US2873224A - Process and apparatus for desurfacing a refractory metal body - Google Patents

Process and apparatus for desurfacing a refractory metal body Download PDF

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Publication number
US2873224A
US2873224A US506532A US50653255A US2873224A US 2873224 A US2873224 A US 2873224A US 506532 A US506532 A US 506532A US 50653255 A US50653255 A US 50653255A US 2873224 A US2873224 A US 2873224A
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solid fuel
acute angle
powdered solid
stream
oxidizing gas
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US506532A
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Ivan P Thompson
Allmang William
Carl E Hartmann
Charles E Winter
Robert W Blackbourn
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Union Carbide Corp
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Union Carbide Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23KSOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
    • B23K7/00Cutting, scarfing, or desurfacing by applying flames
    • B23K7/06Machines, apparatus, or equipment specially designed for scarfing or desurfacing

Definitions

  • the invention relates to thermochemical metal removal, and more particularly to method and apparatus for machine scarfing of cold stainless steel with externally fed powdered solid fuel.
  • the objects of the present invention are to provide a quality surface regardless of the condition of the steel section prior to desurfacing, to maintain uniformly good stability when desurfacing at varying depths of cut, to provide and supply an even distribution of the powder down and into the reaction zone in the quantities found best for desurfacting, and to provide uniform depth to cut across the work surface under the gap between adjacent nozzles as well as under the centers of the nozzles, and to concentrate and stabilize the reaction zone to facilitate carrying long cuts.
  • the process of desurfacing a refractory metal body comprises applying preheat to a local surface portion of such a body, discharging a relatively flat stream of oxidizing gas at an acute angle against such heated portion, supplying a row of streams of powdered solid fuel-laden gas at an acute angle against coplanar surfaces of hard-facing erosion resistant material, discharging the resultant separateflat stream of gas containing uniformly transversely distributed powdered solid fuel at an acute angle toward such oxidizing gas stream, so that the central planes of such streams in the direction of flow thereof fonn dihedral angles with one another and with such surface portion of the body, and relatively moving such streams with respect to the body so that successive surface portions thereof are progressively removed thermochemically by the scarfing action of the combined powdered solid fuel and oxidizing g'as'stream.
  • Fig. 1 is a side elevation of a desurfacing machine according to, and for carrying out the method of the present invention
  • Fig. 2 is a front elevation of the same
  • Fig. 3 is a vertical cross section through the desurfacing head
  • Fig. 4 is a plan view of the work surface showing the reaction zone
  • Fig. 5 is a plan view of the powder nozzle plate
  • Fig. 6 is a section taken along the line 6-6 of Fig. 5;
  • ice Fig. 7 is a section taken along the line 7--7 of Fig. 6.
  • the invention is illustrated as applied to a desurfacing machine comprising a head H mounted on a suitable support S above the path of the work W, such as a cold slab of stainless steel.
  • the head H comprises a nozzle block 12 provided with a plurality of flat slotted nozzles 14 for discharging a relatively ilat stream of cutting oxygen against the work W, as well as upper and lower rows of ports 16 and 18 for discharging preheat gas flames adjacent such scarfing oxygen stream.
  • the cutting oxygen is supplied to the slotted nozzles 14 by tubes 20, and the preheat mixture of oxygen and acetylene is supplied by mixers 22 and tubes 23 to the ports 16 and 18.
  • a relatively flat powder nozzle 10 is mounted on the nozzle block 12, and is shown in detail in Fig. 3.
  • the fiat slotted nozzles 14 discharge a relatively fiat stream 25 of cutting oxygen against the work W, and the rows of ports 16 and 18 discharge preheat gas flames 26 and 28 adjacent such scarfing oxygen stream.
  • the preheating gas flames extend above and below the oxygen stream 25, forming dihedral angles with the work surface 29.
  • the powder nozzle 10 comprises a metal base plate 30 and a metal cover 32 suitably bolted together.
  • the cover 32 is recessed to form relatively long uniformly spaced channels 34, each of which, as shown in Fig. 6, has a top wall 35 converging in the direction of flow with the upper surface of the base 36.
  • the channels 34 have side walls 36 diverging in the direction of flow as shown in Fig. 7'
  • Powder-laden gas is supplied to each channel 34 by a tube 38 mounted in the cover 32 at an angle b, which is an optimum of A change of 5 either side of this optimum angle causes a noticeable change in the powder flow as it exits from the nozzle. Too shallow an angle causes the powder to become concentrated in the middle of the slot, while too steep an angle causes the powder to run down the side edges of the powder slot.
  • the tube 38 terminates at the top wall 35, and directs the stream of powder-laden gas against the top of the base plate 30 therebelow.
  • a disk 40 of hard-facing material such as tungsten carbide is inserted in a socket in the base plate flush with the upper surface thereof.
  • a rubber disk 42 is used as a shim to provide for top surface alignment. As compared to a chromium plated wear plate life of two hours continuous powder flow, a soft rubber disk increased this to eight hours, and with the rubber backed sintered tungsten carbide disks shown, no sign of wear was evident after thirty hours of continuous service.
  • the powder-laden streams of carrier gas such as air, nitrogen or oxygen, for example, coming from the tubes 38 as round streams are flattened by impact at an angle of between 35 and 45 against the carbide disks 40 and passes along the channels 34 and out the flat orifices 37.
  • the discharge face of the powder nozzle 10 is positioned on the blowpipe nozzle 12 so that the channels 34 discharge the separate powder-laden carrier gas streams from the fiat orifices 37 located above the front upper edge of the nozzle 12. These streams combine to form the transversely continuous powder-laden gas stream 45 which forms a dihedral angle with the oxygen stream 25 and the work surface 29.
  • the individual branch tube 38 in connection with each channel 34 is one of a battery of such tubes leading from a distributor 46 shown in Fig. 1, which in turn is connected to a powder-laden gas supply line 47.
  • the powder nozzle 10 itself was found to warp or buck-1e because of the extreme heat of the desurfacing reaction.
  • the powder nozzle had to be water cooled to eliminate this warping. Accordingly, the powder nozzle cover 32 above the channels 34 is provided

