US2883167A - Apparatus for supplying and mixing a liquid into a gaseous medium - Google Patents
Apparatus for supplying and mixing a liquid into a gaseous medium Download PDFInfo
- Publication number
- US2883167A US2883167A US512491A US51249155A US2883167A US 2883167 A US2883167 A US 2883167A US 512491 A US512491 A US 512491A US 51249155 A US51249155 A US 51249155A US 2883167 A US2883167 A US 2883167A
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- US
- United States
- Prior art keywords
- liquid
- gaseous medium
- supplying
- inwardly
- side wall
- Prior art date
- Legal status (The legal status 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 status listed.)
- Expired - Lifetime
Links
- 239000007788 liquid Substances 0.000 title description 24
- 239000002245 particle Substances 0.000 description 5
- 238000011144 upstream manufacturing Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- 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
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/314—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced at the circumference of the conduit
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S261/00—Gas and liquid contact apparatus
- Y10S261/54—Venturi scrubbers
Definitions
- the present invention relates to a device for supplying and spraying a liquid in a gaseous medium flowing in a channel.
- the need for spraying a liquid occurs within many technical fields.
- liquid particles of the smallest possible size are desired in order to cause an intimate contact with the dust particles.
- a division of the liquid into very small particles is desired in order to obtain as great a contact surface as possible.
- the present invention relates to an apparatus for obtaining said efiect by simple means.
- the invention is mainly characterized in that the flow of gasafter it first may have been free to expand-4s contracted abruptly, and that the liquid is conducted towards and is introduced peripherally into the flow of medium at said contraction point, as a thin liquid film, which is caught and broken by the contracted flow of gas and is mixed intimately with the flow of gas in the form of small water particles.
- a suitable apparatus for performing the invention consists of a supply conduit for a gaseous medium, which conduit is provided with a concentric expansion chamber, which is formed with an abrupt shoulder defining a restricted orifice to the subsequent portion of the channel.
- the expansion chamber is provided with means for supplying the liquid, arranged in such a manner that the liquid forms a continuous liquid film around the inner periphery of the chamber, which runs along the convergent envelope surface of said chamber, increasing in thickness towards the said shoulder and orifice to the subsequent portion of the conduit.
- Fig. 1 is a view in section of a conduit embodying the invention
- Fig. 2 is an enlarged detail of a portion of the apparatus shown in Fig. 1;
- Fig. 3 is a View similar to Fig. 1 showing a modification within the scope of the present invention.
- a tubular supply conduit 1 is provided for supplying gaseous dust-laden medium, the direction of flow of which is indicated by the arrow 10.
- the downstream terminal portion 2 of the conduit 1 is surrounded by an expansion chamber 4 which is arranged concentric with the conduit 1, this expansion chamber being defined by a side wall 5 and upstream and downstream, inwardly-extending end walls.
- the side wall 5 of said wall means converges in the direction of flow of the medium and terminates in the inwardly projecting, downstream end wall or shoulder 6, provided with a restricted discharge orifice 7, which orifice is in axial alinement with the downstream terminal portion 2 of conduit 1 and is of less diameter than the downstream end of the wall means and of a diameter less than the smallest interior diameter of the converging side wall 5.
- downstream end of side wall 5 merges into the downstream, inwardly extending end wall 6 on a gradual, inwardly-extending curve as clearly illustrated in the accompanying drawing, which assists in directing the liquid into contact with the gaseous medium flowing through discharge orifice 7.
- a discharge conduit 8 corresponding in size to the size of the orifice 7 constitutes a continuation of the supply conduit 1.
- Fig. 2 it is seen that the liquid fed through the inlets 3 is caused to flow along the side wall 5 in a film by the flow of the gasous medium through the chamber. Since the side wall 5 converges in the direction of flow of the medium, the film gradually increases in thickness as it approaches the downstream, inwardlydirected end wall or shoulder 6.
- the end wall or shoulder '6 preferably of inwardly-curved configuration, guides the film of liquid peripherally into the flow of the medium in the chamber, the flow at the orifice 7 being abruptly contracted. This breaks up the liquid into :a very great number of small liquid particles, which, as indicated by broken lines 9 in Fig. 2, are mixed intimately with the flowing medium indicated by the full line in Fig. 2.
- annular slot 11 may be provided between the side wall 5a of the chamber 4a and the supply conduit terminal portion 2a.
