CN202011812U - Integrated equipment for treating high-concentration organic wastewater - Google Patents
Integrated equipment for treating high-concentration organic wastewater Download PDFInfo
- Publication number
- CN202011812U CN202011812U CN2011200579425U CN201120057942U CN202011812U CN 202011812 U CN202011812 U CN 202011812U CN 2011200579425 U CN2011200579425 U CN 2011200579425U CN 201120057942 U CN201120057942 U CN 201120057942U CN 202011812 U CN202011812 U CN 202011812U
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- organic wastewater
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- anaerobic
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Abstract
The utility model discloses integrated equipment for treating high-concentration organic wastewater, which comprises an anaerobic chamber (13), an aerobic chamber (14), a filtration chamber (15) and a disinfection chamber (16) which are arranged in a box body and are separated by clapboards. The anaerobic chamber (13) is provided with an inlet of the wastewater to be treated and the disinfection chamber is provided with a purified water discharge port; the anaerobic chamber is communicated with the aerobic chamber through a communication pipe; the aerobic chamber is communicated with the filtration chamber through a communication pipe; the filtration chamber is communicated with the disinfection chamber through a communication pipe; and water turning devices (17) for controlling the flow direction of a water body are respectively arranged between the anaerobic chamber and the aerobic chamber, between the aerobic chamber and the filtration chamber and between the filtration chamber and the disinfection chamber. For the integrated equipment disclosed by the utility model, an optimal conventional activated sludge method is avoided and pollution factors in sewage, such as COD (Chemical Oxygen Demand), BOD5 (Biochemical Oxygen demand after 5 days), NH4+-N, TP (total phosphorus) and the like, are removed mainly by utilizing a reaction of biological colonies. The integrated equipment for treating the high-concentration organic wastewater has the advantages of few reactors, few steps, high treatment efficiency and the like. The sewage is subjected to more efficient nitrogen and phosphorus removal by a denitrification technology.
Description
Technical field
The utility model relates to environmental technology field, and is concrete, relates to a kind of processing high concentrated organic wastewater integration apparatus.
Background technology
Sanitary sewage mainly comprises two portions, and a part is the high strength domestic sewage of lavatory flushing ight soil, and another part is the kitchen water except that flushing supply, the sanitary sewage of lower concentrations such as laundry and bath water.Generally two portions waste water is handled together at present, but the processing that has increased the weight of treatment system is so undoubtedly loaded.Simultaneously, because rapid development of economy, universe's urbanization process is accelerated, people's productive life is more concentrated, and the part concentration zones is not set up centralized sewage treatment facility, and main centralized sewage treatment facility ubiquity floor space is big at present, the working cost height.
The utility model content
The purpose of this utility model is to provide a kind of processing high concentrated organic wastewater integration apparatus, and this equipment is a kind of integration apparatus, and reactor is few, step is few, processing efficiency is high.
The utility model high concentrated organic wastewater integration apparatus is included in a casing inner route clapboard and separates anaerobic room, aerobic room, filtration chamber and the sterilized room that is provided with; Described anaerobic room is provided with pending waterwater entrance, and described sterilized room is provided with the discharge outlet of purifying waste water; Between described anaerobic room and the aerobic room, between aerobic room and the filtration chamber, communicate by communicating pipe between filtration chamber and the sterilized room, and be respectively equipped with the water stirrer that the control water body flows to.
In the described anaerobic room biologic packing material is set, the bottom is provided with submersible agitator.
There is blower fan in described aerobic room by pipe connection, the inner biologic packing material that hangs, and aerator is installed in the bottom.In order to form the part oxygen anaerobic environment of holding concurrently, reach the denitrogenation dephosphorizing effect, aerator can partition running, and described aerator adopts the stage aeration device.
Described aerobic room is provided with reflux pump; The pipeline input terminus of described reflux pump is communicated with aerobic room, and the pipeline output terminal is communicated with anaerobic room.Being provided with of reflux pump can be controlled aerobic indoor water body and be back to anaerobic room, thereby reaches better denitrogenation dephosphorizing effect.
Establish filtrate in the described filtration chamber, described filtrate comprises three layers, and the lowest layer is the pebbles layer, and the middle layer is brown bed course, and the superiors are quartz sand layer.
The bottom of described filtration chamber is provided with the sludge pump that can control outside discharging mud.
Described sterilized room bottom is provided with the recoil pump that is used for counterflush.
Described sterilized room has sterilizing unit by pipe connection.
