CN205204908U - Anaerobism, good oxygen series connection biochemical treatment test device - Google Patents
Anaerobism, good oxygen series connection biochemical treatment test device Download PDFInfo
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- CN205204908U CN205204908U CN201521028366.6U CN201521028366U CN205204908U CN 205204908 U CN205204908 U CN 205204908U CN 201521028366 U CN201521028366 U CN 201521028366U CN 205204908 U CN205204908 U CN 205204908U
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Abstract
The utility model discloses an anaerobism, good oxygen series connection biochemical treatment test device, the utility model aims at providing a will you please can verify effectively that waste water treatment sets up normal operating, can verify whether reasonable anaerobism, good oxygen series connection biochemical treatment test device of design simultaneously, it includes anaerobic reactor and aerobic reaction ware, anaerobic reactor is hollow airtight structure, and it from bottom to top divides anaerobism granular sludge district and three -phase separation district in proper order into, is equipped with the water inlet in the bottom that anaerobism granular sludge distinguished, is equipped with the gas outlet at the top that three -phase separation distinguished, and the edge of following the gas outlet upwards extends has the round lateral wall, is equipped with the delivery port on the lateral wall that three -phase separation distinguished, the aerobic reaction ware is hollow structure, cuts apart into carrier thermopnore reaction tank, activated sludge reaction tank and two heavy ponds through two baffles in proper order with the inner space of aerobic reaction ware, it has easy operation, can effectively realize characteristics such as waste water treatment.
Description
Technical field
The utility model relates to a kind of wastewater treatment test device, particularly relates to a kind of anaerobism, aerobic series connection biochemical treatment testing apparatus.
Background technology
Aerobic/anaerobic series connection biochemical process is one of the technological line processing high-level efficiency that high concentrated organic wastewater generally adopts, low cost at present.But, for a certain specific waste water, the feasibility of its aerobic/anaerobic series connection biochemical treatment and treatment effect often need to be verified by test test before technological design and construction, and the design variable of waste water treatment process also needs to provide referential data by test test.So to be tested actual waste water by aerobic/anaerobic tandem test device and just seem particularly important, can avoid building up rear waste water disposal facility like this can not normally run, or because designing unreasonable and wasting the problem of resource.Therefore be badly in need of a kind of testing apparatus effectively verifying this design rationality before manufacture.
Utility model content
Whether reasonably the purpose of this utility model is to overcome the deficiencies in the prior art, and can waste water disposal facility normally run to provide one effectively to verify, can verify design anaerobism, aerobic series connection biochemical treatment testing apparatus simultaneously.
In order to achieve the above object, the anaerobism designed by the utility model, aerobic series connection biochemical treatment testing apparatus, it comprises anaerobic reactor and aerobic reactor; Described anaerobic reactor is hollow closed structure, it is from bottom to top divided into anaerobic grain sludge district and three-phase separation area successively, the medullary ray in Qie Liangge district on the same line, water-in is provided with in the bottom in anaerobic grain sludge district, air outlet is provided with at the top of three-phase separation area, edge along air outlet is upwards extended with a circle sidewall, and the sidewall of three-phase separation area is provided with water outlet; Gas skirt, vapor pipe is provided with in described three-phase separation area, described gas skirt is inverted funnel-form, one end of vapor pipe is connected with air outlet, one end that the other end is little with gas skirt opening is connected, large one the rectifying anaerobic grain sludge district of gas skirt opening, and the bore of the port of the large one end of gas skirt opening is greater than the bore in anaerobic grain sludge district; Described aerobic reactor is the cavity of opening upwards, by two dividing plates, the internal space of aerobic reactor is divided into carrier current movable bed reaction tank, activated sludge reaction pond and second pond successively; Carrier current movable bed reaction tank is provided with water-in, and the water outlet of this water-in and three-phase separation area passes through tubes connection; Dividing plate between described carrier current movable bed reaction tank and activated sludge tank is provided with through hole, and be equipped with aeration head in the bottom of carrier current movable bed reaction tank and activated sludge tank, aeration head is connected with air compressor by aerating pipelines; Dividing plate between described second pond and activated sludge tank is also provided with through hole, the sidewall of second pond is provided with water port, in settling tank, a platform is extended with along the least significant end of water port, upwards be extended with a circle sidewall along flat edge of table, the sidewall of this sidewall and settling tank forms the semi-closed structure of an opening upwards; Be connected by mud return line between described second pond with carrier current movable bed reaction tank, mud return line is provided with reflux pump.
In order to make waste water water distribution more even when entering anaerobic reactor, the water-in in described anaerobic grain sludge district is connected with water distributor.
In order to make more thorough at anaerobic reactor internal oxidition of waste water, described anaerobic grain sludge district accounts for the 1/3-2/3 of anaerobic reactor height overall.
For the ease of process for processing, described anaerobic reactor and aerobic reactor all adopt plastic material to make.
Anaerobism of the present utility model, aerobic series connection biochemical treatment testing apparatus, for a certain specific waste water, waste water enters through the water-in of anaerobic reactor, aerobic reaction pond is entered by the water-in after anaerobic reaction on carrier current movable bed reaction tank, through carrier current movable bed reaction tank, activated sludge reaction pond, waste water is carried out aerobic reaction, then enter second pond to precipitate, finally the waste water after aerobic reaction is discharged, then analyzing and testing is carried out to this reacted waste water.
Therefore, it have simple to operate, effectively can realize the features such as wastewater treatment.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is further described.
As shown in Figure 1, the anaerobism designed by the utility model the utility model, aerobic series connection biochemical treatment testing apparatus, it comprises anaerobic reactor and aerobic reactor; Described anaerobic reactor is hollow closed structure, it is from bottom to top divided into anaerobic grain sludge district 1 and three-phase separation area 2 successively, the medullary ray in Qie Liangge district on the same line, water-in 4 is provided with in the bottom in anaerobic grain sludge district 1, air outlet 5 is provided with at the top of three-phase separation area 2, edge along air outlet 5 is upwards extended with a circle sidewall, and the sidewall of three-phase separation area 2 is provided with water outlet 6; Gas skirt 7, vapor pipe 8 is provided with in described three-phase separation area 2, described gas skirt 7 is in inverted funnel-form, one end of vapor pipe 8 is connected with air outlet 5, one end that the other end is little with gas skirt 7 opening is connected, large one the rectifying anaerobic grain sludge district 1 of gas skirt 7 opening, and the bore of the port of the large one end of gas skirt 7 opening is greater than the bore in anaerobic grain sludge district 1; Described aerobic reactor is the cavity of opening upwards, by two dividing plates 9, the internal space of aerobic reactor is divided into carrier current movable bed reaction tank 10, activated sludge reaction pond 11 and second pond 12 successively; Carrier current movable bed reaction tank 10 is provided with water-in 13, and this water-in 13 is connected by conduit 14 with the water outlet 5 of three-phase separation area 2; Dividing plate 8 between described carrier current movable bed reaction tank 10 and activated sludge tank 11 is provided with through hole, is equipped with aeration head 15 in the bottom of carrier current movable bed reaction tank 10 and activated sludge tank 11, and aeration head 15 is connected with air compressor 17 by aerating pipelines 16; Dividing plate 8 between described second pond 12 and activated sludge tank 11 is also provided with through hole, the sidewall of second pond 12 is provided with water port 3, in settling tank 12, a platform is extended with along the least significant end of water port 3, upwards be extended with a circle sidewall along flat edge of table, the sidewall of this sidewall and settling tank 12 forms the semi-closed structure of an opening upwards; Be connected by mud return line between described second pond 12 with carrier current movable bed reaction tank 10, mud return line is provided with reflux pump.
Claims (4)
1. anaerobism, an aerobic series connection biochemical treatment testing apparatus, is characterized in that: it comprises anaerobic reactor and aerobic reactor; Described anaerobic reactor is hollow closed structure, it is from bottom to top divided into anaerobic grain sludge district and three-phase separation area successively, the medullary ray in Qie Liangge district on the same line, water-in is provided with in the bottom in anaerobic grain sludge district, air outlet is provided with at the top of three-phase separation area, edge along air outlet is upwards extended with a circle sidewall, and the sidewall of three-phase separation area is provided with water outlet; Gas skirt, vapor pipe is provided with in described three-phase separation area, described gas skirt is inverted funnel-form, one end of vapor pipe is connected with air outlet, one end that the other end is little with gas skirt opening is connected, large one the rectifying anaerobic grain sludge district of gas skirt opening, and the bore of the port of the large one end of gas skirt opening is greater than the bore in anaerobic grain sludge district; Described aerobic reactor is the cavity of opening upwards, by two dividing plates, the internal space of aerobic reactor is divided into carrier current movable bed reaction tank, activated sludge reaction pond and second pond successively; Carrier current movable bed reaction tank is provided with water-in, and the water outlet of this water-in and three-phase separation area passes through tubes connection; Dividing plate between described carrier current movable bed reaction tank and activated sludge tank is provided with through hole, and be equipped with aeration head in the bottom of carrier current movable bed reaction tank and activated sludge tank, aeration head is connected with air compressor by aerating pipelines; Dividing plate between described second pond and activated sludge tank is also provided with through hole, the sidewall of second pond is provided with water port, in settling tank, a platform is extended with along the least significant end of water port, upwards be extended with a circle sidewall along flat edge of table, the sidewall of this sidewall and settling tank forms the semi-closed structure of an opening upwards; Be connected by mud return line between described second pond with carrier current movable bed reaction tank, mud return line is provided with reflux pump.
2. a kind of anaerobism according to claim 1, aerobic series connection biochemical treatment testing apparatus, is characterized in that: the water-in in described anaerobic grain sludge district is connected with water distributor.
3. a kind of anaerobism according to claim 1, aerobic series connection biochemical treatment testing apparatus, is characterized in that: described anaerobic grain sludge district accounts for the 1/3-2/3 of anaerobic reactor height overall.
4. a kind of anaerobism according to claim 1, aerobic series connection biochemical treatment testing apparatus, is characterized in that: described anaerobic reactor and aerobic reactor all adopt plastic material to make.
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CN201521028366.6U CN205204908U (en) | 2015-12-14 | 2015-12-14 | Anaerobism, good oxygen series connection biochemical treatment test device |
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CN201521028366.6U CN205204908U (en) | 2015-12-14 | 2015-12-14 | Anaerobism, good oxygen series connection biochemical treatment test device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107473381A (en) * | 2017-09-13 | 2017-12-15 | 安徽有余跨越瓜蒌食品开发有限公司 | A kind of aerobic-anaerobic Assembled tea polyphenol production wastewater treatment system |
CN110467314A (en) * | 2019-08-14 | 2019-11-19 | 浙江巨能环境工程有限公司 | A kind of the anaerobic-aerobic high-efficient treatment device and processing method of high-concentration formaldehyde wastewater |
-
2015
- 2015-12-14 CN CN201521028366.6U patent/CN205204908U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107473381A (en) * | 2017-09-13 | 2017-12-15 | 安徽有余跨越瓜蒌食品开发有限公司 | A kind of aerobic-anaerobic Assembled tea polyphenol production wastewater treatment system |
CN110467314A (en) * | 2019-08-14 | 2019-11-19 | 浙江巨能环境工程有限公司 | A kind of the anaerobic-aerobic high-efficient treatment device and processing method of high-concentration formaldehyde wastewater |
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Address after: 314500 No. 1500 rice road, Indus street, Tongxiang, Zhejiang Patentee after: Zhejiang Juneng Environmental Engineering Co Ltd Address before: 314500, No. 1500 rice road, Indus street, Tongxiang, Zhejiang, Jiaxing Patentee before: ZHEJIANG JUNENG CO., LTD. |
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CP03 | Change of name, title or address |