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US3661370A - Gas delivery manifold and processed material discharge assembly for rotary kiln - Google Patents

Gas delivery manifold and processed material discharge assembly for rotary kiln Download PDF

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Publication number
US3661370A
US3661370A US101282A US3661370DA US3661370A US 3661370 A US3661370 A US 3661370A US 101282 A US101282 A US 101282A US 3661370D A US3661370D A US 3661370DA US 3661370 A US3661370 A US 3661370A
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Prior art keywords
kiln
annular
kiln shell
rear wall
hood
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US101282A
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Eugene F Rossi
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Allis Chalmers Corp
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Allis Chalmers Corp
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Assigned to CONNECTICUT NATIONAL BANK THE, A NATIONAL BANKING ASSOCIATION AS TRUSTEE, WOODS KATHLEEN D., AS TRUSTEE reassignment CONNECTICUT NATIONAL BANK THE, A NATIONAL BANKING ASSOCIATION AS TRUSTEE SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ALLIS-CHALMERS CORPORATION A DE CORP.
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/005Rotary drum or kiln gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/74Construction of shells or jackets
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B7/00Rotary-drum furnaces, i.e. horizontal or slightly inclined
    • F27B7/08Rotary-drum furnaces, i.e. horizontal or slightly inclined externally heated
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0956Air or oxygen enriched air

Definitions

  • Fuel gas conducting tubes for supplying the kiln shell burners are mounted on the outer periphery of the kiln shell and extend axially through the hood and rear wall thereof.
  • the fuel tubes each have portions that project radially inward along an outer surface of the hood rear wall and axially away from the rear wall to an annular fuel gas manifold box mounted close around the hood rear wall neck.
  • the annular manifold box has a pair of axially spaced radial walls connected to rotate with the rotary hood and a nonrotating outer sleeve connected to a stationary fuel gas delivery conduit.
  • An annular air manifold box similar in construction to the fuel gas manifold box, is mounted close around the axially extending portions of the fuel tubes and between the fuel gas manifold box and the rear wall of the firing hood.
  • Air conducting tubes mounted on the kiln shell also extend axially through the rotary hood and rear wall thereof and have portions which project radially inward and axially away from the rear wall to the annular air manifold box.
  • the kiln is provided with a pair of radial discharge ports, circumferentially spaced 180 apart, for discharging processed material twice each revolution of the kiln.
  • the air and fuel gas tubes are arranged along the kiln shell in two groups, with each group of tubes being on one side of the kiln and between the pair of kiln discharge ports to be spaced away from hot processed material discharged through the ports.
  • This invention relates to rotary kilns, used for such purposes as'reducing iron ore to a lower state of oxidation, and having nozzles mounted on the outer surface of the kiln to project radially through the kiln shell and inject air and fuel into the kiln at axially spaced locations along the length of the kiln.
  • the present invention relates to an assembly for delivering air and gaseous fuel from stationary conduits to conduits mounted on the kiln shell to rotate therewith, and for discharging processed material from the kiln.
  • Rotary kilns for such as reducing iron ore to a lower state of oxidation and having nozzles projecting through a kiln shell for injecting air into the kiln, are disclosed in prior patents, for example U.S. Pat. No. 1,216,667 of 1917; U.S. Pat. No. 1,760,078 of 1930; and U.S. Pat. No. 2,344,440 of 1944.
  • Such kilns disclose seals between nonrotating conduit structures and rotating conduit structures having a diameter larger than the diameter of the kiln. It has always been difficult to construct good seals of such large diameter because thermal expansion is proportionately greater for larger sizes, and it is more difficult to provide the dimension tolerances and surface finishes needed for effective seals.
  • the problem was not serious as there is no danger involved if the seals leak air externally of the kiln and the economic loss from leaking air is not great.
  • U.S. Pat. No. 1,797,130 of 1931 accomplishes such fuel injection with a single annular tube extending along the central axis of the kiln and having nozzles which project radially outward from the tube.
  • U.S. Pat. Nos. 2,848,]98; 3,l82,980; and 3,196,938 provide several axially extending fuel conduits inside the kiln shell.
  • U.S. Pat. No. 3,01 1,772 discloses a double wall kiln with gaseous flue being delivered to the space between the walls.
  • the kiln constructions disclosed in this group of patents all involve seals between stationary and rotating fuel delivery conduits having a diameter smaller than the outer diameter of the assembly but all these constructions have two disadvantages.
  • One disadvantage is that-the gaseous fuel conduits are not kept cool by exposure to the atmosphere of surrounding air and a second disadvantage is that such conduits are hidden from view and cannot therefore be inspected. while the kiln is in operation.
  • the kiln must either contain a relatively large charge in order for material to flow over a dam formed by the discharge header (as with.S. Pat. No. 3,235,375); or be provided with internal lifters (as with U.S. Pat. Nos. 3,848,198; 3,011,772 and 3,196,938); or a double shell kiln and lifters for moving processed material back to the feed end of the kiln for discharge (as with U.S. Pat. No. 3, l 32,023).
  • a rotary kiln is provided with a rotary firing hood mounted concentrically over the material discharge end of the kiln to rotate with the kiln.
  • a main burner projects axially through a neck formed by a rear wall of the hood and a plurality of burners project radially through the kiln shell.
  • Fuel gas conducting tubes for supplying the burners projecting through the kiln shell, are mounted on the outer periphery of the kiln shell and extend axially through the rotary hood and rear wall thereof.
  • the fuel tubes each have portions that project radially inward along an outer surface of the hood rear wall and axially away from the rear wall in proximity to the burner assembly, to an annular fuel gas manifold box mounted around the burner assembly.
  • the annular manifold box has a pair of axially spaced radial walls attached to rotate with the burner assembly and a nonrotating outer sleeve connected to a stationary fuel gas delivery conduit.
  • An annular air manifold box similar in construction to the fuel gas manifold box, is mounted around the axially extending portions of the fuel tubes and between the fuel gas manifold box and the rear wall of the firing hood.
  • Air conducting tubes mounted on the kiln shell also extend axially through the hood and rear wall thereof.
  • the air tubes have portions which project radially inward along the outer surface of the hood rear wall and axially away from the rear wall to the annular air manifold box.
  • the kiln is provided with a pair of radial discharge ports, circumferentially spaced apart, for discharging processed material twice each revolution of the kiln.
  • the air and fuel gas tubes are arranged along the kiln shell in two groups, with each group of tubes being on one side of the kiln and between the pair of discharge ports.
  • Processed material therefore discharges from the kiln radially downward between the groups of tubes and down through the single discharge passage of the stationary hood, twice each revolution of the kiln, with the tubes being spaced away from the hot processed material discharged through the kiln ports.
  • FIG. 1 of the accompanying drawing is a fragmentary side elevation, partly in section, of a rotary kiln with a gas delivery manifold and processed material discharge assembly according to the present invention
  • FIG. 2 is an end view taken along line lIlI in FIG. 1 and viewing the structure in the direction indicated by arrows;
  • FIG. 3 is a fragmentary side elevation in section, taken along line III-III in FIG. 2, viewing the structure in the direction indicated by arrows and with a stationary hood, shown in FIGS. 1 and 2, eliminated from this view.
  • a rotary kiln having a cylindrical shell 1 is supported in a conventional manner (not shown) to rotate about a central axis A-A.
  • the shell 1 is refractory lined and provided with a pair of radial discharge ports 2, 3 adjacent the end 4 of kiln shell 1 and (see FIGS. 2, 3) the ports 2, 3 are circumferentially spaced apart I80", for discharging processed material downwardly therethrough; i.e., gravity discharge, twice each revolution of the kiln shell 1.
  • a rotary firing hood 5 is mounted concentrically about the discharge end 4 of the kiln shell 1 and connected thereto to rotate with the kiln shell 1 about the central axis A-A.
  • Hood 5 is provided with a rear wall 6 at the end 4 of kiln shell 1, and a forward wall 7 axially spaced along the kiln shell 1 from the rear wall 6.
  • the walls 6, 7 are axially spaced apart by axially extending tubular elements 8 arranged radially outward of kiln shell 1.
  • the rear wall 6 is provided with a neck 6a through which a conventional main kiln burner 9 projects concentrically to axis A--A into firing hood 5.
  • Rear wall 6 therefore encloses the discharge end 4 of kiln shell I about the burner 9.
  • the rear wall neck 6a is provided with a flange 10 attached thereto which therefore rotates with rear wall 6.
  • the flange 10 is sealed relative to the stationary burner 9 by a bellows seal 11.
  • the bellows seal 11 has a flange 12 which does not rotate, and which engages the rotating flange 10, to provide a friction seal between the stationary burner 9 and the rotating neck 6a of rear wall 6.
  • burner 9 has two branches 16, 17 with branch 16 being adapted for connection to a source of primary air (not shown) and branch 17 being adapted for connection to a source of primary fuel gas (not shown).
  • the burner 9 with its branches I6, 17, is mounted on a retractable burner support assembly 18.
  • a first annular gas manifold box 20 is provided around the rear wall neck 60 and between rear wall 6 and flange 10.
  • the box 20 is adapted for connection to a second stationary source of fuel gas, conduit 21, at a coupling 22.
  • a second annular gas manifold box 23 is provided between the manifold box 20 and rear wall 6, and box 23 is adapted for connection to a second stationary source of air, conduit 24, at a coupling 25.
  • the construction of the manifold boxes 20 and 23 will be described with reference to FIG. 3.
  • the first annular gas manifold box 20 has a first portion which is a cylindrical sleeve 28 with a port 29 in registry with the coupling 22, and sleeve 28 is fitted over and encloses a second portion of box 20 which is an annular channel 30.
  • the channel 30 comprises a pair of axially spaced annular walls 31, 32 attached to a cylindrical collar 33 fitted around a neck portion 6a of rear wall 6, through which the burner 9 projects.
  • the second portion i.e., the channel 30, rotates with the end wall 6.
  • Channel 30 therefore rotates within the inner periphery of the nonrotating sleeve 28.
  • the second annular gas manifold box 23 is constructed in a manner similar to the box 20 but the annular configuration of box 23 is of larger diameter than box 20, for reasons that shall appear as the description of the apparatus proceeds, and box 23 is proportionately larger than box 20 to accommodate air in larger volumes than the fuel gas delivered to box 20.
  • the box 23 has a first portion which is a cylindrical sleeve with a port 41 in registry with the coupling 25 and sleeve 40 is fitted over and encloses a second portion which is an annular channel 42.
  • the channel 42 comprises a pair of axially spaced annular walls 43, 44 attached to a cylindrical collar 45 radially spaced around the neck portion 6a of rear wall 6.
  • the second portion of box 23, i.e., the channel 42 also rotates with end wall 6.
  • Channel 42 therefore rotates within the inner periphery of the nonrotating sleeve 40.
  • Annular seals 46, 47 are provided between the channel 42 (which rotates) and the sleeve 40 (which does not rotate).
  • a first plurality of tubes 50 and a second plurality of tubes 51 are provided which each have a first section 52, 53 respectively, mounted on the outer periphery of kiln shell 1 parallel to the central axis A-A.
