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 PDF

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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
Application number
CN201810643528.9A
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Chinese (zh)
Inventor
周至山
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anhui Wanshanhong Environmental Protection Technology Co Ltd
Original Assignee
Anhui Wanshanhong Environmental Protection Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Anhui Wanshanhong Environmental Protection Technology Co Ltd filed Critical Anhui Wanshanhong Environmental Protection Technology Co Ltd
Priority to CN201810643528.9A priority Critical patent/CN108619820A/en
Publication of CN108619820A publication Critical patent/CN108619820A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters, i.e. particle separators or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/0019Filters, i.e. particle separators or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
    • B01D46/0023Filters, i.e. particle separators 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
    • B01D46/0024Filters, i.e. particle separators 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters, i.e. particle separators or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10Particle separators, e.g. dust precipitators, using filter plates, sheets, or pads having plane surfaces, i.e. axial filtering
    • B01D46/12Particle separators, e.g. dust precipitators, using filter plates, sheets, or pads having plane surfaces, i.e. axial filtering in multiple arrangements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/02Separation 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
    • B01D53/06Separation 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/07Incinerators 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2267/00Multiple filter elements specially adapted for separating dispersed particles from gases or vapours
    • B01D2267/40Different types of filters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2267/00Multiple filter elements specially adapted for separating dispersed particles from gases or vapours
    • B01D2267/70Horizontal 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

A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier
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).
CN201810643528.9A 2018-06-21 2018-06-21 A kind of zeolite runner Adsorption Concentration adds catalysis burning waste gas purifier Pending CN108619820A (en)

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

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CN108619820A true CN108619820A (en) 2018-10-09

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110686259A (en) * 2019-10-18 2020-01-14 郭渊明 Movable thermal oxidizer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110686259A (en) * 2019-10-18 2020-01-14 郭渊明 Movable thermal oxidizer

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