- a separate gaseous medium such as air from the surrounding room, may be supplied by a chamber 12 communicating with the slot 11 for the purpose of preventing condensation and/or deposit of dust in the apparatus from the dustladen medium introduced by the conduit 1.
- the chamber 12 may be supplied with conditioned air, for example by a conditioner 13 which decreases the viscosity of the liquid supplied by the inlets 3a.
- Apparatus for introducing a liquid into a flowing gaseous dust-laden medium comprising means to supply the dust-laden gaseous medium including a tubular supply conduit having an open, downstream end; wall means defining an expansion chamber surrounding that portion of said supply conduit adjacent the open, downstream end thereof and including a side wall and upstream and downstream, inwardly-extending end walls, said portion of said conduit projecting inwardly into said chamber a distance less than the length of said side wall, the side wall of said wall means converging in the direction of flow of the dust-laden medium and merging into the downstream, inwardly-extending end wall of said wall means downstream from said open, downstream end of said supply conduit, said downstream end of said wall means having a restricted discharge orifice therein in axial alinement with said tubular supply conduit, said discharge orifice being of less diameter than said downstream end wall and of a diameter less than the smallest interior diameter of said converging side wall so as to provide an inwardly projecting shoulder in said expansion chamber surrounding said discharge orifice and located substantially transverse to
- Apparatus according to claim 1 wherein the upstream end wall of said wall means is provided with an annular slot positioned intermediate that portion of said supply conduit surrounded by said wall means and said liquid supply means for supplying a separate gaseous medium into said expansion chamber, said annular slot communieating with the surrounding atmosphere and said separate gaseous medium serving to prevent condensation and deposit in said chamber of dust from the dust-laden gaseous medium.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nozzles (AREA)
Description
April 21, 1959 E KRANTZ APPARATUS FOR SUPPLYING AND MIXING A LIQUID INTO A GASEOUS MEDIUM Filed June 1, 1955 FIG. 2.
, EVERT KRANTZ Y Y AJL'TYS- United States Patent APPARATUS FDR SUPPLYING AND MIXING A LIQUID INTO A GASEOUS MEDIUM Evert Krantz, Stockholm, Swedemassignor to Aktiebolaget Svenska Flaktfabriken, Stockholm, Sweden Application June 1, 1955, Serial No. 512,491
Claims priority, application Sweden June 5, 1954 4 Claims. (Cl. 261-16) The present invention relates to a device for supplying and spraying a liquid in a gaseous medium flowing in a channel. The need for spraying a liquid occurs within many technical fields. When spraying a liquid in con- 'nection with precipitation, liquid particles of the smallest possible size are desired in order to cause an intimate contact with the dust particles. In a similar manner, in humidifying, cooling, dehumidifying, or other conditioning, a division of the liquid into very small particles is desired in order to obtain as great a contact surface as possible. The present invention relates to an apparatus for obtaining said efiect by simple means. The invention is mainly characterized in that the flow of gasafter it first may have been free to expand-4s contracted abruptly, and that the liquid is conducted towards and is introduced peripherally into the flow of medium at said contraction point, as a thin liquid film, which is caught and broken by the contracted flow of gas and is mixed intimately with the flow of gas in the form of small water particles.
A suitable apparatus for performing the invention consists of a supply conduit for a gaseous medium, which conduit is provided with a concentric expansion chamber, which is formed with an abrupt shoulder defining a restricted orifice to the subsequent portion of the channel. The expansion chamber is provided with means for supplying the liquid, arranged in such a manner that the liquid forms a continuous liquid film around the inner periphery of the chamber, which runs along the convergent envelope surface of said chamber, increasing in thickness towards the said shoulder and orifice to the subsequent portion of the conduit.
Other characteristics of the invention will be evident from the following description and from the claims.
The invention will now be described more in detail with reference to the accompanying drawings, in which:
Fig. 1 is a view in section of a conduit embodying the invention;
Fig. 2 is an enlarged detail of a portion of the apparatus shown in Fig. 1; and,
Fig. 3 is a View similar to Fig. 1 showing a modification within the scope of the present invention.
Referring now to Fig. 1, a tubular supply conduit 1 is provided for supplying gaseous dust-laden medium, the direction of flow of which is indicated by the arrow 10. The downstream terminal portion 2 of the conduit 1 is surrounded by an expansion chamber 4 which is arranged concentric with the conduit 1, this expansion chamber being defined by a side wall 5 and upstream and downstream, inwardly-extending end walls. The side wall 5 of said wall means converges in the direction of flow of the medium and terminates in the inwardly projecting, downstream end wall or shoulder 6, provided with a restricted discharge orifice 7, which orifice is in axial alinement with the downstream terminal portion 2 of conduit 1 and is of less diameter than the downstream end of the wall means and of a diameter less than the smallest interior diameter of the converging side wall 5. As shown,
2,883, 1 6 7 Patented Apr. 21, 1959 "ice In the preferred form of my invention, the downstream end of side wall 5 merges into the downstream, inwardly extending end wall 6 on a gradual, inwardly-extending curve as clearly illustrated in the accompanying drawing, which assists in directing the liquid into contact with the gaseous medium flowing through discharge orifice 7. A discharge conduit 8 corresponding in size to the size of the orifice 7 constitutes a continuation of the supply conduit 1.
Referring now to Fig. 2, it is seen that the liquid fed through the inlets 3 is caused to flow along the side wall 5 in a film by the flow of the gasous medium through the chamber. Since the side wall 5 converges in the direction of flow of the medium, the film gradually increases in thickness as it approaches the downstream, inwardlydirected end wall or shoulder 6. The end wall or shoulder '6, preferably of inwardly-curved configuration, guides the film of liquid peripherally into the flow of the medium in the chamber, the flow at the orifice 7 being abruptly contracted. This breaks up the liquid into :a very great number of small liquid particles, which, as indicated by broken lines 9 in Fig. 2, are mixed intimately with the flowing medium indicated by the full line in Fig. 2.
As shown in Fig. 3, wherein parts similar to those shown in Fig. l are designated by similar reference characters followed by the letter a, an annular slot 11 may be provided between the side wall 5a of the chamber 4a and the supply conduit terminal portion 2a. A separate gaseous medium, such as air from the surrounding room, may be supplied by a chamber 12 communicating with the slot 11 for the purpose of preventing condensation and/or deposit of dust in the apparatus from the dustladen medium introduced by the conduit 1. In the alternative, the chamber 12 may be supplied with conditioned air, for example by a conditioner 13 which decreases the viscosity of the liquid supplied by the inlets 3a.
While particular embodiments have been herein disclosed, it is not intended to limit the invention to this disclosure, but changes and modifications may be made therein and thereto within the scope of the following claims.
What I claim is:
1. Apparatus for introducing a liquid into a flowing gaseous dust-laden medium comprising means to supply the dust-laden gaseous medium including a tubular supply conduit having an open, downstream end; wall means defining an expansion chamber surrounding that portion of said supply conduit adjacent the open, downstream end thereof and including a side wall and upstream and downstream, inwardly-extending end walls, said portion of said conduit projecting inwardly into said chamber a distance less than the length of said side wall, the side wall of said wall means converging in the direction of flow of the dust-laden medium and merging into the downstream, inwardly-extending end wall of said wall means downstream from said open, downstream end of said supply conduit, said downstream end of said wall means having a restricted discharge orifice therein in axial alinement with said tubular supply conduit, said discharge orifice being of less diameter than said downstream end wall and of a diameter less than the smallest interior diameter of said converging side wall so as to provide an inwardly projecting shoulder in said expansion chamber surrounding said discharge orifice and located substantially transverse to the direction of flow of said dust-laden gaseous medium; and liquid supply means mounted in said expansion chamber about the inner surface of said side Wall and surrounding the inwardly-projecting portion of said supply conduit to form a continuous liquid film covering the entire inner surface of said converging side wall so that upon flow of the gaseous medium from said open, downstream end of said supply conduit and through said expansion chamber and said discharge orifice, said liquid film flows along said inner surface toward and into con tact with the shoulder formed by said downstream end wall, said converging side wall eifecting a gradual increase in the thickness of said film toward said shoulder, said shoulder directing and deflecting said thickened film inwardly into contact with the gaseous medium flowing through said discharge orifice.
2. Apparatus according to claim 1 wherein the downstream end of said side wall merges into said downstream, inwardly-extending end wall on a gradual, inwardly-extending curve to assist in directing said thickened film inwardly into contact with the gaseous medium flowing through said discharge orifice.
3. Apparatus according to claim 1 wherein the upstream end wall of said wall means is provided with an annular slot positioned intermediate that portion of said supply conduit surrounded by said wall means and said liquid supply means for supplying a separate gaseous medium into said expansion chamber, said annular slot communieating with the surrounding atmosphere and said separate gaseous medium serving to prevent condensation and deposit in said chamber of dust from the dust-laden gaseous medium.
4. Apparatus according to claim 1 wherein the upstream end wall of said wall means is provided with an annular slot positioned intermediate that portion of said supply conduit surrounded by said wall means and said liquid supply means for supplying a separate gaseous medium into said expansion chamber, and wherein there is a separate supply chamber in fluid communication with said annular slot and a conditioner in connectionwith said separate supply chamber to condition the separate gaseous medium supplied to said expansion chamber through said annular slot. 1
References Cited in the file of this patent UNITED STATES PATENTS 1,430,912 McElvaney et a1 Oct. 3, 1922 2,104,315 Abramson Jan, 4, 1938 2,183,561 Hamblin. .Dec. 19, 1939 2,353,865 Armstrong July 18, 1944 2,436,319 Meyer Feb. 17, 1948 2,577,451 Clemens et al Dec. 4, 1951 2,657,024 Reinecke Oct. 27, 1953 2,760,821 Kenney Aug. 28, 1956
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE2883167X | 1954-06-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2883167A true US2883167A (en) | 1959-04-21 |
Family
ID=20427656
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US512491A Expired - Lifetime US2883167A (en) | 1954-06-05 | 1955-06-01 | Apparatus for supplying and mixing a liquid into a gaseous medium |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2883167A (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3009687A (en) * | 1957-02-07 | 1961-11-21 | Stamicarbon | Apparatus for the removal of dust from gas containing same |
| US3057700A (en) * | 1959-10-12 | 1962-10-09 | Chemical Construction Corp | Phosphoric acid process |
| US3138441A (en) * | 1960-05-12 | 1964-06-23 | Svenska Flaektfabriken Ab | Gas purification apparatus |
| US3138647A (en) * | 1960-07-12 | 1964-06-23 | Svenska Flaektfabriken Ab | Arrangement in an apparatus for the supply and atomizing of a liquid in a gaseous medium |
| US3151190A (en) * | 1962-09-21 | 1964-09-29 | Kapitula John | Carburetor |
| US3170007A (en) * | 1960-12-23 | 1965-02-16 | Svenska Flaektfabriken Ab | Apparatus for cleaning dust-laden gases |
| DE1205467B (en) * | 1959-02-02 | 1965-11-18 | Vihorlat Narodni Podnik | Device for the mechanical generation of aerosols |
| US3388897A (en) * | 1958-11-28 | 1968-06-18 | Automotive Rubber Co Inc | Apparatus for separating and collecting particles carried by gases |
| US3440803A (en) * | 1967-06-02 | 1969-04-29 | Chemical Construction Corp | Gas scrubber |
| US3638924A (en) * | 1967-03-03 | 1972-02-01 | Slick Ind Co | Scrubbers with adjustable venturis |
| US4131439A (en) * | 1976-10-27 | 1978-12-26 | Hoelter H | Device for the dedusting of dust-containing gases |
| US4328107A (en) * | 1980-11-28 | 1982-05-04 | Synergo, Inc. | Process and apparatus for forming dispersions |
| US4597780A (en) * | 1981-06-04 | 1986-07-01 | Santek, Inc. | Electro-inertial precipitator unit |
| US4639313A (en) * | 1985-07-05 | 1987-01-27 | The Deister Concentrator Company | Floatation apparatus for concentration of minerals from high water content aqueous slurries |
| US4682991A (en) * | 1985-02-07 | 1987-07-28 | L. & C. Steinmuller Gmbh | Method and apparatus for scrubbing flue gas with flowable absorbing material pursuant to the air flow atomization principle |
| US5873380A (en) * | 1994-03-03 | 1999-02-23 | Mitsubishi Denki Kabushiki Kaisha | Wafer cleaning apparatus |
| US6142457A (en) * | 1998-01-30 | 2000-11-07 | Mobil Oil Corporation | Atomizing feed nozzle |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1430912A (en) * | 1921-08-18 | 1922-10-03 | Charles T Mcelvaney | Fuel mixer and ejector |
| US2104315A (en) * | 1936-11-02 | 1938-01-04 | Abramson Alexander | Carburetor for combustion engines |
| US2183561A (en) * | 1938-03-17 | 1939-12-19 | Clyde M Hamblin | Mechanical foam generator |
| US2353865A (en) * | 1940-11-28 | 1944-07-18 | Leslie R Armstrong | Gas burner |
| US2436319A (en) * | 1944-12-19 | 1948-02-17 | Peter A R Meyer | Carburetor |
| US2577451A (en) * | 1949-02-24 | 1951-12-04 | Standard Oil Dev Co | Apparatus for the production of air foam and air foam fire-extinguishing installations |
| US2657024A (en) * | 1950-03-22 | 1953-10-27 | Marshall C Reinecke | Air and liquid mixing device |
| US2760821A (en) * | 1954-04-05 | 1956-08-28 | Alfred L Kenworthy | Compound spray nozzles |
-
1955
- 1955-06-01 US US512491A patent/US2883167A/en not_active Expired - Lifetime
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1430912A (en) * | 1921-08-18 | 1922-10-03 | Charles T Mcelvaney | Fuel mixer and ejector |
| US2104315A (en) * | 1936-11-02 | 1938-01-04 | Abramson Alexander | Carburetor for combustion engines |
| US2183561A (en) * | 1938-03-17 | 1939-12-19 | Clyde M Hamblin | Mechanical foam generator |
| US2353865A (en) * | 1940-11-28 | 1944-07-18 | Leslie R Armstrong | Gas burner |
| US2436319A (en) * | 1944-12-19 | 1948-02-17 | Peter A R Meyer | Carburetor |
| US2577451A (en) * | 1949-02-24 | 1951-12-04 | Standard Oil Dev Co | Apparatus for the production of air foam and air foam fire-extinguishing installations |
| US2657024A (en) * | 1950-03-22 | 1953-10-27 | Marshall C Reinecke | Air and liquid mixing device |
| US2760821A (en) * | 1954-04-05 | 1956-08-28 | Alfred L Kenworthy | Compound spray nozzles |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3009687A (en) * | 1957-02-07 | 1961-11-21 | Stamicarbon | Apparatus for the removal of dust from gas containing same |
| US3388897A (en) * | 1958-11-28 | 1968-06-18 | Automotive Rubber Co Inc | Apparatus for separating and collecting particles carried by gases |
| DE1205467B (en) * | 1959-02-02 | 1965-11-18 | Vihorlat Narodni Podnik | Device for the mechanical generation of aerosols |
| US3057700A (en) * | 1959-10-12 | 1962-10-09 | Chemical Construction Corp | Phosphoric acid process |
| US3138441A (en) * | 1960-05-12 | 1964-06-23 | Svenska Flaektfabriken Ab | Gas purification apparatus |
| DE1233364B (en) * | 1960-05-12 | 1967-02-02 | Svenska Flaektfabriken Ab | Gas purifier |
| US3138647A (en) * | 1960-07-12 | 1964-06-23 | Svenska Flaektfabriken Ab | Arrangement in an apparatus for the supply and atomizing of a liquid in a gaseous medium |
| US3170007A (en) * | 1960-12-23 | 1965-02-16 | Svenska Flaektfabriken Ab | Apparatus for cleaning dust-laden gases |
| US3151190A (en) * | 1962-09-21 | 1964-09-29 | Kapitula John | Carburetor |
| US3638924A (en) * | 1967-03-03 | 1972-02-01 | Slick Ind Co | Scrubbers with adjustable venturis |
| US3440803A (en) * | 1967-06-02 | 1969-04-29 | Chemical Construction Corp | Gas scrubber |
| US4131439A (en) * | 1976-10-27 | 1978-12-26 | Hoelter H | Device for the dedusting of dust-containing gases |
| US4328107A (en) * | 1980-11-28 | 1982-05-04 | Synergo, Inc. | Process and apparatus for forming dispersions |
| US4597780A (en) * | 1981-06-04 | 1986-07-01 | Santek, Inc. | Electro-inertial precipitator unit |
| US4682991A (en) * | 1985-02-07 | 1987-07-28 | L. & C. Steinmuller Gmbh | Method and apparatus for scrubbing flue gas with flowable absorbing material pursuant to the air flow atomization principle |
| US4639313A (en) * | 1985-07-05 | 1987-01-27 | The Deister Concentrator Company | Floatation apparatus for concentration of minerals from high water content aqueous slurries |
| US5873380A (en) * | 1994-03-03 | 1999-02-23 | Mitsubishi Denki Kabushiki Kaisha | Wafer cleaning apparatus |
| US6142457A (en) * | 1998-01-30 | 2000-11-07 | Mobil Oil Corporation | Atomizing feed nozzle |
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