US3288592A - Process for reducing deterioration in equipment handling molten materials - Google Patents
Process for reducing deterioration in equipment handling molten materials Download PDFInfo
- Publication number
- US3288592A US3288592A US323087A US32308763A US3288592A US 3288592 A US3288592 A US 3288592A US 323087 A US323087 A US 323087A US 32308763 A US32308763 A US 32308763A US 3288592 A US3288592 A US 3288592A
- Authority
- US
- United States
- Prior art keywords
- slag
- refractory
- mgo
- magnesia
- approximately
- 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
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- 238000000034 method Methods 0.000 title claims description 24
- 230000006866 deterioration Effects 0.000 title description 22
- 230000008569 process Effects 0.000 title description 10
- 239000012768 molten material Substances 0.000 title description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 289
- 239000000395 magnesium oxide Substances 0.000 claims description 142
- 239000002893 slag Substances 0.000 claims description 120
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 79
- 239000000292 calcium oxide Substances 0.000 claims description 54
- 235000012255 calcium oxide Nutrition 0.000 claims description 54
- 239000000203 mixture Substances 0.000 claims description 21
- 239000002253 acid Substances 0.000 claims description 18
- 239000004615 ingredient Substances 0.000 claims description 16
- 238000007670 refining Methods 0.000 claims description 10
- 239000010459 dolomite Substances 0.000 claims description 8
- 229910000514 dolomite Inorganic materials 0.000 claims description 8
- 230000001590 oxidative effect Effects 0.000 claims description 6
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 claims description 4
- 230000000670 limiting effect Effects 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 claims 1
- 235000012245 magnesium oxide Nutrition 0.000 description 140
- 239000000463 material Substances 0.000 description 43
- 239000011230 binding agent Substances 0.000 description 39
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 28
- 229910052751 metal Inorganic materials 0.000 description 23
- 239000002184 metal Substances 0.000 description 23
- YLUIKWVQCKSMCF-UHFFFAOYSA-N calcium;magnesium;oxygen(2-) Chemical compound [O-2].[O-2].[Mg+2].[Ca+2] YLUIKWVQCKSMCF-UHFFFAOYSA-N 0.000 description 21
- 239000011819 refractory material Substances 0.000 description 18
- 239000000377 silicon dioxide Substances 0.000 description 15
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 11
- 235000011941 Tilia x europaea Nutrition 0.000 description 11
- 239000004571 lime Substances 0.000 description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910000287 alkaline earth metal oxide Inorganic materials 0.000 description 9
- 239000000919 ceramic Substances 0.000 description 9
- 239000010410 layer Substances 0.000 description 9
- 239000002245 particle Substances 0.000 description 9
- 238000009628 steelmaking Methods 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000011822 basic refractory Substances 0.000 description 8
- 239000000470 constituent Substances 0.000 description 8
- 238000004458 analytical method Methods 0.000 description 7
- 239000011449 brick Substances 0.000 description 7
- 230000009467 reduction Effects 0.000 description 7
- 229910052566 spinel group Inorganic materials 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 238000002844 melting Methods 0.000 description 6
- 230000008018 melting Effects 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 5
- 239000001095 magnesium carbonate Substances 0.000 description 5
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000002829 reductive effect Effects 0.000 description 5
- 150000004760 silicates Chemical class 0.000 description 5
- 229910052710 silicon Inorganic materials 0.000 description 5
- 239000010703 silicon Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000007792 addition Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 229910052839 forsterite Inorganic materials 0.000 description 4
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 4
- 238000010310 metallurgical process Methods 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 150000004673 fluoride salts Chemical class 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 238000011065 in-situ storage Methods 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 238000004364 calculation method Methods 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 230000005012 migration Effects 0.000 description 2
- 238000013508 migration Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 229910052596 spinel Inorganic materials 0.000 description 2
- 239000011029 spinel Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910019440 Mg(OH) Inorganic materials 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- -1 and accordingly Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229940043430 calcium compound Drugs 0.000 description 1
- 150000001674 calcium compounds Chemical class 0.000 description 1
- VAWSWDPVUFTPQO-UHFFFAOYSA-N calcium strontium Chemical compound [Ca].[Sr] VAWSWDPVUFTPQO-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010436 fluorite Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000004677 hydrates Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000011295 pitch Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/622—Forming processes; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/626—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B
- C04B35/63—Preparing or treating the powders individually or as batches ; preparing or treating macroscopic reinforcing agents for ceramic products, e.g. fibres; mechanical aspects section B using additives specially adapted for forming the products, e.g.. binder binders
- C04B35/6303—Inorganic additives
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/01—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics
- C04B35/03—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on magnesium oxide, calcium oxide or oxide mixtures derived from dolomite
- C04B35/04—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products based on oxide ceramics based on magnesium oxide, calcium oxide or oxide mixtures derived from dolomite based on magnesium oxide
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B35/00—Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
- C04B35/66—Monolithic refractories or refractory mortars, including those whether or not containing clay
-
- 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
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/42—Constructional features of converters
- C21C5/44—Refractory linings
-
- 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
- C21C7/0087—Treatment of slags covering the steel bath, e.g. for separating slag from the molten metal
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00482—Coating or impregnation materials
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/0087—Uses not provided for elsewhere in C04B2111/00 for metallurgical applications
- C04B2111/00887—Ferrous metallurgy
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/32—Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3205—Alkaline earth oxides or oxide forming salts thereof, e.g. beryllium oxide
- C04B2235/3206—Magnesium oxides or oxide-forming salts thereof
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/32—Metal oxides, mixed metal oxides, or oxide-forming salts thereof, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3205—Alkaline earth oxides or oxide forming salts thereof, e.g. beryllium oxide
- C04B2235/3208—Calcium oxide or oxide-forming salts thereof, e.g. lime
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/02—Composition of constituents of the starting material or of secondary phases of the final product
- C04B2235/30—Constituents and secondary phases not being of a fibrous nature
- C04B2235/34—Non-metal oxides, non-metal mixed oxides, or salts thereof that form the non-metal oxides upon heating, e.g. carbonates, nitrates, (oxy)hydroxides, chlorides
- C04B2235/3418—Silicon oxide, silicic acids or oxide forming salts thereof, e.g. silica sol, fused silica, silica fume, cristobalite, quartz or flint
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2235/00—Aspects relating to ceramic starting mixtures or sintered ceramic products
- C04B2235/70—Aspects relating to sintered or melt-casted ceramic products
- C04B2235/96—Properties of ceramic products, e.g. mechanical properties such as strength, toughness, wear resistance
- C04B2235/9669—Resistance against chemicals, e.g. against molten glass or molten salts
- C04B2235/9676—Resistance against chemicals, e.g. against molten glass or molten salts against molten metals such as steel or aluminium
Definitions
- the present invention has particular utility in metallurgical processes which utilize vessels lined with basic refract-ories that are in contact with molten slags which contain calcia, and has greatest application in steel producing processes which utilize slag-s containing calcia as well as silica and/or alumina, and magnesia refractories.
- the metallurgical equipment which is utilized in the refining and handling of molten steels is generally constructed by means of steel shells that are lined with a refractory which in turn contains the molten metal. Slags of molten metal oxides and/ or other compounds are usually used in these processes to cover the molten metals, and to aid in the purification of the molten metal.
- the slaps which are used in the various metallurgical processes are of two groups: one group is basic in character and is known as basic type slag, and the other group is acidic in character and is known as acid type slag.
- Silica, alumina, and phosphates cause slags and refractories to be acid in character; while CaO and MgO are the principal ingredients which cause refractories and slags to be basic in character.
- acid refractories are used to line metallurgical equipment, it is necessary that the slags be acid in character; and where basic refractories are used to line metallurgical equipment, it is necessary that the slags be basic in character.
- Basic type slags in which the basic material is principally calcia
- calcia type slags are known as calcia type slags, and have particular advantages in the manufacture of steel, inasmuch as they have high heat conductivity and remove sulfur and phosphorous from the molten metal, and accordingly, calcia type slags have wide spread use in steel making processes.
- Various steel making equipment may be operated with calcia type slags, as for example, open hearth furnaces, Bessemer converters, electric furnaces, and basic oxygen furnaces, e.g. those in which the processes disclosed in Blast Furnace and Steel Plant, July 1961, pages 621-632, and cited references, and in Ceramic Bulletin 39, N0.
- magnesia refractory is the preferred material for lining the equipment.
- steel making processes refers to all of the foregoing processes.
