection is intracavitary to be additionally provided with the second heating
Device.The setting of the second concentration drying equipment can carry out subsequent processing to spray liquid in spray chamber, is added by dosing mouth
Drug makes volatile matter qualitative response in condensate liquid and spray liquid, then removes moisture removal by secondary heater heating.
Further preferably, waste collection chamber lower part is also equipped with temperature detect switch (TDS), and temperature detect switch (TDS) is connected with heater.The temperature
The setting of control switch is in the first concentration drying equipment and the second concentration drying equipment, when the intracavitary substance of waste collection is in thick
When, residue temperature is higher than spray liquid boiling temperature, and temperature detect switch (TDS) control heater makes it stop heating.
The utility model compared with prior art, has the advantages that：
The exhaust-gas treatment line of VOCs processor is installed, is rationally designed by various equipment, combination, realizes that an equipment is more
Kind of purposes, two kinds of purposes of whole system are both pollutant disposal system and regenerating active carbon system, between the two free switching.
And each component cooperating in the exhaust-gas treatment line of VOCs processor is installed, the various pollutants in stepwise disposal exhaust gas,
Treatment effect is more preferable.
Detailed description of the invention
Fig. 1 is the connection relationship diagram for being connected with the VOCs processor of exhaust-gas treatment all-in-one machine.
Fig. 2 is the connection relationship diagram for being equipped with the exhaust-gas treatment line of VOCs processor.
1 exhaust producing device；2 condensers；3 first blowers；4 spray throwers；41 first concentration drying equipments；42 first drugs
Box；5 photochemical catalytic oxidation devices；6 energetic ion reactors；7 second blowers；8 exhaust-gas treatment all-in-one machines；9 second concentration drying equipments；
91 second Medicine boxs；10 steam generators；11 driers；12VOCs processor；13 first circulations pump；131 spray heads；14 is online
Monitoring device；15 chimneys.
Specific embodiment
Embodiment 1
A kind of VOCs processor provided by the utility model, including adsorbent chamber, the lower part of the adsorbent chamber are provided with air inlet
Mouthful, the top of adsorbent chamber is provided with exhaust outlet and gas returning port, and the exhaust outlet and gas returning port are provided with the first valve.The exhaust
Mouthful for be discharged that treated can discharge gas, the gas returning port is used to import the exhaust gas during regenerated carbon other useless
Gas disposal equipment.It is provided with active carbon storing frame in adsorbent chamber, is placed with active carbon in active carbon storing frame.The lower part of adsorbent chamber
It is connected with steam generator 10, the steam generator 10 includes liquid storage chamber, is provided with heating device, the steam in liquid storage chamber
Generator 10 is also connected with the air blower by dry drum to active carbon.First circulation pump, absorption are additionally provided in the adsorbent chamber
Chamber top is provided with spray head 131, and the water inlet pipe of first circulation pump 13 extends to spray liquid case or liquid storage chamber, first circulation pump 13
Water pumping pipe be connected to spray head 131.It is additionally provided in the adsorbent chamber for the drier 11 that active carbon is dry；It is described dry
Dry device 11 can be air-heater, by blowing hot-air dry activated carbon.
In the present embodiment, for being dissolved in water, especially hot water soluble adsorbate, by being sprayed in liquid storage chamber to active carbon
Hot water, dissolve active carbon in adsorbate；It then passes to hot steam and blows remaining adsorbate in dissolution active carbon hole, be finally passed through
The hot-air that drier 11 generates is dried；Blowing molten and heated-air drying collective effect by hot water dissolving, hot steam will be active
Charcoal regeneration.Is first passed through organic nature adsorbate not soluble in water by first circulation pump 13, is made according to " the similar principle that mixes "
The organic solvent cycling elution active carbon in liquid case is sprayed, adsorbate in surface adsorbate and hole is removed；Then pass to steam hair
Remaining adsorbate in the hot water and steam blowout active carbon hole that raw device generates, the hot-air for being finally passed through the generation of drier 11 are dried
It is dry, adsorbate, heated-air drying collective effect are blown out for regenerating active carbon by organic solvent dissolution, hot water and steam physics, needed
When can also spray hot water elution.
It is different according to the physicochemical properties of adsorbate without the active carbon in mobile VOCs processor in the present embodiment,
It is blown and heated-air drying regenerated carbon using solvent dissolution, vapor physics.It can be under the premise of moving active carbon, it will
Adsorbate in aperture is dissolved and is blown out, and removes the adsorbate in active carbon, realizes regenerating active carbon.
Embodiment 2
The utility model also provides a kind of exhaust-gas treatment line for being equipped with above-mentioned VOCs processor, including sequentially connected cold
Condenser 2, spray thrower 4 and photochemical catalytic oxidation device 5, the exhaust pipe phase of the air inlet and photochemical catalytic oxidation device 5 of the VOCs processor
Connection, the gas returning port of VOCs processor are connected to condenser 2.The VOCs processor and photochemical catalytic oxidation device 5 are respectively provided with two,
It is connected by way of in parallel between photochemical catalytic oxidation device 5 between VOCs processor.4 lower part of spray thrower is provided with
One concentration drying equipment 41, the first concentration drying equipment 41 includes the first waste collection chamber, the inlet of the first waste collection chamber
It is connected with spray thrower 4 and condenser 2；First waste collection chamber top is provided with the first dosing mouth and the first steam outlet,
First dosing mouth is connected with the first Medicine box 42.First waste collection is intracavitary to be additionally provided with the first temperature detect switch (TDS) and the first heating
Device, the first temperature detect switch (TDS) are connected with primary heater.
Further, exhaust-gas treatment all-in-one machine 8, institute are additionally provided between the photochemical catalytic oxidation device 5 and VOCs processor
Stating exhaust-gas treatment all-in-one machine 8 includes tower body, is provided with energetic ion reaction chamber and spray chamber in tower body.The lower part of the tower body connects
It is connected to air inlet pipe, air inlet pipe is connected with energetic ion reaction chamber, is provided with energetic ion pipe in the energetic ion reaction chamber.
Energetic ion reaction chamber top is additionally provided with gas outlet, and gas outlet is connected to the lower part of spray chamber by gas transport pipe.
Spray chamber is connected with second circulation pump, the water inlet of second circulation pump pass through respectively two water inlet pipes be connected with chemical tank and
The collecting tank of spray chamber lower part, two water inlet pipes are mounted on the second valve, and the top of the spray chamber is also connected with escape pipe.
Energetic ion reaction chamber and spray chamber is arranged in above-mentioned exhaust-gas treatment all-in-one machine 8 in a tower body, can be effective
Using space in tower body, the cost of emission-control equipment is saved, occupied area is also reduced.Exhaust gas is able to carry out height in tower body
Energy ionic reaction, then the remaining chemical substance after spray removal energetic ion reaction, prevents energetic ion reaction or light from urging
The substances such as the ozone added during oxidation etc. do not react completely, prevent the substances such as ozone from remaining, reduce secondary dirt
Dye；The lyotrope in removing exhaust gas also can be further removed simultaneously, further improve exhaust-gas treatment ability.
Further, the liquid collecting bottom of pond portion is also connected with outlet tube, and outlet tube is connected with the second concentration drying equipment
9, the second concentration drying equipment 9 includes the second waste collection chamber, and the inlet of the second waste collection chamber is connected with outlet tube；The
Two waste collection chamber tops are provided with the second dosing mouth and the second steam outlet, and the second dosing mouth is connected with the second Medicine box
91.Second waste collection is intracavitary to be additionally provided with secondary heater and the second temperature detect switch (TDS), the second temperature detect switch (TDS) and secondary heater
It is connected.The setting of the second concentration drying equipment 9 can carry out subsequent processing to spray liquid in spray chamber, pass through dosing
Drug, which is added, in mouth makes volatile matter qualitative response in condensate liquid and spray liquid, then removes moisture removal by secondary heater heating.
In the present embodiment, the exhaust-gas treatment line for being equipped with VOCs processor is rationally designed by various equipment, is combined, and is realized
One equipment multiple use, two kinds of purposes of whole system are both pollutant disposal system and regenerating active carbon system, the two it
Between free switching.And each component cooperating in the exhaust-gas treatment line of VOCs processor is installed, in stepwise disposal exhaust gas
Various pollutants, treatment effect are more preferable.VOCs processor and photochemical catalytic oxidation device 5 are respectively provided with two, and VOCs processor and light are urged
A use can be selected as needed by changing when oxidator 5 uses, and also can be used simultaneously, and also be facilitated in the case where not stopping handling exhaust gas
Maintenance processing is carried out to VOCs processor and photochemical catalytic oxidation device 5.The setting of the concentration drying equipment, can be to condensation
Liquid and highly concentrated spray liquid carry out subsequent processing, and drug, which is added, by dosing mouth makes volatile substances in condensate liquid and spray liquid
Then reaction removes moisture removal by primary heater heating.
Certainly, the above description is not intended to limit the present invention, and the utility model is also not limited to the example above,
The variations, modifications, additions or substitutions that those skilled in the art are made in the essential scope of the utility model, are also answered
Belong to the protection scope of the utility model.
