US3179150A - Furnace - Google Patents

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US3179150A
US3179150A US190971A US19097162A US3179150A US 3179150 A US3179150 A US 3179150A US 190971 A US190971 A US 190971A US 19097162 A US19097162 A US 19097162A US 3179150 A US3179150 A US 3179150A
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secondary air
chamber
flue
burners
furnace
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US190971A
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Gerald D Arnold
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/028Arrangements for the supply or exhaust of gaseous drying medium for direct heat transfer, e.g. perforated tubes, annular passages, burner arrangements, dust separation, combined direct and indirect heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C3/00Combustion apparatus characterised by the shape of the combustion chamber
    • F23C3/006Combustion apparatus characterised by the shape of the combustion chamber the chamber being arranged for cyclonic combustion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00Heating arrangements
    • F26B23/02Heating arrangements using combustion heating

Definitions

  • This invention relates to a furnace.
  • This particular furnace happens to be used to supply hot gaseous products of combustion for use in dehydration.
  • the general organization of a dryer is shown in my Patent 2,822,153.
  • the present furnace is an improvement on those disclosed in said patent.
  • the object of the invention is to provide a furnace in which combustion will be completed within a refractory lined combustion chamber so that no flame will be communicated through the flue.
  • the furnace herein disclosed achieves the desired result by establishing within the combustion chamber vortex currents of secondary air which are opposed to the currents of primary air and burning gases traversing the cylindrical chamber circumferentially in opposite sense of rotation from the vortex currents of secondary air.
  • the burners and the secondary air ports are desirably tangential and located at opposite ends of the cylindrical combustion chamber, from which the flue opens tangentially midway between the burners.
  • FIG. 1 is a view partiallyin side elevation and partially in axial section through a refractory lined furnace combustion chamber.
  • FIG. 2 is a view taken in section on the line 2--2 of FIG. 1.
  • FIG. 3 is a view on a reduced scale, showing in side elevation a dehydrating system in which the furnace herein disclosed may advantageously be used.
  • the furnace 6 has a generally cylindrical wall 8 and end walls 10 and 12 providing a combustion chamber 14 lined with fire brick 16 or other refractory lining material.
  • the material used preferably provides thermal insulation.
  • oil or gas burners 13 are used as carbureting means to provide the required fuel to carburete the primary air and secondary air hereinafter referred to. These fuel burners are disposed in frustoconically expanding throats which are directed tangentially to the combustion chamber 14. Normally, the fuel admitted through each burner 18 is supplied with primary air from any source (not shown), the arrangement being conventional.
  • auxiliary inlet 22 which likewise is tangential and opens into the chamber in the path of gases admitted through the flaring passages 20.
  • the burning gases, augmented by such secondary air as is received through the inlet 22, establishes vortices which whirl at relatively high speeds within the opposite ends of the combustion chamber 14. These vortices move axially toward the center of the furnace for escape through the flue 24.
  • the flue is tangential in the same sense as the flaring inlet passage 20 and the secondary inlet passage 22 at each end of the combustion chamber.
  • Pressure differential between the air inlets into the combustion chamber and the point of ice gas discharge from the dehydrating drum creates a strong current of dehydrating gas through the entire system. As will be explained, the pressure differential is created by the suction of the blower which exhausts hot gases from the dehydrating drum system hereinafter described and with which this furnace is desirably used.
  • the desired pressure differential is preferably established by a blower 36 at, the outlet end of the dryer which exhausts the gas from the drying drum 38 and produces a very substantial suction to whichthe flue 24 is subject. It is suction from the remote end of the drying drum 38 which draws the secondary air through the inlets provided at 22.
  • the material to be dehydrated is supplied to a hopper 40 from which it enters the flue and passes with the hot gases into the drum. The material is separated from the hot gases after the latter have been sucked from the drum by the blower 3 6. These gases are partly products of combustion of the furnace and they are partly made up of air admitted through the aforesaid auxiliary inlets.
  • supplemental secondary inlets are provided at 30 which are tangential with respect to the combustion chamber 14 but directed in an opposite sense to the inlets 20 and. 22. Moreover, the inlets 30 are provided midway between the respective inlets 22 and the outlet flue 24. The inlets 22 and the inlets 30 have dampers 32 and 34 for apportioning air flow.
  • the whirling vortices within the furnace abruptly encounter circumferential currents of secondary air admitted through the inlets 3t) and whirling in a direction opposite to that of the respective vortices from the burners.
  • the resulting turbulence not only produces thorough mixing with these additional quantities of secondary air but also abruptly interrupts the vortical movement with the result that the products of combustion have to make a fresh start as they approach the flue 24. It has been found that if a fire wall is eliminated from a conventional furnace, the flame will extend into the dehydrating drum. This is not the case if the furnace is made as herein disclosed, since the combustion will be completed within the chamber 14 and no burning fuel will issue through the flue 24.
  • a furnace comprising the combination with means forming a generally cylindrical combustion chamber having ends and a generally tangential flue intermediate its ends, of means providing tangential burners constituting means for admitting fuel and primary air adjacent the respective ends of the chamber, and means providing secondary air inlets of generally tangential disposition and constituting means for admitting secondary air tangentially in the same sense in which fuel and primary air are admitted from said burners, whereby the fuel and air admitted to the chamber are directed on a helical path therein, said secondary air inlets opening into the chamber in the path of material from said burners, and means for providing auxiliary secondary air inlets at opposite sides of said flue and disposed intermediate the burners and the flue, said auxiliary secondary air inlets being tangential in a sense opposite to that of the secondary air inlets and the burners.
  • a furnace comprising the combination with means forming a generally cylindrical combustion chamber having a flue opening from its periphery, of first means for admitting a current of air tangentially into said chamber at a point spaced axially from said flue, carbureting means for supplying fuel for mixture with the air so admitted for combustion in said chamber, a second means :3) for admitting a current of air tangentially into said chamber at a point intermediate the flue and said first means, said second means being remote from the first means for permitting combustion of the fuel to progress during a substantial length of unobstructed helical travel circumferentially and axially of said chamber before meeting the current of air admitted through said second means, the first and second means for admitting air being opposite in sense for efiecting impact of said currents to create turbulence, and means for establishing pressure differentials for effecting rapid flow of the several currents of air admitted to said chamber, the impact of such currents upon each other resulting in completion of combustion Within said chamber after first allowing a substantial length of

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Combustion Of Fluid Fuel (AREA)

Description

A ril 20, 1965 e. D. ARNOLD 3,179,150
FURNACE Filed April 30, 1962 INVENTOR. G's-44.12 D. 199N040 Am,mv-MA ATTORNEY 3,179,150 FURNACE Gerald D. Arnold, Galesville, Wis.
Filed Apr. 30, 1962, Ser. No. 190,971 2 Claims. (Cl. 158-1) This invention relates to a furnace.
This particular furnace happens to be used to supply hot gaseous products of combustion for use in dehydration. The general organization ofa dryer is shown in my Patent 2,822,153. The present furnace is an improvement on those disclosed in said patent. The object of the invention is to provide a furnace in which combustion will be completed within a refractory lined combustion chamber so that no flame will be communicated through the flue.
In the past, this objective has generally been achieved through the provision of firebrick baflles within a combustion chamber. The furnace herein disclosed achieves the desired result by establishing within the combustion chamber vortex currents of secondary air which are opposed to the currents of primary air and burning gases traversing the cylindrical chamber circumferentially in opposite sense of rotation from the vortex currents of secondary air. The burners and the secondary air ports are desirably tangential and located at opposite ends of the cylindrical combustion chamber, from which the flue opens tangentially midway between the burners. When the opposing currents meet at substantial velocities, the impact of the gases upon each other promotes agitation with consequent intimate mixing and such interruption of movement in the initial direction of gas advance as to result in completion of combustion before the gases resume motion toward the flue.
In the drawings:
FIG. 1 is a view partiallyin side elevation and partially in axial section through a refractory lined furnace combustion chamber.
FIG. 2 is a view taken in section on the line 2--2 of FIG. 1.
FIG. 3 is a view on a reduced scale, showing in side elevation a dehydrating system in which the furnace herein disclosed may advantageously be used.
As clearly appears in FIG. 1 and FIG. 2, the furnace 6 has a generally cylindrical wall 8 and end walls 10 and 12 providing a combustion chamber 14 lined with fire brick 16 or other refractory lining material. The material used preferably provides thermal insulation. By way of exemplification, oil or gas burners 13 are used as carbureting means to provide the required fuel to carburete the primary air and secondary air hereinafter referred to. These fuel burners are disposed in frustoconically expanding throats which are directed tangentially to the combustion chamber 14. Normally, the fuel admitted through each burner 18 is supplied with primary air from any source (not shown), the arrangement being conventional.
In each instance, secondary air is supllied through an auxiliary inlet 22 which likewise is tangential and opens into the chamber in the path of gases admitted through the flaring passages 20. The burning gases, augmented by such secondary air as is received through the inlet 22, establishes vortices which whirl at relatively high speeds within the opposite ends of the combustion chamber 14. These vortices move axially toward the center of the furnace for escape through the flue 24. The flue is tangential in the same sense as the flaring inlet passage 20 and the secondary inlet passage 22 at each end of the combustion chamber. Pressure differential between the air inlets into the combustion chamber and the point of ice gas discharge from the dehydrating drum creates a strong current of dehydrating gas through the entire system. As will be explained, the pressure differential is created by the suction of the blower which exhausts hot gases from the dehydrating drum system hereinafter described and with which this furnace is desirably used.