  • the tubes 50 are provided to deliver fuel gas and tubes 51 are provided to deliver air, to kiln shell burners 54, only one of which is shown (see FIG. I) and which may be such as are disclosed in US Pat. No. 3,029,l4l.
  • the first sections 52, 53 of tubes 50, 51 project through the tubular elements 8 which extend between the walls 6, 7 of rotary hood 5.
  • the tubes 50 have a second section 55 projecting radially inward along the outer surface of rear wall 6 and a third section 56 projecting axially away from rear wall 6.
  • the third section 56 of tubes 50 extends parallel to axis A-A radially outward of neck 60 of rear wall 6 and radially inward of the second annular gas manifold box 23, and into gas communicating connection with the first annular gas manifold box 20.
  • section 56 extends axially along the outer periphery of the neck 6a and inward of the cylindrical collar 45, and is connected to the annular wall 32 of the second portion of box 20, i.e., channel 30, to discharge gas into the box 20.
  • the tubes 51 have a second section 57 projecting radially inward and along the outer surface of rear wall 6 and a third section 58 projecting axially away from rear wall 6.
  • the third section 58 of tubes 51 extends parallel to axis A-A radially outward of the third sections 56 of tubes 50 and into air communicating connection with the second annular gas manifold box 23.
  • the sections 58 are connected to the annular wall 44 of the second portion of box 23, i.e., channel 42, to discharge air from the box 23.
  • the tubes 50, 51 are mounted on kiln shell 1 to rotate therewith and the annular channels 30, 42, are connected to the tubes 50, 51, the channels 30, 42 are carried by the tubes to rotate relative to the sleeves 28, 40 which are connected to stationary supply conduits 21, 24 and therefore carried in a position fixed in space.
  • the first sections 52, 53 of the tubes 50, 51 are arranged in two groups.
  • the tube sections 52, 53 of a first of the groups are identified in FIG. 2 as tube sections 520 and 53a
  • tube sections 52, 53 of a second of the groups are identified in FIG. 2 as tube sections 52b and 53b.
  • the tube sections 52a and 53a are arranged, alternately, along one side of the periphery of kiln shell I.
  • the individual tube sections 52a and 530 are circumferentially spaced apart from each other and the sections 520, 53a are grouped relative to the circumference of kiln shell 1 to be circumferentially between the discharge ports 2, 3 in kiln shell 1.
  • tube sections 52b and 53b are arranged, alternately, along the side of kiln shell 1 opposite to tube sections 520 and 53a, and the tube sections 52b, 53b are also grouped to be circumferentially between the discharge ports 2, 3. Thus none of the tube sections 52a, 53a or 52b, 53b pass axially over the ports 2, 3 in kiln shell 1.
  • the tubular elements 8 through which the tube sections 52a, 53a pass, are surrounded by a cast refractory shroud 60.
  • the tubular elements through which the tube sections 52b, 53b pass are also surrounded by a cast shroud 61 similar to shroud 60.
  • the shrouds 60, 61 may be fonned in place from a thick mud of refractory cement poured into suitable removable forms (not shown), after which the mud is permitted to dry and harden to a solid body.
  • the shrouds 60, 61 protect the tubular elements 8 from hot gases and processed material emitted from kiln shell ports 2 and 3, and the shrouds 60, 61 define therebetween a pair of radial discharge passages 62, 63 in registry with the kiln shell ports 2 and 3.
  • the apparatus is provided with a stationary hood 64 encircling the outer circumference of rotary hood 5 and stationary hood 64 defines a single downward discharge passage 65.
  • annular seals 66, 67 are provided between the stationary hood 64 and the rotary hood 5.
  • Each of the seals 66, 67 is provided with an annular ring 68 connected to the rotary hood 5 to rotate therewith, and an annular ring 69 pivotally connected by an actuating arm 70 to the stationary hood 64.
  • the pivotal actuating arm 70 is actuated by a weight 71 to bias ring 69 toward frictional engagement with ring 68 to provide a friction seal between rings 68, 69.
  • the apparatus that has been described may be operated to process material according to a variety of operations and processes, such as are disclosed for example in US. Pat. No. 1,797,130, US. Pat. No. 3,029,141, and U.S. Pat. No. 3,182,980.
  • material to be processed by heat and gases supplied by burners 9 and 54 moves axially through the kiln shell ltoward the discharge end 4, because of the usual slight downward sloping alignment of kiln shell 1 toward the discharge end 4.
  • Air and fuel for the primary burner 9 is supplied through the branches l6, 17 of the burner 9.
  • Fuel for the kiln shell burners 54 is supplied through the stationary conduit 21 to the first portion of box 20, i.e., nonrotating sleeve 28 of box 20, and to the second portion of box 20, i.e., annular channel 30 which rotates with kiln shell 1. From channel 30 the fuel gas passes through the sections 56, 55 and 52 of the first plurality of tubes 50.
  • Air for the kiln shell burner 54 is supplied through the stationary conduit 24 to the first portion of box 23, i.e., nonrotating sleeve 40 of box 23, and to the second portion of box 23, i.e., channel 42 which rotates with kiln shell 1. From channel 42 the air passes through the sections 58, 57 and 53 of the second plurality of tubes 51.
  • the foregoing operation is achieved with sealed annular gas manifold boxes 20, 23 being of smaller diameter than the kiln shell 1.
  • the annular seals 34, 35 for the fuel box are only slightly larger in diameter than the neck 6a of rear wall 6 and therefore can be constructed to effectively seal against loss of costly combustible fuelgases utilized in such as the described operations.
  • the tube sections 52 and 53 in tubular elements 8 that pass through the rotary firing hood 5 are not directly exposed to the atmosphere within the kiln or the hot and usually abrasive processed material discharging from the kiln.
  • An apparatus comprising:
  • a cylindrical rotary kiln shell having a plurality of kiln shell mounted burners each projecting radially inward through the kiln shell, and the kiln shell having a radial discharge 'portthrough the shell thereof adjacent one end of the kiln shell for discharging processed material from the kiln shell;
  • a rotary firing hood mounted concentrically about the end of the kiln shell and connected thereto to rotate with thekiln shell about a central axis through the kiln shell, with the rotary firing hood having a rear wall closing the adjacent end of the kiln shell;
  • a first annular gas manifold box concentric to the central axis and axially'spaced away from the kiln shell and hood rear wall adapted for connecting a stationary gas source to the plurality of kiln shell mounted burners, and said annular box having an outer circumference of a diameter smaller than the diameter of the kiln shell;
  • a first plurality of gas conducting tubes each having a first section mounted on the outer periphery of the kiln shell with each said tube first section connected on one end to at least one of said kiln shell mounted burners and each of the first sections being parallel to the central axis and circumferentially spaced away from the radial discharge port in the rotary kiln shell, with the first section of each tube extending through the rotary hood and rear wall thereof, and each tube having a second section projecting radially inward along the outer surface of the rear wall and a third section projecting axially away from the rear wall into connectionwith the annular gas manifold box for conducting gas from the annular gas manifold box into the gas conducting tubes to the shell mounted burners, and with the gas conducting tubes spaced away from exposure to processed, material discharged from the kiln shell through the radial discharge port.
  • An apparatus having a stationary hood encircling the outer circumference of the rotary hood and defining a downward discharge passage through which processed material from the rotary kiln shell is discharged upon rotation of the kiln shell to bring the kiln shell radial discharge port in registry with the stationary hood discharge passage.
  • An apparatus having a second annular gas manifold box with an outer diameter smaller than the diameter of the kiln shell but larger than the outer diameter of the first annular box, said second annular box being between the first gas manifold box and the rear wall of the rotary hood, concentric about the central axis and with an inner periphery radially outward of the third sections of the first plurality of gas tubes, and a second plurality of gas conducting tubes each having a first section mounted on the periphery of the kiln shell with each said tube first section connected on one end to at least one of the kiln shell mounted burners and each of the tube first sections being parallel to the central axis and circumferentially spaced away from the discharge port in the rotary kiln shell, with the first section of each tube of the second plurality extending through the rotary hood and rear wall thereof, and each tube of the second plurality having a second section projecting radially inward along the outer surface of the rear wall and a third section project
  • An apparatus having a main burner concentric to the central axis of the kiln and projecting through a central opening defined by the first and second annular gas manifold boxes, through the rear wall of the rotary hood, and into the adjacent end of the rotary kiln shell.
  • the rotary kiln shell having a pair of radial discharge ports circumferentially spaced apart, and the first sections of the gas conducting tubes being circumferentially arranged in two groups with both groups arranged circumferentially spaced from both discharge ports, to discharge processed material between the groups of tubes twice each revolution of the rotary kiln.
  • each tube of the first plurality being circumferentially located between a pair of tubes of the second plurality.
  • the first annular gas manifold box having a first portion comprising a cylindrical sleeve with a port adapted to be connected to a stationary gas source, and the first annular gas manifold box having a second portion comprising an annular channel defined by a cylindrical collar with a pair of axially spaced radially extending annular walls, the cylindrical sleeve being arranged to engage the outer periphery of the annular walls to enclose the annular channel of the said first annular gas manifold box and the third section of each gas conducting tube being connected to the annular channel for receiving gas there-from.
  • each annular gas manifold box having a first portion comprising a cylindrical nular gas manifold box, and the third section of each tube of the first plurality of tubes being connected to the annular channel of the first manifold box and the third section of each tube of the second plurality of tubes being connected to the annular channel of the second manifold box.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Incineration Of Waste (AREA)

Abstract

A rotary kiln is disclosed with a rotary firing hood mounted concentrically over the material discharge end of the kiln to rotate with the kiln. A main burner assembly projects axially through a neck formed by a rear wall of the hood and a plurality of burners project radially through the kiln shell. Fuel gas conducting tubes for supplying the kiln shell burners, are mounted on the outer periphery of the kiln shell and extend axially through the hood and rear wall thereof. The fuel tubes each have portions that project radially inward along an outer surface of the hood rear wall and axially away from the rear wall to an annular fuel gas manifold box mounted close around the hood rear wall neck. The annular manifold box has a pair of axially spaced radial walls connected to rotate with the rotary hood and a nonrotating outer sleeve connected to a stationary fuel gas delivery conduit. An annular air manifold box, similar in construction to the fuel gas manifold box, is mounted close around the axially extending portions of the fuel tubes and between the fuel gas manifold box and the rear wall of the firing hood. Air conducting tubes mounted on the kiln shell also extend axially through the rotary hood and rear wall thereof and have portions which project radially inward and axially away from the rear wall to the annular air manifold box. The kiln is provided with a pair of radial discharge ports, circumferentially spaced 180* apart, for discharging processed material twice each revolution of the kiln. The air and fuel gas tubes are arranged along the kiln shell in two groups, with each group of tubes being on one side of the kiln and between the pair of kiln discharge ports to be spaced away from hot processed material discharged through the ports.

Description

United States Patent Rossi [451 May 9, 1972 [54] GAS DELIVERY MANIFOLD AND PROCESSED MATERIAL DISCHARGE ASSEMBLY FOR ROTARY KILN Primary E.\-aminerJohn .l. Camby A!1orne \-Arth ur M. Streich, Robert B. Benson and John P. Hines [5 7] ABSTRACT A rotary kiln is disclosed with a rotary firing hood mounted F m l concentrically over the material discharge end of the kiln to rotate with the kiln. A main burner assembly projects axially through a neck formed by a rear wall of the hood and a plurality of burners project radially through the kiln shell. Fuel gas conducting tubes for supplying the kiln shell burners. are mounted on the outer periphery of the kiln shell and extend axially through the hood and rear wall thereof. The fuel tubes each have portions that project radially inward along an outer surface of the hood rear wall and axially away from the rear wall to an annular fuel gas manifold box mounted close around the hood rear wall neck. The annular manifold box has a pair of axially spaced radial walls connected to rotate with the rotary hood and a nonrotating outer sleeve connected to a stationary fuel gas delivery conduit. An annular air manifold box, similar in construction to the fuel gas manifold box, is mounted close around the axially extending portions of the fuel tubes and between the fuel gas manifold box and the rear wall of the firing hood. Air conducting tubes mounted on the kiln shell also extend axially through the rotary hood and rear wall thereof and have portions which project radially inward and axially away from the rear wall to the annular air manifold box. The kiln is provided with a pair of radial discharge ports, circumferentially spaced 180 apart, for discharging processed material twice each revolution of the kiln. The air and fuel gas tubes are arranged along the kiln shell in two groups, with each group of tubes being on one side of the kiln and between the pair of kiln discharge ports to be spaced away from hot processed material discharged through the ports.
8 Claims, 3 Drawing Figures PATENTEDMAY 9 I972 SHEET 1 BF 3 BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to rotary kilns, used for such purposes as'reducing iron ore to a lower state of oxidation, and having nozzles mounted on the outer surface of the kiln to project radially through the kiln shell and inject air and fuel into the kiln at axially spaced locations along the length of the kiln. In particular the present invention relates to an assembly for delivering air and gaseous fuel from stationary conduits to conduits mounted on the kiln shell to rotate therewith, and for discharging processed material from the kiln.
2. Description of the Prior Art Rotary kilns for such as reducing iron ore to a lower state of oxidation and having nozzles projecting through a kiln shell for injecting air into the kiln, are disclosed in prior patents, for example U.S. Pat. No. 1,216,667 of 1917; U.S. Pat. No. 1,760,078 of 1930; and U.S. Pat. No. 2,344,440 of 1944. Such kilns disclose seals between nonrotating conduit structures and rotating conduit structures having a diameter larger than the diameter of the kiln. It has always been difficult to construct good seals of such large diameter because thermal expansion is proportionately greater for larger sizes, and it is more difficult to provide the dimension tolerances and surface finishes needed for effective seals. For conduits and nozzles delivering only air to the kiln, the problem was not serious as there is no danger involved if the seals leak air externally of the kiln and the economic loss from leaking air is not great.
Early examples of prior art patents disclose constructions which avoided delivering gaseous fuel through such distribution systems for leaks of combustible gases could involve both danger and significant economic loss. 1
Early prior art patents disclose other ways for admitting fuel to the kiln. The three previously mentioned prior art patents introduced a reducing atmosphere into the kiln by injecting fuel through the usual axial burner projecting into the material discharge end of the furnace, and the first two of those references also disclose including combustible material with the charge material fed to the furnace.
Other ways have been disclosed by priorart to inject gaseousfuel into such a kiln without creating a need for such large diameter seals. U.S. Pat. No. 1,797,130 of 1931 accomplishes such fuel injection with a single annular tube extending along the central axis of the kiln and having nozzles which project radially outward from the tube. U.S. Pat. Nos. 2,848,]98; 3,l82,980; and 3,196,938 provide several axially extending fuel conduits inside the kiln shell. U.S. Pat. No. 3,01 1,772 discloses a double wall kiln with gaseous flue being delivered to the space between the walls. The kiln constructions disclosed in this group of patents all involve seals between stationary and rotating fuel delivery conduits having a diameter smaller than the outer diameter of the assembly but all these constructions have two disadvantages. One disadvantage is that-the gaseous fuel conduits are not kept cool by exposure to the atmosphere of surrounding air and a second disadvantage is that such conduits are hidden from view and cannot therefore be inspected. while the kiln is in operation.
U.S. Pat. Nos. 3,132,023 of 1964 and 3,235,375 do disclose constructions in which both air and fuel conduits carried to rotate with the kiln are external to the kiln and a joint between the rotating and nonrotating conduits does not require seals having a diameter larger than the kiln. The constructions disclosed in these two patents however (and U.S. Pat. Nos. 2,848,198; 3,196,938; and 3,0l 1,772 of the previous group) discharge processed material from the kiln through an opening central of the seal and therefore necessarily smaller than the diameter of the kiln. With such a construction the kiln must either contain a relatively large charge in order for material to flow over a dam formed by the discharge header (as with.S. Pat. No. 3,235,375); or be provided with internal lifters (as with U.S. Pat. Nos. 3,848,198; 3,011,772 and 3,196,938); or a double shell kiln and lifters for moving processed material back to the feed end of the kiln for discharge (as with U.S. Pat. No. 3, l 32,023).
SUMMARY OF THE INVENTION It is an object of the present invention to provide a new and improved gas delivery manifold and processed material discharge assembly in which gases from stationary sources of supply are delivered to tubesmounted on the outer periphery of a kiln to rotate with kiln, through sealed annular manifolds of diameter smaller than the kiln and mounted in spaced axial alignment relative to the discharge end of the kiln, and having provision for discharging processed material radially outward from the inner periphery of the kiln without direct exposure of the tubes to the hot processed material discharging from the kiln.
According to a preferred embodiment of the present invention a rotary kiln is provided with a rotary firing hood mounted concentrically over the material discharge end of the kiln to rotate with the kiln. A main burner projects axially through a neck formed by a rear wall of the hood and a plurality of burners project radially through the kiln shell. Fuel gas conducting tubes for supplying the burners projecting through the kiln shell, are mounted on the outer periphery of the kiln shell and extend axially through the rotary hood and rear wall thereof. The fuel tubes each have portions that project radially inward along an outer surface of the hood rear wall and axially away from the rear wall in proximity to the burner assembly, to an annular fuel gas manifold box mounted around the burner assembly. The annular manifold box has a pair of axially spaced radial walls attached to rotate with the burner assembly and a nonrotating outer sleeve connected to a stationary fuel gas delivery conduit. An annular air manifold box, similar in construction to the fuel gas manifold box, is mounted around the axially extending portions of the fuel tubes and between the fuel gas manifold box and the rear wall of the firing hood. Air conducting tubes mounted on the kiln shell also extend axially through the hood and rear wall thereof. The air tubes have portions which project radially inward along the outer surface of the hood rear wall and axially away from the rear wall to the annular air manifold box. The kiln is provided with a pair of radial discharge ports, circumferentially spaced apart, for discharging processed material twice each revolution of the kiln. The air and fuel gas tubes are arranged along the kiln shell in two groups, with each group of tubes being on one side of the kiln and between the pair of discharge ports. A stationary hood defining a single downward discharge passage, encloses the outer periphery of the rotary firing hood. Processed material therefore discharges from the kiln radially downward between the groups of tubes and down through the single discharge passage of the stationary hood, twice each revolution of the kiln, with the tubes being spaced away from the hot processed material discharged through the kiln ports.
