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Publication numberUS3363661 A
Publication typeGrant
Publication dateJan 16, 1968
Filing dateDec 7, 1965
Priority dateDec 7, 1965
Also published asDE1501833A1, DE6606067U
Publication numberUS 3363661 A, US 3363661A, US-A-3363661, US3363661 A, US3363661A
InventorsWilliam B Horton
Original AssigneeFletcher Co H E
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Apparatus for producing a flame jet by combusting counter flow reactants
US 3363661 A
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Description  (OCR text may contain errors)

Jan. i6, W6 Wv B. HORTON Em APPARATUS FOR PRDUCING A FLAME JET BY COMBUSTING COUNTER FLOW REACTANTS Filed Dec. 7] 1965 2 Sheets-5heet l H 4b n, /0 @1lb 39 I9 El /g I7 AIR Jan. 16, 1968 W. B. HORTON 3,363,66

APPARATUS FOR PRODUCING A FLAME JET BY COMBUSTING COUNTER FLOW REACTANTS Filed Dec, 7, 1965 2 Sheets-Sheet 2 IS e, Eva/9.5. W

TEMP.

L i ia' l AIR RATIO /FUEL United States Patent APPARATUS FOR PRODUCING A FLAME JET BY COMBUSTING COUNTER FLOW REACTANTS William B. Horton, Concord, Mass., assigner to H. E.

Fletcher Co., West Chelmsford, Mass., a corporation of Massachusetts Filed Dec. 7, 1965, Ser. No. 512,170 2 Claims. (Cl. 15S-27.4)

ABSTRACT OF THE DISCLQSURE A combustor comprising spaced concentric tubular bodies and having a space for premixing fuel, oxygen and a quantity of nitrogen at one end thereof and a central flame discharge nozzle at the other end thereof. A flame stabilizing wall separates the premixing space from the combustion chamber. Oxygen and nitrogen pass through the space between the tubular bodies and is led in a reversely turned path in the area of the discharge nozzle to provide a secondary flame initiating region.

This invention relates to methods and apparatus for Kburning quantities of fuel and oxidant at superatmospheric pressures in a confined space to provide a flame jet and, more particularly, the invention is concerned with a novel technique for bringing together desired quantities of fuel and air in a combustion chamber in a controlled manner so that a greatly extended range of fuel-to-air ratios may be burned stably within the combustion chamber at high through-put velocity.

It is a chief object of the invention therefore to improve methods of producing flame jets and to devise a method of combusting by which increased amounts of reactants can be combusted within a given chamber volume.

Another object of the invention is to provide a method of controlling the manner in which an oxidant is mixed with fuel so as to accomplish cooling of the flame within an extended range of stable burning. Another object of the invention is to devise improved burner structures for receiving and burning reactants.

In realizing the foregoing objectives, it is important to evaluate prior art techniques for producing flame jets. It is now customary in the art to employ a tubular burner structure into an inner end of which fuel and an oxidant such as air are introduced under pressure with the resulting mixture being instantly combusted. This produces a stream of products of combustion which is emitted from an outer end of the burner structure at very high velocity.

It has been found by those skilled in the art that for any given volume of burner chamber in which combustion thus takes place there is a definite limit as to the fuelto-air ratio which may be used, as well as the quantities of fuel and air which may ybe introduced into the burner and combusted while maintaining stable burning. Experience has shown that undesirable limitations are thereby imposed on the performance capabilities and the operating temperature ranges of such flame jets and this becomes especially important in connection with operations where the :llame jet is employed to produce spalling of mineral bodies of various types.

With these shortcomings of conventional flame jets in mind, I have conceived of a novel method of burning fuel and oxidant in a manner such that a relatively larger quantityl of fuel and oxidant may be combusted for any given chamber volume without appreciable loss of llame stability and with a desirable lowering of flame temperatures.

My improved method of burning is based on the novel concept of providing a primary flow of air which is mixed ICC with fuel and burned initially in a combustion chamber and further providing a secondary flow of air which is injected into an end of the burner chamber opposite to that in which combustion is initiated to thereby set up a counter fiow of air. This counter flow of air is caused to move in opposed relation to the flow of products of combustion to thereby set up a region of extreme turbulence at the exit end of the burner chamber. As a result of this turbulence a highly desirable secondary mixing of fuel with air is produced in very close proximity to the outlet nozzle through which the flame nozzle is emitted.

I find that by thus introducing a counter flow of air into the exit end of the burner an extended range of usable fuel-to-air ratios of a determinable nature may be realized and as a result significantly larger quantities of fuel may be utilized in a given burner volume. I also find that the flame so produced has the ability to run with excess air and this excess air provides for substantial cooling of the flame.

The nature of the invention and its other objects and novel features are more fully described Ibelow in connection with the description of the accompanying drawings in which:

FIGURE 1 is a cross sectional view of a preferred form of burner construction of the invention in which a counter fiow of oxidant may be employed;

FIGURE 2 is a fragmentary cross sectional view of a burner generally similar to the burner of FIG. 1 but illustrating a modified form of inlet means for producing a counter flow of oxidant;

FIGURE 3 is a cross section taken on the line 3--3 of FIGURE l;

FIGURE 4 is a cross section taken on the line 4-4 of FIGURE 1;

FIGURE 5 is another cross-sectional view generally corresponding to FIGURE l but further illustrating another modified arrangement for regulating flows of fuel and oxidant independently;

FIGURE 6 is a graph showing an air to fuel ratio plotted against temperature changes;

FIGURE 7 is a cross sectional view of a modified form of burner for secondary flow; and

FIGURE 8 is a cross section taken on the line 8-8 of FIGURE 7.

In carrying out the method of the invention in one preferred form, I produce a flame jet by combusting air and fuel in the same general manner disclosed in Patent No. 3,103,251. In Patent No. 3,103,251 issued to the assignee of the applicant in the present invention, there has been disclosed a method of flame working a mineral body in which cooling of a flame jet may be realized by employing air as an oxidant, and allowing inert gas in the air to reduce temperature of the flame. The range of fuelto-air ratios used is limited by the need for remaining within a region of stable 'burning to avoid faulty flame operation or flame extinction.

There has further -been disclosed in application Ser. No. 306,887 filed Sept. 5, 1963, entitled, Method and Apparatus for Producing Flame I et and Controlling Temperature and Flame Stability of Same, now issued under date of Iune i4, 1966 as Patent No. 3,255,802, also owned by the assignee of the present applicant, a method and means for inducing products of combustion to recirculate against a flame stabilizing surface and thereby produce a region of Iiame initiating which permits combustion reaction to take place over a somewhat extended range of fuel-to-air ratios without flame extinction.

In producing a jet flame in accordance with the present invention, I preferably employ a burner construction having a flame stabilizing surface of the class disclosed in application Ser. No. 306,887, and I also make use of the cooling action of quantities of inert gas as referred to in Patent No. 3,103,251.

However, in addition I provide for controlling flow of oxidant in a specific manner to create in a burner charnber a region of high turbulence at a point appreci-ably removed from the llame stabilizing surface and in this way there is created and maintained a secondary flame initiating region.

Considering in more detail the preferred form of burner structure for carrying out the method of the invention as illustrated in FIGURE l, arrow in general refers to a tubular body which is made up of an outer tubular section 12 and an inner tubular portion 13 occurring in spaced relation to the tubular portion 12. Fitted into adjacent ends of the tubular bodies 12 and 13 is a nozzle piece 14 which is .shouldered at 14a to receive an end of the t-ubular member 13 as shown with an extended end of the tubular body 12 being located around a shouldered part 14b of the nozzle piece 14.

At the opposite end of the tubular burner structure described, there is provided an injector head 11 against which the tubular section 12 is fitted as shown, and this injector head is formed with an inner annular part 11a having a shouldered .section 11b against which is received the tubular member 13. Mounted through the injector head 11 is an air conduit 15 which communicates with an annular manifold volume 16 occurring between the part 11 and the part 11a. Numeral 30 denotes a fuel conduit which extends centrally through the member 11 and communicates with an aperture or well 23 in turn leading into the interior of the tubular member 13. Air is supplied under pressure and led through the tubular member 15 into the manifold space 16. Fuel is supplied under pressure through the conduit 36 and passes through the surrounding injector part 31 into the well 23. The nozzle 14 may, if desired, be cooled by a flow of water indicated by arrows, conducted through the annular passage 39 shown at the left hand side of FIGURE 1.

In accordance with the invention the air supplied through the conduit 15 is separated into two independent flows. These flows of air may be referred to conveniently as a primary flow and a secondary flow. The primary flow of air as it enters the annular manifold space 16 passes through a series of openings 22 which communicate with the well 23 and thus allow the air to be discharged through the well into the burner chamber.

The secondary flow of air is caused to exit through a plurality of openings 17 from the manifold volume 16 and passes through an annular passageway 18 occurring between tubes 12 and 13 to exert a desirable cooling action with respect to combustor tube 13. This secondary flow of air continues into the end of the burner structure and is there diverted abruptly through a plurality of inlet openings 19 which are arranged around the tubular member 13 and which preferably are formed with an angle as shown in FIGURE 1 so that the air is caused to be substantially reversed in its path of flow and is caused to move in a direction from left to right as viewed in FIGURE 1.

In accordance with the invention the fuel and air leaving the Well 23 by some suitable `means is ignited and continuously burns to produce a stream of products of combustion, which stream moves at high velocity from right to left as viewed in FIGURE l. The flow of products of combustion containing portions of unburned fuel meets abruptly with the plurality of flows of secondary oxidant or air injected inwardly through the openings 19. As a result there is formed an exceedingly highly turbulent region which is generally indicated by arrows at the point noted by numeral 36. Since the .secondary air is being injected around the entire circumference of the burner tube 13, there is created an outer toroidal flow of oxidant which tends to become intimately mixed with the central flow of products of combustion carrying unburned fuel therein.

As a result of the meeting of the secondary flow of -air with the stream of products of combustion, there is realized a gradation of the fuel-to-air ratio from rich to lean at some point or region of which the ratio is stoichiometric. The effect of the turbulent region is to create a flame initiating region which tends to maintain more stable burning than would otherwise be the case. In effect this flame initiating region created by the turbulence of the secondary air in-put may be conveniently thought of as a secondary flame initiating region since there is a first or primary flame emitting region at the area closely adjacent to the well 23. The annular member 11a is formed with a special flame stabilizing surface 11d which tends to promote the formation of a toroidal path of ow of burning material 35 so that this burning material is thrown back upon itself to come into contact with fresh quantities of fuel and oxidant emitted through the well 23 as set forth in application Ser. No. 306,887.

Thus there are created two flame initiating regions separated from one another and cooperating to promote stable burning at both ends of the burner structure.

I have found that the provision of a counter flow of air at the region 36 allows large quantities of fuel and air to be combusted. For example in prior art burners having a chamber diameter and length shown, for example, by volume 20 in the drawings where these dimensions were 2 inches and 16 inches respectively, a maximum of 400 s.c.f.m. of air could be burned stably. The present burner of the invention, having the identical combustor dimensions, is capable of burning over 500 s.c.f.m. of air with fuel. In addition, the improved burner of the invention is found to provide much easier igniting and, more importantly, is stable over an appreciably wider range of fuel-to-air ratios. This latter feature is illustrated diagrammatically in FIGURE 6 in which S denotes the stoichiometric ratio and L1 represents the limits of stable burning of a conventional burner of the class described. In comparison L2 represents the limits of stable burning of the same burner provided with means for employing counter flow oxidant.

Where the fuel to air ratio provides for an appreciable excess of air being utilized, there is realized a highly significant cooling which extends the cooling effects obtainable by the technique of Patent No. 3,103,251. This cooling action is capable of rendering the flame jet which is released from the burner structure capable of producing thermal spalling action with a considerably larger number of minerals, and particularly minerals such as slate and other substances where relatively lower temperatures must be employed.

In thus employing a counter flow of oxidant such as air, I may also realize a desirable cooling effect for the nozzle portion of the burner. An arrangement of this type has been disclosed in FIGURE 2 for example. As shown therein the secondary air flow 42 passes through an annular passage 43 contained between tubes 40 and 41. Nozzle piece 44 contains the annular space 45 through which the secondary air flows before becoming discharged through reversely directed annular openings 46. It will be apparent that the secondary air in passing over the relatively large surface area presented by opening 4S and holes `46, provides a very substantial cooling effect to the nozzle piece 44. It will also be observed that in the arrangement of FIGURE 2 the reversely directed openings 46 afford a modified and desirable means of injecting a counter ilow along paths which are in axially opposed relationship to a lflow of stream of products of combustion as indicated by the arrow 49 and thus there may be created an even more turbulent region as represented by the reference character 47.

Summarizing therefore the novel steps of the invention are, in essence, the operations of directing opposed flows of oxidant from two extremities of an enclosed combustion chamber volume. One flow which may be thought of as the primary flow contains fuel. The secondary air flow is provided to assist in burning the fuel which is carried in the stream of products of combustion and to maintain high combustion stability, All of the air so supplied can be consumed in the combustion reaction.

Furthermore, this secondary flow of air is heated, having acted as a coolant for the combustor tube 13 as it traveled through the passage 18. This contained heat adds further to t-he flame stabilizing effect of the turbulent region created by this in-put of secondary air.

I may desire to modify the structure described in various ways as, for example, in FIGURE 5 I have shown a burner construction similar in all respects to that shown in FIGURE 1 with the exception that the flow of air which is to constitute the primary air may be independently supplied through a valve member V, while the secondary flow of air to constitute the counter flow of the invention may be independently supplied through a valve V1. There may be thus realized desirable controls in the ame stability realized for any given quantity of fuel and air to be combusted and likewise there may be realized a variable control of the temperature of the jet emerging from the burner structure in line with the description above with reference to FIGURE 2.

Various other changes and modifications may be resorted to within the scope of the appended claims.

I claim: 1. A burner apparatus for burning liquid fuel, oxygen and a quantity of nitrogen at superatmospheric pressure and producing a nitrogen cooled flame jet, said apparatus including an enclosure body having a discharge nozzle formed with a central flame exit aperture, the opposite end of said enclosure body having an annular mixing space for premixing oxygen, nitrogen and liquid fuel droplets, said enclosure body further having a relatively larger combustion chamber communicating with the premixing space, a cylindrical sleeve located around the annular mixing space and the combustion chamber in spaced relation to form an annular passageway which at its intermediate portion is isolated from the interior of the combustion chamber, a flame stabilizing Wall constructed and arranged to separate the premixing space and the combustion chamber, said flame stabilizing wall being formed with a fuel injecting passageway for conducting a fuel mixture from the premixing space into the combustion chamber, said flame stabilizing wall further presenting a at annular flame stabilizing surface which is located around and which extends abruptly away from said fuel injection passageway, said combustion chamber having a predetermined size which defines a volume limited by the quantity of nitrogen relative to the quantity of oxygen and fuel droplets combusted therein whereby a range of stable burning above and below stoichiometric range is realized and recirculation of flame portions may be induced against the said flame stabilizing surface in a toroidal path of ow to provide a primary ame initiating region and said enclosure body occurring around the annular mixing space having further formed at outer portions thereof passageways for conducting nitrogen and oxygen independently of liquid fuel into and along the said annular passageway between the combustion chamber and the said cylindrical sleeve, said discharge nozzle being formed with a tubular Section received in the end of the said combustion chamber and having axially disposed openings located therethrough, the outer end of said nozzle including an enlarged annular flange portion mounted within the end of the cylindrical sleeve and deiining a space through which nitrogen and oxygen passing from the annular passageway may be led in a reversely turned path of flow and discharged into products of combustion approaching the discharge nozzle to provide a secondary ame initiating region at points appreciably spaced away from the said primary ame initiating region.

2. A structure according to claim 1 in which the said combustion chamber is formed with air passageways located at the extreme end of the combustion chamber in close proximity to the space through which nitrogen and oxygen is lead in a reversely turned path of ilow into the stream of products of combustion in the combustion chamber, said air passageways at the end of the combustion chamber being arranged to direct jets of downstream air into the reversely turned path of flow of air passing through the nozzle in a manner to cooperate therewith and to increase high turbulence and promote secondary flame initiating at points separated from the said primary llame initiating region.

References Cited UNITED STATES PATENTS 2,515,845 7/1950 Van Den Bussche 158-116 2,725,929 12/1955 Massier l58-734 2,734,560 2/1956 Harris et al. 158-4 3,179,150 4/1965 Arnold 15S-l 3,224,486 12/1965 Geller 158-4 FOREIGN PATENTS 181,228 10'/ 1962 Sweden.

FREDERICK L. MATTESON, JR., Primary Examiner. E. G. FAVORS, Assistant Examiner.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2515845 *May 13, 1947Jul 18, 1950Shell DevFlame pocket fluid fuel burner
US2725929 *Nov 24, 1951Dec 6, 1955Selas Corp Of AmericaCombustion chamber type burner
US2734560 *Oct 9, 1951Feb 14, 1956 Burner and combustion system
US3179150 *Apr 30, 1962Apr 20, 1965Arnold Gerald DFurnace
US3224486 *Dec 7, 1964Dec 21, 1965Lorant B GellerMethod and apparatus for producing air-fuel flames of sonic and supersonic velocities
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US4257760 *Jan 4, 1979Mar 24, 1981Schuurman Hubert GCyclone burners
US4384434 *Sep 29, 1981May 24, 1983Browning Engineering CorporationHigh velocity flame jet internal burner for blast cleaning and abrasive cutting
US4559008 *Jan 5, 1984Dec 17, 1985Deutsche Forschungs- Und Versuchsanstalt Fur Luft-Und Raumfahrt E.V.Starting aid device for a high pressure combustion chamber
US6874452Jan 14, 2003Apr 5, 2005Joseph S. AdamsResonant combustion chamber and recycler for linear motors
US6997145Feb 15, 2005Feb 14, 2006Adams Joseph SRecycler for linear motor
EP0007424A1 *Jun 15, 1979Feb 6, 1980Smit Ovens Nijmegen B.V.Burner device for combustion of liquid fuel
EP0094068A2 *May 7, 1983Nov 16, 1983Joh. Vaillant GmbH u. Co.Fan-type burner
EP0421049A1 *Apr 24, 1990Apr 10, 1991Ente Nazionale Per L'energia Elettrica - (Enel)Improvements in a fuel burner for a boiler
Classifications
U.S. Classification431/158, 431/238
International ClassificationF23C7/02, F23D11/00, F23C6/04, F23C3/00
Cooperative ClassificationF23C7/02, F23D11/00, F23C3/00, F23C6/045
European ClassificationF23D11/00, F23C6/04B, F23C7/02, F23C3/00