CN201309855Y - Sewage processing device used in ozone contacting oxidation reaction - Google Patents
Sewage processing device used in ozone contacting oxidation reaction Download PDFInfo
- Publication number
- CN201309855Y CN201309855Y CNU2008202019464U CN200820201946U CN201309855Y CN 201309855 Y CN201309855 Y CN 201309855Y CN U2008202019464 U CNU2008202019464 U CN U2008202019464U CN 200820201946 U CN200820201946 U CN 200820201946U CN 201309855 Y CN201309855 Y CN 201309855Y
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- oxidation reactor
- waste disposal
- quilt
- cotton
- agent
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
A sewage processing device used in an ozone contacting oxidation reaction comprises a control circuit module, an ozone generator, a flocculant feeding and stirring tank, a water pump, and an annular oxidation reactor, wherein the water pump pumps the ozone generated by the ozone generator, sewage and a flocculant in the flocculant feeding and stirring tank to the annular oxidation reactor for reaction; a return outlet is formed on the annular oxidation reactor and connected with the water pump to form a return branch. The sewage processing device has the advantages of high integrity, small volume and convenient use, and can ensure the purification rate to meet the sewage discharge standard.
Description
Technical field:
The utility model belongs to the O3 contacted oxidation reaction sewage disposal in the sewage disposal, and what be specifically related to is a kind of O3 contacted oxidation reaction waste disposal plant.
Background technology:
In the existing sewage disposal machine, the equipment of employing ozonizer and contact oxidation is large-scale reaction tower structure, its height and volume are all bigger, floor space is big, it all is site assembly, the installation sequence complexity, in addition, majority is claimed the company that has purification techniques, the actual efficiency of its treating plant is but often inconsistent with the purification efficiency of claiming, in fact in addition cleaning project stable, comprehensively, up to standard for a long time, thereby still there are the not up to standard and misgivings of being punished of sewage discharge in the producer that makes desire solve sewage disposal after spending.
Summary of the invention:
At the defective that prior art exists, the purpose of this utility model provides a kind of effectively sewage disposal device volume that can overcome above-mentioned defective greatly and to the purification efficiency problem of unstable of sewage.
The technical scheme in the invention for solving the technical problem is: a kind of O3 contacted oxidation reaction waste disposal plant, key is that described treatment unit comprises pilot circuit module, ozonizer, the wad a quilt with cotton reinforced stirred pot of agent, water pump, annular oxidation reactor with fixed attention, the agent three that wads a quilt with cotton with fixed attention in the oxygen that ozonizer takes place described water pump, sewage and the reinforced stirred pot of the agent of wadding a quilt with cotton with fixed attention sucks hybrid reaction in the annular oxidation reactor, and one bypass outlet is set at annular oxidation reactor, insert water pump, constitute a back flow reaction branch road.
Described waste disposal plant is provided with an air compressor, and described air compressor is connected with the ozonizer inlet after excess pressure adjustment, drying etc. are handled.
Described annular oxidation reactor end is provided with an ozone and destroys device.
Described annular oxidation reactor is provided with pressure limiting valve.
The reinforced stirred pot of the described agent of wadding a quilt with cotton with fixed attention is provided with an agitator motor and agitator.
Described annular oxidation reactor contains a tempering tank, is used for sewage and the agent of wadding a quilt with cotton with fixed attention, is provided with a jet pipe in the tempering tank, is used to inject ozone, and described tempering tank connects a circulation type mixing tank, and described mixing tank end is provided with a refluxing opening.
Adopt the utility model to have smaller volume, the convenient use so that O3 contacted oxidation reaction waste disposal plant has higher degree of integration.And can guarantee the purification rate of sewage to make sewage discharge up to standard.
Description of drawings:
Fig. 1 is the utility model Facad structure synoptic diagram.
Fig. 2 is the utility model side structure synoptic diagram.
Fig. 3 is the utility model annular oxidation reactor structural representation.
Fig. 4 is the utility model structure flow chart.
Embodiment:
As Fig. 1～shown in Figure 4, a kind of O3 contacted oxidation reaction waste disposal plant, it is characterized in that described treatment unit comprises pilot circuit module 1, ozonizer 2, the wad a quilt with cotton reinforced stirred pot 3 of agent, water pump 4, annular oxidation reactor 5 with fixed attention, described water pump sucks hybrid reaction in the annular oxidation reactor 5 with oxygen, sewage and the reinforced stirred pot 3 interior agent threes that wad a quilt with cotton with fixed attention of the agent of wadding a quilt with cotton with fixed attention that ozonizer 2 takes place, and one bypass outlet 51 is set at annular oxidation reactor, insert water pump 4, constitute a back flow reaction branch road.The monitoring and the operation of pilot circuit module 1 control complete machine.
Described waste disposal plant is provided with an air compressor 6, and described air compressor is connected with the ozonizer inlet after excess pressure adjustment, drying etc. are handled.
Described annular oxidation reactor end is provided with an ozone and destroys device 52.Ozone destroy device 52 can eliminate more than the ozone that from annular oxidation reactor, overflows.
Described annular oxidation reactor is provided with pressure limiting valve.Pressure limiting valve can prevent the refluence of reactant or the ultimate pressure that pressure surpasses annular oxidation reactor.
The reinforced stirred pot of the described agent of wadding a quilt with cotton with fixed attention is provided with an agitator motor 31 and agitator 32.The agent that can prevent to wad a quilt with cotton with fixed attention of agitator motor 31 and agitator 32 is left standstill and precipitated and separated, guarantees reaction effect.
Described annular oxidation reactor contains a tempering tank, is used for sewage and the agent of wadding a quilt with cotton with fixed attention, is provided with a jet pipe in the tempering tank, is used to inject ozone, and described tempering tank connects a circulation type mixing tank, and described mixing tank end is provided with a refluxing opening 51.
During use, operate: as required, be filled to a certain amount ofly at the reinforced stirred pot 3 of the agent of wadding a quilt with cotton with fixed attention, drop into flocculation agent powder (diatomite) the reinforced stirred pot 3 of agent that advances to wad a quilt with cotton with fixed attention according to following explanation.Open general supply, outside supporting air compressor 6 work, reinforced stirrer is worked simultaneously.Open compressed air inlet valve.Adjust air flowmeter to working flow.Adjust the air pressure of air compressor and adjust valve to operating pressure, open ozonizer 2 power supplys, ozonizer is started working.Open the sewage inlet valve.The pumping source of fetching boiling water, water pump is started working.After the sewage outlet of annular oxidation reactor begins water outlet, open return valve.It is suitable to working flow to adjust sewage inlet valve and return valve.Open the self-circulation time relay of reinforced backflow T-valve, the beginning self-feeding.After half an hour, water outlet begins normally, enters supporting settling tank precipitation, enters normal operating conditions.
Claims (6)
1. waste disposal plant is reacted in an O3 contacted oxidation, it is characterized in that described treatment unit comprises pilot circuit module (1), ozonizer (2), the wad a quilt with cotton reinforced stirred pot (3) of agent, water pump (4), annular oxidation reactor (5) with fixed attention, the agent three that wads a quilt with cotton with fixed attention in the oxygen that ozonizer (2) takes place described water pump, sewage and the reinforced stirred pot (3) of the agent of wadding a quilt with cotton with fixed attention sucks hybrid reaction in the annular oxidation reactor (5), and one bypass outlet (51) is set at annular oxidation reactor, insert water pump (4), constitute a back flow reaction branch road.
2. by the described O3 contacted oxidation reaction of claim 1 waste disposal plant, it is characterized in that described waste disposal plant is provided with an air compressor (6), described air compressor is connected with the ozonizer inlet after excess pressure adjustment, drying etc. are handled.
3. by the described O3 contacted oxidation reaction waste disposal plant of claim 2, it is characterized in that described annular oxidation reactor end is provided with an ozone and destroys device (52).
4. by the described O3 contacted oxidation reaction waste disposal plant of claim 3, it is characterized in that described annular oxidation reactor is provided with pressure limiting valve.
5. by claim 2 or 3 or 4 described O3 contacted oxidation reaction waste disposal plants, it is characterized in that the reinforced stirred pot of the described agent of wadding a quilt with cotton with fixed attention is provided with an agitator motor (31) and agitator (32).
6. by the described O3 contacted oxidation reaction waste disposal plant of claim 5, it is characterized in that described annular oxidation reactor contains a tempering tank, be used for sewage and the agent of wadding a quilt with cotton with fixed attention, be provided with a jet pipe in the tempering tank, be used to inject ozone, described tempering tank connects a circulation type mixing tank, and described mixing tank end is provided with a refluxing opening (51).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202019464U CN201309855Y (en) | 2008-10-17 | 2008-10-17 | Sewage processing device used in ozone contacting oxidation reaction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008202019464U CN201309855Y (en) | 2008-10-17 | 2008-10-17 | Sewage processing device used in ozone contacting oxidation reaction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201309855Y true CN201309855Y (en) | 2009-09-16 |
Family
ID=41107107
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2008202019464U Expired - Lifetime CN201309855Y (en) | 2008-10-17 | 2008-10-17 | Sewage processing device used in ozone contacting oxidation reaction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201309855Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178618A (en) * | 2016-09-09 | 2016-12-07 | 成都九十度工业产品设计有限公司 | A kind of precipitation still for processing Metallurgical Waste Water |
-
2008
- 2008-10-17 CN CNU2008202019464U patent/CN201309855Y/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178618A (en) * | 2016-09-09 | 2016-12-07 | 成都九十度工业产品设计有限公司 | A kind of precipitation still for processing Metallurgical Waste Water |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20090916 |