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US1729763A - Apparatus and method of fuel burning - Google Patents

Apparatus and method of fuel burning Download PDF

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Publication number
US1729763A
US1729763A US66335A US6633525A US1729763A US 1729763 A US1729763 A US 1729763A US 66335 A US66335 A US 66335A US 6633525 A US6633525 A US 6633525A US 1729763 A US1729763 A US 1729763A
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furnace
burner
flue
combustion
fuel
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US66335A
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Florez Luis De
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Texaco Inc
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Texaco Inc
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B5/00Combustion apparatus with arrangements for burning uncombusted material from primary combustion
    • F23B5/02Combustion apparatus with arrangements for burning uncombusted material from primary combustion in main combustion chamber

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  • This invention relates to improvements in the art of burning fuel in a furnace and articularly in a furnace of the type in w 'ch the fuel is su plied by a jet.
  • the object of my invention is to accomphsh the introduction, by utilizing the energy of a jet such as that formed by the fuel burner, irrespective of theparticular form of burner used, of gases extraneous to the jet such as flue gases or other suitable dilutmg medium into the fire box of the furnace.
  • the invention is applicable where a fuel oil burner of the steam atomizing type, either with or without forced draft, is used, or where a gas burner with or without a steam jet and forced draft is used, or
  • the energy available to aspirate the flue gases from a suitable source and inject them 1nto the furnace is derived from the initial pressure under which the various elements required for combustion or to assist combustion are fed to the burner, and also to the velocity head generated by the expansion of the gases and vapors incident to combustion which velocity head is used to overcome the dlifere'nce in pressure between the source of supply of the flue gases and that existing in the fire box.
  • I will refer to the various combinations of elements discharged from the burners of whatever type they may be into the combustion chamber as the output of the burners. I will, however, for the pur pose oflllustration, describe the application of the invention to the various types of burners to which I have hereinbefore r -ferred.
  • FIG. 1 is a vertical sectional view of a furnace in which tubular heating elements are employed, the burner in this instance being of the steam atomizing type,
  • Figure 2 is a similar-view showing the apllcation of the invention where fuel oil is injected without the use of steam to produce combustion in the fire box of a furnace used in connection with a shell still;
  • Figure 3 is a fragmental sectional view 7 showing the application of-the invention to a owdered coal burner.
  • the furnace includes a fire box 1, having the usual bridge wall 2 and'flue 3, which leads to a stack 4, the heating elements 5 being arranged in the path of the products of combustion as they pass from the fire box to the flue.
  • the burner here illustrated includes an outer tube 6 which is made preferably of heat resisting-material, has an 0 en end 7 and variable air.
  • inlet ports 8 t e tube being mounted in a housing 9.
  • a steam tube 10 opening toward the open end 7 of the outer tube 6 and receiving its steam from a source of supply through a steam inlet 11.
  • A11 011 supply tube 12 is arranged within the steam tube 10 and opens toward the end of the same, terminating preferably short of the open end of the steam tube.
  • the air inlet ports 8 may be supplied with air under ressure from a suitable source,such as a b ower 13-
  • the burner extends into a chamber 14 in the housing 9 which chamber is preferably in the form of a Venturi tube opening into the combustion chamber of the furnace.
  • Communication is established between the chamber 14 and the flue 3 by means of a duct 15, the flue 3 being provided with a baflle 16 adjacent the duct.
  • This duct 15 communicates with the chamber 14 at a point preferably to the rear-of the open end of the tube 6, and is provided with a damper 16 by means of which the effective area of the duct may be varied.
  • the combustion chamber of the furnace may also be provided with an air inlet opening 17 having a damper 18 therein, for controlling the effective area of the duct.
  • the elfect of the jet-caused by the burner is to create a reduced pressure in the rear of the chamber 14 and draw a portion of the flue gases therein from the duct 3. These flue gases are then forced into the fire box of the furnace by the jet.
