CN108619820A - A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier - Google Patents
A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier Download PDFInfo
- Publication number
- CN108619820A CN108619820A CN201810643528.9A CN201810643528A CN108619820A CN 108619820 A CN108619820 A CN 108619820A CN 201810643528 A CN201810643528 A CN 201810643528A CN 108619820 A CN108619820 A CN 108619820A
- Authority
- CN
- China
- Prior art keywords
- waste gas
- burning waste
- limited block
- gas purifier
- catalysis burning
- 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.)
- Pending
Links
- 238000006555 catalytic reaction Methods 0.000 title claims abstract description 33
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 33
- 239000002912 waste gas Substances 0.000 title claims abstract description 22
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 21
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 239000010457 zeolite Substances 0.000 title claims abstract description 21
- 239000002808 molecular sieve Substances 0.000 claims abstract description 16
- 238000002485 combustion reaction Methods 0.000 claims abstract description 15
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 239000000428 dust Substances 0.000 claims description 13
- 238000001914 filtration Methods 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 2
- 238000000746 purification Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 26
- 238000000034 method Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 206010014561 Emphysema Diseases 0.000 description 1
- 241000220317 Rosa Species 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000002894 chemical waste Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/62—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series
- B01D46/64—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in series arranged concentrically or coaxially
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/06—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/07—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases in which combustion takes place in the presence of catalytic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2267/00—Multiple filter elements specially adapted for separating dispersed particles from gases or vapours
- B01D2267/40—Different types of filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2267/00—Multiple filter elements specially adapted for separating dispersed particles from gases or vapours
- B01D2267/70—Horizontal arrangement
Abstract
The present invention relates to purifier technical fields, and it discloses a kind of zeolite runner Adsorption Concentration and adds catalysis burning waste gas purifier, including equipment platform, the top of the equipment platform is fixedly connected sequentially has exhaust pipe from left to right, molecular sieve adsorption runner, it is catalyzed combustion box and primary filter case, and exhaust pipe, molecular sieve adsorption runner, pass through the first connecting tube respectively successively from left to right between catalysis combustion box and primary filter case, second connecting tube is connected with third connecting tube, the right side of the water filter box is communicated with conduit, the first axial flow blower is installed between the inner wall of the conduit, the right end of the conduit is communicated with suction hood.The present invention solves existing zeolite runner Adsorption Concentration and adds catalysis burning waste gas cleaning equipment clean-up effect poor, and also very inconvenient problem when moving, has reached good purification, efficient, and to the device it is mobile when very convenient, time saving and energy saving effect.
Description
Technical field
The present invention relates to purifier technical field, specially a kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas net
Makeup is set.
Background technology
Waste gas purification is primarily referred to as the industrial waste gas generated for industrial site such as dust particle, flue gas flue dust, different
The work that taste gas, toxic and harmful gas are administered, common waste gas purification have factory's fume and exhaust gas purifying, workshop dust useless
Gas purification, organic waste-gas purification, the purification of exhaust gas peculiar smell, acid-base waste gas purifying, purification of chemical waste gas etc..
With the development of society, the consciousness of compatriots' environmental protection gradually enhances, the big factory of various pollution discharge capacities is fitted with
Blowdown apparatus is gradually controlled to the blowdown of factory, and existing zeolite runner Adsorption Concentration adds catalysis burning waste gas net
The effect for changing equipment clean is not apparent enough, and polluted gas in exhaust gas is dissolved with more residual, and existing purifier body
Product is excessively huge, very inconvenient when being moved, and needs to carry out carrying work using larger mechanical equipment, bothersome to take
Power.
Invention content
(1) the technical issues of solving
In view of the deficiencies of the prior art, the present invention provides a kind of zeolite runner Adsorption Concentrations to add catalysis burning waste gas purification
Device solves existing zeolite runner Adsorption Concentration and adds catalysis burning waste gas cleaning equipment clean-up effect poor, and in movement
When also very inconvenient problem.
