CN208244416U - VOCs exhaust treatment system - Google Patents
VOCs exhaust treatment system Download PDFInfo
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- CN208244416U CN208244416U CN201820584332.2U CN201820584332U CN208244416U CN 208244416 U CN208244416 U CN 208244416U CN 201820584332 U CN201820584332 U CN 201820584332U CN 208244416 U CN208244416 U CN 208244416U
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- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 27
- 239000007789 gas Substances 0.000 claims abstract description 164
- 239000002912 waste gas Substances 0.000 claims abstract description 30
- 238000001179 sorption measurement Methods 0.000 claims abstract description 29
- 238000000746 purification Methods 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 15
- 210000003437 trachea Anatomy 0.000 claims abstract description 5
- 238000005192 partition Methods 0.000 claims description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 230000001590 oxidative effect Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract 1
- 239000004215 Carbon black (E152) Substances 0.000 description 5
- 229930195733 hydrocarbon Natural products 0.000 description 5
- 150000002430 hydrocarbons Chemical class 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 239000005864 Sulphur Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000003916 acid precipitation Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910000892 beryllide Inorganic materials 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Natural products O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000009429 distress Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000013056 hazardous product Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 229910052704 radon Inorganic materials 0.000 description 1
- SYUHGPGVQRZVTB-UHFFFAOYSA-N radon atom Chemical compound [Rn] SYUHGPGVQRZVTB-UHFFFAOYSA-N 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000000271 synthetic detergent Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of VOCs exhaust treatment system, it includes sequentially connected emission-control equipment, waste gas burner and gas cooling device, wherein, emission-control equipment includes the second clean room for being set to the waste gas purification component bottom, third clean room, the first clean room being set to above second clean room and the adsorption chamber being set to above the third clean room, second clean room and first clean room, it is connected by trachea between third clean room and adsorption chamber and the third clean room, first clean room is connected to first air inlet, the adsorption chamber is connected to first gas outlet.Technical solutions of the utility model make exhaust gas by sufficiently treated product be liquid water pollution-free and can be used directly, the advantages of protecting atmospheric environment, reached environmental purification.
Description
Technical field
The utility model relates to exhaust-gas treatment field more particularly to a kind of VOCs exhaust treatment systems.
Background technique
In industrial processes of today, exhaust gas will necessarily be generated, if these exhaust gas are just discharged into sky without processing
Environment will certainly be impacted in gas.Wherein gaseous state exhaust gas is that most species are also that harmfulness is maximum in industrial waste gas.
Mainly have in VOCs exhaust gas at present nitrogenous organic exhaust gas, sulphur-containing exhaust gas and hydrocarbon organic exhaust gas (such as: alkanes, aromatic hydrocarbons, ester
Class, aldehydes and other etc.).And existing waste gas burning processing when often ignore have in exhaust gas the gas for being difficult to burn and
It can be generated after burning to environment and the harmful gas of human body, can be drawn when above-mentioned gas is directly burned and is emitted into atmosphere
The pollution for playing atmosphere is very easy to cause the direct natural calamity such as acid rain, and there are also cumulative effects for some, can be more serious
Endanger the health of people.
Therefore, it is necessary to provide the new VOCs exhaust treatment system of one kind to solve above-mentioned technical problem.
Utility model content
The main purpose of the utility model is to provide a kind of VOCs exhaust treatment system, it is intended to solve in distress in the prior art
Product does not obtain the problem of handling after being disposed to atmosphere with the gas for processing of burning and burnt.
To achieve the above object, the utility model proposes a kind of VOCs exhaust treatment system, including it is sequentially connected useless
Flash Gas Compression Skid System, waste gas burner and gas cooling device;
The emission-control equipment includes sequentially connected first air inlet, waste gas purification component and the first gas outlet;
The waste gas burner includes sequentially connected second air inlet, waste gas burning component and the second gas outlet;
The gas cooling device includes sequentially connected third air inlet, cooling chamber and outlet;
Second air inlet is connected to first gas outlet, and the third air inlet is connected to second gas outlet;
The waste gas purification component includes the second clean room for being set to the waste gas purification component bottom, third purification
Room, the first clean room being set to above second clean room and the adsorption chamber being set to above the third clean room,
Exhaust gas sequentially enters first clean room, the second clean room, third clean room and adsorption chamber by trachea, and described first
Clean room is connected to first air inlet, and the adsorption chamber is connected to first gas outlet.
Preferably, second clean room and the third clean room are embedded in below ground.
Preferably, activated carbon adsorption part and the pure adsorption piece of diatom are provided in the adsorption chamber.
