SU1625330A3 - Apparatus for aerating liquids - Google Patents

Apparatus for aerating liquids Download PDF

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Publication number
SU1625330A3
SU1625330A3 SU864027574A SU4027574A SU1625330A3 SU 1625330 A3 SU1625330 A3 SU 1625330A3 SU 864027574 A SU864027574 A SU 864027574A SU 4027574 A SU4027574 A SU 4027574A SU 1625330 A3 SU1625330 A3 SU 1625330A3
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SU
USSR - Soviet Union
Prior art keywords
rotor
stator
liquid
walls
aeration
Prior art date
Application number
SU864027574A
Other languages
Russian (ru)
Inventor
Эбнер Хайнрих
Original Assignee
Хайнрих Фрингс Гмбх Унд Ко, Кг (Фирма)
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Application filed by Хайнрих Фрингс Гмбх Унд Ко, Кг (Фирма) filed Critical Хайнрих Фрингс Гмбх Унд Ко, Кг (Фирма)
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Publication of SU1625330A3 publication Critical patent/SU1625330A3/en

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Classifications

    • 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
    • B01F23/233Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2334Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer
    • B01F23/23342Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer the stirrer being of the centrifugal type, e.g. with a surrounding stator

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

1. A device for aerating liquids comprising : a rotor (2) whose rotational axis is vertical and which is disposed near the bottom of a tank and which intakes air and liquid ; and a stator (4) which extends around the rotor (2) and has a closed ring of right-angled cross-section flow ducts (8) each having an entry for the liquid-air mixture, the flow ducts (8) being inclined relatively to the radial direction in the direction of rotation of the rotor (2), characterised in that the flow ducts (8) are separated from one another by wedge-shaped gaps whose vertices are disposed between the immediately adjacent inlets, and the vertical boundary surfaces of each flow duct (8) either extend parallel to one another or converge or diverge at an angle of at most 7 degrees.

Description

от параллельности не должно превышать 7°0 Предложенна  конструкци  обеспечивает равномерное перемешивание жидкости и газа и эффективную аэрацию в резервуарах увеличенного диаметра„ 6 ил0from parallelism should not exceed 7 ° 0. The proposed design ensures uniform mixing of liquid and gas and effective aeration in large-diameter tanks “6 or 0”

Изобретение относитс  к устройствам , предназначенным дл  внесени  и растворени  газа в жидкости.The invention relates to devices for introducing and dissolving a gas in a liquid.

Цель изобретени  - повышение эффективности аэрации за счет обеспечени  равномерного перемешивани  жидкости с газомоThe purpose of the invention is to increase the efficiency of aeration by ensuring uniform mixing of the liquid with gas.

На фиг01 изображено устройство дл  аэрации жидкости, вид сбоку в частичном разрезе, на фиг. 2 - статор устройства дл  аэрации, вид сверху с частичным разрезом; на фиг.3-разрез А-А на биг. 2 в увеличенном масштабе; на фиг04 - изображение П-образного проточного канала в поперечном сечении в увеличенном масштабе; на фиг.5 - горизонтальный разрез статора с расшир ющимис  наружу проточными каналами; на фиг.6 - горизонтальный разрез статора со сход щимис  наружу проточными каналами.FIG. 01 shows a device for aerating a liquid, side view in partial section; FIG. 2 shows the stator of the aeration device, a top view with a partial cut; Fig.3 is a section aa on big. 2 on an enlarged scale; on Fig image of the U-shaped flow channel in cross section on an enlarged scale; Fig. 5 is a horizontal section of the stator with outwardly expanding flow channels; Fig. 6 is a horizontal section of the stator with flow channels converging to the outside.

Устройство дл  аэрации размещено над дном 1 аэрационного резервуара и состоит из ротора 2, приводимого во вращение двигателем 3, и окружающего ротор 2 статора 40 Вертикальный вал 5 ротора проходит сквозь дно 1 резерву- ара, к которому фланцем крепитс  двигатель 3. Подлежащий вводу в жидкость воздух через воздухопровод 6 засасываетс  сверху и соосно подводитс  к ротору 2, который через сквозное ак- сиальное отверстие 7 статора 4 одновременно засасывает и жидкость гиз резервуара. Вместе с воздухом жидкость поступает в статор.The aeration device is located above the bottom 1 of the aeration tank and consists of a rotor 2 driven by the motor 3 and the stator rotor 2 surrounding the rotor 40. The vertical rotor shaft 5 passes through the bottom 1 of the tank to which the flange 3 is attached. air through the air duct 6 is sucked in from above and coaxially supplied to the rotor 2, which through the axial through hole 7 of the stator 4 simultaneously sucks the fluid from the tank. Together with the air, the liquid enters the stator.

В статоре 4 смесь жидкости с воз- духом попадает в проточные каналы 8, которые согласно фиг.1-3 образованы вертикальными стенками 9, которые вставлены между кольцевыми дисками 10 и 11. Вертикальные стенки 9 со- седних проточных каналов 8 либо расход тс  в направлении внешней окружности статора 4, либо сужаютс , либо параллельны друг другу. Такое выполнение дает примерно одинаковую входную скорость смеси жидкости с воздухом из ротора 2 в статор 4 и соответствующую выходную скорость потока из проточных каналов 8.In the stator 4, the mixture of fluid with air enters the flow channels 8, which, according to FIGS. 1-3, are formed by vertical walls 9, which are inserted between the annular disks 10 and 11. The vertical walls 9 of the adjacent flow channels 8 or diverge in the direction the outer circumference of the stator 4, either narrowed or parallel to each other. This embodiment provides approximately the same input speed of the mixture of liquid with air from the rotor 2 into the stator 4 and the corresponding output flow rate from the flow channels 8.

Как показано на фиг.4, особо проста  конструкци  статора может быть получена за счет того, что проточные каналы 8 образованы П-образными профил ми 12, которые установлены на кольцевом диске 13, Така  конструкци  обеспечивает не только простое изготовление, но также дает преимущество при очистке статора, так как клиновидные области между соседними проточными каналами  вл ютс  легкодоступными .As shown in FIG. 4, an especially simple stator structure can be obtained due to the fact that the flow channels 8 are formed by U-shaped profiles 12, which are mounted on an annular disk 13. Such a construction provides not only simple manufacturing, but also gives an advantage when cleaning the stator, since the wedge-shaped areas between adjacent flow channels are easily accessible.

Чтобы можно было задать необходимую дл  аэрации в резервуаре определенного диаметра выходную скорость смеси жидкости с воздухом из статора при имеющейс  мощности на роторе, ветикальные ограничительные стенки отдельных проточных каналов 8 выполн ютс  не только параллельными. Если, например, стенки 9 отдельных проточных каналов 8 выполнены расход щимис  к внешней окружноет статора 4, т получаетс  замедление потока в каналах 8о Угол oi между вертикальными стенками 9 при этом не должен превышать 7°, так как в противном случае можно ожидать повышенной турбулентности и меньшей дальности вытекающего из каналов 8 потока,,In order to be able to set the output speed of the mixture of fluid with air from the stator with available power on the rotor for aeration in a tank of a certain diameter, the limiting walls of the individual flow channels 8 are not only parallel. If, for example, the walls 9 of the individual flow channels 8 are made diverging to the outer circumference of the stator 4, the flow is slowed down in the channels 8o. The angle oi between the vertical walls 9 should not exceed 7 °, since otherwise you can expect increased turbulence and shorter range of flow from channel 8

Если нужно повысить скорость потока в области внешней окружности статора 4 относительно входной скорости , то стенки 9 выполнены суженными в направлении наружу, как это показано на фиг.6, и в этом случае угол об между вертикальными стенками 9 отдельных каналов должен быть огра1- ничен максимумом 7°.If it is necessary to increase the flow rate in the region of the outer circumference of the stator 4 relative to the input velocity, then the walls 9 are narrowed outwardly, as shown in Fig. 6, and in this case the angle between the vertical walls 9 of the individual channels should be limited by a maximum 7 °.

Устройство работает следующим образом .The device works as follows.

Ротор приводитс  во вращение двигателем 3, установленным над дном 1 резервуара с обрабатываемой жидкостью. Воздух поступает по воздуховоду 6, перемешиваетс  с жидкостью, котора  засасываетс  через отверстие 7. Смесь жидкость с воздухом или газом поступает в проточные каналы 8.The rotor is driven by a motor 3 mounted above the bottom 1 of the reservoir with the liquid to be treated. The air enters through the duct 6, mixes with the fluid that is sucked through the opening 7. The mixture of liquid with air or gas enters the flow channels 8.

Ограниченные вертикальными направл ющими стенками и пр моугольные вBounded by vertical guide walls and rectangular in

сечении проточные; каналы осуществл ют направленное выбрасывание смеси жидкости и воздуха в жидкость, подлежащую аэрации, и в области вокруг статора достигаетс  равномерна  аэраци  жидкости.flow sections; the channels make directional ejection of the mixture of liquid and air into the liquid to be aerated, and uniform aeration of the liquid is achieved in the area around the stator.

Вследствие сравнительно высокой выходной скорости потока равномерна  аэраци  может быть достигнута в резервуарах увеличенного диаметра.Due to the relatively high output flow rate, uniform aeration can be achieved in tanks of increased diameter.

Claims (1)

Формула изобретени Invention Formula Устройство дл  аэрации жидкостей, содержащее ротор с вертикальной осью вращени  и трубопроводом дл  подводаA device for the aeration of liquids containing a rotor with a vertical axis of rotation and a pipeline for supplying А-АAa ФигЗFigz воздуха, окружающий ротор статора в виде кольцевого диска и венца проточных каналов с вертикальными ограничительными стенками, расположенных вокруг сквозного аксиального отверсти , отличающеес  тем, что, с целью повышени  эффективности аэрации путем обеспечени  равномерного перемешивани  жидкости с газом, проточные каналы выполнены либо с параллельными одна другой стенками, либо со стенками, имеющими расширение или сужение максимально с пр моугольным поперечным сечением и расположены на статоре с расхождением к его наружной кромке.air surrounding the stator rotor in the form of an annular disk and a crown of flow channels with vertical restrictive walls located around the axial through hole, characterized in that, in order to increase the efficiency of aeration by ensuring uniform mixing of the liquid with the gas, the flow channels are either parallel to each other walls, or with walls having an expansion or contraction as much as possible with a rectangular cross section and located on the stator with a divergence to its outer edge kyo. Фиг.IFig.i 1313 Фиг.44 №/г5No. / G5
SU864027574A 1985-06-05 1986-06-04 Apparatus for aerating liquids SU1625330A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT0169685A AT383108B (en) 1985-06-05 1985-06-05 VENTILATION DEVICE FOR LIQUIDS

Publications (1)

Publication Number Publication Date
SU1625330A3 true SU1625330A3 (en) 1991-01-30

Family

ID=3519010

Family Applications (1)

Application Number Title Priority Date Filing Date
SU864027574A SU1625330A3 (en) 1985-06-05 1986-06-04 Apparatus for aerating liquids

Country Status (10)

Country Link
EP (1) EP0204688B2 (en)
JP (1) JPS6244167A (en)
CN (1) CN86103733A (en)
AT (1) AT383108B (en)
BR (1) BR8602601A (en)
DE (1) DE3616680A1 (en)
ES (1) ES8703748A1 (en)
FI (1) FI88262C (en)
IN (1) IN165315B (en)
SU (1) SU1625330A3 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2718649C2 (en) * 2015-10-19 2020-04-10 Сосьете Де Продюи Нестле С.А. Apparatus and method for aeration of a food product
RU2802517C2 (en) * 2019-12-25 2023-08-30 Общество С Ограниченной Ответственностью "Сибводразработка" Multi-nozzle vacuum ejection device

Families Citing this family (9)

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Publication number Priority date Publication date Assignee Title
JPH0717440Y2 (en) * 1988-05-18 1995-04-26 株式会社荏原製作所 Mixing / aeration device
DE4207077C2 (en) * 1991-03-07 1997-07-03 Horst Adler Compact wastewater treatment plant with special sludge return element
FI91242C (en) * 1992-07-17 1994-06-10 Outokumpu Mintec Oy The aerator
AT398046B (en) * 1992-09-10 1994-08-25 Frings & Co Heinrich DEVICE FOR ENTERING GAS IN LIQUIDS
DE9316251U1 (en) * 1993-10-25 1994-02-10 Charatjan, Manuela, 76332 Bad Herrenalb Device for stirring or for stirring and simultaneously gassing liquids, suspensions and heterogeneous fluids
DE19519553C2 (en) * 1995-05-27 1997-04-24 Michael Dipl Ing Godzik Centrifugal aerator for introducing a gas into a liquid
DE102009044168A1 (en) 2009-10-02 2011-04-07 Green Finance Ag Process and apparatus for the continuous production of alkyl esters of higher fatty acids
CN102921320A (en) * 2012-11-05 2013-02-13 无锡托普搅拌设备有限公司 Gas-liquid dispersion stirrer
WO2020213048A1 (en) * 2019-04-15 2020-10-22 エム・テクニック株式会社 Stirrer

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AT269083B (en) * 1966-04-05 1969-03-10 Frings Fa Heinrich Aerating device for liquids
US3690621A (en) * 1969-03-04 1972-09-12 Itsuko Tanaka Agitator
NO142830C (en) * 1978-02-28 1980-10-29 Trondhjems Mek Verksted As DEVICE FOR DISTRIBUTING A GAS IN A FLUID MEDIUM
FR2444494A1 (en) * 1978-12-21 1980-07-18 Jeumont Schneider Aeration of waste water - by submerged, vertical flow pump into which compressed air is injected from stationary supply system
DE2907257C2 (en) * 1979-02-24 1982-04-22 Ukrainskij Naucno-Issledovatel'skij Uglechimiceskij Institut, Charkov Device for ventilating turbidity
JPS5823036U (en) 1981-07-31 1983-02-14 パイオニア株式会社 tape recorder

Non-Patent Citations (1)

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Title
Патент Австрии Р 269083, кл. 12 d 1/03, 1969. *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2718649C2 (en) * 2015-10-19 2020-04-10 Сосьете Де Продюи Нестле С.А. Apparatus and method for aeration of a food product
RU2802517C2 (en) * 2019-12-25 2023-08-30 Общество С Ограниченной Ответственностью "Сибводразработка" Multi-nozzle vacuum ejection device

Also Published As

Publication number Publication date
ES8703748A1 (en) 1987-03-01
FI88262C (en) 1993-04-26
ES555750A0 (en) 1987-03-01
EP0204688A3 (en) 1988-06-22
IN165315B (en) 1989-09-16
DE3616680A1 (en) 1986-12-11
EP0204688A2 (en) 1986-12-10
FI862145A (en) 1986-12-06
CN86103733A (en) 1986-12-17
EP0204688B2 (en) 1992-11-11
DE3616680C2 (en) 1989-05-24
EP0204688B1 (en) 1990-01-03
AT383108B (en) 1987-05-25
JPS6244167A (en) 1987-02-26
FI88262B (en) 1993-01-15
ATA169685A (en) 1986-10-15
BR8602601A (en) 1987-02-03
JPH0313866B2 (en) 1991-02-25
FI862145A0 (en) 1986-05-21

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