(2) technical solution
To achieve the above object, the present invention provides the following technical solutions：A kind of zeolite runner Adsorption Concentration adds catalysis to burn
Waste gas purification apparatus, including equipment platform, the top of the equipment platform are fixedly connected sequentially have exhaust pipe, molecule from left to right
Sieve adsorption runner, catalysis combustion box and primary filter case, and exhaust pipe, molecular sieve adsorption runner, catalysis combustion box and primary mistake
It is connected respectively with third connecting tube by the first connecting tube, the second connecting tube successively from left to right between filter box, the water filter
The right side of case is communicated with conduit, and the first axial flow blower, the right end of the conduit are installed between the inner wall of the conduit
It is communicated with suction hood, activated carbon mistake is installed with successively from left to right between the inner roof wall and inner bottom wall of the primary filter case
Filtering layer and filtering dust layer, the third connecting tube are installed with the second axial flow blower between top ratio and inner bottom wall, institute
Four edges for stating equipment platform bottom are installed with holder, and the lower end of the holder is hinged with idler wheel by pin,
The side of the holder is inlaid with the first screwed pipe, and the inner ring of first screwed pipe is threaded with the first bolt, two institutes
The opposite one end of the first bolt is stated to run through the side of holder and be connected with fixed block, the fixation by first bearing seat
The bottom of block is fixedly connected with slide bar, and the second screwed pipe, the inner ring of second screwed pipe are inlaid at the top of the fixed block
It is threaded with the second bolt, and the lower end of the second bolt through fixed block and is connected with limit by second bearing seat
Block, one side of the limited block far from idler wheel is fixedly connected with lantern ring, and lantern ring is actively socketed on the outside of slide bar.
Preferably, the transverse horizontal length value between the activated carbon filter layer and filtering dust layer is five centimetres.
Preferably, the level height value at the top of exhaust pipe is more than molecular sieve adsorption runner, catalysis combustion box and primary filter
The top level elevation value of case.
Preferably, limited block is located at the lower section of fixed block, and the lateral length value of limited block bottom is more than at the top of limited block
Lateral length value.
Preferably, the limited block is arc-shaped close to the one side of idler wheel, and the arc surface of limited block and idler wheel is outer
Circle is adapted.
Preferably, the bottom end of the slide bar is fixedly connected with block, and the side of block and one of limited block far from idler wheel
There are gaps between side.
Preferably, vertically long angle value is five centimetres between the top and the bottom of equipment platform of second bolt, and the
Two bolts are between idler wheel and slide bar.
(3) advantageous effect
Compared with prior art, the present invention provides a kind of zeolite runner Adsorption Concentrations to add catalysis burning waste gas purification dress
It sets, has following advantageous effect：
1, the present invention is by the catalysis combustion box of setting, compared with directly burning, has initiation temperature is low, low energy consumption to show
Work feature, catalysis burning can almost handle all hydro carbons organic exhaust gas and foul gas, and use scope is very wide, processing
Efficient, non-secondary pollution can be effectively by the ash of pulmonary emphysema by the activated carbon filter layer and filtering dust layer of setting
Dirt and particulate matter are effectively filtered, and the purification work subsequently to exhaust gas is facilitated.
2, the present invention can be effective after exhaust gas is concentrated by hydrophobic zeolite runner by the molecular sieve adsorption runner of setting
It is adsorbed in zeolite, achievees the purpose that purify exhaust gas, the exhaust gas after zeolite adsorbs is gone volatile organic in removing exhaust gas
Object, purified exhaust gas is directly by smoke stack emission to air.
3, the present invention facilitates movement of the staff to the device, avoids utilization by the holder and idler wheel of setting
Big machinery carries bothersome laborious situation, passes through the first screwed pipe of setting, the first bolt, fixed block, slide bar, the second screw thread
Pipe, the second bolt, limited block and lantern ring, can be carried out effectively and idler wheel is fixed, and ensure that the device is being moved easily
While can effectively fix, ensure that the stability of the device at work.
Description of the drawings
Fig. 1 is the sectional view of present invention catalysis combustion box front view；
Fig. 2 is the sectional view of primary filter case front view of the present invention；
Fig. 3 is the enlarged structure schematic diagram at A in Fig. 1 of the present invention.
