CN204338019U - A kind of ozone tail gas hot blast decomposer - Google Patents
A kind of ozone tail gas hot blast decomposer Download PDFInfo
- Publication number
- CN204338019U CN204338019U CN201420806224.7U CN201420806224U CN204338019U CN 204338019 U CN204338019 U CN 204338019U CN 201420806224 U CN201420806224 U CN 201420806224U CN 204338019 U CN204338019 U CN 204338019U
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- CN
- China
- Prior art keywords
- tail gas
- tank
- ozone tail
- ozone
- hot blast
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- 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.)
- Expired - Fee Related
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
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- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
A kind of ozone tail gas hot blast decomposer that the utility model provides, the extraneous air entered from air inlet end carries out heat drying after filtering in inlet air heating tank, after dry filter with enter the ozone tail gas heat of mixing mixed in surge tank and decompose, residual ozone gas gives off final decomposition completely in ozone decomposed tank, the utility model structure is simple, very clear, small in volume, installation discharge and drainage impurity all efficient and convenient, Automated condtrol can be adopted, time saving and energy saving safer for operating personnel, compare and pass logical ozonolysis equipment, adopt this ozone tail gas hot blast decomposer operating efficiency higher, each critical piece greatly improves service life, greatly reduce the cost of maintenance, manpower and materials reduce a lot, do not need frequent maintenance, and process ozone tail gas effect is very good through practice operation, there is very high economic worth.
Description
Technical field
The utility model relates to a kind of decomposer, and particularly one is used for ozone tail gas decomposer, belongs to Ozone generation field.
Background technology
In originally traditional ozone tail gas decomposer, mixing surge tank is cancelled, the ozone gas entered from ozone tail gas control valve directly enters in inlet air heating tank from gas port end, its hot-blast outlet of giving vent to anger directly enters and is mixed into gas port, the result caused like this is: the heating tube in inlet air heating tank is fallen by the ozone corrosion of high concentration in a short period of time and cannot normal heating work, and simultaneously some steam enters in ozone-decomposing agent and causes ozone-decomposing agent to lose efficacy and finally cannot divide and take off ozone.Because the ozone tail gas effect of ozone decomposed tank built-in ozone-decomposing agent process clean dried atm number low concentration is fine; and this ozone-decomposing agent is afraid of moisture; if round granular ozone-decomposing agent very easily resolves into particle until powdery and lost efficacy cannot ozone decomposition when in gaseous mixture, steam is larger; thus above-mentioned common ozone tail gas decomposer; very large drawback is all had to ozone devices protection and the actual normal operating of operating personnel during practical operation uses, all infeasible.
Utility model content
Problem to be solved in the utility model is for above-mentioned technological deficiency, provides a kind of and installs the ozone tail gas hot blast decomposer that Operation and Maintenance is more practical, convenient and swift, treatment effect is good.
For overcoming the above problems the scheme that the utility model adopts:
A kind of ozone tail gas hot blast decomposer, comprise air intake filter, inlet air heating tank, heating tube, mixing surge tank, ozone tail gas decomposes tank, it is inner that described heating tube inserts air inlet heating tank, described heating tube head and the tail two ends are provided with heating tube binding post, described inlet air heating tank side is provided with air inlet end, described inlet air heating tank upper end is provided with hot blast gas outlet, lower end is provided with the water trap that catchments, described air intake filter side is provided with air inlet end opposite side and is connected with the air inlet end of inlet air heating tank by pipeline, pipeline between described air inlet end and air inlet end is provided with air intake control valve, described air intake filter lower end is provided with water trap, described mixing surge tank side is provided with and blends gas port, described mixing surge tank upper end is provided with ozone tail gas import, lower end is provided with hot blast air inlet successively and catchments water trap, described ozone tail gas import is provided with ozone tail gas control valve, the hot blast air inlet of described mixing surge tank is connected with the hot blast gas outlet of inlet air heating tank by pipeline, described ozone tail gas decomposition tank side is provided with and is mixed into gas port, described ozone tail gas decomposes tank upper end and is provided with exhaust port, lower end is provided with the water trap that catchments, the gas port that is mixed into that described ozone tail gas decomposes tank is connected by the gas port that blends of pipeline with mixing surge tank, described ozone tail gas decomposes tank inside and is provided with lower clapboard successively, stainless (steel) wire, median septum, ozone decomposition catalyst and upper spacer, described lower clapboard, median septum and upper spacer are equipped with multiple manhole.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, described lower clapboard, median septum and upper spacer are the stainless plate being covered with 3mm aperture.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, described stainless (steel) wire is 100 orders.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, described ozone decomposition catalyst is round granular, and diameter is about 6mm.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, the tank body that described inlet air heating tank, mixing surge tank and ozone tail gas decompose tank adopts stainless steel material, stainless steel materials is rolled into cylindrical tube and adopts argon arc welding to form.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, the pipeline of described heating tube adopts stainless steel material to make.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, the hot blast air inlet in described mixing surge tank is made into cylindrical tube, is highly 1/3 of mixing surge tank.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, described pipeline by bolt respectively with air intake filter, inlet air heating tank, mix surge tank and ozone tail gas and decompose tank and achieve a fixed connection.
