CN204058034U - Waste gas catalytic oxidation waste water plant can be collected - Google Patents
Waste gas catalytic oxidation waste water plant can be collected Download PDFInfo
- Publication number
- CN204058034U CN204058034U CN201420481420.1U CN201420481420U CN204058034U CN 204058034 U CN204058034 U CN 204058034U CN 201420481420 U CN201420481420 U CN 201420481420U CN 204058034 U CN204058034 U CN 204058034U
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- reactive tank
- waste gas
- inlet pipe
- catalytic oxidation
- water plant
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Abstract
One can collect waste gas catalytic oxidation waste water plant, comprises transformer, reactive tank, positive plate, negative plate, inlet pipe, waste gas collecting system; Described positive plate is connected with the positive pole of transformer, and described negative plate is connected with the negative pole of transformer; Described positive plate and negative plate paralleling and interleaving are arranged in reactive tank; Described reactive tank inside is an airtight cavity; Described reactive tank is provided with water-in and water outlet; Reaction tank bottom arranges inlet pipe; Described inlet pipe is arranged air inlet port upwards; Granule electrode is provided with in described reactive tank; Described waste gas collecting system comprises vacuum fan, ventpipe, pneumatic trough; Described vacuum fan is arranged on the top of reactive tank, and communicates with reactive tank; Described ventpipe one end is connected with vacuum fan, and the other end stretches in pneumatic trough.The waste gas that reactive tank inside produces is collected in pneumatic trough by ventpipe, avoids the problem allowing waste gas directly discharge, protects environment, it also avoid some potential safety hazards simultaneously.
Description
Technical field
The utility model relates to catalytic oxidation equipment, particularly a kind of device collecting the waste gas that catalytic oxidation produces.
Background technology
At present, the domestic microbiotic having 300 many enterprises to produce more than 70 kind, account for 20% ~ 30% of Gross World Product, the feature of the waste water produced in production of antibiotics process is: water-quality constituents is complicated, Pollutants in Wastewater content is high, in waste water difficult degradation and objectionable impurities many, effluent part salt content is high.Domestic and international pretreated method adopts the mode of Fenton and ozone oxidation, because these modes have the shortcomings such as processing cost is high, oxidation is not thorough, create again the mode of catalytic oxidation to process antibiotic waste water, at present, the equipment of this catalytic oxidation is comparatively ripe, generally comprises transformer, reactive tank, positive plate, negative plate, inlet pipe; Described positive plate is connected with the positive pole of transformer, and described negative plate is connected with the negative pole of transformer; Described positive plate and negative plate paralleling and interleaving are arranged in reactive tank; Described side, reactive tank bottom is provided with water-in, and side, top is provided with water outlet; Described reactive tank inner bottom part arranges inlet pipe, inlet pipe is arranged air inlet port upwards; Granule electrode is provided with in described reactive tank.Directly will discharge in atmosphere if such equipment has waste gas to produce, exist and pollute and safe hidden danger.
Summary of the invention
For above-mentioned the deficiencies in the prior art part, the problem that the utility model solves is that waste gas can not get reclaiming, and polluted air, causes potential safety hazard.
The technical solution of the utility model:
One can collect waste gas catalytic oxidation waste water plant, comprises transformer, reactive tank, positive plate, negative plate, inlet pipe, waste gas collecting system; Described positive plate is connected with the positive pole of transformer, and described negative plate is connected with the negative pole of transformer; Described positive plate and negative plate paralleling and interleaving are arranged in reactive tank; Described reactive tank inside is an airtight cavity; Described side, reactive tank bottom is provided with water-in, and side, top is provided with water outlet; Described reactive tank inner bottom part arranges inlet pipe; Described inlet pipe is arranged air inlet port upwards; Granule electrode is provided with in described reactive tank; Described waste gas collecting system comprises vacuum fan, ventpipe, pneumatic trough; Described vacuum fan is arranged on the top of reactive tank, and communicates with reactive tank; Described ventpipe one end is connected with vacuum fan, and the other end stretches in pneumatic trough.
Further, the S-shaped structure of described inlet pipe, described air inlet port is evenly distributed in the inlet pipe of S shape structure.
Further, described granule electrode is gac-nano titanium oxide.
Further, described reactive tank is made up of PVC material.
Further, described positive plate is that graphite material is made.
Further, described negative plate is made up of stainless material.
The beneficial effects of the utility model
Reactive tank is airtight structure, and reactive tank installs waste gas collecting system, and waste gas collecting system comprises vacuum fan, ventpipe, pneumatic trough; Vacuum fan is arranged on the top of reactive tank, and communicates with reactive tank; Ventpipe one end is connected with vacuum fan, and the other end stretches in pneumatic trough.By the effect of vacuum fan, can the waste gas that reactive tank inside produces be collected in pneumatic trough by ventpipe, avoid the problem allowing waste gas directly discharge, protect environment, it also avoid some potential safety hazards simultaneously.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present utility model.
Fig. 2 is the structural representation of inlet pipe of the present utility model.
Embodiment
Below to being described in further detail the utility model content by reference to the accompanying drawings.
As shown in Figure 1, one can collect waste gas catalytic oxidation waste water plant, comprises transformer 1, reactive tank 2, positive plate 3, negative plate 4, inlet pipe 5, waste gas collecting system 6.Transformer 1 can control voltage, electric current size, regulate suitable operating voltage.Positive plate 3 is made up of graphite material, is connected with the positive pole of transformer 1.Negative plate 4 is made up of stainless material, is connected with the negative pole of transformer 1.Positive plate 3 and negative plate 4 paralleling and interleaving are arranged in reactive tank 2, and the paralleling and interleaving of positive plate 3 and negative plate 4 is arranged, and can accelerate speed and the effect of catalytic oxidation.Reactive tank 2 preferably PVC material is made, and its inside is an airtight cavity.Side, reactive tank 2 bottom is provided with water-in 21, and side, top is provided with water outlet 22.In reactive tank, inlet pipe 5 is set bottom 2.Inlet pipe 5 is arranged air inlet port 51 upwards, as shown in Figure 2.Be provided with granule electrode in reactive tank 2, particle motor can be preferably gac-nano titanium oxide.Waste gas collecting system comprises vacuum fan 61, ventpipe 62, pneumatic trough 63.Vacuum fan 61 is arranged on the top of reactive tank 2, and communicates with reactive tank 2.Ventpipe 62 one end is connected with vacuum fan 61, and the other end stretches in pneumatic trough 63.Further, the S-shaped structure of inlet pipe 5, air inlet port is evenly distributed in the inlet pipe of S shape structure, makes inlet pipe 5 air inlet more even, those skilled in the art considered that inlet pipe 5 also can be other structure, as Z-shaped, X-shaped etc.Reactive tank 2 is in airtight structure, reactive tank 2 is installed waste gas collecting system 6, gas sampling 6 system comprises vacuum fan 61, ventpipe 62, pneumatic trough 63, vacuum fan 61 is arranged on the top of reactive tank 2, and communicate with reactive tank 2, ventpipe 62 one end is connected with vacuum fan 61, the other end stretches in pneumatic trough 63, such vibrational power flow, by the effect of vacuum fan 61, can the waste gas that reactive tank 2 inside produces be collected in pneumatic trough 63 by ventpipe 62, avoid the problem allowing waste gas directly discharge, protect environment, it also avoid some potential safety hazards simultaneously.
Claims (6)
1. can collect a waste gas catalytic oxidation waste water plant, it is characterized in that, comprise transformer, reactive tank, positive plate, negative plate, inlet pipe, waste gas collecting system; Described positive plate is connected with the positive pole of transformer, and described negative plate is connected with the negative pole of transformer; Described positive plate and negative plate paralleling and interleaving are arranged in reactive tank; Described reactive tank inside is an airtight cavity; Described side, reactive tank bottom is provided with water-in, and side, top is provided with water outlet; Described reactive tank inner bottom part arranges inlet pipe; Described inlet pipe is arranged air inlet port upwards; Granule electrode is provided with in described reactive tank; Described waste gas collecting system comprises vacuum fan, ventpipe, pneumatic trough; Described vacuum fan is arranged on the top of reactive tank, and communicates with reactive tank; Described ventpipe one end is connected with vacuum fan, and the other end stretches in pneumatic trough.
2. according to claim 1ly collect waste gas catalytic oxidation waste water plant, it is characterized in that, the S-shaped structure of described inlet pipe, described air inlet port is evenly distributed in the inlet pipe of S shape structure.
3. according to claim 1ly collect waste gas catalytic oxidation waste water plant, it is characterized in that, described granule electrode is gac-nano titanium oxide.
4. according to claim 1ly collect waste gas catalytic oxidation waste water plant, it is characterized in that, described reactive tank is made up of PVC material.
5. according to claim 1ly collect waste gas catalytic oxidation waste water plant, it is characterized in that, described positive plate is that graphite material is made.
6. according to claim 1ly collect waste gas catalytic oxidation waste water plant, it is characterized in that, described negative plate is made up of stainless material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420481420.1U CN204058034U (en) | 2014-08-26 | 2014-08-26 | Waste gas catalytic oxidation waste water plant can be collected |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420481420.1U CN204058034U (en) | 2014-08-26 | 2014-08-26 | Waste gas catalytic oxidation waste water plant can be collected |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204058034U true CN204058034U (en) | 2014-12-31 |
Family
ID=52199588
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420481420.1U Expired - Fee Related CN204058034U (en) | 2014-08-26 | 2014-08-26 | Waste gas catalytic oxidation waste water plant can be collected |
Country Status (1)
| Country | Link |
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| CN (1) | CN204058034U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105399188A (en) * | 2015-12-07 | 2016-03-16 | 江苏博大环保股份有限公司 | Polarity regulation electrocatalytic oxidation device |
| CN106365258A (en) * | 2016-09-06 | 2017-02-01 | 深圳市君想环境科技有限公司 | Three-dimensional electrode electrocatalytic oxidization device for high-salt-content high-COD (chemical oxygen demand) wastewater |
| CN115340207A (en) * | 2022-07-27 | 2022-11-15 | 北京京能能源技术研究有限责任公司 | Method for treating wastewater discharged by circulating water by using reclaimed water source |
-
2014
- 2014-08-26 CN CN201420481420.1U patent/CN204058034U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105399188A (en) * | 2015-12-07 | 2016-03-16 | 江苏博大环保股份有限公司 | Polarity regulation electrocatalytic oxidation device |
| CN106365258A (en) * | 2016-09-06 | 2017-02-01 | 深圳市君想环境科技有限公司 | Three-dimensional electrode electrocatalytic oxidization device for high-salt-content high-COD (chemical oxygen demand) wastewater |
| CN115340207A (en) * | 2022-07-27 | 2022-11-15 | 北京京能能源技术研究有限责任公司 | Method for treating wastewater discharged by circulating water by using reclaimed water source |
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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 |
Granted publication date: 20141231 Termination date: 20180826 |
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| CF01 | Termination of patent right due to non-payment of annual fee |