CN206008378U - A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas - Google Patents
A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas Download PDFInfo
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- CN206008378U CN206008378U CN201620974984.8U CN201620974984U CN206008378U CN 206008378 U CN206008378 U CN 206008378U CN 201620974984 U CN201620974984 U CN 201620974984U CN 206008378 U CN206008378 U CN 206008378U
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- activated carbon
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- activity charcoal
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Abstract
This utility model is related to one kind containing dust and organic waste gas treatment equipment, refer in particular to one kind and can pass through the absorption of activated carbon thermopnore containing dust and VOCs treatment combination unit, which includes the functional areas of activated carbon discharging area seven of fresh activity charcoal storage area, fresh activity charcoal charging Jun Pei areas, purified gas relief area, activated carbon areal area, the uniform gas distribution area of eddy flow, waste gas gas-solid rotational flow separation region and adsorption saturation from top to bottom successively；Hou Liuge areas are located in seating nipple, and seating nipple is made up of end socket from top to bottom, cylinder and broach hopper；Seating nipple is on supporting leg.Described activated carbon thermopnore adsorption combined device is serial module structure combinative structure.Gas-solid cyclonic separation, activated carbon granule absorption, fresh activity charcoal charging, adsorption saturation activated carbon discharging reclaimer operation are carried out simultaneously can, be conducive to the labor operations intensity for mitigating operator, simplify operating procedure flow process, organic exhaust gas adsorption continual can be adsorbed.
Description
Technical field
This utility model is related to one kind containing dust and organic waste gas treatment equipment, and refering in particular to one kind can be flowed by activated carbon
Bed absorption is combined the unit containing dust and VOCs treatment.
Background technology
Activated carbon adsorption organic exhaust gas are a kind of most widely used, most practical VOCs treatment technique.The method can use
Organic component in recovery waste gas.
Conventional carbon absorption organic exhaust gas facility is usually single-activity charcoal absorption facility, and most tradition are living
Property charcoal absorption organic exhaust gas, often through the absorption that activated carbon and fixed bed facility carries out organic exhaust gas；Which adsorbs facility often
Secondary property adds activated carbon granule to carry out adsorbing separation, after whole activated carbon granule adsorption saturations failure, is disposably changed
The activated carbon granule of the adsorption saturation, carries out adsorption operations again after replacing.
Conventional carbon granular absorption organic exhaust gas, due to adopting fixed bed facility, during activated carbon granule is changed,
Intermittently operated is needed, operation must periodicity stopping production map function；Stop activated carbon granule adsorption operations, need inspection is opened manually
Repairing manhole carries out the activated carbon granule replacing of adsorption saturation and clears up, and labor cleaning and replacement operation complexity are loaded down with trivial details, labor intensity
Height, changes trouble, and efficiency is low, while also tending to, due to changing not in time, easily cause to adsorb supersaturation, organic exhaust gas can not be complete
Complete adsorbed, and affect adsorption effect.
For reclaiming containing the dust in dust and organic exhaust gas, often generally using setting up at independent gas solid separation recovery
Reason facility is separately separated and recovered pretreatment.
Conventional carbon granular absorption organic exhaust gas facility is set with the dust recovery in the VOCs treatment containing dust
It is often independent split type facility to apply unit, arrangement dispersion, and total floor space is larger, land utilization ratio is not high.
Content of the invention
This utility model is aiming at the problems referred to above, there is provided one kind can pass through activated carbon thermopnore continuous feed, continuous suction
The activated carbon adsorption organic waste gas treatment device of attached, continuous discharge.
In order to solve the above problems, this utility model adopts technical scheme,
Activated carbon thermopnore absorption organic waste gas treatment device includes fresh activity charcoal storage area, fresh from top to bottom successively
Active carbon material feeding Jun Pei area, purified gas relief area, activated carbon areal area, the uniform gas distribution area of eddy flow, waste gas gas-solid rotational flow separation region,
And the functional areas of the activated carbon discharging area of adsorption saturation seven；Fresh activity charcoal charging Jun Pei areas, purified gas relief area, activated carbon
Areal area, the uniform gas distribution area of eddy flow, waste gas gas-solid rotational flow separation region be located at seating nipple in, seating nipple by end socket from top to bottom,
Cylinder and broach hopper composition；Seating nipple is on supporting leg.
It is characterized in that：
Fresh activity charcoal storage area is hopper construction, and it is in fall that main body stores cylinder and bottom by the fresh activity charcoal on top
The fresh activity charcoal storage hopper composition of cone, the top of fresh activity charcoal storage cylinder is cover plate for sealing；Fresh activity charcoal is store
Storaging bucket bottom is sequentially provided with rotary table feeder, active carbon material feeding valve from top to bottom.
It is equal that fresh activity charcoal charging Jun Pei areas are provided with the equal orchestration one, active carbon material feeding of active carbon material feeding mouth, active carbon material feeding
Orchestration two；The active carbon material feeding valve of fresh activity charcoal storage area is connected with active carbon material feeding mouth.
Purified gas relief area side is provided with purification air vent, and opposite side arranges overhaul of the equipments manhole one.
Activated carbon areal area is mainly activated carbon granule layer.
The uniform gas distribution area of eddy flow is provided with the uniform gas distribution perforated plate of activated carbon.
Waste gas gas-solid rotational flow separation region side is provided with air inlet, and opposite side is provided with inspection manhole two；Top is provided with eddy flow point
From deflector；Bottom is provided with broach hopper；Broach hopper bottom is provided with ash discharging hole, ash-valve and rotating blanking apptss.
The activated carbon discharging area of adsorption saturation is provided with the equal orchestration one of activated carbon blanking, the equal orchestration two of activated carbon blanking, activity
Charcoal discharge nozzle, activated carbon outlet valve and rotating blanking apptss.
The fresh activity charcoal granule of fresh activity charcoal storage area stores the rotary feeding of feed hopper bottom by fresh activity charcoal
The active carbon material feeding mouth in device, inlet valve and fresh activity charcoal charging Jun Pei areas is put into fresh activity charcoal charging Jun Pei areas；Activated carbon
Granule is fallen along active carbon material feeding mouth using self gravitation effect, and first passing around the equal orchestration one of active carbon material feeding is carried out uniformly
After cloth, then uniform distribution is carried out through the equal orchestration two of active carbon material feeding, to guarantee the activated carbon entered in activated carbon areal area
Even particle distribution.
Organic exhaust gas enter waste gas gas-solid rotational flow separation region along cylinder body outer wall horizontal tangential, along cylinder by air inlet
Body, bottom cone and cyclonic separation deflector make downwards tangential swirl motion, carry out gas-solid cyclonic separation, and gas enters eddy flow
Uniform gas distribution area, solid dust enter broach hopper cone base, periodically by ash discharging hole, ash-valve and rotating blanking apptss row
Go out, and carry out solid dust granule recovery.
Waste gas after gas solid separation by the uniform gas distribution perforated plate of the activated carbon in the uniform gas distribution area of eddy flow, from bottom to top
Enter activated carbon adsorption layer.Purified gas after being adsorbed by activated carbon granule rise to purified gas relief area, arrange from air vent is purified
Go out.
In activated carbon adsorption layer, organic exhaust gas from bottom to top carry out counter current contacting absorption with activated carbon granule layer successively,
Lower floor's activated carbon granule is first adsorbed saturation, and then the activated carbon granule on upper strata is gradually from bottom to top adsorbed saturation.Whole living
Property charcoal granular layer absorption organic exhaust gas saturation situation from bottom to top gradually increase successively, until saturation.
When the activated carbon granule of bottom adsorption saturation passes through activated carbon discharge nozzle, activated carbon baiting valve and rotating blanking apptss
Blanking is carried out, dispatch goes out.
When the activated carbon granule of bottom adsorption saturation carries out the operation that dispatch goes out activated carbon thermopnore adsorption combined device
Cheng Zhong, the unadsorbed saturated activity charcoal granule on activated carbon granule layer top are uniformly flowed downward by action of gravity, by activity
The equal orchestration one of charcoal blanking and the equal orchestration two of activated carbon blanking carry out activated carbon granule again with distribution, supplement and replace bottom row
The saturated activity charcoal granule for going out；Simultaneously the fresh activity charcoal granule of fresh activity charcoal storage area by the rotary table feeder of bottom,
The equal orchestration two of the equal orchestration one, active carbon material feeding of active carbon material feeding valve, active carbon material feeding mouth, active carbon material feeding carries out fresh activity charcoal
Supplement.
Activated carbon granule is to the absorption of organic exhaust gas and the feed flow of fresh activity charcoal granule and adsorption saturation activity
The blowing of charcoal granule can be carried out simultaneously, so as to realize the continuous uninterrupted adsorption operations of VOCs treatment.
Described dust-laden exhaust gas air inlet is entered along cylinder body outer wall horizontal tangential in waste gas gas-solid rotational flow separation region side
Waste gas gas-solid rotational flow separation region.
Described waste gas gas-solid rotational flow separation region arranges cyclonic separation deflector, and the upper cone angle of its deflector is arranged
60°；Described deflector bottom be bending-type tube structure, bottom level phase suitable for reading with the broach hopper of gas-solid rotational flow separation region
Flat.
The cone angle of the broach hopper of described gas-solid rotational flow separation region arranges 75 °.
Described activated carbon uniformly bores a hole air distribution plate for conical structure, and activated carbon is uniformly bored a hole air distribution plate inner cone angle
Arrange 60 °.Activated carbon air distribution plate of uniformly boring a hole is provided with uniform qi-emitting hole, apertureAdjacent interporal lacuna is 5mm.
The equal orchestration one, two of described active carbon material feeding and the equal orchestration one, two of activated carbon blanking are upper and lower cone knot
Structure is connected and composed, and cone angle arranges 90 °；The equal orchestration one, two of active carbon material feeding and the equal orchestration one, two of activated carbon blanking pass through
Connector connection, the equal orchestration one, two of active carbon material feeding is supported to be fixed on end socket by supporting connector, activated carbon blanking is matched somebody with somebody
Device one is fixed on cylinder by supporting connector, and the equal orchestration two of activated carbon blanking is equal by supporting connector to be fixed on activated carbon
On even perforation air distribution plate.
Described adsorption saturation activated carbon granule discharge method is middle bottom discharge；Activated carbon thermopnore adsorption combined device
Activated carbon discharge nozzle of the adsorption saturation activated carbon granule of bottom along bottom of device, by activated carbon outlet valve and rotation under
Glassware carries out uniform discharge.
Compared with containing the VOCs treatment facility of dust with conventional treatment：
Activated carbon thermopnore adsorption combined device of the present invention is serial module structure combinative structure.Can carry out simultaneously
Gas-solid cyclonic separation, activated carbon granule absorption, the charging of fresh activity charcoal, adsorption saturation activated carbon discharging reclaimer operation, are conducive to
Mitigate the labor operations intensity of operator, simplify operating procedure flow process, organic exhaust gas adsorption continual can be adsorbed, no
Production operation is affected, and adsorption treatment efficiency high is reclaimed to organic exhaust gas adsorption up to more than 99%；This combination unit is from version
On by gas-solid cyclonic separation, activated carbon granule absorption, fresh activity charcoal particulate charge, adsorption saturation activated carbon granule discharging reclaim
Operation effectively combines, simple and compact for structure, can save floor space more than 50%, and cost of effectively reducing investment outlay, for entering
One step subsequent treatment process creates good condition.
Description of the drawings
Fig. 1 is activated carbon adsorption thermopnore combination unit top view.
Fig. 2 is the A-A elevation of Fig. 1.
Fig. 3 is the B-B elevation of Fig. 1.
