CN204958652U - Water processing system is subsided to integration high efficiency - Google Patents
Water processing system is subsided to integration high efficiency Download PDFInfo
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- CN204958652U CN204958652U CN201520524544.8U CN201520524544U CN204958652U CN 204958652 U CN204958652 U CN 204958652U CN 201520524544 U CN201520524544 U CN 201520524544U CN 204958652 U CN204958652 U CN 204958652U
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- water
- settler
- reverse osmosis
- osmosis filter
- ultraviolet sterilizer
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Abstract
The utility model belongs to the technical field of sewage treatment device, especially, relate to a water processing system is subsided to integration high efficiency, medicine storage tank and charge device are connected, reverse osmosis filter is connected with middle aqueous phase, former pond is connected with the temperature equalizing basin, the temperature equalizing basin is connected with the biological reaction pond, the biological reaction pond is connected with the clarifier with charge device simultaneously, the clarifier passes through clarifier outlet pipe way with reverse osmosis filter and is connected, reverse osmosis filter's dense water pipe way is connected with clarifier outlet pipe way and is constituted circulation circuit, reverse osmosis filter outlet pipe way is connected with middle water tank, middle water tank is connected with ultraviolet sterilizer, ultraviolet sterilizer is connected with the clean water basin, the ultraviolet sterilizer lower extreme is connected with the clarifier and is formed circulation circuit. The beneficial effects of the utility model are that: the novel area that has reduced the reverse osmosis link, does not use the reaction tank, and effectively improving treatment capacity improves a water quality of water.
Description
Technical field
The utility model belongs to technical field of sewage treatment equipment, particularly relates to a kind of integrated high-efficiency sedimentation water treatment system.
Background technology
Water resources is very important natural resources, and the vital movement of the mankind and activity in production need to use water invariably.Along with the quickening of urbanization process, quantity of wastewater effluent also constantly increases.Water technology is water conservation, improves the requisite means of water surrounding, plays a part more and more important in national economy, is widely used in work, agricultural and purifying domestic sewage reuse.Under the condition of water resources famine, the surface water such as river, river, lake, the trade effluents such as recirculated water, water coolant, pit water, the process water of the every profession and trades such as Steel Plant, power plant, textile printing and dyeing factory, chemical plant, chemical fibre factory, rubber plant, colliery and Small water works domestic water, can Recovery Purifying recycling.Integrated water treatment equipment because its occupation of land is little, energy consumption is low, the advantage such as convenient is installed and there is certain application prospect.
But it is low to there is level of automation in existing water purifying plant, the shortcomings such as security is not high, and also effluent quality needs to be improved further.The biological reaction tank used in water treatment system utilizes bacterial classification to remove to anhydrate middle part dirt, because the survival of bacterial classification and the performance of activity need in suitable condition as temperature, pH, sewage directly uses biological reaction tank treatment effect not good without any process, and efficiency is not high; Mix sewage and medicine by coagulation reaction tank in water treatment, and need separating device to be separated, settling efficiency is not high and floor space large, and the water quality obtained does not meet the quality of reused water requirement of process water or circulating cooling supplementary feed.
Utility model content
In order to overcome above-mentioned the deficiencies in the prior art, the purpose of this utility model is to provide a kind of integrated high-efficiency sedimentation water treatment system, effectively can improve processing power, improve effluent quality, reach the quality of reused water requirement as industry circulating cooling supplementary feed such as power plant.
To achieve these goals, the utility model adopts following technical scheme:
A kind of integrated high-efficiency sedimentation water treatment system, comprise former pond, medicine storing pot, chemicals dosing plant, reverse osmosis filter, intermediate water tank, clean water basin, described medicine storing pot is connected with described chemicals dosing plant, described reverse osmosis filter is connected with described intermediate water tank, characterized by further comprising lower water temperature pond, biological reaction tank, settler, ultraviolet sterilizer, described former pond is connected with described lower water temperature pond, described lower water temperature pond is connected with described biological reaction tank, described biological reaction tank, described chemicals dosing plant is connected with described settler simultaneously, described settler is connected by settler outlet pipeline with described reverse osmosis filter, dense water lines and the described settler outlet pipeline of described reverse osmosis filter connect and compose circulation loop, described reverse osmosis filter outlet pipeline is connected with described intermediate water tank, described intermediate water tank is connected with described ultraviolet sterilizer, described ultraviolet sterilizer is connected with described clean water basin, described ultraviolet sterilizer lower end is connected with described settler and forms circulation loop.
Described settler is cantboard clarifier, described settler comprises whirl cylinder, the water-in be communicated with whirl cylinder, water outlet, dosing mouth, described whirl cylinder bottom is provided with slurry chamber, the first reaction chamber is provided with in the middle part of described whirl cylinder, the second reaction chamber is provided with between described first reaction chamber and described whirl cylinder, described first reaction chamber both sides external is fixed with the first swash plate respectively, and the angle of described first swash plate and vertical direction is 30-60 °, and described first swash plate lower end is provided with the second vertical plate.
Described settler outlet pipeline is provided with topping-up pump.
The under meter being provided with water pump between described settler with described biological reaction tank and being connected with water pump.
The pipeline of described reverse osmosis filter is provided with tensimeter.
Cooling tube and temperature sensor is provided with in described lower water temperature pond.
Described ultraviolet sterilizer exit is provided with chlorine detector.
The beneficial effects of the utility model are: can pass into different media in cooling tube, the temperature of lower water temperature pool inner water is heated or cools, with the survival temperature making its temperature be applicable to flora in biological reaction tank, and then bacterial classification is made to play its degraded to Organic substance in water and oils preferably; The biological reaction tank medicine such as water and flocculation agent out directly enters settler, do not need coagulation reaction tank, the water dealt by biological reaction tank by negative pressure before pump by water pump is sucked in the lump, mix in settler with flocculation agent again, complete tiny flocculation fast, and prevent from forming alumen ustum or comparatively big flocculating body; And settler to adopt with the first reaction chamber be first swash plate of 30-60 ° and the second swash plate of being connected with the first swash plate, solve the shortcoming that common swash plate design capacity of resisting impact load is poor, spoil disposal is difficult, effluent quality is uneven, there is energy dissipating, rectification and mud-water separation dual function, reduce the spoil disposal load in swash plate district, increase the processing power of settler; Add ultraviolet sterilizer, reduce chlorine content in water, ultraviolet sterilizer lower end is connected with settler and forms circulation loop, and the water not meeting examination criteria can reenter settler and process.The utility model reduces floor space, decrease reverse osmosis link, do not use reaction tank, effectively can improve processing power, improve effluent quality, final outflow water turbidity is less than 2 ~ 5NTU, and COD clearance is 65 ~ 85%, reaches the quality of reused water requirement as industry circulating cooling supplementary feed such as power plant.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model settler.
In figure, 1, former pond, 2, medicine storing pot, 3, chemicals dosing plant, 4, reverse osmosis filter, 5, intermediate water tank, 6, clean water basin, 7, lower water temperature pond, 8, biological reaction tank, 9, settler, 10, ultraviolet sterilizer, 11, settler outlet pipeline, 12, dense water lines, 13, tensimeter, 14, water-in, 15, water outlet, 16, dosing mouth, 17, slurry chamber, 18, the first reaction chamber, 19, the second reaction chamber, the 20, first swash plate, the 21, second vertical plate, 22, topping-up pump, 23, water pump, 24, under meter, 25, whirl cylinder.
Embodiment
Below in conjunction with accompanying drawing, a kind of embodiment of the present utility model is explained.
As shown in Figure 1, the utility model provides a kind of integrated high-efficiency sedimentation water treatment system, comprise former pond 1, medicine storing pot 2, chemicals dosing plant 3, reverse osmosis filter 4, intermediate water tank 5, clean water basin 6, described medicine storing pot 2 is connected with described chemicals dosing plant 3, described reverse osmosis filter 4 is connected with described intermediate water tank 5, characterized by further comprising lower water temperature pond 7, biological reaction tank 8, settler 9, ultraviolet sterilizer 10, described former pond 1 is connected with described lower water temperature pond 7, described lower water temperature pond 7 is connected with described biological reaction tank 8, in biological reaction tank 8, cultivation can remove organic bacterial classification, and to ensure there is suitable temperature in biological reaction tank 8, the conditions such as humidity, be convenient to survival and the breeding of bacterial classification, described biological reaction tank 8, described chemicals dosing plant 3 are connected with described settler 9 simultaneously, described settler 9 is connected by settler outlet pipeline 11 with described reverse osmosis filter 4, dense water lines 12 and the described settler outlet pipeline 11 of described reverse osmosis filter 4 connect and compose circulation loop, there is reverse osmosis membrane in reverse osmosis filter 4, can again be filtered from reverse osmosis filter 4 dense water out, the pipeline of described reverse osmosis filter 4 is provided with tensimeter 13, for controlling the pressure of reverse osmosis filter 4,
Described reverse osmosis filter 4 outlet pipeline is connected with described intermediate water tank 5, described intermediate water tank 5 is connected with described ultraviolet sterilizer 10, described ultraviolet sterilizer 10 is connected with described clean water basin 6, described ultraviolet sterilizer 10 lower end is connected with described settler 9 and forms circulation loop, ultraviolet sterilizer 10 exit is provided with chlorine detector, and the water not meeting examination criteria can reenter settler 9 and process.
As shown in Figure 2, described settler 9 is cantboard clarifier 9, described settler 9 comprises whirl cylinder 25, the water-in 14 be communicated with whirl cylinder 25, water outlet 15, dosing mouth 16, described whirl cylinder 25 bottom is provided with slurry chamber 17, the first reaction chamber 18 is provided with in the middle part of described whirl cylinder 25, the second reaction chamber 19 is provided with between described first reaction chamber 18 and described whirl cylinder 25, described first reaction chamber 18 both sides external is fixed with the first swash plate 20 respectively, described first swash plate 20 is 30-60 ° with the angle of vertical direction, and described first swash plate 20 lower end is provided with the second vertical plate 21.Instead of swash plate common in prior art, solve the shortcoming that common swash plate design capacity of resisting impact load is poor, spoil disposal is difficult, effluent quality is uneven, there is energy dissipating, rectification and mud-water separation dual function, reduce the spoil disposal load in swash plate district, increase the processing power of settler 9.
Described settler outlet pipeline 11 is provided with topping-up pump 22.
The under meter 24 being provided with water pump 23 between described settler 9 with described biological reaction tank 8 and being connected with water pump 23, eliminates coagulation reaction tank, directly in settler 9, completes coagulation and sedimentation work.
Cooling tube and temperature sensor is provided with in described lower water temperature pond 7.Different media can be passed in cooling tube, the temperature of water in lower water temperature pond 7 is heated or cooled, with the survival temperature making its temperature be applicable to flora in biological reaction tank 8, and then make bacterial classification play its degraded to Organic substance in water and oils preferably.According to the living necessities of bacterial classification, the pH value in lower water temperature pond 7 can also be adjusted to desired value, to ensure its processing power of the maximum performance of bacterial classification.
Above an example of the present utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.
Claims (7)
1. an integrated high-efficiency sedimentation water treatment system, comprise former pond, medicine storing pot, chemicals dosing plant, reverse osmosis filter, intermediate water tank, clean water basin, described medicine storing pot is connected with described chemicals dosing plant, described reverse osmosis filter is connected with described intermediate water tank, characterized by further comprising lower water temperature pond, biological reaction tank, settler, ultraviolet sterilizer, described former pond is connected with described lower water temperature pond, described lower water temperature pond is connected with described biological reaction tank, described biological reaction tank, described chemicals dosing plant is connected with described settler simultaneously, described settler is connected by settler outlet pipeline with described reverse osmosis filter, dense water lines and the described settler outlet pipeline of described reverse osmosis filter connect and compose circulation loop, described reverse osmosis filter outlet pipeline is connected with described intermediate water tank, described intermediate water tank is connected with described ultraviolet sterilizer, described ultraviolet sterilizer is connected with described clean water basin, described ultraviolet sterilizer lower end is connected with described settler and forms circulation loop.
2. high-efficiency sedimentation water treatment system according to claim 1, it is characterized in that described settler is cantboard clarifier, described settler comprises whirl cylinder, the water-in be communicated with whirl cylinder, water outlet, dosing mouth, described whirl cylinder bottom is provided with slurry chamber, the first reaction chamber is provided with in the middle part of described whirl cylinder, the second reaction chamber is provided with between described first reaction chamber and described whirl cylinder, described first reaction chamber both sides external is fixed with the first swash plate respectively, the angle of described first swash plate and vertical direction is 30-60 °, described first swash plate lower end is provided with the second vertical plate.
3. high-efficiency sedimentation water treatment system according to claim 1 and 2, is characterized in that described settler outlet pipeline is provided with topping-up pump.
4. high-efficiency sedimentation water treatment system according to claim 1 and 2, is characterized in that the under meter being provided with water pump between described settler with described biological reaction tank and being connected with water pump.
5. high-efficiency sedimentation water treatment system according to claim 1 and 2, is characterized in that the pipeline of described reverse osmosis filter is provided with tensimeter.
6. high-efficiency sedimentation water treatment system according to claim 1 and 2, is characterized in that being provided with cooling tube and temperature sensor in described lower water temperature pond.
7. high-efficiency sedimentation water treatment system according to claim 1 and 2, is characterized in that described ultraviolet sterilizer exit is provided with chlorine detector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520524544.8U CN204958652U (en) | 2015-07-18 | 2015-07-18 | Water processing system is subsided to integration high efficiency |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520524544.8U CN204958652U (en) | 2015-07-18 | 2015-07-18 | Water processing system is subsided to integration high efficiency |
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| Publication Number | Publication Date |
|---|---|
| CN204958652U true CN204958652U (en) | 2016-01-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520524544.8U Expired - Fee Related CN204958652U (en) | 2015-07-18 | 2015-07-18 | Water processing system is subsided to integration high efficiency |
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| Country | Link |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107814444A (en) * | 2017-11-17 | 2018-03-20 | 北京欧美中科学技术研究院 | A kind of water purification equipment of high treating effect |
-
2015
- 2015-07-18 CN CN201520524544.8U patent/CN204958652U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107814444A (en) * | 2017-11-17 | 2018-03-20 | 北京欧美中科学技术研究院 | A kind of water purification equipment of high treating effect |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160113 Termination date: 20160718 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |