Method of improvement of the heat-balance in the refining of steel

Claim 1

A method of producing steel in a convertor comprising: (1) introducing oxygen shrouded by a protective medium into the convertor by means of tuyeres located in the lining of the convertor below the surface of a bath in said convertor; and (2) concurrently therewith blowing oxygen onto the surface of the bath; the improvement of that method comprising that for at least a major part of the refining time, 20 to 80% of the oxygen is introduced into said convertor by gas jets directed onto the surface of the bath which act as free jets in the space above the surface of the bath, said jets having a sufficient velocity to suck in large amounts of reaction products of the bath, and that the remaining amount of oxygen is concurrently blown into said bath by means of said tuyeres, whereby the heat balance in said method is improved and the proportion of scrap charged into said convertor for melting is increased.

Claim 2

A method of producing steel in a convertor comprising: (1) introducing oxygen shrouded by a protective medium into the convertor by means of tuyeres located in the lining of the convertor below the surface of a bath in said convertor; and (2) concurrently therewith blowing oxygen onto the surface of the bath; the improvement of that method comprising that for at least a major part of the refining time, 20 to 80% of the oxygen is introduced into said convertor by gas jets directed onto the surface of the bath which act as free jets in the space above the surface of the bath, said jets having a sufficient velocity to suck in large amounts of reaction products of the bath, and that the remaining amount of oxygen is concurrently blown into said bath by means of said tuyeres, whereby the heat balance in said method is improved and the proportion of scrap charged into said convertor for melting is increased.

Claim 5

A method as in any of the preceding claims 1 to 3, characterized in that the distance between the outlet openings of the oxygen jets and the static surface of the bath corresponds with 50 to 200 times the diameter of the oxygen outlet openings.

Claim 6

A method as in any of the preceding claims 1 to 4, characterized in that the oxygen feed onto the surface of the bath is effected by nozzles which are built into the converter brickwork and are protected against premature burning away by a shrouding of hydrocarbon.

Claim 7

A method as in any of the preceding claims 1 to 5, characterized in that the quantity of hydrocarbon for the top-blowing oxygen nozzles amounts to about 0.5 to 5% by wt. referred to the oxygen.

Claim 8

A method as in any of the preceding claims 1 to 6, characterized in that the proportionate amounts of the media blown onto and through the bath are regulated independently of one another.

Claim 9

A method as in any of the preceding claims 1 to 7, characterized in that the significant proportion of the slag-formers, in particular lime, is charged into the oxygen which flows through the nozzles underneath the surface of the bath.

Claim 10

A method as in any of the preceding claims 1 to 8, characterized in that carbon-containing fuels are fed to the iron melt in the converter.

Claim 11

A method as in any of the preceding claims 1 to 9, characterized in that as carbon-containing fuels coal of various qualities, graphite, carbonized lignite, coke and in particular coke dust as well as mixtures of them are used.

Claim 12

A method as in any of the preceding claims 1 to 10, characterized in that the carbon-containing fuels are introduced into the melt in powder form and dry underneath the surface of the bath.

Claim 13

A method as in any of the preceding claims 1 to 11, characterized in that the solid iron-carriers charged into the converter, such as scrap, solid pig iron, pellets or sponge iron, are preheated.