CN204911191U - Advanced treatment equipment is united to peculiar smell, foul gas - Google Patents
Advanced treatment equipment is united to peculiar smell, foul gas Download PDFInfo
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- CN204911191U CN204911191U CN201520665086.XU CN201520665086U CN204911191U CN 204911191 U CN204911191 U CN 204911191U CN 201520665086 U CN201520665086 U CN 201520665086U CN 204911191 U CN204911191 U CN 204911191U
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Abstract
The utility model discloses an advanced treatment equipment is united to peculiar smell, foul gas belongs to the waste gas treatment technical field. It includes: malleation gas collection air supply system, pretreatment systems, degree of depth processing system, materialization washing system and tail gas discharge system. Pressure -fired gas gathering system collects required process gas by vacuum pump or gas collecting channel and is connected with the pretreatment systems import, and pretreatment systems is connected with degree of depth processing system, in degree of depth processing system and the materialization and washing system be connected, in the materialization and washing system and discharge system's exhaust fan be connected, the export and the chimney of fan are connected the emission. The utility model is used for efficient handling to peculiar smell, foul gas to no secondary pollution reaches emission standard.
Description
Technical field
The utility model relates to a kind of malodorous gas processing device, belongs to waste treatment technical field.
Background technology
At present, the industry such as chemical industry, agricultural chemicals, printing, sewage treatment plant, smelting, destructor plant can produce peculiar smell and foul gas affects air quality and nearby residents life in production run.In existing treatment technology, generally adopt traditional soda acid spray and active carbon absorption technology to can't resolve the impact of peculiar smell and foul gas, and the drawbacks such as secondary pollution operating cost is high can be produced.
Summary of the invention
In order to overcome above-mentioned the deficiencies in the prior art part, the utility model provides a kind of peculiar smell, foul gas combined depth treatment facility, effectively can process peculiar smell, foul gas, and non-secondary pollution, reach discharge standard.
The utility model is achieved by the following technical solution: a kind of peculiar smell, foul gas combined depth treatment facility, it comprises malleation gas collection supply air system, pretreatment system, in advanced treatment system and materialization and washing system, described pretreatment system, following structure is included with washing system: a tower main body in advanced treatment system and materialization, gas outlet is arranged at the top of tower main body, air inlet is arranged at the bottom of tower main body, the inner top layer of tower main body is provided with except water layer, below except water layer is arranged at intervals with some spraying layers and packing layer, every layer of spraying layer is arranged on above the packing layer corresponding with it, in described pretreatment system, advanced treatment system and materialization and washing system include the cyclic water tank supplied water by water source, water is delivered to each spraying layer by water circulating pump by cyclic water tank, pretreatment micro-pore aeration reactor is housed bottom described pretreatment system, advanced treating micro-pore aeration reactor is housed bottom described advanced treatment system, and described pretreatment micro-pore aeration reactor and advanced treating micro-pore aeration reactor are connected to ozone generator by pipeline, described malleation gas collection supply air system is imported and exported with pretreatment system and is connected, described pretreatment system gas outlet is connected with the air inlet of described advanced treatment system, described advanced treatment system gas outlet is connected with washing system air inlet with described materialization, in described materialization and washing system gas outlet is connected to exhaust blower, and the exhaust outlet of exhaust blower is connected to chimney.
Spraying layer and the packing layer of described tower main body have two-stage, and they are from top to bottom one-level spraying layer, one-level packing layer, secondary spraying layer and secondary packing layer respectively.
Described pretreatment micro-pore aeration reactor and advanced treating micro-pore aeration reactor are corundum microporous aerator reactors.
Combined Treatment agent is added in the cyclic water tank of described advanced treatment system.
The beneficial effects of the utility model are: the utility model can carry out more effectively and thoroughly processing to peculiar smell, foul gas, and non-secondary pollution, reach discharge standard.Solve the difficult problem that traditional soda acid spray can't resolve with active carbon absorption technology, and stable, efficient, thorough, operating cost is cheap.
Accompanying drawing explanation
According to drawings and embodiments the utility model is further illustrated below.
Fig. 1 is the utility model structural representation.
In figure, (1) malleation gas collection supply air system, (2) ozone generator, (3) pretreatment system, (4) are except in water layer, (5) one-level spraying layer, (6) one-level packing layer, (7) secondary spraying layer, (8) secondary packing layer, (9) water source, (10) pretreatment micro-pore aeration reactor, (11) cyclic water tank, (12) water circulating pump, (13) advanced treatment system, (14) advanced treating micro-pore aeration reactor, (15) materialization and washing system, (16) exhaust blower, (17) chimney.
Detailed description of the invention
A kind of peculiar smell as shown in Figure 1, foul gas combined depth treatment facility, it comprises malleation gas collection supply air system 1, pretreatment system 3, in advanced treatment system 13 and materialization and washing system 15, described pretreatment system 3, following structure is included with washing system 15: a tower main body in advanced treatment system 13 and materialization, gas outlet is arranged at the top of tower main body, air inlet is arranged at the bottom of tower main body, the inner top layer of tower main body is provided with except water layer 4, below except water layer 4 is arranged at intervals with some spraying layers and packing layer, every layer of spraying layer is arranged on above the packing layer corresponding with it, in described pretreatment system 3, advanced treatment system 13 and materialization and washing system 15 include the cyclic water tank 11 supplied water by water source 9, water is delivered to each spraying layer by water circulating pump 12 by cyclic water tank 11, pretreatment micro-pore aeration reactor 10 is housed bottom described pretreatment system 3, each micropore size on micro-pore aeration reactor is 15 ~ 20 μm, advanced treating micro-pore aeration reactor 14 is housed bottom described advanced treatment system 13, and described pretreatment micro-pore aeration reactor 10 and advanced treating micro-pore aeration reactor 14 are connected to ozone generator 2 by pipeline, described malleation gas collection supply air system 1 collects required process gas by vavuum pump or gas skirt, malleation gas collection supply air system 1 is imported and exported with pretreatment system 3 and is connected, described pretreatment system 3 gas outlet is connected with the air inlet of described advanced treatment system 13, described advanced treatment system 13 gas outlet is connected with washing system 15 air inlet with described materialization, in described materialization and washing system 15 gas outlet is connected to exhaust blower 16, and the exhaust outlet of exhaust blower 16 is connected to chimney 17.
Spraying layer and the packing layer of described tower main body have two-stage, and they are from top to bottom one-level spraying layer 5, one-level packing layer 6, secondary spraying layer 7 and secondary packing layer 8 respectively.
Described pretreatment micro-pore aeration reactor 10 and advanced treating micro-pore aeration reactor 14 are corundum microporous aerator reactors.
Combined Treatment agent can be according to circumstances added in the cyclic water tank 11 of described advanced treatment system 13.
Operation principle of the present utility model is: malleation gas collection supply air system 1 is collected required process gas and entered pretreatment system 3, ozone generator 2 passes through pretreatment micro-pore aeration reactor 10 with required process gas generation gas phase to gas phase, and the intersection pretreatment of gas phase to liquid phase makes the molecule of required process gas change.
Advanced treatment system 13 adds Combined Treatment agent and combines with the ozone that ozone generator 2 produces in its cyclic water tank, the one-level spraying layer being promoted to advanced treatment system 13 at water circulating pump passes through the one-level packing layer of advanced treatment system, secondary spraying layer, secondary packing layer make it to produce liquid phase to liquid phase, liquid phase is to the advanced treating of gas phase further for the gas processed through pretreatment system 3 advanced treating, and its end product is H2O, CO2 and carboxylic acid.
The carboxylic acid generation acid-base neutralization reaction produced with washing system 15 pairs of advanced treatment systems 13 in materialization, generates nontoxic material.
To make a gift to someone chimney 17 qualified discharge through exhaust blower 16 through the gas in materialization and after washing system process.
A kind of peculiar smell described in the utility model, foul gas combined depth treating apparatus effectively can process peculiar smell, foul gas, and non-secondary pollution, reach discharge standard.
Claims (4)
1. a peculiar smell, foul gas combined depth treatment facility, it is characterized in that: it comprises malleation gas collection supply air system (1), pretreatment system (3), in advanced treatment system (13) and materialization and washing system (15), described pretreatment system (3), following structure is included with washing system (15): a tower main body in advanced treatment system (13) and materialization, gas outlet is arranged at the top of tower main body, air inlet is arranged at the bottom of tower main body, the inner top layer of tower main body is provided with except water layer (4), except the below of water layer (4) is arranged at intervals with some spraying layers and packing layer, every layer of spraying layer is arranged on above the packing layer corresponding with it, include with washing system (15) cyclic water tank (11) supplied water by water source (9) in described pretreatment system (3), advanced treatment system (13) and materialization, water is delivered to each spraying layer by water circulating pump (12) by cyclic water tank (11), pretreatment micro-pore aeration reactor (10) is equipped with in described pretreatment system (3) bottom, advanced treating micro-pore aeration reactor (14) is equipped with in described advanced treatment system (13) bottom, and described pretreatment micro-pore aeration reactor (10) and advanced treating micro-pore aeration reactor (14) are connected to ozone generator (2) by pipeline, described malleation gas collection supply air system (1) is imported and exported with pretreatment system (3) and is connected, described pretreatment system (3) gas outlet is connected with the air inlet of described advanced treatment system (13), described advanced treatment system (13) gas outlet is connected with washing system (15) air inlet with described materialization, in described materialization and washing system (15) gas outlet is connected to exhaust blower (16), and the exhaust outlet of exhaust blower (16) is connected to chimney (17).
2. peculiar smell according to claim 1, foul gas combined depth treatment facility, it is characterized in that: spraying layer and the packing layer of described tower main body have two-stage, they are from top to bottom one-level spraying layer (5), one-level packing layer (6), secondary spraying layer (7) and secondary packing layer (8) respectively.
3. peculiar smell according to claim 1, foul gas combined depth treatment facility, is characterized in that: described pretreatment micro-pore aeration reactor (10) and advanced treating micro-pore aeration reactor (14) are corundum microporous aerator reactors.
4. peculiar smell according to claim 1, foul gas combined depth treatment facility, is characterized in that: add Combined Treatment agent in the cyclic water tank (11) of described advanced treatment system (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520665086.XU CN204911191U (en) | 2015-08-28 | 2015-08-28 | Advanced treatment equipment is united to peculiar smell, foul gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520665086.XU CN204911191U (en) | 2015-08-28 | 2015-08-28 | Advanced treatment equipment is united to peculiar smell, foul gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204911191U true CN204911191U (en) | 2015-12-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520665086.XU Expired - Fee Related CN204911191U (en) | 2015-08-28 | 2015-08-28 | Advanced treatment equipment is united to peculiar smell, foul gas |
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| CN (1) | CN204911191U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115069070A (en) * | 2022-07-28 | 2022-09-20 | 鞍钢化学科技有限公司 | System and method for anaerobic positive pressure recovery of coal-based needle coke tail gas |
-
2015
- 2015-08-28 CN CN201520665086.XU patent/CN204911191U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115069070A (en) * | 2022-07-28 | 2022-09-20 | 鞍钢化学科技有限公司 | System and method for anaerobic positive pressure recovery of coal-based needle coke tail gas |
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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: 20151230 Termination date: 20160828 |