Other features and objects of the invention that have been attained will appear from the more detailed description to follow with reference to an embodiment of the present invention shown in the accompanying drawing.
BRIEF DESCRIPTION OF THE DRAWING FIG. 1 of the accompanying drawing is a fragmentary side elevation, partly in section, of a rotary kiln with a gas delivery manifold and processed material discharge assembly according to the present invention;
FIG. 2 is an end view taken along line lIlI in FIG. 1 and viewing the structure in the direction indicated by arrows; and
- FIG. 3 is a fragmentary side elevation in section, taken along line III-III in FIG. 2, viewing the structure in the direction indicated by arrows and with a stationary hood, shown in FIGS. 1 and 2, eliminated from this view.
DESCRIPTION OF THE PREFERRED EMBODIMENT Referring to FIG. 1 of the drawings, a rotary kiln having a cylindrical shell 1 is supported in a conventional manner (not shown) to rotate about a central axis A-A. As shown in FIG. 3, the shell 1 is refractory lined and provided with a pair of radial discharge ports 2, 3 adjacent the end 4 of kiln shell 1 and (see FIGS. 2, 3) the ports 2, 3 are circumferentially spaced apart I80", for discharging processed material downwardly therethrough; i.e., gravity discharge, twice each revolution of the kiln shell 1.
Referring to FIGS. 1 and 3, a rotary firing hood 5 is mounted concentrically about the discharge end 4 of the kiln shell 1 and connected thereto to rotate with the kiln shell 1 about the central axis A-A. Hood 5 is provided with a rear wall 6 at the end 4 of kiln shell 1, and a forward wall 7 axially spaced along the kiln shell 1 from the rear wall 6. The walls 6, 7 are axially spaced apart by axially extending tubular elements 8 arranged radially outward of kiln shell 1. The rear wall 6 is provided with a neck 6a through which a conventional main kiln burner 9 projects concentrically to axis A--A into firing hood 5. Rear wall 6 therefore encloses the discharge end 4 of kiln shell I about the burner 9. The rear wall neck 6a is provided with a flange 10 attached thereto which therefore rotates with rear wall 6. The flange 10 is sealed relative to the stationary burner 9 by a bellows seal 11. The bellows seal 11 has a flange 12 which does not rotate, and which engages the rotating flange 10, to provide a friction seal between the stationary burner 9 and the rotating neck 6a of rear wall 6.
Referring to FIG. 1, burner 9 has two branches 16, 17 with branch 16 being adapted for connection to a source of primary air (not shown) and branch 17 being adapted for connection to a source of primary fuel gas (not shown). The burner 9 with its branches I6, 17, is mounted on a retractable burner support assembly 18. A first annular gas manifold box 20 is provided around the rear wall neck 60 and between rear wall 6 and flange 10. The box 20 is adapted for connection to a second stationary source of fuel gas, conduit 21, at a coupling 22. A second annular gas manifold box 23 is provided between the manifold box 20 and rear wall 6, and box 23 is adapted for connection to a second stationary source of air, conduit 24, at a coupling 25. The construction of the manifold boxes 20 and 23 will be described with reference to FIG. 3.
As shown in FIG. 3, the first annular gas manifold box 20 has a first portion which is a cylindrical sleeve 28 with a port 29 in registry with the coupling 22, and sleeve 28 is fitted over and encloses a second portion of box 20 which is an annular channel 30. The channel 30 comprises a pair of axially spaced annular walls 31, 32 attached to a cylindrical collar 33 fitted around a neck portion 6a of rear wall 6, through which the burner 9 projects. As will appear from the description to follow, the second portion; i.e., the channel 30, rotates with the end wall 6. Channel 30 therefore rotates within the inner periphery of the nonrotating sleeve 28. Annular seals 34, 35 are provided between the channel 30 (which rotates) and the sleeve 28 (which does not rotate). The second annular gas manifold box 23 is constructed in a manner similar to the box 20 but the annular configuration of box 23 is of larger diameter than box 20, for reasons that shall appear as the description of the apparatus proceeds, and box 23 is proportionately larger than box 20 to accommodate air in larger volumes than the fuel gas delivered to box 20. The box 23 has a first portion which is a cylindrical sleeve with a port 41 in registry with the coupling 25 and sleeve 40 is fitted over and encloses a second portion which is an annular channel 42. The channel 42 comprises a pair of axially spaced annular walls 43, 44 attached to a cylindrical collar 45 radially spaced around the neck portion 6a of rear wall 6. As will appear from the description to follow, the second portion of box 23, i.e., the channel 42, also rotates with end wall 6. Channel 42 therefore rotates within the inner periphery of the nonrotating sleeve 40. Annular seals 46, 47 are provided between the channel 42 (which rotates) and the sleeve 40 (which does not rotate).
Referring to FIGS. 1 and 3, a first plurality of tubes 50 and a second plurality of tubes 51 are provided which each have a first section 52, 53 respectively, mounted on the outer periphery of kiln shell 1 parallel to the central axis A-A. The tubes 50 are provided to deliver fuel gas and tubes 51 are provided to deliver air, to kiln shell burners 54, only one of which is shown (see FIG. I) and which may be such as are disclosed in US Pat. No. 3,029,l4l. The first sections 52, 53 of tubes 50, 51 project through the tubular elements 8 which extend between the walls 6, 7 of rotary hood 5. The tubes 50 have a second section 55 projecting radially inward along the outer surface of rear wall 6 and a third section 56 projecting axially away from rear wall 6. The third section 56 of tubes 50 extends parallel to axis A-A radially outward of neck 60 of rear wall 6 and radially inward of the second annular gas manifold box 23, and into gas communicating connection with the first annular gas manifold box 20. As shown in FIG. 3 section 56 extends axially along the outer periphery of the neck 6a and inward of the cylindrical collar 45, and is connected to the annular wall 32 of the second portion of box 20, i.e., channel 30, to discharge gas into the box 20. The tubes 51 have a second section 57 projecting radially inward and along the outer surface of rear wall 6 and a third section 58 projecting axially away from rear wall 6. The third section 58 of tubes 51 extends parallel to axis A-A radially outward of the third sections 56 of tubes 50 and into air communicating connection with the second annular gas manifold box 23. The sections 58 are connected to the annular wall 44 of the second portion of box 23, i.e., channel 42, to discharge air from the box 23. Since the tubes 50, 51 are mounted on kiln shell 1 to rotate therewith and the annular channels 30, 42, are connected to the tubes 50, 51, the channels 30, 42 are carried by the tubes to rotate relative to the sleeves 28, 40 which are connected to stationary supply conduits 21, 24 and therefore carried in a position fixed in space.
Referring to FIG. 2, the first sections 52, 53 of the tubes 50, 51, are arranged in two groups. The tube sections 52, 53 of a first of the groups are identified in FIG. 2 as tube sections 520 and 53a, and tube sections 52, 53 of a second of the groups are identified in FIG. 2 as tube sections 52b and 53b. The tube sections 52a and 53a are arranged, alternately, along one side of the periphery of kiln shell I. The individual tube sections 52a and 530 are circumferentially spaced apart from each other and the sections 520, 53a are grouped relative to the circumference of kiln shell 1 to be circumferentially between the discharge ports 2, 3 in kiln shell 1. Likewise, the tube sections 52b and 53b are arranged, alternately, along the side of kiln shell 1 opposite to tube sections 520 and 53a, and the tube sections 52b, 53b are also grouped to be circumferentially between the discharge ports 2, 3. Thus none of the tube sections 52a, 53a or 52b, 53b pass axially over the ports 2, 3 in kiln shell 1.
Referring to FIGS. 2 and 3, the tubular elements 8 through which the tube sections 52a, 53a pass, are surrounded by a cast refractory shroud 60. As shown in FIG. 2, the tubular elements through which the tube sections 52b, 53b pass are also surrounded by a cast shroud 61 similar to shroud 60. The shrouds 60, 61 may be fonned in place from a thick mud of refractory cement poured into suitable removable forms (not shown), after which the mud is permitted to dry and harden to a solid body. The shrouds 60, 61 protect the tubular elements 8 from hot gases and processed material emitted from kiln shell ports 2 and 3, and the shrouds 60, 61 define therebetween a pair of radial discharge passages 62, 63 in registry with the kiln shell ports 2 and 3.
Referring to FIGS. 1 and 2, the apparatus is provided with a stationary hood 64 encircling the outer circumference of rotary hood 5 and stationary hood 64 defines a single downward discharge passage 65.
Referring to FIG. 1, annular seals 66, 67 are provided between the stationary hood 64 and the rotary hood 5. Each of the seals 66, 67 is provided with an annular ring 68 connected to the rotary hood 5 to rotate therewith, and an annular ring 69 pivotally connected by an actuating arm 70 to the stationary hood 64. The pivotal actuating arm 70 is actuated by a weight 71 to bias ring 69 toward frictional engagement with ring 68 to provide a friction seal between rings 68, 69.
The apparatus that has been described may be operated to process material according to a variety of operations and processes, such as are disclosed for example in US. Pat. No. 1,797,130, US. Pat. No. 3,029,141, and U.S. Pat. No. 3,182,980. In operation with the described apparatus material to be processed by heat and gases supplied by burners 9 and 54, moves axially through the kiln shell ltoward the discharge end 4, because of the usual slight downward sloping alignment of kiln shell 1 toward the discharge end 4. Air and fuel for the primary burner 9 is supplied through the branches l6, 17 of the burner 9. Fuel for the kiln shell burners 54 is supplied through the stationary conduit 21 to the first portion of box 20, i.e., nonrotating sleeve 28 of box 20, and to the second portion of box 20, i.e., annular channel 30 which rotates with kiln shell 1. From channel 30 the fuel gas passes through the sections 56, 55 and 52 of the first plurality of tubes 50. Air for the kiln shell burner 54 is supplied through the stationary conduit 24 to the first portion of box 23, i.e., nonrotating sleeve 40 of box 23, and to the second portion of box 23, i.e., channel 42 which rotates with kiln shell 1. From channel 42 the air passes through the sections 58, 57 and 53 of the second plurality of tubes 51. After the material in kiln shell 1 has been processed and arrives at the discharge end 4 of kiln shell 1, the material is discharged from the kiln twice each revolution of kiln shell 1 and rotary hood'5, through ports land 3 and between the shrouds 60, 61 enclosing the two groups of tube sections 52a, 53a and 52b, 53b, to fall downwardly through the stationary hood discharge passage 65. 7
With the described apparatus the foregoing operation is achieved with sealed annular gas manifold boxes 20, 23 being of smaller diameter than the kiln shell 1. In fact, the annular seals 34, 35 for the fuel box are only slightly larger in diameter than the neck 6a of rear wall 6 and therefore can be constructed to effectively seal against loss of costly combustible fuelgases utilized in such as the described operations. Furthermore, the tube sections 52 and 53 in tubular elements 8 that pass through the rotary firing hood 5 are not directly exposed to the atmosphere within the kiln or the hot and usually abrasive processed material discharging from the kiln.
From the foregoing detailed description of the present invention it has been shown how the objects of the present invention have been attained in a preferred manner. However, modification and equivalents of the disclosed concepts such as readily occur to those skilled in the art are intended to be inv cluded in the scope of this invention. Thus, the scope of the invention is intended to be limited only by the scope of the claims such as are or may hereafter be, appended hereto.
The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
1. An apparatus comprising:
a. a cylindrical rotary kiln shell having a plurality of kiln shell mounted burners each projecting radially inward through the kiln shell, and the kiln shell having a radial discharge 'portthrough the shell thereof adjacent one end of the kiln shell for discharging processed material from the kiln shell;
b. a rotary firing hood mounted concentrically about the end of the kiln shell and connected thereto to rotate with thekiln shell about a central axis through the kiln shell, with the rotary firing hood having a rear wall closing the adjacent end of the kiln shell;
c. a first annular gas manifold box concentric to the central axis and axially'spaced away from the kiln shell and hood rear wall adapted for connecting a stationary gas source to the plurality of kiln shell mounted burners, and said annular box having an outer circumference of a diameter smaller than the diameter of the kiln shell; and
d. a first plurality of gas conducting tubes each having a first section mounted on the outer periphery of the kiln shell with each said tube first section connected on one end to at least one of said kiln shell mounted burners and each of the first sections being parallel to the central axis and circumferentially spaced away from the radial discharge port in the rotary kiln shell, with the first section of each tube extending through the rotary hood and rear wall thereof, and each tube having a second section projecting radially inward along the outer surface of the rear wall and a third section projecting axially away from the rear wall into connectionwith the annular gas manifold box for conducting gas from the annular gas manifold box into the gas conducting tubes to the shell mounted burners, and with the gas conducting tubes spaced away from exposure to processed, material discharged from the kiln shell through the radial discharge port.
2. An apparatus according to claim 1 having a stationary hood encircling the outer circumference of the rotary hood and defining a downward discharge passage through which processed material from the rotary kiln shell is discharged upon rotation of the kiln shell to bring the kiln shell radial discharge port in registry with the stationary hood discharge passage.
3. An apparatus according to claim 1 having a second annular gas manifold box with an outer diameter smaller than the diameter of the kiln shell but larger than the outer diameter of the first annular box, said second annular box being between the first gas manifold box and the rear wall of the rotary hood, concentric about the central axis and with an inner periphery radially outward of the third sections of the first plurality of gas tubes, and a second plurality of gas conducting tubes each having a first section mounted on the periphery of the kiln shell with each said tube first section connected on one end to at least one of the kiln shell mounted burners and each of the tube first sections being parallel to the central axis and circumferentially spaced away from the discharge port in the rotary kiln shell, with the first section of each tube of the second plurality extending through the rotary hood and rear wall thereof, and each tube of the second plurality having a second section projecting radially inward along the outer surface of the rear wall and a third section projecting axially away from the rear wall into connection with the second annular gas manifold box.
4. An apparatus according to claim 3 having a main burner concentric to the central axis of the kiln and projecting through a central opening defined by the first and second annular gas manifold boxes, through the rear wall of the rotary hood, and into the adjacent end of the rotary kiln shell.
5. In an apparatus according to claim 1, the rotary kiln shell having a pair of radial discharge ports circumferentially spaced apart, and the first sections of the gas conducting tubes being circumferentially arranged in two groups with both groups arranged circumferentially spaced from both discharge ports, to discharge processed material between the groups of tubes twice each revolution of the rotary kiln.
6. In an apparatus according to claim 3, the tubes of the first and second pluralities thereof being arranged with each tube of the first plurality being circumferentially located between a pair of tubes of the second plurality.
7. In an apparatus according to claim 1, the first annular gas manifold box having a first portion comprising a cylindrical sleeve with a port adapted to be connected to a stationary gas source, and the first annular gas manifold box having a second portion comprising an annular channel defined by a cylindrical collar with a pair of axially spaced radially extending annular walls, the cylindrical sleeve being arranged to engage the outer periphery of the annular walls to enclose the annular channel of the said first annular gas manifold box and the third section of each gas conducting tube being connected to the annular channel for receiving gas there-from.
8. In an apparatus according to claim 3, each annular gas manifold box having a first portion comprising a cylindrical nular gas manifold box, and the third section of each tube of the first plurality of tubes being connected to the annular channel of the first manifold box and the third section of each tube of the second plurality of tubes being connected to the annular channel of the second manifold box.
t I 1 k I

