SU733514A3 - Method of purification of waste liquor - Google Patents
Method of purification of waste liquor Download PDFInfo
- Publication number
- SU733514A3 SU733514A3 SU741995248A SU1995248A SU733514A3 SU 733514 A3 SU733514 A3 SU 733514A3 SU 741995248 A SU741995248 A SU 741995248A SU 1995248 A SU1995248 A SU 1995248A SU 733514 A3 SU733514 A3 SU 733514A3
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- water
- aeration
- jets
- angle
- waste water
- Prior art date
Links
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
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1257—Oxidation ditches
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/234—Surface aerating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/234—Surface aerating
- B01F23/2341—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
- B01F23/23413—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using nozzles for projecting the liquid into the gas atmosphere
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
-
- 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
- C02F3/12—Activated sludge processes
- C02F3/1278—Provisions for mixing or aeration of the mixed liquor
- C02F3/1294—"Venturi" aeration means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
-
- 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
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
Изобретение относитс к очистке сточных вод, содержащих активный ил в виде суспензии, в аэротенках с поверхностной аэрацией, конкретно в аэротенках цилиндрической формы. Известны способы очистки сточных вод, при которых поверхностна или механическа аэраци производитс с помопцью вертикальных или горизонтальных щеток, либо пропеллерными ме шалкалда, которые одновременно осуществл ют перемешивание сточной воды с активным клон 1 , Энергетические затраты при исполь зовании данных способов очистки велики ,, Известен способ очистки сточных , вод, включающий их аэрацию и перемешивание стру ми вода подаваемыми под углом к поверхности сточных вод в аэротенке цилиндрической форм 12. Одна1;о использование данного спо соба, хот и обеспечивает хорошую аэрацию сточных вод, но требует допа нительного механического устройства дл перемешивани сточной воды с активным илом что значительно повы шает экономические затраты и снижает эффективность процесса. Целью изобретени вл етс повышение зффективнос ти процесса. Дл достижени поставленной цели угол подачи струй аэрирующей воды составл ет 10-60°, а скорость подачи 3-12 м/с, причем направление подачи аэрирующей воды и основного потока воды в аэротенке совпадают.. На фиг.1 изображен аэротенк, вид сверху; на фиг.2 - разрез А-А фиг.1. Аэротенк 1 имеет цилиндрическую форму и снабжен трубопроводами 2-4 соответственно дл подачи аэрирующей воды, подачи сточных вод и отвода очищенной воды. На трубопроводе 2 дл подачи аэрирующей воды выполнены регулируемые отверсти 5. Позици УН обозначает направление основного потока воды в аэротенке. Струи аэрирующей воды подаютс из отверстий 5, расположенных на некоторой высоте над поверхностью воды в аэротенке, и образуют определенный угол относительно поверхности очищаемой воды. Количество вводимого кислорода обусловлено этим углом и регулируетс посредством изменени положени выходного отверсти 5. Чем вы е выходна скорость вод ных струй, тем интенсивнее проходитThe invention relates to the treatment of wastewater containing activated sludge in the form of a suspension, in aerotanks with surface aeration, specifically in cylindrical aerotanks. Wastewater treatment methods are known, in which surface or mechanical aeration is carried out with the help of vertical or horizontal brushes or propeller arms, which simultaneously mix wastewater with an active clone 1, Energy costs when using these cleaning methods are large, wastewater treatment, including their aeration and jet mixing with water supplied at an angle to the surface of the wastewater in the aeration tank of cylindrical forms 12. One; Nogo method exists, although provides good aeration of sewage, but requires dopa tional mechanical device for mixing the waste water with activated sludge which significantly povy creases economic costs and reduces process efficiency. The aim of the invention is to increase the efficiency of the process. To achieve this goal, the angle of the jet of aerating water is 10-60 °, and the feed rate is 3-12 m / s, and the direction of the supply of aerating water and the main flow of water in the aeration tank coincide. figure 2 - section aa of figure 1. Aerotank 1 has a cylindrical shape and is equipped with pipelines 2-4, respectively, for supplying aerating water, supplying wastewater and draining purified water. Adjustable apertures 5 are made on the pipeline 2 for supplying aeration water. The position of the CN indicates the direction of the main water flow in the aeration tank. The jets of aerating water are supplied from holes 5 located at a certain height above the surface of the water in the aeration tank and form a certain angle relative to the surface of the water to be purified. The amount of oxygen introduced is due to this angle and is regulated by changing the position of the outlet 5. The higher the output velocity of the water jets, the more intense the
процесс очистки. Однако пропорцис нально возрастают и энергетические затраты. Оптимальньгй диапазон скорос тей, при котором учитываютс энерго затраты, достаточное введение кис лорода и обеспечение интенсивногоcleaning process. However, energy costs also increase proportionally. The optimal speed range at which energy costs are taken into account, sufficient introduction of oxygen and ensuring intensive
перемешивани сточной воды с активны 4 илом лежит в пределах 3-12 м/сmixing waste water with active 4 sludge lies within 3-12 m / s
Влн ниё уг-ла подачи аэрирующей во,чы и скорости ее подачи на эффективность очистки приведены в таблице,The angle of the supply of aerating air, water and its feed rate to the cleaning efficiency is given in the table,
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL7301201.A NL163196C (en) | 1973-01-29 | 1973-01-29 | METHOD FOR AERATING WASTE WATER. |
Publications (1)
Publication Number | Publication Date |
---|---|
SU733514A3 true SU733514A3 (en) | 1980-05-05 |
Family
ID=19818099
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU741995248A SU733514A3 (en) | 1973-01-29 | 1974-01-28 | Method of purification of waste liquor |
Country Status (15)
Country | Link |
---|---|
JP (1) | JPS5636998B2 (en) |
AT (1) | AT335929B (en) |
BE (1) | BE810276A (en) |
CA (1) | CA1014283A (en) |
CH (1) | CH575886A5 (en) |
DD (1) | DD110028A5 (en) |
DE (1) | DE2404198C3 (en) |
ES (1) | ES422681A1 (en) |
FR (1) | FR2215398B1 (en) |
GB (1) | GB1458302A (en) |
IT (1) | IT1002785B (en) |
NL (1) | NL163196C (en) |
SE (1) | SE8000075L (en) |
SU (1) | SU733514A3 (en) |
ZA (1) | ZA74565B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4202762A (en) * | 1973-01-29 | 1980-05-13 | Stamicarbon, B.V. | Process and device for the aeration of waste water |
US4306968A (en) * | 1978-10-10 | 1981-12-22 | Mcneil Corporation | Sewage treatment system |
JPH0162897U (en) * | 1987-10-14 | 1989-04-21 | ||
JP3829472B2 (en) * | 1998-04-27 | 2006-10-04 | ブラザー工業株式会社 | Sewing needle holding device for sewing machine |
-
1973
- 1973-01-29 NL NL7301201.A patent/NL163196C/en not_active IP Right Cessation
-
1974
- 1974-01-24 CH CH100374A patent/CH575886A5/xx not_active IP Right Cessation
- 1974-01-25 AT AT62674*#A patent/AT335929B/en not_active IP Right Cessation
- 1974-01-25 GB GB365674A patent/GB1458302A/en not_active Expired
- 1974-01-28 ES ES422681A patent/ES422681A1/en not_active Expired
- 1974-01-28 CA CA191,048A patent/CA1014283A/en not_active Expired
- 1974-01-28 IT IT47976/74A patent/IT1002785B/en active
- 1974-01-28 ZA ZA740565A patent/ZA74565B/en unknown
- 1974-01-28 SU SU741995248A patent/SU733514A3/en active
- 1974-01-29 DE DE2404198A patent/DE2404198C3/en not_active Expired
- 1974-01-29 BE BE140270A patent/BE810276A/en not_active IP Right Cessation
- 1974-01-29 DD DD176246A patent/DD110028A5/xx unknown
- 1974-01-29 FR FR7402844A patent/FR2215398B1/fr not_active Expired
- 1974-01-29 JP JP1213774A patent/JPS5636998B2/ja not_active Expired
-
1980
- 1980-01-04 SE SE8000075A patent/SE8000075L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
AU6497274A (en) | 1975-07-31 |
FR2215398B1 (en) | 1979-04-06 |
NL163196C (en) | 1980-08-15 |
ZA74565B (en) | 1974-11-27 |
DE2404198A1 (en) | 1974-08-01 |
NL7301201A (en) | 1974-07-31 |
CH575886A5 (en) | 1976-05-31 |
BE810276A (en) | 1974-07-29 |
DE2404198B2 (en) | 1978-08-10 |
SE8000075L (en) | 1980-01-04 |
DE2404198C3 (en) | 1979-04-05 |
NL163196B (en) | 1980-03-17 |
IT1002785B (en) | 1976-05-20 |
FR2215398A1 (en) | 1974-08-23 |
CA1014283A (en) | 1977-07-19 |
DD110028A5 (en) | 1974-12-05 |
AT335929B (en) | 1977-04-12 |
ATA62674A (en) | 1976-07-15 |
JPS49105361A (en) | 1974-10-05 |
ES422681A1 (en) | 1976-04-01 |
GB1458302A (en) | 1976-12-15 |
JPS5636998B2 (en) | 1981-08-27 |
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