CN204509007U - A kind of iron-carbon micro-electrolysis-class Fenton experimental installation - Google Patents
A kind of iron-carbon micro-electrolysis-class Fenton experimental installation Download PDFInfo
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- CN204509007U CN204509007U CN201520130858.XU CN201520130858U CN204509007U CN 204509007 U CN204509007 U CN 204509007U CN 201520130858 U CN201520130858 U CN 201520130858U CN 204509007 U CN204509007 U CN 204509007U
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Abstract
The utility model discloses a kind of iron-carbon micro-electrolysis-class Fenton experimental installation, be made up of reactor, pipeline and peristaltic pump, reactor is made up of cylindrical tank and bottom pyramidal end socket, cylindrical tank inside is filled with iron powder and carbon granule, cylindrical tank body sidewall is provided with the first medicament and adds mouth, the second medicament interpolation mouth and waste water injection port, bottom pyramidal end socket is connected with cylindrical tank by flange, between bottom pyramidal end socket and cylindrical tank, screen cloth is installed, prevents iron powder and carbon granule blocking pipe; The bottom of reactor is provided with pipeline, and the other end of pipeline is plugged in cylindrical tank, and pipeline is provided with peristaltic pump, for whole pipeline provides power to be back in reactor by waste water pump.The utility model is to study iron-carbon micro-electrolysis-class Fenton coupling technique to the treatment mechanism of different waste water, probing into the synergy of iron-carbon micro-electrolysis technology and class Fenton technology, simultaneously for follow-up industrial application provides test parameter, theoretical foundation and technical director.
Description
Technical field
The utility model relates to the field such as environmental protection technology and water treating equipment exploitation, and particularly a kind of laboratory needle is to the iron-carbon micro-electrolysis-class Fenton experimental installation of wastewater treatment.
Background technology
China's most area shortage of water resources problem has become the focus that people pay close attention to, and be main path for service water reuse, therefore for the problem be treated as urgently of trade effluent, because trade effluent has following characteristics: high salinity, high COD and colourity belong to the wastewater treatment category of difficult degradation, environmental recovery bonds scholars shortly find, ferric-carbon micro-electrolysis and the Fenton oxidation method oxidisability higher because reagent has, there is the ability of higher removal Persistent organic pollutants, and its technique is simple, the object of " treatment of wastes with processes of wastes against one another " can be reached the while of easy to operate, nearly 20-30 is widely used in trade effluent pre-treatment, deep especially particularly for independent study mechanism, but for the two, whether there is synergy could not further investigate.Therefore people are in the urgent need to a kind of iron-carbon micro-electrolysis for wastewater treatment-class Fenton experimental installation, to study iron-carbon micro-electrolysis-class Fenton coupling technique to the treatment effect of different sewage, simultaneously for follow-up industrial application provides test parameter, theoretical foundation and technical director.After using the utility model experimental installation, under effectively can studying different experimental conditions, iron-carbon micro-electrolysis-class Fenton coupling technique to the disposition of different waste water, simultaneously for follow-up industrial application provides test parameter, theoretical foundation and technical director.
Summary of the invention
The utility model is to study iron-carbon micro-electrolysis-class Fenton coupling technique to the treatment mechanism of different waste water, probe into the synergy of iron-carbon micro-electrolysis technology and class Fenton technology, simultaneously for follow-up industrial application provides test parameter, theoretical foundation and technical director, a kind of simple to operate, reasonable in design, the experimental result provided is reliably for the iron-carbon micro-electrolysis-class Fenton experimental installation of wastewater treatment.
The utility model is made up of reactor, pipeline and peristaltic pump, reactor is made up of cylindrical tank and bottom pyramidal end socket, the material of cylindrical tank is the synthetic glass with acidproof corrosion resistant character, cylindrical tank inside is filled with iron powder and carbon granule, cylindrical tank body sidewall is provided with the first medicament and adds mouth, the second medicament interpolation mouth and waste water injection port, and the first medicament adds mouth, the second medicament adds mouth and waste water injection port is all provided with valve; Bottom pyramidal end socket is connected with cylindrical tank by flange, is provided with screen cloth between bottom pyramidal end socket and cylindrical tank, prevents iron powder and carbon granule blocking pipe; The bottom of reactor is provided with pipeline, and the other end of pipeline is plugged in cylindrical tank, and pipeline is for waste water turnover experimental installation, pipeline is provided with sampling of wastewater mouth, sampling of wastewater mouth is provided with valve, and pipeline is provided with peristaltic pump, for whole pipeline provides power to be back in reactor by waste water pump; Whole experimental installation is supported by angle bar.
The beneficial effects of the utility model:
The utility model is to study iron-carbon micro-electrolysis-class Fenton coupling technique to the treatment mechanism of different waste water, probing into the synergy of iron-carbon micro-electrolysis technology and class Fenton technology, simultaneously for follow-up industrial application provides test parameter, theoretical foundation and technical director.Have and plant the advantages such as simple to operate, reasonable in design, experimental result is reliable, have broad application prospects.
Accompanying drawing explanation
Fig. 1 is Structure and energy schema of the present utility model.
Embodiment
Refer to shown in Fig. 1, the utility model is made up of reactor 1, pipeline 2 and peristaltic pump 3, reactor 1 is made up of cylindrical tank 7 and bottom pyramidal end socket 9, the material of cylindrical tank 7 is the synthetic glass with acidproof corrosion resistant character, cylindrical tank 7 inside is filled with iron powder and carbon granule 6, cylindrical tank 7 sidewall is provided with the first medicament interpolation mouth 11, second medicament interpolation mouth 12 and waste water injection port 4, first medicament adds mouth 11, second medicament interpolation mouth 12 and waste water injection port 4 is all provided with valve; Bottom pyramidal end socket 9 is connected with cylindrical tank 7 by flange 8, is provided with screen cloth 10 between bottom pyramidal end socket 9 and cylindrical tank 7, prevents iron powder and carbon granule 6 blocking pipe 2; The bottom of reactor 1 is provided with pipeline 2, the other end of pipeline 2 is plugged in cylindrical tank 7, pipeline 2 is for waste water turnover experimental installation, pipeline 2 is provided with sampling of wastewater mouth 5, sampling of wastewater mouth 5 is provided with valve, pipeline 2 is provided with peristaltic pump 3, for whole pipeline provides power to be back in reactor 1 by waste water pump; Whole experimental installation is supported by angle bar.
Claims (2)
1. iron-carbon micro-electrolysis-class Fenton experimental installation, it is characterized in that: be by reactor (1), pipeline (2) and peristaltic pump (3) composition, reactor (1) is made up of cylindrical tank (7) and bottom pyramidal end socket (9), cylindrical tank (7) inside is filled with iron powder and carbon granule (6), cylindrical tank (7) sidewall is provided with the first medicament and adds mouth (11), second medicament adds mouth (12) and waste water injection port (4), first medicament adds mouth (11), second medicament adds mouth (12) and waste water injection port (4) is all provided with valve, bottom pyramidal end socket (9) is connected with cylindrical tank (7) by flange (8), is provided with screen cloth (10) between bottom pyramidal end socket (9) and cylindrical tank (7), the bottom of reactor (1) is provided with pipeline (2), the other end of pipeline (2) is plugged in cylindrical tank (7), pipeline (2) is provided with peristaltic pump (3), pipeline (2) is provided with sampling of wastewater mouth (5), and sampling of wastewater mouth (5) is provided with valve.
2. a kind of iron-carbon micro-electrolysis according to claim 1-class Fenton experimental installation, is characterized in that: the material of described cylindrical tank (7) is the synthetic glass with acidproof corrosion resistant character.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130858.XU CN204509007U (en) | 2015-03-07 | 2015-03-07 | A kind of iron-carbon micro-electrolysis-class Fenton experimental installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520130858.XU CN204509007U (en) | 2015-03-07 | 2015-03-07 | A kind of iron-carbon micro-electrolysis-class Fenton experimental installation |
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| Publication Number | Publication Date |
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| CN204509007U true CN204509007U (en) | 2015-07-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520130858.XU Active CN204509007U (en) | 2015-03-07 | 2015-03-07 | A kind of iron-carbon micro-electrolysis-class Fenton experimental installation |
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| CN (1) | CN204509007U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110040901A (en) * | 2019-05-13 | 2019-07-23 | 上海明奥环保科技有限公司 | It is a kind of can sludge reuse light electrolysis/heterogeneous Fenton fluidized-bed process and device |
-
2015
- 2015-03-07 CN CN201520130858.XU patent/CN204509007U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110040901A (en) * | 2019-05-13 | 2019-07-23 | 上海明奥环保科技有限公司 | It is a kind of can sludge reuse light electrolysis/heterogeneous Fenton fluidized-bed process and device |
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