US2755750A - Fluid mixing apparatus - Google Patents

Fluid mixing apparatus Download PDF

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Publication number
US2755750A
US2755750A US279137A US27913752A US2755750A US 2755750 A US2755750 A US 2755750A US 279137 A US279137 A US 279137A US 27913752 A US27913752 A US 27913752A US 2755750 A US2755750 A US 2755750A
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gas
air
fuel
whirlers
inlet tube
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US279137A
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Escher Hans
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Australian Iron and Steel Pty Ltd
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Australian Iron and Steel Pty Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D17/00Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel

Definitions

  • the object of the invention is to provide an apparatus for mixing fluids which results in intensive mixing with a minimum of energy dissipation.
  • Apparatus in accordance with the present invention comprises an assembly of a plurality of whirlers, each whirler being so arranged that in at least a majority of cases the stream of fluid issuing therefrom rotates in a direction opposite to the direction of rotation of the adjacent stream and the contacting boundary layers move in the same direction.
  • Each whirler consists of a number of fixed blades held in a suitable frame the blades being helical somewhat like the blades of a screw propeller or air screw so that a rotary motion is imparted to fluid flowing over the surface of the blades.
  • Fig. 1 represents a sectional elevation on line 1-1 of Fig. 2 of a gas burner constructed and operating in accordance with the invention
  • Fig. 2 represents a front end sectional view on line 22 of Fig. 1 of the gas burner
  • Fig. 3 represents an elevation partly in section of a modified gas burner constructed and operating in accordance with the invention.
  • the main gas supply enters through pipe 11 and the air supply through pipe 12.
  • a number of pipes 13 provided at their outlets with whirlers 14 is attached to a plate 15 forming a partition between the air and fuel gas space of the burner.
  • the whirlers 14 are of similar construction to the whirlers 6 described above, the outer ends of the blades being secured to the wall of tubes 13, while the inner ends of the blades are secured to a central boss.
  • the fuel gas flows into the casing 16 surrounding tubes 13 and in between the tubes 13 and then through openings 17 into the combustion chamber 18.
  • the air streams enter the combustion chamber at substantially the same point through whirlers 14, the vanes or blades of which are so arranged that the air stream issuing from each whirler rotates in a direction opposite to the direction of rotation of the adjacent stream, with the contacting boundary layers moving in the same direction (see Fig. 2).
  • This results in a pumping action which moves Patented July 24, 1956 the gas from the outer space 19 to the inner space 20 and vice versa giving intimate mixing of air, fuel gas and burnt gases in the combustion chamber 18, thereby increasing the efficiency of the burner.
  • an additional or alternative fuel may be introduced through pipe 21 the outlet end of which may be provided with whirlers 22.
  • the gas burner arrangement shown in Figs. 1 and 2 may be modified as shown in Fig. 3 by the provision of additional fuel pipes 23 positioned within the air supply pipes 13 with the front ends projecting through the centre of whirlers 14 and the rear ends connected to an annular header 24 provided with a tangential feed (not shown).
  • Solid fuel such as pulversised coal, or the like, is fed into the pipes 23 through header 24.
  • the rotary motion of the air issuing from the whirlers 14 in the pipes 13 causes intensive and intimate mixing of the pulverised fuel with the gas issuing from openings 17 and the air thus assuring efiicient combustion of gaseous and solid fuel.
  • the front ends of pipes 23 may be provided with cone spreaders or the interior of the pipes may be rifled so as to assist in the breaking up of the pulverised fuel as it emerges from the pipes 23.
  • the pulverised fuel may be replaced by fuel oil if desired.
  • blast furnace gas may be fed in through pipe 11, coke oven gas through pipe 21 and pulverised coal through pipes 23 thus making maximum use of fuel from the various sources.
  • Gas burner apparatus comprising a combustion chamber, a gas inlet tube, a central fuel inlet tube in said gas inlet tube, a plurality of air inlet tubes arranged within said gas inlet tube in a circular pattern around said central fuel inlet tube, the outlet ends of each of said tubes being connected to a combustion chamber, whirlers provided in the outlet end of each air inlet tube and the central fuel inlet tube, said whirlers being constructed and arranged so that in at least a majority of cases the stream of air issuing from one whirler rotates in a direction opposite to the direction of rotation of the adjacent air streams and the adjacent boundary layers move in the same direction and the general axial direction of the air streams is the same as that of the gas stream.
  • Gas burner apparatus comprising a combustion chamber, a gas inlet tube, a plurality of air inlet tubes arranged within said gas inlet tube in a circular pattern, the outlet ends of the air inlet tubes and the gas inlet tube being connected to said combustion chamber, a whirler in the outlet end of each air inlet tube, said whirlers being constructed and arranged so that in at least a majority of cases the stream of air issuing from one whirler rotates in a direction opposite to the direction of rotation of the adjacent air stream and the adjacent boundary layers move in the same direction and the general axial direction of the air streams is the same as that of the gas stream, each whirler having an opening at its center, and a fuel inlet pipe for solid fuel positioned within each air inlet tube projecting into the combustion chamber through the opening in the center of the Whirler positioned in the outlet end of the respective air inlet pipe.

Description

y 4, 1956 H. ESCHER 2,755,75G
' FLUID MIXING APPARATUS Filed March 28. 1952 2 Sheets-Sheet 1 In van 790; 5& a m
July 24, 1956 H. ESCHER 2,755,750
FLUID MIXING APPARATUS Filed March 28. 1952 2 Sheets-Sheet 2 In vemv nited States Patent FLUID MIXING APPARATUS Hans Escher, Wollongong, New South Wales, Australia, assignor to Australian Iron & Steel Limited, Sydney, New South Wales, Australia Application March 28, 1952, Serial No. 279,137 Claims priority, application Australia January 4, 1952 2 Claims. (Cl. 110-22) This invention relates to an improved apparatus for mixing fluids.
The object of the invention is to provide an apparatus for mixing fluids which results in intensive mixing with a minimum of energy dissipation.
It is also an object of the invention to provide apparatus of relatively simple construction.
Apparatus in accordance with the present invention comprises an assembly of a plurality of whirlers, each whirler being so arranged that in at least a majority of cases the stream of fluid issuing therefrom rotates in a direction opposite to the direction of rotation of the adjacent stream and the contacting boundary layers move in the same direction.
Each whirler consists of a number of fixed blades held in a suitable frame the blades being helical somewhat like the blades of a screw propeller or air screw so that a rotary motion is imparted to fluid flowing over the surface of the blades.
The invention will be better understood by reference to the following description of two specific embodiments of the invention, which are shown more or less schematically in the accompanying drawings, in which:
Fig. 1 represents a sectional elevation on line 1-1 of Fig. 2 of a gas burner constructed and operating in accordance with the invention;
Fig. 2 represents a front end sectional view on line 22 of Fig. 1 of the gas burner; and
Fig. 3 represents an elevation partly in section of a modified gas burner constructed and operating in accordance with the invention.
Referring to the gas burner arrangement shown in Figs. 3 and 4 the main gas supply enters through pipe 11 and the air supply through pipe 12. A number of pipes 13 provided at their outlets with whirlers 14 is attached to a plate 15 forming a partition between the air and fuel gas space of the burner. The whirlers 14 are of similar construction to the whirlers 6 described above, the outer ends of the blades being secured to the wall of tubes 13, while the inner ends of the blades are secured to a central boss. The fuel gas flows into the casing 16 surrounding tubes 13 and in between the tubes 13 and then through openings 17 into the combustion chamber 18. The air streams enter the combustion chamber at substantially the same point through whirlers 14, the vanes or blades of which are so arranged that the air stream issuing from each whirler rotates in a direction opposite to the direction of rotation of the adjacent stream, with the contacting boundary layers moving in the same direction (see Fig. 2). This results in a pumping action which moves Patented July 24, 1956 the gas from the outer space 19 to the inner space 20 and vice versa giving intimate mixing of air, fuel gas and burnt gases in the combustion chamber 18, thereby increasing the efficiency of the burner.
If desired, an additional or alternative fuel may be introduced through pipe 21 the outlet end of which may be provided with whirlers 22.
The gas burner arrangement shown in Figs. 1 and 2 may be modified as shown in Fig. 3 by the provision of additional fuel pipes 23 positioned within the air supply pipes 13 with the front ends projecting through the centre of whirlers 14 and the rear ends connected to an annular header 24 provided with a tangential feed (not shown). Solid fuel, such as pulversised coal, or the like, is fed into the pipes 23 through header 24. The rotary motion of the air issuing from the whirlers 14 in the pipes 13 causes intensive and intimate mixing of the pulverised fuel with the gas issuing from openings 17 and the air thus assuring efiicient combustion of gaseous and solid fuel. The front ends of pipes 23 may be provided with cone spreaders or the interior of the pipes may be rifled so as to assist in the breaking up of the pulverised fuel as it emerges from the pipes 23. By reducing the diameter of pipes 23 the pulverised fuel may be replaced by fuel oil if desired.
The burner construction described above is particularly suitable for burning a variety of fuels simultaneously. For example, blast furnace gas may be fed in through pipe 11, coke oven gas through pipe 21 and pulverised coal through pipes 23 thus making maximum use of fuel from the various sources.
It will be evident from the simple nature of the apparatus described above that existing equipment can be readily converted to operate in accordance with the present process.
While the invention has been described with reference to a heat exchanger unit and a gas burner it may be readily applied to other constructions in which it is desired to secure intensive mixing with a minimum of energy dissipation.
I claim:
1. Gas burner apparatus comprising a combustion chamber, a gas inlet tube, a central fuel inlet tube in said gas inlet tube, a plurality of air inlet tubes arranged within said gas inlet tube in a circular pattern around said central fuel inlet tube, the outlet ends of each of said tubes being connected to a combustion chamber, whirlers provided in the outlet end of each air inlet tube and the central fuel inlet tube, said whirlers being constructed and arranged so that in at least a majority of cases the stream of air issuing from one whirler rotates in a direction opposite to the direction of rotation of the adjacent air streams and the adjacent boundary layers move in the same direction and the general axial direction of the air streams is the same as that of the gas stream.
2. Gas burner apparatus comprising a combustion chamber, a gas inlet tube, a plurality of air inlet tubes arranged within said gas inlet tube in a circular pattern, the outlet ends of the air inlet tubes and the gas inlet tube being connected to said combustion chamber, a whirler in the outlet end of each air inlet tube, said whirlers being constructed and arranged so that in at least a majority of cases the stream of air issuing from one whirler rotates in a direction opposite to the direction of rotation of the adjacent air stream and the adjacent boundary layers move in the same direction and the general axial direction of the air streams is the same as that of the gas stream, each whirler having an opening at its center, and a fuel inlet pipe for solid fuel positioned within each air inlet tube projecting into the combustion chamber through the opening in the center of the Whirler positioned in the outlet end of the respective air inlet pipe.
1,418,877 Mabee June 6, 1922 4 Reeves Mar. 13, Joubert Aug. 26, Seymour July 31, Chase May 24, Burg Jan. 16, Moyer Aug. 5, Hanzalek July 10,
FOREIGN PATENTS Great Britain of France Apr. 8,
US279137A 1952-01-04 1952-03-28 Fluid mixing apparatus Expired - Lifetime US2755750A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2861629A (en) * 1952-10-09 1958-11-25 Surface Combustion Corp Burner apparatus
US3504994A (en) * 1967-01-10 1970-04-07 British Petroleum Co Burner for use with fluid fuels
US4160640A (en) * 1977-08-30 1979-07-10 Maev Vladimir A Method of fuel burning in combustion chambers and annular combustion chamber for carrying same into effect
US4412496A (en) * 1982-04-27 1983-11-01 Foster Wheeler Energy Corp. Combustion system and method for a coal-fired furnace utilizing a low load coal burner
US4561364A (en) * 1981-09-28 1985-12-31 University Of Florida Method of retrofitting an oil-fired boiler to use coal and gas combustion
US4572084A (en) * 1981-09-28 1986-02-25 University Of Florida Method and apparatus of gas-coal combustion in steam boilers
US4597342A (en) * 1981-09-28 1986-07-01 University Of Florida Method and apparatus of gas-coal combustion in steam boilers
US5094610A (en) * 1989-05-11 1992-03-10 Mitsubishi Jukogyo Kabushiki Kaisha Burner apparatus
US20120308951A1 (en) * 2010-08-19 2012-12-06 Shucheng Zhu Coal decomposition equipment
US9500368B2 (en) 2008-09-23 2016-11-22 Siemens Energy, Inc. Alternately swirling mains in lean premixed gas turbine combustors

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191112416A (en) * 1911-05-23 1912-02-08 William Henry Yardley Improvements in Vaporizing and Mixing Devices for Internal Combustion Engines.
US1418877A (en) * 1920-09-22 1922-06-06 Leroy R Mabee Fuel mixer for gasoline engines
US1448151A (en) * 1921-03-05 1923-03-13 Edwin A Reeves Commingling device
US1505961A (en) * 1922-07-31 1924-08-26 Chilian Longley Hervey Engine air percolator
US1679177A (en) * 1926-02-10 1928-07-31 Seymour William Mixing device
US1859431A (en) * 1929-05-27 1932-05-24 Francis F Chase Vaporizer
US1943286A (en) * 1928-03-16 1934-01-16 Burg Eugen Burner for furnaces
US2251371A (en) * 1940-07-02 1941-08-05 George O Moyer Homogenizer
FR925868A (en) * 1945-04-30 1947-09-16 Brown Arrangement of burners and secondary air supply, in particular for pulverized coal boilers and in combination with a pressurized fireplace
US2560223A (en) * 1948-02-04 1951-07-10 Wright Aeronautical Corp Double air-swirl baffle construction for fuel burners

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB191112416A (en) * 1911-05-23 1912-02-08 William Henry Yardley Improvements in Vaporizing and Mixing Devices for Internal Combustion Engines.
US1418877A (en) * 1920-09-22 1922-06-06 Leroy R Mabee Fuel mixer for gasoline engines
US1448151A (en) * 1921-03-05 1923-03-13 Edwin A Reeves Commingling device
US1505961A (en) * 1922-07-31 1924-08-26 Chilian Longley Hervey Engine air percolator
US1679177A (en) * 1926-02-10 1928-07-31 Seymour William Mixing device
US1943286A (en) * 1928-03-16 1934-01-16 Burg Eugen Burner for furnaces
US1859431A (en) * 1929-05-27 1932-05-24 Francis F Chase Vaporizer
US2251371A (en) * 1940-07-02 1941-08-05 George O Moyer Homogenizer
FR925868A (en) * 1945-04-30 1947-09-16 Brown Arrangement of burners and secondary air supply, in particular for pulverized coal boilers and in combination with a pressurized fireplace
US2560223A (en) * 1948-02-04 1951-07-10 Wright Aeronautical Corp Double air-swirl baffle construction for fuel burners

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2861629A (en) * 1952-10-09 1958-11-25 Surface Combustion Corp Burner apparatus
US3504994A (en) * 1967-01-10 1970-04-07 British Petroleum Co Burner for use with fluid fuels
US4160640A (en) * 1977-08-30 1979-07-10 Maev Vladimir A Method of fuel burning in combustion chambers and annular combustion chamber for carrying same into effect
US4561364A (en) * 1981-09-28 1985-12-31 University Of Florida Method of retrofitting an oil-fired boiler to use coal and gas combustion
US4572084A (en) * 1981-09-28 1986-02-25 University Of Florida Method and apparatus of gas-coal combustion in steam boilers
US4597342A (en) * 1981-09-28 1986-07-01 University Of Florida Method and apparatus of gas-coal combustion in steam boilers
US4412496A (en) * 1982-04-27 1983-11-01 Foster Wheeler Energy Corp. Combustion system and method for a coal-fired furnace utilizing a low load coal burner
US5094610A (en) * 1989-05-11 1992-03-10 Mitsubishi Jukogyo Kabushiki Kaisha Burner apparatus
US9500368B2 (en) 2008-09-23 2016-11-22 Siemens Energy, Inc. Alternately swirling mains in lean premixed gas turbine combustors
EP2340398B1 (en) * 2008-09-23 2017-05-31 Siemens Energy, Inc. Alternately swirling mains in lean premixed gas turbine combustors
US20120308951A1 (en) * 2010-08-19 2012-12-06 Shucheng Zhu Coal decomposition equipment

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