- the molal ratio of the basic ingredients of the slag to the acid ingredients of the slag be greater than 1.5 :1 e.g. at least about 1.6: 1; the ratio should preferably be between 2.0:1 and 4.5 :1; and most desirably between 2.5 :1 and 3.5 :1.
- Magnesia refractories are obtained by burning magnesium oxide containing materials-for example, magnesium carbonate ores containing some impurities, or the magnesium hydroxide that is precipitated from solutions,
- magnesia refractories means refractories such as brick and rammed or monolithic linings containing substantial proportions of magnesia, frequently from about 35 percent by weight to virtually 100 percent.
- the carbon dioxide or water is driven off leaving magnesium oxide with minor amounts of impurities.
- Magnesium oxide can exist in either of two states which differ in structure and properties.
- the alpha or amorphous state of MgO is first achieved.
- Amorphous magnesia is quite reactive; it hydrates readily and is an active fiuxing agent for metals.
- the MgO changes over to its beta phase which is crystalline in character and highly thermal resistant. This beta phase is commonly called periclase.
- the melting point of periclase varies depending upon the impurities contained or associated therewith, and can be as high as 2800 C. The transition of magnesia from its alpha to its beta phase may be quite slow.
- the burning of magnesium carbonate to periclase crystals is promoted by the molten glassy materials that are generally formed by the impurities found in the magnesium carbonate ores. These impurities generally include SiO A1 0 Fe O and C210; and refractory manufactures may add small amounts of some of these materials to provide a molten flux which speeds up and catalyzes the substantially complete conversion of the alpha phase MgO into the periclase form.
- the periclase crystals that are formed during burning of magnesium carbonateor hydroxide-containing raw materials are quite small and must be held together by a binder in order to form refractory shapes.
- CaO, MgO, tar or pitch, and minor amounts of other materials added to or present in the raw materials before burning form this binder.
- the amount of binder forming materials used generally comprises between about 6% and about 20% of the refractory, and these materials melt at the burning temperature to form a glassy phase around the periclase particles, or form a carbon binder.
- the other binder forming materials used may vary, but generally include CaO, MgO, Fe O Cr O A1 0 and SiO so as to form forsterite and spinals or other glassy materials, frequently in combination with tar or pitch.
- the MgCo ores or precipitates are burned they are crushed and mixed with various additional binder materials, which may be temporary or permanent in nature, to hold the refractory grains in place.
- the additional binder materials may be more of the glassy phase materials, or they may be an asphaltic tar.
- the tar acts as a temporary binder, and is ultimately converted to a carbon binder.
- the crushed burned material is mixed with approximately 5% of asphalt and is pressed into the form of bricks at up to 100,000 pounds per square inch.
- the asphaltic material acts as a temporary binder which holds the brick together until it is used.
- tar or vasphaltic material is decomposed to carbon and the glassy phase-forming binder materials which 'were incorporated during burning unite and cooperate with the carbon to form a binder network or hinder networks. Since the particles of periclase generally key each other together and do not move provided they are not subjected to undue load prior to burning in, refractory materials so formed can be used at temperatures above the softening or melting point of the glassy phase bond material.
- Metallurgical equipment that is lined with refractories including those enumerated above which are lined with magnesia brick, must either be taken out of operation periodically for lining replacement, or other provision must be made for lining maintenance.
- the deterioration of the magnesia refractory in steel making equipment is appreciable; and basic oxygen furnaces, for example, must currently be taken out of service frequently in order to have their working linings renewed.
- the actual cost of the lining, and the labor for installing it, is appreciable, as is the lost production during the relining operation; so that a sizable percentage of the cost of steel can be attributed to the direct and indirect costs of replacing the working lining of the metallurgical equipment used in its manufacture. It has been determined that approximately 15 pounds of refractory are consumed for every ton of steel that is produced in basic oxygen furnaces.
- an object of the present invention is the provision of new and improved means for reducing the deterioration of magnesia refractory materials used in steel making processes.
- a more particular object is the provision of new and improved means for reducing the deterioration of magnesia refractories that are in contact with molten calcia type slags.
- Another object of the present invention is the provision of new and improved slag forming materials for steel making processes of the basic type which greatly reduce the deterioration of the refractory used in the equipment involved, expedite operation by rapid formation of proper slag, or both.
- Still another object of the present invention is the provision of new and improved binder materials for refractories which are used with specific slags, as, for example, the binder of the magnesia refractory for use with calcia type slags.
- a further object of the present invention is the provision of a new and improved slag-making material which fluxes more rapidly than do presently used materials.
- the present invention is based upon a realization that, at the elevated operating temperatures of steel making equipment, molten slags contained in the equipment form a liquid-solid ceramic system with the binders and the refractory of the ceramic linings of the equipment, and approach equilibrium with respect to each other by the migration of elements from one to the other.
- the binder and the slag that are used together may be tailored to one another, so that the main constituents of each match closely, and no great change in either is necessary for the two to reach equilibrium.
- the driving force tending to cause the major constituents of the binder to go into solution in the slag is reduced; there is reduced dissolution in the slag; and the life of the refractory is increased.
- alkaline earth metals as used herein includes all the metals of Group IIa of the periodic table having an atomic number from 12 through 56, i.e., magnesium, calcium strontium and barium, more particularly calcium and magnesium, and the term alkaline earths is used as meaning the oxides of these alkaline earth metals.
- the binder materials which hold the periclase particles in place in the refractory are of the same general nature as is the slag that is in contact therewith at the elevated operating conditions.
- the molten slag and the refractory binder make up a liquid-solid ceramic system which tends to reach an equilibrium state at the operating temperature of the equipment.
- the migration of the binder materials to the slag and vice versa loosens the periclase particles in the brick to speed up the deterioration of the surface of the brickwork.
- the ceramic binder materials that are formed during the making of present day magnesia refractory are either composed principally of spinels and silicates of magnesia, or include spinels and silicates of magnesia.
- One of the silicates which is commonly formed is forsterite (2MgO.SiO although aluminum silicate may also be formed.
- the spinels which are usually formed are MgO.Al O MgO.Fe O and MgO.Cr O or mixtures thereof.
- the overall composition of the ceramic binders of the refractory will, of course, be mixtures of the above spinels and silicates, and may include still others not mentioned, forming a highly complex mixture.
- the ceramic binders that are usually formed and used contain MgO.
- the MgO that remains in the binder after firing is readily available to be fluxed out by slag as will later be described.
- the MgO constituent of the spinels and silicates is believed to be fairly reactive so that it is also fluxed to some extent by the slags.
- all commercial magnesia refractories include some form of MgO which goes into solution with calcia iron-silica slags.
- magnesia concentration in a calcia type slag should be between approximately 4% and approximately 12% by weight.
- the speed with which the silica is neutralized is a function of the surface area of the alkaline earth metal oxides. While deterioration of magnesia refractory is reduced by the addition of any form of active magnesia, as above stated, a further decrease in deterioration of the magnesia refractory is achieved by the use of highly active pebble or finely divided alkaline earth metal oxides having a surface area greater than approximately 3.5 square meters per gram as determined by nitrogen absorption techniques.
- a decrease in deterioration of any basic refractory can be achieved by the use of any highly active pebble or finely divided alkaline earth metal oxide having a surface area greater than approximately 3.5 square meters per gram as determined by nitrogen absorption techniques, if it is used in suflicient quantities to react with the silica formed in situ to form a slag wherein the base to acid molal ratio is greater than 1:1 and thereby prevent the silica from contacting the refractory.
- a reduction in lining deterioration can be achieved by using highly active calcia having a surface area greater than approximately 3.5 square meters per gram as determined by nitrogen absorption techniques instead of the conventionally used calcia, and the very best results can be achieved by using both the alpha magnesia and the calcia in the highly active form above described.
- the activity of calcia and magnesia varies with the calcining methods that are used in production, and the calcia and alpha magnesia in the metallurgical grade of dolomitic lime produced by the Gibsonburg Lime Products Company, of Gibsonburg, Ohio, give excellent results.
- the MgO in the slag gradually converts to the periclase form, which settles out in lower temperature portions of the slag as small solid crystals which mechanically thicken the slag.
- the layer of slag adjacent the refractory is more viscous and tends to be retained on the surface of the refractory.
- the conversion of MgO to periclase is a time rate function and the viscous layer adjacent the refractory of the furnace tends to be retained in the furnace when the main body of slag is dumped.
- the present invention makes still other advantages possible. It is preferred to charge calcined dolomite, not only because it is low in cost, but also because the MgO is combined with approximately an equal molal percentage of CaO. Approximately equal percentages of C210 and MgO form, at a comparatively low temperature, melts having a high degree of fluidity. While it has been thought that the addition of MgO to a CaO type slag would lower the fluidity of the slag, it has been found that the addition of calcined dolomite causes the opposite effect and, in fact, makes it possible to eliminate the fluoride salts normally used in slag charges to induce fluidity.
- Fluoride salts are known to be detrimental to refractories; and in slag-charging compositions according to the invention, it is preferred either to eliminate the fluoride salts, or to keep their concentrations to a very low value, preferably below 3%.
- the present invention not only contemplates tailoring the composition of the slag to the refractory binder as one of its embodiments, but also contemplates tailoring the composition of the binder to that of the slag charging materials as another embodiment.
- MgO combines with silica to form forsterite and that MgO will also combine with alumina, or ferric oxide to form high melting spinels.
- dolomitic lime in place of the usually used calcia lime as part of the binder material for the periclase particles of the refractory, a binder material is produced which is at first highly fluid at normal refractory firing temperatures, so that it flows around and encases the periclase particles.
- dolomitic lime can be added to the MgCO or Mg(OH) raw materials in place of the Cat) and other constituents which are presently added to make up the glassy phaseproducing binder.
- the CaO content of the calcined dolomite may form a spinel with alumina or ferric oxide, and will at the same time provide a CaO content in the binder which tends to match that of the slag.
- Most of the MgO of the dolomitic lime forms periclase, while the remaining portion may also form a spinel with alumina, ferric oxide, or other sesquioxides.
- Periclase particles are substantially insoluble in the slag-binder ceramic system, and to the extent that the MgO forms periclase, it does not enter into the reactive slag-binder system but hardens the binder around the original periclase crystals.
- Table I has been prepared giving the pertinent information of some of the heats which have been run in a basic oxygen furnace. It will be understood, however, that the invention may be used with the various other types of metallurgical equipment utilizing slag in contact with basic magnesia refractory, and that the conditions which exist in the basic oxygen furnace are considered to be the most severe.
- the basic oxygen furnace in which the various heats listed in Table I were made was lined with a high magnesia basic refractory having an MgO content of 76%. Each of the heats listed in the table was conducted by charging the furnace with a weighed amount of molten metal from a blast furnace. The composition of the metal had been previously determined. In accordance with the analysis of the metal, as received from the blast furnace, the amount of basic oxides required for the removal of the silicon, phosphorous, and sulphur of the metal charge was determined and added. Oxygen or oxygen-enriched air was directed at the surface of the slag and metal for a period of between 20 to 40 minutes following which the slag and metal were sequentially poured off into ladles and an analysis of their compositions was made.
- the C30 lime added was taken as 92%, and analysis course, attributable to the fact that a layer of the slag indicated that it also contained approximately 1% MgO. materials adheres to the side surfaces of the refractory
- the dolomitic lime on the other hand contains approxand that in some instances a greater amount of this maimately 40% MgO by weight, and approximately 56% terial is poured from the furnace with the slag than in CaO by weight. From the total amount of the C30 added others.
- the dolomitic lime had a surface area of 3.5 square meters per gram as determined by nitrogen absorption techniques.
- Heat C is given as typical of the results achievedwhen approximately 10% of the tot-a1 alkaline earth metal oxide slag charge is in the form of magnesium oxide and when no fluorspar is added to the charge. As shown in the Table, heats so made will generally give less than a 0.7 part loss of refractory during the run.
- Test results indicate that a tailoring of the slag to provide a dissolved M-gO content of from between approximately 3 and approximately 15% of the total slag forming ingredients causes a very marked reduction in the amount Best results are achieved with between approximately 5% and approximately 10% of dissolved MgO.
- the above data further shows that an even further reduction in the loss of refractory is obtained by eliminating the fluoride containing materials which are normally added to the slag forming materials.
- the MgO is preferably added in the form of dolomitic lime, or equivalents thereof from natural or purposely combined materials, and, as previously indicated, the amount of dolomitic lime which is used can be varied over a considerable extent so that amounts up to approximately 30% of the total charge can be in the form of the dolomitic lime.
- dolomitic lime there appears to be no criticality in the lower limit of the amount of dolomitic lime which is charged, inasmuch as the beneficial effect which is achieved is generally proportional to the amount used. In order that a substantial advantage will be achieved, however, over the prior art calcium oxide lime slag forming materials, more than approximately 10% of the charge should be in the form of the dolomitic lime.
- a preferred range of dolomitic lime is between 15 and 20% of the total slag forming charge materials.
- the inst-ant invention is concerned with refining slags which are used in contact with basic refractories, and particularly magnesia refractories having particles of periclase held together by a refractory binder which includes magnesia.
- the slags must have a base to acid rnolal ratio greater than 1:1, preferably greater than about 1.6: 1, more desirably between 2.021 and 45:1 and should most desirably have a base to acid ratio of between 2.5:1 and 3.5 :1.
- the slags of the invention have a base to acid ratio as specified above, but they must contain at least 10% and preferably more than 12% by weight of SiO or 30% by weight of A1 or an appropriate mixture of SiO and A1 0 Where a mixture of SiO and Al O forms the acid portion of the slags, the percent of SiO therein when divided by 12% and added to the percent of A1 0 therein divided by 30% should be at least equal to 1.
- the slag must contain calcia as its principal basic constituent and must have a proper magnesia to calcia ratio in order that the slag will have the proper heat transfer characteristics.
- magnesia to calcia ratio should be not greater than about 1:3, should preferably be more than about 1:15, and for best results should be between about 2:15 and about 1:4.
- Higher percentages of MgO cause the slag to become more viscous and refractory, to hinder heat transfer to the metal, and the ratio of MgO to CaO should never be greater than 1:1.
- refractory wear can be effectively reduced by using MgO in the above percentage ranges, without decreasing the heat transfer, the fluidity, and other desirable characteristics which calcia-silica and calcia-alumina type slags have.
- slag and refractory binder compositions are tailored relative to each other to provide a solid-liquid ceramic system at operating temperatures which is more nearly in equilibrium than are slag and binder compositions used heretofore. It is further to be understood that while the invention has been described in considerable detail, it is not limited to the particular embodiments shown and described; and it is intended to cover hereby all novel adaptations, modifications, and arrangements thereof which come within the practice of those skilled in the art to which'the invention relates.
- molten calcia type refining slags having a final composition including at least 10 percent by weight of SiO' and a base to acid mol-al ratio of at least 1.6 to 1 in contact with a magnesia refractory and which is exposed to a highly oxidizing atmosphere: the method of reducing the deterioration of the magnesia refractory by charging to the metallurgical equipment slag forming ingredients containing active MgO and CaO in particulate form, the ingredients including from approximately 10.0 percent to approximately 30.0 percent by weight of exposed calcined dolomite, and the limiting of the concentration of fluoride containing salts in the slag to less than approxirnately 3.0 percent by weight.
- molten metal is covered by molten calcia type refining slags having a final composition including at least 12 percent by weight of Si0 and a base to acid rnolal ratio between 2.0 to 1 and 4.5 to 1 in contact with a magnesia refractory and wherein a highly oxidizing atmosphere is blown into contact with the molten metal: the method of reducing the deterioration of the magnesia refractory by charging to the metallurgical equipment slag forming ingredients containing active MgO and CaO in particulate form, the ingredients comprising approximately 20.0 percent by weight of exposed calcined dolomite.
- molten metal is covered by molten calcia type refining slags having a final composition including at least 12 percent by weight of SiO and a base to acid molal ratio between 2.0 to 1 and 4.5 to l in contact with a magnesia refractory and wherein a highly oxidizing atmosphere is blown into contact with the molten metal: the method of reducing the deterioration of the magnesia refractory by charging to the metallurgical equipment slag forming ingredients containing active MgO and CaO in particulate form, the ingredients comprising approximately 20 percent by weight of exposed calcined dolomite, and the limiting of the concentration of fluoride containing salts in the slag to less than approximately 3.0 percent by weight.
