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Publication numberUS2654592 A
Publication typeGrant
Publication dateOct 6, 1953
Filing dateOct 25, 1950
Priority dateOct 25, 1950
Publication numberUS 2654592 A, US 2654592A, US-A-2654592, US2654592 A, US2654592A
InventorsHarris Lawrence M
Original AssigneeFoamrock Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Furnace
US 2654592 A
Abstract  available in
Images(1)
Previous page
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Claims  available in
Description  (OCR text may contain errors)

L. M. HARRIS Oct. 6, 1953 FURNACE Filed OCT.. 25, 1950 ESN 2,55: zm.

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ATTORNEYS Patented Oct. 6, 1953 UNITED STATES TENT OFFICE FURNACE Lawrence M. Harris, Stafford, Tex., assigner of one-half to Foamrock Corporation, Stafford, Tex., a corporation of Texas Application October 25, 1950, Serial No. 192,066

3 Claims.

This invention relates to new and useful improvements in furnaces.

In the treatment of clay aggregate and similar materials the use of high temperature furnaces or kilns is quite common and the usual rotary kiln is constructed of a rotating heating chamber having a burner or burners at one end thereof. The invention herein will be described as applied to the ordinary rotary kiln. In such kiln, the material to be treated is ordinarily introduced into the chamber from that end which is remote from the burners so that the material traverses the chamber longitudinally thereof. Since the chamber is relatively long over an extended length the gases of combustion from the burner flame are depended upon to preheat the material prior to its entry or contact with the intense heating zone created by the burners; because the intense heating zone extends for only a relatively short space with respect to the over-all length of the burner chamber, the material being treated is not subjected to the intense heating zone for any great length of time with the result that the capacity of the burner is limited and the length of the intense heating zone is also limited; further, since the burner or burners are immediately adjacent one end of the kiln chamber a control of the oxygen Within the flame area is somewhat diflicult.

It is one object of the present invention to provide an improved furnace or kiln for treating clay aggregate or similar material having means for increasing the intense heating zone within. the treating chamber, whereby more efficient treatment with greater capacity and less fuel consumption per unit of material being treated may be obtained.

Another object of the invention is to provide a second elongate burner, in addition to the usual burner or burners heretofore provided within the heating chamber, which elongate burner projects beyond the intense heating zone created by the usual burner or burners to provide a second heating Zone which increases the heating area to thereby subject the material being treated to intense heat for an extended period of time, whereby the efficiency of the treatment is enhanced.

A still further object is to provide a double burner in a furnace or kiln with the inner extended burner being so located that the outer or normal burner or burners consume the major portion of the oxygen which is admitted to the combustion chamber to thereby allow the burnu ing which takes place in the second burner to 2 occur in an area of reducing atmosphere which results in more efficient treatment of the material.

A particular object is to provide an elongate or extended burner within the usual furnace or kiln which is constructed of a heat resistant alloy material and which is formed with cooling fins within its bore whereby the air required for burning and directed through the burner will function to maintain said burner cool to prevent damage thereto by the intense heating zone of the normal burner of the furnace or kiln and through which Zone said elongate burner extends.

The construction designed to carry out the invention will be hereinafter described, together with other features thereof.

The invention will be more readily understood from a reading of the following specification and by reference to the accompanying drawings forming a part thereof, wherein an example of the invention is shown and wherein:

Figure 1 is a view partly in section and partly in elevation of a kiln, constructed in accordance with the invention,

Figure 2 is a partial plan view of the kiln illustrating the disposition of the burners,

Figure 3 is a transverse sectional view, taken on the line 3-3 of Figure 2, and

Figure 4 is an enlarged cross-sectional view of the elongate burner.

In the drawings the numeral I0 designates an ordinary rotary kiln comprising a generally cylindrical housing or casing Il .having its interior suitably lined with fire brick I2 or similar ire resistant material. The casing or housing is disposed on an incline in a horizontal plane and is mounted upon suitable rollers I3 whereby said casing or housing is rotatable. The material to be treated is introduced into the casing at one end thereof through an inlet I4 and said material travels downwardly and longitudinally of the chamber A formed within the interior of the housing, the material escaping from the opposite end of the housing through an outlet I 5. The housing l I is constantly rotated and because it is disposed at an incline, it is apparent that the material will be moved longitudinally of the chamber A; because of the rotation the material will tend to be disposed higher on one side of the chamber as indicated by the dotted line I6 in Figure 3.

At the outlet end of the kiln a suitable Wall structure Il is formed and a series of burners B extend through this wall and into the end of the chamber A. Each burner Bis illustrated as comprising an outer tubular conduit I 8 having a gas or fuel pipe I9 disposed concentrically therein. A gas or fuel supply line 22 has connection with the pipe I9 and a hand valve 23 controls the flow of fuel into said pipe. Although this type of burner has been found satisfactory, it is pointed out that the burner B may be of any well known type now in general use.

The burners B are illustrated as three in number and are normally employed in kilns of this character so that the provision of the burners B in themselves form no particular part of the present invention. Because the material being treated tends to ride upwardly on the wall of the chamber A as indicated by the dotted line I6 (Figure 3), the burners B are disposed at an angle in a hori-VY zontal plane with respect to the axis of the chamber A, whereby the flame from each burner is directed against the material. When the burners B are operating each will form a flame indicated by F in Figure 1 which extends inwardly into the chamber A to form an intense heating zone. The gases of combustion now through the chamber A in a direction toward the material inlet and escape through a suitable stack or chimney 24 provided for this purpose.

Because the chamber A is relatively long the provision of the first series of burners B forms the 'intense heating Zone only adjacent to the outlet end of the chamber and therefore, the material being treated must travel through a relatively long path from the inlet 1,4 to the intense heating zone or ame F, during which path it is subjected only to the heat from the gases of combustion. In carrying out the present invention, a second elongate burner C is provided. This burner extends through the wall I1 and into the chamber A well beyond the end of the first series of burners' B. It is preferable that the end of burner C be disposed near the end of the flame F or of the intense heating zone created by the first burners. The elongate burner C' includes an outer conduit 25 which has connection with an air inlet pipe 25 to which a suitable blower 21 may be connected. The bore of conduit 25 is preferably formed with a plurality of the inwardly directed fin elements 28 which are disposed longitudinally of the conduit and which preferably extend throughout the entire length thereof. A gas or fuel pipe 29 exe tends axially within the conduit 25Y and communicates with the fuel supply-line 22. A suitable valve 30 in the pipe 29 controls the supply of fuel to the burner C.

Because the end of the burner' C is some distance inwardly of the ends of the burnersv B and is preferably adjacent the outer end ofthe flame' F from the burners B, it will be apparent that the flame G formed by the' second burner will project well in advance ofthe flame F; This name G thereby forms a second intense heating zone which actually is a continuation of the' first intense heating zone. The material traveling through the chamber A is therefore subjected to intense heat over an extended area and for an extended period of time whereby the efficiency of the treatment is increased. A

The burner C projects through the intense heating Zone created by the flame F and as has been noted is constructed of a heat resistant alloy so that the conduit 25 is not affected by this intense heat. To further protect the conduit 25 from damage by the heat, thel internal finsY are in contact with the incoming fresh air and thus it might be said. that the conduit isv air-cooled which assists in preventing damage thereto by excessive heat. By locating the second burner outlet at a distance spaced inwardly from the first burner, the flame F from each burner B is disposed between the flame G and the outlet end of the kiln which is open to atmosphere. The names F thereby consume or burn the major portion of the oxygen so thatthe burning effected by the burner C will take place in a condition of reducing atmosphere which increases the eciency of the treatment. In actual practice over an extended period of time, it has been found that the arrangement shown and described herein has reduced fuel consumption approximately twentyfive (25%) per cent. This is due to the fact that because the over-all capacity of the kiln is increased, the available heat within the unit is more effectively utilized.

The operation of the kiln is obvious. The material to be treated is introduced through the inlet and passes downwardly through the rotating casing toward the outlet l5. Because two intense heating zones are provided the hea-t from the gases of combustion are increased over the normal kiln so that a higher preheating of the material is carried out. The material is then subjected to the heating' zone created by the" name G of the burner C after which it passes through the intense heating zone created by the flames' Ac-v tually the two heating zones are effect a single zone and thus the material being treated is subjected to intense heat over a longer period of time as compared with the normal type of kiln. Although only a single burner C is illustrated in the drawing to form the second or extended heat'- ing zone, it is obvious that any desired number of elongate burners C may be employed. j

The invention has been shown and described as applied to a rotary kiln but it is noted that the improved burner arrangement is applicable to any type of kiln or furnace.

The foregoing disclosure and description of the invention is illustrative and explanatory thereof and various changes in the size, shape and materials, as well as in the details of the illustrated construction may be made, within the scope of the appended claims, without departing from the spirit of the invention.

Having described the invention, I claim:`

1. A kiln including an elongate housing circular in cross-section forming a longitudinal chamber, an inlet at one end of the chamber and an outlet at the opposite end of saidY chamber, whereby material to be treated and introduced through the inlet travels longitudinally cf the chamber to reach said outlet, a first elongate burner having its outlet end adjacent to the out-I let end of the chamber for creating any intense heating zone which extends longitudinally within the chamber nearer its outlet end, means for mounting said first burner at an angle to the longitudinal axis of said chamber for directing. the flame therefrom downwardly against the' bottom wall surface of said chamber, a second elongate burner spaced vertically above said r'st burner and extending through the longitudinallyv heating zone created` by the rst burner and' having its outlet end disposed within the extremity of the heating zone of the rst burner whereby the in tense heating zone created by the second burner forms an extension of said firstv heating Zone', and means for mounting said' second burner' at sub"-v stantially the same angle as said r'st burner whereby the material being treatedy is subjected to substantially the same intense heatv by Vsaid second burner asby said first burner.

2. A kiln as set forth in claim 1, wherein the elongate second burner comprises a tubular conduit having an axial fuel pipe therein, means for directing air through said conduit and fuel through the pipe to produce a combustible mixture, and longitudinal radially directed iin elements within and extending substantially the length of the bore of the conduit between which the introduced air flows, whereby said air cools the conduit of said second burner.

3. A furnace including, an elongate housing forming a longitudinal chamber and having an inlet at one end and being open at its opposite end to form an outlet, whereby material to be treated and introduced through the inlet travels longitudinally of the chamber and is discharged through the open outlet end, a first elongate pipe burner extending into the open discharge end of the chamber at an angle to the longitudinal axis of said housing to direct the flame therefrom downwardly against the bottom wall surface of the housing and having its outlet end adjacent said discharge end to project a longitudinal flame inwardly into the chamber and thereby create an intense heating zone, and a second pipe burner which is elongate and is directed at substantially the same angle as said first burner extending into the chamber through the open discharge end thereof and having a length sufficient to dispose its outlet end within the inner extremity of the heating zone created by the rst burner, whereby the second burner projects a longitudinal fiame inwardly of the chamber beyond the intense heating zone created by the first burner and thereby forms a second intense heating zone within the chamber which is an extension of said first heating zone.

LAWRENCE M. HARRIS.

References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 680,613 Partridge Aug. 13, 1901 822,929 Dellwik June 12, 1906 1,088,974 Lindhard Nov. 14, 1911 1,895,795 Hollowell Jan. 31, 1933 2,137,185 Seil Nov. 15, 1938 2,157,254 Borch May 9, 1939 2,301,017 Cherry Nov. 3, 1942 v 2,430,601 Cleary Nov. 11, 1947 2,584,808 Newhouse Feb. 5, 1952

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
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US822929 *Mar 22, 1906Jun 12, 1906Eduard Goldschmid JNodulizing ores, &c.
US1088974 *Feb 6, 1912Mar 3, 1914James W MasonCarbureter.
US1895795 *Jul 3, 1930Jan 31, 1933Natural Products Refining CoKiln
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US2430601 *Dec 8, 1941Nov 11, 1947American Aggregate CompanyMethod for treating argillaceous material
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2954613 *Apr 13, 1955Oct 4, 1960Baker David SApparatus and method for drying materials
US3074705 *Aug 17, 1961Jan 22, 1963Smidth & Co As F LRotary kiln and method of burning material therein
US3456934 *Feb 23, 1967Jul 22, 1969Dolomitwerke GmbhBurner projecting into a rotary kiln
US4690639 *Dec 3, 1986Sep 1, 1987Voorheis Industries, Inc.Constant pressure variable orifice burner nozzle assembly
US4746290 *May 29, 1986May 24, 1988International Technolgy CorporationOxidation, pyrolysis, purification
US4748921 *Aug 3, 1987Jun 7, 1988Mendenhall Robert LamarVaporization and combustion to remove toxic hydrocarbons
US4925389 *Jan 23, 1989May 15, 1990International Technology CorporationMethod and apparatus for treating waste containing organic contaminants
US4957429 *Aug 18, 1989Sep 18, 1990Mendenhall Robert LamarMethod and apparatus for removing volatile hydrocarbons from particulate soils
US5085581 *May 24, 1990Feb 4, 1992Mendenhall Robert LamarMethod and apparatus for removing volatile hydrocarbons from particulate soils
US5305696 *Oct 5, 1992Apr 26, 1994Mendenhall Robert LamarProcess and system for treating contaminated particulate soil compositions
US5425923 *Oct 27, 1992Jun 20, 1995Cmi CorporationThermal soil remediation system
US6110430 *Apr 6, 1998Aug 29, 2000Cmi CorporationShells, drums of thermoconductive material for discharging heat, tubes for heat exchanging
US6267493Jun 2, 1999Jul 31, 2001Cmi CorporationDrum mixer having a plurality of isolated aggregate transport channels
US6340240May 21, 2001Jan 22, 2002Cmi CorporationDrum mixer having isolated aggregate transport channels
EP1065461A1 *Jun 20, 2000Jan 3, 2001L'air Liquide Société Anonyme pour l'étude et l'exploration des procédés Georges ClaudeCombustion process, applicable in cement production
Classifications
U.S. Classification432/109
International ClassificationF27B7/20, F27B7/34
Cooperative ClassificationF27B7/34
European ClassificationF27B7/34