As is apparent from my patent above identified, the desired pressure differential is preferably established by a blower 36 at, the outlet end of the dryer which exhausts the gas from the drying drum 38 and produces a very substantial suction to whichthe flue 24 is subject. It is suction from the remote end of the drying drum 38 which draws the secondary air through the inlets provided at 22. The material to be dehydrated is supplied to a hopper 40 from which it enters the flue and passes with the hot gases into the drum. The material is separated from the hot gases after the latter have been sucked from the drum by the blower 3 6. These gases are partly products of combustion of the furnace and they are partly made up of air admitted through the aforesaid auxiliary inlets.
In accordance with the present invention, supplemental secondary inlets are provided at 30 which are tangential with respect to the combustion chamber 14 but directed in an opposite sense to the inlets 20 and. 22. Moreover, the inlets 30 are provided midway between the respective inlets 22 and the outlet flue 24. The inlets 22 and the inlets 30 have dampers 32 and 34 for apportioning air flow.
In consequence of this arrangement, the whirling vortices within the furnace abruptly encounter circumferential currents of secondary air admitted through the inlets 3t) and whirling in a direction opposite to that of the respective vortices from the burners. The resulting turbulence not only produces thorough mixing with these additional quantities of secondary air but also abruptly interrupts the vortical movement with the result that the products of combustion have to make a fresh start as they approach the flue 24. It has been found that if a fire wall is eliminated from a conventional furnace, the flame will extend into the dehydrating drum. This is not the case if the furnace is made as herein disclosed, since the combustion will be completed within the chamber 14 and no burning fuel will issue through the flue 24.
I claim:
1. A furnace comprising the combination with means forming a generally cylindrical combustion chamber having ends and a generally tangential flue intermediate its ends, of means providing tangential burners constituting means for admitting fuel and primary air adjacent the respective ends of the chamber, and means providing secondary air inlets of generally tangential disposition and constituting means for admitting secondary air tangentially in the same sense in which fuel and primary air are admitted from said burners, whereby the fuel and air admitted to the chamber are directed on a helical path therein, said secondary air inlets opening into the chamber in the path of material from said burners, and means for providing auxiliary secondary air inlets at opposite sides of said flue and disposed intermediate the burners and the flue, said auxiliary secondary air inlets being tangential in a sense opposite to that of the secondary air inlets and the burners.
2. A furnace comprising the combination with means forming a generally cylindrical combustion chamber having a flue opening from its periphery, of first means for admitting a current of air tangentially into said chamber at a point spaced axially from said flue, carbureting means for supplying fuel for mixture with the air so admitted for combustion in said chamber, a second means :3) for admitting a current of air tangentially into said chamber at a point intermediate the flue and said first means, said second means being remote from the first means for permitting combustion of the fuel to progress during a substantial length of unobstructed helical travel circumferentially and axially of said chamber before meeting the current of air admitted through said second means, the first and second means for admitting air being opposite in sense for efiecting impact of said currents to create turbulence, and means for establishing pressure differentials for effecting rapid flow of the several currents of air admitted to said chamber, the impact of such currents upon each other resulting in completion of combustion Within said chamber after first allowing a substantial length of travel of burning gases helically of the 15 chamber before said impact occurs.
References Cited by'the Examiner UNITED STATES PATENTS 930,424 1/11 Koons 158-1 1,091,475 3/ 14 Best l1028 2,286,909 6/42 Goddard 15 8-4- 2,672,108 3/54 Arnold 110-28 2,876,831 3/59 Knight 158-99 FOREIGN PATENTS 134,083 7/ 33 Austria.
216,656 6/24 Great Britain.
3 87,751 2/3 3 Great Britain.
JAMES W. WESTHAVER, Primary Examiner.
PERCY L. PATRICK, FREDERICK L. MATTESON,
E11,, Examiners.