Wherein：1st, cover plate；2nd, fresh activity charcoal storage cylinder；3rd, rotary table feeder；4th, active carbon material feeding valve；5th, activated carbon
Charging aperture；6-1, support connector one；6-2, support connector two；The equal orchestration one of 7-1, active carbon material feeding；7-2, activated carbon enter
Expect equal orchestration two；8th, end socket；9th, air vent is purified；10th, cylinder；11st, connector is supported；12nd, the equal orchestration one of activated carbon blanking；
13rd, activated carbon is uniformly bored a hole air distribution plate；14th, inspection manhole two；15th, cyclonic separation deflector；16th, ash discharging hole；17th, ash-valve；
18th, rotating blanking apptss；19th, activated carbon outlet valve；20th, rotating blanking apptss；21st, supporting leg；22nd, activated carbon discharge nozzle；23rd, conical material
Bucket；24th, connector is supported；25th, air inlet；26th, the equal orchestration two of activated carbon blanking；27th, inspection manhole one；28th, fresh activity charcoal
Storage hopper；29th, the activated carbon discharging area of adsorption saturation；30th, waste gas gas-solid rotational flow separation region；31st, the uniform gas distribution area of eddy flow；
32nd, activated carbon areal area；33rd, purified gas relief area；34th, fresh activity charcoal charging Jun Pei areas；35th, fresh activity charcoal storage area.
Specific embodiment
As shown in Figures 1 to 3, one kind is provided containing dust and organic exhaust gas active-carbon for the technical solution of the utility model
Thermopnore adsorption combined schematic device.
Certain enterprise's production waste gas contains a small amount of dust granules and benzene organic exhaust gas, if the waste gas is unprocessed to affect week
Surrounding environment, need to carry out the pretreatment of waste gas gas solid separation to this waste gas and activated carbon adsorption benzene organic waste-gas purification is processed.
Described device include fresh activity charcoal storage area 35, fresh activity charcoal charging Jun Pei areas 34, activated carbon areal area 32,
The activated carbon blanking of the uniform gas distribution area 31 of waste gas gas-solid rotational flow separation region 30, eddy flow, purified gas relief area 33 and adsorption saturation
29 7, area unit ingredient, version are serial module structure unit equipment.
Fresh activity charcoal storage area 35 is provided with fresh activity charcoal storage cylinder 2 and fresh activity charcoal storage hopper 28, top
Portion is sealed for cover plate 1.Bottom is provided with rotary table feeder 3, active carbon material feeding valve 4.
Fresh activity charcoal charging Jun Pei areas are provided with equal one 7-1 of orchestration of active carbon material feeding mouth 5, active carbon material feeding, activated carbon and enter
Expect two 7-2 of equal orchestration.
Activated carbon areal area 32 is mainly activated carbon granule layer.
Waste gas gas-solid rotational flow separation region 30 is provided with air inlet 25, cyclonic separation deflector 15.Bottom be provided with broach hopper 23,
Ash discharging hole 16, ash-valve 17 and rotating blanking apptss 18.
The uniform gas distribution area 31 of eddy flow is provided with the uniform gas distribution perforated plate 13 of activated carbon.
33 top of purified gas relief area is provided with purification air vent 9.Middle part arranges overhaul of the equipments manhole 1.
The activated carbon discharging area 29 of adsorption saturation is provided with the equal orchestration 1 of activated carbon blanking, the equal orchestration two of activated carbon blanking
26th, activated carbon discharge nozzle 22, activated carbon outlet valve 19, rotating blanking apptss 20.
The fresh activity charcoal granule of fresh activity charcoal storage area 35 is put into newly by the rotary table feeder 3 of bottom, inlet valve 4
Fresh active carbon material feeding Jun Pei area 34；Activated carbon granule is fallen using self gravitation effect, is passed through first along active carbon material feeding mouth 5
Cross after equal one 7-1 of orchestration of active carbon material feeding carries out uniform distribution, then uniform cloth is carried out through equal two 7-2 of orchestration of active carbon material feeding
Material, to guarantee that the activated carbon granule in activated carbon areal area is evenly distributed.
Containing a small amount of dust granules and benzene organic exhaust gas, entered along cylinder body outer wall horizontal tangential direction by air inlet 25
Enter air inlet gas-solid rotational flow separation region 30, along cylinder 10, bottom pyramidal hopper 23 and cyclonic separation deflector 15 is downward cuts
To swirling motion, gas-solid cyclonic separation is carried out, gas enters uniform gas distribution area 31, and solid dust enters 23 bottom of broach hopper,
Periodically discharged by ash discharging hole 16, ash-valve 17 and rotating blanking apptss 18, and carry out solid dust granule recovery.
Waste gas containing benzene after gas solid separation is uniformly bored a hole air distribution plate 13 by the activated carbon in the uniform gas distribution area 31 of eddy flow,
The activated carbon adsorption layer of activated carbon areal area 32 is from bottom to top entered.Purified gas after being adsorbed by activated carbon granule rise to purification
Gas relief area 33, finally discharges from purification air vent 9.
In the activated carbon adsorption layer of activated carbon areal area 32, organic exhaust gas are from bottom to top entered with activated carbon granule layer successively
Row counter current contacting adsorb, lower floor's activated carbon granule first be adsorbed saturation, then the activated carbon granule on upper strata gradually from bottom to top by
Adsorption saturation.Whole activated carbon granule layer absorption organic exhaust gas saturation situation from bottom to top gradually increases successively, until saturation.
When the activated carbon granule of bottom adsorption saturation is by bottom activated carbon discharge nozzle 22, activated carbon outlet valve 19 and rotation
Turning blanking device 20 carries out blanking, and dispatch goes out.
Go out activated carbon thermopnore adsorption combined device operating process when the activated carbon granule of bottom adsorption saturation carries out dispatch
In, the unadsorbed saturated activity charcoal granule on activated carbon granule layer top is uniformly flowed downward by action of gravity, by activated carbon
The equal orchestration 1 of blanking and the equal orchestration 2 26 of activated carbon blanking carry out activated carbon granule again with distribution, supplement and replace bottom
The saturated activity charcoal granule of discharge；While rotary feeding of the fresh activity charcoal granule of fresh activity charcoal storage area 34 by bottom
Equal one 7-1 of orchestration of device 3, active carbon material feeding valve 4, active carbon material feeding mouth 5, active carbon material feeding, equal two 7-2 of orchestration of active carbon material feeding enter
Row fresh activity charcoal granule is supplemented.
Activated carbon granule is to containing a small amount of dust granules and the absorption of benzene organic exhaust gas and entering for fresh activity charcoal granule
Stream is moved and the blowing of adsorption saturation activated carbon granule can be carried out simultaneously.So as to realize containing a small amount of dust granules and benzene
The continuous uninterrupted adsorption operations of VOCs treatment.
Compared with containing the VOCs treatment facility of dust with conventional treatment：
This activated carbon thermopnore adsorption combined device containing a small amount of dust granules and benzene organic exhaust gas is serial module structure
Change combinative structure.Gas-solid cyclonic separation, activated carbon granule absorption, fresh activity charcoal charging, adsorption saturation work are carried out simultaneously can
Property charcoal discharging reclaimer operation, be conducive to the labor operations intensity for mitigating operator, simplify operating procedure flow process, to organic exhaust gas
Absorption continual can adsorb, do not affect production operation, to organic exhaust gas adsorption containing benzene recycle efficiency high up to 99% with
On；Containing a small amount of dust granules waste gas gas solid separation dust organic efficiency up to more than 90%.This combination unit is from version
On by gas-solid cyclonic separation, activated carbon granule absorption, fresh activity charcoal particulate charge, adsorption saturation activated carbon granule discharging reclaim
Operation effectively combines, simple and compact for structure, can save floor space more than 50%, and cost of effectively reducing investment outlay, for entering
One step subsequent treatment process creates good condition.
Claims (6)
1. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas, it is characterised in that：Described device from
Include fresh activity charcoal storage area, fresh activity charcoal charging Jun Pei areas, purified gas relief area, activated carbon distribution under up to successively
The functional areas of activated carbon discharging area seven of area, the uniform gas distribution area of eddy flow, waste gas gas-solid rotational flow separation region and adsorption saturation；Newly
Fresh active carbon material feeding Jun Pei area, purified gas relief area, activated carbon areal area, the uniform gas distribution area of eddy flow, waste gas gas-solid cyclonic separation
Area is located in seating nipple, and seating nipple is made up of end socket from top to bottom, cylinder and broach hopper；Seating nipple is on supporting leg；
Fresh activity charcoal storage area is hopper construction, and it is in reverse taper that main body stores cylinder and bottom by the fresh activity charcoal on top
Fresh activity charcoal storage hopper composition, fresh activity charcoal storage cylinder top be cover plate for sealing；Fresh activity charcoal storage material
Bucket bottom is sequentially provided with rotary table feeder, active carbon material feeding valve from top to bottom；
Fresh activity charcoal charging Jun Pei areas are provided with the equal orchestration of the equal orchestration one, active carbon material feeding of active carbon material feeding mouth, active carbon material feeding
Two；The active carbon material feeding valve of fresh activity charcoal storage area is connected with active carbon material feeding mouth；
Purified gas relief area side is provided with purification air vent, and opposite side arranges overhaul of the equipments manhole one；
Activated carbon areal area is mainly activated carbon granule layer；
The uniform gas distribution area of eddy flow is provided with the uniform gas distribution perforated plate of activated carbon；
Waste gas gas-solid rotational flow separation region side is provided with air inlet, and opposite side is provided with inspection manhole two；Top is provided with cyclonic separation and leads
Stream plate；Bottom is provided with broach hopper；Broach hopper bottom is provided with ash discharging hole, ash-valve and rotating blanking apptss；
The activated carbon discharging area of adsorption saturation is provided with the equal orchestration one of activated carbon blanking, the equal orchestration two, activated carbon of activated carbon blanking and goes out
Expects pipe, activated carbon outlet valve and rotating blanking apptss；
The fresh activity charcoal granule of fresh activity charcoal storage area is stored the rotary table feeder of feed hopper bottom, is entered by fresh activity charcoal
The active carbon material feeding mouth in material valve and fresh activity charcoal charging Jun Pei areas is put into fresh activity charcoal charging Jun Pei areas；Activated carbon granule edge
Active carbon material feeding mouth, is fallen using self gravitation effect, first passed around after the equal orchestration one of active carbon material feeding carries out uniform distribution,
Uniform distribution is carried out again through active carbon material feeding equal orchestration two, to guarantee the activated carbon granule entered in activated carbon areal area distribution
Uniformly；
Organic exhaust gas enter waste gas gas-solid rotational flow separation region along cylinder body outer wall horizontal tangential, along cylinder, bottom by air inlet
Portion's cone and cyclonic separation deflector make downwards tangential swirl motion, carry out gas-solid cyclonic separation, and it is uniform that gas enters eddy flow
Gas distribution area, solid dust enter broach hopper cone base, are periodically discharged by ash discharging hole, ash-valve and rotating blanking apptss,
And carry out solid dust granule recovery；
Waste gas after gas solid separation is from bottom to top entered by the uniform gas distribution perforated plate of the activated carbon in the uniform gas distribution area of eddy flow
Activated carbon adsorption layer；Purified gas after being adsorbed by activated carbon granule rise to purified gas relief area, discharge from air vent is purified；
In activated carbon adsorption layer, organic exhaust gas from bottom to top carry out counter current contacting absorption, lower floor with activated carbon granule layer successively
Activated carbon granule is first adsorbed saturation, and then the activated carbon granule on upper strata is gradually from bottom to top adsorbed saturation, whole activated carbon
Granular layer absorption organic exhaust gas saturation situation from bottom to top gradually increases successively, until saturation；
When the activated carbon granule of bottom adsorption saturation is carried out by activated carbon discharge nozzle, activated carbon baiting valve and rotating blanking apptss
Blanking, dispatch go out；
When the activated carbon granule of bottom adsorption saturation is carried out in the operating process that dispatch goes out activated carbon thermopnore adsorption combined device,
The unadsorbed saturated activity charcoal granule on activated carbon granule layer top is uniformly flowed downward by action of gravity, by activated carbon blanking
Orchestration one and the equal orchestration two of activated carbon blanking carry out activated carbon granule again with distribution, and it is full that supplementary replacement bottom is discharged
And activated carbon granule；The fresh activity charcoal granule of fresh activity charcoal storage area is by the rotary table feeder of bottom, activated carbon simultaneously
The equal orchestration two of the equal orchestration one, active carbon material feeding of inlet valve, active carbon material feeding mouth, active carbon material feeding carries out fresh activity charcoal supplement.
2. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas as claimed in claim 1, which is special
Levy and be：Activated carbon granule is to the absorption of organic exhaust gas and the feed flow of fresh activity charcoal granule and adsorption saturation activated carbon
The blowing of granule is carried out simultaneously, so as to realize the continuous uninterrupted adsorption operations of VOCs treatment.
3. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas as claimed in claim 1, which is special
Levy and be：Described waste gas gas-solid rotational flow separation region arranges cyclonic separation deflector, and the upper cone angle of its deflector is arranged
60°；Described deflector bottom be bending-type tube structure, bottom level phase suitable for reading with the broach hopper of gas-solid rotational flow separation region
Flat.
4. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas as claimed in claim 1, which is special
Levy and be：The cone angle of the broach hopper of described gas-solid rotational flow separation region arranges 75 °.
5. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas as claimed in claim 1, which is special
Levy and be：Described activated carbon uniformly bores a hole air distribution plate for conical structure, and activated carbon is uniformly bored a hole air distribution plate inner cone angle
60 ° are arranged, activated carbon air distribution plate of uniformly boring a hole is provided with uniform qi-emitting hole, apertureAdjacent interporal lacuna is 5mm.
6. a kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas as claimed in claim 1, which is special
Levy and be：The equal orchestration one, two of described active carbon material feeding and the equal orchestration one, two of activated carbon blanking are upper and lower conical structure
Connect and compose, cone angle arranges 90 °；The equal orchestration one, two of active carbon material feeding and the equal orchestration one, two of activated carbon blanking pass through
Connector connection, the equal orchestration one, two of active carbon material feeding is supported to be fixed on end socket by supporting connector, activated carbon blanking is matched somebody with somebody
Device one is fixed on cylinder by supporting connector, and the equal orchestration two of activated carbon blanking is equal by supporting connector to be fixed on activated carbon
On even perforation air distribution plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620974984.8U CN206008378U (en) | 2016-08-29 | 2016-08-29 | A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620974984.8U CN206008378U (en) | 2016-08-29 | 2016-08-29 | A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206008378U true CN206008378U (en) | 2017-03-15 |
Family
ID=58253768
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620974984.8U Withdrawn - After Issue CN206008378U (en) | 2016-08-29 | 2016-08-29 | A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
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| Country | Link |
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| CN (1) | CN206008378U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106166431A (en) * | 2016-08-29 | 2016-11-30 | 江苏江大环境工程有限责任公司 | A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
| CN108421367A (en) * | 2018-03-23 | 2018-08-21 | 深圳市贝优通新能源技术开发有限公司 | A kind of intelligent formaldehyde collection processing equipment based on Internet of Things |
-
2016
- 2016-08-29 CN CN201620974984.8U patent/CN206008378U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106166431A (en) * | 2016-08-29 | 2016-11-30 | 江苏江大环境工程有限责任公司 | A kind of activated carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
| CN106166431B (en) * | 2016-08-29 | 2019-04-12 | 江苏江大环境工程有限责任公司 | A kind of active carbon thermopnore adsorption combined device containing dust and organic exhaust gas |
| CN108421367A (en) * | 2018-03-23 | 2018-08-21 | 深圳市贝优通新能源技术开发有限公司 | A kind of intelligent formaldehyde collection processing equipment based on Internet of Things |
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