Description

Feb. 10, 1959 l. P. THOMPSON ETAL PROCESS AND APPARATUS FOR DESURFACINQ A REFRACTORY METAL BODY Filed May ,6, 1955 Q Q i? 3 Sheets-Sheet 1 INVENTORS IVAN P.THOMP$ON WILLIAM ALLMANG CARL E.HARTMANN CHARLES E-WINTER ROBERT W. BLACKBOURN ATTORNEY Feb. 10, 1959 P. THoMPsbN ETAL PROCESS AND APPARATUS FOR DESURFACING A REFRACTORY METAL BODY Filed May 6, 1955 3 Sheets-Sheet 2 Powder Tubes Air Tube Concentrated Reachon Zone ATTO RNEY Feb. 10, 1959 l. P. THOMPSON El'AL 2,873,224
PROCESS AND APPARATUS FOR DESURFACING A REFRACTORY METAL BODY :s Sheets-Sheet 3 Filed May 6, 1955 INVENTORS IVAN P.
THOMPSON A WILLIA ALLMANG HARTMANN S E.W|NTER CARL E. CHARLE ROBERT W.VBLACKBOURN $20M J v ATTORNEY United States Patent PROCESS AND APPARATUS FOR DESURFACING A REFRACTORY METAL BODY Application May 6, 1955, Serial N 0. 506,532
4 Claims. (Cl. 148-95) The invention relates to thermochemical metal removal, and more particularly to method and apparatus for machine scarfing of cold stainless steel with externally fed powdered solid fuel.
The success of the operation of cold desurfacing of stainless steel with manually operated powder fed blowpipes depends largely on the flexibility of the hand operation and the skill of the operator. These features are lost in the mechanization of the process for operation by machine, which accordingly presents new problems. The angle of inclination of the desurfacing nozzle cannot be adjusted as the surface quality of the steel section changes. The speed at which the mechanized desurfacing pass is made cannot be changed to suit the conditions, and the nozzle height must be kept constant. Another problem is to accomplish blending of the cuts made by thev individual nozzles.
The objects of the present invention are to provide a quality surface regardless of the condition of the steel section prior to desurfacing, to maintain uniformly good stability when desurfacing at varying depths of cut, to provide and supply an even distribution of the powder down and into the reaction zone in the quantities found best for desurfacting, and to provide uniform depth to cut across the work surface under the gap between adjacent nozzles as well as under the centers of the nozzles, and to concentrate and stabilize the reaction zone to facilitate carrying long cuts.
According to the present invention, the process of desurfacing a refractory metal body comprises applying preheat to a local surface portion of such a body, discharging a relatively flat stream of oxidizing gas at an acute angle against such heated portion, supplying a row of streams of powdered solid fuel-laden gas at an acute angle against coplanar surfaces of hard-facing erosion resistant material, discharging the resultant separateflat stream of gas containing uniformly transversely distributed powdered solid fuel at an acute angle toward such oxidizing gas stream, so that the central planes of such streams in the direction of flow thereof fonn dihedral angles with one another and with such surface portion of the body, and relatively moving such streams with respect to the body so that successive surface portions thereof are progressively removed thermochemically by the scarfing action of the combined powdered solid fuel and oxidizing g'as'stream.
In the drawings:
Fig. 1 is a side elevation of a desurfacing machine according to, and for carrying out the method of the present invention;
Fig. 2 is a front elevation of the same;
Fig. 3 is a vertical cross section through the desurfacing head;
Fig. 4 is a plan view of the work surface showing the reaction zone;
Fig. 5 is a plan view of the powder nozzle plate;
Fig. 6 is a section taken along the line 6-6 of Fig. 5; and
" ice Fig. 7 is a section taken along the line 7--7 of Fig. 6.