  • the magnitude of the jet will be dependent upon the amount of fuel burned, since the air requirements and steam requirements will be substantially regulated for good combustion in accordance with the amount of fuel handled, and the quantity of flue gases will also be substantially proportional to the amount of fuel burned. Consequently for a given opening of the damper 16' a substantially constant proportion of flue gaseswill be admitted to the furnace, the proportion, however, bearing a definite relation to the output of the burner and varying with the output of the burner.
  • the variation of the area of the duct 15 varies the ratio of the flue gases to the output of the burner.
  • the auxiliary air port 17 which is controlled by the damper 18 may be used should it be found desirable to operate the burner with an insufliciency of air, the desired auxiliary air being adniitted through this port.
  • the construction. illustrated in Figure 2 includes a furnace having a fire box 19, a
  • the tube 24 having an open inner end 25 ismounted in a housing 26 and is provided with variable air inlet orts 27 whlch may or may not be supplied with air under pressure.
  • An oil injection tube 28 extends into the tube 24 and terminates short of the open end of this tube.
  • the housing 26 is provided with a chamber 29 in which the burner is located, which chamberopens into the fire box of the furnace and as illustrated is preferably cylindrical in form, communication being established between the chamber and the flue 21 by a duct 30 having a control damper 31 therein for varying the effective area of the duct, there being provided a bailie 32 adjacent the duct which extends into the flue 21.
  • a duct 30 having a control damper 31 therein for varying the effective area of the duct, there being provided a bailie 32 adjacent the duct which extends into the flue 21.
  • This burner includes a tube 33 having an open end 34, opening into a chamber 35 of the housing 36, and having variable air inlet ports 37 which may either be supplied with air under atmospheric or superatmospheric pressure.
  • the powdered coal injector 38 which is connected to a suitable pressure source 39 extends into the tube 33 and discharges therein at a point to the rear of the open end of the tube.
  • the chamber 35' has communication with the flue of the furnace through a duct 40 having a control damper 41 therein which duct preferably communicates with the chamber 35 to the rear of the open end of the tube 34.
  • the method of effecting a recirculation of a portion of the flue gases which comprises passing a jet of burning fuel and the products of combustion thereof into the furnace, permitting a predetermined expansion of the gaseous combustion products and utilizing the kinetic energy of such expansion to draw flue gases into the furnace, thereby maintaining the temperature of the furnace relatively low.
  • the method of heating a furnace chamber which comprises injecting thereinto a jet of fuel, forming a high temperature flame by supplying substantially the amount of air required for complete combustion of said fuel, permitting the flame and the gaseous products of combustion to expand, thereby creating kinetic energy, and employing such energy to effect the introduction of hot flue ases to mix with the combustion products, W ereby the temperature of the furnace chamber is kept relatively low by such admixture.
  • the method of effecting a recirculation of a portion of the flue gases which comprises passing a jet of burning fuel and the products of combustion thereof into the furnace, permitting a predetermined expansion of the gaseous combustion products, utilizing the kinetic energy of i such expansion to draw flue gases into the furnace, and regulating the quantity of flue gases so recirculated to provide the desired temperature conditions in the furnace.
  • said burner means for supplying fuel and air to the burner, said burner being adapted to produce a norm ally developed high temperature flame, a flue for leading away Waste gases from the fire box, a fire resisting passage surroundin said burner and extending therebeyond an spaced therefrom a suflicient distance to permit substantial expansion of the flame and the hot products of combustion while in said passage, and a conduit means connecting said flue with said passage and enabling the drawing in of a portion of said waste gases by the expansion of the hot combustion gases.
  • a fire box in combination, a fire box, a fuel burner projecting into said fire box, means for supplying fuel and air to the burner, said burner bein adapted to produce a normally developed igh temperature flame, a flue for leading away waste gases from the fire box, a fire resisting Venturi tube surrounding said burner and extending therebeyond and spaced therefrom a suflicient distance to permit substantial expansion of the flame and the hot products of combustion while in said Venturi tube, a conduit means rounding said burner and extending therebeyond and spaced therefrom a suflicient dis tance to permit substantial expansion of the flame and the hot products of combustion while in said Venturi tube, a conduit means connecting said flue with said Venturi tube and enabling the drawing in of a portion of said Waste gases by the expansion of the hot combustion gases, and means located in said conduit means for controlling the flow of waste gases therethrough.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Description

Oct. 1, 1929.
L. DE FLOREZ APPARATUS AND METHOD OF FUEL BURNING Filed Nov. 2, 1925 2 Sheets-Sheet 1 awuemtoz a 7"2 III/ll w w w Oct. 1, 1929. L. DE FLOREZ APPARATUS AND METHOD OF FUEL BURNING 2 Sheets-Sheet 2 avwemtoz Filed Nov. 2, 1925 a? HIM/n Patented Oct. 1, 1929 UNITED [STATES PATENT OFFICE 121718 on now, or won-am, eounne'rrcu'r, Assmuon To run" 'rnxns a conromrrou or nnmwmn nrm'rus am) Eamon or rum. BUENING.
Application fled November 2, 1925. Serial No. 68,335.
This invention relates to improvements in the art of burning fuel in a furnace and articularly in a furnace of the type in w 'ch the fuel is su plied by a jet.
It is well inown that for the maximum economy fuel should be burned with just sufficient air for proper combustion, but in practice it is often found that burning fuel under such conditions creates 'fire box temperatures which are too high for practical operation inasmuch as they cause a rapid deterioration of brick settings and the heating elements.
In order to permit the combustion of the fuel under the most efiicient conditions, and
5 at the same time reduce the fire box temperature to a practical maximum and to attain other advantages, such as increasing the velocity of the heated gases by the heating surfaces to efliect a greater transfer of heat, it
has been the practice to introduce a portion of the spent products of combustion or flue gases, either from the furnace itself, or from other suitable sources, whereby the tempera ture of combustion is moderated and it is thus made possible to control to some ditions resulting in rapid deterioration and consequently high cost of maintenance.
The object of my invention is to accomphsh the introduction, by utilizing the energy of a jet such as that formed by the fuel burner, irrespective of theparticular form of burner used, of gases extraneous to the jet such as flue gases or other suitable dilutmg medium into the fire box of the furnace.
For instance, the invention is applicable where a fuel oil burner of the steam atomizing type, either with or without forced draft, is used, or where a gas burner with or without a steam jet and forced draft is used, or
where a powdered fuel burner in which the powdered fuel is served to the burner by a streem of alror other suitable vehicle is use The jet of incandescent gases injected into the furnace 1s composed of fuel, air and in some lnstances steam, all of which or part of which may be supplied to the burner under pressure. Irrespective of the particular type of burner used in the application of my inventlon, the; energy available to aspirate the flue gases from a suitable source and inject them 1nto the furnace is derived from the initial pressure under which the various elements required for combustion or to assist combustion are fed to the burner, and also to the velocity head generated by the expansion of the gases and vapors incident to combustion which velocity head is used to overcome the dlifere'nce in pressure between the source of supply of the flue gases and that existing in the fire box. v
For the purpose of simplifying the disclosure of the invention I will refer to the various combinations of elements discharged from the burners of whatever type they may be into the combustion chamber as the output of the burners. I will, however, for the pur pose oflllustration, describe the application of the invention to the various types of burners to which I have hereinbefore r -ferred.
In the drawings: v Figure 1 is a vertical sectional view ofa furnace in which tubular heating elements are employed, the burner in this instance being of the steam atomizing type,
Figure 2 is a similar-view showing the apllcation of the invention where fuel oil is injected without the use of steam to produce combustion in the fire box of a furnace used in connection with a shell still; and
Figure 3 is a fragmental sectional view 7 showing the application of-the invention to a owdered coal burner.
eferring now particularly to the construetion shown in Figure 1, the furnace includes a fire box 1, having the usual bridge wall 2 and'flue 3, which leads to a stack 4, the heating elements 5 being arranged in the path of the products of combustion as they pass from the fire box to the flue.
The burner here illustrated includes an outer tube 6 which is made preferably of heat resisting-material, has an 0 en end 7 and variable air. inlet ports 8 t e tube being mounted in a housing 9. ounted within the outer tube 6 is a steam tube 10, opening toward the open end 7 of the outer tube 6 and receiving its steam from a source of supply through a steam inlet 11. A11 011 supply tube 12 is arranged within the steam tube 10 and opens toward the end of the same, terminating preferably short of the open end of the steam tube.
If desired, the air inlet ports 8 may be supplied with air under ressure from a suitable source,such as a b ower 13- The burner extends into a chamber 14 in the housing 9 which chamber is preferably in the form of a Venturi tube opening into the combustion chamber of the furnace. The
1 open endof the outer tube 6 which tube extends beyond the steam tube 10, is located preferab y at the throat of the Venturi tube.
Communication is established between the chamber 14 and the flue 3 by means of a duct 15, the flue 3 being provided with a baflle 16 adjacent the duct. This duct 15 communicates with the chamber 14 at a point preferably to the rear-of the open end of the tube 6, and is provided with a damper 16 by means of which the effective area of the duct may be varied.
The combustion chamber of the furnace may also be provided with an air inlet opening 17 having a damper 18 therein, for controlling the effective area of the duct.
In operation the elfect of the jet-caused by the burner is to create a reduced pressure in the rear of the chamber 14 and draw a portion of the flue gases therein from the duct 3. These flue gases are then forced into the fire box of the furnace by the jet.
The magnitude of the jet will be dependent upon the amount of fuel burned, since the air requirements and steam requirements will be substantially regulated for good combustion in accordance with the amount of fuel handled, and the quantity of flue gases will also be substantially proportional to the amount of fuel burned. Consequently for a given opening of the damper 16' a substantially constant proportion of flue gaseswill be admitted to the furnace, the proportion, however, bearing a definite relation to the output of the burner and varying with the output of the burner. The variation of the area of the duct 15 varies the ratio of the flue gases to the output of the burner.
The auxiliary air port 17 which is controlled by the damper 18 may be used should it be found desirable to operate the burner with an insufliciency of air, the desired auxiliary air being adniitted through this port.
The construction. illustrated in Figure 2 includes a furnace having a fire box 19, a
bridge wall 20, and a flue'21, leading to a stack 22. A shell still 23 is supported above the fire box of the furnace. In this form the tube 24 having an open inner end 25 ismounted in a housing 26 and is provided with variable air inlet orts 27 whlch may or may not be supplied with air under pressure. An oil injection tube 28 extends into the tube 24 and terminates short of the open end of this tube. The housing 26 is provided with a chamber 29 in which the burner is located, which chamberopens into the fire box of the furnace and as illustrated is preferably cylindrical in form, communication being established between the chamber and the flue 21 by a duct 30 having a control damper 31 therein for varying the effective area of the duct, there being provided a bailie 32 adjacent the duct which extends into the flue 21. In this form of the invention, where the oil is fed through the pipe 28 under pressure without the use of steam, the resultant et caused by the burner creates a reduced pressure in the rear of the chamber 29 and draws a portion of the flue gases therein through the duct 30, which flue gases are then forced into the fire box by the et.
When a powdered coal burner such as illustrated in Figure 3 is used, the operation of injecting the portion of the flue gases into the firebox of the furnace is substantially the same. This burner includes a tube 33 having an open end 34, opening into a chamber 35 of the housing 36, and having variable air inlet ports 37 which may either be supplied with air under atmospheric or superatmospheric pressure. The powdered coal injector 38 which is connected to a suitable pressure source 39 extends into the tube 33 and discharges therein at a point to the rear of the open end of the tube. The chamber 35' has communication with the flue of the furnace through a duct 40 having a control damper 41 therein which duct preferably communicates with the chamber 35 to the rear of the open end of the tube 34.
