US3205067A - Removal of deleterious gases from molten metal - Google Patents
Removal of deleterious gases from molten metal Download PDFInfo
- Publication number
- US3205067A US3205067A US264767A US26476763A US3205067A US 3205067 A US3205067 A US 3205067A US 264767 A US264767 A US 264767A US 26476763 A US26476763 A US 26476763A US 3205067 A US3205067 A US 3205067A
- Authority
- US
- United States
- Prior art keywords
- metal
- molten metal
- removal
- gas
- hydrogen
- 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
Links
- 229910052751 metal Inorganic materials 0.000 title description 25
- 239000002184 metal Substances 0.000 title description 25
- 239000007789 gas Substances 0.000 title description 14
- 230000002939 deleterious effect Effects 0.000 title description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 16
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical class [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 229910000831 Steel Inorganic materials 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 239000010959 steel Substances 0.000 claims description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 238000005266 casting Methods 0.000 description 5
- 239000002893 slag Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 239000006028 limestone Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- -1 ferrous metals Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 125000005587 carbonate group Chemical group 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/072—Treatment with gases
Definitions
- Methods which have so far been employed for reducing excessive amounts of hydrogen in metal include bubbling an inert or relatively inert gas through the molten metal, or blowing the surface of the metal with such a gas.
- gases used in these methods are argon, helium, nitrogen, carbon monoxide and carbon dioxide, selection from this range depending on the type of metal treated.
- Alternative methods for reducing excessive hydrogen content are vacuum casting and prolonged heat treatment of the solidified metal. All these methods have the disadvantage of requiring special apparatus, which in the case of vacuum casting and of heat treatment, is particularly costly. In the case of treatment with inert gases, the main disadvantages are the additional time required during which the metal must be maintained in the molten state, the consequent loss of temperature, and the splashing which may result from the treatment.
- a further method which has been employed, particularly with ferrous metals, is the use of a solid compound which, when placed on, or plunged below, the metal surface, decomposes to produce a gas which is substantially insoluble in the metal but into which the hydrogen can diffuse and thus be removed.
- a solid compound which, when placed on, or plunged below, the metal surface, decomposes to produce a gas which is substantially insoluble in the metal but into which the hydrogen can diffuse and thus be removed.
- the type .of material used for this purpose in the steel industry is a carbonate, such as limestone, which on heating decomposes to give carbon dioxide gas and an oxide, such as calcium oxide (lime).
- slag particularly lime based slags, should be absent, and it is a disadvantage of the method just described that a solid material such as lime is a product of the reaction.
- a process for reducing the hydrogen content of molten steel comprises introducin g to the molten metal surface an inert or relatively inert gas in the liquefied state. It has been found by analysis that when gas is added in this form, a substantial amount of hydrogen is removed; this is accomplished without excessive loss of heat and without the production of a slag. This is true even though the temperature of the gases in these states are very low, e.g. liquid nitrogen, l98 C. and liquid argon, 184 C.
- the liquefied gas may be added to the molten metal in any convenient manner which insures that the bulk of the material reaches the surface in the liquid state.
- a feature of the process is that, on the liquefied gas reaching the surface, the instantaneous change from the liquid state provides a blanket of gas through which the transfer of heat is sufiiciently retarded to enable the liquefied gas to move to other areas and eventually provide a thorough scavenging of the metal surface.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Description
United States Patent 3,205,067 REMOVAL OF DELETERIOUS GASES FROM MOLTEN METAL Charles Henry King, London, England, assignor to The British Oxygen Company Limited, a British company No Drawing. Filed Mar. 13, 1963, Ser. No. 264,767 Claims priority, application Great Britain, Mar. 22, 1962, 11,095/ 62 2 Claims. (CI. 75-59) In the manufacture of steel, it sometimes happens that trouble is experienced in the finished products due to the presence of excessive amounts of hydrogen gas which has become dissolved in the metal during the melting operation. When hydrogen is present in amounts above the safe limit, porosity occurs in the ingots :or castings, and in the case of the former, flaking, hair line cracks and other forms of unsoundness may develop in subsequent processing even though the porosity was not obvious in the ingot form. Porosity also arises from this cause in the preparation of ingots or castings made from non-ferrous metals, and in iron castings.
Methods which have so far been employed for reducing excessive amounts of hydrogen in metal include bubbling an inert or relatively inert gas through the molten metal, or blowing the surface of the metal with such a gas. Examples of gases used in these methods are argon, helium, nitrogen, carbon monoxide and carbon dioxide, selection from this range depending on the type of metal treated. Alternative methods for reducing excessive hydrogen content are vacuum casting and prolonged heat treatment of the solidified metal. All these methods have the disadvantage of requiring special apparatus, which in the case of vacuum casting and of heat treatment, is particularly costly. In the case of treatment with inert gases, the main disadvantages are the additional time required during which the metal must be maintained in the molten state, the consequent loss of temperature, and the splashing which may result from the treatment.
A further method which has been employed, particularly with ferrous metals, is the use of a solid compound which, when placed on, or plunged below, the metal surface, decomposes to produce a gas which is substantially insoluble in the metal but into which the hydrogen can diffuse and thus be removed. Normally the type .of material used for this purpose in the steel industry is a carbonate, such as limestone, which on heating decomposes to give carbon dioxide gas and an oxide, such as calcium oxide (lime). In steel degassing operations it is desirable that slag, particularly lime based slags, should be absent, and it is a disadvantage of the method just described that a solid material such as lime is a product of the reaction. When limestone is added to the surface, a layer of lime or slag forms in the vicinity of the added limestone ice creating a barrier between the metal surface and the carbon dioxide gas, thereby reducing the efficiency of trans fer of hydrogen into the gas. Also there are operational disadvantages associated with plunging solids below the surface of molten metal.
According to the present invention a process for reducing the hydrogen content of molten steel comprises introducin g to the molten metal surface an inert or relatively inert gas in the liquefied state. It has been found by analysis that when gas is added in this form, a substantial amount of hydrogen is removed; this is accomplished without excessive loss of heat and without the production of a slag. This is true even though the temperature of the gases in these states are very low, e.g. liquid nitrogen, l98 C. and liquid argon, 184 C.
The liquefied gas may be added to the molten metal in any convenient manner which insures that the bulk of the material reaches the surface in the liquid state.
A feature of the process is that, on the liquefied gas reaching the surface, the instantaneous change from the liquid state provides a blanket of gas through which the transfer of heat is sufiiciently retarded to enable the liquefied gas to move to other areas and eventually provide a thorough scavenging of the metal surface.
The invention is illustrated by the following experiment:
100 lbs. of scrap was melted in an electric furnace, under conditions conducive to obtaining a molten metal with a high hydrogen content. The bulk of the slag was removed from the metal surface, and a sample of the molten metal removed for analysis. About 1 /2 lbs. of liquid nitrogen was carefully added to the molten metal, and, after two minutes, a further sample of metal was taken for analysis. During this time the furnace currrent was passing, no ill effects being observed. It was found that the first sample taken contained 3.8 cc. of hydrogen per 100 grams of metal, and the second sample contained 1.7 cc. of hydrogen per 100 grams of metal, indicating a substantial degree .of degassing.
I claim:
1. In the process for reducing the hydrogen content of molten steel by the action of nitrogen thereon, the step of introducing the nitrogen in its liquid state to the surface of the molten steel.
2. The process as claimed in claim 1, wherein the proportion of liquid nitrogen to molten steel is of the order of one and a half percent by weight.
References Cited by the Examiner UNITED STATES PATENTS 2,068,785 1/37 Bain et al -59 2,395,458 2/46 Cape 7559 3,042,484 7/62 Mating 75 59 BENJAMIN HENKIN, Primary Examiner.
Claims (1)
1. IN THE PROCESS FOR REDUCING THE HYDROGEN CONTENT OF MOLTEN STEEL BY THE ACTION OF NITROGEN THEREON, THE STEP OF INTRODUCING THE NITROGEN IN ITS LIQUID STATE TO THE SURFACE OF THE MOLTEN STEEL.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB11095/62A GB971270A (en) | 1962-03-22 | 1962-03-22 | Removal of hydrogen from molten metal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3205067A true US3205067A (en) | 1965-09-07 |
Family
ID=9979942
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US264767A Expired - Lifetime US3205067A (en) | 1962-03-22 | 1963-03-13 | Removal of deleterious gases from molten metal |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3205067A (en) |
| GB (1) | GB971270A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3506436A (en) * | 1966-11-25 | 1970-04-14 | Kaiser Ind Corp | Environmental control process for gaseously removing carbon from liquid metals |
| US4154602A (en) * | 1977-01-31 | 1979-05-15 | Kawasaki Steel Corporation | Method of denitriding a high chromium molten steel with a minimum chromium loss |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2068785A (en) * | 1933-11-20 | 1937-01-26 | United States Steel Corp | Method of manufacturing low carbon steel |
| US2395458A (en) * | 1945-02-28 | 1946-02-26 | Coast Metals Inc | Method of treating molten metals |
| US3042484A (en) * | 1960-03-23 | 1962-07-03 | Maring Walter Dale | Composition and a method for treating molten metals |
-
1962
- 1962-03-22 GB GB11095/62A patent/GB971270A/en not_active Expired
-
1963
- 1963-03-13 US US264767A patent/US3205067A/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2068785A (en) * | 1933-11-20 | 1937-01-26 | United States Steel Corp | Method of manufacturing low carbon steel |
| US2395458A (en) * | 1945-02-28 | 1946-02-26 | Coast Metals Inc | Method of treating molten metals |
| US3042484A (en) * | 1960-03-23 | 1962-07-03 | Maring Walter Dale | Composition and a method for treating molten metals |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3506436A (en) * | 1966-11-25 | 1970-04-14 | Kaiser Ind Corp | Environmental control process for gaseously removing carbon from liquid metals |
| US4154602A (en) * | 1977-01-31 | 1979-05-15 | Kawasaki Steel Corporation | Method of denitriding a high chromium molten steel with a minimum chromium loss |
Also Published As
| Publication number | Publication date |
|---|---|
| GB971270A (en) | 1964-09-30 |
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