CN203878010U - Aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater - Google Patents
Aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater Download PDFInfo
- Publication number
- CN203878010U CN203878010U CN201420288137.7U CN201420288137U CN203878010U CN 203878010 U CN203878010 U CN 203878010U CN 201420288137 U CN201420288137 U CN 201420288137U CN 203878010 U CN203878010 U CN 203878010U
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- Prior art keywords
- iron
- carbon micro
- treatment device
- communicated
- tubing system
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- Expired - Lifetime
Links
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 26
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 238000005273 aeration Methods 0.000 title claims abstract description 10
- 239000003673 groundwater Substances 0.000 title abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 238000011109 contamination Methods 0.000 claims description 8
- 238000012544 monitoring process Methods 0.000 claims description 4
- 238000005516 engineering process Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 7
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 3
- 238000005067 remediation Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000003895 groundwater pollution Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 230000008569 process Effects 0.000 description 8
- 238000005201 scrubbing Methods 0.000 description 4
- 239000000284 extract Substances 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000005619 thermoelectricity Effects 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model relates to a groundwater pollution remediation technology, and in particular relates to an aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater. The combined treatment device comprises a pipeline system, a water inlet pump, a water outlet pump and a groundwater treatment device, wherein the pipeline system is divided into a pipeline system I and a pipeline system II; the pipeline system I is communicated with the water outlet pump, and the pipeline system II is communicated with the water inlet pump; the water inlet pump and the water outlet pump are communicated with the groundwater treatment device respectively. By adopting the technical scheme, the aeration and iron-carbon micro-electrolysis combined treatment device disclosed by the utility model has the beneficial effects that the combined treatment device has a relatively good removal effect on organic pollutants which are difficult to degrade; compared with other remediation technologies for treating the organic polluted groundwater, the combined treatment device has the characteristics of low cost, no secondary pollution and good treatment effect.
Description
Technical field
The utility model relates to Remedy Technology of Contaminated Groundwater, particularly the aeration of organic contamination underground water and iron-carbon micro-electrolysis combined apparatus.
Background technology
The pollution remediation technology of underground water is an important thermoelectricity problem of the upper water resource pollution control of society now, the reparation problem of the Organic pollutants underground water particularly wherein relating to.
The more technology of research has the processing of extraction out, original position aeration, permeability response wall, in situ chemical oxidation, biology in situ reparation etc. both at home and abroad at present, and many Remedy Technology of Contaminated Groundwaters with unusual effect and corresponding device systems engineerings are there are, but these technology are by the relative merits of self, extract showering technology out as underground water and be used for Organic Contamination of Groundwater reparation mainly by after underground water extraction, adopt sewage disposal technology to process contaminated underground water, have repairing efficiency short, be easy to the advantages such as field actually operating.But its corresponding system is comparatively complicated, and processing cost is higher, is easily subject to secondary pollution, and treatment effect neither be fine.
Summary of the invention
The problem occurring in order to solve prior art, the purpose of this utility model is to provide aeration and the iron-carbon micro-electrolysis combined apparatus of organic polluted underground water, and cost is low to be arranged simply, effective, has avoided secondary pollution.
In order to reach above-mentioned technical purpose, technology contents of the present utility model is:
Comprise tubing system, intake pump, go out water pump and underground water treating device, wherein said tubing system is divided into tubing system one and tubing system two, tubing system one with go out water pump and be communicated with, tubing system two is communicated with intake pump; Described intake pump and go out water pump and be all communicated with described underground water treating device.Described underground water treating device comprises pH regulator pond and iron-carbon micro-electrolysis reactor, between described pH regulator pond and iron-carbon micro-electrolysis reactor, is communicated with pipeline, is provided with transferpump in the middle of described pipeline; Described pH regulator pond with go out water pump and be communicated with, described iron-carbon micro-electrolysis reactor is communicated with intake pump.Described iron-carbon micro-electrolysis reactor bottom is provided with desilting mouth and gas blower.
Further, between described pH regulator pond and iron-carbon micro-electrolysis reactor, be provided with real time monitoring apparatus.
Further, described tubing system one and tubing system two are respectively made up of a fairlead and multiple arm, and described multiple arms are all connected with described fairlead.
Adopt after technique scheme, the beneficial effects of the utility model are: the organic pollutant of difficult degradation is had to good removal effect; Compared with other recovery techniques of administering organic contamination underground water, have that cost is low, non-secondary pollution and a good feature for the treatment of effect.
Brief description of the drawings
In order to further illustrate technology contents of the present utility model, below by specifically embodiment and brief description of the drawings elaborate.
Fig. 1 is overall schematic of the present utility model;
Fig. 2 is pipeline schematic diagram of the present utility model.
In figure, 1 is micro-electrolysis reaction still, and 2 is pH regulator pond, and 3 for going out water pump, and 4 is intake pump, and 5 is real time monitoring apparatus, and 6 is extraction pump, and 7 is desilting mouth, and 8 is gas blower, and 9 is that tubing system one, 10 is that tubing system two, 11 is bypass line.
Embodiment
For detailed explanation the technical solution of the utility model, below by embodiment, the utility model is further explained.
As shown in Figure 1, this device is divided into three, groundwater treatment part, underground water transport portion and tubing system part, three connects by pipeline, tubing system is divided into tubing system 1 and tubing system 2 10, tubing system 1 with go out water pump 3 and be connected, tubing system two is connected with intake pump 4, go out water pump 3 and be connected with groundwater treatment system by pipeline respectively with intake pump 4, underground water is processed.Going out water pump 3 extracts underground water to send into treatment system out, process underground water later from treatment system and pass through again intake pump 4, by tubing system 2 10, underground water after treatment is sent into underground, so circulation, underground water is carried out to continuous pollution processing, relatively simple for structure, and continuous treating processes effectively prevents secondary pollution, and scrubbing effect is better.Treatment system comprises that pH regulator pond 2 and micro-electrolysis reaction still 1 form, going out water pump 3 is connected by pipeline with pH regulator pond 2, underground water is sent in pH regulator pond 2, sent in micro-electrolysis reaction still 1 by extraction pump 6 from pH regulator pond 2 underground water out, reactor 1 underground water after treatment is discharged and is sent in tubing system 2 10 and then enter undergroundly by intake pump 4 again, completes whole circulation.Wherein desilting mouth 7 is arranged at reactor 1 bottom, and gas blower 8, and the sewage in micro-electrolysis reaction still 1 is blasted to air, improves organic evaporation rate.First the contaminated underground water extracting is processed through pH regulator pond 2, process entering in micro-electrolysis reaction still 1 subsequently, finally enter underground by intake pump 4 again, whole process is comparatively reasonable, specific aim and the order processed are stronger, scrubbing process can not be interrupted continuously, and micro-electrolysis reaction still 1 bottom arrange desilting mouth 7 and gas blower 8 pollutent is for further processing, prevent secondary pollution.
Further, as shown in Figure 1, between micro-electrolysis reaction still 1 and pH regulator pond 2, be provided with real time monitoring apparatus 5, two treating processess are monitored in real time, maneuvering ability is better, can after going wrong, feed back in time, has ensured the stability of whole device scrubbing process.
Further, as shown in Figure 2, tubing system 1 and tubing system 2 10 are made up of a house steward and multiple arm 11 respectively, and multiple arms 11 are all connected with house steward, are evenly distributed on house steward.In the process that groundwater abstraction and underground water are sent into, multiple equally distributed arms 11 can extract and send into the contaminated underground water of nearly all position of underground water, in whole process, effectively prevent that scrubbing blind area from appearring in underground water, there will not be the underground water in partial area to can not get polluting processing, improved the comprehensive of organic contamination processing, processing efficiency is higher.
Claims (3)
1. the aeration of organic contamination underground water and iron-carbon micro-electrolysis combined apparatus, comprise tubing system, intake pump, go out water pump and underground water treating device, it is characterized in that: described tubing system is divided into tubing system one and tubing system two, tubing system one with go out water pump and be communicated with, tubing system two is communicated with intake pump; Described intake pump and go out water pump and be all communicated with described underground water treating device; Described underground water treating device comprises pH regulator pond and iron-carbon micro-electrolysis reactor, between described pH regulator pond and iron-carbon micro-electrolysis reactor, is communicated with pipeline, is provided with transferpump in the middle of described pipeline; Described pH regulator pond with go out water pump and be communicated with, described iron-carbon micro-electrolysis reactor is communicated with intake pump; Described iron-carbon micro-electrolysis reactor bottom is provided with desilting mouth and gas blower.
2. the aeration of organic contamination underground water according to claim 1 and iron-carbon micro-electrolysis combined apparatus, is characterized in that: between described pH regulator pond and iron-carbon micro-electrolysis reactor, be provided with real time monitoring apparatus.
3. the aeration of organic contamination underground water according to claim 1 and iron-carbon micro-electrolysis combined apparatus, it is characterized in that: described tubing system one and tubing system two are respectively made up of a fairlead and multiple arm, described multiple arms are all connected with described fairlead.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420288137.7U CN203878010U (en) | 2014-05-30 | 2014-05-30 | Aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420288137.7U CN203878010U (en) | 2014-05-30 | 2014-05-30 | Aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203878010U true CN203878010U (en) | 2014-10-15 |
Family
ID=51678534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420288137.7U Expired - Lifetime CN203878010U (en) | 2014-05-30 | 2014-05-30 | Aeration and iron-carbon micro-electrolysis combined treatment device of organic polluted groundwater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203878010U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108002606A (en) * | 2017-12-26 | 2018-05-08 | 广州桑尼环保科技有限公司 | Household garbage-compressing waste water treatment system and method |
-
2014
- 2014-05-30 CN CN201420288137.7U patent/CN203878010U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108002606A (en) * | 2017-12-26 | 2018-05-08 | 广州桑尼环保科技有限公司 | Household garbage-compressing waste water treatment system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160905 Address after: 213000 No. 2188 Longcheng Road, bell tower area, Jiangsu, Changzhou Patentee after: SUNTIME ENVIRONMENTAL REMEDIATION CO., LTD. Address before: 3, building 9, Dongjiang green building, No. 301, Lang long road, Nanshan District, Guangdong, Shenzhen 518057, China Patentee before: GUANGDONG DONGJIANG SHANGTIAN ENVIRONMENTAL REMEDIATION CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 213000 2188 Longcheng Road, Zhong Lou District, Changzhou, Jiangsu Patentee after: Shanda Environmental Restoration Co., Ltd. Address before: 213000 2188 Longcheng Road, Zhong Lou District, Changzhou, Jiangsu Patentee before: SUNTIME ENVIRONMENTAL REMEDIATION CO., LTD. |