Method of coating carbon steel

Claim 3

The method claimed in claim 1, wherein the atmosphere in said furnace heated by direct combustion of fuel and air contains 0% oxygen and 0% excess combustibles..].

Claim 4

The method claimed in claim 2, wherein the strip temperature exiting said furnace heated by direct combustion of fuel and air ranges from about 595° to about 650° C.

Claim 5

The method claimed in claim 1, wherein the strip temperature exiting said subsequent furnace ranges from about 675° to about 900° C.

Claim 6

The method claimed in claim 1, wherein the atmosphere of said subsequent furnace contains at least about 15% hydrogen.

Claim 7

In a method of fluxless hot dip metallic coating of carbon steel strip and sheet wherein the strip and sheet surface is prepared for coating by a preliminary treatment involving heating in a furnace heated by direct combustion of fuel and air therein and in an atmosphere containing gaseous products of combustion, followed by further treatment under conditions reducing to iron oxide, the improvement which comprises .[.conducting said heating in an atmosphere containing from about 3% oxygen by volume to about 2% hydrogen plus carbon monoxide by volume.]. .Iadd.operating said furnace at fuel air ratios ranging from stoichiometrically equivalent to about 3% by volume oxygen, .Iaddend.at a temperature above the temperature at which said strip and sheet is oxidized and within the range of about 540° to about 705° C, whereby to produce an iron oxide film of controlled thickness, and conducting said further treatment in a subsequent furnace containing at least about .Badd..[.5%.]..Baddend. .Iadd.15% .Iaddend.hydrogen by volume at a temperature sufficient to reduce any oxide present on the strip and sheet as it exits said direct fired furnace. .[.

Claim 8

In a method of fluxless hot dip metallic coating of carbon steel strip and sheet wherein the strip and sheet surface is prepared for coating by a preliminary treatment involving heating in a furnace heated by direct combustion of fuel and air therein and in an atmosphere containing gaseous products of combustion, followed by further treatment under conditions reducing to iron oxide, the improvement which comprises .[.conducting said heating in an atmosphere containing from about 3% oxygen by volume to about 2% hydrogen plus carbon monoxide by volume.]. .Iadd.operating said furnace at fuel air ratios ranging from stoichiometrically equivalent to about 3% by volume oxygen, .Iaddend.at a temperature above the temperature at which said strip and sheet is oxidized and within the range of about 540° to about 705° C, whereby to produce an iron oxide film of controlled thickness, and conducting said further treatment in a subsequent furnace containing at least about .Badd..[.5%.]..Baddend. .Iadd.15% .Iaddend.hydrogen by volume at a temperature sufficient to reduce any oxide present on the strip and sheet as it exits said direct fired furnace. .[.

Claim 9

The improvement claimed in claim 6, wherein said atmosphere in said furnace heated by direct combustion of fuel and air contains 0% oxygen and 0% hydrogen plus carbon monoxide..]. .[.8. The improvement claimed in claim 6, wherein the strip and sheet is heated in said furnace heated by direct combustion of fuel and air to a temperature of about 540° to about 705° C..]. .[.9. The improvement claimed in claim 6, wherein the atmosphere in said subsequent furnace contains at least about 15%

Claim 10

hydrogen and balance substantially nitrogen..]. 10. The improvement claimed in claim 6, wherein the strip is heated in said subsequent furnace

Claim 11

to a temperature of about 675° to about 900° C. 11. The improvement claimed in claim 6, wherein the coating metal is chosen from the class consisting of zinc, zinc alloys, aluminum, aluminum alloys and terne.