US3909188A - Fuel burner for liquid and gaseous fuels - Google Patents

Fuel burner for liquid and gaseous fuels Download PDF

Info

Publication number
US3909188A
US3909188A US441837A US44183774A US3909188A US 3909188 A US3909188 A US 3909188A US 441837 A US441837 A US 441837A US 44183774 A US44183774 A US 44183774A US 3909188 A US3909188 A US 3909188A
Authority
US
United States
Prior art keywords
air
fuel
atomizing
burner system
atomizing nozzle
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
Application number
US441837A
Inventor
Wallace W Velie
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from US00282694A external-priority patent/US3847537A/en
Application filed by Individual filed Critical Individual
Priority to US441837A priority Critical patent/US3909188A/en
Priority to CA219,809A priority patent/CA1019667A/en
Application granted granted Critical
Publication of US3909188A publication Critical patent/US3909188A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/36Details, e.g. burner cooling means, noise reduction means
    • F23D11/40Mixing tubes or chambers; Burner heads
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/10Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space the spraying being induced by a gaseous medium, e.g. water vapour
    • 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
    • F23D17/002Burners for combustion conjointly or alternatively of gaseous or liquid or pulverulent fuel gaseous or liquid fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00Feeding or distributing other fuel to combustion apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2207/00Ignition devices associated with burner
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D2900/00Special features of, or arrangements for burners using fluid fuels or solid fuels suspended in a carrier gas
    • F23D2900/11401Flame intercepting baffles forming part of burner head

Definitions

  • a fuel burner system comprises an air-atomizing fuel nozzle, an air compressor, liquid and gaseous fuel sources and a valve in the delivery line from the liquid and gaseous fuel reservoirs to the nozzle to select the type of fuel (i.e. liquid or gaseous) delivered to the nozzle in accordance with one aspect of the disclo sure.
  • the liquid fuel source may be a reservoir which is pressurized by the air compressor to deliver the fuel to the air atomizing nozzle.
  • the vacuum side of the air compressor may be periodically connected to the fuel reservoir through suitable valving to provide an automatic reservoir refilling capability.
  • the air compressor then acts not only to supply atomization (primary) air, but also to deliver liquid fuel to the nozzle during the liquid fuel burning cycle, and to draw liquid fuel from a remote liquid fuel supply source during the liquid fuel reservoir refilling cycle.
  • a flame spreader is employed in combination with the ainatomizing nozzle according to another aspect of the disclosure to stabilize and shape the flame. The position and diameter of the flame spreader are set to provide optimum fuel burning characteristics.
  • a fuel nozzle is essential to most fuel burners and consists of a device to prepare the fuel, gaseous or liquid, for efficient combustion. Such devices have a variety of configurations, depending upon the physical characteristics of the fuel being consumed.
  • gaseous fuel nozzles consist of simple metering devices or orifices. Gas under its natural or supply system pressure is forced through the ori fice, downstream of which is usually a tube to conduct the naturally aspirated mixture of fuel and entrapped air to a burner head.
  • liquid fuel nozzles typically use high fuel pressure, swirl and mechanical techniques to create a spray, which is directed into the burner where it is mixed with a forced supply of air and burned.
  • a disadvantage of the above gaseous and liquid fuel nozzles is that they have functionally different designs for fundamentally different processes; therefore, they are not mutually interchangeable. Increasing emphasis upon dual fuel burning appliances enhances the need for a common fuel nozzle.
  • a nozzle In order for a nozzle to be compatible with both gas or liquid fuels, it must effectively disperse gaseous fuels, as well as atomize liquid fuels, and entrain ambient air. Experiments have shown that liquid fuels when atomized to sufficiently small drops will burn with characteristics approaching a gas. However, most of the liquid spray nozzles currently available produce a wide range of drop sizes. The importance of this can be illustrated by the fact that if only one drop in 100 is times the average drop size, it contains 90 percent of the fuel spray volume, and therefore, controls the combustion process. Many pneumatic atomizers are capable of relatively small and uniform drop production, although those on the market have neglected to consider their dual fuel (gas as well as liquid) possibilities. Many are inherently capable of excellent gas dispersion.
  • a compressed gas when expanded through an aperture it creates a region in the vicinity of its exit surface such that if fluids (liquidor gaseous) are introduced adjacent to that region, they will be drawn into the gas stream via surface tension and dispersed along with ambient air. If the fluid is a liquid, it will be concurrently shattered by the high velocity gas stream into uniformly small drops. Therefore, a pneumatic atomizer has the potential capability of accommodating both gaseous and liquid fuels as previously described.
  • this inven- It is a further objective of this invention to provide a burner which, in its simplest form, consists of an airatomizing nozzle, a compressed air source, liquid and gaseous fuel sources and a means of selecting the fuel to be consumed.
  • Yet another object of the present invention is to provide a fuel burner system in which a flame spreader is employed in combination with the atomizing nozzle to stabilize and shape the flame.
  • a simple fuel burner system emphasizing a compressed gas atomizing nozzle, a source of pressurized gas for dispersion of the fuel, sources of liquid and gaseous fuels, and regulators as required for regulating the flow of pressurized gas and fuel to the air-atomizing nozzle.
  • a valve is provided in the delivery line to the nozzle from the sources of liquid and gaseous fuel to select the type of fuel (i.e., liquid or gaseous) to be delivered to the nozzle.
  • the pressure side of the air compressor may be connected to both the air-atomizing nozzle and to the liquid reservoir to provide a fuel delivery means. Orifices or pressure regulators are provided in the line from the air compressor to the liquid fuel reservoir to control the air pressure in the liquid fuel reservoir. Additionally, the vacuum side of the air compressor may be periodically connected to the liquid fuel reservoir to provide reservoir refill capability. In this latter case, a valve is provided in the suction line of the air compressor for connecting the vacuum side of the air compressor to the liquid fuel reservoir during the refilling cycle. The valve may be operated by a mechanically actuated float switch operated by a float in the liquid fuel reservoir.
  • Suitable means may be optionally provided in the pressure line from the air compressor to regulate the primary air pressure to the air-atomizing nozzle. Also, a flame spreader may be employed downstream of the fuel nozzle to stabilize and shape the flame.
  • FIG. 1 represents one embodiment of a pneumatic type atomizer illustrating important design and performance features which adapt it to multiple fuel use.
  • FIG. 2 represents the simplest embodiment of the invention showing the relationship of major components, including the pneumatic atomizer.
  • FIG. 3 shows'an embodiment of FIG. 2 with a pressurized liquid fuel reservoir as a means of fuel delivery.
  • FIG. 4 shows an embodiment of FIG. 3 with liquid fuel refilling means for extending operation time.
  • FIG. 5 shows a self'contained embodiment of FIG. 2.
  • FIG.6 represents the flame spreader embodiment of the invention.
  • the fuel atomizer is illustrative of a configuration useful for multiple fuel operation. It consists of an open ended atomizer body 10 containing a Compressible flow nozzle 1 at the terminus of an air or gas conduit 2 and so constructed that when a compressed gas 33 is expanded through the aperture 4 a region is created in the vicinity of surfaces 5 and 8 such that liquid or gaseous fuel 31 introduced through a conduit 6 adjacent to surfaces 5 and 8 is efficiently and completely dispersed along with ambient air 11. Specific dimensions of the nozzle are important to effective performance of the nozzle using both liquid and gaseous fuels.
  • a sharp-edged air aperture is desirable, or more specifically, one in which the thickness of the edge 63 of air aperture 4 is as thin as possible and less than the hydraulic diameter (i.e., aperture area aperture perimeter) of air aperture 4.
  • the ratio of the mean diameter of gas conduit 2 to the hydraulic diameter of air aperture 4 should be greater than approximately 10.
  • the exit area of atomizing housing 10 should be less than about 0.4 square inch for a liquid fuel dispersion rate of about 1 g.p.h. since too large of an exit area may result in excessive exposure of volatile liquid fuels to combustion heat resulting in vaporization and surface burning. At the same time, the exit area should not be so small that operation on gaseous fuel produces excessive exit velocity.
  • the length (L) of the open end of the atomizer housing 10 above air aperture 4 should be minimized to enhance aspiration of the ambient air at the housing exit. Approximately one-fourth inch or less has been found to be acceptable for this length (L).
  • the fuel inlet should be as far below the aperture end of nozzle 1 as practical to avoid surface disturbance of liquid fuel and to uniformly distribute gaseous fuels around nozzle 1 prior to dispersion.
  • the fuel inlet conduit 6 should have as small a diameter as possible but large enough to avoid excessive gaseous fuel velocity and thus distortion of the dispersed gas.
  • the inside conduit area should not be less than about 3 X 10' in. per cu. ft./hr. of gaseous fuel flow rate.
  • FIG. 1 serves to illustrate the design principles involved in effective use of the pneumatic type nozzle.
  • FIG. 2 is a schematic representation of the simplest embodiment of the present invention.
  • the fuel burnersystem includes a source of pressurized gas, specifically illustrated as air compressor 100, fordispersion of the fuel, sources of liquid and gaseous fuels, 102 and 104, respectively, an air atomizing nozzle 106, and regulators lor regulating the flow or pressurized gas 108 and fuel 110 and 112 to the atomizing nozzle.
  • a valve 114 is provided in the delivery line 116 from the sources of liquid and gaseous fuel to the nozzle 102 to select the type of fuel (i.e., liquid or gaseous) delivered to the nozzle.
  • FIG. 3 is a schematic representation of a more sophisticated burner system of FIG. 2 wherein liquid fuel reservoir is pressurized by the air compressor 100.
  • the air pressure to reservoir 80 is regulated by pressure regulator 81 or other suitable means.
  • the air pressure serves as a means of delivering liquid fuel to the atomizer.
  • a valve 83 is placed in the fuel delivery line 116 to serve as a manual or automatic means of shutting off the burner.
  • This type of air-atomizing fuel burner system is particularly useful for portable burner applications requiring about 1.0 gallons per hour (hereinafter g.p.h.) burningrates such as construction heaters.
  • burning rates in the range of 0.1 to 1.0 g.p.h. can conveniently be provided using the burner system at primary air pressures between about 8 and 18 p.s.i.g.
  • the air pressure in liquid fuel reservoir 80 is regulated by a simple gas pressure regulator to about 1 p.s.i.g. I
  • FIG. 4 is a schematic representation of a more elaborate embodiment of the present invention wherein au tomatic fuel replenishment capability is added to the burner system of FIG. 3.
  • the liquid fuel refilling aspects of this system aredescribed in more detail in my copending application Ser. No. 282,694, filed Aug. 22, 1972, the disclosure of which is expressly incorporated herein by reference.
  • the first major component is air compressor which is of conventional design such as a reciprocating diaphragm pressure/vacuum pump and has three separate functions in the overall system. First, it supplies primary air to air-atomizing nozzle 14 to disperse the fuel. Second, it supplies air pressure to liquid fuel reservoir 12 to deliver liquid fuel to the nozzle. Third, the air compressor acts as a vacuum pump to refill liquid fuel reservoir 12 from a remote liquid fuel supply source 16 when the fuel level in the reservoir 12 reaches a predetermined low level.
  • the second major component of the fuel burner system is liquid fuel reservoir 12 which is also of conventional design.
  • the liquid fuel reservoir is sized to give a reasonable burning time (e.g. 10 to 15 minutes) at the desired burning rate (e.g. less than 1 g.p.h.) and to be compatible with the air compressor characteristics such that refill occurs fairly rapidly (e.g. 5 to 10 seconds).
