US2088879A - Furnace for burning granular fuel and the like - Google Patents

Furnace for burning granular fuel and the like Download PDF

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US2088879A
US2088879A US679203A US67920333A US2088879A US 2088879 A US2088879 A US 2088879A US 679203 A US679203 A US 679203A US 67920333 A US67920333 A US 67920333A US 2088879 A US2088879 A US 2088879A
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furnace
fuel
walls
combustion chamber
air
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US679203A
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Stouff Louis Marie Joseph
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C99/00Subject-matter not provided for in other groups of this subclass
    • F23C99/005Suspension-type burning, i.e. fuel particles carried along with a gas flow while burning

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

Aug. 3, 1937. M. J. STOUFF FURNACE FOR BURNING GRANULAR FUEL AND THE LIKE Filed July 6, 1953 I P e na '3, 193 7 p fiumreo .s'rarss r e I [2,088,879 FURNACE sofa BURNING GRANULAR FUEL ,A T EIJ Louis'Marie Joseph Sto'ufi, Lyon, France Application July 6, 1933, seris1 No. In France July7, 1932 This invention relates to a furnace for; burning granular fuel and more particularly to a I furnace of the kind in which the granular fuel is delivered to the upper end of the combustion chamber and falls through the combustion chamberagainst an upwardly directed airstream by which the fuel particles are held in suspension during combustion, the ash being'continuously removed from the bottom of the furnace.
The object of the present invention is to provide anew or improved furnace of thetype just referred to which will be efficient and stable in operation.
There already exist processes where combustion of the fuel takes place in a current of air.
pulverized fuel which is usually burnt upon a grate. On the other hand the present invention does not necessitate pulverization and permits of using granular fuel of all grain sizes from mm. to 30 mm. for example. There is no longer a grate or carrying surface, but merely the lateral walls of the chamberjandthe fuel where the chamber walls guide the ascending air grains are constantly in gaseous suspension;
In the previous processes-the fuel had only a limited stay in the chamber and had to be burnt during this period contrary to the present invensuspension in the chamber and where it remains indefinitely if itis not burnt.
Inthe known processes the flame does not fill the furnace, contrary to the present invention current and where the grains in aerodynamic suspension are distributed homogeneously in the whole.
Infurnaces of the general character above referred to it has been proposed to rnake thefurnace combustion chamber of conical or similar form with a View to regulating the air stream in l the furnace chamber in such manner as toenable fuel particlesto remain in suspension in the furnace for a sufficient period to permit combustion, For example, it has been proposedto design the furnace in such a way that the velocity of the air remains substantially the same at all heights of the combustion chamber.
In accordance'with the present invention a furnace of the kind referred to is arranged so that the fuel particles are held in suspension in the furnace in a stable and permanent manner during the course of combustion by an upwardly directed gas stream whose velocity is substantially uniform at all points in any one horizontal section of the furnace and decreases progressively furnace, so that the whole of'the furnace space is filled with fuel particles. This result is brought *5 about "by constructing the furnace in the form'of fa'truncatedcone having an angle of no mo-re'than about 25-:and of such length that the crosssectional area at the upper'end of the furnace'isnot less than l5'times the cross sectional area of the" lower end of the furnace andpreferably from 50to 100 times. Owing tothis arrangement very important technical advantages will beobtained,
among which the 'main advantages are the fol- I lowing; the combustion will be homogenous, that These processes, however, necessitate the use of in a horizontal plane, taken at any desired level of'the furnace, thedensity of the fuel and its percentage of carbonic gas and oxygen will be constant at all points; any desired fuel, even in relatively thick particles,may beburned, wherebys .also be used "without objection; moreover the V combustion will fill up the entire furnace,rwherefi a maximumof heat will be produced per cubic :l'meter oft'he furnace space to be heated.
. tion in which the fuel is permanently in a gaseous 'Airmay'be in part blown into the furnace at If necessary a portion of the combustiontj 'The air entry orifices are symmetrically disturbulence.
In order to facilitate the comprehension of my invention, I have illustrated the latter by way of example in the accompanying drawing, wherein:
Fig. 1 is adiagrammatical section of a furnace according to my invention.
Fig. 2 is a vertical axial section of the lower part of one form of furnace.
Fig. 3 is a horizontal section on line 3-3 of Fig. 2.
Referring to Fig. 1 the combustion chamber b is made of the shape of a vertical truncated cone, the apex of which is turned downwardly. The angle formed between the walls, that is, the angle of the cone is 24, the ratio between the bases of the truncated cone being equal to 16. Through said combustion chamber I cause a current of air to pass upwardly in the direction of the ar- 55 rows 0, whilst the fuel is charged at f into the chamber.
Owing to the dimensions adopted, the walls fit the diverging form of the current of air and the fuel remains in stable suspension until it will be completely burned. The velocity of air at the lower part is sufficient for preventing the heaviest grains of fuel from being lowered until the combustion thereof will be complete. The velocity of the gases at the upper part is sufficiently low to prevent the unburned smallest particles of fuel from being carried away by said gases, the supporting power of which is too weak for compensating the weight of such particles.
Generally it will be observed that each grain of fuel accomplishes a rapid irregular oscillating movement around a medium level and substantially in a vertical direction. Owing to such oscillation an intense renewal of air will be produced at the surface of the grain, whereby the combustion thereof will be highly enhanced.
A very rapid oscillating movement being imparted to the grains a, the latter will bombard the walls b. If openings are provided at suitable points of said walls, for instance at the top and bottom, a certain amount of slag or dross will be discharged through said openings. The two ends 11 and e of the furnace, through which air is admitted and gas discharged respectively, may entirely or in part fulfill the function of the openings mentioned.
The furnace shown in Figs. 2 and 3 has its lower part provided with fireproof walls I, forming a truncated cone. Arranged centrally in the lower open end of said truncated cone is a pipe 4, through which compressed air is supplied into the furnace in the direction of the arrow 3. As this arrangement is operated like an injector, an induced current of air will pass through the free annular space 5 between the pipe 4 and the walls I of the furnace.
Slag or dross will drop freely through said annular space, wherein it will meet with an upward current of air and be cooled by the latter.
Loosely arranged on the pipe 4 is a sleeve 6, on which a vertical rod 1 is mounted. A scraper or poker 8 is secured to the end of said rod 1 by means of a horizontal pivotal connection 9. Through the agency of gear-wheels I and H rotary movement around the axis of the furnace will be imparted to the scraper 8 to bring the latter into frictional engagement with the lower -wall and remove slag or dross therefrom, which will drop through the above mentioned annular space. However if certain portions thereof adhere too strongly to the walls, the scraper 8 will posite direction, that is upwardly. By adjusting the plug l2 upwardly or downwardly, the dimensions of the air supply opening will be modified without preventing slag or dross from dropping freely through the same.
A jet of compressed air is directed through the pipe I3 into the furnace. The pipe I3 is arranged substantially tangentially to a horizontal circumference, the centre of which is situated on the axis of the furnace, whereby the jet of compressed air will be caused to detach slag or dross from the walls by its whirling movement.
Provided in the walls I of the furnace are other air'supply openings [4, I5, I6. Upon closing said openings more or less, the temperature at the base of the furnace will be varied as required. A further air supply is provided at ll, formed of a horizontal slot extending around the wall of the furnace.
I claim:
1. In a granular fuel burning furnace, the combination with a combustion chamber constructed in the form of a vertical truncated cone having an angle of not more than 25 and of such length that the cross sectional area at the upper end of the furnace is not less than about times the cross sectional area of the lower end of the furnace and means for introducing the granular fuel downwardly through the combustion chamber, of a compressed air supply pipe in the open lower end of the combustion chamber, means on said pipe coacting with the furnace wall to form an annular opening around the pipe, through which a flow of secondary air is induced, a scraper mounted to rotate about the compressed air supply pipe to act on the walls of the combustion chamber near the base thereof, and means for supporting said scraper in such a way that it is capable of yielding in a direction away from the wall of the combustion chamber when encountering an obstruction, as described.
2. In a granular fuel burning furnace, the combination with a combustion chamber constructed in the form of a vertical truncated cone having an angle of not more than and of such length that the cross sectional area at the upper end of the furnace is not less than about 15 times the cross sectional area of the lower end of the furnace and means for introducing the granular fuel downwardly through the combustion chamber, of a compressed air supply pipe in the open lower end of the combustion chamber, means on said pipe coacting with the furnace wall to form an annular opening around the pipe, through which a flow of secondary air is induced, means mounted to rotate on said compressed air supply pipe for scraping the walls of the combustion chamber near the base thereof, and a second compressed air supply pipe in the base of the combustion chamber to produce a jet substantially tangential to the furnace walls, as described.
LOUIS MARIE JOSEPH STOUFF.
US679203A 1932-07-07 1933-07-06 Furnace for burning granular fuel and the like Expired - Lifetime US2088879A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2509866A (en) * 1944-09-26 1950-05-30 Standard Oil Dev Co Low-temperature combustion and apparatus therefor
US2614513A (en) * 1950-03-28 1952-10-21 Hofft Company Inc Method of and vortex-type furnace for burning waste fuel
US2741549A (en) * 1952-11-01 1956-04-10 Exxon Research Engineering Co Conversion of carbonaceous solids into volatile products
US2881719A (en) * 1949-07-08 1959-04-14 Babcock & Wilcox Co Cyclone furnace
US3522016A (en) * 1963-12-12 1970-07-28 British Titan Products Scraper apparatus for reaction chamber
US4011822A (en) * 1975-08-11 1977-03-15 Occidental Petroleum Corporation Burner for decarbonizing organic char

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2509866A (en) * 1944-09-26 1950-05-30 Standard Oil Dev Co Low-temperature combustion and apparatus therefor
US2881719A (en) * 1949-07-08 1959-04-14 Babcock & Wilcox Co Cyclone furnace
US2614513A (en) * 1950-03-28 1952-10-21 Hofft Company Inc Method of and vortex-type furnace for burning waste fuel
US2741549A (en) * 1952-11-01 1956-04-10 Exxon Research Engineering Co Conversion of carbonaceous solids into volatile products
US3522016A (en) * 1963-12-12 1970-07-28 British Titan Products Scraper apparatus for reaction chamber
US4011822A (en) * 1975-08-11 1977-03-15 Occidental Petroleum Corporation Burner for decarbonizing organic char

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