Claims (9)
1. a kind of VOCs processor, including adsorbent chamber, the lower part of the adsorbent chamber is provided with air inlet, the top setting of adsorbent chamber
There are exhaust outlet and gas returning port；It is provided with active carbon storing frame in adsorbent chamber, is placed with active carbon in active carbon storing frame；Its feature
It is, the lower part of adsorbent chamber is connected with steam generator, and the steam generator includes liquid storage chamber, and heating is provided in liquid storage chamber
Device, the steam generator are also connected with the air blower by dry drum to active carbon.
2. a kind of VOCs processor as described in claim 1, which is characterized in that be additionally provided with first circulation in the adsorbent chamber
Pump, adsorbent chamber top is provided with spray head；The water inlet pipe of first circulation pump extends to spray liquid case or liquid storage chamber, first circulation pump
Water pumping pipe be connected to spray head.
3. a kind of VOCs processor as described in claim 1, which is characterized in that be additionally provided in the adsorbent chamber for that will live
Property the dry drier of charcoal.
4. installing the exhaust-gas treatment line just like VOCs processor described in claims 1 to 3 any one, which is characterized in that including
Sequentially connected condenser, spray thrower and photochemical catalytic oxidation device, air inlet and the photochemical catalytic oxidation device of the VOCs processor
Exhaust pipe is connected, and the gas returning port of VOCs processor is connected to condenser.
5. exhaust-gas treatment line as claimed in claim 4, which is characterized in that the VOCs processor and photochemical catalytic oxidation device are all provided with
Two are set, is connected by way of in parallel between photochemical catalytic oxidation device between VOCs processor.
6. exhaust-gas treatment line as claimed in claim 4, which is characterized in that the spray thrower lower part is provided with the first concentration desiccation
Equipment, the first concentration drying equipment include the first waste collection chamber, the inlet of the first waste collection chamber and spray thrower and condensation
Device is connected；First waste collection chamber top is provided with the first dosing mouth and the first steam outlet, and the first waste collection is intracavitary
It is additionally provided with primary heater.
7. exhaust-gas treatment line as claimed in claim 4, which is characterized in that between the photochemical catalytic oxidation device and VOCs processor
It is additionally provided with exhaust-gas treatment all-in-one machine, the exhaust-gas treatment all-in-one machine includes tower body, and energetic ion reaction chamber is provided in tower body
And spray chamber；The lower part of the tower body is connected with air inlet pipe, and air inlet pipe is connected with energetic ion reaction chamber, the energetic ion
Energetic ion pipe is provided in reaction chamber；
Energetic ion reaction chamber top is additionally provided with gas outlet, and gas outlet is connected under spray chamber by gas transport pipe
Portion；Spray chamber is connected with second circulation pump, and the water inlet of the second circulation pump passes through two water inlet pipes respectively and is connected with medicament
The collecting tank of case and spray chamber lower part, two water inlet pipes are mounted on the second valve, and the top of the spray chamber is also connected with outlet
Pipe.
8. exhaust-gas treatment line as claimed in claim 7, which is characterized in that the liquid collecting bottom of pond portion is also connected with outlet tube, out
Liquid pipe is connected with the second concentration drying equipment, and the second concentration drying equipment includes the second waste collection chamber, the second waste collection chamber
Inlet be connected with outlet tube；Second waste collection chamber top is provided with the second dosing mouth and the second steam outlet, the
Two waste collections are intracavitary to be additionally provided with secondary heater.
9. the exhaust-gas treatment line as described in claim 6 or 8, which is characterized in that waste collection chamber lower part is also equipped with temperature control and opens
It closes, temperature detect switch (TDS) is connected with heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820471551.XU CN208161311U (en) | 2018-04-04 | 2018-04-04 | Active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820471551.XU CN208161311U (en) | 2018-04-04 | 2018-04-04 | Active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208161311U true CN208161311U (en) | 2018-11-30 |
Family
ID=64373272
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820471551.XU Expired - Fee Related CN208161311U (en) | 2018-04-04 | 2018-04-04 | Active carbon VOCs processor and the exhaust-gas treatment line for being equipped with the processor |
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| CN (1) | CN208161311U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607532A (en) * | 2018-04-04 | 2018-10-02 | 王惠勇 | Activated carbon adsorption regenerator and the exhaust-gas treatment line for being equipped with adsorbing regenerator |
-
2018
- 2018-04-04 CN CN201820471551.XU patent/CN208161311U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607532A (en) * | 2018-04-04 | 2018-10-02 | 王惠勇 | Activated carbon adsorption regenerator and the exhaust-gas treatment line for being equipped with adsorbing regenerator |
| CN108607532B (en) * | 2018-04-04 | 2023-09-01 | 王惠勇 | Activated carbon adsorption regenerator and exhaust gas treatment line provided with same |
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
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| CF01 | Termination of patent right due to non-payment of annual fee |