Of course when a gas burner is used the action of the jet in injecting the extraneous I gases into the furnace is similar to that when the other types of burners are used.
I have illustrated three types of burners and have illustrated the chambers into which the burners extend in the forms of cylinders and a Venturi tube, but it is to be understood that either the cylindrical form or the Venturi tube form may be used with any of the burners, and furthermore, that the burners may be so disposed as to discharge directly into the fire box of the furnace, communication being established with the flue so that the pressure created by the jet will draw the requisite amount of flue gases from the flue and inject them into the fire box.
I do not wish to be limited to the particular embodiment of the invention which I have shown, for it is obvious that many details of construction of the apparatus may be made without departing from the scope of the claims.
WVhat I claim is:
1. In the heating of a furnace, the method of effecting a recirculation of a portion of the flue gases which comprises passing a jet of burning fuel and the products of combustion thereof into the furnace, permitting a predetermined expansion of the gaseous combustion products and utilizing the kinetic energy of such expansion to draw flue gases into the furnace, thereby maintaining the temperature of the furnace relatively low.
2. The method of heating a furnace chamber which comprises injecting thereinto a jet of fuel, forming a high temperature flame by supplying substantially the amount of air required for complete combustion of said fuel, permitting the flame and the gaseous products of combustion to expand, thereby creating kinetic energy, and employing such energy to effect the introduction of hot flue ases to mix with the combustion products, W ereby the temperature of the furnace chamber is kept relatively low by such admixture.
3. In the heating of a furnace, the method of effecting a recirculation of a portion of the flue gases which comprises passing a jet of burning fuel and the products of combustion thereof into the furnace, permitting a predetermined expansion of the gaseous combustion products, utilizing the kinetic energy of i such expansion to draw flue gases into the furnace, and regulating the quantity of flue gases so recirculated to provide the desired temperature conditions in the furnace.
4. In a furnace, in combination, a fire box,
a fuel burner projecting into said fire box,
means for supplying fuel and air to the burner, said burner being adapted to produce a norm ally developed high temperature flame, a flue for leading away Waste gases from the fire box, a fire resisting passage surroundin said burner and extending therebeyond an spaced therefrom a suflicient distance to permit substantial expansion of the flame and the hot products of combustion while in said passage, and a conduit means connecting said flue with said passage and enabling the drawing in of a portion of said waste gases by the expansion of the hot combustion gases.
5. In a furnace, in combination, a fire box, a fuel burner projecting into said fire box, means for supplying fuel and air to the burner, said burner bein adapted to produce a normally developed igh temperature flame, a flue for leading away waste gases from the fire box, a fire resisting Venturi tube surrounding said burner and extending therebeyond and spaced therefrom a suflicient distance to permit substantial expansion of the flame and the hot products of combustion while in said Venturi tube, a conduit means rounding said burner and extending therebeyond and spaced therefrom a suflicient dis tance to permit substantial expansion of the flame and the hot products of combustion while in said Venturi tube, a conduit means connecting said flue with said Venturi tube and enabling the drawing in of a portion of said Waste gases by the expansion of the hot combustion gases, and means located in said conduit means for controlling the flow of waste gases therethrough.
In testimony whereof, I have signed my name to this specification this 30th day of October, 1925i LUIS DE FLOREZ.
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2499814A (en) * 1945-05-23 1950-03-07 Joseph R Butler Combustion gas recirculating steam and air injector means for furnaces
US2504320A (en) * 1945-02-26 1950-04-18 Lindberg Eng Co Method of and apparatus for forced convection heating
US2603195A (en) * 1949-07-12 1952-07-15 Shell Dev Tubular heater and method of controlling radiation effects therein
US2648599A (en) * 1949-03-22 1953-08-11 Petro Chem Process Company Inc Heat control in vertical furnace by flue gas recirculation
US2688360A (en) * 1951-04-13 1954-09-07 Thermo Projects Inc Fuel combustion system, including gas assisted atomizer
US2849221A (en) * 1955-04-06 1958-08-26 Surface Combustion Corp Heat treating furnace
US2857961A (en) * 1954-07-13 1958-10-28 Brown Fintube Co Oil burners
DE1127523B (en) * 1957-05-07 1962-04-12 Wagner Hochdruck Dampfturbinen Liquid fuel burners
DE1177271B (en) * 1955-01-11 1964-09-03 Thermal Res & Engineering Corp Liquid fuel burner
US3238991A (en) * 1962-11-23 1966-03-08 Goldmann Otto Fuel oil gasification burner
US3838652A (en) * 1972-01-06 1974-10-01 Rodenhuis & Verloop Bv Furnace installation for burning liquid or gaseous fuel, in particular for a boiler
US4183306A (en) * 1976-10-08 1980-01-15 Kureha Kagaku Kogyo Kabushiki Kaisha Hot gas recirculation type burning furnace
US4355601A (en) * 1981-09-25 1982-10-26 Conoco Inc. Recirculating flue gas fluidized bed heater
US4438756A (en) * 1982-12-13 1984-03-27 Joseph G. Chamberlain Apparatus and method for accomplishing efficient burning of biomass fuel materials
US4760803A (en) * 1985-10-23 1988-08-02 Schulz Johann G Process for generating energy in a furnace or combustion engine
CN103322798A (en) * 2013-05-23 2013-09-25 江阴江顺铝型材成套设备制造有限公司 Air-blowing type anti-vortex combustion chamber for hot-shearing furnace

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2504320A (en) * 1945-02-26 1950-04-18 Lindberg Eng Co Method of and apparatus for forced convection heating
US2499814A (en) * 1945-05-23 1950-03-07 Joseph R Butler Combustion gas recirculating steam and air injector means for furnaces
US2648599A (en) * 1949-03-22 1953-08-11 Petro Chem Process Company Inc Heat control in vertical furnace by flue gas recirculation
US2603195A (en) * 1949-07-12 1952-07-15 Shell Dev Tubular heater and method of controlling radiation effects therein
US2688360A (en) * 1951-04-13 1954-09-07 Thermo Projects Inc Fuel combustion system, including gas assisted atomizer
US2857961A (en) * 1954-07-13 1958-10-28 Brown Fintube Co Oil burners
DE1177271B (en) * 1955-01-11 1964-09-03 Thermal Res & Engineering Corp Liquid fuel burner
US2849221A (en) * 1955-04-06 1958-08-26 Surface Combustion Corp Heat treating furnace
DE1127523B (en) * 1957-05-07 1962-04-12 Wagner Hochdruck Dampfturbinen Liquid fuel burners
US3238991A (en) * 1962-11-23 1966-03-08 Goldmann Otto Fuel oil gasification burner
US3838652A (en) * 1972-01-06 1974-10-01 Rodenhuis & Verloop Bv Furnace installation for burning liquid or gaseous fuel, in particular for a boiler
US4183306A (en) * 1976-10-08 1980-01-15 Kureha Kagaku Kogyo Kabushiki Kaisha Hot gas recirculation type burning furnace
US4355601A (en) * 1981-09-25 1982-10-26 Conoco Inc. Recirculating flue gas fluidized bed heater
US4438756A (en) * 1982-12-13 1984-03-27 Joseph G. Chamberlain Apparatus and method for accomplishing efficient burning of biomass fuel materials
US4760803A (en) * 1985-10-23 1988-08-02 Schulz Johann G Process for generating energy in a furnace or combustion engine
CN103322798A (en) * 2013-05-23 2013-09-25 江阴江顺铝型材成套设备制造有限公司 Air-blowing type anti-vortex combustion chamber for hot-shearing furnace

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