In figure：1 equipment platform, 2 exhaust pipes, 3 molecular sieve adsorption runners, 4 catalysis combustion box, 5 primary filter casees, 6 first
Connecting tube, 7 second connecting tubes, 8 third connecting tubes, 9 conduits, 10 first axial flow blowers, 11 suction hoods, 12 activated carbon filter layers,
13 filtering dust layers, 14 second axial flow blowers, 15 holders, 16 idler wheels, 17 first screwed pipes, 18 first bolts, 19 first bearings
Seat, 20 fixed blocks, 21 slide bars, 22 second screwed pipes, 23 second bolts, 24 second bearing seats, 25 limited blocks, 26 lantern rings, 27 gears
Block.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As shown in Figs. 1-3, the present invention provides a kind of technical solution：A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas
Purifier, including equipment platform 1, the top of equipment platform 1 is fixedly connected sequentially from left to right has exhaust pipe 2, molecular sieve to inhale
Attached runner 3, catalysis combustion box 4 and primary filter case 5, the level height value at 2 top of exhaust pipe be more than molecular sieve adsorption runner 3,
It is catalyzed the top level elevation value of combustion box 4 and primary filter case 5, the gas after evolution can be made effectively to be emitted into high-altitude
In, and pass through respectively successively from left to right between exhaust pipe 2, molecular sieve adsorption runner 3, catalysis combustion box 4 and primary filter case 5
First connecting tube 6, the second connecting tube 7 are connected with third connecting tube 8, and the right side of water filter box 5 is communicated with conduit 9, conduit 9
The first axial flow blower 10 is installed between inner wall, the right end of conduit 9 is communicated with suction hood 11, the interior top of primary filter case 5
It is installed with activated carbon filter layer 12 and filtering dust layer 13, activated carbon filter layer between wall and inner bottom wall successively from left to right
Transverse horizontal length value between 12 and filtering dust layer 13 is five centimetres, ensure that activated carbon filter layer 12 and filtering dust layer
There are certain space between 13, exhaust gas is enable more effectively to filter, being compared by top for third connecting tube is solid between inner bottom wall
Dingan County is equipped with the second axial flow blower 14, and four edges of 1 bottom of equipment platform are installed with holder 15, under holder 15
End is hinged with idler wheel 16 by pin, and the side of holder 15 is inlaid with the first screwed pipe 17, the inner ring screw thread of the first screwed pipe 17
It is connected with the first bolt 18, the opposite one end of two the first bolts 18 runs through the side of holder 15 and passes through first bearing seat 19
It is connected with fixed block 20, the bottom of fixed block 20 is fixedly connected with slide bar 21, and the bottom end of slide bar 21 is fixedly connected with block
27, the sliding of lantern ring 26 can be limited, avoid the case where being detached from slide bar 21 when lantern ring 26 moves down, and the side of block 27
There are gap between the one side of face and limited block 25 far from idler wheel 16, avoid about 25 limited block it is mobile when by block
The top of 27 blocking, fixed block 20 is inlaid with the second screwed pipe 22, and the inner ring of the second screwed pipe 22 is threaded with the second spiral shell
Bolt 23, vertically long angle value is five centimetres between the top and the bottom of equipment platform 1 of the second bolt 23, and the second bolt 23 is located at
Between idler wheel 16 and slide bar 21, and the lower end of the second bolt 23 is connected with through fixed block 20 and by second bearing seat 24
Limited block 25, limited block 25 is located at the lower section of fixed block 20, and the lateral length value of 25 bottom of limited block is pushed up more than limited block 25
The lateral length value in portion ensure that stability when being limited to idler wheel 16, limited block 25 are circular arc close to the one side of idler wheel 16
Shape, and the arc surface of limited block 25 is adapted with the outer ring of idler wheel 16, one side of the limited block 25 far from idler wheel 16 is fixedly connected
There is lantern ring 26, and lantern ring 26 is actively socketed on the outside of slide bar 21.
Further molecular sieve adsorption runner 3 is the corrugated type paper prepared with molecular sieve, activated carbon fiber or carbonaceous material
Board group fills.
Operation principle：When work, suction hood 11 is taken over exhaust gas and is connected, starts the first axial flow blower 10 in the device
With the equal electric elements of the second axial flow blower 14, the exhaust gas in suction hood 11 is directed into just by the first axial flow blower 10 by conduit 9
The inside of grade Rose Box 5, by the effect of activated carbon filter layer 12 and filtering dust layer 13, to the dust particles etc. in exhaust gas
It is filtered, is coordinated by the second axial flow blower 14, molecular sieve adsorption runner 3 is by the second connecting tube 7 by primary filter case 5
Exhaust gas guides to catalysis combustion box 4 and carries out catalysis burning, and oxidation reaction occurs under the action of catalyst for exhaust gas, generates nontoxic
Tasteless carbon dioxide and water removes volatile organic matter in removing exhaust gas, purifies after the concentration of over-molecular sieve adsorption runner 3
Exhaust gas afterwards is directly discharged by exhaust pipe 2 in air, when moving the device, the first bolt 18 is rotated, in the first screwed pipe
17 and first bearing seat 19 under the action of push limited block 25 leave idler wheel 16, the second bolt 23 is rotated further by, in the second screwed pipe
22 and second bearing seat 14 under the action of, drive limited block 25 move up, the device can be moved at this time, it is to be moved extremely finger
When positioning is set, limited block 25 is utilized to fix idler wheel 16 according to the method described above.
The electric elements occurred in this article are electrically connected with extraneous main controller and 220V alternating currents, and main controller can be meter
Calculation machine etc. plays the conventionally known equipment of control.
It should be noted that herein, relational terms such as first and second and the like are used merely to a reality
Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation
In any actual relationship or order or sequence.Moreover, the terms "include", "comprise" or its any other variant are intended to
Non-exclusive inclusion, so that the process, method, article or equipment including a series of elements is not only wanted including those
Element, but also include other elements that are not explicitly listed, or further include for this process, method, article or equipment
Intrinsic element.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of variations, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (7)
1. a kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier, including equipment platform (1), it is characterised in that：
The top of the equipment platform (1) is fixedly connected sequentially from left to right exhaust pipe (2), molecular sieve adsorption runner (3), catalysis combustion
Saggar (4) and primary filter case (5), and exhaust pipe (2), molecular sieve adsorption runner (3), catalysis combustion box (4) and primary filter
It is connected respectively with third connecting tube (8) by the first connecting tube (6), the second connecting tube (7) successively from left to right between case (5)
Logical, the right side of the water filter box (5) is communicated with conduit (9), and first axle stream is installed between the inner wall of the conduit (9)
The right end of wind turbine (10), the conduit (9) is communicated with suction hood (11), the inner roof wall and inner bottom wall of the primary filter case (5)
Between be installed with activated carbon filter layer (12) and filtering dust layer (13), the quilt of the third connecting tube successively from left to right
It is installed with the second axial flow blower (14) between top ratio and inner bottom wall, four edges of equipment platform (1) bottom are equal
It is installed with holder (15), the lower end of the holder (15) is hinged with idler wheel (16), the side of the holder (15) by pin
Face is inlaid with the first screwed pipe (17), and the inner ring of first screwed pipe (17) is threaded with the first bolt (18), two institutes
The opposite one end of the first bolt (18) is stated to run through the side of holder (15) and be connected with by first bearing seat (19) solid
Determine block (20), the bottom of the fixed block (20) is fixedly connected with slide bar (21), and is inlaid at the top of the fixed block (20)
Two screwed pipes (22), the inner ring of second screwed pipe (22) are threaded with the second bolt (23), and the second bolt (23)
Lower end through fixed block (20) and is connected with limited block (25) by second bearing seat (24), and the limited block (25) is separate
The one side of idler wheel (16) is fixedly connected with lantern ring () 26, and lantern ring (26) is actively socketed on the outside of slide bar (21).
2. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：Transverse horizontal length value between the activated carbon filter layer (12) and filtering dust layer (13) is five centimetres.
3. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：Level height value at the top of exhaust pipe (2) is more than molecular sieve adsorption runner (3), catalysis combustion box (4) and primary filter case
(5) top level elevation value.
4. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：Limited block (25) is located at the lower section of fixed block (20), and the lateral length value of limited block (25) bottom is more than limited block (25)
The lateral length value at top.
5. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：The limited block (25) is arc-shaped, and the arc surface of limited block (25) and idler wheel (16) close to the one side of idler wheel (16)
Outer ring be adapted.
6. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：The bottom end of the slide bar (21) is fixedly connected with block (27), and the side of block (27) and the separate idler wheel of limited block (25)
(16) there are gaps between one side.
7. a kind of zeolite runner Adsorption Concentration according to claim 1 adds catalysis burning waste gas purifier, feature to exist
In：Vertically long angle value is five centimetres between the top and the bottom of equipment platform (1) of second bolt (23), and the second bolt
(23) between idler wheel (16) and slide bar (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810643528.9A CN108619820A (en) | 2018-06-21 | 2018-06-21 | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810643528.9A CN108619820A (en) | 2018-06-21 | 2018-06-21 | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108619820A true CN108619820A (en) | 2018-10-09 |
Family
ID=63691843
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810643528.9A Pending CN108619820A (en) | 2018-06-21 | 2018-06-21 | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108619820A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110686259A (en) * | 2019-10-18 | 2020-01-14 | 郭渊明 | Movable thermal oxidizer |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076065A (en) * | 2016-08-22 | 2016-11-09 | 苏州云白环境设备股份有限公司 | Use zeolite runner and the cleaning equipment for waste organic gas of heat-storage type burner |
| CN205853763U (en) * | 2016-05-19 | 2017-01-04 | 拜默实验设备（上海）股份有限公司 | A kind of roller devices of large-scale cabinet |
| CN106422701A (en) * | 2016-10-29 | 2017-02-22 | 王保锋 | Chemical industrial waste gas treatment device |
| CN206327396U (en) * | 2016-12-01 | 2017-07-14 | 郭宝厚 | Multifunctional pathological specimen cart |
| CN107813852A (en) * | 2017-12-06 | 2018-03-20 | 惠州市德度实业发展有限公司 | A kind of special conveying arrangement of small hydraulic project machinery |
| CN207262452U (en) * | 2017-08-16 | 2018-04-20 | 邓金华 | A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner |
| CN208771047U (en) * | 2018-06-21 | 2019-04-23 | 安徽万山红环保科技有限公司 | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purification device |
-
2018
- 2018-06-21 CN CN201810643528.9A patent/CN108619820A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205853763U (en) * | 2016-05-19 | 2017-01-04 | 拜默实验设备（上海）股份有限公司 | A kind of roller devices of large-scale cabinet |
| CN106076065A (en) * | 2016-08-22 | 2016-11-09 | 苏州云白环境设备股份有限公司 | Use zeolite runner and the cleaning equipment for waste organic gas of heat-storage type burner |
| CN106422701A (en) * | 2016-10-29 | 2017-02-22 | 王保锋 | Chemical industrial waste gas treatment device |
| CN206327396U (en) * | 2016-12-01 | 2017-07-14 | 郭宝厚 | Multifunctional pathological specimen cart |
| CN207262452U (en) * | 2017-08-16 | 2018-04-20 | 邓金华 | A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner |
| CN107813852A (en) * | 2017-12-06 | 2018-03-20 | 惠州市德度实业发展有限公司 | A kind of special conveying arrangement of small hydraulic project machinery |
| CN208771047U (en) * | 2018-06-21 | 2019-04-23 | 安徽万山红环保科技有限公司 | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purification device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110686259A (en) * | 2019-10-18 | 2020-01-14 | 郭渊明 | Movable thermal oxidizer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103611418B (en) | Joint treatment device and method for organic waste gas | |
| CN205850524U (en) | Catalytic combustion system after waste gas Adsorption Concentration | |
| CN205055820U (en) | Purification treatment system of msw incineration tail gas | |
| CN207680207U (en) | A kind of high-efficient energy-saving environment friendly organic waste gas treatment system | |
| CN214416003U (en) | Organic waste gas treatment device | |
| CN203861953U (en) | Asphalt flue-gas processing device | |
| CN205461588U (en) | Papermaking waste gas treatment system | |
| CN108261917A (en) | A kind of industry hot waste gas processing unit and treatment process | |
| CN208771047U (en) | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purification device | |
| CN108619820A (en) | A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier | |
| CN212383473U (en) | Desulfurization and denitrification dust removal device | |
| CN203663702U (en) | Joint treatment device for organic waste gas | |
| CN107051083A (en) | A kind of multifunctional industrial emission-control equipment | |
| CN107497237A (en) | A kind of flue gas controller being recycled to | |
| CN101844024A (en) | Flue gas mercury removal device | |
| CN201267741Y (en) | Cooking fumes purifier | |
| CN108744762A (en) | A kind of dedusting-adsorption desorption combination integrated apparatus and its working method | |
| CN211411488U (en) | Organic waste gas treatment device | |
| CN107824030A (en) | A kind of flue gas desulfurization and denitrification cleaning system | |
| CN209791189U (en) | Welding fume purification device | |
| CN209639023U (en) | A kind of domestic garbage pyrolysis cleaning equipment | |
| CN209237611U (en) | A kind of lacquer spraying waste gas processing unit | |
| CN206404559U (en) | A kind of novel coating exhaust treatment system | |
| CN208449051U (en) | Multistage waste gas purification apparatus | |
| CN207769499U (en) | Small-sized movable garbage-incineration smoke purifying activated carbon adsorber |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |