US1526596A - Apparatus for treating liquids with gases - Google Patents

Apparatus for treating liquids with gases Download PDF

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Publication number
US1526596A
US1526596A US567225A US56722522A US1526596A US 1526596 A US1526596 A US 1526596A US 567225 A US567225 A US 567225A US 56722522 A US56722522 A US 56722522A US 1526596 A US1526596 A US 1526596A
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Prior art keywords
atomizer
gases
liquid
treating liquids
tank
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US567225A
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William E Greenawalt
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    • 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
    • B01F23/2331Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/81Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis the stirrers having central axial inflow and substantially radial outflow
    • 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
    • B01F23/2331Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements
    • B01F23/23311Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the introduction of the gas along the axis of the stirrer or along the stirrer elements through a hollow stirrer axis
    • 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
    • B01F23/2335Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the direction of introduction of the gas relative to the stirrer
    • B01F23/23352Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the direction of introduction of the gas relative to the stirrer the gas moving perpendicular to the axis of rotation
    • 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
    • B01F23/2336Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
    • B01F23/23362Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced under the stirrer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/111Centrifugal stirrers, i.e. stirrers with radial outlets; Stirrers of the turbine type, e.g. with means to guide the flow

Definitions

  • the invention has for its object the effective atomization, or fine subdivision, of gas in liquid, to accomplish certain results, as for example, the a plication of gas to liquids to facilitate esired chemical reactions, and in the flotation treatment of ores.
  • the invention may be considered as an improvement, or modification, of patents issued to William E. Greenawalt, No. 1,374,500; April 12. 1921'; No. 1,374,446, April 21, 1921: and No. 1,374,445, April 12, 1921.
  • FIG. 1 shows a vertical section of the apparatus in which the air, or gas, is introduced into the hollow rotary member through a hollow shaft:
  • Fig. 2 is a modification of Fig. 1, in which the air is introduced through a stationary pipe;
  • Fig. 3 is a horizontal section of the rotary gas distributor, or atomizer:-Fig. 4: a detail vertical section of the atomizer as shown in Fig. 1: and
  • Fig. 5 a detail vertical section of the atomizer as shown in Fig. 2.
  • 1 is a tank adapted to contain the liquid to be treated
  • 2 is a rotary atomizer suspended within the tank by means of the hollow shaft 3 and submerged in the liquid.
  • the atomizer has a hollow interior communicating with the hollow shaft, and is provided with dischar e passages 4 extending outwardly, prefera lv from the centrol portion toward the riphery.
  • These discharge passages are ormed by the curved vanes, or partitions, 5, and are adapted to discharge the g or gas n q r m he n r r 1922.
  • Serial No. 567,225 is adapted to discharge the g or gas n q r m he n r r 1922.
  • the air When the atomizer is rotated at a proper speed, the air will be sucked down through the hollow shaft. This speed will usually range from 250 to 800 R. P. M., depending tion 9 of the modified atomizer 7, through a stationary pipe 10, so arranged that air will flow into the interior of the atomizer either by suction, or by pressure from the outside, and liquid from the tank will flow into the interior of the atomizer through the annulus 12 formed by the pipe 10 and the lower portion 9 of the atomizer.
  • a tank adapted to contain liquid, a hollow rotary member journaled on a vertical axis suspended within the tank and submerged in the liquid, said rotary memher having discharge passages arranged so that two adjacent ischarge passages have a common partition and so that the outlet of one discharge passage is recessed relative to the common partition, said common partition of one discharge passage being adapted to deflectliquid away from the outlet of the other discharge passage and a tubular member adapted to deliver gas to the interior of said rotary member.
  • a tank adapted to contain liquid, a hollow rotary member journaled on a vertical axis suspended within the tank and submerged in the liquid, said rotary member having discharge passages with divergent partitions toward the outlets and with the outlets of the discharge passages arran ed so as to form a serrated periphery e rotary member, and atubular member adapted to deliver gas to the interior of said rotary member.
  • a tank adapted to contain liquid, a hollow rotary member journaled .on a vertical axis suspended within the tank and submerged in the liquid, said rotary memher having a serrated periphery and discharge passages arranged with divergent sides extending outwardly and terminating in the serrations, and a tubular member adapted to deliver eras to the interior of said rotary member.

Description

Feb. 17. 1925- 1,526,596
. w. E. GREENAWALT APPARATUS FOR TREATING LIQUIDS WITH GASES Filed June 9, 1922 Patented Feb. 17, 1925.
UNITED STATES PATENT OFFICE.
APPARATUS FOR TREATING LIQUIDS WITH'GASES.
Applicationiflled. June a,
To all whom it may concern:
Be it known that I, WILLIAM E. GREENA- WALT, a citizen of the United States, residing in the city and county of Denver and State of Colorado, have invented certain new and useful Improvements in Apparatus for Treating Liquids with Gases, of which the following is a specification.
The invention has for its object the effective atomization, or fine subdivision, of gas in liquid, to accomplish certain results, as for example, the a plication of gas to liquids to facilitate esired chemical reactions, and in the flotation treatment of ores.
The invention may be considered as an improvement, or modification, of patents issued to William E. Greenawalt, No. 1,374,500; April 12. 1921'; No. 1,374,446, April 21, 1921: and No. 1,374,445, April 12, 1921.
In the operation of the apparatus as described in the above patents, it was found that excellent results can be obtained under some conditions and for some purposes by the use of a serrated periphery of the hollow rotary gas distributor with gas discharge passages arranged so that their outlets terminate in the peripheral serrations.
The invention can best be described by referring to the accompanying drawings,
in which, Fig. 1 shows a vertical section of the apparatus in which the air, or gas, is introduced into the hollow rotary member through a hollow shaft: Fig. 2, is a modification of Fig. 1, in which the air is introduced through a stationary pipe; Fig. 3 is a horizontal section of the rotary gas distributor, or atomizer:-Fig. 4: a detail vertical section of the atomizer as shown in Fig. 1: and Fig. 5 a detail vertical section of the atomizer as shown in Fig. 2.
Referring to Fig. 1 of the drawings, 1 is a tank adapted to contain the liquid to be treated, 2 is a rotary atomizer suspended within the tank by means of the hollow shaft 3 and submerged in the liquid. The atomizer has a hollow interior communicating with the hollow shaft, and is provided with dischar e passages 4 extending outwardly, prefera lv from the centrol portion toward the riphery. These discharge passages are ormed by the curved vanes, or partitions, 5, and are adapted to discharge the g or gas n q r m he n r r 1922. Serial No. 567,225.
of the atomizer toward its periphery and into the surrounding liquid in the tank.
When the atomizer is rotated at a proper speed, the air will be sucked down through the hollow shaft. This speed will usually range from 250 to 800 R. P. M., depending tion 9 of the modified atomizer 7, through a stationary pipe 10, so arranged that air will flow into the interior of the atomizer either by suction, or by pressure from the outside, and liquid from the tank will flow into the interior of the atomizer through the annulus 12 formed by the pipe 10 and the lower portion 9 of the atomizer.
In either arrangement as shown by Figs. 4 or 5 it has been found that better results are obtained under some conditions and for some purposes by terminating the exterior of the discharge passages 4 at approximately a right angle, as shown by 16, Fig. 3, than by the acute an le formed by the peripheral circle 14. is condition may be regarded as formed by recessing, or cutting away, a portion of the periphery as shown by 15, so that the periphery of the atomizer will have a serrated appearance, as shown in horizontal section in Fig. 3.
The ejecting of a mixture of gas and liquid from the interior of the atomizer into the surrounding liquid in the tank gives a finer atomization than when only gas is ejected. In Figure 5 this may conveniently be realized by introducing the air throu h the pipe 10 1n regulable amounts and t e liquid through the annulus 12. In Fig. 4 it may conveniently be realized by havingan opening 6 in the lower portion of the atomizer, so arranged that it may be closed with'a plug, so that'if desired only air will be ejected. r
I claim:
1. In apparatus for treating liquids with gases, a tank adapted to contain liquid, a hollow rotary member journaled on a vertical axis suspended within the tank and submerged in the liquid, said rotary memher having discharge passages arranged so that two adjacent ischarge passages have a common partition and so that the outlet of one discharge passage is recessed relative to the common partition, said common partition of one discharge passage being adapted to deflectliquid away from the outlet of the other discharge passage and a tubular member adapted to deliver gas to the interior of said rotary member.
2. In apparatus for treating liquids with gases, a tank adapted to contain liquid, a hollow rotary member journaled on a vertical axis suspended within the tank and submerged in the liquid, said rotary member having discharge passages with divergent partitions toward the outlets and with the outlets of the discharge passages arran ed so as to form a serrated periphery e rotary member, and atubular member adapted to deliver gas to the interior of said rotary member.
3. In apparatus for treating liquids with gases, a tank adapted to contain liquid, a hollow rotary member journaled .on a vertical axis suspended within the tank and submerged in the liquid, said rotary memher having a serrated periphery and discharge passages arranged with divergent sides extending outwardly and terminating in the serrations, and a tubular member adapted to deliver eras to the interior of said rotary member.
WILLIAM E. GREENAWALT.
US567225A 1922-06-09 1922-06-09 Apparatus for treating liquids with gases Expired - Lifetime US1526596A (en)

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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2530814A (en) * 1945-10-12 1950-11-21 Schenley Ind Inc Apparatus for aerating liquids
US2556486A (en) * 1949-01-03 1951-06-12 Co Bartlett & Snow Co Sand treating apparatus
DE759121C (en) * 1940-04-05 1952-08-21 Waldhof Zellstoff Fab Method and device for ventilating foaming water
US2635860A (en) * 1951-06-11 1953-04-21 Premier Mill Corp Centrifugal mixing device
US2798697A (en) * 1955-05-27 1957-07-09 Robert M Soden Means for removing material in liquid form from tanks and the like
US2800315A (en) * 1954-10-04 1957-07-23 Edwin C Griesbach Device for the dispersion of gas in a liquid
US3385576A (en) * 1967-05-02 1968-05-28 American Cyanamid Co Apparatus for dispersing a gas in a liquid
US3387832A (en) * 1967-05-02 1968-06-11 American Cyanamid Co Apparatus for dispersing a gas in a liquid
US3521864A (en) * 1967-09-20 1970-07-28 Welles Products Corp Method and apparatus for controlling oxygen transfer and power requirements in a water aeration system
US3614072A (en) * 1969-01-02 1971-10-19 James H Brodie Hydraulic flow inducer
US3663117A (en) * 1970-01-21 1972-05-16 Cornell Mfg Co Aeration pump
US3814396A (en) * 1972-02-16 1974-06-04 Envirotech Corp Aeration apparatus
US3896027A (en) * 1973-06-22 1975-07-22 Kenneth A Digney Method of treating sewage to enhance aerobic decomposition
US4045522A (en) * 1974-01-03 1977-08-30 Nafziger Joel L Animal waste treatment system
US4990166A (en) * 1989-06-08 1991-02-05 Babich William F Gas stream purifying equipment
US5160459A (en) * 1990-11-27 1992-11-03 Claudio Guarnaschelli Fluid mixer
EP0847798A1 (en) * 1995-10-20 1998-06-17 Paul Esser Method of introducing a gas into a liquid and apparatus therefor
US5770062A (en) * 1993-05-03 1998-06-23 Wildlife Science, Inc. Device for aiding the solubilization of gases in liquids
US6394430B1 (en) * 1998-10-13 2002-05-28 Ekato Rühr-und Mischtechnik GmbH Auto-aspirating rotational dispersion device
US20070251865A1 (en) * 2004-04-22 2007-11-01 Hydor Srl Rotating Aerator for Aquariums and Ponds
US20090110559A1 (en) * 2007-10-25 2009-04-30 Midan Industries Ltd. Submersible mixing propeller
US20090213684A1 (en) * 2007-10-25 2009-08-27 Midan Industries Ltd. Apparatus for distribution of a gas into a body of liquid
US20100207285A1 (en) * 2007-10-17 2010-08-19 Hiroyuki Tanaka Underwater aeration device
US8366312B1 (en) * 2006-08-01 2013-02-05 United Services Automobile Association (Usaa) Systems to store and agitate fuel
US20130134101A1 (en) * 2010-08-04 2013-05-30 Stefan Blendinger Sparging Device for a Flotation Cell
US20160310914A1 (en) * 2015-04-21 2016-10-27 Huei-Wern TSUEI Aerator
CN111215015A (en) * 2019-12-26 2020-06-02 浙江长城搅拌设备股份有限公司 Special stirring device for viscous fluid mixing and gas dispersing
US11484848B2 (en) * 2018-12-03 2022-11-01 Invent Umwelt—Und Verfahrenstechnik Ag Apparatus for aerating bodies of water

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE759121C (en) * 1940-04-05 1952-08-21 Waldhof Zellstoff Fab Method and device for ventilating foaming water
US2530814A (en) * 1945-10-12 1950-11-21 Schenley Ind Inc Apparatus for aerating liquids
US2556486A (en) * 1949-01-03 1951-06-12 Co Bartlett & Snow Co Sand treating apparatus
US2635860A (en) * 1951-06-11 1953-04-21 Premier Mill Corp Centrifugal mixing device
US2800315A (en) * 1954-10-04 1957-07-23 Edwin C Griesbach Device for the dispersion of gas in a liquid
US2798697A (en) * 1955-05-27 1957-07-09 Robert M Soden Means for removing material in liquid form from tanks and the like
US3385576A (en) * 1967-05-02 1968-05-28 American Cyanamid Co Apparatus for dispersing a gas in a liquid
US3387832A (en) * 1967-05-02 1968-06-11 American Cyanamid Co Apparatus for dispersing a gas in a liquid
US3521864A (en) * 1967-09-20 1970-07-28 Welles Products Corp Method and apparatus for controlling oxygen transfer and power requirements in a water aeration system
US3614072A (en) * 1969-01-02 1971-10-19 James H Brodie Hydraulic flow inducer
US3663117A (en) * 1970-01-21 1972-05-16 Cornell Mfg Co Aeration pump
US3814396A (en) * 1972-02-16 1974-06-04 Envirotech Corp Aeration apparatus
US3896027A (en) * 1973-06-22 1975-07-22 Kenneth A Digney Method of treating sewage to enhance aerobic decomposition
US4045522A (en) * 1974-01-03 1977-08-30 Nafziger Joel L Animal waste treatment system
US4990166A (en) * 1989-06-08 1991-02-05 Babich William F Gas stream purifying equipment
US5160459A (en) * 1990-11-27 1992-11-03 Claudio Guarnaschelli Fluid mixer
US5770062A (en) * 1993-05-03 1998-06-23 Wildlife Science, Inc. Device for aiding the solubilization of gases in liquids
EP0847798A1 (en) * 1995-10-20 1998-06-17 Paul Esser Method of introducing a gas into a liquid and apparatus therefor
US6394430B1 (en) * 1998-10-13 2002-05-28 Ekato Rühr-und Mischtechnik GmbH Auto-aspirating rotational dispersion device
US8172205B2 (en) * 2004-04-22 2012-05-08 Hydor Srl Rotating aerator for aquariums and ponds
US20070251865A1 (en) * 2004-04-22 2007-11-01 Hydor Srl Rotating Aerator for Aquariums and Ponds
US8366312B1 (en) * 2006-08-01 2013-02-05 United Services Automobile Association (Usaa) Systems to store and agitate fuel
US20100207285A1 (en) * 2007-10-17 2010-08-19 Hiroyuki Tanaka Underwater aeration device
US8297599B2 (en) * 2007-10-17 2012-10-30 Tsurumi Manufacturing Co., Ltd. Underwater aeration device
US20090213684A1 (en) * 2007-10-25 2009-08-27 Midan Industries Ltd. Apparatus for distribution of a gas into a body of liquid
US7997788B2 (en) 2007-10-25 2011-08-16 Midan Industries Ltd. Submersible mixing propeller
US20090110559A1 (en) * 2007-10-25 2009-04-30 Midan Industries Ltd. Submersible mixing propeller
US20130134101A1 (en) * 2010-08-04 2013-05-30 Stefan Blendinger Sparging Device for a Flotation Cell
US8794446B2 (en) * 2010-08-04 2014-08-05 Siemens Aktiengesellschaft Sparging device for a flotation cell
US20160310914A1 (en) * 2015-04-21 2016-10-27 Huei-Wern TSUEI Aerator
US11484848B2 (en) * 2018-12-03 2022-11-01 Invent Umwelt—Und Verfahrenstechnik Ag Apparatus for aerating bodies of water
CN111215015A (en) * 2019-12-26 2020-06-02 浙江长城搅拌设备股份有限公司 Special stirring device for viscous fluid mixing and gas dispersing
CN111215015B (en) * 2019-12-26 2022-07-12 浙江长城搅拌设备股份有限公司 Special stirring device for viscous fluid mixing and gas dispersing

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