Above-mentioned a kind of ozone tail gas hot blast decomposer, wherein, the described water trap that catchments, air intake control valve, ozone tail gas control valve all adopt the mode be threaded, and need install that to discharge part with bolts.
The beneficial effect of this programme:
A kind of ozone tail gas hot blast decomposer that the utility model provides, the extraneous air that air inlet end enters carries out heat drying after filtering in inlet air heating tank, after dry filter with enter the ozone tail gas heat of mixing mixed in surge tank and decompose, residual ozone gas gives off final decomposition completely in ozone decomposed tank, and the lower end of inlet air heating tank and mixing surge tank and ozone decomposed tank is equipped with the water trap that catchments, such steam cannot enter in ozone-decomposing agent, and gaseous mixture is dry, greatly improve the activity of ozone-decomposing agent, the capability improving of ozone-decomposing agent ozone decomposition is to optimum state, ozone-decomposing agent keeps cylindrical particles shape for a long time simultaneously, extend the service life of ozone-decomposing agent, the utility model structure is simple simultaneously, very clear, small in volume, installation discharge and drainage impurity all efficient and convenient, Automated condtrol can be adopted, time saving and energy saving safer for operating personnel, compare and pass logical ozonolysis equipment, adopt this ozone tail gas hot blast decomposer operating efficiency higher, each critical piece greatly improves service life, greatly reduces the cost of maintenance, manpower and materials reduce a lot, do not need frequent maintenance, and process ozone tail gas effect is very good through practice operation, has very high economic worth.
Accompanying drawing explanation
Fig. 1 is the utility model overall structure figure.
Detailed description of the invention
As shown in the figure, a kind of ozone tail gas hot blast decomposer, comprise air intake filter 2, inlet air heating tank 9, heating tube 8, mixing surge tank 16, ozone tail gas decomposes tank 18, it is inner that described heating tube 8 inserts air inlet heating tank 9, described heating tube 8 head and the tail two ends are provided with heating tube binding post 10, described inlet air heating tank 9 side is provided with air inlet end 7, described inlet air heating tank 9 upper end is provided with hot blast gas outlet 11, lower end is provided with the water trap 3 that catchments, described air intake filter 2 side is provided with air inlet end 1 opposite side and is connected with the air inlet end 7 of inlet air heating tank 9 by pipeline 5, pipeline 5 between described air intake filter 2 and air inlet end 7 is provided with air intake control valve 6, described air intake filter 2 lower end is provided with water trap 4, described mixing surge tank 16 side is provided with and blends gas port 13, described mixing surge tank 16 upper end is provided with ozone tail gas import 15, lower end is provided with hot blast air inlet 12 successively and catchments water trap 3, described ozone tail gas import 15 is provided with ozone tail gas control valve 14, the hot blast air inlet 12 of described mixing surge tank 16 is connected with the hot blast gas outlet 11 of inlet air heating tank 9 by pipeline 5, described ozone tail gas decomposition tank 18 side is provided with and is mixed into gas port 19, described ozone tail gas decomposes tank 18 upper end and is provided with exhaust port 25, lower end is provided with the water trap 3 that catchments, the gas port 19 that is mixed into that described ozone tail gas decomposes tank 18 is connected by the gas port 13 that blends of pipeline 5 with mixing surge tank 16, described ozone tail gas decomposes tank 18 inside and is provided with lower clapboard 21 successively, stainless (steel) wire 17, median septum 22, ozone decomposition catalyst 23 and upper spacer 24, described lower clapboard 21, median septum 22 and upper spacer 24 are equipped with multiple manhole, described lower clapboard 21, median septum 22 and upper spacer 24 are the stainless plate being covered with 3mm aperture, described stainless (steel) wire 17 is 100 orders, described ozone decomposition catalyst 23 is round granular, diameter is about 6mm.
A kind of ozone tail gas hot blast decomposer that the utility model provides, during work, air filters from air inlet end 1 through entering air intake filter 2, emitted by water trap 4 after removal of impurities, pure air after filtration controls the air capacity size added by air intake control valve 6, then from bottom to top flowed out from hot blast gas outlet 11 by the air inlet end 7 of inlet air heating tank 9, the clean hot blast of pass-out is from bottom to top entered by the hot wind inlet 12 of mixing surge tank 16, with by ozone tail gas control valve 14 from the ozone tail gas convection current that the upper port ozone tail gas import 15 mixing surge tank 16 enters mix and divide take off contained by about 80% ozone amount, simultaneously mixed gas blends gas port 13 from the side of mixing surge tank 16 and flows out, the gas port 13 that blends that residual gas is heavier than air from the side gives off, mist is from bottom to top entered by the gas port 19 that is mixed into of ozone decomposed tank 18, stainless (steel) wire 17(100 order is entered by the lower clapboard 21 being covered with 3mm aperture) finally arrived in ozone decomposition catalyst 23 by the median septum 22 being covered with 3mm aperture again, in such mist, the ozone of remaining contained 20% is completely broken down, the gas being broken off ozone is given off by exhaust port 25 by the upper spacer 24 being covered with 3mm aperture.
A kind of ozone tail gas hot blast decomposer that the utility model provides, the extraneous air that air inlet end enters carries out heat drying after filtering in inlet air heating tank, after dry filter with enter the ozone tail gas heat of mixing mixed in surge tank and decompose, residual ozone gas gives off final decomposition completely in ozone decomposed tank, and the lower end of inlet air heating tank and mixing surge tank and ozone decomposed tank is equipped with the water trap that catchments, such steam cannot enter in ozone-decomposing agent, and gaseous mixture is dry, greatly improve the activity of ozone-decomposing agent, the capability improving of ozone-decomposing agent ozone decomposition is to optimum state, ozone-decomposing agent keeps cylindrical particles shape for a long time simultaneously, extend the service life of ozone-decomposing agent, the utility model structure is simple simultaneously, very clear, small in volume, installation discharge and drainage impurity all efficient and convenient, Automated condtrol can be adopted, time saving and energy saving safer for operating personnel, compare and pass logical ozonolysis equipment, adopt this ozone tail gas hot blast decomposer operating efficiency higher, each critical piece greatly improves service life, greatly reduces the cost of maintenance, manpower and materials reduce a lot, do not need frequent maintenance, and process ozone tail gas effect is very good through practice operation, has very high economic worth.
Be only the utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the change that can expect easily or replacement, all should be encompassed in protection domain of the present utility model.Therefore, protection domain of the present utility model should be as the criterion with the protection domain of claims.
Claims (9)
1. an ozone tail gas hot blast decomposer, comprise air intake filter, inlet air heating tank, heating tube, mixing surge tank, ozone tail gas decomposes tank, it is characterized by, it is inner that described heating tube inserts air inlet heating tank, described heating tube head and the tail two ends are provided with heating tube binding post, described inlet air heating tank side is provided with air inlet end, described inlet air heating tank upper end is provided with hot blast gas outlet, lower end is provided with the water trap that catchments, described air intake filter side is provided with air inlet end opposite side and is connected with the air inlet end of inlet air heating tank by pipeline, pipeline between described air inlet end and air inlet end is provided with air intake control valve, described air intake filter lower end is provided with water trap, described mixing surge tank side is provided with and blends gas port, described mixing surge tank upper end is provided with ozone tail gas import, lower end is provided with hot blast air inlet successively and catchments water trap, described ozone tail gas import is provided with ozone tail gas control valve, the hot blast air inlet of described mixing surge tank is connected with the hot blast gas outlet of inlet air heating tank by pipeline, described ozone tail gas decomposition tank side is provided with and is mixed into gas port, described ozone tail gas decomposes tank upper end and is provided with exhaust port, lower end is provided with the water trap that catchments, the gas port that is mixed into that described ozone tail gas decomposes tank is connected by the gas port that blends of pipeline with mixing surge tank, described ozone tail gas decomposes tank inside and is provided with lower clapboard successively, stainless (steel) wire, median septum, ozone decomposition catalyst and upper spacer, described lower clapboard, median septum and upper spacer are equipped with multiple manhole.
2. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, described lower clapboard, median septum and upper spacer are the stainless plate being covered with 3mm aperture.
3. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, described stainless (steel) wire is 100 orders.
4. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, described ozone decomposition catalyst is round granular, and diameter is about 6mm.
5. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, the tank body that described inlet air heating tank, mixing surge tank and ozone tail gas decompose tank adopts stainless steel material, stainless steel materials is rolled into cylindrical tube and adopts argon arc welding to form.
6. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, is characterized by, and the pipeline of described heating tube adopts stainless steel material to make.
7. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, the hot blast air inlet in described mixing surge tank is made into cylindrical tube, is highly 1/3 of mixing surge tank.
8. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, is characterized by, described pipeline by bolt respectively with air intake filter, inlet air heating tank, mix surge tank and ozone tail gas and decompose tank and achieve a fixed connection.
9. a kind of ozone tail gas hot blast decomposer as claimed in claim 1, it is characterized by, the described water trap that catchments, air intake control valve, ozone tail gas control valve all adopt the mode be threaded, and need install that to discharge part with bolts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420806224.7U CN204338019U (en) | 2014-12-19 | 2014-12-19 | A kind of ozone tail gas hot blast decomposer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420806224.7U CN204338019U (en) | 2014-12-19 | 2014-12-19 | A kind of ozone tail gas hot blast decomposer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204338019U true CN204338019U (en) | 2015-05-20 |
Family
ID=53221323
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420806224.7U Expired - Fee Related CN204338019U (en) | 2014-12-19 | 2014-12-19 | A kind of ozone tail gas hot blast decomposer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204338019U (en) |
-
2014
- 2014-12-19 CN CN201420806224.7U patent/CN204338019U/en not_active Expired - Fee Related
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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: 20150520 Termination date: 20171219 |