CN207262452U - A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner - Google Patents
A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner Download PDFInfo
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- CN207262452U CN207262452U CN201721022120.7U CN201721022120U CN207262452U CN 207262452 U CN207262452 U CN 207262452U CN 201721022120 U CN201721022120 U CN 201721022120U CN 207262452 U CN207262452 U CN 207262452U
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- Prior art keywords
- exhaust gas
- zeolite runner
- heat storage
- thickening
- monitor
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Abstract
The utility model discloses a kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner, including disposing case, the disposal case upper inside is provided with zeolite runner, and disposal case on both sides of the middle is provided with the first groove, the zeolite runner is internally provided with adsorption zone, and adsorption zone surface is provided with the first venthole, the adsorption zone side is connected with cooling zone, its adsorption zone opposite side is connected with desorption area, and desorption area surface is provided with the second venthole, dehydrating unit is connected among first groove, and dehydrating unit bottom is provided with activated carbon net, the activated carbon sieve bottom is provided with basket strainer, and basket strainer both sides are connected with the second groove, the disposal bottom portion is provided with diaphragm seal, its diaphragm seal bottom side is connected with air intake vent, and it is connected with connecting pipe on the upside of disposal case.The organic exhaust gas zeolite runner thickening-purification technology and heat storage burner, can effectively adsorb moisture in exhaust gas, improve waste gas absorption efficiency, energy conservation and environmental protection, is conducive to promote.
Description
Technical field
Environmental technology field is the utility model is related to, is specially a kind of organic exhaust gas zeolite runner thickening-purification technology and accumulation of heat combustion
Burn device.
Background technology
Often it is difficult to reach improvement requirement using a kind of purification techniques under many circumstances, and it is uneconomical.Utilize different lists
The advantage of first Treatment process, using combined treatment technique, can not only meet emission request, but also can reduce the operation of cleaning equipment
Expense.Therefore, in VOCs treatment, developed rapidly, boiled using the group technology of two or more purification techniques
A kind of new technology that stone runner concentration technique grows up aiming at the improvement of low concentration VOCs, with catalysis burning or high temperature
Burning is combined, and forms zeolite runner Adsorption Concentration+incineration technology, zeolite runner thickening-purification technology device common at present,
The moisture in removing exhaust gas cannot be effectively removed, causes moisture to form absorption competition with pollutant, occupies runner adsorption space and drop
Low stain thing removal efficiency, and leakproofness is bad that runner can be made to there are problems that altering wind in the application.
Utility model content
The purpose of this utility model is to provide a kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner, with
Solve to propose zeolite runner thickening-purification technology device common at present in above-mentioned background technology, it is impossible to the effective water gone in removing exhaust gas
Point, cause moisture to form absorption competition with pollutant, occupy runner adsorption space and reduce contaminant removal efficiency, and seal
Property bad runner can be made to there is the problem of altering wind in the application.
To achieve the above object, the utility model provides following technical solution：A kind of organic exhaust gas zeolite runner concentration is net
Change and heat storage burner, including disposal case, the disposal case upper inside is provided with zeolite runner, and disposes case on both sides of the middle
The first groove is provided with, the zeolite runner is internally provided with adsorption zone, and adsorption zone surface is provided with the first venthole, described
Adsorption zone side is connected with cooling zone, its adsorption zone opposite side is connected with desorption area, and is desorbed area surface and is provided with the second ventilation
Hole, is connected with dehydrating unit among first groove, and dehydrating unit bottom is provided with activated carbon net, the activated carbon net bottom
Portion is provided with basket strainer, and basket strainer both sides are connected with the second groove, and the disposal bottom portion is provided with diaphragm seal, its diaphragm seal
Bottom side is connected with air intake vent, and disposes and connecting pipe is connected with the upside of case, and the first monitor is provided with the right side of the connecting pipe,
And first is provided with the first valve inside monitor, the first monitor bottom is connected with air storage chamber, and is set inside air storage chamber
Switch is equipped with, is connected with heat storage burner on the right side of first monitor, and heat storage burner bottom is connected with the second prison
Instrument is surveyed, second monitor is internally provided with the second valve, its second monitor bottom left is connected with snorkel, and second
Monitor bottom right is connected with air outlet.