Claims (1)

1. A FURNACE COMPRISING THE COMBINATION WITH MEANS FORMING A GENERALLY CYLINDRICAL COMBUSTION CHAMBER HAVING END OF A GENERALLY TANGENTIAL FLUE INTERMEDIATE ITS ENDS, OF MEANS PROVIDING TANGENTIAL BURNERS CONSTITUTING MEANS FOR ADMITTING FUEL AND PRIMARY AIR ADJACENT THE RESPECTIVE ENDS OF THE CHAMBER, AND MEANS PROVIDING SECONDARY AIR INLETS OF GENERALLY TANGENTIAL DIPOSITION AND CONSTITUTING MEANS FOR ADMITTING SECONDARY AIR TANGENTIALLY IN THE SAME SENSE IN WHICH FUEL AND PRIMARY AIR ARE ADMITTED FROM SAID BURNER, WHEREBY THE FUEL AND AIR ADMITTED TO THE CHAMBER ARE DIRECTED ON A HELICAL PATH THEREIN, SAID SECONDARY AIR INLETS OPENING INTO THE CHAMBER IN THE PATH OF MATERIAL FROM SAID BURNERS, AND MEANS FOR PROVIDING AUXILIARY SECONDARY AIR INLETS AT OPPOSITE SIDES OF SAID FLUE AND DISPOSED INTERMEDIATE THE BURNERS AND THE FLUE, SAID AUXILIARY SECONDARY AIR INLETS BEING TANGENTIAL IN A SENSE OPPOSITE TO THAT OF THE SECONDARY AIR INLETS AND THE BURNERS.
US190971A 1962-04-30 1962-04-30 Furnace Expired - Lifetime US3179150A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3363661A (en) * 1965-12-07 1968-01-16 Fletcher Co H E Apparatus for producing a flame jet by combusting counter flow reactants
US3779691A (en) * 1970-05-08 1973-12-18 Mitsui Shipbuilding Eng Apparatus for burning high viscosity liquid fuels
US3959007A (en) * 1972-07-28 1976-05-25 Structural Materials Process for the preparation of siliceous ashes
US4002127A (en) * 1975-03-13 1977-01-11 Derek Angus Cyclone structure
US4218426A (en) * 1976-04-09 1980-08-19 Continental Carbon Company Method and apparatus for the combustion of waste gases
US4642046A (en) * 1983-10-28 1987-02-10 Kabushiki Kaisha Toshiba Pulse combustor
US20130034817A1 (en) * 2006-06-23 2013-02-07 Elisabeth Cecille Rummelhoff Afterburner for gas from gassification plant

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US980424A (en) * 1910-02-05 1911-01-03 John H Koons Furnace.
US1091475A (en) * 1904-02-19 1914-03-31 John H Best Tangential-flame furnace.
GB216656A (en) * 1923-04-25 1924-06-05 George Henry Franklin Improvements in and relating to oil-fired furnaces
GB387751A (en) * 1931-09-23 1933-02-16 John Hamilton Improvements relating to gaseous and liquid fuel burning apparatus
AT134083B (en) * 1928-03-19 1933-07-10 Josef Ing Groedl Oil firing.
US2286909A (en) * 1940-12-16 1942-06-16 Robert H Goddard Combustion chamber
US2672108A (en) * 1948-10-01 1954-03-16 Gerald D Arnold Furnace
US2876831A (en) * 1951-03-08 1959-03-10 Surface Combustion Corp Internal-combustion burners

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1091475A (en) * 1904-02-19 1914-03-31 John H Best Tangential-flame furnace.
US980424A (en) * 1910-02-05 1911-01-03 John H Koons Furnace.
GB216656A (en) * 1923-04-25 1924-06-05 George Henry Franklin Improvements in and relating to oil-fired furnaces
AT134083B (en) * 1928-03-19 1933-07-10 Josef Ing Groedl Oil firing.
GB387751A (en) * 1931-09-23 1933-02-16 John Hamilton Improvements relating to gaseous and liquid fuel burning apparatus
US2286909A (en) * 1940-12-16 1942-06-16 Robert H Goddard Combustion chamber
US2672108A (en) * 1948-10-01 1954-03-16 Gerald D Arnold Furnace
US2876831A (en) * 1951-03-08 1959-03-10 Surface Combustion Corp Internal-combustion burners

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3363661A (en) * 1965-12-07 1968-01-16 Fletcher Co H E Apparatus for producing a flame jet by combusting counter flow reactants
US3779691A (en) * 1970-05-08 1973-12-18 Mitsui Shipbuilding Eng Apparatus for burning high viscosity liquid fuels
US3959007A (en) * 1972-07-28 1976-05-25 Structural Materials Process for the preparation of siliceous ashes
US4002127A (en) * 1975-03-13 1977-01-11 Derek Angus Cyclone structure
US4218426A (en) * 1976-04-09 1980-08-19 Continental Carbon Company Method and apparatus for the combustion of waste gases
US4642046A (en) * 1983-10-28 1987-02-10 Kabushiki Kaisha Toshiba Pulse combustor
US20130034817A1 (en) * 2006-06-23 2013-02-07 Elisabeth Cecille Rummelhoff Afterburner for gas from gassification plant

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