Preferably, the bottom of first clean room, the second clean room and third clean room is provided with solution, described
The surface of solution is provided with the first partition panel for completely cutting off gas and liquid and is set on first partition panel simultaneously
Perpendicular to first partition panel and for separating the second partition panel of the clean room, offered on first partition panel
For entering exhaust gas and the stomata of exhaust gas being discharged, second partition panel is all connected to first clean room, the second clean room
And the top of third clean room.
Preferably, muti-piece is provided in the solution for improving the baffle plate of exhaust gas Yu the solution time of contact.
Preferably, being set to the indoor solution of first purification is strong acid solution, is set to second purification
The indoor solution is strong base solution, and being set to the third and purifying the indoor solution is strong oxidizing solution.
Preferably, the waste gas burning component includes sequentially connected gas mixer chamber, multiple gas delivery tubes, igniter
And the gas collector for collecting burnt gas, the gas mixer chamber are connected to second air inlet, the gas
Collector is connected to second gas outlet, is provided with air air inlet, multiple gas delivery tubes in the gas mixing room
One end be all connected to gas mixer chamber, be provided with igniter on the other end of multiple gas delivery tubes.
Preferably, the cavity of the gas mixer chamber is formed as cone, and one end connection described first of the cavity goes out
Port, the other end of the cavity are connected with mounting plate, and multiple gas delivery tubes are connected on the mounting plate.
Preferably, air pump is provided on the gas collector.
Preferably, it is provided with multiple condenser pipes in the cavity of the cooling chamber, liquid water is accommodated in the cavity, it is described
Condenser pipe is located at below the water surface of the liquid water, and multiple described condenser pipe one end are connected to the third air inlet, described cold
The solidifying pipe other end is connected to the outlet.
In the technical solution of the utility model, using sequentially connected emission-control equipment, waste gas burner and gas
Body cooling device is successively handled exhaust gas, will be difficult to burned exhaust gas in exhaust gas first and is carried out in emission-control equipment
Processing, wherein the structure cloth of the first clean room, the second clean room, third clean room and adsorption chamber in emission-control equipment
It sets so that the structure of emission-control equipment is more compact, utilization rate reaches maximum.The gas that then passes through that treated is by exhaust gas
After burner, the product to be burnt enters gas cooling device and condenses to product, condensed liquid water energy
Enough directly uses so that current exhaust gas can effectively simultaneously safe discharge, while the product of exhaust gas can obtain it is optimal
It utilizes, achievees the effect that refuse reclamation.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, the structure that can also be shown according to these attached drawings obtains other attached drawings.
Fig. 1 is the structural schematic diagram of the VOCs exhaust treatment system of the utility model embodiment;
Fig. 2 is the structural schematic diagram of the emission-control equipment of the utility model embodiment;
Fig. 3 is the structural schematic diagram of the waste gas burner of the utility model embodiment;
Fig. 4 is the structural schematic diagram of the gas cooling chamber of the utility model embodiment.
Drawing reference numeral explanation:
The embodiments will be further described with reference to the accompanying drawings for the realization, functional characteristics and advantage of the utility model aim.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describing, it is clear that described embodiment is only a part of the embodiment of the utility model, rather than all
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are not making creative work premise
Under every other embodiment obtained, fall within the protection scope of the utility model.
It is to be appreciated that the directional instruction (such as up, down, left, right, before and after ...) of institute in the utility model embodiment
It is only used for explaining in relative positional relationship, the motion conditions etc. under a certain particular pose (as shown in the picture) between each component, such as
When the fruit particular pose changes, then directionality instruction also correspondingly changes correspondingly.
In addition, the description for being such as related to " first ", " second " in the present invention is used for description purposes only, and cannot manage
Solution is its relative importance of indication or suggestion or the quantity for implicitly indicating indicated technical characteristic.Define as a result, " the
One ", the feature of " second " can explicitly or implicitly include at least one of the features.It is " more in the description of the present invention,
It is a " it is meant that at least two, such as two, three etc., unless otherwise specifically defined.
Also, the technical solution between each embodiment of the utility model can be combined with each other, but must be with ability
Based on domain those of ordinary skill can be realized, it will be understood that when the combination of technical solution appearance is conflicting or cannot achieve
The combination of this technical solution is not present, also not within the protection scope of the requires of the utility model.
The utility model provides a kind of VOCs exhaust treatment system, it is intended to which solution has in the prior art is difficult to processing of burning
Gas is disposed to the problem of not obtaining processing of product after atmosphere and burning.
