CN109502736B - Oxygenation system in river surge biochemical pollution control technology - Google Patents
Oxygenation system in river surge biochemical pollution control technology Download PDFInfo
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- CN109502736B CN109502736B CN201811637825.9A CN201811637825A CN109502736B CN 109502736 B CN109502736 B CN 109502736B CN 201811637825 A CN201811637825 A CN 201811637825A CN 109502736 B CN109502736 B CN 109502736B
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- Prior art keywords
- water
- water inlet
- water outlet
- oxygen
- cavity
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- 238000006213 oxygenation reaction Methods 0.000 title claims abstract description 30
- 238000005516 engineering process Methods 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 128
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000001301 oxygen Substances 0.000 claims abstract description 42
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 42
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 6
- 238000007789 sealing Methods 0.000 claims description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 5
- 241000894006 Bacteria Species 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 230000001546 nitrifying effect Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The invention discloses an oxygenation system in a river biochemical pollution control technology, which comprises a deep water oxygenation pool, wherein the deep water oxygenation pool is divided into a water inlet cavity and a water outlet cavity from top to bottom, the water inlet cavity and the water outlet cavity are communicated at the bottom, the water inlet cavity is positioned at the upstream of a river, the water outlet cavity is positioned at the downstream of the river, a water inlet is arranged at the top of the water inlet cavity, a water outlet is arranged at the top of the water outlet cavity, the water inlet is higher than the water outlet, an air supply pipe is inserted into the water inlet cavity, the air supply pipe is inserted into the bottom of the water inlet cavity, the air supply pipe is connected with an oxygen supply device, and an air outlet is arranged on the air supply pipe.
Description
Technical Field
The invention relates to an oxygenation system in river biochemical pollution control technology.
Background
River pollution control is a difficult problem puzzling local governments at all levels, and industry specialists try different pollution control modes to treat sewage, but the effect is very poor. In recent years, a new pollution control mode is adopted, and bacteria control is realized. Bacteria such as nitrifying bacteria are cultivated in a river water body, organic matters in the water body are decomposed by the bacteria such as nitrifying bacteria, the oxygen content of the water body is required to be sufficient for cultivating nitrifying bacteria, in order to improve the oxygen content of the water body, technicians can inject oxygen into the water body, oxygen bubbles can be absorbed by water in the process of floating up in the water body, so that the oxygenation effect is achieved, in general, the oxygen is discharged into the water body through small holes, micro bubbles smaller than 2mm can be generated, the mutual contact area of gas (oxygen), water and solid (active sludge microorganisms) is enlarged, the gas, liquid and solid mass transfer efficiency is high, but in the practical situation, because most of river depths are shallow, the rising path of the oxygen bubbles is too short after entering the water body, the water body is not enough to absorb the air bubbles, the bubbles are already rising to the water surface, the test results show that the oxygen is introduced in the depth of 1M, the oxygen utilization rate is only 16%, and the oxygen utilization rate can reach 80% in the depth of 5M, so that the depth of water is deeper, and the oxygen utilization rate is higher. In order to enable the water body to absorb enough oxygen and enable the oxygen content to be enough, technicians can increase the depth of the water body and prolong the ascending path of oxygen bubbles by digging a deep river bed, but the mode is large in engineering and high in cost. The supply of pure oxygen is increased by technicians, so that the water body absorbs enough oxygen, but the consumption of oxygen is huge, the waste is serious, and the pollution control cost is increased.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide an oxygenation system in river biochemical pollution control technology.
The invention aims at being realized by the following technical scheme: the oxygenation system in the river biochemical pollution control technology comprises a deep water oxygenation pool, wherein the deep water oxygenation pool is divided into a water inlet chamber and a water outlet chamber from top to bottom, the water inlet chamber and the water outlet chamber are communicated with each other at the bottom, the water inlet chamber is positioned at the upstream of the river, the water outlet chamber is positioned at the downstream of the river, a water inlet is arranged at the top of the water inlet chamber, a water outlet is arranged at the top of the water outlet chamber, the height of the water inlet is higher than that of the water outlet, an air supply pipe is inserted into the water inlet chamber, the air supply pipe is inserted to the bottom of the water inlet chamber, the air supply pipe is connected with an oxygen supply device, and an air outlet is arranged on the air supply pipe; a bubble refiner is arranged at the bottom of the air supply pipe.
The top of the deepwater oxygenation pool is provided with a sealing cover, an oxygen collecting pipe is arranged on the sealing cover and used for feeding oxygen into deepwater oxygenation Chi Nacha, and the other end of the oxygen collecting pipe is connected with an air inlet of the oxygen supply device.
After adopting this technical scheme, compare with prior art, this technical scheme has following advantage: by adding the deep water oxygenation pool with deeper depth on the riverbed and controlling the water flow path to pass through the bottom of the deep water oxygenation pool, the rise time and the residence time of oxygen bubbles in the water are increased, favorable conditions are created for absorbing oxygen to the water, even a saturated state can be achieved, the cost is low, and the effect is obvious.
Drawings
FIG. 1 is a block diagram of an oxygenation system in a river biochemical pollution control technology of the invention.
Detailed Description
The present technology is further described below with reference to the accompanying drawings.
The oxygenation system in the river biochemical pollution control technology of the embodiment comprises a deep water oxygenation pool 1, wherein the deep water oxygenation pool 1 is divided into a water inlet chamber 11 and a water outlet chamber 12 from top to bottom, the water inlet chamber 11 and the water outlet chamber 12 are communicated at the bottom, the water inlet chamber 11 is positioned at the upstream a of the river, the water outlet chamber 12 is positioned at the downstream b of the river, a water inlet 13 is arranged at the top of the water inlet chamber 11, a water outlet 14 is arranged at the top of the water outlet chamber 12, the water inlet 13 is higher than the water outlet 14, river water can naturally flow into the water inlet chamber 11 and flow out of the water outlet chamber 12, an air supply pipe 2 is inserted into the water inlet chamber 11, the air supply pipe 2 is connected with an oxygen supply device, the oxygen supply device of the embodiment is an oxygen pump 3, a bubble refiner 4 is arranged at the bottom of the air supply pipe 2, a large number of air outlets are designed by the bubble refiner 4, and oxygen bubbles are refined as far as possible, so that the oxygen is absorbed by a water body. The top of the deep water oxygenation pool 1 is provided with a sealing cover 5, an oxygen collection pipe 6 is inserted into the deep water oxygenation pool 1 on the sealing cover 5, the other end of the oxygen collection pipe 6 is connected with an air inlet of an oxygen pump 3 (namely an oxygen supply device), the purpose of recycling redundant oxygen in the deep water oxygenation pool 1 is achieved, and the water level of a water inlet 13 and a water outlet 14 is required to be higher than the water levels of the two water inlets in use, so that oxygen is prevented from escaping from the water inlet 13 and the water outlet 14.
The deep water oxygenation pool 1 with deeper depth is inserted into the bottom of a river bed, the deep water oxygenation pool 1 can be inserted by piling, the cost is low, the depth of the river bed is artificially and locally increased, river water flows into the water inlet chamber 11 from the water inlet of the upstream a, the water flow in the water inlet chamber 11 flows from top to bottom, as shown by an arrow in fig. 1, then flows into the water outlet chamber 12 through the water inlet chamber 11 and the channel 15 at the bottom of the water outlet chamber 12, flows from bottom to top in the water outlet chamber 12 Shui Liuchan, finally flows out from the water outlet 14 and enters the downstream b, pure oxygen is discharged from the bubble refiner 4 at the bottom of the air supply pipe 2 in the water inlet chamber 11, pure oxygen bubbles are divided into two moving conditions, the big bubbles can overcome the resistance of downward water flow of the water inlet chamber 11 and always rise, the big bubbles rise due to the fact that the depth of the deep water oxygenation pool 1 is enough, the small bubbles can be absorbed by the water body and flow along with the water flow, the big bubbles are longer than the big bubbles, the flow path needs to pass through the water inlet chamber 11 and the water outlet chamber 12, the pure oxygen can be absorbed by the small bubbles, the high oxygen can reach the best condition, the good oxygen cultivation effect can be achieved, the low cost is achieved, and the good environment is cultivated.
The above description is only of the preferred embodiment of the present invention, and is not intended to limit the present invention in any way. Any person skilled in the art can make many possible variations and modifications to the technical solution of the present invention or modifications to equivalent embodiments using the methods and technical contents disclosed above, without departing from the scope of the technical solution of the present invention. Therefore, all equivalent changes according to the shape, structure and principle of the present invention are covered in the protection scope of the present invention.
Claims (1)
1. An oxygenation system in river surge biochemical pollution control technology is characterized in that: the deep water oxygenation pool is divided into a water inlet cavity and a water outlet cavity from top to bottom, the water inlet cavity and the water outlet cavity are communicated at the bottom, the water inlet cavity is positioned at the upstream of a river, the water outlet cavity is positioned at the downstream of the river, a water inlet is arranged at the top of the water inlet cavity, a water outlet is arranged at the top of the water outlet cavity, the water inlet is higher than the water outlet, an air supply pipe is inserted into the water inlet cavity, the air supply pipe is inserted to the bottom of the water inlet cavity, the air supply pipe is connected with an oxygen supply device, and an air outlet is arranged on the air supply pipe; a bubble refiner is arranged at the bottom of the air supply pipe; a sealing cover is arranged at the top of the deepwater oxygenation pool, an oxygen collecting pipe is arranged on the sealing cover and used for feeding oxygen into deepwater oxygenation Chi Nacha, and the other end of the oxygen collecting pipe is connected with an air inlet of an oxygen supply device;
The flow path of river water in the oxygenation system is as follows: river water flows into the water inlet chamber from the upstream water inlet, flows from top to bottom in the water inlet chamber, then enters the water outlet chamber through the water inlet chamber and the channel at the bottom of the water outlet chamber, flows from bottom to top in the water outlet chamber Shui Liuchan, and finally flows out from the water outlet to downstream; pure oxygen is discharged from a bubble refiner at the bottom of an air supply pipe in the water inlet chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201811637825.9A CN109502736B (en) | 2018-12-29 | 2018-12-29 | Oxygenation system in river surge biochemical pollution control technology |
Applications Claiming Priority (1)
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CN201811637825.9A CN109502736B (en) | 2018-12-29 | 2018-12-29 | Oxygenation system in river surge biochemical pollution control technology |
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CN109502736A CN109502736A (en) | 2019-03-22 |
CN109502736B true CN109502736B (en) | 2024-04-30 |
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CN201811637825.9A Active CN109502736B (en) | 2018-12-29 | 2018-12-29 | Oxygenation system in river surge biochemical pollution control technology |
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CN114847220B (en) * | 2022-05-25 | 2023-06-06 | 佛山市弘峻水处理设备有限公司 | Solar full-automatic oxygenation ship for aquaculture |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06262195A (en) * | 1993-03-10 | 1994-09-20 | Takuma Co Ltd | Deep layer aeration tank |
JP2003088886A (en) * | 2001-09-19 | 2003-03-25 | Yokogawa Electric Corp | Method and device for increasing dissolved oxygen |
KR100617018B1 (en) * | 2006-05-03 | 2006-08-29 | 주식회사 건화엔지니어링 | Deep aeration tank with upward aeration facilities |
WO2013082059A2 (en) * | 2011-12-01 | 2013-06-06 | Praxair Technology, Inc. | Method and system for enhancing mass transfer in aeration/oxygenation systems |
CN106115950A (en) * | 2016-08-24 | 2016-11-16 | 郑晓宇 | A kind of over-saturation dissolved oxygen aerator |
CN209507721U (en) * | 2018-12-29 | 2019-10-18 | 佛山市弘峻水处理设备有限公司 | A kind of aeration system in creek biochemistry pollution treatment technology |
-
2018
- 2018-12-29 CN CN201811637825.9A patent/CN109502736B/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06262195A (en) * | 1993-03-10 | 1994-09-20 | Takuma Co Ltd | Deep layer aeration tank |
JP2003088886A (en) * | 2001-09-19 | 2003-03-25 | Yokogawa Electric Corp | Method and device for increasing dissolved oxygen |
KR100617018B1 (en) * | 2006-05-03 | 2006-08-29 | 주식회사 건화엔지니어링 | Deep aeration tank with upward aeration facilities |
WO2013082059A2 (en) * | 2011-12-01 | 2013-06-06 | Praxair Technology, Inc. | Method and system for enhancing mass transfer in aeration/oxygenation systems |
CN106115950A (en) * | 2016-08-24 | 2016-11-16 | 郑晓宇 | A kind of over-saturation dissolved oxygen aerator |
CN209507721U (en) * | 2018-12-29 | 2019-10-18 | 佛山市弘峻水处理设备有限公司 | A kind of aeration system in creek biochemistry pollution treatment technology |
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