Claims (8)

1. An apparatus comprising: a. a cylindrical rotary kiln shell having a plurality of kiln shell mounted burners each projecting radially inward through the kiln shell, and the kiln shell having a radial discharge port through the shell thereof adjacent one end of the kiln shell for discharging processed material from the kiln shell; b. a rotary firing hood mounted concentrically about the end of the kiln shell and connected thereto to rotate with the kiln shell about a central axis through the kiln shell, with the rotary firing hood having a rear wall closing the adjacent end of the kiln shell; c. a first annular gas manifold box concentric to the central axis and axially spaced away from the kiln shell and hood rear wall adapted for connecting a stationary gas source to the plurality of kiln shell mounted burners, and said annular box having an outer circumference of a diameter smaller than the diameter of the kiln shell; and d. a first plurality of gas conducting tubes each having a first section mounted on the outer periphery of the kiln shell with each said tube first section connected on one end to at least one of said kiln shell mounted burners and each of the first sections being parallel to thE central axis and circumferentially spaced away from the radial discharge port in the rotary kiln shell, with the first section of each tube extending through the rotary hood and rear wall thereof, and each tube having a second section projecting radially inward along the outer surface of the rear wall and a third section projecting axially away from the rear wall into connection with the annular gas manifold box for conducting gas from the annular gas manifold box into the gas conducting tubes to the shell mounted burners, and with the gas conducting tubes spaced away from exposure to processed material discharged from the kiln shell through the radial discharge port.
2. An apparatus according to claim 1 having a stationary hood encircling the outer circumference of the rotary hood and defining a downward discharge passage through which processed material from the rotary kiln shell is discharged upon rotation of the kiln shell to bring the kiln shell radial discharge port in registry with the stationary hood discharge passage.
3. An apparatus according to claim 1 having a second annular gas manifold box with an outer diameter smaller than the diameter of the kiln shell but larger than the outer diameter of the first annular box, said second annular box being between the first gas manifold box and the rear wall of the rotary hood, concentric about the central axis and with an inner periphery radially outward of the third sections of the first plurality of gas tubes, and a second plurality of gas conducting tubes each having a first section mounted on the periphery of the kiln shell with each said tube first section connected on one end to at least one of the kiln shell mounted burners and each of the tube first sections being parallel to the central axis and circumferentially spaced away from the discharge port in the rotary kiln shell, with the first section of each tube of the second plurality extending through the rotary hood and rear wall thereof, and each tube of the second plurality having a second section projecting radially inward along the outer surface of the rear wall and a third section projecting axially away from the rear wall into connection with the second annular gas manifold box.
4. An apparatus according to claim 3 having a main burner concentric to the central axis of the kiln and projecting through a central opening defined by the first and second annular gas manifold boxes, through the rear wall of the rotary hood, and into the adjacent end of the rotary kiln shell.
5. In an apparatus according to claim 1, the rotary kiln shell having a pair of radial discharge ports circumferentially spaced 180* apart, and the first sections of the gas conducting tubes being circumferentially arranged in two groups with both groups arranged circumferentially spaced from both discharge ports, to discharge processed material between the groups of tubes twice each revolution of the rotary kiln.
6. In an apparatus according to claim 3, the tubes of the first and second pluralities thereof being arranged with each tube of the first plurality being circumferentially located between a pair of tubes of the second plurality.
7. In an apparatus according to claim 1, the first annular gas manifold box having a first portion comprising a cylindrical sleeve with a port adapted to be connected to a stationary gas source, and the first annular gas manifold box having a second portion comprising an annular channel defined by a cylindrical collar with a pair of axially spaced radially extending annular walls, the cylindrical sleeve being arranged to engage the outer periphery of the annular walls to enclose the annular channel of the said first annular gas manifold box and the third section of each gas conducting tube being connected to the annular channel for receiving gas there-from.
8. In an apparatus according to claim 3, each annular gas manifold box having a first portion comprising a cylindrical sleeve with a port adapted to be connected to a stationary gas source, and each annular gas manifold box having a second portion comprising an annular channel defined by a cylindrical collar with a pair of axially spaced radially extending annular walls, the cylindrical sleeve of each said box being arranged to engage the outer periphery of the annular walls of each said box to enclose the annular channel of each said annular gas manifold box, and the third section of each tube of the first plurality of tubes being connected to the annular channel of the first manifold box and the third section of each tube of the second plurality of tubes being connected to the annular channel of the second manifold box.
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US4198761A (en) * 1978-04-20 1980-04-22 Societe pour la Recherche, l'Etude et Mise au Point de Tous Brevets, S.O.R.E.B. Forced blowing method for fluids enabling thermal exchanges within a moving mass of material placed in a rotating cylinder
US4374650A (en) * 1981-05-18 1983-02-22 Allis-Chalmers Corporation Bi-flow rotary kiln coal gasification process
US4440351A (en) * 1981-12-21 1984-04-03 Allis-Chalmers Corporation Apparatus for delivering fluid to a rotating body
US5619936A (en) * 1993-05-28 1997-04-15 Kleen Soil Technologies, L.C. Thermal desorption unit and processes
US6221127B1 (en) 1999-11-10 2001-04-24 Svedala Industries, Inc. Method of pyroprocessing mineral ore material for reducing combustion NOx
US6474984B2 (en) 2000-11-20 2002-11-05 Metso Minerals Industries, Inc. Air injection for nitrogen oxide reduction and improved product quality

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DE3128556A1 (en) * 1981-07-18 1983-06-01 Acos Finos Piratini S.A., Porto Alegro METHOD FOR MEASURING THE GAS BLOWED INTO A TURNTUBE

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US2091850A (en) * 1933-07-29 1937-08-31 American Lurgi Corp Apparatus for the performance of metallurgical or chemical reactions
US2941791A (en) * 1956-08-23 1960-06-21 Wienert Fritz Otto Rotary kilns

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US1572805A (en) * 1925-06-15 1926-02-09 Alfred Petter Pehrson Rotary furnace
US2091850A (en) * 1933-07-29 1937-08-31 American Lurgi Corp Apparatus for the performance of metallurgical or chemical reactions
US2941791A (en) * 1956-08-23 1960-06-21 Wienert Fritz Otto Rotary kilns

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4198761A (en) * 1978-04-20 1980-04-22 Societe pour la Recherche, l'Etude et Mise au Point de Tous Brevets, S.O.R.E.B. Forced blowing method for fluids enabling thermal exchanges within a moving mass of material placed in a rotating cylinder
US4374650A (en) * 1981-05-18 1983-02-22 Allis-Chalmers Corporation Bi-flow rotary kiln coal gasification process
US4440351A (en) * 1981-12-21 1984-04-03 Allis-Chalmers Corporation Apparatus for delivering fluid to a rotating body
US5619936A (en) * 1993-05-28 1997-04-15 Kleen Soil Technologies, L.C. Thermal desorption unit and processes
US6221127B1 (en) 1999-11-10 2001-04-24 Svedala Industries, Inc. Method of pyroprocessing mineral ore material for reducing combustion NOx
US6474984B2 (en) 2000-11-20 2002-11-05 Metso Minerals Industries, Inc. Air injection for nitrogen oxide reduction and improved product quality

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BR7108555D0 (en) 1973-05-17
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MY7400108A (en) 1974-12-31
DE2164563B2 (en) 1974-01-10
JPS5118201B1 (en) 1976-06-08
GB1329199A (en) 1973-09-05
DE2164563A1 (en) 1972-08-10
CA950664A (en) 1974-07-09

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Effective date: 19830329