  • fuel reservoir 12 is connected to the air pressure side of air compressor 100, and also to the fuel side of air atomizing nozzle 14.
  • reservoir 12 is connected to the vacuum side of air compressor 100, and also to remote liquid fuel supply source 16.
  • gaseous fuel supply source 17 which is also of conventional design. Liquid fuels which have no measurable vapor pressure at ambient conditions require a means of delivery. By contrast, most gaseous fuels (e.g., hydrogen, methane, petroleum gases) have a substantial vapor pressure which can be used for fuel delivery or the gaseous fuels can be obtained under pressure from a central delivery system.
  • fuel supply 17 is connected to the fuel side of air-atomizing nozzle 14.
  • air-atomizing nozzle 14 The fourth major component of the fuel burner system is air-atomizing nozzle 14.
  • airatomizing nozzle is used throughout the specification and claims in its generic sense as meaning a nozzle, such as the type shown in FIG. 1, in which fuel is prepared for combustion by low-pressure dispersion using a compressible gas (e.g., air) as the dispersing medium.
  • a compressible gas e.g., air
  • primary air gas
  • atomize fuel also delivered to the nozzle at low pressure (e.g. l to 4 p.s.i.g.).
  • suction line 26 of air compressor 100 is connected to ambient.
  • Air compressor 100 supplies primary air through air pressure line 18 to air-atomizing nozzle 14.
  • the pressure in air pressure line 18 is regulated by pressure regulator 22.
  • Part of the air pressure in air pressure line 18 is bled off through air pressure line to fuel reservoir 12.
  • the pressure in fuel reservoir 12 is controlled, for a given primary air pressure by the diameter ratio of flow restriction orifice 38 to flow restriction orifice 36.
  • the fuel level in liquid fuel reservoir 12 is at high level 56, float 52 is at its uppermost position, float switch 54 is open, the solenoid-operated valve 24 is connecting the vacuum side of air compressor 100 to ambient, and valve 43 is connecting the fuel side of nozzle 14 to liquid fuel reservoir 12.
  • the air pressure in fuel reservoir 12 forces the liquid fuel through delivery line 46 to air-atomizing nozzle 14, and the fuel flow rate is regulated by flow restrictor 48.
  • the liquid fuel from delivery line 46 is atomized into fine particles by the primary air from air pressure line 18 and is ignited and burned in the presence of secondary air in conventional manner.
  • liquid fuel reservoir 12 As the liquid fuel is burned at air-atomizing nozzle 14, the fuel level in liquid fuel reservoir 12 gradually drops to low level 58. At this level, float 52 closes float switch 54 which energizes the solenoid of valve 24 and connects the vacuum side of air compressor 100 to liquid fuel reservoir 12.
  • the vacuum in liquid fuel reservoir 12 is controlled, for a given air compressor vacuum pressure, by the diameter ratio of flow restriction orifice 38 to flow restriction orifice 36.
  • fuel is drawn into liquid fuel reservoir 12 through liquid fuel supply line 40 from the liquid fuel supply source 16 and is simultaneously filtered by filter 44.
  • float 52 opens float switch 54 which de-energizes the solenoid of valve 24 and reconnects the vacuum side of air compressor 100 to ambient, thus re-establishing the liquid fuel burning cycle.
  • valve 43 is manually operated to connect the fuel side of airatomizing nozzle 14 to gaseous fuel supply source 17.
  • Air compressor 100 supplies primary air through air pressure line 18 to air-atomizing nozzle 14.
  • the pressure in air pressure line 18 is regulated by pressure regulator 22.
  • Gaseous fuel is delivered through delivery line 46 to air-atomizing nozzle 14, and the fuel flow rate is regulated by fuel flow restrictor 49.
  • gaseous fuel from delivery line 46 is dispersed by the primary air from air pressure line 18 and is ignited and burned in the presence of secondary air.
  • FIG. 5 illustrates in schematic form a self-contained burner system of the present invention.
  • the dispersion gas for dispersion of the fuel is itself a gaseous fuel having significant vapor pressure at ambient conditions such as propane, butane, methane, etc.
  • the fuel may be the dispersion gas, another gas, or a liquid fuel such as diesel fuel, kerosene, waste oil, etc.
  • the dispersion gas and fuel may share source 120, as illustrated, or be separately contained.
  • the dispersion gas and fuel are metered to atomizer 122 from the top and bottom of supply source 120, respectively, by regulators 124 and 126, respectively.
  • the dispersion gas may also serve as a pilot flame 128 for the burner. No source of energy other than the pressure of the high vapor pressure dispersion gas is required for the burners operation.
  • only one source of dispersion gas has been illustrated, it will be appreciated that two sources will be required when burning both liquid and gaseous fuels.
  • FIG. 6 illustrates the air-atomizing nozzle and flame spreader combination of the present invention.
  • the air-atomizing nozzle and flame spreader combination of FIG. 6 is ideally suited for use in the overall airatomizing fuel burner system of FIGS. 2, 3 or 4, and, accordingly, will be described as part of these systems. It should be understood, however, that the airatomizing nozzle and flame spreader combination in accordance with this aspect of the invention and can be used with other primary air and fuel supply systems and that the air-atomizing nozzle described can be used without the flame spreader.
  • Flame spreader 66 can be formed from any conventional material such as stainless steel or ceramics. Flame spreader 66 is generally disc-shaped and typically has a flat, planar or convex flame engaging sur- I I face. The exact shape and materials of construction of the flame spreader 66, however, do not form part of the present invention. The flame spreader has been found to be particularly useful in fuel burner systems employing low fuel burning rates in the range between 0 and 1.5 g.p.h.
  • Flame spreader 66 may be supported relative to airatomizing nozzle 14 by simple legs 76 as illustrated in FIG. 6.
  • Air-atomizing nozzle 14 is supported by burner base 68.
  • Above the burner base 68 and attached to it is an optional flame shield 67.
  • Ignitor 78 is attached to burner base 68 and is of conventional design, such as a high voltage spark ignitor.
  • primary air disperses the fuel into fine particles or a mist as it expands through air aperture 62 of nozzle head 60. These fine particles or mist are mixed with secondary air which is drawn into the system above the atomizer by natural aspiration.
  • the sprayed fuel is ignited by ignitor 78 and the resulting flame directed perpendicular to flame spreader 66. At flame spreader 66, the flame is stabilized and shaped, the upper surface of flame shield 67 acts as a radiation shield.
  • Flame spreader 66 should be positioned perpendicular to air-atomizing nozzle 14 and approximately centered (i.e., within about 0.25 inch) on the nozzle. For optimum combustion, flame spreader 66 should be in the gaseous or hydroxyl type combustion zone. This zone is downstream from the drop vaporization zone and upstream from the yellow flame or carbonaceous combustion zone. If flame spreader 66 is too far into the drop vaporization zone, deposits from liquid vaporization and cracking will form on its surface. On the other hand. if flame spreader 66 is too large or too far into the yellow flame or carbonaceous zone, carbon will collect on its surface.
  • flame spreader 66 should be moved further away from air-atomizing nozzle 14 as the fuel spray is increased.
  • adequate combustion has been found to occur when the axial separation distance (X) between nozzle head 60 and flame spreader 66 is between about 1.5 and inches for low burning rates of between about 0.05 and 1.5 g.p.h., respectively.
  • D flame spreader diameter
  • X axial separation distance
  • the ignitor 78 location is not critical; however, it should be on the fringe of the spray and about 1.0 to 2.5 inches downstream from the air-atomizing nozzle for most applications.
  • the air-atomizing fuel burner system of FIG. 3 was employed in combination with the flame spreader and air-atomizing combination of FIG. 6.
  • the flame spreader diameter (D) and axial separation distance (X) between air-atomizing nozzle 62 and flame spreader 66 were 4 and 4.5 inches, respectively.
  • Flame spreader 66 was made of 309 stainless steel, and of conventional disc-shaped design with a flat, planar, flame engaging surface. It was positioned perpendicular to air-atomizing nozzle 14 with its center within 0.25 inch of the center of spray of air-atomizing nozzle 14.
  • Nozzle head 60 had an air aperture 62 size of 0.032 inch diameter with an edge thickness of about 5 thousandths of an inch. Referring to FIG.
  • the air pressure in the pressure line from air compressor 100 was 15 p.s.i.g.
  • An air pressure regulator 81 maintained the pressure in liquid fuel reservoir 102 at 1.25 p.s.i.g. which provided fuel delivery to air-atomizing nozzle 106.
  • the liquid fuel burning rate was 0.80 g.p.h.
  • Propane was used as the gaseous fuel and was contained in gaseous fuel supply source 104 under normal vapor pressure.
  • the propane pressure downstream of fuel pressure regulator 112 was 3.5 p.s.i.g.
  • the propane fuel burning rate was 1.2 g.p.h.
  • Three-way valve 114 was used to select the type of fuel (i.e., liquid or gaseous) supplied to airatomizing nozzle 106.
  • An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering liquid fuel to said air-atomizing nozzle means, means for delivering gaseous fuel to said air-atomizing nozzle means, means for selecting the type of fuel delivered to said air-atomizing nozzle means, and means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed -fuel can be ignited in the presence of secondary air to produce a combustion flame.
  • said means for delivering liquid fuel to said airatomizing nozzle means from said liquid fuel reservoir means includes a fuel flow restriction means for metering the flow of liquid fuel to said air-atomizing means.
  • said means for connecting the vacuum side of said air compressor means to said liquid fuel reservoir means includes means responsive to the fuel level in said liquid fuel reservoir and a valve pilot operated by said responsive means.
  • said means for supplying air under pressure to said air-atomizing nozzle means from said air compressor means includes means for regulating the air pressure supplied to said air-atomizing nozzle means.
  • An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering fuel to said air-atomizing nozzle means, means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to produce a combustion flame, and flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in the gaseous or hydroxyl-type combustion zone of said combustion flame.
  • a low pressure air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary air to atomize fuel, means for delivering fuel under low pressure to said air-atomizing nozzle means, means for delivering primary air to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to.
  • flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in the gaseous or hydroxyl-type combustion zone of said combustion flame.

Abstract

A fuel burner system comprises an air-atomizing fuel nozzle, an air compressor, liquid and gaseous fuel sources and a valve in the delivery line from the liquid and gaseous fuel reservoirs to the nozzle to select the type of fuel (i.e. liquid or gaseous) delivered to the nozzle in accordance with one aspect of the disclosure. The liquid fuel source may be a reservoir which is pressurized by the air compressor to deliver the fuel to the air atomizing nozzle. In addition, the vacuum side of the air compressor may be periodically connected to the fuel reservoir through suitable valving to provide an automatic reservoir refilling capability. The air compressor then acts not only to supply atomization (primary) air, but also to deliver liquid fuel to the nozzle during the liquid fuel burning cycle, and to draw liquid fuel from a remote liquid fuel supply source during the liquid fuel reservoir refilling cycle. A flame spreader is employed in combination with the air-atomizing nozzle according to another aspect of the disclosure to stabilize and shape the flame. The position and diameter of the flame spreader are set to provide optimum fuel burning characteristics.

Description

States Patent [191 1*Sept. 30, 1975 [54] FUEL BURNER FOR LIQUID AND GASEOUS FUELS [76] Inventor: Wallace W. Velie, 616 W. 20th St.,
Upland, Calif. 91786 1 Notice: The portion of the term of this patent subsequent to Nov. 12, 1991,
has been disclaimcd.
[22] Filed: Feb. 12, 1974 [21] Appl. No.: 441,837
Related US. Application Data [63] Continuation-impart of Ser. No. 282,694, Aug. 22,
1972, Pat. NO. 3,847,537.
[52] US. Cl. 431/285; 431/90; 431/347 [51] Int. Cl. F23D 11/10 [58] Field of Search... 431/278, 280, 284, 285-347,
43l/DIG. 21, DIG. 22; 239/4165, 423, 424
Primarv E.raminer-Edward G. Favors Attorney, Agent, or FirmF1eit & Jacobson [57] ABSTRACT A fuel burner system comprises an air-atomizing fuel nozzle, an air compressor, liquid and gaseous fuel sources and a valve in the delivery line from the liquid and gaseous fuel reservoirs to the nozzle to select the type of fuel (i.e. liquid or gaseous) delivered to the nozzle in accordance with one aspect of the disclo sure. The liquid fuel source may be a reservoir which is pressurized by the air compressor to deliver the fuel to the air atomizing nozzle. In addition, the vacuum side of the air compressor may be periodically connected to the fuel reservoir through suitable valving to provide an automatic reservoir refilling capability. The air compressor then acts not only to supply atomization (primary) air, but also to deliver liquid fuel to the nozzle during the liquid fuel burning cycle, and to draw liquid fuel from a remote liquid fuel supply source during the liquid fuel reservoir refilling cycle. A flame spreader is employed in combination with the ainatomizing nozzle according to another aspect of the disclosure to stabilize and shape the flame. The position and diameter of the flame spreader are set to provide optimum fuel burning characteristics.
27 Claims, 6 Drawing Figures US. Patent Sept. 30,1975 Sheet 1 of3 3,909,188
Fig. 5 /24 /2a R V /22 Fig me FUEL ' US. Patent Sept. 30,1975 Sheet2 of3 3,909,188
NQQ
kawmsk t US. Patent Sept. 30,1975 Sheet 3 of3 3,909,188
FUEL BURNER FOR LIQUID AND GASEOUS FUELS CROSS-REFERENCE TO RELATED APPLICATION This is a continuation-in-part of application Ser. No. 282,694 filed Aug. 22, 1972 now US. Pat. No. 3,847,537.
BACKGROUND OF THE INVENTION There is an increasing interest in burners having multiple fuel capability, particularly those which can burn gaseous as well as liquid fuels. An optimum burner is one which requires the least mechanical readjustment during fuel switchover and which produces approximately the same flame pattern, cleanliness, and combustion efficiency, regardless of the fuel used.
A fuel nozzle is essential to most fuel burners and consists of a device to prepare the fuel, gaseous or liquid, for efficient combustion. Such devices have a variety of configurations, depending upon the physical characteristics of the fuel being consumed.
Almost exclusively, gaseous fuel nozzles consist of simple metering devices or orifices. Gas under its natural or supply system pressure is forced through the ori fice, downstream of which is usually a tube to conduct the naturally aspirated mixture of fuel and entrapped air to a burner head. By contrast, liquid fuel nozzles typically use high fuel pressure, swirl and mechanical techniques to create a spray, which is directed into the burner where it is mixed with a forced supply of air and burned.
A disadvantage of the above gaseous and liquid fuel nozzles is that they have functionally different designs for fundamentally different processes; therefore, they are not mutually interchangeable. Increasing emphasis upon dual fuel burning appliances enhances the need for a common fuel nozzle.
In order for a nozzle to be compatible with both gas or liquid fuels, it must effectively disperse gaseous fuels, as well as atomize liquid fuels, and entrain ambient air. Experiments have shown that liquid fuels when atomized to sufficiently small drops will burn with characteristics approaching a gas. However, most of the liquid spray nozzles currently available produce a wide range of drop sizes. The importance of this can be illustrated by the fact that if only one drop in 100 is times the average drop size, it contains 90 percent of the fuel spray volume, and therefore, controls the combustion process. Many pneumatic atomizers are capable of relatively small and uniform drop production, although those on the market have neglected to consider their dual fuel (gas as well as liquid) possibilities. Many are inherently capable of excellent gas dispersion. For example, when a compressed gas is expanded through an aperture it creates a region in the vicinity of its exit surface such that if fluids (liquidor gaseous) are introduced adjacent to that region, they will be drawn into the gas stream via surface tension and dispersed along with ambient air. If the fluid is a liquid, it will be concurrently shattered by the high velocity gas stream into uniformly small drops. Therefore, a pneumatic atomizer has the potential capability of accommodating both gaseous and liquid fuels as previously described.
Accordingly, it is the primary objective of this inven- It is a further objective of this invention to provide a burner which, in its simplest form, consists of an airatomizing nozzle, a compressed air source, liquid and gaseous fuel sources and a means of selecting the fuel to be consumed.
It is a still further objective of this invention to define designs for liquid fuel sources, which will increase burner self sufficiency.
Yet another object of the present invention is to provide a fuel burner system in which a flame spreader is employed in combination with the atomizing nozzle to stabilize and shape the flame.
Still further objects and advantages of the present invention will become apparent upon reading the following specification and claims, taken in conjunction with the accompanying drawings.
SUMMARY OF THE INVENTION A simple fuel burner system is provided emphasizing a compressed gas atomizing nozzle, a source of pressurized gas for dispersion of the fuel, sources of liquid and gaseous fuels, and regulators as required for regulating the flow of pressurized gas and fuel to the air-atomizing nozzle. A valve is provided in the delivery line to the nozzle from the sources of liquid and gaseous fuel to select the type of fuel (i.e., liquid or gaseous) to be delivered to the nozzle.
In a more sophisticated version of the burner, the pressure side of the air compressor may be connected to both the air-atomizing nozzle and to the liquid reservoir to provide a fuel delivery means. Orifices or pressure regulators are provided in the line from the air compressor to the liquid fuel reservoir to control the air pressure in the liquid fuel reservoir. Additionally, the vacuum side of the air compressor may be periodically connected to the liquid fuel reservoir to provide reservoir refill capability. In this latter case, a valve is provided in the suction line of the air compressor for connecting the vacuum side of the air compressor to the liquid fuel reservoir during the refilling cycle. The valve may be operated by a mechanically actuated float switch operated by a float in the liquid fuel reservoir.
Suitable means may be optionally provided in the pressure line from the air compressor to regulate the primary air pressure to the air-atomizing nozzle. Also, a flame spreader may be employed downstream of the fuel nozzle to stabilize and shape the flame.
The overall operation of the fuel burner system and its embodiments will now be described.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 represents one embodiment of a pneumatic type atomizer illustrating important design and performance features which adapt it to multiple fuel use.
FIG. 2 represents the simplest embodiment of the invention showing the relationship of major components, including the pneumatic atomizer.
FIG. 3 shows'an embodiment of FIG. 2 with a pressurized liquid fuel reservoir as a means of fuel delivery.
FIG. 4 shows an embodiment of FIG. 3 with liquid fuel refilling means for extending operation time.
FIG. 5 shows a self'contained embodiment of FIG. 2.
FIG."6 represents the flame spreader embodiment of the invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring to FIG. 1, the fuel atomizer is illustrative of a configuration useful for multiple fuel operation. It consists of an open ended atomizer body 10 containing a Compressible flow nozzle 1 at the terminus of an air or gas conduit 2 and so constructed that when a compressed gas 33 is expanded through the aperture 4 a region is created in the vicinity of surfaces 5 and 8 such that liquid or gaseous fuel 31 introduced through a conduit 6 adjacent to surfaces 5 and 8 is efficiently and completely dispersed along with ambient air 11. Specific dimensions of the nozzle are important to effective performance of the nozzle using both liquid and gaseous fuels. In particular, a sharp-edged air aperture is desirable, or more specifically, one in which the thickness of the edge 63 of air aperture 4 is as thin as possible and less than the hydraulic diameter (i.e., aperture area aperture perimeter) of air aperture 4. Furthermore, the ratio of the mean diameter of gas conduit 2 to the hydraulic diameter of air aperture 4 should be greater than approximately 10. Some variation in the above dimensions is obviously possible without seriou sly affecting nozzle performance. The best hydraulic diameter for air aperture 4 appears to be between about lO and 3O thousandths of an inch and the preferred thickness of edge 63 is about 5 thousandths of an inch. It should be noted that air aperture 4 has been greatly enlarged in FIG. 1 for the purposes of illustration/The exit area of atomizing housing 10 should be less than about 0.4 square inch for a liquid fuel dispersion rate of about 1 g.p.h. since too large of an exit area may result in excessive exposure of volatile liquid fuels to combustion heat resulting in vaporization and surface burning. At the same time, the exit area should not be so small that operation on gaseous fuel produces excessive exit velocity. The length (L) of the open end of the atomizer housing 10 above air aperture 4 should be minimized to enhance aspiration of the ambient air at the housing exit. Approximately one-fourth inch or less has been found to be acceptable for this length (L). Concurrently, the fuel inlet should be as far below the aperture end of nozzle 1 as practical to avoid surface disturbance of liquid fuel and to uniformly distribute gaseous fuels around nozzle 1 prior to dispersion. The fuel inlet conduit 6 should have as small a diameter as possible but large enough to avoid excessive gaseous fuel velocity and thus distortion of the dispersed gas. The inside conduit area should not be less than about 3 X 10' in. per cu. ft./hr. of gaseous fuel flow rate.
An open ended atomizer body is not a mandatory requirement'of the pneumatic type atomizer and successful performance is possible by placing fuel conduit 6 close to surface Sand adjacent to the aperture 4. The broad aspect of the invention is recognition of the fact that the pneumatic type fuel atomizer configurations generally have the characteristics which make them potentially applicable to dual fuel operation. FIG. 1 serves to illustrate the design principles involved in effective use of the pneumatic type nozzle.
FIG. 2 is a schematic representation of the simplest embodiment of the present invention. Broadly speaking, the fuel burnersystem includes a source of pressurized gas, specifically illustrated as air compressor 100, fordispersion of the fuel, sources of liquid and gaseous fuels, 102 and 104, respectively, an air atomizing nozzle 106, and regulators lor regulating the flow or pressurized gas 108 and fuel 110 and 112 to the atomizing nozzle. A valve 114 is provided in the delivery line 116 from the sources of liquid and gaseous fuel to the nozzle 102 to select the type of fuel (i.e., liquid or gaseous) delivered to the nozzle.
FIG. 3 is a schematic representation of a more sophisticated burner system of FIG. 2 wherein liquid fuel reservoir is pressurized by the air compressor 100. The air pressure to reservoir 80 is regulated by pressure regulator 81 or other suitable means. The air pressure serves as a means of delivering liquid fuel to the atomizer. A valve 83 is placed in the fuel delivery line 116 to serve as a manual or automatic means of shutting off the burner.
This type of air-atomizing fuel burner system is particularly useful for portable burner applications requiring about 1.0 gallons per hour (hereinafter g.p.h.) burningrates such as construction heaters. By wayof illustration, burning rates in the range of 0.1 to 1.0 g.p.h. can conveniently be provided using the burner system at primary air pressures between about 8 and 18 p.s.i.g. The air pressure in liquid fuel reservoir 80 is regulated by a simple gas pressure regulator to about 1 p.s.i.g. I
FIG. 4 is a schematic representation of a more elaborate embodiment of the present invention wherein au tomatic fuel replenishment capability is added to the burner system of FIG. 3. The liquid fuel refilling aspects of this system aredescribed in more detail in my copending application Ser. No. 282,694, filed Aug. 22, 1972, the disclosure of which is expressly incorporated herein by reference. The first major component is air compressor which is of conventional design such as a reciprocating diaphragm pressure/vacuum pump and has three separate functions in the overall system. First, it supplies primary air to air-atomizing nozzle 14 to disperse the fuel. Second, it supplies air pressure to liquid fuel reservoir 12 to deliver liquid fuel to the nozzle. Third, the air compressor acts as a vacuum pump to refill liquid fuel reservoir 12 from a remote liquid fuel supply source 16 when the fuel level in the reservoir 12 reaches a predetermined low level.
The second major component of the fuel burner system is liquid fuel reservoir 12 which is also of conventional design. The liquid fuel reservoir is sized to give a reasonable burning time (e.g. 10 to 15 minutes) at the desired burning rate (e.g. less than 1 g.p.h.) and to be compatible with the air compressor characteristics such that refill occurs fairly rapidly (e.g. 5 to 10 seconds). During the liquid fuel burning cycle, fuel reservoir 12 is connected to the air pressure side of air compressor 100, and also to the fuel side of air atomizing nozzle 14. During the liquid fuel refilling cycle, reservoir 12 is connected to the vacuum side of air compressor 100, and also to remote liquid fuel supply source 16.
The third major component of the fuel burner system is gaseous fuel supply source 17 which is also of conventional design. Liquid fuels which have no measurable vapor pressure at ambient conditions require a means of delivery. By contrast, most gaseous fuels (e.g., hydrogen, methane, petroleum gases) have a substantial vapor pressure which can be used for fuel delivery or the gaseous fuels can be obtained under pressure from a central delivery system. During the gaseous fuel burning cycle, fuel supply 17 is connected to the fuel side of air-atomizing nozzle 14.
The fourth major component of the fuel burner system is air-atomizing nozzle 14. The term airatomizing nozzle is used throughout the specification and claims in its generic sense as meaning a nozzle, such as the type shown in FIG. 1, in which fuel is prepared for combustion by low-pressure dispersion using a compressible gas (e.g., air) as the dispersing medium. In low-pressure atomization, primary air (gas) is delivered to the nozzle at relatively low pressure (e.g., l to 25 p.s.i.g.) and used to atomize fuel also delivered to the nozzle at low pressure (e.g. l to 4 p.s.i.g.).
The overall operation of the fuel burner system will now be described. During the liquid fuel burning cycle, suction line 26 of air compressor 100 is connected to ambient. Air compressor 100 supplies primary air through air pressure line 18 to air-atomizing nozzle 14. The pressure in air pressure line 18 is regulated by pressure regulator 22. Part of the air pressure in air pressure line 18 is bled off through air pressure line to fuel reservoir 12. The pressure in fuel reservoir 12 is controlled, for a given primary air pressure by the diameter ratio of flow restriction orifice 38 to flow restriction orifice 36. At the start of the liquid fuel burning cycle, the fuel level in liquid fuel reservoir 12 is at high level 56, float 52 is at its uppermost position, float switch 54 is open, the solenoid-operated valve 24 is connecting the vacuum side of air compressor 100 to ambient, and valve 43 is connecting the fuel side of nozzle 14 to liquid fuel reservoir 12. The air pressure in fuel reservoir 12 forces the liquid fuel through delivery line 46 to air-atomizing nozzle 14, and the fuel flow rate is regulated by flow restrictor 48. At nozzle 14, the liquid fuel from delivery line 46 is atomized into fine particles by the primary air from air pressure line 18 and is ignited and burned in the presence of secondary air in conventional manner.
As the liquid fuel is burned at air-atomizing nozzle 14, the fuel level in liquid fuel reservoir 12 gradually drops to low level 58. At this level, float 52 closes float switch 54 which energizes the solenoid of valve 24 and connects the vacuum side of air compressor 100 to liquid fuel reservoir 12. The vacuum in liquid fuel reservoir 12 is controlled, for a given air compressor vacuum pressure, by the diameter ratio of flow restriction orifice 38 to flow restriction orifice 36. During the liquid fuel refilling cycle, fuel is drawn into liquid fuel reservoir 12 through liquid fuel supply line 40 from the liquid fuel supply source 16 and is simultaneously filtered by filter 44. Once the fuel in liquid fuel reservoir 12 has reached high level 56, float 52 opens float switch 54 which de-energizes the solenoid of valve 24 and reconnects the vacuum side of air compressor 100 to ambient, thus re-establishing the liquid fuel burning cycle.
During the gaseous fuel burning cycle, valve 43 is manually operated to connect the fuel side of airatomizing nozzle 14 to gaseous fuel supply source 17. Air compressor 100 supplies primary air through air pressure line 18 to air-atomizing nozzle 14. The pressure in air pressure line 18 is regulated by pressure regulator 22. Gaseous fuel is delivered through delivery line 46 to air-atomizing nozzle 14, and the fuel flow rate is regulated by fuel flow restrictor 49. At nozzle 14, gaseous fuel from delivery line 46 is dispersed by the primary air from air pressure line 18 and is ignited and burned in the presence of secondary air.
FIG. 5 illustrates in schematic form a self-contained burner system of the present invention. In this embodiment, the dispersion gas for dispersion of the fuel is itself a gaseous fuel having significant vapor pressure at ambient conditions such as propane, butane, methane, etc. The fuel may be the dispersion gas, another gas, or a liquid fuel such as diesel fuel, kerosene, waste oil, etc. The dispersion gas and fuel may share source 120, as illustrated, or be separately contained. The dispersion gas and fuel are metered to atomizer 122 from the top and bottom of supply source 120, respectively, by regulators 124 and 126, respectively. The dispersion gas may also serve as a pilot flame 128 for the burner. No source of energy other than the pressure of the high vapor pressure dispersion gas is required for the burners operation. Although only one source of dispersion gas has been illustrated, it will be appreciated that two sources will be required when burning both liquid and gaseous fuels.
Turning now to another aspect of the present invention, FIG. 6 illustrates the air-atomizing nozzle and flame spreader combination of the present invention. The air-atomizing nozzle and flame spreader combination of FIG. 6 is ideally suited for use in the overall airatomizing fuel burner system of FIGS. 2, 3 or 4, and, accordingly, will be described as part of these systems. It should be understood, however, that the airatomizing nozzle and flame spreader combination in accordance with this aspect of the invention and can be used with other primary air and fuel supply systems and that the air-atomizing nozzle described can be used without the flame spreader.
Flame spreader 66 can be formed from any conventional material such as stainless steel or ceramics. Flame spreader 66 is generally disc-shaped and typically has a flat, planar or convex flame engaging sur- I I face. The exact shape and materials of construction of the flame spreader 66, however, do not form part of the present invention. The flame spreader has been found to be particularly useful in fuel burner systems employing low fuel burning rates in the range between 0 and 1.5 g.p.h.
Flame spreader 66 may be supported relative to airatomizing nozzle 14 by simple legs 76 as illustrated in FIG. 6. Air-atomizing nozzle 14 is supported by burner base 68. Above the burner base 68 and attached to it is an optional flame shield 67. Ignitor 78 is attached to burner base 68 and is of conventional design, such as a high voltage spark ignitor.
During operation, primary air disperses the fuel into fine particles or a mist as it expands through air aperture 62 of nozzle head 60. These fine particles or mist are mixed with secondary air which is drawn into the system above the atomizer by natural aspiration. The sprayed fuel is ignited by ignitor 78 and the resulting flame directed perpendicular to flame spreader 66. At flame spreader 66, the flame is stabilized and shaped, the upper surface of flame shield 67 acts as a radiation shield.
Flame spreader 66 should be positioned perpendicular to air-atomizing nozzle 14 and approximately centered (i.e., within about 0.25 inch) on the nozzle. For optimum combustion, flame spreader 66 should be in the gaseous or hydroxyl type combustion zone. This zone is downstream from the drop vaporization zone and upstream from the yellow flame or carbonaceous combustion zone. If flame spreader 66 is too far into the drop vaporization zone, deposits from liquid vaporization and cracking will form on its surface. On the other hand. if flame spreader 66 is too large or too far into the yellow flame or carbonaceous zone, carbon will collect on its surface.
Since increasing the fuel spray rate increases the flame length, flame spreader 66 should be moved further away from air-atomizing nozzle 14 as the fuel spray is increased. By way of illustration, adequate combustion has been found to occur when the axial separation distance (X) between nozzle head 60 and flame spreader 66 is between about 1.5 and inches for low burning rates of between about 0.05 and 1.5 g.p.h., respectively. For optimum burning characteristics for most burner applications, it has been found best to use a ratio of flame spreader diameter (D) to axial separation distance (X) of about 1. The ignitor 78 location is not critical; however, it should be on the fringe of the spray and about 1.0 to 2.5 inches downstream from the air-atomizing nozzle for most applications.
To illustrate the present invention, the air-atomizing fuel burner system of FIG. 3 was employed in combination with the flame spreader and air-atomizing combination of FIG. 6. Referring to FIG. 6, the flame spreader diameter (D) and axial separation distance (X) between air-atomizing nozzle 62 and flame spreader 66 were 4 and 4.5 inches, respectively. Flame spreader 66 was made of 309 stainless steel, and of conventional disc-shaped design with a flat, planar, flame engaging surface. It was positioned perpendicular to air-atomizing nozzle 14 with its center within 0.25 inch of the center of spray of air-atomizing nozzle 14. Nozzle head 60 had an air aperture 62 size of 0.032 inch diameter with an edge thickness of about 5 thousandths of an inch. Referring to FIG. 3, the air pressure in the pressure line from air compressor 100 was 15 p.s.i.g. An air pressure regulator 81 maintained the pressure in liquid fuel reservoir 102 at 1.25 p.s.i.g. which provided fuel delivery to air-atomizing nozzle 106. The liquid fuel burning rate was 0.80 g.p.h. Propane was used as the gaseous fuel and was contained in gaseous fuel supply source 104 under normal vapor pressure. The propane pressure downstream of fuel pressure regulator 112 was 3.5 p.s.i.g. The propane fuel burning rate was 1.2 g.p.h. Three-way valve 114 was used to select the type of fuel (i.e., liquid or gaseous) supplied to airatomizing nozzle 106.
The invention in its broader aspects is not limited to the specific details shown and described, and departures may be made from such details without departing from the principles of the invention and without sacrificing its chief advantages.
What is claimed is:
1. An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering liquid fuel to said air-atomizing nozzle means, means for delivering gaseous fuel to said air-atomizing nozzle means, means for selecting the type of fuel delivered to said air-atomizing nozzle means, and means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed -fuel can be ignited in the presence of secondary air to produce a combustion flame.
2. The air-atomizing fuel burner system of claim 1 in which said primary gas is air and said primary gas delivery means, includes air compressor means.
3. The air-atomizing fuel burner of claim 2 and further comprising fuel reservoir means for storing liquid fuel, means for delivering liquid fuel from said liquid fuel reservoir means to said air-atomizing nozzle means, means for delivering a portion of said air under pressure from said air compressor means to said liquid fuel reservoir means.
4. The air-atomizing fuel burner system of claim 3 in which said means for delivering a portion of the air under pressure from said air compressor means to said liquid fuel reservoir means includes air flow restriction or regulation means for controlling the pressure of air to said liquid fuel reservoir means.
5. The air-atomizing fuel burner system of claim 3 in which said means for delivering liquid fuel to said airatomizing nozzle means from said liquid fuel reservoir means includes a fuel flow restriction means for metering the flow of liquid fuel to said air-atomizing means.
6. The air-atomizing fuel burner system of claim 3 and further comprising means for supplying liquid fuel to said fuel reservoir means from a remote fuel supply source, and means for connecting the vacuum side of said air compressor means to ambient during the liquid fuel burning cycle of said air-atomizing nozzle means and to said liquid fuel reservoir during the liquid fuel reservoir refilling cycle.
7. The air-atomizing fuel burner system of claim 6 in which said means for connecting the vacuum side of said air compressor means to said liquid fuel reservoir means includes means for restricting the flow of air from said liquid fuel reservoir means.
8. The air-atomizing fuel burner system of claim 6 in which said means for connecting the vacuum side of said air compressor means to said liquid fuel reservoir means includes means responsive to the fuel level in said liquid fuel reservoir and a valve pilot operated by said responsive means.
9. The air-atomizing fuel burner system of claim 2 in which said means for supplying air under pressure to said air-atomizing nozzle means from said air compressor means includes means for regulating the air pressure supplied to said air-atomizing nozzle means.
10. The air-atomizing fuel burner system of claim 2 and further comprising flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame.
11. The air-atomizing fuel burner system of claim 10 in which the ratio of flame spreader diameter to separation distance between said flame spreader and airatomizing nozzle is about 1.
12. The air-atomizing fuel burner system of claim 10 in which said flame spreader is located in the gaseous or hydroxyl type combustion zone in said combustion flame.
13. The air-atomizing fuel burner system of claim 10 in which the location of said flame spreader relative to said air-atomizing nozzle is based on the fuel burning rate.
14. The air-atomizing fuel burner system of claim 13 in which said flame spreader is moved further downstream from said air-atomizing nozzle as the fuel burning rate increases.
15. The air-atomizing fuel burner system of claim 10 in which said flame spreader is between about 1.5 and inches downstream from said air-atomizing nozzle means.
16. The air-atomizing fuel burner system of claim 2 in which said means for delivering gaseous fuel to said air-atomizing nozzle means includes means for regulating the flow of gaseous fuel to said air-atomizing nozzle means.
17. The air-atomizing fuel burner system of claim 16 in which said means for regulating the flow of gaseous fuel to said air-atomizing nozzle means is a gaseous fuel pressure regulator.
18. The air-atomizing fuel burner system of claim 2 in which said means for controlling the type of fuel delivered to said air-atomizing nozzle means comprises a three-way valve.
19. The air-atomizing fuel burner system of claim 2 in which said air-atomizing nozzle means comprises an air aperture having an edge with a thickness approximately equal to or less than the hydraulic diameter of said air aperture.
20. The air-atomizing fuel burner system of claim 18 in which said hydraulic diameter is about to 30 mils.
21. The air'atomizing fuel burner system of claim 1 and further comprising means for igniting the dispersed fuel in the presence of said secondary air to produce said combustion flame.
22. An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering fuel to said air-atomizing nozzle means, means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to produce a combustion flame, and flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in the gaseous or hydroxyl-type combustion zone of said combustion flame.
23. The air-atomizing fuel burner system of claim 22 in which the ratio of flame spreader diameter to separation distance between said flame spreader and airatomizing nozzle means is about 1.
24. The air-atomizing fuel burner system of claim 22 in which said flame spreader is between about 1.5 and 5 inches downstream from said air-atomizing nozzle.
25. A low pressure air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary air to atomize fuel, means for delivering fuel under low pressure to said air-atomizing nozzle means, means for delivering primary air to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to.
produce a combustion flame, and flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in the gaseous or hydroxyl-type combustion zone of said combustion flame.
26. The air-atomizing fuel burner system of claim 25 in which said primary air and said fuel are each delivered to said air-atomizing nozzle means at a pressure of about 1 to 15 psi.
27. The air atomizing fuel burner system of claim 25 in which said fuel is delivered to said air-atomizing nozzle means at a pressure of about 1 to 4 psi.

Claims (27)

1. An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering liquid fuel to said air-atomizing nozzle means, means for delivering gaseous fuel to said airatomizing nozzle means, means for selecting the type of fuel delivered to said air-atomizing nozzle means, and means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to produce a combustion flame.
2. The air-atomizing fuel burner system of claim 1 in which said primary gas is air and said primary gas delivery means includes air compressor means.
3. The air-atomizing fuel burner of claim 2 and further comprising fuel reservoir means for storing liquid fuel, means for delivering liquid fuel from said liquid fuel reservoir means to said air-atomizing nozzle means, means for delivering a portion of said air under pressure from said air compressor means to said liquid fuel reservoir means.
4. The air-atomizing fuel burner system of claim 3 in which said means for delivering a portion of the air under pressure from said air compressor means to said liquid fuel reservoir means includes air flow restriction or regulation means for controlling the pressure of air to said liquid fuel reservoir means.
5. The air-atomizing fuel burner system of claim 3 in which said means for delivering liquid fuel to said air-atomizing nozzle means from said liquid fuel reservoir means includes a fuel flow restriction means for metering the flow of liquid fuel to said air-atomizing means.
6. The air-atomizing fuel burner system of claim 3 and further comprising means for supplying liquid fuel to said fuel reservoir means from a remote fuel supply source, and means for connecting the vacuum side of said air compressor means to ambient during the liquid fuel burning cycle of said air-atomizing nozzle means and to said liquid fuel reservoir during the liquid fuel reservoir refilling cycle.
7. The air-atomizing fuel burner system of claim 6 in which said means for connecting the vacuum side of said air compressor means to said liquid fuel reservoir means includes means for restricting the flow of air from said liquid fuel reservoir means.
8. The air-atomizing fuel burner system of claim 6 in which said means for connecting the vacuum side of said air compressor means to said liquid fuel reservoir means includes means responsive to the fuel level in said liquid fuel reservoir and a valve pilot operated by said responsive means.
9. The air-atomizing fuel burner sYstem of claim 2 in which said means for supplying air under pressure to said air-atomizing nozzle means from said air-compressor means includes means for regulating the air pressure supplied to said air-atomizing nozzle means.
10. The air-atomizing fuel burner system of claim 2 and further comprising flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame.
11. The air-atomizing fuel burner system of claim 10 in which the ratio of flame spreader diameter to separation distance between said flame spreader and air-atomizing nozzle is about 1.
12. The air-atomizing fuel burner system of claim 10 in which said flame spreader is located in the gaseous or hydroxyl type combustion zone in said combustion flame.
13. The air-atomizing fuel burner system of claim 10 in which the location of said flame spreader relative to said air-atomizing nozzle is based on the fuel burning rate.
14. The air-atomizing fuel burner system of claim 13 in which said flame spreader is moved further downstream from said air-atomizing nozzle as the fuel burning rate increases.
15. The air-atomizing fuel burner system of claim 10 in which said flame spreader is between about 1.5 and 5 inches downstream from said air-atomizing nozzle means.
16. The air-atomizing fuel burner system of claim 2 in which said means for delivering gaseous fuel to said air-atomizing nozzle means includes means for regulating the flow of gaseous fuel to said air-atomizing nozzle means.
17. The air-atomizing fuel burner system of claim 16 in which said means for regulating the flow of gaseous fuel to said air-atomizing nozzle means is a gaseous fuel pressure regulator.
18. The air-atomizing fuel burner system of claim 2 in which said means for controlling the type of fuel delivered to said air-atomizing nozzle means comprises a three-way valve.
19. The air-atomizing fuel burner system of claim 2 in which said air-atomizing nozzle means comprises an air aperture having an edge with a thickness approximately equal to or less than the hydraulic diameter of said air aperture.
20. The air-atomizing fuel burner system of claim 18 in which said hydraulic diameter is about 10 to 30 mils.
21. The air-atomizing fuel burner system of claim 1 and further comprising means for igniting the dispersed fuel in the presence of said secondary air to produce said combustion flame.
22. An air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary gas under pressure to disperse fuel, means for delivering fuel to said air-atomizing nozzle means, means for delivering primary gas under pressure to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to produce a combustion flame, and flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in the gaseous or hydroxyl-type combustion zone of said combustion flame.
23. The air-atomizing fuel burner system of claim 22 in which the ratio of flame spreader diameter to separation distance between said flame spreader and air-atomizing nozzle means is about 1.
24. The air-atomizing fuel burner system of claim 22 in which said flame spreader is between about 1.5 and 5 inches downstream from said air-atomizing nozzle.
25. A low pressure air-atomizing fuel burner system comprising air-atomizing nozzle means for using primary air to atomize fuel, means for delivering fuel under low pressure to said air-atomizing nozzle means, means for delivering primary air to said air-atomizing nozzle means to disperse said fuel so that the dispersed fuel can be ignited in the presence of secondary air to produce a combustion flame, and flame spreader means located downstream of said air-atomizing nozzle means for stabilizing and shaping said flame, said flame spreader means being located in The gaseous or hydroxyl-type combustion zone of said combustion flame.
26. The air-atomizing fuel burner system of claim 25 in which said primary air and said fuel are each delivered to said air-atomizing nozzle means at a pressure of about 1 to 15 psi.
27. The air atomizing fuel burner system of claim 25 in which said fuel is delivered to said air-atomizing nozzle means at a pressure of about 1 to 4 psi.
US441837A 1972-08-22 1974-02-12 Fuel burner for liquid and gaseous fuels Expired - Lifetime US3909188A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US441837A US3909188A (en) 1972-08-22 1974-02-12 Fuel burner for liquid and gaseous fuels
CA219,809A CA1019667A (en) 1974-02-12 1975-02-11 Fuel burner for liquid and gaseous fuels

