CN204779146U - Contact oxidation tank device - Google Patents
Contact oxidation tank device Download PDFInfo
- Publication number
- CN204779146U CN204779146U CN201520328141.6U CN201520328141U CN204779146U CN 204779146 U CN204779146 U CN 204779146U CN 201520328141 U CN201520328141 U CN 201520328141U CN 204779146 U CN204779146 U CN 204779146U
- Authority
- CN
- China
- Prior art keywords
- contact
- oxidation pool
- grid
- activated carbon
- adsorption layer
- Prior art date
- 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
Links
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 65
- 230000003647 oxidation Effects 0.000 title claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
The utility model provides a contact oxidation tank device, contact oxidation tank body upper portion one side is equipped with the water inlet, contact oxidation tank body bottom is equipped with the delivery port, the level filtering grid, the second grade filters the grid and activated carbon adsorption layer all establishes in contact oxidation tank body bottom, the device setting is put in in contact oxidation tank body both sides to the oxidation medicine, be provided with agitating unit between contact oxidation tank body and level filtering grid, agitating unit includes agitator motor, stirring head and lift puddler, agitator motor links to each other with lift puddler one end, the stirring head links to each other with the lift puddler other end, the delivery port links to each other with the drain line, be provided with the drain pump on the drain line. The beneficial effects of the utility model are that can not only take place the catalytic oxidation reaction can also deposit or can be got rid of in the lump by absorbent impurity producing among the reaction sequence.
Description
Technical field
The utility model relates to technical field of sewage treatment equipment, more particularly, relates to a kind of catalytic oxidation pool device.
Background technology
Sewage disposal (sewagetreatment, wastewatertreatment): the process reaching a certain water body of draining or the water quality requirement that reuses for making sewage it is purified.Sewage disposal is widely used in building, agricultural, and the every field such as traffic, the energy, petrochemical industry, environmental protection, urban look, medical treatment, food and drink, also come into the daily life of common people more and more.
In recent years; the most important thing of city domestic sewage discharge to be the primary pollution source city domestic sewage process of Chinese city water be urban water conservation at present and in the future and treatment work; this just requires that we will grab the construction of process sanitary sewage facility as the important content of urban infrastructure, and is too impatient to wait thing.
Utility model content
The utility model overcomes deficiency of the prior art, existing contact-oxidation pool can only come in contact oxidizing reaction, can not throw out simultaneously in filtering waste water, provide a kind of catalytic oxidation pool device, can not only come in contact oxidizing reaction can also will produce precipitation or can be removed in the lump by the impurity adsorbed in reaction process.
The purpose of this utility model is achieved by following technical proposals.
A kind of catalytic oxidation pool device, comprise contact-oxidation pool body, single filter grid, cascade filtration grid, activated carbon adsorption layer and oxidative drug throwing device, described contact-oxidation pool body upper part side is provided with water-in, described contact-oxidation pool body bottom portion mid-way is provided with water outlet, described single filter grid is arranged on described contact-oxidation pool body bottom portion, the quantity of described single filter grid is two, described cascade filtration grid is arranged on described contact-oxidation pool body bottom portion, described cascade filtration grid is arranged on inside described single filter grid, the quantity of described cascade filtration grid is two, described activated carbon adsorption layer is also arranged on described contact-oxidation pool body bottom portion, described activated carbon adsorption layer is arranged on inside described cascade filtration grid, the quantity of described activated carbon adsorption layer is four, and described activated carbon adsorption layer is symmetrical arranged between two, described oxidative drug throwing device is arranged on described contact-oxidation pool body both sides, whipping appts is provided with between described contact-oxidation pool body and described single filter grid, described whipping appts comprises agitator motor, stirring-head and lifting agitator arm, described agitator motor is connected with described lifting agitator arm one end, described stirring-head is connected with the described lifting agitator arm the other end, described water outlet is connected with discharge pipe line, described discharge pipe line is provided with wet-pit.
The height of described single filter grid, described cascade filtration grid and described activated carbon adsorption layer is more than or equal to the degree of depth of described contact-oxidation pool body.
The pore size filter of described single filter grid is 50-100mm, and the pore size filter of described cascade filtration grid is 10-50mm.
Described contact-oxidation pool both sides are provided with aerating pipelines, described aerating pipelines is provided with aeration devices, described aeration devices comprises aeration head and aeration pipe connecting, described aeration head adopts cross section to be semicircular structure, be provided with aeration spout uniformly at described aeration head top, be connected with described aeration pipe connecting bottom described aeration head.
The beneficial effects of the utility model are: compared with prior art, the utility model is provided with single filter grid, cascade filtration grid and activated carbon adsorption layer, bulk pollutent in sewage can be filtered by two-stage filtration and remove, activated carbon adsorption layer can by can by the fritter pollutent that adsorbs and other impurity absorption clean; Contact-oxidation pool body both sides are provided with oxidative drug throwing device, and make this device can not only can also carry out contact oxidation, the setting of aerating pipelines by impurity screening, the oxygen needed for contact oxidation provides condition simultaneously; The setting of whipping appts, makes catalytic oxidation medicine to react by the material fully and in sewage, also can ensure the oxygen content in sewage simultaneously; Water outlet is arranged on and is positioned at the inner most activated carbon adsorption layer bottom of contact-oxidation pool body, ensure the sewage of discharging contact-oxidation pool body, through the sewage of two-layer filtration, charcoal absorption and catalytic oxidation, for follow-up sewage disposal, save the time of process, improve the efficiency of sewage disposal.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present utility model;
Fig. 2 is the structural representation of aerating pipelines in the utility model.
In figure: 1 is contact-oxidation pool body, 2 is single filter grid, and 3 is cascade filtration grid, 4 is activated carbon adsorption layer, and 5 is oxidative drug throwing device, and 6 is water-in, 7 is water outlet, 8 is agitator motor, and 9 is stirring-head, and 10 is lifting agitator arm, 11 is wet-pit, 12 is aerating pipelines, and 13 is aeration head, and 14 is aeration pipe connecting.
Embodiment
Below by specific embodiment, the technical solution of the utility model is further described.
As depicted in figs. 1 and 2, wherein, 1 is contact-oxidation pool body, 2 is single filter grid, and 3 is cascade filtration grid, and 4 is activated carbon adsorption layer, 5 is oxidative drug throwing device, and 6 is water-in, and 7 is water outlet, 8 is agitator motor, and 9 is stirring-head, and 10 is lifting agitator arm, 11 is wet-pit, 12 is aerating pipelines, and 13 is aeration head, and 14 is aeration pipe connecting.
A kind of catalytic oxidation pool device, comprise contact-oxidation pool body, single filter grid, cascade filtration grid, activated carbon adsorption layer and oxidative drug throwing device, contact-oxidation pool body upper part side is provided with water-in, mid-way is provided with water outlet to contact-oxidation pool body bottom portion, single filter grid is arranged on contact-oxidation pool body bottom portion, the quantity of single filter grid is two, cascade filtration grid is arranged on contact-oxidation pool body bottom portion, cascade filtration grid is arranged on inside single filter grid, the quantity of cascade filtration grid is two, activated carbon adsorption layer is also arranged on contact-oxidation pool body bottom portion, activated carbon adsorption layer is arranged on inside cascade filtration grid, the quantity of activated carbon adsorption layer is four, and activated carbon adsorption layer is symmetrical arranged between two, oxidative drug throwing device is arranged on contact-oxidation pool body both sides, whipping appts is provided with between contact-oxidation pool body and single filter grid, whipping appts comprises agitator motor, stirring-head and lifting agitator arm, agitator motor is connected with lifting agitator arm one end, stirring-head is connected with the lifting agitator arm the other end, water outlet is connected with discharge pipe line, discharge pipe line is provided with wet-pit.
The height of single filter grid, cascade filtration grid and activated carbon adsorption layer is more than or equal to the degree of depth of contact-oxidation pool body.
The pore size filter of single filter grid is 50-100mm, and the pore size filter of cascade filtration grid is 10-50mm.
Contact-oxidation pool both sides are provided with aerating pipelines, aerating pipelines is provided with aeration devices, aeration devices comprises aeration head and aeration pipe connecting, aeration head adopts cross section to be semicircular structure, be provided with aeration spout uniformly at aeration head top, be connected with aeration pipe connecting bottom aeration head.
Compared with prior art, the present embodiment is provided with single filter grid, cascade filtration grid and activated carbon adsorption layer, bulk pollutent in sewage can be filtered by two-stage filtration and remove, activated carbon adsorption layer can by can by the fritter pollutent that adsorbs and other impurity absorption clean; Contact-oxidation pool body both sides are provided with oxidative drug throwing device, and make this device can not only can also carry out contact oxidation, the setting of aerating pipelines by impurity screening, the oxygen needed for contact oxidation provides condition simultaneously; The setting of whipping appts, makes catalytic oxidation medicine to react by the material fully and in sewage, also can ensure the oxygen content in sewage simultaneously; Water outlet is arranged on and is positioned at the inner most activated carbon adsorption layer bottom of contact-oxidation pool body, ensure the sewage of discharging contact-oxidation pool body, through the sewage of two-layer filtration, charcoal absorption and catalytic oxidation, for follow-up sewage disposal, save the time of process, improve the efficiency of sewage disposal.
Above the utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.
Claims (4)
1. a catalytic oxidation pool device, it is characterized in that: comprise contact-oxidation pool body, single filter grid, cascade filtration grid, activated carbon adsorption layer and oxidative drug throwing device, described contact-oxidation pool body upper part side is provided with water-in, described contact-oxidation pool body bottom portion mid-way is provided with water outlet, described single filter grid is arranged on described contact-oxidation pool body bottom portion, the quantity of described single filter grid is two, described cascade filtration grid is arranged on described contact-oxidation pool body bottom portion, described cascade filtration grid is arranged on inside described single filter grid, the quantity of described cascade filtration grid is two, described activated carbon adsorption layer is also arranged on described contact-oxidation pool body bottom portion, described activated carbon adsorption layer is arranged on inside described cascade filtration grid, the quantity of described activated carbon adsorption layer is four, and described activated carbon adsorption layer is symmetrical arranged between two, described oxidative drug throwing device is arranged on described contact-oxidation pool body both sides, whipping appts is provided with between described contact-oxidation pool body and described single filter grid, described whipping appts comprises agitator motor, stirring-head and lifting agitator arm, described agitator motor is connected with described lifting agitator arm one end, described stirring-head is connected with the described lifting agitator arm the other end, described water outlet is connected with discharge pipe line, described discharge pipe line is provided with wet-pit.
2. a kind of catalytic oxidation pool device according to claim 1, is characterized in that: the height of described single filter grid, described cascade filtration grid and described activated carbon adsorption layer is more than or equal to the degree of depth of described contact-oxidation pool body.
3. a kind of catalytic oxidation pool device according to claim 1, is characterized in that: the pore size filter of described single filter grid is 50-100mm, and the pore size filter of described cascade filtration grid is 10-50mm.
4. a kind of catalytic oxidation pool device according to claim 1, it is characterized in that: described contact-oxidation pool both sides are provided with aerating pipelines, described aerating pipelines is provided with aeration devices, described aeration devices comprises aeration head and aeration pipe connecting, described aeration head adopts cross section to be semicircular structure, be provided with aeration spout uniformly at described aeration head top, be connected with described aeration pipe connecting bottom described aeration head.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520328141.6U CN204779146U (en) | 2015-05-20 | 2015-05-20 | Contact oxidation tank device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520328141.6U CN204779146U (en) | 2015-05-20 | 2015-05-20 | Contact oxidation tank device |
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| CN204779146U true CN204779146U (en) | 2015-11-18 |
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| CN201520328141.6U Expired - Fee Related CN204779146U (en) | 2015-05-20 | 2015-05-20 | Contact oxidation tank device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467213A (en) * | 2018-11-13 | 2019-03-15 | 佛山市雅洁源科技股份有限公司 | A kind of emulsifying liquid waste water processing equipment and its treatment process |
-
2015
- 2015-05-20 CN CN201520328141.6U patent/CN204779146U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467213A (en) * | 2018-11-13 | 2019-03-15 | 佛山市雅洁源科技股份有限公司 | A kind of emulsifying liquid waste water processing equipment and its treatment process |
| CN109467213B (en) * | 2018-11-13 | 2021-10-26 | 佛山市雅洁源科技股份有限公司 | Emulsion wastewater treatment equipment and treatment process thereof |
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