CN205367953U - Oily sewage rapidly transacting device - Google Patents
Oily sewage rapidly transacting device Download PDFInfo
- Publication number
- CN205367953U CN205367953U CN201521082941.0U CN201521082941U CN205367953U CN 205367953 U CN205367953 U CN 205367953U CN 201521082941 U CN201521082941 U CN 201521082941U CN 205367953 U CN205367953 U CN 205367953U
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- Prior art keywords
- outlet
- flocculation
- basin
- import
- plate clarifying
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- 239000010865 sewage Substances 0.000 title abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000005189 flocculation Methods 0.000 claims abstract description 28
- 230000016615 flocculation Effects 0.000 claims abstract description 28
- 230000001112 coagulating effect Effects 0.000 claims abstract description 26
- 230000015556 catabolic process Effects 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- 239000000839 emulsion Substances 0.000 claims abstract description 18
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 10
- 230000008676 import Effects 0.000 claims description 18
- 238000007667 floating Methods 0.000 claims description 11
- 239000000701 coagulant Substances 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000001556 precipitation Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000002000 scavenging effect Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000002253 acid Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004899 motility Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses an oily sewage rapidly transacting device according to oily sewage's characteristics, through setting gradually breakdown of emulsion reaction tank, flocculation coagulating basin, inclined lamellar precipitation pond, high pressure solution gas pitcher, air supporting device and ultrafiltration device, carries out water oil separating, mixes progressively that congeal and flocculation, solid -liquid separation, pressure dissolve gas air supporting purification treatment, the ultrafiltration is handled to oily sewage, the final oily sewage that realizes handles betterly, for prior art, the utility model has the advantages of with low costs, the processing speed is fast, the treatment effect good, convenient to use, mobilizable oily water treatment device, can remove in the place of difference and use.
Description
Technical field
This utility model relates to technical field of sewage, is specifically related to a kind of oil-polluted water quick treatment device.
Background technology
The scavenging effect that prior art processes oil-polluted water is poor, it usually needs can be only achieved good scavenging effect with follow-up biochemical system in conjunction with use, relatively costly, and motility is also strong, and the less enterprise of the water yield is difficult to set up new biochemical system.
Utility model content
For the deficiencies in the prior art, this utility model aims to provide a kind of oil-polluted water quick treatment device,, processing speed low by cost is fast, high treating effect, easy to use in the way of realize being separated from water by oil preferably, and after flocculating sedimentation solid-liquid separation, it is ensured that water outlet reaches the discharge standard of requirement.
To achieve these goals, this utility model adopts the following technical scheme that
A kind of oil-polluted water quick treatment device, including the breakdown of emulsion reaction tank for adding demulsifier, its import is by a pump connection oil-polluted water pipe, and the import of outlet then connection flocculation coagulating basin, described flocculation coagulating basin is used for dosing coagulant and flocculant；The outlet of described flocculation coagulating basin is in the import of inclined-plate clarifying basin, and the outlet of inclined-plate clarifying basin is then communicated in the import of high pressure dissolving by another pump；The outlet of described high pressure dissolving is in the import of air-floating apparatus, and the outlet of described air-floating apparatus is then communicated in the import of ultrafiltration apparatus；The outlet of described ultrafiltration apparatus is in outlet pipe.
As preferably, described breakdown of emulsion reaction tank and flocculation coagulating basin are also each configured with blender, and the head of described blender is positioned at its corresponding breakdown of emulsion reaction tank or flocculation coagulating basin.By stirring, it is possible to make the reaction in breakdown of emulsion reaction tank and flocculation coagulating basin more fully with effective.
As preferably, the inlet and outlet of described inclined-plate clarifying basin lays respectively at the both sides of described inclined-plate clarifying basin, and includes upper inlet and lower inlet, upper outlet and lower outlet respectively；The outlet of described flocculation coagulating basin is in a pipeline, and the upper inlet of described inclined-plate clarifying basin and lower inlet are communicated in described pipeline respectively through valve；The inlet communication of another pump described is in a body, and the upper outlet of described inclined-plate clarifying basin and lower outlet are communicated in described body respectively through valve, thus being communicated in described high pressure dissolving.Through the flocculation in flocculation coagulating basin and coagulating treatment, it is contemplated that the proportion of the dregs of fat, different types of oily waste water alumen ustum floats or sinks, so the turnover moisture upper entering and lower leaving of inclined-plate clarifying basin and bottom in and top out two kinds, convenient on-the-spot concrete operations.
The beneficial effects of the utility model are in that: this utility model feature according to oil-polluted water, by setting gradually breakdown of emulsion reaction tank, flocculation coagulating basin, inclined-plate clarifying basin, high pressure dissolving, air-floating apparatus and ultrafiltration apparatus, progressively oil-polluted water is carried out oil-water separation, coagulation and flocculation treatment, solid-liquid separation, pressure air-dissolving air-float purified treatment, hyperfiltration treatment, finally realize oily waste water treatment preferably, relative to prior art, it is low that this utility model has cost, processing speed is fast, high treating effect, advantage easy to use, it it is moveable oil-contained waste water treatment device, use can be moved in different places.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below with reference to accompanying drawing, the utility model will be further described, it is necessary to explanation, and the present embodiment, premised on the technical program, gives detailed embodiment and concrete operating process, but protection domain of the present utility model is not limited to the present embodiment.
As shown in Figure 1, a kind of oil-polluted water quick treatment device, including the breakdown of emulsion reaction tank 1 for adding demulsifier, its import connects oil-polluted water pipe 3 by a pump 2, the import of outlet then connection flocculation coagulating basin 4, described flocculation coagulating basin 4 is for dosing coagulant and flocculant；The outlet of described flocculation coagulating basin 4 is in the import of inclined-plate clarifying basin 5, and the outlet of inclined-plate clarifying basin 5 is then communicated in the import of high pressure dissolving 7 by another pump 6；The outlet of described high pressure dissolving 7 is in the import of air-floating apparatus 8, and the outlet of described air-floating apparatus 8 is then communicated in the import of ultrafiltration apparatus 9；The outlet of described ultrafiltration apparatus 9 is in outlet pipe 10.
As preferably, described breakdown of emulsion reaction tank 1 and flocculation coagulating basin 4 are also each configured with blender 11, and the head of described blender 11 is positioned at its corresponding breakdown of emulsion reaction tank 1 or flocculation coagulating basin 4.By stirring, it is possible to make the reaction in breakdown of emulsion reaction tank and flocculation coagulating basin more fully with effective.
As preferably, the inlet and outlet of described inclined-plate clarifying basin 5 lays respectively at the both sides of described inclined-plate clarifying basin 5, and includes upper inlet and lower inlet, upper outlet and lower outlet respectively；The outlet of described flocculation coagulating basin 4 is in a pipeline 12, and the upper inlet of described inclined-plate clarifying basin 5 and lower inlet are communicated in described pipeline 12 respectively through valve 13；The inlet communication of another pump 6 described is in a body 14, and the upper outlet of described inclined-plate clarifying basin 5 and lower outlet are communicated in described body 14 respectively through valve 13, thus being communicated in described high pressure dissolving 7.
During use, oil-polluted water first passes through pump and enters described breakdown of emulsion reaction tank from oil-polluted water pipe, is reached the purpose of oil-water separation when the pH required by the demulsifier effect in breakdown of emulsion reaction tank, changes traditional strong acid or conventional dose breakdown of emulsion, make operation safer and simpler, better processing effect.In breakdown of emulsion process, the mixture in breakdown of emulsion reaction tank can be stirred by blender so that reacts more abundant.In breakdown of emulsion reaction tank, reactant flows automatically to flocculation coagulating basin, under the effect of blender, oil droplet cohesion is formed big alumen ustum；Flocculation coagulating basin waste water out flows automatically to inclined-plate clarifying basin and carries out solid-liquid separation, consider the proportion of the dregs of fat, different types of oily waste water alumen ustum floats or sinks, so the turnover moisture upper entering and lower leaving of inclined-plate clarifying basin and bottom in and top out two kinds, convenient on-the-spot concrete operations.Inclined-plate clarifying basin water out is extracted into high pressure dissolving by pump and is pressurized to a certain degree, also can add compression air in high pressure dissolving simultaneously, and air is dissolved in pressurized water；Dissolved air water after pressurization enters in air-floating apparatus, and dissolved air water reduces to normal pressure suddenly, and the air being dissolved in water precipitates out from water with micro-bubble form, is carried by the suspended particle in water and bubbles through the water column, the Slag Scraping Device in air-floating apparatus scrapes, thus realizing solid-liquid separation.After being processed by air-floating apparatus, water body is further improved, and the water outlet of air-floating apparatus carries out qualified discharge or reuse after advanced treating again through ultrafiltration apparatus.
For a person skilled in the art, it is possible to according to above technical scheme and design, make various corresponding change and deformation, and all these changes and deformation should be construed as being included within this utility model scope of the claims.
Claims (3)
1. an oil-polluted water quick treatment device, it is characterized in that, including the breakdown of emulsion reaction tank for adding demulsifier, its import is by a pump connection oil-polluted water pipe, the import of outlet then connection flocculation coagulating basin, described flocculation coagulating basin is used for dosing coagulant and flocculant；The outlet of described flocculation coagulating basin is in the import of inclined-plate clarifying basin, and the outlet of inclined-plate clarifying basin is then communicated in the import of high pressure dissolving by another pump；The outlet of described high pressure dissolving is in the import of air-floating apparatus, and the outlet of described air-floating apparatus is then communicated in the import of ultrafiltration apparatus；The outlet of described ultrafiltration apparatus is in outlet pipe.
2. oil-polluted water quick treatment device according to claim 1, it is characterised in that described breakdown of emulsion reaction tank and flocculation coagulating basin are also each configured with blender, the head of described blender is positioned at its corresponding breakdown of emulsion reaction tank or flocculation coagulating basin.
3. oil-polluted water quick treatment device according to claim 1, it is characterised in that the inlet and outlet of described inclined-plate clarifying basin lays respectively at the both sides of described inclined-plate clarifying basin, and includes upper inlet and lower inlet, upper outlet and lower outlet respectively；The outlet of described flocculation coagulating basin is in a pipeline, and the upper inlet of described inclined-plate clarifying basin and lower inlet are communicated in described pipeline respectively through valve；The inlet communication of another pump described is in a body, and the upper outlet of described inclined-plate clarifying basin and lower outlet are communicated in described body respectively through valve, thus being communicated in described high pressure dissolving.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521082941.0U CN205367953U (en) | 2015-12-21 | 2015-12-21 | Oily sewage rapidly transacting device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521082941.0U CN205367953U (en) | 2015-12-21 | 2015-12-21 | Oily sewage rapidly transacting device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205367953U true CN205367953U (en) | 2016-07-06 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521082941.0U Active CN205367953U (en) | 2015-12-21 | 2015-12-21 | Oily sewage rapidly transacting device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205367953U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082383A (en) * | 2016-08-17 | 2016-11-09 | 湘潭辉昇环保设备制造有限公司 | Multi-functional sewage dissolved air flotation purifier |
| CN111348778A (en) * | 2020-03-26 | 2020-06-30 | 渠计虎 | Port oil spilling sewage treatment structure and treatment method thereof |
| CN114702150A (en) * | 2022-03-30 | 2022-07-05 | 乾通环境科技(苏州)有限公司 | Pretreatment system for high-turbidity oil-containing seawater for small and medium-sized seawater desalination plants |
-
2015
- 2015-12-21 CN CN201521082941.0U patent/CN205367953U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082383A (en) * | 2016-08-17 | 2016-11-09 | 湘潭辉昇环保设备制造有限公司 | Multi-functional sewage dissolved air flotation purifier |
| CN111348778A (en) * | 2020-03-26 | 2020-06-30 | 渠计虎 | Port oil spilling sewage treatment structure and treatment method thereof |
| CN111348778B (en) * | 2020-03-26 | 2022-04-29 | 大庆瑞赛克环保科技有限公司 | Port oil spilling sewage treatment structure and treatment method thereof |
| CN114702150A (en) * | 2022-03-30 | 2022-07-05 | 乾通环境科技(苏州)有限公司 | Pretreatment system for high-turbidity oil-containing seawater for small and medium-sized seawater desalination plants |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |