SU733514A3 - Method of purification of waste liquor - Google Patents

Method of purification of waste liquor Download PDF

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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
Application number
SU741995248A
Other languages
Russian (ru)
Inventor
Ян Фонтейн Фреерк
Францискус Иеннекенс Губертус
Original Assignee
Стамикарбон Н.Ф. (Фирма)
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Стамикарбон Н.Ф. (Фирма) filed Critical Стамикарбон Н.Ф. (Фирма)
Application granted granted Critical
Publication of SU733514A3 publication Critical patent/SU733514A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1257Oxidation ditches
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/234Surface aerating
    • B01F23/2341Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
    • B01F23/23413Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere using nozzles for projecting the liquid into the gas atmosphere
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/20Jet mixers, i.e. mixers using high-speed fluid streams
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1278Provisions for mixing or aeration of the mixed liquor
    • C02F3/1294"Venturi" aeration means
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/50Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological 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

1458302 Waste water aeration STAMICARBON BV 25 Jan 1974 [29 Jan 1973] 03656/74 Heading B1C In a process and apparatus for the aeration of waste water containing suspended biologically active sludge, jets of recycled water are directed at an angle of not greater than 60‹ and at a velocity of from 3 to 12 metres/ second onto the surface of the waste water which is contained in a basin of circular, elliptical or regular polygonal horizontal crosssection, whereby aeration of the water and a rotary flow Vr is produced. In Fig. 1, two tubes 2, 3 having outflow openings 6 direct the jets of water onto the waste water in circular basin 1. Untreated water is introduced at 4 and treated water leaves at 5 while pump units 7 draw water from the basin and feed it to the tubes. In Fig. 2 the pump units include an impeller 11 driven by motor 13. Some of openings 6 may be blanked off to vary the output and the angle of the jets may be varied in an arrangement of relatively rotatable apertured pipes 100, 104 shown in Fig. 3. The output of the jets may be varied by changing the speed of motor 13.

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)

Опыты 7-11 были приведены дл  сра нени , Данные экспериментальных исследований предложенного способа показали Значительное повышение эффективности очистки сточных вод в указанных пределах угла подачи и скорости полачи струй аэрирующей воды. Формула изобретени  Способ очистки сточных вод, содержагдий активный ил в виде суспензии , в аэротенке цилиндрической формы путем аэрации их стру ми воды, направленными под углом к поверхности сточной воды в аэротенке, отличающийс  тем, что, с целью повышени  эффективности процесса воду подают под углом 10-60 со скоростью 3-12 м/с в направлении основного потока воды в аэротенке. Источники информации, прин тые во внимание при экспертизе 1,Шишкин З.Н. и др. Канализаци . М,, 1960, с.425-426, 2,Патент ЩР № 56763, клЛ2 е 4/01, 05.05.72 (прототип).Experiments 7-11 were given for comparison. The data of experimental studies of the proposed method showed a significant increase in the efficiency of wastewater treatment within the indicated limits of the feed angle and the speed of half of the streams of aerating water. DETAILED DESCRIPTION OF THE INVENTION Wastewater treatment method, containing activated sludge as a suspension, in a cylindrical aerotank by aeration with water jets directed at an angle to the surface of the waste water in the aeration tank, characterized in that water is fed at an angle of 10 to increase the process efficiency -60 at a speed of 3-12 m / s in the direction of the main flow of water in the aeration tank. Sources of information taken into account in the examination 1, Shishkin Z.N. and others. Sewers. M ,, 1960, pp.425-426, 2, Patent SCHR No. 56763, cll2 e 4/01, 05.05.72 (prototype).
SU741995248A 1973-01-29 1974-01-28 Method of purification of waste liquor SU733514A3 (en)

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)

* Cited by examiner, † Cited by third party
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

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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