As shown in Figure 1, VOCs exhaust treatment system includes sequentially connected emission-control equipment 10, waste gas burner 20
And gas cooling device 30.Wherein, emission-control equipment 10 includes sequentially connected first air inlet 101, waste gas purification group
Part (not indicating) and the first gas outlet 102.Waste gas burner 20 includes sequentially connected second air inlet 201, exhaust gas combustion
Burn component (not indicating) and the second gas outlet 202.Gas cooling device includes sequentially connected third air inlet 301, cooling
Room (not indicating) and outlet 302.Also, the second air inlet 201 is connected to the first gas outlet 102, the connection of third inlet gas 301 the
Two gas outlets 202.
As shown in Fig. 2, waste gas purification component includes the second clean room 104 for being set to waste gas purification component bottom, third
Clean room 105, the first clean room 103 for being set to the top of the second clean room 104 and it is set to 105 top of third clean room
Adsorption chamber 106.Meanwhile exhaust gas sequentially enters the first clean room 103, the second clean room 104, third purification by trachea 107
Room 105 and adsorption chamber 106, also, the first clean room 103 is connected to the first air inlet 101, and adsorption chamber 106 is connected to the first outlet
Mouth 102.
Specifically, VOCs exhaust gas mainly includes nitrogenous organic exhaust gas, hydrocarbon organic exhaust gas, sulphur-containing exhaust gas and other exhaust gas
(such as: fluoride, hydrogen chloride, beryllide, flue dust and industrial dust), if sulphur-containing exhaust gas therein, nitrogenous exhaust gas and its
When the corresponding product withdraw generated after his exhaust gas is burned is into atmosphere, the direct natural calamity such as acid rain is easily caused, and
There are also cumulative effect, the more serious health for endangering people of meeting for some.And in the present embodiment, VOCs exhaust gas from A first into
After port 101 enters, the first clean room 103, the second clean room 104 and third clean room 105 can be sequentially entered, respectively will
After sulphur-containing exhaust gas, nitrogenous exhaust gas and other waste gas purifications, the residue that absorption 106 takes away exhaust gas out of clean room is finally entered
And the product absorption of production is walked, so that the exhaust gas from A1 at discharge only contains only hydrocarbon organic exhaust gas, and it is hydrocarbon
Organic exhaust gas will become vapor and CO2 (carbon dioxide) after the burning of waste gas burning component, finally by vapor
By gas cooling device 30, enables vapor become liquid water discharge, be able to use VOCs exhaust gas conversion to reach
The purpose of liquid water further enhances the recycling of exhaust gas on the basis of protecting natural environment, realizes waste benefit
With.
Further, the second clean room 104 and third clean room 105 be embedded and below ground, it is preferable that first is net
Change room 103 and adsorption chamber 106 is all set in ground or more, trachea 107 is directly connected to ground the second clean room 104 below
And third clean room 105.In above-mentioned preferred embodiment, because the first clean room 103, second in waste gas purification component is net
Change the compact-sized of room 104, third clean room 105 and adsorption chamber 106, so that the utilization rate of product reaches maximization.Certainly,
In other examples, the first clean room 103, the second clean room 104, third clean room 105 and adsorption chamber 106 can be equal
It is set to below ground, it is only necessary to which the first air inlet pipe 101 and the first escape pipe 102 are provided projectingly on ground or more to connect
Other pipelines.It is, of course, also possible to only be provided projectingly some component, for example only the first clean room 103 is set to ground
More than, to be adapted to the landform that other are not suitable for installation.
In above-mentioned preferred embodiment, activated carbon adsorption part 1061 and the pure absorption of diatom are provided in adsorption chamber 106
Part 1062.Activated carbon adsorption part 1061 can remove deliquescent organic substance, synthetic detergent, microorganism, virus and one
Quantitative heavy metal, and can decolourize, deodorization.And there is the pure adsorption piece 1062 of diatom extremely strong physical adsorption property and ion to hand over
It is transsexual can, thus can the pernicious gases such as effective formaldehyde adsorption, benzene, radon, TOVC.
In addition, the bottom of the first clean room 103, the second clean room 104 and third clean room 105 is provided with solution
108, the surface of solution 108 is provided with the first partition panel 109 for completely cutting off gas and liquid and is set to the first partition
The second partition panel 110 on plate 109 and perpendicular to the first partition panel 109 and for separating above-mentioned clean room.Meanwhile first separates
It is offered on plate 109 for entering exhaust gas and the stomata (not shown) of exhaust gas being discharged, and second short slab is all connected to
State the top of clean room.
Further, muti-piece is provided in solution 108 for improving the baffle plate of exhaust gas Yu 108 time of contact of solution
111, so that currency of the gas in solution 108 increases, the reaction rate of gas and solution is improved, and then improve useless
The treatment effeciency of gas.
In this embodiment, VOCs exhaust gas, which passes through, successively enters in 102 in the first clean room from the first air inlet 101, and
After being reacted from the first clean room 103 with the solution 108 of the first clean room 103 enter the second clean room 104, and with the second clean room
Solution 108 in 104 enters third clean room 105 after reacting, and after being reacted with the solution 108 in third clean room 105
Into adsorption chamber 106, then it is discharged from the first gas outlet 102 of adsorption chamber 106.Meanwhile exhaust gas can be in multiple partition panels
It under effect, is merely able to enter in solution 108 and reacted with solution 108, so that be difficult to can after burning or burning by certain
It generates the gas for generating hazardous material to environment and human body to react, directly reduces exhaust gas bring environmental pollution, in turn
The purity of product after improving subsequent waste gas burning has ensured the quality for recycling product.
Wherein, the solution 108 being set in the first clean room 103 is strong acid solution, is set in the second clean room 108
Solution 108 is strong base solution, and the solution 108 being set in third clean room 108 is strong oxidizing solution.Pass through strong acid, highly basic
The waste gas purification mode that chemical mode is carried out with strong oxidizer, react away be difficult to it is burned or can generate after burning to environment and
The harmful gas of human body.
As shown in figure 3, waste gas burning component 30 includes sequentially connected gas mixer chamber 203, multiple gas delivery tubes
205, igniter (not shown) and the gas collector 207 for collecting burnt gas.Wherein, gas mixing formula 203 connects
Logical second air inlet 201, gas collector 207 are connected to the second gas outlet 202, are provided with air air inlet in gas mixing room
204, one end of multiple gas delivery tubes 205 is all connected on gas mixer chamber 203, the other end of multiple gas delivery tubes 205
On be provided with igniter.
In the present embodiment, from emission-control equipment treated hydrocarbon exhaust gas that gas discharges from A1 by second into
Port 201 enter gas mixer chamber 203 in, and air air inlet 204 be used for by air be emitted into gas mixer chamber 203 with
Exhaust gas is mixed, so that exhaust gas is adequately mixed with air.Mixed gas is transmitted to gas along gas delivery tube 205
It at body collector 207, and burns in the exit of gas delivery tube 205, mixed gas is burnt into vapor, into
And it is discharged from the second gas outlet A2 202.Also, protective shell 208 is provided with to protect gas in the periphery of multiple gas delivery tubes
Body transfer tube 205.
Wherein, the cavity of gas mixer chamber 203 is formed as cone, and one end of cavity connects the first gas outlet 201, cavity
The other end be connected with mounting plate 206, be connected with multiple gas delivery tubes 205 on mounting plate 206, conical cavity be convenient for from
The gas and adequately mix from the air that air air inlet 204 enters that A1 enters, prevent in combustion because mixing not
The explosion accident uniformly caused occurs.
Further, air pump (not shown), the gas are provided on gas collector 207 and at the second gas outlet 202
When pump can not be completely exhausted out in gas collector 207, gas bleeding is to be completely exhausted out.
In addition, being provided with multiple condenser pipes 303 in the cavity of cooling chamber (not indicating), liquid water is accommodated in the cavity
304, the condenser pipe 303 is located at below the water surface of liquid water 304, and multiple described 303 one end of condenser pipe are connected to the third
Air inlet 301, the condenser pipe other end connection outlet 302.
In this embodiment, gas enters at the third air inlet 301 from A2, and liquid water enters from water inlet 305,
It is flowed out from 306, when gas is flowed through from multiple condenser pipes 303, water can be condensated into because of the effect of liquid water 304, thus
It flows out from outlet 302, and is collected at B.To reach VOCs exhaust gas after conversion, burning, condensing again
The effect for becoming usable water further improves the utilization of resources of exhaust gas, and then protects whole ecological environment.
The above is only the preferred embodiment of the present invention, and therefore it does not limit the scope of the patent of the utility model,
Under all utility models in the utility model are conceived, equivalent structure made based on the specification and figures of the utility model
Transformation, or directly/be used in other related technical areas indirectly and be included in the scope of patent protection of the utility model.
Claims (10)
1. a kind of VOCs exhaust treatment system, which is characterized in that the VOCs exhaust treatment system includes sequentially connected exhaust gas
Processing unit, waste gas burner and gas cooling device;
The emission-control equipment includes sequentially connected first air inlet, waste gas purification component and the first gas outlet;
The waste gas burner includes sequentially connected second air inlet, waste gas burning component and the second gas outlet;
The gas cooling device includes sequentially connected third air inlet, cooling chamber and outlet;
Second air inlet is connected to first gas outlet, and the third air inlet is connected to second gas outlet;
The waste gas purification component includes the second clean room for being set to the waste gas purification component bottom, third clean room, sets
The first clean room being placed in above second clean room and the adsorption chamber being set to above the third clean room, exhaust gas are logical
It crosses trachea and sequentially enters first clean room, the second clean room, third clean room and adsorption chamber, first clean room
It is connected to first air inlet, the adsorption chamber is connected to first gas outlet.
2. VOCs exhaust treatment system as described in claim 1, which is characterized in that second clean room and the third
Clean room is embedded in below ground.
3. VOCs exhaust treatment system as described in claim 1, which is characterized in that be provided with active carbon suction in the adsorption chamber
Attachment and the pure adsorption piece of diatom.
4. VOCs exhaust treatment system as described in claim 1, which is characterized in that first clean room, the second clean room
And the bottom of third clean room is provided with solution, the surface of the solution is provided with for completely cutting off gas and liquid
It one partition panel and is set on first partition panel and perpendicular to first partition panel and for separating the clean room
The second partition panel, offer on first partition panel for entering exhaust gas and the stomata of exhaust gas being discharged, described second every
Disconnected plate is all connected to the top of first clean room, the second clean room and third clean room.
5. VOCs exhaust treatment system as claimed in claim 4, which is characterized in that be provided with muti-piece in the solution and be used for
Improve the baffle plate of exhaust gas and the solution time of contact.
6. VOCs exhaust treatment system as claimed in claim 4, which is characterized in that be set to the indoor institute of first purification
Stating solution is strong acid solution, and being set to the indoor solution of second purification is strong base solution, and it is net to be set to the third
Changing the indoor solution is strong oxidizing solution.
7. VOCs exhaust treatment system as claimed in any one of claims 1 to 6, which is characterized in that the waste gas burning component packet
Include sequentially connected gas mixer chamber, multiple gas delivery tubes, igniter and the gas collection for collecting burnt gas
Device, the gas mixer chamber are connected to second air inlet, and the gas collector is connected to second gas outlet, the gas
Air air inlet is provided in mixing chamber, one end of multiple gas delivery tubes is all connected to gas mixer chamber, multiple described
Igniter is provided on the other end of gas delivery tube.
8. VOCs exhaust treatment system as claimed in claim 7, which is characterized in that the cavity of the gas mixer chamber is formed as
One end of cone, the cavity connects first gas outlet, and the other end of the cavity is connected with mounting plate, the installation
Multiple gas delivery tubes are connected on plate.
9. VOCs exhaust treatment system as claimed in claim 7, which is characterized in that be provided with gas on the gas collector
Pump.
10. VOCs exhaust treatment system as claimed in claim 7, which is characterized in that be provided in the cavity of the cooling chamber
Multiple condenser pipes accommodate liquid water in the cavity, and the condenser pipe is located at below the water surface of the liquid water, multiple described
Condenser pipe one end is connected to the third air inlet, and the condenser pipe other end is connected to the outlet.
Priority Applications (1)
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CN201820584332.2U CN208244416U (en) | 2018-04-23 | 2018-04-23 | VOCs exhaust treatment system |
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CN201820584332.2U CN208244416U (en) | 2018-04-23 | 2018-04-23 | VOCs exhaust treatment system |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110822454A (en) * | 2019-10-29 | 2020-02-21 | 芜湖职业技术学院 | Waste gas treatment environment-friendly device suitable for small-size workplace |
CN114682086A (en) * | 2020-12-31 | 2022-07-01 | 中国石油化工股份有限公司 | Method and device for treating nitrogen-containing organic waste gas |
CN117379947A (en) * | 2023-12-11 | 2024-01-12 | 龙口市化工厂 | Grain tobacco fumigation sulfuryl fluoride gas adsorption purification device |
-
2018
- 2018-04-23 CN CN201820584332.2U patent/CN208244416U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110822454A (en) * | 2019-10-29 | 2020-02-21 | 芜湖职业技术学院 | Waste gas treatment environment-friendly device suitable for small-size workplace |
CN114682086A (en) * | 2020-12-31 | 2022-07-01 | 中国石油化工股份有限公司 | Method and device for treating nitrogen-containing organic waste gas |
CN117379947A (en) * | 2023-12-11 | 2024-01-12 | 龙口市化工厂 | Grain tobacco fumigation sulfuryl fluoride gas adsorption purification device |
CN117379947B (en) * | 2023-12-11 | 2024-02-20 | 龙口市化工厂 | Grain tobacco fumigation sulfuryl fluoride gas adsorption purification device |
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