CN201890794U - Novel high-efficiency physicochemical water treatment settling tank device - Google Patents
Novel high-efficiency physicochemical water treatment settling tank device Download PDFInfo
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- CN201890794U CN201890794U CN2010205964405U CN201020596440U CN201890794U CN 201890794 U CN201890794 U CN 201890794U CN 2010205964405 U CN2010205964405 U CN 2010205964405U CN 201020596440 U CN201020596440 U CN 201020596440U CN 201890794 U CN201890794 U CN 201890794U
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Abstract
The utility model discloses a novel high-efficiency physicochemical water treatment settling tank device structure, which relates to field of sewage treatment and reclaimed water recycling facility treatment. The novel high-efficiency physicochemical water treatment settling tank device mainly comprises a vortex hydraulic mixer, a flocculation reaction stirrer, a flocculation reaction tank, an inclined pipe settling region, a water collection tank and a sludge concentration region, wherein a guide drum with an open lower end is further arranged in the flocculation reaction tank, and the flocculation reaction stirrer is arranged in the guide drum which is provided with a plurality of guide holes. The novel high-efficiency physicochemical water treatment settling tank device functionally integrates drug feeding and mixing, flocculation reaction, sewage settling and clarification and sludge concentration, and achieves purposes of multiple tanks. Upward irregular vortex is generated in the guide drum of the flocculation reaction stirrer to lift the wastewater to the guide holes by the aid of the guide drum with the guide holes, then the waste water flows out of the guide holes into the flocculation reaction tank, and further flows into the guide drum from the lower portion of the guide drum to flow cyclically, and thereby coagulation effect is enhanced greatly.
Description
Technical field
The utility model relates to sewage disposal and middle water reuse facility process field, mainly is at a kind of new and effective materialization water treatment deposition pool device that is used for the municipal wastewater purifying treatment.
Background technology
Current, China on the one hand water resources extremely lacks and is seriously polluted, and the not treated or treated phenomenon of just discharging not up to standard of sewage is very general on the other hand, thereby has caused the waste of great lot of water resources and to influence from social surroundings.Handle although adopted in the market by the method for two-stage precipitation in-depth water treatment, however treatment effect and not obvious.This facility is made up of mixing pit, reaction tank, settling tank, sludge thickener etc. respectively, mainly has shortcomings such as technical process is long, floor space is big, construction cost is high, water consumption is big, running cost is high, long-term operation poor stability.
Summary of the invention
The utility model purpose is exactly at overcoming the shortcoming that above-mentioned traditional water treatment facility exists, the established technology long flow path, floor space is big, water consumption is big, construction cost and shortcomings such as high running cost height, long-term operation poor stability, a kind of efficient materialization sedimentation pond for water treatment constructional device that design is adopted.
The utility model adopts following technical scheme:
A kind of new and effective materialization water treatment deposition pool device, it is mainly by the eddy current hydraulic mixer, the flocculation reaction stirrer, flocculation tank, the tube settling district, water leg and mud enrichment region are formed, described eddy current hydraulic mixer is located at the flocculation tank front end, be provided with described flocculation reaction stirrer in the described flocculation tank, the water side of flocculation tank communicates with the water intake end of mud enrichment region, be provided with the mud thickner in the described mud enrichment region, mud thickner lowermost end is provided with shore pipe and mud is back to the mud return line of described flocculation tank bottom, be provided with the tube settling tripping device on mud enrichment region top, this tube settling tripping device links to each other with water leg described and that the external world communicates, the guide shell that also comprises lower ending opening in the wherein said flocculation tank, described flocculation reaction stirrer is located in the described guide shell, and this guide shell is provided with some pod apertures.
The ingress of eddy current hydraulic mixer is provided with water inlet pipe and coagulating agent chemical feed pipe.
The bottom of flocculation tank is provided with the water inlet pipe that leads to described guide shell, and the outlet of described eddy current hydraulic mixer and mud return line feeds respectively in this water inlet pipe.
The utility model integrates dosing mixing, flocculation reaction, settlement of sewage clarification, mud concentrating function, and the function of many ponds effect is played in a pond.Both efficiently solve traditional coagulating sedimentation clarification water-purifying process and accounted for problems such as big at area, that water treatment process is long, energy consumption is high, dosage is big, the mud concentrated effect is poor, water consumption is big, have the deposition efficiency height again, occupation of land face is little, the concentrated aqueous rate of mud is low, water consumption is little, technical process is short, but also has reduced energy consumption and construction investment.Employing with guide shell of pod apertures, make the flocculation reaction stirrer in guide shell, form the irregular eddy current that makes progress, after waste water is promoted to pod apertures, be expelled in the flocculation tank from pod apertures again, waste water further enters in the guide shell from the guide shell bottom again, formation circulates, and has greatly strengthened coagulation effect.This device is specially adapted in municipal water supply processing, sewage disposal or middle water Treatment for Reuse and the sludge concentration and treatment process, is a kind of new and effective materialization water treatment deposition pool device that substitutes traditional coagulating sedimentation water technology.
Description of drawings
Fig. 1 is a utility model structural representation of the present invention.
Be arranged in order in the drawings and be (1) water inlet pipe, (2) coagulating agent chemical feed pipe, (3) micro swirl hydraulic mixer, (4) flocculation basin water inlet pipe, (5) pod apertures, (6) coagulating stirrer, (8) flocculation tank, (9) guide shell, (10) tube settling district, (11) water leg, (13) mud enrichment region, (14) mud thickner, (15) mud discharging pipe, (16) mud return line.
Embodiment is as follows
As shown in the figure, the utility model is a kind of constructional device of new and effective materialization sedimentation pond for water treatment, and this pond body is followed successively by micro swirl hydraulic mixer 3, flocculation basin water inlet pipe 4, guide shell 9, coagulating stirrer 6, pod apertures 5, flocculation tank 8, mud enrichment region 13, tube settling district 10, water leg 11 from feed-water end to water side.The entrance end of micro swirl hydraulic mixer 3 is provided with to micro swirl hydraulic mixer 3 and feeds the water inlet pipe 1 of waste water and the coagulating agent chemical feed pipe 2 of feeding coagulating agent.The water outlet of micro swirl hydraulic mixer 3 feeds the flocculation basin water inlet pipe 4 of being located at flocculation tank 8 bottoms.Be provided with the guide shell 9 that lower ending opening, top are provided with some pod apertures that are interspersed 5 in the flocculation tank 8, the opening end of guide shell 9 can adopt various ways such as directly barrel-shaped, tubaeform or a plurality of prosopyles.The water outlet of flocculation basin water inlet pipe 4 directly feeds in the pod apertures 5 from opening end.Be provided with coagulating stirrer 6 in the pod apertures 5, the blade of coagulating stirrer 6 is located at the middle and lower part of pod apertures 5.
The water side of flocculation tank 8 communicates with the water intake end of mud enrichment region 13, can adopt the form of traverse baffle between the two, and waste water is flowed into the mud enrichment region 13 certainly from flocculation tank 8.Be provided with mud thickner 14 in the mud enrichment region 13, mud thickner bottom center is communicated with shore pipe 15 and mud return line 16, and the outlet of this mud return line 16 feeds in the flocculation basin water inlet pipe 4.The top of flocculation tank 8 is tube settling districts 10, and the water outlet in tube settling district 10 communicates with water leg 11.
New and effective materialization water treatment deposition pool device of the present utility model, when carrying out the sewage disposal use, sewage flows into micro swirl hydraulic mixer 3 by water inlet pipe 1, and by coagulating agent chemical feed pipe 3 dosing coagulant in eddy current hydraulic mixer 3.Through dosing blended sewage, and the mud that passes through mud return line 16 backflows, enter into from flocculation basin water inlet pipe 4 in the guide shell 9 of flocculation tank 8, under the effect of the stirring of coagulating stirrer 6 and eddy current, be promoted to pod apertures 5 places of guide shell 9, and outwards acutely gush out to flocculation tank 8 tops from pod apertures 5.Waste water flow to flocculation tank 8 bottoms downwards from flocculation tank 8 tops again, is back in the guide shell 9 from guide shell 9 lower ending openings under pressure then, carries out circulating coagulation and handles.Fully after the flocculation reaction, from flowing into mud enrichment region 13, further mix with mud by traverse baffle.Mud in the mud enrichment region 13 is after mud thickner 14 is handled, and a part is discharged by mud discharging pipe 15, and another part is by mud return line 16 reuses.Waste water further upwards carries out separating of mud and water from flowing into tube settling district 10 after mud enrichment region 13 is handled, isolated clear water after water leg 11 is collected, the discharge system.
Claims (3)
1. new and effective materialization water treatment deposition pool device, it is mainly by the eddy current hydraulic mixer, the flocculation reaction stirrer, flocculation tank, the tube settling district, water leg and mud enrichment region are formed, described eddy current hydraulic mixer is located at the flocculation tank front end, be provided with described flocculation reaction stirrer in the described flocculation tank, the water side of flocculation tank communicates with the water intake end of mud enrichment region, be provided with the mud thickner in the described mud enrichment region, mud thickner lowermost end is provided with shore pipe and mud is back to the mud return line of described flocculation tank bottom, be provided with the tube settling tripping device on mud enrichment region top, this tube settling tripping device links to each other with water leg described and that the external world communicates, it is characterized in that also comprising in the described flocculation tank guide shell of lower ending opening, described flocculation reaction stirrer is located in the described guide shell, and this guide shell is provided with some pod apertures.
2. new and effective materialization water treatment deposition pool device according to claim 1 is characterized in that the ingress of described eddy current hydraulic mixer is provided with water inlet pipe and coagulating agent chemical feed pipe.
3. new and effective materialization water treatment deposition pool device according to claim 1, the bottom that it is characterized in that described flocculation tank is provided with the water inlet pipe that leads to described guide shell, and the outlet of described eddy current hydraulic mixer and mud return line feeds respectively in this water inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205964405U CN201890794U (en) | 2010-11-08 | 2010-11-08 | Novel high-efficiency physicochemical water treatment settling tank device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205964405U CN201890794U (en) | 2010-11-08 | 2010-11-08 | Novel high-efficiency physicochemical water treatment settling tank device |
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| Publication Number | Publication Date |
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| CN201890794U true CN201890794U (en) | 2011-07-06 |
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| CN2010205964405U Expired - Fee Related CN201890794U (en) | 2010-11-08 | 2010-11-08 | Novel high-efficiency physicochemical water treatment settling tank device |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102309872A (en) * | 2011-09-06 | 2012-01-11 | 江苏海洲水务工程有限公司 | Clarifying tank |
| CN102432360A (en) * | 2011-08-25 | 2012-05-02 | 广东拉多美化肥有限公司 | Fusing and mixing device |
| CN102515383A (en) * | 2011-11-24 | 2012-06-27 | 西安热工研究院有限公司 | Water-saving clarification and purification system and process thereof |
| CN103214141A (en) * | 2012-12-07 | 2013-07-24 | 北京翰祺环境技术有限公司 | Sewage advanced treatment and recycling method capable of substantially raising economy |
| CN105502623A (en) * | 2016-01-26 | 2016-04-20 | 何旭红 | Neutralizing and settling pool |
| CN106241929A (en) * | 2016-08-31 | 2016-12-21 | 上海汉盛环保科技有限公司 | A kind of high-density air floats sedimentation tank device |
| CN107935288A (en) * | 2017-12-19 | 2018-04-20 | 北京中洁蓝环保科技有限公司 | A kind of MVR evaporations divide the pretreatment system of salt |
| CN110902787A (en) * | 2019-11-08 | 2020-03-24 | 陕西大唐水务有限责任公司 | Fluidized bed precipitation device and sewage treatment system thereof |
| CN111170546A (en) * | 2020-01-13 | 2020-05-19 | 蓝深集团股份有限公司 | High-density clarification tank |
| CN111620474A (en) * | 2020-06-16 | 2020-09-04 | 浙江大学 | Biochemical tail water mechanical coagulation clarification device and method thereof |
| CN115532141A (en) * | 2022-12-01 | 2022-12-30 | 山东华城工程技术有限公司 | Multistage flocculation turbine mixing system feeds water |
-
2010
- 2010-11-08 CN CN2010205964405U patent/CN201890794U/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102432360A (en) * | 2011-08-25 | 2012-05-02 | 广东拉多美化肥有限公司 | Fusing and mixing device |
| CN102432360B (en) * | 2011-08-25 | 2013-09-04 | 广东拉多美化肥有限公司 | Fusing and mixing device |
| CN102309872A (en) * | 2011-09-06 | 2012-01-11 | 江苏海洲水务工程有限公司 | Clarifying tank |
| CN102515383A (en) * | 2011-11-24 | 2012-06-27 | 西安热工研究院有限公司 | Water-saving clarification and purification system and process thereof |
| CN102515383B (en) * | 2011-11-24 | 2013-08-28 | 西安西热水务环保有限公司 | Water-saving clarification and purification system and process thereof |
| CN103214141A (en) * | 2012-12-07 | 2013-07-24 | 北京翰祺环境技术有限公司 | Sewage advanced treatment and recycling method capable of substantially raising economy |
| CN105502623A (en) * | 2016-01-26 | 2016-04-20 | 何旭红 | Neutralizing and settling pool |
| CN106241929A (en) * | 2016-08-31 | 2016-12-21 | 上海汉盛环保科技有限公司 | A kind of high-density air floats sedimentation tank device |
| CN107935288A (en) * | 2017-12-19 | 2018-04-20 | 北京中洁蓝环保科技有限公司 | A kind of MVR evaporations divide the pretreatment system of salt |
| CN110902787A (en) * | 2019-11-08 | 2020-03-24 | 陕西大唐水务有限责任公司 | Fluidized bed precipitation device and sewage treatment system thereof |
| CN111170546A (en) * | 2020-01-13 | 2020-05-19 | 蓝深集团股份有限公司 | High-density clarification tank |
| CN111620474A (en) * | 2020-06-16 | 2020-09-04 | 浙江大学 | Biochemical tail water mechanical coagulation clarification device and method thereof |
| CN111620474B (en) * | 2020-06-16 | 2024-01-30 | 浙江大学 | Biochemical tail water mechanical coagulation clarification equipment and method thereof |
| CN115532141A (en) * | 2022-12-01 | 2022-12-30 | 山东华城工程技术有限公司 | Multistage flocculation turbine mixing system feeds water |
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| 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: 20110706 Termination date: 20131108 |