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US00282694A US3847537A (en) 1972-08-22 1972-08-22 Air-atomizing fuel burner
US441837A US3909188A (en) 1972-08-22 1974-02-12 Fuel burner for liquid and gaseous fuels

Publications (1)

Publication Number Publication Date
US3909188A true US3909188A (en) 1975-09-30

Family

ID=26961623

Family Applications (1)

Application Number Title Priority Date Filing Date
US441837A Expired - Lifetime US3909188A (en) 1972-08-22 1974-02-12 Fuel burner for liquid and gaseous fuels

Country Status (1)

Country Link
US (1) US3909188A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4134719A (en) * 1976-09-27 1979-01-16 Velie Wallace W Multi-flame fuel burner for liquid and gaseous fuels
FR2493473A1 (en) * 1980-11-06 1982-05-07 Gianola Ste Financiere Prod Multiple fuel type boiler - has horizontal cylindrical chamber with burner in furnace door closed at front by stay-supported cover
US4606284A (en) * 1982-04-06 1986-08-19 Coal Industry (Patents) Limited Underfeed stokers
US4651711A (en) * 1985-08-14 1987-03-24 Scheu Manufacturing Company Forced air heater
WO1997045676A1 (en) * 1996-05-24 1997-12-04 International Thermal Investments Ltd. Multi-fuel burner with adjustable metering valve
US5927961A (en) * 1993-07-09 1999-07-27 International Thermal Investments Ltd. Multifuel burner with pressurized fuel-holding tank
US20040219466A1 (en) * 2003-05-02 2004-11-04 Marino John A. Aggregate dryer burner with compressed air oil atomizer
US20050053877A1 (en) * 2003-09-05 2005-03-10 Hauck Manufacturing Company Three stage low NOx burner and method
US20100269789A1 (en) * 2000-03-02 2010-10-28 New Power Concepts Llc Metering fuel pump
US20110143294A1 (en) * 2009-12-14 2011-06-16 David Deng Dual fuel heating source with nozzle
US10066838B2 (en) 2006-05-30 2018-09-04 David Deng Dual fuel heating system
US20200378597A1 (en) * 2016-06-03 2020-12-03 BSH Hausgeräte GmbH Gas burner and domestic cooking appliance

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1481764A (en) * 1922-06-22 1924-01-22 Frank M Weaver Gas burner
US2335085A (en) * 1941-03-18 1943-11-23 Colonnade Company Valve construction
US3212556A (en) * 1962-03-16 1965-10-19 Johansson Ernest Oil vaporizing device for oil burners

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1481764A (en) * 1922-06-22 1924-01-22 Frank M Weaver Gas burner
US2335085A (en) * 1941-03-18 1943-11-23 Colonnade Company Valve construction
US3212556A (en) * 1962-03-16 1965-10-19 Johansson Ernest Oil vaporizing device for oil burners

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4134719A (en) * 1976-09-27 1979-01-16 Velie Wallace W Multi-flame fuel burner for liquid and gaseous fuels
FR2493473A1 (en) * 1980-11-06 1982-05-07 Gianola Ste Financiere Prod Multiple fuel type boiler - has horizontal cylindrical chamber with burner in furnace door closed at front by stay-supported cover
US4606284A (en) * 1982-04-06 1986-08-19 Coal Industry (Patents) Limited Underfeed stokers
US4651711A (en) * 1985-08-14 1987-03-24 Scheu Manufacturing Company Forced air heater
US5927961A (en) * 1993-07-09 1999-07-27 International Thermal Investments Ltd. Multifuel burner with pressurized fuel-holding tank
WO1997045676A1 (en) * 1996-05-24 1997-12-04 International Thermal Investments Ltd. Multi-fuel burner with adjustable metering valve
US20100269789A1 (en) * 2000-03-02 2010-10-28 New Power Concepts Llc Metering fuel pump
US6969249B2 (en) 2003-05-02 2005-11-29 Hauck Manufacturing, Inc. Aggregate dryer burner with compressed air oil atomizer
US20040219466A1 (en) * 2003-05-02 2004-11-04 Marino John A. Aggregate dryer burner with compressed air oil atomizer
US20050053877A1 (en) * 2003-09-05 2005-03-10 Hauck Manufacturing Company Three stage low NOx burner and method
US7163392B2 (en) 2003-09-05 2007-01-16 Feese James J Three stage low NOx burner and method
US10066838B2 (en) 2006-05-30 2018-09-04 David Deng Dual fuel heating system
US20110143294A1 (en) * 2009-12-14 2011-06-16 David Deng Dual fuel heating source with nozzle
US9829195B2 (en) * 2009-12-14 2017-11-28 David Deng Dual fuel heating source with nozzle
US20200378597A1 (en) * 2016-06-03 2020-12-03 BSH Hausgeräte GmbH Gas burner and domestic cooking appliance
US11543122B2 (en) * 2016-06-03 2023-01-03 BSH Hausgeräte GmbH Gas burner and domestic cooking appliance

Similar Documents

Publication Publication Date Title
US3909188A (en) Fuel burner for liquid and gaseous fuels
EP0186376B1 (en) Ultrasonic injection nozzles
US4134719A (en) Multi-flame fuel burner for liquid and gaseous fuels
US3847537A (en) Air-atomizing fuel burner
US3736093A (en) Integral regulated hand torch
US2285689A (en) Atomizer
GB259044A (en) Improvements in burners for liquid fuel
US2940674A (en) Instant flame torch
US5743726A (en) Apparatus for the vaporization of fuels and supply of air for combustion
US2552658A (en) Nozzle for gas turbines
US5566887A (en) Multi-vent airblast atomizer and fuel injector
GB1448924A (en) Atomiser for liquids particularly for use in burning liquid fuels
JPS6097067A (en) Acting substance emitting apparatus
GB516724A (en) Improvements in or relating to liquid fuel burners or liquid atomisers
US1214880A (en) Gas-torch.
GB618688A (en) Improvements in or relating to fuel-supply systems for gas-turbines
US1645893A (en) Welding and cutting apparatus
US1192589A (en) Crude-oil burner.
JPH0518567Y2 (en)
JPS6026255Y2 (en) Pressure-driven variable flow rate burner
US2568880A (en) Oil burner nozzle
US1013822A (en) Heater.
JP3021874B2 (en) Combustion equipment
GB1355647A (en) Liquid-fuel injection system
US932947A (en) Combined lighting and heating system.