As shown in the drawings, the invention is illustrated as applied to a desurfacing machine comprising a head H mounted on a suitable support S above the path of the work W, such as a cold slab of stainless steel. The head H comprises a nozzle block 12 provided with a plurality of flat slotted nozzles 14 for discharging a relatively ilat stream of cutting oxygen against the work W, as well as upper and lower rows of ports 16 and 18 for discharging preheat gas flames adjacent such scarfing oxygen stream. The cutting oxygen is supplied to the slotted nozzles 14 by tubes 20, and the preheat mixture of oxygen and acetylene is supplied by mixers 22 and tubes 23 to the ports 16 and 18.
According to the present invention a relatively flat powder nozzle 10 is mounted on the nozzle block 12, and is shown in detail in Fig. 3. The fiat slotted nozzles 14 discharge a relatively fiat stream 25 of cutting oxygen against the work W, and the rows of ports 16 and 18 discharge preheat gas flames 26 and 28 adjacent such scarfing oxygen stream. The preheating gas flames extend above and below the oxygen stream 25, forming dihedral angles with the work surface 29.
The powder nozzle 10 comprises a metal base plate 30 and a metal cover 32 suitably bolted together. The cover 32 is recessed to form relatively long uniformly spaced channels 34, each of which, as shown in Fig. 6, has a top wall 35 converging in the direction of flow with the upper surface of the base 36. The channels 34 have side walls 36 diverging in the direction of flow as shown in Fig. 7'
and leading to uniformly closely spaced fiat slots 37.
Powder-laden gas is supplied to each channel 34 by a tube 38 mounted in the cover 32 at an angle b, which is an optimum of A change of 5 either side of this optimum angle causes a noticeable change in the powder flow as it exits from the nozzle. Too shallow an angle causes the powder to become concentrated in the middle of the slot, while too steep an angle causes the powder to run down the side edges of the powder slot.
The tube 38 terminates at the top wall 35, and directs the stream of powder-laden gas against the top of the base plate 30 therebelow. A disk 40 of hard-facing material such as tungsten carbide is inserted in a socket in the base plate flush with the upper surface thereof. A rubber disk 42 is used as a shim to provide for top surface alignment. As compared to a chromium plated wear plate life of two hours continuous powder flow, a soft rubber disk increased this to eight hours, and with the rubber backed sintered tungsten carbide disks shown, no sign of wear was evident after thirty hours of continuous service.
The powder-laden streams of carrier gas such as air, nitrogen or oxygen, for example, coming from the tubes 38 as round streams are flattened by impact at an angle of between 35 and 45 against the carbide disks 40 and passes along the channels 34 and out the flat orifices 37. The discharge face of the powder nozzle 10 is positioned on the blowpipe nozzle 12 so that the channels 34 discharge the separate powder-laden carrier gas streams from the fiat orifices 37 located above the front upper edge of the nozzle 12. These streams combine to form the transversely continuous powder-laden gas stream 45 which forms a dihedral angle with the oxygen stream 25 and the work surface 29. The individual branch tube 38 in connection with each channel 34 is one of a battery of such tubes leading from a distributor 46 shown in Fig. 1, which in turn is connected to a powder-laden gas supply line 47.
Originally the powder nozzle 10 itself was found to warp or buck-1e because of the extreme heat of the desurfacing reaction. The powder nozzle had to be water cooled to eliminate this warping. Accordingly, the powder nozzle cover 32 above the channels 34 is provided

Claims (2)

1. PROCESS OF DESURFACING A REFRACTORY METAL BODY, WHICH COMPRISES APPLYING PREHEAT TO A LOCAL SURFACE PORTION OF SUCH BODY, DISCHARGING A RELATIVELY FLAT STREAM OF OXIDIZING GAS AT AN ACUTE ANGLE AGAINST SUCH HEATED POR TION, PROJECTING A ROW OF STEAMS OF POWDERED SOLID FUEL LADEN GAS AT AN ACUTE ANGLE AGAINST COPLANAR SURFACES OF HARD EROSION RESISTANT CARBIDE MATERIAL, DISCHARGING THE RESULTANT SEPARATE FLAT STREAM OF GAS CONTAINING INIFORMLY TRANSVERSELY DISTRIBUTED POWDERED SOLID FUEL AT AN ACUTE ANGLE TOWARD SUCH OXIDIZING GAS STREAM, SO THAT THE CEN TRAL PLANES OF SUCH STREAMS IN THE DIRECTION OF FLOW THEREOF FROM DIHEDRAL ANGLES WITH ONE ANOTHER AND WITH SUCH SURFACE PORTION OF THE BODY, AND RELATIVELY MOVING SUCH STREMS AND THE BODY SO THAT SUCCESSIVE SURFACE PORTION THEREOF ARE PROGRESSIVELY REMOVED THERMOCHEMICALLY BY THE SCARFING ACTION OF THE COMBINED POWDERED SOLID FUEL AND OXIDIZING GAS STREAM.
3. APPARATUS FOR DESURFACING A REFRACTORY METAL BODY, WHICH COMPRISES MEANS FOR APPLYING PREHEAT TO A LOCAL SURFACE PORTION OF SUCH BODY, MEANS FOR DISCHARGING RELATIVELY FLAT STREAM OF OXIDIZING GAS AT AN ACUTE ANGLE AGAINST SUCH HEATED PORION, MEANS FOR PROJECTING A ROW OF STREAMS OF POWDERED SOLID FUEL-LADEN GAS AT AN ACUTE ANGLE AGAINST COPLANAR SURFACVES OF HARD EROSION RESISTANT CARBIDE MATERIAL, MEANS FOR DISCHARGING THE RESULTANT SEPARATED FLAT STREAM OF GAS CONTAINING UNIFORMLY TRANSVERSELY DISTRIBUTED POWDERED SOLID FUEL AT AN ACUTE ANGLE TOWARD SUCH OXIDIZING GAS STEAM, SO TAHT THE CENTRAL PLANES OF SUCH STREAMS IN THE DIRECTION OF FLOW THEREOF FORM DIHEDRAL ANGLES WITH ONE ANOTHER AND WITH SUCH SURFACE PORTION OF THE BODY, AND MEANS FOR RELATIVELY MOVING SUCH STEAMS AND THE BODY SO THAT SUCCESSIVE SURFACE PORTIONS THEREOF ARE PROGRESSIVELY REMOVED THERMOCHEMICCALLY BY THE COMBINED SCARFING ACTION OF THE POWDERED SOLID FUEL AND OXIDIZING GAS STREAM.
US506532A 1955-05-06 1955-05-06 Process and apparatus for desurfacing a refractory metal body Expired - Lifetime US2873224A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3163559A (en) * 1957-11-12 1964-12-29 Union Carbide Corp Water jet method of deslagging a metal surface
US3216867A (en) * 1963-04-29 1965-11-09 Union Carbide Corp Thermochemical scarfing process
US3230117A (en) * 1960-08-12 1966-01-18 Messer Griesheim Gmbh Process and apparatus for flame scarfing
US3477646A (en) * 1967-01-06 1969-11-11 Union Carbide Corp Scarfing unit
US3856282A (en) * 1972-10-21 1974-12-24 Messer Griesheim Gmbh Device for applying flame-scarfing powder
US4120703A (en) * 1975-08-29 1978-10-17 Union Carbide Corporation Method and apparatus for reducing smoke and preventing secondary fins during scarfing
EP0331766A1 (en) * 1988-03-05 1989-09-13 Fa. Horst K. Lotz Limiting of scarfing puddle width by means of granulation

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB583672A (en) *
US2470999A (en) * 1944-07-28 1949-05-24 Linde Air Prod Co Thermochemical metal removal
US2532103A (en) * 1947-04-17 1950-11-28 Air Reduction Method and apparatus for thermochemically scarfing billets and the like
US2622048A (en) * 1950-04-18 1952-12-16 Union Carbide & Carbon Corp External powder scarfing process and apparatus
US2664368A (en) * 1951-06-06 1953-12-29 Union Carbide & Carbon Corp External powder feed scarfing process and apparatus
US2754234A (en) * 1953-03-18 1956-07-10 Union Carbide & Carbon Corp Thermochemical metal removal

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB583672A (en) *
US2470999A (en) * 1944-07-28 1949-05-24 Linde Air Prod Co Thermochemical metal removal
US2532103A (en) * 1947-04-17 1950-11-28 Air Reduction Method and apparatus for thermochemically scarfing billets and the like
US2622048A (en) * 1950-04-18 1952-12-16 Union Carbide & Carbon Corp External powder scarfing process and apparatus
US2664368A (en) * 1951-06-06 1953-12-29 Union Carbide & Carbon Corp External powder feed scarfing process and apparatus
US2754234A (en) * 1953-03-18 1956-07-10 Union Carbide & Carbon Corp Thermochemical metal removal

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3163559A (en) * 1957-11-12 1964-12-29 Union Carbide Corp Water jet method of deslagging a metal surface
US3230117A (en) * 1960-08-12 1966-01-18 Messer Griesheim Gmbh Process and apparatus for flame scarfing
US3216867A (en) * 1963-04-29 1965-11-09 Union Carbide Corp Thermochemical scarfing process
US3477646A (en) * 1967-01-06 1969-11-11 Union Carbide Corp Scarfing unit
US3856282A (en) * 1972-10-21 1974-12-24 Messer Griesheim Gmbh Device for applying flame-scarfing powder
US4120703A (en) * 1975-08-29 1978-10-17 Union Carbide Corporation Method and apparatus for reducing smoke and preventing secondary fins during scarfing
EP0331766A1 (en) * 1988-03-05 1989-09-13 Fa. Horst K. Lotz Limiting of scarfing puddle width by means of granulation

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