CN203890132U - Anaerobic sewage treatment device - Google Patents
Anaerobic sewage treatment device Download PDFInfo
- Publication number
- CN203890132U CN203890132U CN201420215394.8U CN201420215394U CN203890132U CN 203890132 U CN203890132 U CN 203890132U CN 201420215394 U CN201420215394 U CN 201420215394U CN 203890132 U CN203890132 U CN 203890132U
- Authority
- CN
- China
- Prior art keywords
- anaerobic
- inner circulation
- internal recycle
- water
- circulation tank
- 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.)
- Expired - Fee Related
Links
Classifications
-
- Y02W10/12—
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model provides a sewage treatment device which comprises an anaerobic reaction tank and also comprises an inner circulation tank, wherein the inner circulation tank is arranged outside the anaerobic reaction tank and is communicated with the anaerobic reaction tank through a water outlet pipe; a water collector is arranged on the upper part of the inner circulation tank; the inner circulation tank is provided with an aerobic water outlet in a wall above the water collector; a centrifugal pump is arranged at the bottom of the inner circulation tank; the anaerobic reaction tank is provided with an anaerobic water inlet end; the anaerobic water inlet end is connected with a pipeline mixer; the pipeline mixer is respectively connected with the centrifugal pump and a raw water inlet end; an exhaust valve is arranged on the top of the inner circulation tank; an emptying valve is arranged at the bottom of the inner circulation tank. According to the inner circulation tank, sewage and sludge which are not completely subjected to anaerobic treatment can be circulated into an anaerobic system for performing secondary treatment, and load increase of an aerobic treatment system is avoided, so that the sewage treatment system can normally operate. The problem of the conventional sewage treatment device that lots of activated anaerobic sludge is usually taken out during anaerobic water discharge is solved.
Description
Technical field
The utility model relates to sewage treatment area, refers in particular to a kind of waste disposal plant.
Background technology
Anaerobic treatment process is mainly applicable to the treatment of Organic Wastewater of middle and high concentration.It utilizes anaerobic bacterium that the organic substance decomposing in waste water is accounted for to 25% for methane (accounting for 75%), CO2() and a small amount of mud.Because whole treating processes does not need oxygen supply, therefore energy consumption is very low, also can reduce a lot of operational maintenance problems (oxygen system needs very complicated maintenance conventionally) simultaneously, therefore in treatment of Organic Wastewater, has obtained widely and has used.Anaerobic technique has the following advantages: 1, surplus sludge volume is few; 2, low nutritional needs; 3, produce available methane gas; 4, running cost is lower.But the system for anaerobic treatment of conventional design has a distinct disadvantage, after being subject to heavy-duty service, anaerobic effluent usually all enters Aerobic Pond with a large amount of active anaerobic sludges, and to Aerobic Pond, processing has increased burden, has affected the effect of aerobic treatment.
Summary of the invention
The technical problems to be solved in the utility model, is to provide a kind of waste disposal plant, solve existing waste disposal plant in the time of anaerobic effluent usually all with a large amount of active anaerobic sludges.
The utility model is achieved in that
A kind of waste disposal plant, comprise anaerobic reaction-pot, also comprise internal recycle tank, described internal recycle tank is outside and be communicated with by rising pipe with anaerobic reaction-pot at described anaerobic reaction-pot, water collector is installed on internal recycle tank top, internal recycle tank has outputted aerobic water mouth on the wall above water collector, internal recycle pot bottom is provided with impeller pump, described anaerobic reaction-pot has anaerobism feed-water end, anaerobism feed-water end is connected with line mixer, line mixer respectively with impeller pump, former water upstream end connects, internal recycle tank top is provided with drain tap, internal recycle pot bottom has emptying valve.
The utility model has the advantage of: internal recycle tank of the present utility model can by not completely the sewage of anaerobic treatment and sludge circulation to secondary treatment again in anaerobic system, avoid aerobic treatment system loading to increase, Sewage treatment systems can normally be moved.
Brief description of the drawings
The utility model is further described with reference to the accompanying drawings in conjunction with the embodiments.
Fig. 1 is structural representation of the present utility model.
Embodiment
Refer to shown in Fig. 1, a kind of waste disposal plant, comprise anaerobic reaction-pot 1, also comprise internal recycle tank 2, internal recycle tank 2 is outside and be communicated with by rising pipe 3 with anaerobic reaction-pot 1 at anaerobic reaction-pot 1, water collector 4 is installed on internal recycle tank 2 tops, internal recycle tank 2 has outputted aerobic water mouth 5 on the wall above water collector 4, internal recycle tank 2 bottoms are provided with impeller pump 6, anaerobic reaction-pot 1 has anaerobism feed-water end 7, anaerobism feed-water end 7 is connected with line mixer 8, line mixer 8 respectively with impeller pump 6, former water upstream end 9 connects, internal recycle tank 2 tops are provided with drain tap 10, internal recycle tank 2 bottoms have emptying valve 11.
When concrete enforcement, preferably at anaerobic reaction-pot 1 top, anaerobism drain tap 12 is installed, is convenient to anaerobic reaction-pot 1 pressure equilibrium.In use, the anaerobism muddy water in anaerobic reaction-pot 1 flows to internal recycle tank 2 by rising pipe 3 to the utility model, and anaerobism muddy water supernatant liquor after internal recycle tank 2 precipitations is collected by outputted aerobic water mouth 5 and flow to aerobic treatment system by water collector 4.Mud after precipitation is mixed in anaerobic reaction-pot 1 through line mixer 8 and the former water of former water upstream end 9 by impeller pump 6, mud both can second stage employ, can not increase load to aerobic system again, impeller pump 6 can strengthen anaerobism water inlet flow velocity, anaerobic system bottom mud is rushed and makes mud and sewage contact reacts time lengthen to anaerobic reaction-pot 1 middle part, better bring into play anaerobic treatment effect.The drain tap 10 of internal recycle tank 2 can not timing be opened Valved discharge internal recycle tank 2 interior air can prevent that gas from blocking up phenomenon, makes impeller pump 6 can not produce idle running and damages impeller pump 6.Regularly open emptying valve 11 and unnecessary anaerobic sludge can be drained into anaerobic reaction-pot 1 and internal recycle tank 2 outsides, keep the normal ratio of anaerobic reaction-pot 1 and internal recycle tank 2 anaerobic sludges.Avoid anaerobic sludge to enter into aerobic treatment system, avoid aerobic treatment system loading to increase, Sewage treatment systems can normally be moved.
The above embodiment, it is preferred embodiments of the present utility model, be not to limit the utility model practical range, the equivalence of doing according to structure, feature and principle described in the utility model claim therefore all changes or modifies, and all should comprise in the utility model patent claim.
Claims (1)
1. a waste disposal plant, comprise anaerobic reaction-pot, it is characterized in that: also comprise internal recycle tank, described internal recycle tank is outside and be communicated with by rising pipe with anaerobic reaction-pot at described anaerobic reaction-pot, water collector is installed on internal recycle tank top, internal recycle tank has outputted aerobic water mouth on the wall above water collector, internal recycle pot bottom is provided with impeller pump, described anaerobic reaction-pot has anaerobism feed-water end, anaerobism feed-water end is connected with line mixer, line mixer respectively with impeller pump, former water upstream end connects, internal recycle tank top is provided with drain tap, internal recycle pot bottom has emptying valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420215394.8U CN203890132U (en) | 2014-04-29 | 2014-04-29 | Anaerobic sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420215394.8U CN203890132U (en) | 2014-04-29 | 2014-04-29 | Anaerobic sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203890132U true CN203890132U (en) | 2014-10-22 |
Family
ID=51716560
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420215394.8U Expired - Fee Related CN203890132U (en) | 2014-04-29 | 2014-04-29 | Anaerobic sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203890132U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105712476A (en) * | 2016-01-29 | 2016-06-29 | 北京交通大学 | Gas circulating stirring type anaerobic culture domestication device and method |
| CN106430573A (en) * | 2016-11-30 | 2017-02-22 | 中冶华天南京工程技术有限公司 | Anaerobic circulation system integrating sludge retention, heating and circulation functions |
-
2014
- 2014-04-29 CN CN201420215394.8U patent/CN203890132U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105712476A (en) * | 2016-01-29 | 2016-06-29 | 北京交通大学 | Gas circulating stirring type anaerobic culture domestication device and method |
| CN106430573A (en) * | 2016-11-30 | 2017-02-22 | 中冶华天南京工程技术有限公司 | Anaerobic circulation system integrating sludge retention, heating and circulation functions |
| CN106430573B (en) * | 2016-11-30 | 2019-07-05 | 中冶华天南京工程技术有限公司 | A kind of anaerobism circulatory system integrating retention sludge, heating and circulatory function |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104045156B (en) | Integrated high-efficiency self-supported denitrification reactor | |
| CN104118971A (en) | Method for strengthening nitrogen and phosphorus removal by using hydrolysis and fermentation of mixed sludge of sewage plant | |
| CN102531290B (en) | Method and device for sludge digestive fluid two-level biological denitrification | |
| CN103979683A (en) | Integrated expanded granular sludge bed-membrane bioreactor whole-course autotrophy denitrification device and process thereof | |
| CN103951055B (en) | The method of denitrification process low ratio of carbon to ammonium waste water while of methanation | |
| CN103011404A (en) | Internal-mixing anaerobic reaction tank | |
| CN204211601U (en) | Sewerage integrated processing system | |
| CN103979681A (en) | Nitrification/denitrification integrated rural domestic sewage treatment system | |
| CN204981348U (en) | Reinforce denitrogenation perpendicular - horizontal undercurrent integrated constructed wetland | |
| CN203890132U (en) | Anaerobic sewage treatment device | |
| CN103214156B (en) | Surplus sludge fermenting and coupling denitrification device and method in condition of low dissolved oxygen | |
| CN203545784U (en) | Combined type oxidation ditch with external sedimentation basin | |
| CN103508519B (en) | Free-replacement iron-carbon micro-electrolysis water treatment device | |
| CN203582658U (en) | Multi-stage aeration reclaimed water treatment system for medium and small towns | |
| CN204022633U (en) | A kind of residual sludge reduction treatment unit | |
| CN208700849U (en) | A kind of integration MBR sewage-treatment plant | |
| CN103351058A (en) | Pre-acidification anaerobic UASB treatment device and method for sewage | |
| CN207072839U (en) | Catalytic ozonation pilot-plant | |
| CN207210064U (en) | Internal-circulation type biofilter anaerobic reactor | |
| CN203007037U (en) | Internal mixing anaerobic reactor | |
| CN204897529U (en) | STREAMING anaerobic sludge bed reactor in two backward flows | |
| CN205328812U (en) | Festival ground type treatment of domestic sewage integrated device | |
| CN203319762U (en) | Self-circulation anaerobic reactor | |
| CN105585118A (en) | Gas expanded granular sludge bed anaerobic reactor | |
| CN203639204U (en) | Change-free iron-carbon micro-electrolytic water treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: FUJIAN QINRONG ENVIRONMENTAL PROTECTION TECHNOLOGY Free format text: FORMER NAME: FUZHOU QINRONG ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: The New District New Town District Fuzhou Fujian province 350012 Building 1 unit 804 Patentee after: Fujian Environmental Protection Technology Co., Ltd. Rong Qin Address before: The New District New Town District Fuzhou Fujian province 350012 Building 1 unit 804 Patentee before: FUZHOU QINRONG ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141022 Termination date: 20180429 |