CN204097285U - Biochemistry filtered process all-in-one - Google Patents
Biochemistry filtered process all-in-one Download PDFInfo
- Publication number
- CN204097285U CN204097285U CN201420518680.1U CN201420518680U CN204097285U CN 204097285 U CN204097285 U CN 204097285U CN 201420518680 U CN201420518680 U CN 201420518680U CN 204097285 U CN204097285 U CN 204097285U
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- pond
- aerobic pond
- basin
- tube
- clean water
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- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of biochemistry filtered process all-in-one, it is characterized in that, the inside of casing is anoxic pond, Aerobic Pond, tube settler, filtering basin, clean water basin and sludge sump by baffle interval, at the middle part of anoxic pond and Aerobic Pond and bottom, elastic filler and micro-hole aerator are installed respectively, inclined tube filler is located at the middle part of tube settler, filtrate is filled with in the bottom of filtering basin, be provided with roots blower in the side of casing, roots blower is linked together by pipeline and the micro-hole aerator be located at bottom anoxic pond and Aerobic Pond.By above setting, the utility model is a kind of high-efficiency sewage treatment technology combining membrane separation technique and filter in one, due to biomembranous filteration, biology is trapped within bio-reactor completely, achieves hydraulic detention time and is separated with the thorough of sludge age.The utility model sewage treatment capacity is strong, and pollutants removal rate is high.
Description
Technical field
The utility model relates to a kind of sewage disposal device, is specifically a kind ofly to integrate pre-treatment, biochemical treatment, the biochemistry filtered process all-in-one of disposing of sewage continuously that filters.
Background technology
Current, for the integration apparatus of sewage disposal, for equalizing tank, anaerobic pond, Aerobic Pond, second pond integrative-structure, be difficult to remove impurity, suspended substance and the coliform in sewage at process medical waste water or the large life kitchen waste water of oleaginousness, need to add other utility appliance outward at body, just can reach the in line standard of national regulation, be unfavorable for the bookkeeping of construction and sewage disposal, need duplicate construction, waste land resources, reduces treatment effect simultaneously.
Summary of the invention
The purpose of this utility model is to provide one by all kinds for the treatment of facility in one, can adopt the efficient biochemical water technology that biotechnology combines with filtering technique.
To achieve these goals, the inside of the utility model casing is anoxic pond by baffle interval, Aerobic Pond, tube settler, filtering basin, clean water basin and sludge sump, at the middle part of anoxic pond and Aerobic Pond and bottom, elastic filler and micro-hole aerator are installed respectively, Aerobic Pond overflow weir and settling tank overflow weir is welded with in the upper side of Aerobic Pond and tube settler, the bottom of described Aerobic Pond overflow weir is connected with the side, bottom of tube settler by upflow tube, inclined tube filler is located at the middle part of tube settler, filtrate is filled with in the bottom of filtering basin, the bottom of filtering basin is connected with the bottom of clean water basin by closed tube, backwashing pump is located at the bottom of clean water basin, described backwashing pump is connected with the bottom of filtering basin by pipeline, rising pipe is located at the side, top of clean water basin, water inlet pipe is located at anoxic pond outer upper, roots blower is provided with in the side of casing, roots blower is linked together by pipeline and the micro-hole aerator be located at bottom anoxic pond and Aerobic Pond.
By above setting, the utility model is a kind of high-efficiency sewage treatment technology combining membrane separation technique and filter in one, due to biomembranous filteration, biology is trapped within bio-reactor completely, achieves hydraulic detention time and is separated with the thorough of sludge age.The utility model sewage treatment capacity is strong, and pollutants removal rate is high.
Accompanying drawing explanation
Existing composition graphs is described further the utility model.
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the vertical view of Fig. 1.
In figure: 1, casing, 2, anoxic pond, 3, Aerobic Pond, 4, tube settler, 5, filtering basin, 6, clean water basin, 7, sludge sump, 8, elastic filler, 9, micro-hole aerator, 10, Aerobic Pond overflow weir, 11, settling tank overflow weir, 12, upflow tube, 13, inclined tube filler, 14, filtrate, 15, closed tube, 16, backwashing pump, 17, rising pipe, 18, water inlet pipe, 19, roots blower.
Embodiment
As Fig. 1, 2, shown in, the inside of the utility model casing 1 is anoxic pond 2 by baffle interval, Aerobic Pond 3, tube settler 4, filtering basin 5, clean water basin 6 and sludge sump 7, at the middle part of anoxic pond 2 and Aerobic Pond 3 and bottom, elastic filler 8 and micro-hole aerator 9 are installed respectively, Aerobic Pond overflow weir 10 and settling tank overflow weir 11 is welded with in the upper side of Aerobic Pond 3 and tube settler 4, the bottom of described Aerobic Pond overflow weir 10 is connected with the side, bottom of tube settler 4 by upflow tube 12, inclined tube filler 13 is located at the middle part of tube settler 4, filtrate 14 is filled with in the bottom of filtering basin 5, the bottom of filtering basin 5 is connected with the bottom of clean water basin 6 by closed tube 15, backwashing pump 16 is located at the bottom of clean water basin 6, described backwashing pump 16 is connected by the bottom of pipeline with filtering basin 5, rising pipe 17 is located at the side, top of clean water basin 6, water inlet pipe 18 is located at anoxic pond 2 outer upper, roots blower 19 is provided with in the side of casing 1, roots blower 19 is linked together by pipeline and the micro-hole aerator 9 be located at bottom anoxic pond 2 and Aerobic Pond 3.
By above setting, sewage enters anoxic pond 2 and Aerobic Pond 3 from water inlet pipe 18 of the present utility model, open roots blower 19, gas enters micro-hole aerator 9 by pipeline and enters anoxic pond 2 and Aerobic Pond 3, the microorganism be suspended in elastic filler 8 utilizes air to be decomposed by the oxidation operation in sewage, and NO3-N and NO2-N denitrification is generated nitrogen, sewage overflows across Aerobic Pond overflow weir 10 and enters tube settler 4, sewage in tube settler 4 through inclined tube filler 13 precipitate after, overflowing across settling tank overflow weir 11 enters in filtering basin 5, sewage in filtering basin 5 through filtrate 14 filter after, clean water basin 6 are entered through closed tube 15, water in clean water basin 6 is discharged through rising pipe 17.When filtering basin 5 need back flushing, open backwashing pump 16, close the valve on closed tube 15, the clear water in clean water basin 6 can carry out back flushing to filtering basin 5 and tube settler 4.
Claims (1)
1. biochemistry filtered process all-in-one, it is characterized in that: the inside of casing is anoxic pond by baffle interval, Aerobic Pond, tube settler, filtering basin, clean water basin and sludge sump, at the middle part of anoxic pond and Aerobic Pond and bottom, elastic filler and micro-hole aerator are installed respectively, Aerobic Pond overflow weir and settling tank overflow weir is welded with in the upper side of Aerobic Pond and tube settler, the bottom of described Aerobic Pond overflow weir is connected with the side, bottom of tube settler by upflow tube, inclined tube filler is located at the middle part of tube settler, filtrate is filled with in the bottom of filtering basin, the bottom of filtering basin is connected with the bottom of clean water basin by closed tube, backwashing pump is located at the bottom of clean water basin, described backwashing pump is connected with the bottom of filtering basin by pipeline, rising pipe is located at the side, top of clean water basin, water inlet pipe is located at anoxic pond outer upper, roots blower is provided with in the side of casing, roots blower is linked together by pipeline and the micro-hole aerator be located at bottom anoxic pond and Aerobic Pond.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420518680.1U CN204097285U (en) | 2014-09-09 | 2014-09-09 | Biochemistry filtered process all-in-one |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420518680.1U CN204097285U (en) | 2014-09-09 | 2014-09-09 | Biochemistry filtered process all-in-one |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204097285U true CN204097285U (en) | 2015-01-14 |
Family
ID=52265730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420518680.1U Expired - Fee Related CN204097285U (en) | 2014-09-09 | 2014-09-09 | Biochemistry filtered process all-in-one |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204097285U (en) |
-
2014
- 2014-09-09 CN CN201420518680.1U patent/CN204097285U/en not_active Expired - Fee Related
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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: 20150114 Termination date: 20170909 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |