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Publication numberUS1381095 A
Publication typeGrant
Publication dateJun 7, 1921
Filing dateMar 27, 1920
Priority dateMar 27, 1920
Publication numberUS 1381095 A, US 1381095A, US-A-1381095, US1381095 A, US1381095A
InventorsFletcher C Starr
Original AssigneeFletcher C Starr
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Fuel-oil burner
US 1381095 A
Abstract  available in
Previous page
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Claims  available in
Description  (OCR text may contain errors)

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Specication of Letters Patent.

Patented J une 7,1921.

App1cation filed March 27, 1920. Serial No. 369,321.

To [IZZ whom t may conce-rn.'

Be it known that I, FLETCHER C. STARR, a citizen of the United States, residing at Philadelphia, in the county of Philadelphia and State of Pennsylvania, have invented certain new and useful Improvements in Fuel-Oil Burners, of which the following is a specification.

This invention relates to oil atomiziiig burners which eject the oil in the form of an extremely fine mist or spray, and particularly to the type in which the atomization is effected mechanically by introducing the jets or streams of oil tangentially into a nebulizing chamber, thereby setting up a rapid rotation or whirling motion which disrupts the oil and produces a more or less complete atomization.

Inasmuch as mechanical atomization ldepends directly upon the velocity of rotation, oil burners of this type have heretofore been operated under a high oil pressure. (lne of the objects of my invention is to obtain a high velocity of rotation in the nebulizing chamber with a low oil pressure. I obtain this result by causing streams of air, introduced tangentially into the mixing or nebulizing chamber, to impinge upon the oil and speed up its rotation. The air not only causes an increased velocity of rotation but mixes with the oil particles to form a vapor or as.

further object is to greatly augment the flexibility of operation of the burner and eX- tend its range of control. Thus the burner may be operated at a very low oil pressure and by increasing the tangential air supply a good mixture may be obtained at the extreme low limit of capacity. Then by increasing the oil pressure or by opening the oil control valve wider, the capacity of the burner may be increased while maintaining the proper mixture by introducing a stream of air transverse to the rotating streams and in the rear thereof. I am thus enabled to obtain a wide range of ope-ration and great exibility and at the same time increasing the efficiency over prior burners.

In the following detailed description I shall refer to the accompanying drawings. in which-Figure l is a longitudinal sectional view of a burner embodying my invention, and showing also its relation to the burner opening in the furnace wall; Fig. 2 is a transverse sectional view on the line 2 2 of Fig. l; Fig. 3 is a perspective view, partly and oil supply pipes which are provided witlP regulating valves, the burner being in section: Fig. S is a sectional view on the line 8-8 of Fig. T; and Fig. 9 is an enlarged front elevation of the tip or nozzle of the burner shown in Fig. 7.

T he burner nozzle may be in the form of a metal block 3 which is supported at the mouth of the fuel inlet of the furnace 4c by a yoke frame 5. The'nozzle is provided with an elongated mixing chamber 7, and adjacent its rear end are introduced alternate pairs of oil and air inlet ducts or channels 8, 8 and 9, 9 respectively, tangential with respectto the bore of the nozzle. Inlet oil and air supply pipes 8a and 9a are threaded into the block.

The oil entering the chamber 7 tangentially at opposite points sets up a whirling motion which is greatly augmented by the air streams'which also enter the chamber tangeiitially at diametiically opposite points intermediate the oil inlets. By this arrangement the oil may be iindei a comparatively low pressure and by placing the air under a very much higher pressure the entering air streams impinge upon the oil and supply the energy necessary to cause the oil to whirl with a high velocity, thereby nebulizing the oil a-nd forming an intimate mixture of air and minute oil particles.

It has heretofore been proposed to introduce an auxiliary fluid, such as air or steam, into the atomizing or whirling chamber but it. was specified that the pressure of the auxiliary fluid should not exceed that of the oil and it was introduced at such points or in such manner that it could not impinge directly upon the entering oil jets. My method, on the contrary introduces the air under a much higher pressure than the oil and directly impinges upon the cil jets or film. By causing the jets or streams of air entering under high velocity to directly iinpinge upon the tangentially entering jets of oil, as indicated in Fig. 2, I secure a mechanical disrupting action of the high vev'locity air streams upon the oil jets, at the same time supplying the energy required to produce the velocity of rotation upon which the atoinization depends and furthermore secure amore intimate and thorough mixture of the air and oil.

By causing the' air to initially impinge upon the oil jets as they enter the whirling chamber, and by its disrupting action causing an intimate mixture of oil and air particles, I am enabled to secure a more effective and persistent whirling or rotary motion of the mass because a column of mixed oil and air will maintain a rotary motion whereas a column of air alone will not do so.

As the whirling atomized mixture strikes the converging walls of the whirling or atomizing chamber adjacent the nozzle, the velocity is increased. To further increase the velocity, I introduce another force acting in a longitudinal direction along the axis of the burner by means of a pipe 15 entering the rear end of the atoinizing chamber through which steam or air under pressure is introduced. This not only exerts a pressure to force the already mixed air and 'atomized oil through the nozzle but supplies additional air for combustion. Furthermore this additional air supply lends great flexibility and range to the burner. Thus the burner can be operated efficiently at the extreme low limit of capacity at a very low oil pressure while obtaining a good mixture by opening the supply of air to the tangential air inlet pipes. Then by increasing the oil pressure or by opening wider the oil control valve, the capacity of the burner may be `increased and the proper amount of air supplied by openingthe valve controlling the air supplied to the rear pipe 15 to the desired extent. It is evident, therefore, that a very wide range of flexibility of operation is afforded by the coperative use of the axial and tangential streams of air and that under all conditions of operation, the efliciencyof the burner is enhanced by such co* operative action.

In Figs. 4 to 6 I have shown a modification which differs from the construction previously described in having a plug 17 located in a recess in the rear end of the burner and having a central bore with which the rear axially disposed air pipe 15 is connected. The oil inlet ports enter an annular recess 18 in the plug from which channels 19, cut in the conical forward end of the plug, lead tangentially into the atomizing chamber 7.

A further modication is illustrated in Figs. 7 to 9. In this form the plug 17 extends forwardly beyond the air inlet ducts and is provided with annular grooves 18 and 20, connected respectively with the oil `and air supply pipes. The oil groove 18 communicates with the bore 7-of the burner by means of ducts 19 which enter midway between the air ducts 9". The operation will be understood from the previous description in connection with the other iigures. As 1t is sometimes desirable to renew the burner tip or nozzle, this may be in the form of a separable plug 23, threaded into the end of the burner, and provided with a projecting hexagonal portion b v which it may be screwed, or unscrewed. I prefer to make the barrel of the burner in two parts 3 3 and which are threaded into an outer casing as shown in Fig. 7. Instead of inakiiig the tip 23 as a separate member, it may be made integral with the front barrel portion 3.

I have described in detail the particular i atomizing medium will impinge upon thel fuel streams to form a whirling mass, and injecting a stream of atomizing medium axially into said whirling mass to complete the atomization of the fuel and to force the resulting mixture outwardly from said confined space.

2. An oil atomizing burner, comprising a body or casing having an axially disposed a-tomizing and mixing chamber, alternately arranged tangential oil .and air inlet ports entering said chamber and so disposed that the air jets will impinge directly upon the entering oil and an axially disposed inlet in the rear of said ports through which a stream of air or steam may be injected to exert an impelling pressure upon the rotating mixture of air and oil issuing from said ports.

3. An oil atomizing burner, comprising a body or casing having an axially disposed atomizing and mixing chamber converging at its forward end into a nozzle opening, means for injecting alternately arranged the chamber, and means for injecting a stream of air'or steam into the rear end of said chamber and in an axial direction.

f1. An atomizing burner comprising a body or casing having a mixing chamber, tangential oil and air inlet ports entering said chamber and so disposed that an air jet will impinge directly upon the entering oil, and an inlet arranged in rear of said ports and through which an atomizing medium may be injected to exert an impelling pressure upon the rotating mixture of air and oil issuing from said ports.

5, An oil atomizing burner comprising jets of oil and air tangential tothe wall ofy n body or casing having an axially disposed atomizing und mixing chamber having at its forward endv a nozzle opening, means for injecting jets of oil and an atomizing medium tangential to the Wall of the chamber, and means for injecting a Stream of atomizing medium into the rear portion of said chamber and toward said nozzle opening.

6. The method of atomizing a hydrocarbon fuel, which consists in directing a 10 stream of fuel and atomizing medium tangentiully into a. confined space to form a whirling mass,v :1nd directing a stream of utomizing medium axially into Said whirling mass to force the mixture outwardly 15

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2566040 *Sep 26, 1947Aug 28, 1951New York Central Railroad CompFuel burning method and burner
US2905234 *Feb 17, 1956Sep 22, 1959Dortmund Hoerder Huttenunion AApparatus for the combustion of liquid fuels
US2999647 *Mar 3, 1958Sep 12, 1961Benjamin SosnickMist and spray production method and nozzle designs for its usage
US3139895 *Nov 29, 1961Jul 7, 1964IbmPneumatic switch
US3174497 *Sep 4, 1962Mar 23, 1965Sperry Rand CorpFluid power amplifier not-gate
US3192938 *Sep 5, 1961Jul 6, 1965Sperry Rand CorpFluid multi-stable device
US3198214 *Oct 30, 1963Aug 3, 1965R I V Anstalt Zur Verwaltung VFluid regulator
US3208462 *Sep 14, 1962Sep 28, 1965Sperry Rand CorpFluid control apparatus
US3208463 *Apr 4, 1963Sep 28, 1965Hyman HurvitzPure fluid amplifiers
US3256899 *Nov 26, 1962Jun 21, 1966Bowles Eng CorpRotational-to-linear flow converter
US3267946 *Apr 12, 1963Aug 23, 1966Moore Products CoFlow control apparatus
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US5337926 *Jul 22, 1993Aug 16, 1994The Procter & Gamble CompanySpray pump package employing multiple orifices for dispensing liquid in different spray patterns with automatically adjusted optimized pump stroke for each pattern
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US5458136 *Mar 31, 1994Oct 17, 1995Paul Ritzau Pari-Werk GmbhAssembly for producing aerosol pulses
US6491236 *Dec 10, 1998Dec 10, 2002AlstomMethod and device for injecting a fuel/liquid mixture into the combustion chamber of a burner
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US8669016Oct 2, 2009Mar 11, 2014Hamilton Sundstrand CorporationSwirl chamber for a fuel cell cooling manifold
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U.S. Classification239/400, 239/468, 239/428, 239/404
International ClassificationF23D11/10
Cooperative ClassificationF23D11/10
European ClassificationF23D11/10