CN203916445U - Waste gas tower purifier - Google Patents
Waste gas tower purifier Download PDFInfo
- Publication number
- CN203916445U CN203916445U CN201420315837.0U CN201420315837U CN203916445U CN 203916445 U CN203916445 U CN 203916445U CN 201420315837 U CN201420315837 U CN 201420315837U CN 203916445 U CN203916445 U CN 203916445U
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- CN
- China
- Prior art keywords
- gas
- waste gas
- tower
- secondary oxidation
- zoneofoxidation
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- Expired - Fee Related
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Abstract
The utility model relates to waste gas tower purifier.The device that object is to provide should fundamentally be removed foul gas, and has simple in structure, manufacture and the lower feature of operating cost.Technical scheme is: waste gas tower purifier, comprises off-gas oxidizing tower, waste gas pipeline and ClO 2 solution groove; The division board that described off-gas oxidizing tower arranges by inner chamber middle part is divided into the zoneofoxidation on top and the resolver of bottom; The atomizer that is communicated with carrier pipe is equipped with at the top of zoneofoxidation, configures some left and right and interlock and horizontally disposed buffering dividing plate in zoneofoxidation; On division board, be fixed with secondary oxidation groove, the return duct that is communicated with ClO 2 solution groove is equipped with in the bottom of resolver, is also furnished with for gas after purifying being caused to the receiving tube of off-gas oxidizing tower outside in resolver; In the inner chamber of described secondary oxidation groove, left and right is being staggered installation of some dividing plates, and a plurality of apertures that the inner chamber of secondary oxidation groove is made by wall portion communicate with zoneofoxidation; Secondary oxidation trench bottom communicates with resolver.
Description
Technical field
The utility model relates to a kind of environmental protecting device, is specifically related to a kind of waste gas purification apparatus.
Background technology
In life or industrial activity, foul gas has a strong impact on the healthy of people and sense of smell sense organ.The material of foul gas is mainly following five classes: sulfur-containing compound, nitrogen-containing compound, halogen and derivative, hydro carbons and aromatic hydrocarbon.Main deodorizing method is masking method at present, cannot fundamentally remove malodor source.
Utility model content
The utility model object is to provide a kind of deodorizing purifier efficiently can be recycled, and this device should fundamentally be removed foul gas, and has simple in structure, manufacture and the lower feature of operating cost.
The technical solution adopted in the utility model is: waste gas tower purifier, comprise off-gas oxidizing tower that erect to arrange, toward the waste gas pipeline of conveying waste gas in off-gas oxidizing tower and by the carrier pipe with noncorrosive pump toward the ClO 2 solution groove of carrying chlorine dioxide in off-gas oxidizing tower; It is characterized in that: the division board that described off-gas oxidizing tower arranges by inner chamber middle part is divided into the zoneofoxidation on top and the resolver of bottom; The atomizer that is communicated with carrier pipe is equipped with at the top of zoneofoxidation, configures some left and right and interlock and horizontally disposed buffering dividing plate in zoneofoxidation; On division board, be fixed with secondary oxidation groove, the return duct that is communicated with ClO 2 solution groove is equipped with in the bottom of resolver, is also furnished with for gas after purifying being caused to the receiving tube of off-gas oxidizing tower outside in resolver; In the inner chamber of described secondary oxidation groove, left and right is being staggered installation of some dividing plates, and a plurality of apertures that the inner chamber of secondary oxidation groove is made by wall portion communicate with zoneofoxidation; Secondary oxidation trench bottom communicates with resolver.
Described receiving tube is communicated with the delivery pipe with air-introduced machine through the wall portion of off-gas oxidizing tower.
The entrance point of described waste gas pipeline is communicated with gas sampling cover.
Described secondary oxidation groove is the cylindrical structural concentric with off-gas oxidizing tower, and its bottom is higher than the top height of ClO 2 solution groove.
Described some buffering dividing plates are the major arc structure isometrical with off-gas oxidizing tower, and the breach that cushions between two dividing plate is spaced apart towards equal left and right.
Described some dividing plates are the major arc structure isometrical with secondary oxidation groove, and the breach that cushions between two dividing plate is spaced apart towards equal left and right.
Described some buffering dividing plate in the vertical direction equidistant placement.
Described some dividing plate in the vertical direction equidistant placement.
The beneficial effects of the utility model are: owing to having adopted strong oxidizer chlorine dioxide, be deodorant, can foul smell be oxidized to tasteless chemical substance with foul smell generation chemical reaction, fundamentally remove stink.And residue chlorine dioxide can be recycled, non-environmental-pollution beyond the region of objective existence row, operating cost is also lower.In addition, this apparatus structure advantages of simple, cost of manufacture is not high yet, is applicable to all kinds of enterprise configuration and uses.
Accompanying drawing explanation
Fig. 1 is main TV structure schematic diagram of the present utility model.
The specific embodiment
In waste gas tower purifier shown in the drawings, off-gas oxidizing tower 1 (pref. cylindrical) is erect and is arranged, toward carrying waste gas in off-gas oxidizing tower, (entrance point of waste gas pipeline is communicated with gas sampling cover 2 in the wall portion that waste gas pipeline 3 passes through off-gas oxidizing tower, with the waste gas of extract to need processing), in off-gas oxidizing tower, carry after extracting ClO 2 solution with the carrier pipe 13 of noncorrosive pump 8 from ClO 2 solution groove 9; Above structure and existing emission-control equipment are roughly the same.
Improvement of the present utility model is: the division board 20 arranging by inner chamber middle part is divided into the zoneofoxidation 21 on top and the resolver 22 of bottom by the inner chamber of off-gas oxidizing tower.The atomizer 14 (specification of atomizer and quantity are determined as required) that is communicated with carrier pipe is equipped with at the top of zoneofoxidation; In zoneofoxidation, configuring some left and right interlocks and horizontally disposed buffering dividing plate 4; These buffering dividing plates are the major arc structure isometrical with off-gas oxidizing tower, cushion between two the breach (breach that is lastblock buffering dividing plate is turned left, and the breach of next block buffering dividing plate is turned right) spaced apart towards equal left and right of dividing plate.As preferably, described some buffering dividing plate in the vertical direction equidistant placement (also can non-equidistant setting).
The bottom of resolver is equipped with and is communicated with the return duct 15 of ClO 2 solution groove (return duct, ClO 2 solution groove, noncorrosive pump, carrier pipe connect successively, formed the chlorine dioxide circulatory system), in resolver, be also furnished with for Purge gas being caused to the receiving tube 16 of off-gas oxidizing tower outside, described receiving tube is communicated with (receiving tube, air-introduced machine and delivery pipe have formed air venting system) through the wall portion of off-gas oxidizing tower with the delivery pipe 7 with air-introduced machine 6.
On division board, be fixed with secondary oxidation groove 5, this secondary oxidation groove is for being designed to cylindrical structural (as preferably, with off-gas oxidizing tower arranged concentric); A plurality of aperture 5-3 (aperture of aperture is chosen as 2-4mm conventionally) that the inner chamber of this secondary oxidation groove is made by wall portion communicate with zoneofoxidation; Secondary oxidation trench bottom is shaped with opening 5-2 and communicates with resolver.In the inner chamber of secondary oxidation groove, left and right is being staggered installation of some dividing plate 5-1, and these dividing plates are the major arc structure isometrical with secondary oxidation groove, and the breach that cushions between two dividing plate distributes towards equal left and right; As preferably, described some dividing plate in the vertical directions equidistant and horizontally disposed (also can non-equidistant setting).
As recommendation, described secondary oxidation bottom land end is higher than the top height of ClO 2 solution groove; To be conducive to the backflow of ClO 2 solution.
Operation principle of the present utility model is:
Solid chlorine dioxide is mixed with and from chlorine dioxide, adds entrance 11 after solution and join the interior storage of ClO 2 solution groove 9, can pass through the liquid level of level indicator 10 observable ClO 2 solutions.Start noncorrosive pump 8, the ClO 2 solution carrier pipe 13 of flowing through is dispensed to atomizer 14, and atomizer 14 is dispersed into fine drop by chlorine dioxide, increases the specific area contacting with air.Drop from top to bottom one-level one-level flow through buffering dividing plate 4 after bottom division board, by the aperture 5-3 on secondary oxidation groove 5, entered in secondary oxidation groove, after baffle plate diversion, from bottom, flow to off-gas oxidizing tower bottom.
Foul smell is collected by gas sampling cover 2 is unified, through waste gas pipeline 3, from off-gas oxidizing top of tower, imports.Foul smell fully contacts in tower with chlorine dioxide drop, after odorous substance and chlorine dioxide generation oxidation reaction, becomes odorless, tasteless material and enters Purge gas receiving tube 16, through 6 guiding of fiberglass air-introduced machine, from delivery pipe 7, discharges.
Claims (8)
1. waste gas tower purifier, comprises and erects the waste gas pipeline (3) of the off-gas oxidizing tower (1) of arranging, the interior conveying of past off-gas oxidizing tower waste gas and the ClO 2 solution groove (9) toward the interior conveying of off-gas oxidizing tower chlorine dioxide by the carrier pipe (13) with noncorrosive pump (8); It is characterized in that: the division board (20) that described off-gas oxidizing tower arranges by inner chamber middle part is divided into the zoneofoxidation (21) on top and the resolver (22) of bottom; The atomizer (14) that is communicated with carrier pipe is equipped with at the top of zoneofoxidation, configures some left and right and interlock and horizontally disposed buffering dividing plate (4) in zoneofoxidation; On division board, be fixed with secondary oxidation groove (5), the return duct (15) that is communicated with ClO 2 solution groove is equipped with in the bottom of resolver, is also furnished with for Purge gas being caused to the receiving tube (16) of off-gas oxidizing tower outside in resolver; In the inner chamber of described secondary oxidation groove, left and right is being staggered installation of some dividing plates (5-1), and a plurality of apertures (5-3) that the inner chamber of secondary oxidation groove is made by wall portion communicate with zoneofoxidation; Secondary oxidation trench bottom communicates with resolver.
2. waste gas tower purifier according to claim 1, is characterized in that: described receiving tube is communicated with the delivery pipe with air-introduced machine through the wall portion of off-gas oxidizing tower.
3. waste gas tower purifier according to claim 2, is characterized in that: the entrance point of described waste gas pipeline is communicated with gas sampling cover (2).
4. waste gas tower purifier according to claim 3, is characterized in that: described secondary oxidation groove is the cylindrical structural concentric with off-gas oxidizing tower, and its bottom is higher than the top height of ClO 2 solution groove.
5. waste gas tower purifier according to claim 4, is characterized in that: described some buffering dividing plates are the major arc structure isometrical with off-gas oxidizing tower, and the breach that cushions between two dividing plate is spaced apart towards equal left and right.
6. waste gas tower purifier according to claim 5, is characterized in that: described some dividing plates are the major arc structure isometrical with secondary oxidation groove, and the breach that cushions between two dividing plate is spaced apart towards equal left and right.
7. waste gas tower purifier according to claim 6, is characterized in that: described some buffering dividing plate in the vertical direction equidistant placement.
8. waste gas tower purifier according to claim 7, is characterized in that: described some dividing plate in the vertical direction equidistant placement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420315837.0U CN203916445U (en) | 2014-06-13 | 2014-06-13 | Waste gas tower purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420315837.0U CN203916445U (en) | 2014-06-13 | 2014-06-13 | Waste gas tower purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203916445U true CN203916445U (en) | 2014-11-05 |
Family
ID=51812328
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420315837.0U Expired - Fee Related CN203916445U (en) | 2014-06-13 | 2014-06-13 | Waste gas tower purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203916445U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287114A (en) * | 2016-07-21 | 2017-01-04 | 四川追月科技有限责任公司 | A kind of vacuum heat-preservation thermal-insulation device |
| CN106975337A (en) * | 2017-04-28 | 2017-07-25 | 包训祥 | Chlorine dioxide gaseous oxidation denitration integrated device and its technique |
| CN114832595A (en) * | 2022-04-11 | 2022-08-02 | 福建德尔科技股份有限公司 | Electronic grade sulfur hexafluoride alkali washing device and control method thereof |
-
2014
- 2014-06-13 CN CN201420315837.0U patent/CN203916445U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287114A (en) * | 2016-07-21 | 2017-01-04 | 四川追月科技有限责任公司 | A kind of vacuum heat-preservation thermal-insulation device |
| CN106975337A (en) * | 2017-04-28 | 2017-07-25 | 包训祥 | Chlorine dioxide gaseous oxidation denitration integrated device and its technique |
| CN114832595A (en) * | 2022-04-11 | 2022-08-02 | 福建德尔科技股份有限公司 | Electronic grade sulfur hexafluoride alkali washing device and control method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141105 |