CN207562623U - A kind of adsorbent equipment of coating cloud exhaust gas - Google Patents
A kind of adsorbent equipment of coating cloud exhaust gas Download PDFInfo
- Publication number
- CN207562623U CN207562623U CN201721894903.4U CN201721894903U CN207562623U CN 207562623 U CN207562623 U CN 207562623U CN 201721894903 U CN201721894903 U CN 201721894903U CN 207562623 U CN207562623 U CN 207562623U
- Authority
- CN
- China
- Prior art keywords
- fixing bracket
- layer
- adsorbent equipment
- cavity
- outlet side
- 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.)
- Active
Links
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a kind of adsorbent equipment of coating cloud exhaust gas, is provided with adsorbent chamber in adsorbent equipment, is obliquely provided with multilayer fixing bracket in adsorbent chamber from top to bottom, activated carbon cotton is uniformly provided on fixing bracket, multilayer fixing bracket joins end to end successively；The inlet end of adsorbent equipment has gradually increased longitudinal cross-section product from outer to inner；The outlet side from-inner-to-outer of adsorbent equipment is accumulated with diminishing longitudinal cross-section.The adsorbent equipment of the utility model can effectively remove the VOCs in the coating cloud exhaust gas in paint spray booth or combined padding and drying system.
Description
Technical field
It is more particularly to a kind of for coating cloud exhaust gas of the processing containing VOCs the utility model is related to technical field of environment protection equipment
Adsorbent equipment.
Background technology
Paint spray booth and combined padding and drying system generate a large amount of coating cloud exhaust gas in operation process, and coating cloud exhaust gas has VOCs（Volatility
The abbreviation of organic compound）The characteristics of concentration is low, air quantity is big, this kind of coating cloud exhaust gas direct emission can cause serious environment dirty
Dye.After existing way is usually handled coating cloud exhaust gas by water curtain, water mist, then high altitude discharge processing is carried out, however, passing through
Water curtain, water mist processing can only absorb some of particulate matters and micro VOCs, and a large amount of VOCs is discharged into air, can not be done
It is discharged to cleaning, causes environmental pollution.
Utility model content
The purpose of this utility model is to provide a kind of harmful substance that can be effectively removed in coating cloud exhaust gas and can recycle
Coating cloud exhaust treatment system.
To achieve these goals, the utility model provides a kind of adsorbent equipment of coating cloud exhaust gas, is set in adsorbent equipment
There is adsorbent chamber, be obliquely provided with multilayer fixing bracket in adsorbent chamber from top to bottom, uniformly set on fixing bracket active
Charcoal cotton, multilayer fixing bracket join end to end successively；The inlet end of adsorbent equipment is transversal with gradual increased longitudinal direction from outer to inner
Area；The outlet side from-inner-to-outer of adsorbent equipment is accumulated with diminishing longitudinal cross-section.
Further embodiment is that six layers of fixing bracket are provided in adsorbent chamber, and first layer fixing bracket is fixed with the second layer
First cavity of the opening towards inlet end is formed between stent, is formed and opened between third layer fixing bracket and the 4th layer of fixing bracket
Mouth forms opening towards inlet end towards the second cavity of inlet end between layer 5 fixing bracket and layer 6 fixing bracket
Third cavity, between first layer fixing bracket and the roof of adsorbent equipment formed opening towards outlet side the 4th cavity, second
Fiveth cavity of the opening towards outlet side, the 4th layer of fixing bracket and the are formed between layer fixing bracket and third layer fixing bracket
Form sixth cavity of the opening towards outlet side between five layers of fixing bracket, the bottom wall of layer 6 fixing bracket and adsorbent equipment it
Between formed opening towards outlet side the 7th cavity.
The beneficial effects of the utility model are：By being arranged on fixing bracket is inclined in adsorbent chamber, multilayer fixes branch
End to end mode between frame, not only reduces the volume of adsorbent equipment, and improves effective adsorption plane of activated carbon cotton
Product, the resistance that coating cloud exhaust gas is subject to during by fixing bracket is smaller, is conducive to coating cloud exhaust gas quickly through adsorbent chamber.