Preferably, it is multilayer network structure in the disposal case, and absorbent wool is filled with inside dehydrating unit.
Preferably, the connection mode of first groove and dehydrating unit is is slidably connected, and the second groove and basket strainer
Connection mode also to be slidably connected.
Preferably, the diaphragm seal is distributed with two on disposal case is symmetrical above and below, and it is with connecting pipe, disposal case
Gap is zero.
Preferably, the desorption area is evenly distributed with the first venthole, and the suction to connect with desorption area with cooling zone surface
Second ventilation pore diameter size of attached area surface distribution is sequentially reduced from right to left.
Compared with prior art, the beneficial effects of the utility model are：The organic exhaust gas zeolite runner thickening-purification technology and storage
Hot burner, compared with existing exhaust gas zeolite runner enrichment facility under, be multilayer network structure in disposal case, and remove
Absorbent wool is filled with inside wet device, moisture may form absorption competition with pollutant, occupy runner adsorption space and reduce dirt
Thing removal efficiency is contaminated, contained humidity in exhaust gas is reduced, the adsorption capacity of zeolite runner is improved, so as to remove dirt as much as possible
The connection mode of dye thing, the first groove and dehydrating unit is is slidably connected, and the connection mode of the second groove and basket strainer is also
It is slidably connected so that dehydrating unit can be replaced often with basket strainer, is conducive to cleaning and is safeguarded, and can be to the full extent
Play its effect, diaphragm seal is distributed with two on disposal case is symmetrical above and below, and itself and connecting pipe, the gap of disposing case are
Zero, zeolite runner seals can be improved, leakproofness is bad to make runner there are problems that altering wind, good leakproofness in the application
It is the key that zeolite runner plays a role, desorption area is evenly distributed with the first venthole with cooling zone surface, and with being desorbed area's phase
Second ventilation pore diameter size of the adsorption zone surface distribution connect is sequentially reduced from right to left, the set by adsorption zone surface
Two ventholes cause the region that zeolite wheel surface has just been desorbed, i.e., the exhaust gas that the most strong region of adsorption capacity passes through is most, improve
The exhaust gas adsorption capacity of zeolite runner, is allowed to preferably to play a role.
Brief description of the drawings
Fig. 1 is the utility model positive structure schematic；
Fig. 2 is the utility model zeolite rotaring wheel structure schematic diagram.
In figure：1st, case is disposed, 2, zeolite runner, the 3, first groove, 4, activated carbon net, the 5, second groove, 6, air intake vent, 7,
Basket strainer, 8, dehydrating unit, 9, snorkel, 10, air outlet, the 11, second monitor, the 12, second valve, 13, heat-accumulation combustion dress
Put, 14, air storage chamber, 15, connecting pipe, the 16, first monitor, the 17, first valve, 18, switch, 19, diaphragm seal, 20, desorption
Area, the 21, first venthole, 22, cooling zone, 23, adsorption zone, the 24, second venthole.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained, shall fall within the protection scope of the present invention.
- 2 are please referred to Fig.1, the utility model provides a kind of technical solution：A kind of organic exhaust gas zeolite runner thickening-purification technology and
Heat storage burner, including disposal case 1, disposal 1 upper inside of case are provided with zeolite runner 2, and dispose 1 on both sides of the middle of case and set
There is the first groove 3, the connection mode of the first groove 3 and dehydrating unit 8 is is slidably connected, and the company of the second groove 5 and basket strainer 7
It is also to be slidably connected to connect mode so that dehydrating unit 8 can be replaced often with basket strainer 7, is conducive to cleaning and is safeguarded, and energy
It is enough to play its effect to the full extent, it is multilayer network structure in disposal case 1, and the inside of dehydrating unit 8 is filled with absorbent wool, water
Absorption competition may be formed with pollutant by dividing, and occupied runner adsorption space and reduced contaminant removal efficiency, reduce institute in exhaust gas
Moisture content, reduces moisture in exhaust gas, improves the adsorption capacity of zeolite runner 2, so that pollutant as much as possible is removed,
Zeolite runner 2 is internally provided with adsorption zone 23, and 23 surface of adsorption zone is provided with the first venthole 21, and 23 side of adsorption zone connects
Cooling zone 22 is connected to, its 23 opposite side of adsorption zone is connected with desorption area 20, and is desorbed 20 surface of area and is provided with the second venthole 24,
Desorption area 20 is evenly distributed with the first venthole 21, and 23 surface of adsorption zone point to connect with desorption area 20 with 22 surface of cooling zone
24 diameter of the second venthole of cloth is sequentially reduced from right to left, and the second venthole 24 set by 23 surface of adsorption zone makes
The region that 2 surface of zeolite runner has just been desorbed is obtained, i.e., the exhaust gas that the most strong region of adsorption capacity passes through is most, improves zeolite runner
2 exhaust gas adsorption capacity, is allowed to preferably play a role, and dehydrating unit 8, and 8 bottom of dehydrating unit are connected among the first groove 3
Portion is provided with activated carbon net 4, and 4 bottom of activated carbon net is provided with basket strainer 7, and 7 both sides of basket strainer are connected with the second groove 5, place
Put 1 bottom of case and diaphragm seal 19 is installed, its 19 bottom side of diaphragm seal is connected with air intake vent 6, and disposes the upside of case 1 and be connected with connection
Pipeline 15, diaphragm seal 19 are distributed with two on disposal case 1 is symmetrical above and below, and it is with connecting pipe 15, the gap of disposing case 1 is equal
It is zero, 2 leakproofness of zeolite runner can be improved, leakproofness is bad can makes runner there are problems that altering wind in the application, and good is close
Envelope property is the key that zeolite runner 2 plays a role, and the right side of connecting pipe 15 is provided with the first monitor 16, and the first monitor 16
Inside is provided with the first valve 17, and 16 bottom of the first monitor is connected with air storage chamber 14, and air storage chamber 14 is internally provided with switch
18, the right side of the first monitor 16 is connected with heat storage burner 13, and 13 bottom of heat storage burner is connected with the second monitor
11, the second monitor 11 is internally provided with the second valve 12, its 11 bottom left of the second monitor is connected with snorkel 9, and
Two monitors, 11 bottom right is connected with air outlet 10.
Operation principle：When using the organic exhaust gas zeolite runner thickening-purification technology and heat storage burner, first to the device
Structure simply understood, first, by organic exhaust gas connect air intake vent 6, make exhaust gas from air intake vent 6 enter disposal case 1
, organic exhaust gas removes in removing exhaust gas contained dust by basket strainer 7 first, and then being adsorbed by activated carbon net 4 wherein has
Evil material and gas with foreign flavor, moisture contained in exhaust gas is adsorbed finally by dehydrating unit 8, and then, organic exhaust gas enters
Into zeolite runner 2, exhaust gas is first into the adsorption zone 23 of zeolite runner 2, then passes sequentially through desorption area 23 and cooling
Area 22, carries out organic exhaust gas air concentration, exhaust gas after concentration by connecting pipe 15, at this time by the first monitor 16 come
Whether detection organic exhaust gas supports heat storage burner 13 to burn enough, if enough, gas continues to lead to by connecting pipe 15
Burn toward heat storage burner 13, if being insufficient to, open the first valve 17, by organic exhaust gas then by pipeline again into
Enter into zeolite runner 2 and concentrated, open switch 18 at this time, the auxiliary gas in air storage chamber 14 is led into heat storage burner
Burn in 13, after gas is by burning, via the second monitor 11, whether detection gas quality reaches discharge standard, reach
It can be discharged after, if not up to, organic exhaust gas being drained into disposal case 1 again through snorkel 9, is re-started dense
Contracting, here it is the operation principle of the organic exhaust gas zeolite runner thickening-purification technology and heat storage burner.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from the principle of the utility model and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner, including disposal case (1), it is characterised in that：Institute
State disposal case (1) upper inside and zeolite runner (2) is installed, and dispose case (1) on both sides of the middle and be provided with the first groove (3), institute
State zeolite runner (2) and be internally provided with adsorption zone (23), and adsorption zone (23) surface is provided with the first venthole (21), the suction
Attached area (23) side is connected with cooling zone (22), its adsorption zone (23) opposite side is connected with desorption area (20), and is desorbed area (20)
Surface is provided with the second venthole (24), and dehydrating unit (8), and dehydrating unit (8) bottom are connected among first groove (3)
Portion is provided with activated carbon net (4), and activated carbon net (4) bottom is provided with basket strainer (7), and basket strainer (7) both sides are connected with
Second groove (5), described disposal case (1) bottom are provided with diaphragm seal (19), its diaphragm seal (19) bottom side is connected with air intake vent
(6), connecting pipe (15) and on the upside of disposal case (1) is connected with, the first monitor is installed on the right side of the connecting pipe (15)
(16), the first valve (17) and inside the first monitor (16) is installed, the first monitor (16) bottom is connected with gas storage
Room (14), and air storage chamber (14) is internally provided with switch (18), and heat-accumulation combustion dress is connected with the right side of first monitor (16)
Put (13), and heat storage burner (13) bottom is connected with the second monitor (11), is set inside second monitor (11)
There is the second valve (12), its second monitor (11) bottom left is connected with snorkel (9), and the second monitor (11) bottom, right
Side is connected with air outlet (10).
2. a kind of organic exhaust gas zeolite runner thickening-purification technology according to claim 1 and heat storage burner, its feature exist
In：It is multilayer network structure in the disposal case (1), and absorbent wool is filled with inside dehydrating unit (8).
3. a kind of organic exhaust gas zeolite runner thickening-purification technology according to claim 1 and heat storage burner, its feature exist
In：The connection mode of first groove (3) and dehydrating unit (8) is to be slidably connected, and the second groove (5) and basket strainer (7)
Connection mode also to be slidably connected.
4. a kind of organic exhaust gas zeolite runner thickening-purification technology according to claim 1 and heat storage burner, its feature exist
In：On disposing, case (1) is symmetrical above and below to be distributed with two, and itself and connecting pipe (15), disposal case (1) to the diaphragm seal (19)
Gap be zero.
5. a kind of organic exhaust gas zeolite runner thickening-purification technology according to claim 1 and heat storage burner, its feature exist
In：Desorption area (20) is evenly distributed with the first venthole (21) with cooling zone (22) surface, and connects with desorption area (20)
Adsorption zone (23) surface distribution the second venthole (24) diameter be sequentially reduced from right to left.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721022120.7U CN207262452U (en) | 2017-08-16 | 2017-08-16 | A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721022120.7U CN207262452U (en) | 2017-08-16 | 2017-08-16 | A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207262452U true CN207262452U (en) | 2018-04-20 |
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ID=61925002
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721022120.7U Expired - Fee Related CN207262452U (en) | 2017-08-16 | 2017-08-16 | A kind of organic exhaust gas zeolite runner thickening-purification technology and heat storage burner |
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| CN (1) | CN207262452U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108619847A (en) * | 2018-07-11 | 2018-10-09 | 安徽万山红环保科技有限公司 | A kind of dipping lacquer exhaust gas spray cleaning adds zeolite runner Adsorption Concentration to be catalyzed combustion purification device |
| CN108619820A (en) * | 2018-06-21 | 2018-10-09 | 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 purifier |
| CN108980863A (en) * | 2018-06-13 | 2018-12-11 | 重庆大学 | One kind utilizing method based on the pretreated gas oxidizing fire of desulfurization dewatering |
| CN115845586A (en) * | 2022-11-29 | 2023-03-28 | 江苏绿叶环境工程集团有限公司 | Quick SOx/NOx control equipment of flue gas stream |
-
2017
- 2017-08-16 CN CN201721022120.7U patent/CN207262452U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108980863A (en) * | 2018-06-13 | 2018-12-11 | 重庆大学 | One kind utilizing method based on the pretreated gas oxidizing fire of desulfurization dewatering |
| CN108619820A (en) * | 2018-06-21 | 2018-10-09 | 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 purifier |
| CN108619847A (en) * | 2018-07-11 | 2018-10-09 | 安徽万山红环保科技有限公司 | A kind of dipping lacquer exhaust gas spray cleaning adds zeolite runner Adsorption Concentration to be catalyzed combustion purification device |
| CN115845586A (en) * | 2022-11-29 | 2023-03-28 | 江苏绿叶环境工程集团有限公司 | Quick SOx/NOx control equipment of flue gas stream |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180420 Termination date: 20190816 |
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| CF01 | Termination of patent right due to non-payment of annual fee |