Described integration apparatus anaerobic room provides a kind of anaerobic environment, hang biologic packing material therein, add bacterial classification, former water enters the anaerobic pond bottom from pending waterwater entrance after pre-treatment, slowly upwards by microbial film (packing layer), issue unboiled water at anaerobic environment and separate acidifying,, add diving mixer in the anaerobic room bottom for increasing even water quality; Treating water turns over downwards from anaerobic room by two water stirrers, enter aerobic room from the aerobic room bottom, hang biologic packing material in the aerobic room, add bacterial classification, the stage aeration device is established in the bottom, but stage aeration device independent operating, form aerobic zone and aerobic area, reach and remove part N, P purpose,, the aerobic zone treating water is back to the nitrated N of removing of anaerobic zone generation anaerobism, P for N, P equipment in the better removal water add reflux pump in aerobic room; Treating water is through two water stirrers, turn over downwards from the aerobic room top, enter the filtration chamber from the bottom, filtration chamber, slowly upwards successively by pebbles layer, palm fibre pad and quartz sand, reach the filtration purpose, equipment portion adopts and adds mud, and sludge output is little, mainly be the suspended substance and the biological bacterium colony that comes off in the former water, establish the sludge pump spoil disposal in the bottom, filtration chamber; Treating water enters after sterilizing from the discharge outlet discharging of purifying waste water from the sterilized room bottom through water stirrer.
In sum, the utility model compared with prior art has the following advantages:
(1), this practical type is a kind of integration apparatus, reactor is few, step is few, processing efficiency is high; And utilize the denitrification technology that sewage is carried out more effective denitrogenation dephosphorizing.
(2), the utility model integration apparatus, avoid optimizing traditional activated sludge process, mainly be through the reaction of biological bacterium colony, remove COD, BOD in the sewage
5, NH
4 +Pollution factor such as-N, TP.
(3), the utility model integration apparatus shortens the technical process of sewage disposal, and is simple in structure; Energy-conservation, do not use mud, reduce tradition and reflux, take up an area of few; Anti impulsion load is strong, and is stable; Mud generation and demand are little.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is an A-A diagrammatic cross-section among Fig. 1.
Fig. 3 is a B-B diagrammatic cross-section among Fig. 1.
Fig. 4 is a C-C diagrammatic cross-section among Fig. 1.
Fig. 5 is a D-D diagrammatic cross-section among Fig. 1.
Fig. 6 is an E-E diagrammatic cross-section among Fig. 1.
Sterilizing unit; 9-reflux pump; 10-recoil pump; 11-sludge pump; 12-flocculation agent adding set; 13-anaerobic room; 14-aerobic room; 15-filtration chamber; 16-sterilized room; 17-water stirrer; 18-diving mixer.
Embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
As shown in Figure 1, the utility model integration apparatus is included in a casing inner route clapboard and separates anaerobic room 13, aerobic room 14, filtration chamber 15 and the sterilized room 16 that is provided with; Described anaerobic room 13 is provided with pending waterwater entrance, and described sterilized room is provided with the discharge outlet of purifying waste water; Between described anaerobic room and the aerobic room, between aerobic room and the filtration chamber, communicate by communicating pipe between filtration chamber and the sterilized room, and be respectively equipped with the water stirrer 17 that the control water body flows to.In anaerobic room 13 and the aerobic room 14 biologic packing material 1 is set all.The anaerobic room bottom also is provided with the submersible agitator 18 that is used for even water quality.Aerobic room 14 is connected with blower fan 5 by pipeline 6, and the stage aeration device is installed in the bottom.
Establish filtrate in the described filtration chamber 15, described filtrate is divided into three layers, and the lowest layer is paved pebbles, and the palm fibre pad is laid in the middle layer, and quartz sand is laid by the superiors.Can also there be flocculation agent adding set 12 filtration chamber 15 by pipe connection.Flocculation agent adding set 12 can add flocculation agent in filtration chamber 15, make impurities suspended substance in biomass particle in the water and the former water, forms coacervation of colloid and becomes the floc sedimentation shape, thereby precipitate better.
Described sterilized room 16 has sterilizing unit 8 by pipe connection.
Former water enters anaerobic room 13 bottoms behind pre-treatment lattice slag, water quality is even in the anaerobic room under the effect of diving mixer 18, treating water is microbial film acidication on filler 1 upwards slowly, enter aerobic room 14 bottoms through water stirrer 17, under blower fan 5, aerator 7 aerating system effects, slowly fully react and remove COD, BOD through microbial film on the filler 1
5 Aerator 7 can partition running form the double oxygen anaerobic environment of part, reach the denitrogenation dephosphorizing effect, treating water enters 15 bottoms, filtration chamber through water stirrer 17, treating water once slowly upwards reaches the filtration purpose through pebbles 2, palm fibre pad 3, quartz sand 4, and filtration aftertreatment water enters sterilized room 16 through water stirrer 17 and effluxes after sterilizing unit 8 sterilizations.Be better denitrogenation dephosphorizing, add reflux pump 9 in the aerobic room 14 and be back to anaerobic room 13 that a small amount of mud adds sludge pump 11 regular desilts in the filtration chamber 15, filtrate stops up needs back flushing, adds recoil pump 10 in the sterilized room 16.
Claims (9)
1. handle the high concentrated organic wastewater integration apparatus for one kind, it is characterized in that, be included in a casing inner route clapboard and separate anaerobic room (13), aerobic room (14), filtration chamber (15) and the sterilized room (16) that is provided with; Described anaerobic room (13) is provided with pending waterwater entrance, and described sterilized room is provided with the discharge outlet of purifying waste water; Between described anaerobic room and the aerobic room, between aerobic room and the filtration chamber, communicate by communicating pipe between filtration chamber and the sterilized room, and be respectively equipped with the water stirrer (17) that the control water body flows to.
2. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that biologic packing material (1) is set in the described anaerobic room (13), and the bottom is provided with submersible agitator (18).
3. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that described aerobic room (14) is connected with blower fan (5) by pipeline (6), the inner biologic packing material (1) that hangs, and aerator (7) is installed in the bottom.
4. a kind of processing high concentrated organic wastewater integration apparatus according to claim 3 is characterized in that described aerator (7) is the stage aeration device.
5. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that described aerobic room (14) is provided with reflux pump (9); The pipeline input terminus of described reflux pump (9) is communicated with aerobic room, and the pipeline output terminal is communicated with anaerobic room.
6. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that described filtration chamber establishes filtrate in (15), and described filtrate comprises three layers, and the lowest layer is the pebbles layer, and the middle layer is brown bed course, and the superiors are quartz sand layer.
7. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that the bottom of described filtration chamber (15) is provided with the sludge pump (11) that can control outside discharging mud.
8. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that, described sterilized room (16) bottom is provided with the recoil pump (10) that is used for counterflush.
9. a kind of processing high concentrated organic wastewater integration apparatus according to claim 1 is characterized in that described sterilized room (16) has sterilizing unit (8) by pipe connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200579425U CN202011812U (en) | 2011-03-08 | 2011-03-08 | Integrated equipment for treating high-concentration organic wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200579425U CN202011812U (en) | 2011-03-08 | 2011-03-08 | Integrated equipment for treating high-concentration organic wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202011812U true CN202011812U (en) | 2011-10-19 |
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ID=44782425
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200579425U Expired - Fee Related CN202011812U (en) | 2011-03-08 | 2011-03-08 | Integrated equipment for treating high-concentration organic wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202011812U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104370421A (en) * | 2014-11-14 | 2015-02-25 | 安徽建筑大学 | Modified pumice bioreactor device |
| CN106830320A (en) * | 2017-02-27 | 2017-06-13 | 兰州理工大学 | A kind of method of integrated form biological bed and treatment rural scattered domestic sewage |
| CN110498568A (en) * | 2019-08-29 | 2019-11-26 | 上海浩为环境工程有限公司 | A kind of sewage simultaneous phosphorus and nitrogen removal integrated apparatus and method |
-
2011
- 2011-03-08 CN CN2011200579425U patent/CN202011812U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104370421A (en) * | 2014-11-14 | 2015-02-25 | 安徽建筑大学 | Modified pumice bioreactor device |
| CN104370421B (en) * | 2014-11-14 | 2016-08-24 | 安徽建筑大学 | A kind of modified foam bioreactor device |
| CN106830320A (en) * | 2017-02-27 | 2017-06-13 | 兰州理工大学 | A kind of method of integrated form biological bed and treatment rural scattered domestic sewage |
| CN110498568A (en) * | 2019-08-29 | 2019-11-26 | 上海浩为环境工程有限公司 | A kind of sewage simultaneous phosphorus and nitrogen removal integrated apparatus and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Sichuan GaoTong Environmental Protection Technology Co., Ltd. Assignor: Sichuan Stong OMEX Environmental Engineering Co., Ltd. Contract record no.: 2012510000087 Denomination of utility model: Integrated equipment for treating high-concentration organic wastewater Granted publication date: 20111019 License type: Exclusive License Record date: 20120824 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111019 Termination date: 20140308 |