Description of the drawings
Fig. 1 is the structure diagram of the adsorption system embodiment of the utility model.
Fig. 2 is the structure diagram of the desorption combustion system embodiment of the utility model.
Fig. 3 is the structure diagram of the filter device of the adsorption system embodiment of the utility model.
Fig. 4 is the structure diagram of the adsorbent equipment of the adsorption system embodiment of the utility model.
Fig. 5 is the structure diagram of the desorption case of the desorption combustion system embodiment of the utility model.
Fig. 6 is the structure diagram of the catalytic combustion system of the desorption combustion system embodiment of the utility model.
Fig. 7 is the structure diagram of the heat-exchange device of the desorption combustion system embodiment of the utility model.
The utility model is described in further detail with reference to the accompanying drawings and embodiments.
Specific embodiment
The coating cloud exhaust treatment system of the utility model includes adsorption system and desorption combustion system, passes through adsorption system
Multiple absorption removes the VOCs in the exhaust gas of paint spray booth and combined padding and drying system in operation process, reaches the standard of cleaning discharge, can be straight
Run in and put；It is burnt again by being desorbed combustion system and being desorbed VOCs, is converted into CO2And H2O is discharged.
Referring to Fig. 1, Fig. 1 is the structure diagram of the adsorption system embodiment of the utility model.Arrow in Fig. 1 represents gas
The flow direction of body, the coating cloud exhaust gas generated in paint spray booth 1 are introduced by air inlet pipe 100 in washing pool 2, and washing pool 2 is closing
Pond fills a certain amount of water in washing pool 2, and the side wall of air inlet pipe 100 from washing pool 2 enters and is inserted into the water surface hereinafter, air inlet pipe
Pipeline fan 101 is provided in 100, exhaust gas can be constantly introduced in washing pool 2 by pipeline fan 101, coating cloud exhaust gas warp
After crossing the washing of washing pool 2, the dust in coating cloud exhaust gas is dissolved in the water of washing pool 2, and the upper end of washing pool 2 is provided with air outlet pipe
102, air outlet pipe 102 is connect with exhaust piping 103, and exhaust piping 103 is connect with the inlet end of filter device 3, and filter device 3 is right
Coating cloud exhaust gas is filtered processing, removes oily matter.The outlet side of filter device 3 is connect with the inlet end of adsorbent equipment 4, is inhaled
Adsorption device 4 adsorbs the VOCs in coating cloud exhaust gas, removes VOCs so that and the harmful substance removal in coating cloud exhaust gas is clean,
It can direct emission.The outlet side of adsorbent equipment 4 is connect with downtake pipe 5, is also set between adsorbent equipment 4 and downtake pipe 5
The first centrifugal blower 51 is equipped with, the first centrifugal blower 51 provides power for the flowing of gas, can adjust air draft by frequency control
Amount.It is connected between filter device 3, adsorbent equipment 4 and downtake pipe 5 by pipeline.
Referring to Fig. 2, Fig. 2 is the structure diagram of the desorption combustion system embodiment of the utility model.Arrow table in Fig. 2
Show the flow direction of gas, desorption combustion system includes desorption case 6, catalytic combustion system 7 and heat-exchange device 8, desorption case 6,
It is attached between catalytic combustion system 7 and heat-exchange device 8 by pipeline.Wherein, heat-exchange device 8 includes cold flow pipeline 80
With hot-fluid pipeline 81, hot-fluid pipeline 81 is passed through from cold flow pipeline 80.The inlet end of cold flow pipeline 80 is connect with air blower 82, cold
The outlet side in flow tube road 80 be desorbed case 6 inlet end connect, desorption case 6 and catalytic combustion system 7 between be provided with second from
Scheming 52, the inlet end of catalytic combustion system 7 are connect with being desorbed the outlet side of case 6, the outlet side of catalytic combustion system 7 and hot-fluid
The inlet end connection of pipeline 81, the outlet side of hot-fluid pipeline 81 connect with second exhaust pipe 9, are desorbed in case 6 and are provided with activated carbon
Cotton installation position.
Referring to Fig. 3, Fig. 3 is the structure diagram of the filter device of the adsorption system embodiment of the utility model.Join simultaneously
See Fig. 1, the inside of filter device 3 is hollow structure, and the middle part of filter device 3 is provided with filter chamber 30, vertically on
（The Y direction of Fig. 3）, three layer of first fixing bracket 31,32,33 is arranged at intervals in filter chamber 30 from bottom to top, first fixes
Stent 31,32,33 is laterally（The X-direction of Fig. 3）Be arranged in filter chamber 30, the first fixing bracket 31 can use screen or its
His breathable fixed frame is both provided with coating cloud cotton 300 on the first fixing bracket 31,32,33.
In one end of the inlet end 37 close to filter device 3, set between the first fixing bracket 31 and the first fixing bracket 32
The first closed plate 301 is equipped with, the second closed plate 302 is provided between the first fixing bracket 33 and the roof 34 of filter device 3；
Close to one end of the outlet side 38 of filter device 3, third is provided between the first fixing bracket 31 and the bottom wall 35 of filter device 3
Closed plate 303 is provided with the 4th closed plate 304 between first fixing bracket 32 and the first fixing bracket 33.First fixing bracket
31st, the first cavity 311 is surrounded between third closed plate 303 and bottom wall 35, the first cavity 311 has the connected with inlet end 37
One opening 321；The second cavity 312 is surrounded between first fixing bracket 31, the first closed plate 301 and the first fixing bracket 32, the
Two cavitys 312 have the second opening 322 connected with outlet side 38；First fixing bracket 32, the 4th closed plate 304 and first are solid
Third cavity 313 is surrounded between fixed rack 33, third cavity 313 has the third opening 323 connected with inlet end 37；First is solid
The 4th cavity 314 is surrounded between fixed rack 33, the second closed plate 302 and roof 34, the 4th cavity 314 has to be connected with outlet side 38
The 4th logical opening 324.
The inlet end 37 of filter device 3 has gradually increased longitudinal cross-section product from outer to inner；The outlet of filter device 3
38 from-inner-to-outers is held to be accumulated with diminishing longitudinal cross-section.The arrow in gas flow direction such as Fig. 3 in filter device 3
Shown, coating cloud exhaust gas enters from inlet end 37 in filter device 3, and in the inside of inlet end 37, coating cloud exhaust gas is opened respectively from first
Mouth 321 and third opening 323 enter in the first cavity 311 and third cavity 313.Coating cloud exhaust gas into the first cavity 311,
Enter outlet side 38 after across the first fixing bracket 31；Into the coating cloud exhaust gas in third cavity 313, a part passes through first to consolidate
Enter outlet side 38 after fixed rack 32, another part enters outlet side 38 after passing through the first fixing bracket 33.Due to the first fixation
Coating cloud cotton 300 is both provided on stent 31,32,33, coating cloud cotton 300 has very the oily matter in coating cloud exhaust gas and particulate matter
Good adsorptivity, therefore, after coating cloud cotton 300, oily matter and particulate matter therein are filtered coating cloud exhaust gas.It can basis
Actual needs, first fixing bracket of three layers or more of setting in filter chamber 30, and be respectively provided on every layer of first fixing bracket
Coating cloud cotton.Since the first fixing bracket is laterally set, the volume of filter device is greatly reduced, coating cloud exhaust gas enters filtering dress
It postpones and is divided into multiply air-flow, per one air-flow only by one layer of first fixing bracket, reduce the resistance of coating cloud exhaust gas, favorably
Quickly pass through out of filter device in coating cloud exhaust gas.Multilayered structure in filter device substantially increases effective mistake of coating cloud cotton
Filtering surface accumulates.
Referring to Fig. 4, Fig. 4 is the structure diagram of the adsorbent equipment of the adsorption system embodiment of the utility model.Join simultaneously
See Fig. 1 and Fig. 3, the inside of adsorbent equipment 4 is hollow structure, and the middle part of adsorbent equipment 4 is provided with adsorbent chamber 40, in adsorbent chamber 40
It is obliquely provided with six layer of second fixing bracket 41 from top to bottom, activated carbon cotton 42 is uniformly fixed at the second fixing bracket
On 41, six layer of second fixing bracket 41 joins end to end successively.The second fixing bracket of first layer 41 and the second fixing bracket of the second layer
First cavity 401 of the opening towards inlet end 43, the second fixing bracket of third layer 41 and the 4th layer of second fixation are formed between 41
Second cavity 402 of the opening towards inlet end 43, the second fixing bracket of layer 5 41 and layer 6 second are formed between stent 41
Third cavity 403 of the opening towards inlet end 43 is formed between fixing bracket 41, the second fixing bracket of first layer 41 is filled with absorption
It puts and fourth cavity 404 of the opening towards outlet side 44 is formed between 4 roof, the second fixing bracket of the second layer 41 and third layer the
Fiveth cavity 405 of the opening towards outlet side 44, the 4th layer of second fixing bracket 41 and the 5th are formed between two fixing brackets 41
Layer the second fixing bracket 41 between formed opening towards outlet side 44 the 6th cavity 406, the second fixing bracket of layer 6 41 with
Seventh cavity 407 of the opening towards outlet side 44 is formed between the bottom wall of adsorbent equipment 4.The inlet end 43 of adsorbent equipment 4 is outside
And it is interior with gradually increased longitudinal cross-section product, 44 from-inner-to-outer of outlet side of adsorbent equipment 4 is with diminishing longitudinal direction
Cross-sectional area.As shown by the arrows in figure 4, the inlet end 43 of adsorbent equipment 4 is with filtering for gas flow direction in adsorbent equipment 4
The outlet side 38 of device 3 connects, and the coating cloud exhaust gas after the filtering of filter device 3 enters from inlet end 43 in adsorbent equipment 4, so
The 4th cavity is entered by the second fixing bracket of first layer 41 and the second fixing bracket of the second layer 41 respectively from the first cavity 401 afterwards
404 and the 5th cavity 405, pass through the second fixing bracket of third layer 41 respectively from the second cavity 402 and the 4th layer second is fixed branch
Frame 41 enters the 5th cavity 405 and the 6th cavity 406, passes through 41 He of the second fixing bracket of layer 5 respectively from third cavity 403
The second fixing bracket of layer 6 41 enters the 6th cavity 406 and the 7th cavity 407, finally from the 4th cavity 404, the 5th cavity
405th, the 6th cavity 406 and the 7th cavity 407 enter outlet side 44, due to the activated carbon cotton 42 set on the second fixing bracket 41
There is very strong suction-operated, after coating cloud exhaust gas is by adsorbent equipment 4, main nuisance therein to the VOCs in coating cloud exhaust gas
Matter VOCs is adsorbed, and can directly be discharged by downtake pipe 5.It in other implementations, can also be according to practical need
Will, the number of plies of the second fixing bracket 41 of change.Since the second fixing bracket 41 is obliquely installed and is joined end to end, work is substantially increased
The effective area of property charcoal cotton 42 reduces the volume of adsorbent equipment 4.
Referring to Fig. 5, Fig. 5 is the structure diagram of the desorption case of the desorption combustion system embodiment of the utility model.Simultaneously
Referring to Fig. 1, Fig. 2 and Fig. 4, adsorption system after a period of operation, the activity on the second fixing bracket 41 in adsorbent equipment 4
Charcoal cotton 42 has adsorbed a large amount of VOCs, and the adsorption efficiency of activated carbon cotton 42 is caused to decline, is needed by being desorbed combustion system to work
VOCs on property charcoal cotton 42 carries out desorption burning.Adsorption system is stopped, and the side plate of adsorbent equipment 4 is opened, by adsorbent equipment 4
The second interior fixing bracket 41 takes out, and is transferred in desorption case 6.The inside for being desorbed case 6 is hollow structure, is desorbed in case 6
Portion is provided with desorption chamber 60, is desorbed the fixed installation position that the second fixing bracket 41 is provided in chamber 60, will by the way that position is fixedly mounted
Second fixing bracket 41 is mounted in desorption chamber 60.In the present embodiment, two the second fixing brackets 41 of installation in desorption chamber 60,
Two the second fixing brackets 41 are obliquely arranged in desorption chamber 60, and two the second fixing brackets 41 join end to end.In others
In embodiment, more than two layers of the second fixing bracket 41 can also be set in desorption chamber 60.Two the second fixing brackets 41 will
Desorption chamber 60 is separated into three small cavitys, is respectively two and is open towards the first cavity 601,602 of inlet end 61 and one
The second cavity 603 being open towards outlet side 62.The inlet end 61 for being desorbed case 6 is transversal with gradual increased longitudinal direction from outer to inner
Area, 62 from-inner-to-outer of outlet side for being desorbed case 6 are accumulated with diminishing longitudinal cross-section.The gas flowing being desorbed in case 6
As illustrated by arrows 5, hot-air enters from inlet end 61 in the first cavity 601,602, with the second fixing bracket 41 in direction
Activated carbon cotton 42 contact, the VOCs on activated carbon cotton 42 is desorbed, hot-air when by activated carbon cotton 42, VOCs with
Activated carbon cotton 42 detaches, and VOCs enters in the second cavity 603 together with hot-air, and then entering catalysis from outlet side 62 burns
In device 7, the second centrifuge 52 being desorbed between case 6 and catalytic combustion system 7 provides power for the flowing of gas.Second fixes
Activated carbon cotton 42 on stent 41 is reusable after desorption, can be placed again into adsorbent equipment 4 and use.
Referring to Fig. 6, Fig. 6 is the structural representation of the catalytic combustion system of the desorption combustion system embodiment of the utility model
Figure.Referring also to Fig. 2 and Fig. 5, catalytic combustion system 7 include outer cover 71, shell 72 and inner casing 73, and shell 72 and inner casing 73 are set
In the inside of outer cover 71, the heat-insulation chamber 710 of annular is formed between outer cover 71 and shell 72, is formed back between shell 72 and inner casing 73
Shape runner 720.The inlet end 711 of catalytic combustion system 7 is arranged on the bottom of shell 72, the entrance 721 of back-shaped runner 720 with into
Gas end 711 connects, and the bottom of shell 72 is provided with air supplement entrance 75, and air supplement entrance 75 is located at back-shaped runner 720
At entrance 721.Air supplement entrance 75 is connect with wind turbine, and ozone is supplemented into back-shaped runner 720.Desorption case 6 goes out
Gas end 62 is connect with the inlet end 711 of catalytic combustion system 7, and VOCs gases enter by inlet end 711 in back-shaped runner 720,
It is flowed along the direction shown in the arrow in Fig. 6, enters after back-shaped runner 720 from the outlet 722 of back-shaped runner 720 and heat
In room 730, outlet 722 is connected with heating room 730.After the heating of heat-generating pipe 731, VOCs gases can reach needed for catalysis burning
The temperature wanted.VOCs gases after heating enter in catalytic combustor 740, and three layers of catalysis block are provided in catalytic combustor 740
741, catalysis block 741 uses cellular metal catalytic block or ceramic catalytic block, is catalyzed on block 741 and is attached with a large amount of noble metal
Catalyst, noble metal catalyst use one or more in platinum, palladium, rhodium, silver or ruthenium etc..Since catalysis block 741 has honeycomb
The structure of shape, so as to substantially increase the contact area of VOCs gases and noble metal catalyst so that VOCs gases are in your gold
It fully burns under the catalytic action of metal catalyst, is converted into CO2And H2O, CO2And H2Contain a large amount of heat, finally, CO in O2、
H2The high-temperature mixed gas of O and air enters from the outlet side at the top for being arranged on shell 72 712 in heat-exchange device 8.
Due to generating a large amount of heat in VOCs gas combustion process, the heat in catalytic combustor 740 passes through inner casing 73
Side wall be transferred in back-shaped runner 720, VOCs gases in back-shaped runner 720 are preheated, VOCs gases pass through back-shaped stream
Temperature increases behind road 720, efficiently utilizes the heat that burning generates in catalytic combustor 740, and capacity usage ratio is high.In addition,
The heat-insulation chamber 710 formed between outer cover 71 and shell 72 can prevent the heat in back-shaped runner 720 from distributing outward, reduce energy
Loss.Entrance 75 is supplemented by air, ozone is supplemented into VOCs gases, improve the content of oxygen in VOCs gases,
Be conducive to the abundant burning of VOCs gases.
Referring to Fig. 7, Fig. 7 is the structure diagram of the heat-exchange device of the desorption combustion system embodiment of the utility model.
Referring also to Fig. 2, Fig. 5 and Fig. 6, heat-exchange device 8 include the cold flow pipeline 80 laterally set and longitudinally disposed hot-fluid pipeline
81, more heat-exchange tubes 810 are provided in hot-fluid pipeline 81, cooling fin 811 has been covered on the outer wall of heat-exchange tube 810, and heat is handed over
Pipe 810 is changed to pass through out of cold flow pipeline 8, the inlet end 811 of hot-fluid pipeline 81 is connect with the outlet side 712 of catalytic combustion system 7,
Inlet end 811 has gradual increased transverse cross-sectional area from outer to inner.VOCs burn in catalytic combustion system 7 after high temperature
Mixed gas is entered by inlet end 811 in hot-fluid pipeline 81, from the outlet side of hot-fluid pipeline 81 after heat-exchange tube 810
812 discharges, outlet side 812 are connect with second exhaust pipe 9, and 812 from-inner-to-outer of outlet side has diminishing lateral cross
Product.The inlet end 801 of cold flow pipeline 80 is connect with air blower 82, and inlet end 801 has gradually increased longitudinal direction horizontal stroke from outer to inner
Sectional area.Air blower 82 endlessly introduces air in cold flow pipeline 80, when air flows in cold flow pipeline 80, high temperature
Mixed gas flows in heat-exchange tube 810, heat exchange occurs between air and high-temperature mixed gas, due to heat-exchange tube 810
Outer wall on be covered with cooling fin 811, can be effectively by the heat transfer of the high-temperature mixed gas in heat-exchange tube 810 to cold flow pipe
In road 80, the air of cold flow pipeline 80 absorbs the heat on cooling fin 811, temperature raising, by heat-exchange tube 810 to air into
Row preheating.Assisted heating device is additionally provided in cold flow pipeline 80, assisted heating device includes more heating tubes 800, heating tube
800 abut with the outlet side 802 of cold flow pipeline 80, and the outlet side 802 of cold flow pipeline 80 is connect with being desorbed the inlet end 61 of case 6.
802 from-inner-to-outer of outlet side is accumulated with diminishing longitudinal cross-section.When the temperature of the air by outlet side 802 does not reach
It during to temperature needed for desorption, then is heated by heating tube 800, the VOCs of activated carbon cotton 42 in case 6 is desorbed to meet
Desorption temperature.By heat-exchange device 8, with the cryogenic gas in cold flow pipeline 80 heat occurs for the high-temperature gas in hot-fluid pipeline 81
It exchanges, takes full advantage of the energy of desorption combustion system itself, reduce the temperature for the mixed gas discharged from second exhaust pipe 9
Degree.
Certainly, above-described embodiment is only the preferable embodiment of the utility model, and when practical application can also have more
Variation, for example, being not provided with back-shaped runner in catalytic combustion system, the inlet end of catalytic combustion system is directly connected with heating room；
Or adsorption system is also connect with combined padding and drying system；Repack water curtain room or water mist room into again or by washing pool.These changes equally may be used
To realize the purpose of this utility model, within the spirit and principle of the utility model, any modification for being made equally is replaced
It changes, improve, should be included in the protection domain of the utility model claims.
Claims (2)
1. a kind of adsorbent equipment of coating cloud exhaust gas, it is characterised in that：
Adsorbent chamber is provided in the adsorbent equipment, multilayer fixing bracket is obliquely provided with from top to bottom in the adsorbent chamber,
Activated carbon cotton is uniformly provided on the fixing bracket, fixing bracket described in multilayer joins end to end successively；
The inlet end of the adsorbent equipment has gradually increased longitudinal cross-section product from outer to inner；
The outlet side from-inner-to-outer of the adsorbent equipment is accumulated with diminishing longitudinal cross-section.
2. adsorbent equipment according to claim 1, it is characterised in that：
Six layers of fixing bracket are provided in the adsorbent chamber, fixing bracket described in first layer and fixing bracket described in the second layer
Between form first cavity of the opening towards the inlet end, fixing bracket described in third layer and the 4th layer of fixing bracket it
Between form second cavity of the opening towards the inlet end, between fixing bracket described in fixing bracket described in layer 5 and layer 6
Form third cavity of the opening towards the inlet end, shape between the roof of fixing bracket and the adsorbent equipment described in first layer
Into opening towards the 4th cavity of the outlet side, formed between fixing bracket described in fixing bracket described in the second layer and third layer
The 5th cavity being open towards the outlet side is formed between fixing bracket described in the 4th layer of fixing bracket and layer 5 and is opened
Mouthful towards the outlet side the 6th cavity, opening is formed between the bottom wall of fixing bracket and the adsorbent equipment described in layer 6
Towards the 7th cavity of the outlet side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721894903.4U CN207562623U (en) | 2017-12-28 | 2017-12-28 | A kind of adsorbent equipment of coating cloud exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721894903.4U CN207562623U (en) | 2017-12-28 | 2017-12-28 | A kind of adsorbent equipment of coating cloud exhaust gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207562623U true CN207562623U (en) | 2018-07-03 |
Family
ID=62686281
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721894903.4U Active CN207562623U (en) | 2017-12-28 | 2017-12-28 | A kind of adsorbent equipment of coating cloud exhaust gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207562623U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109647130A (en) * | 2019-01-16 | 2019-04-19 | 河北航天环境工程有限公司 | A kind of novel absorbent charcoal adsorbent equipment |
-
2017
- 2017-12-28 CN CN201721894903.4U patent/CN207562623U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109647130A (en) * | 2019-01-16 | 2019-04-19 | 河北航天环境工程有限公司 | A kind of novel absorbent charcoal adsorbent equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107998763A (en) | Paint spray booth's organic waste gas treatment system | |
| CN207486917U (en) | A kind of integrated kitchen range of lampblack-preventing reflux | |
| CN207762929U (en) | A kind of desorption combustion system of coating cloud exhaust gas | |
| CN108870492A (en) | A kind of center fume purifier of fume | |
| CN107335312A (en) | It is a kind of except the air cleaning unit of haze | |
| CN208432134U (en) | A kind of heat energy from waste gas switch for heat supply | |
| CN207769491U (en) | A kind of coating cloud exhaust treatment system being desorbed manually | |
| CN207562623U (en) | A kind of adsorbent equipment of coating cloud exhaust gas | |
| CN207769502U (en) | A kind of adsorption system of coating cloud exhaust gas | |
| CN110375357A (en) | A kind of range hood and its control method | |
| CN207609464U (en) | A kind of black smoke purification device for diesel generator | |
| CN108151047B (en) | Biomass combustion heat energy full-utilization flue gas purification hot air device | |
| CN208003691U (en) | A kind of heat-exchange device for coating cloud exhaust-gas treatment | |
| CN211041019U (en) | Activated carbon adsorption desorption catalytic combustion equipment | |
| CN108815988A (en) | The Adsorption Concentration system and method for intermittent low concentration volatile organic matter | |
| CN107952333A (en) | A kind of coating cloud exhaust treatment system being desorbed manually | |
| CN107362657A (en) | A kind of noise reduction environmental protection tourie for chemical industry equipment | |
| CN207769433U (en) | A kind of coating cloud exhaust treatment system being continuously desorbed | |
| CN107930293A (en) | A kind of coating cloud exhaust treatment system being continuously desorbed | |
| CN206499897U (en) | A kind of double tower exhaust gas purification and treatment device | |
| JP3221952U (en) | High efficiency desulfurization denitration exhaust gas purification device | |
| CN109589748A (en) | A kind of organic waste gas treatment system and solvent recovery process | |
| CN108579330A (en) | One kind being directed to Wind Volume high concentration polluted air from paint booth governing system and method | |
| CN208742226U (en) | One kind being directed to Wind Volume high concentration polluted air from paint booth governing system | |
| CN104941365B (en) | Purifier for exhaust gas of industrial boiler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |