CN203319793U - Novel sewage purifier - Google Patents
Novel sewage purifier Download PDFInfo
- Publication number
- CN203319793U CN203319793U CN2013203289832U CN201320328983U CN203319793U CN 203319793 U CN203319793 U CN 203319793U CN 2013203289832 U CN2013203289832 U CN 2013203289832U CN 201320328983 U CN201320328983 U CN 201320328983U CN 203319793 U CN203319793 U CN 203319793U
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- CN
- China
- Prior art keywords
- water
- active carbon
- novel sewage
- catalytic ozonation
- carbon adsorber
- 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.)
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- 239000010865 sewage Substances 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 24
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 24
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 18
- 239000000126 substance Substances 0.000 claims abstract description 5
- 230000003197 catalytic effect Effects 0.000 claims description 21
- 238000006385 ozonation reaction Methods 0.000 claims description 21
- 238000005189 flocculation Methods 0.000 claims description 11
- 230000016615 flocculation Effects 0.000 claims description 11
- 238000001556 precipitation Methods 0.000 claims description 11
- 230000000694 effects Effects 0.000 abstract description 3
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 239000006096 absorbing agent Substances 0.000 abstract 1
- 230000003311 flocculating effect Effects 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 7
- 238000007599 discharging Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
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- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a novel sewage purifier, comprising a water inlet and a water outlet, wherein the water inlet is communicated with a chemical feed pipe; and a flocculating oil separation tank, an ultra-filtration filter, and an active carbon absorber are sequentially arranged between the water inlet and the water outlet. The novel sewage purifier disclosed by the utility model has good on-site wastewater treatment effect and is convenient to move; and pollution to surrounding water is effectively reduced.
Description
Technical field
The utility model relates to technical field of waste water processing, especially relates to a kind of Novel sewage treating plant.
Background technology
Oil field can produce a large amount of sewage in exploration and performance history, and its impact on environment and human health, more and more cause people's common concern.The well site of oil field operation property has determined that the wastewater flow rate of its generation is little, the characteristics of dispersion and discontinuity, and well site waste water can not be administered in time thoroughly, causes the well site surrounding enviroment poor, seriously polluted.Therefore, reasonably dispose these distributing well site waste water and become the important procedure of polluting control in oilfield development process.Because the kind of waste water produced in oilfield development process is more, centralized collection is disposed mixing water quality and can be caused handling procedure complicated.The pollutant emission point of take is processed on the spot as unit adopts mobile sewage treatment apparatus to carry out pollutent, and setting up distributing well site Sewage treatment systems is that the important channel of controlling is polluted in current oil field with polluting master mode.
Summary of the invention
Technical problem to be solved in the utility model is: a kind of Novel sewage treating plant is provided, and site disposal waste water is effective, and conveniently moving has effectively reduced the pollution to peripheral water body.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of Novel sewage treating plant, comprise water-in and water port, described water-in is communicated with chemical feed pipe, is sequentially set with successively flocculation oil partiting precipitation pool, ultra filtration filter and active carbon adsorber between described water-in and water port.
Preferably, be provided with one-level catalytic ozonation device between described ultra filtration filter and active carbon adsorber.
Preferably, be provided with secondary catalytic ozonation device between described active carbon adsorber and one-level catalytic ozonation device.
Preferably, described flocculation oil partiting precipitation pool, ultra filtration filter, active carbon adsorber, one-level catalytic ozonation device and secondary catalytic ozonation device all are set to one.
Adopted technique scheme, the beneficial effects of the utility model are: owing to being sequentially set with successively flocculation oil partiting precipitation pool, ultra filtration filter and active carbon adsorber between the water-in of Novel sewage treating plant and water port, by flocculation oil partiting precipitation pool and ultra filtration filter, waste water is carried out to pre-treatment, active carbon adsorber is as subsequent disposal, select the core processing part according to COD concentration difference: as COD<1000mg/L, adopt active carbon adsorber (dosing), ultra filtration filter and active carbon adsorber; During at 1000～2000mg/L, adopt active carbon adsorber (dosing), ultra filtration filter, one-level catalytic ozonation device and active carbon adsorber as COD; During at 2000～4000mg/L, adopt active carbon adsorber (dosing), ultra filtration filter, one-level catalytic ozonation device, secondary catalytic ozonation device and active carbon adsorber as COD.The utility model adopts the integrated type structure, can move flexibly, processes on the spot, and water quality reaches national sewage comprehensive discharge secondary standard.The utility model has improved the human settlement of place and well site periphery greatly, has reduced the pollution to receiving water body around place.
The accompanying drawing explanation
Structural representation when Fig. 1 is the utility model COD<1000mg/L;
Fig. 2 is the utility model COD structural representation when 1000～2000mg/L;
Fig. 3 is the utility model COD structural representation when 2000～4000mg/L;
Wherein: 1, water-in; 2, water port; 3, chemical feed pipe; 4, flocculation oil partiting precipitation pool; 5, ultra filtration filter; 6, active carbon adsorber; 7, one-level catalytic ozonation device; 8, secondary catalytic ozonation device.
Embodiment
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Embodiment mono-:
As shown in Figure 1, this Novel sewage treating plant, comprise water-in 1 and water port 2, water-in 1 is communicated with chemical feed pipe 3, be sequentially set with successively flocculation oil partiting precipitation pool 4, ultra filtration filter 5 and active carbon adsorber 6 between water-in 1 and water port 2, this Novel sewage treating plant can use when COD<1000mg/L, waste water is successively through flocculation oil partiting precipitation pool 4, ultra filtration filter 5 and active carbon adsorber 6, the water of discharging from water port 2 can reach emission standard, has good water treatment effect.
Embodiment bis-:
As shown in Figure 2, as COD during at 1000～2000mg/L, on the basis of embodiment mono-structure, set up one-level catalytic ozonation device 7 between ultra filtration filter 5 and active carbon adsorber 6, waste water is successively through flocculation oil partiting precipitation pool 4, ultra filtration filter 5, one-level catalytic ozonation device 7 and active carbon adsorber 6, and the water of discharging from water port 2 can reach emission standard.
Embodiment tri-:
As shown in Figure 3, as COD during at 2000～4000mg/L, on the basis of embodiment bis-structures, set up secondary catalytic ozonation device 8 between active carbon adsorber 6 and one-level catalytic ozonation device 7, waste water is successively through flocculation oil partiting precipitation pool 4, ultra filtration filter 5, one-level catalytic ozonation device 7, secondary catalytic ozonation device 8 and active carbon adsorber 6, and the water of discharging from water port 2 can reach emission standard.
This Novel sewage treating plant is the organic wastewater with medium-low concentration extensively existed for oil field, research and design mobile oil field wastewater treatment integrated equipment, equipment has flexible movement, processes the characteristics such as convenient.The site disposal effect is good, and water quality treatment reaches national sewage comprehensive discharge secondary standard.The project achievement in research has been improved the human settlement of place and well site periphery greatly, has reduced the pollution to receiving water body around place.
Claims (4)
1. a Novel sewage treating plant, comprise water-in (1) and water port (2), described water-in (1) is communicated with chemical feed pipe (3), it is characterized in that, be sequentially set with successively flocculation oil partiting precipitation pool (4), ultra filtration filter (5) and active carbon adsorber (6) between described water-in (1) and water port (2).
2. Novel sewage treating plant as claimed in claim 1, is characterized in that, between described ultra filtration filter (5) and active carbon adsorber (6), is provided with one-level catalytic ozonation device (7).
3. Novel sewage treating plant as claimed in claim 2, is characterized in that, between described active carbon adsorber (6) and one-level catalytic ozonation device (7), is provided with secondary catalytic ozonation device (8).
4. Novel sewage treating plant as claimed in claim 3, it is characterized in that, described flocculation oil partiting precipitation pool (4), ultra filtration filter (5), active carbon adsorber (6), one-level catalytic ozonation device (7) and secondary catalytic ozonation device (8) all are set to one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203289832U CN203319793U (en) | 2013-05-23 | 2013-05-23 | Novel sewage purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203289832U CN203319793U (en) | 2013-05-23 | 2013-05-23 | Novel sewage purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203319793U true CN203319793U (en) | 2013-12-04 |
Family
ID=49659162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013203289832U Expired - Fee Related CN203319793U (en) | 2013-05-23 | 2013-05-23 | Novel sewage purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203319793U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106477761A (en) * | 2015-08-31 | 2017-03-08 | 宜兴市昌吉利化工有限公司 | The method processing the Organic substance in high slat-containing wastewater using ozone, activated carbon combined apparatus |
-
2013
- 2013-05-23 CN CN2013203289832U patent/CN203319793U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106477761A (en) * | 2015-08-31 | 2017-03-08 | 宜兴市昌吉利化工有限公司 | The method processing the Organic substance in high slat-containing wastewater using ozone, activated carbon combined apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131204 Termination date: 20140523 |