US2604393A - Method of desulfurizing iron and steel with metal hydrides - Google Patents

Method of desulfurizing iron and steel with metal hydrides Download PDF

Info

Publication number
US2604393A
US2604393A US80103A US8010349A US2604393A US 2604393 A US2604393 A US 2604393A US 80103 A US80103 A US 80103A US 8010349 A US8010349 A US 8010349A US 2604393 A US2604393 A US 2604393A
Authority
US
United States
Prior art keywords
metal
sulphur
molten
slag
hydride
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US80103A
Inventor
Smalley Oliver
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US80103A priority Critical patent/US2604393A/en
Application granted granted Critical
Publication of US2604393A publication Critical patent/US2604393A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/04Removing impurities by adding a treating agent
    • C21C7/064Dephosphorising; Desulfurising
    • C21C7/0645Agents used for dephosphorising or desulfurising

Definitions

  • invention relates .to desulphurizing molten ferrous metal. It relates particularlytothe desulphurizing of molten ferrous metal when, it is desired that the sulphur content shall be: relatively low.
  • the primary object of thisinvention is the removal of sulphur, sulphur compounds and contaminating oxides from molten cast iron andsteel byeither furnace or ladle treatment or by treatment at the spout as the metal flows from the furnace.
  • Another object of thisinvention isto produce strong reducing conditions at the slag and metal interface simultaneously with reaction and removal of sulphur and sulphur compoundsby action of an alkali metal.
  • Another object of the invention is to produce strong. reducing conditions at the slag and metal interface simultaneously with reaction and removal of sulphur and sulphur compounds and contaminating oxides by introducing a hydride of an alkali metal, which hydride is adapted to dissociate into nascent hydrogen and virgin alkali metal.
  • These metallic hydrides are not merely metals holding hydrogen in the occluding state, but are true compounds possessing different physical and chemical properties than the elements from which they are produced.
  • One of their most useful properties is that they dissociate on heating into pure metal and nascent hydrogen, thus providing the maximum desulphurizing power of the metal in the presence of one of the strongest reducing agents, namely nascent hydrogen.
  • nascent hydrogen such as that evolved from a hydride, is more active chemically than hydrogen of the same purity by other means.
  • an alkali metal hydride for removing sulphur does not limit the treatment of the molten iron or steel for other purposes, such as carbide stabilization or graphitization.
  • the hydride may be introduced into the molten metal in conjunction with a material such as sodium carbonate, lithium carbonate, lime, magnesia, fluorspar, or any of the wellknown materials commonly used to increase the basicity and fluidity of the slag.
  • a further distinct advantage of this invention 7 is that less expensive iron may be produced befurnace or cupola, I prefer to draw the metal into a ladle to form a pool of metal, and cover the pool with a sulphur-carrying slag, and then introduce the hydride directly into the molten metal either in the pool or as the metal runs down the spout from the furnace. However, I. have added thehydride to the surface of a pool of molten metal at the metal and slag interface and find that satisfactory results may be :obtained in that manner. It is to be understood that the hydride may be added to the poolor mass of the molten metal whether in thefurnace or the'ladle.
  • the preferable method is to introduce the 'hydride'into the pool ofmolten'metal and allow the hydrogen-to-bubble up'through the molten metal and produce an active gas condition which helps to rapidly :circulate the molten pool and helps remove-the sulphur content at a faster rate.
  • the sulfur may be removed in the form of sulphides transferred from the molten pool into the slag-covering the molten pool, or it may be evolved as a gaseous material, or both, dependent upon the type of hydride employed and the temperature of the molten pool.
  • the treatment of molten ferrous .metalzfor the purpose 'of removing sulphur gases, sulphur compounds and contaminating oxides comprising the steps of providing a molten ferrous emtal, covering said metal with a basic slag, adding to the'molten ferrous metal at least one hydride 01; an alkali metal, said'hydride addition-being introduced in conjunction with a material, to increase the basicity and sulphur-carrying capacity of theslag.

Description

Patented July 22, 1952 METHOD OEDESULFURIZING IRON AND STEELWITHMETAL HYDRIDES Oliver Small er, Larchmont, N. Y. H No Drawing. ApplicationMarehL 1949,
7 Serial No. 80,103
2*Claim's.
invention relates .to desulphurizing molten ferrous metal. It relates particularlytothe desulphurizing of molten ferrous metal when, it is desired that the sulphur content shall be: relatively low.
The primary object of thisinvention, is the removal of sulphur, sulphur compounds and contaminating oxides from molten cast iron andsteel byeither furnace or ladle treatment or by treatment at the spout as the metal flows from the furnace. Y
Another object of thisinvention isto produce strong reducing conditions at the slag and metal interface simultaneously with reaction and removal of sulphur and sulphur compoundsby action of an alkali metal.
Another object of the invention is to produce strong. reducing conditions at the slag and metal interface simultaneously with reaction and removal of sulphur and sulphur compounds and contaminating oxides by introducing a hydride of an alkali metal, which hydride is adapted to dissociate into nascent hydrogen and virgin alkali metal. a
Desulphurization of both iron and steel by controlling or modifying the basicity of the slag by the addition of such materials as lime, fluorspar, sodium compounds andbarium carbonate is well understood, although the chemical reactions may be somewhat involved. In a general way, the disadvantages ofthese materials are their limited desulphurizing ability during the relatively short,
time-temperature interval available in actual foundry practice. That is, in actual foundry practice the temperature of the metal will remain within a suitable range for. desulphurizing for a very limited period of time, and therefore most of the common known methods of removing sulphur will not reduce the sulphur content of the metal to a sufliciently low value because the desulphurizing action is relatively slow and the temperature of the metal drops below the minimum working temperature. Furthermore, most generally known practice requires a large volume of slag to produce a reasonably low sulphur value. If a large volume of slag is not employed the slag will begin to give its sulphur content back to the molten metal and prevent reduction of the sulphur content to a satisfactory value. Where the sulphur is removed as a sulphide, conditions necessitate a stable sulphide and a high sulphurcarrying basic slag; otherwise the sulphur would readily be transferred back to the molten iron or steel.
It is commonly assumed that desulphurization results from the formation of sulphides andsulphater although it is more than probable that.
much of the sulphur may be lost in gaseous form according to the degree of action with the agent used, and the temperature and reducing conditions of melting. I have found that the best conditions for desulphurizing are hot melting under strong reducing conditions at the slag and metal interface, with an active gas condition in the molten iron or steel during the processor desulphurization. Further, strong reducing conditions will; reduce contaminating oxides, and thereby remove the influence-of the oxide and facilitatetheremoval of sulphur. Oxide reduction is therefore a part of the sulphur removal process. To do this within the limited time available presents a number of practical difiiculties, and one of the greatest, particularly in the spout and ladle, is temperature loss of the molten iron or steel itself. In the removal of sulphur, therefore, speed of action is of vital consideration, and this is true also in the furnace, for the removal of the sulphur from metal to slag is a gradual pr0cess, and too active or too much slag by volume can become a serious handicap in the melting operation. On the other hand, if a large amount of slag is not-used the process reverses, causing the metal to take sul-. phur from the slag, and this reversal can cause serious limitations.
With the foregoing factors to be considered, I have found that removal of contaminating oxides andthereafter rapid desulphurization canlb-obtained, and the sulphur content of molten. iron or steel reduced to a satisfactory low valueby introducing metallic hydrides. Metallic hydrides will break down into metal and nascent hydrogen, and I have found hydrides of alkali metals to be readily available and very satisfactory. For example, lithium hydride, sodium hydride, potassium hydride, calcium hydride, magnesium hydride and barium hydride are alkali hydrides which are highly active reaction agents for desulphurization, and other examples of metallic hydrides would include zirconium hydrides and titanium hydrides.
These metallic hydrides are not merely metals holding hydrogen in the occluding state, but are true compounds possessing different physical and chemical properties than the elements from which they are produced. One of their most useful properties is that they dissociate on heating into pure metal and nascent hydrogen, thus providing the maximum desulphurizing power of the metal in the presence of one of the strongest reducing agents, namely nascent hydrogen. It is a wellknown fact that nascent hydrogen, such as that evolved from a hydride, is more active chemically than hydrogen of the same purity by other means.
The use of an alkali metal hydride for removing sulphur does not limit the treatment of the molten iron or steel for other purposes, such as carbide stabilization or graphitization. Further, the hydride may be introduced into the molten metal in conjunction with a material such as sodium carbonate, lithium carbonate, lime, magnesia, fluorspar, or any of the wellknown materials commonly used to increase the basicity and fluidity of the slag.
In actual practice, although I have demonstrated that it is possible to desulphurize in'a by this improved method are that no expensive apparatus is required to stir the metal, and no vacuum machine is required. This invention provides a method of sulphur removal which is the essence of simplicity and is foolproof in its operation. The actual amount of the hydride necessary to produce the desired sulphur reduction is dependent upon the amount of sulphunoriginally contained by the molteniron, and the degree of purity desired in the finished product.
A further distinct advantage of this invention 7 is that less expensive iron may be produced befurnace or cupola, I prefer to draw the metal into a ladle to form a pool of metal, and cover the pool with a sulphur-carrying slag, and then introduce the hydride directly into the molten metal either in the pool or as the metal runs down the spout from the furnace. However, I. have added thehydride to the surface of a pool of molten metal at the metal and slag interface and find that satisfactory results may be :obtained in that manner. It is to be understood that the hydride may be added to the poolor mass of the molten metal whether in thefurnace or the'ladle.
-As previously stated, however, the preferable method is to introduce the 'hydride'into the pool ofmolten'metal and allow the hydrogen-to-bubble up'through the molten metal and produce an active gas condition which helps to rapidly :circulate the molten pool and helps remove-the sulphur content at a faster rate. The sulfur may be removed in the form of sulphides transferred from the molten pool into the slag-covering the molten pool, or it may be evolved as a gaseous material, or both, dependent upon the type of hydride employed and the temperature of the molten pool. I have-evolved chemical equations setting forth my theory of sulphur removal, but regardless of whether or not the chemical reactions do take place as'I believe, itis not my 'intention to limit this invention by any theory or hypothesis, but only to set forth'the fact that a hydride of analkali metal will reduce the sulphur content of molten iron'or steel if it is introduced onto the surface, or into a pool of the molten metal in a'ladle, or into the'spout as the metal is tapped from a furnace into a-ladle. 1
In' actual tests which I have made to'demonstrate the effectiveness-of hydrides'for removing sulphurfrom molten metals, I have beenable to reduce a cupola-melted cast iron having a high'sulphur content to a sulphur'content below 5009 percent, and this has been accomplished by the addition of hydrides in'quantites as low as one-half of'one per cent by weight of the metal treated. Ordinary desulphurization treatment with sodium bicarbonate-and high basic slags did not reduce the same iron to 'a value much lower than 045 per cent. V
Theobvious advantages of removing sulphur cause the original charge into the furnace may be made without particular attention to the sulphur-bearing qualities of the charged materials.
Although the invention has been described in its preferred form with a certain degree of particularity, it is understood that the present disclosure of the preferred form has been made only by way of example and that numerous changesin the details and the combination and arrangement of steps may be resorted to without departing from the spirit and the scope of the invention as hereinafter claimed.
What'is claimedis:
1. The treatment of molten ferrous metal to reduce the sulphur content thereof, comprising the stepsof providing a mass of 'molten :ferrous material, covering said mass with. basic molten slag, introducing a reagent to saidmass, said'reagent having the formula ReHz, where .R is an alkali .metal and :1: denotes the valence --relationship, and'thereafter separating the molten ferrous metal from any slag thereon.
2. The treatment of molten ferrous .metalzfor the purpose 'of removing sulphur gases, sulphur compounds and contaminating oxides, comprising the steps of providing a molten ferrous emtal, covering said metal with a basic slag, adding to the'molten ferrous metal at least one hydride 01; an alkali metal, said'hydride addition-being introduced in conjunction with a material, to increase the basicity and sulphur-carrying capacity of theslag.
' OLIVER SMALLE-Y.
' REFERENCES CITED The following references .are of record in the fileof this patent:
UNITED STATES PATENTS Applications, pages 18 and 19. Edited by :H. Osborg. Published in 1935 by the "Electro- Chemical 5 Society, New York, .N. Y.

Claims (1)

1. THE TREATMENT OF MOLTEN FERROUS METAL TO REDUCE THE SULPHUR CONTENT THEREOF, COMPRISING THE STEPS OF PROVIDING A MASS OF MOLTEN FERROUS MATERIAL, COVERING SAID MASS WITH BASIC MOLTEN SLAG, INTRODUCING A REAGENT TO SAID MASS, SAID REAGENT HAVING THE FORMULA RXHX, WHERE R IS AN ALKALI METAL AND X DENOTES THE VALENCE RELATIONSHIP, AND THEREAFTER SEPARATING THE MOLTEN FERROUS METAL FROM ANY SLAG THEREON.
US80103A 1949-03-07 1949-03-07 Method of desulfurizing iron and steel with metal hydrides Expired - Lifetime US2604393A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US80103A US2604393A (en) 1949-03-07 1949-03-07 Method of desulfurizing iron and steel with metal hydrides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US80103A US2604393A (en) 1949-03-07 1949-03-07 Method of desulfurizing iron and steel with metal hydrides

Publications (1)

Publication Number Publication Date
US2604393A true US2604393A (en) 1952-07-22

Family

ID=22155276

Family Applications (1)

Application Number Title Priority Date Filing Date
US80103A Expired - Lifetime US2604393A (en) 1949-03-07 1949-03-07 Method of desulfurizing iron and steel with metal hydrides

Country Status (1)

Country Link
US (1) US2604393A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2874038A (en) * 1955-09-19 1959-02-17 Ruhenbeck Adalbert Method of treating molten metals
US3124450A (en) * 1964-03-10 Purification of metals
US3743541A (en) * 1967-02-17 1973-07-03 Scholemann Ag Reduction of solid, liquid or gaseous oxide-containing compounds
US3981753A (en) * 1968-04-30 1976-09-21 Kennecott Copper Corporation Stop-weld composition and the method of using it
US4078915A (en) * 1972-10-27 1978-03-14 Suddeutsche Kalkstickstoff-Werke Aktiengesellschaft Method and composition for the desulfurization of molten metals

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1515794A (en) * 1924-11-18 And samuel peacock
US1869496A (en) * 1930-09-06 1932-08-02 Osborg Hans Art of treating metals
US1869980A (en) * 1931-06-26 1932-08-02 Osborg Hans Process of treating molten metals and alloys with compositions containing lithium and products resulting from such treatment
US1869979A (en) * 1930-09-06 1932-08-02 Osborg Hans Art of treating metals
US1931144A (en) * 1930-10-10 1933-10-17 Du Pont Treatment of metals
US2110066A (en) * 1935-05-09 1938-03-01 Heuer Russell Pearce Iron and steel desulphurization

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1515794A (en) * 1924-11-18 And samuel peacock
US1869496A (en) * 1930-09-06 1932-08-02 Osborg Hans Art of treating metals
US1869979A (en) * 1930-09-06 1932-08-02 Osborg Hans Art of treating metals
US1931144A (en) * 1930-10-10 1933-10-17 Du Pont Treatment of metals
US1869980A (en) * 1931-06-26 1932-08-02 Osborg Hans Process of treating molten metals and alloys with compositions containing lithium and products resulting from such treatment
US2110066A (en) * 1935-05-09 1938-03-01 Heuer Russell Pearce Iron and steel desulphurization

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3124450A (en) * 1964-03-10 Purification of metals
US2874038A (en) * 1955-09-19 1959-02-17 Ruhenbeck Adalbert Method of treating molten metals
US3743541A (en) * 1967-02-17 1973-07-03 Scholemann Ag Reduction of solid, liquid or gaseous oxide-containing compounds
US3981753A (en) * 1968-04-30 1976-09-21 Kennecott Copper Corporation Stop-weld composition and the method of using it
US4078915A (en) * 1972-10-27 1978-03-14 Suddeutsche Kalkstickstoff-Werke Aktiengesellschaft Method and composition for the desulfurization of molten metals

Similar Documents

Publication Publication Date Title
US2915386A (en) Device for supplying treating agents sequentially to molten metal
US1335370A (en) Desulfurizing cast-iron
US2604393A (en) Method of desulfurizing iron and steel with metal hydrides
US2848317A (en) Desulfurizing of steel
US4054445A (en) Deoxidizing and desulphurizing steel
CN108300836B (en) Composite deoxidizer
US2819956A (en) Addition agent for and method of treating steel
US3421887A (en) Process for producing a magnesium-containing spherical graphite cast iron having little dross present
US4154606A (en) Composition and method for the desulfurization of molten iron
US2587573A (en) Desulfurizing process
JP2014101542A (en) Processing method of copper removal from molten pig iron
US1963269A (en) Method of desulphurizing and purifying iron
US1983604A (en) Production of refined metal
US3954446A (en) Method of producing high duty cast iron
US3892561A (en) Composition for treating steels
US2049081A (en) Alloys
US1994679A (en) Process of producing alloys
US4042377A (en) Method of and composition for the desulfurization of steel
US2079848A (en) Making steel
US2730442A (en) Method of dephosphorizing and refining thomas and bessemer steels
US1920465A (en) Refining ferrous metals
US2462871A (en) Treating agent
EP0143276B1 (en) Process to control the shape of inclusions in steels
JPS6241308B2 (en)
JPS6123243B2 (en)