- the method of reducing the deterioration of the magnesia refractory which includes the step of introducing slag forming ingredients containing from approximately 10 percent to approximately 30 percent by weight of dolomitic lime into the equipment, said slag forming ingredients being in such proportions as to provide a magnesia to calcia rnolal ratio in the slag of from about 1:15 to about 1:3 at least at the interfaces between the slag and refractory, whereby conversion of the magnesia in the dolomitic lime to periclase occurs at the interface and physically thickens the slag adjacent the interface
- a method for operating ,metall-urigcal equipment lined with a basic magnesia-containing refractory which method includes the steps of charging to the equipment, in contact with the magnesia refractory lining, a calcium compound which is reactive to neutralize SiO and form a calcium oxide-containing refining slag, and molten ferrous metal containing silicon, and treating the metal with a highly oxidizing atmosphere to form a slag which causes deterioration of therefractory and which has a final composition including at least 10 percent by weight of SiO and a base to acid molal ratio of at least 1.6 to 1: .the improvement of reducing deterioration of the refractory by additionally charging into the equipment exposed calcined dolomite in an amount which provides a slag having a magnesia to calcia molal ratio of from about 1:15 to about 1:3.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Structural Engineering (AREA)
- Inorganic Chemistry (AREA)
- Metallurgy (AREA)
- Analytical Chemistry (AREA)
- Furnace Housings, Linings, Walls, And Ceilings (AREA)
- Compositions Of Oxide Ceramics (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US323087A US3288592A (en) | 1963-01-16 | 1963-11-12 | Process for reducing deterioration in equipment handling molten materials |
GB1469/64A GB1028682A (en) | 1963-01-16 | 1964-01-13 | Improved process for reducing deterioration in equipment handling molten materials |
DE19641303099D DE1303099C2 (de) | 1963-01-16 | 1964-01-16 | Verfahren zur verminderung einer abnutzung der auskleidung einer insbesondere nach dem sauerstoffblasverfahren arbeitenden stahlgewinnungsanlage |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US25175763A | 1963-01-16 | 1963-01-16 | |
US323087A US3288592A (en) | 1963-01-16 | 1963-11-12 | Process for reducing deterioration in equipment handling molten materials |
Publications (1)
Publication Number | Publication Date |
---|---|
US3288592A true US3288592A (en) | 1966-11-29 |
Family
ID=26941812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US323087A Expired - Lifetime US3288592A (en) | 1963-01-16 | 1963-11-12 | Process for reducing deterioration in equipment handling molten materials |
Country Status (3)
Country | Link |
---|---|
US (1) | US3288592A (enrdf_load_stackoverflow) |
DE (1) | DE1303099C2 (enrdf_load_stackoverflow) |
GB (1) | GB1028682A (enrdf_load_stackoverflow) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3857698A (en) * | 1971-11-11 | 1974-12-31 | Steetley Ltd | Lime composition for basic oxygen steel-making process |
US3915696A (en) * | 1970-01-08 | 1975-10-28 | Ferdinand Fink | Sintered preformed slag for the steel industry |
EP0015396A1 (en) * | 1979-02-07 | 1980-09-17 | Union Carbide Corporation | A method for increasing vessel lining life for basic oxygen furnaces |
WO1981002584A1 (en) * | 1980-03-11 | 1981-09-17 | R Jordan | Carbonaceous fines in an oxygen-blown blast furnace |
EP0107299A1 (en) * | 1982-09-01 | 1984-05-02 | Ivor Gray Nixon | Use of fluxes for refining metals, particularly steel melts |
CN100436618C (zh) * | 2005-07-11 | 2008-11-26 | 台州盛世环境工程有限公司 | 一种用于高温熔融状态下的熔剂 |
CN1800811B (zh) * | 2005-08-24 | 2010-04-28 | 袁家义 | 用于x射线荧光光谱分析的熔剂 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5832209B2 (ja) * | 1976-04-15 | 1983-07-12 | 株式会社神戸製鋼所 | 改質転炉スラグおよび改質法 |
DE2852248C3 (de) * | 1978-12-02 | 1982-02-11 | Dolomitwerke GmbH, 5603 Wülfrath | Verfahren zur Erhöhung der Haltbarkeit basischer Ausmauerungen von Konvertern beim Frischen von Roheisen |
DE3040630C2 (de) * | 1980-10-29 | 1983-03-31 | Stahlwerke Peine-Salzgitter Ag, 3150 Peine | Verfahren zur Erzeugung von Stahl im basischen Konverter unter Verwendung von flüssiger Konverterschlacke |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
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US1939638A (en) * | 1931-07-25 | 1933-12-12 | Dwight & Lloyd Metallurg Compa | Refractory material and method of manufacturing |
US2361416A (en) * | 1942-03-04 | 1944-10-31 | Herbert A Reece | Fluxing material for metallurgical furnaces and method of operating said furnaces |
US2668759A (en) * | 1952-05-22 | 1954-02-09 | Inland Steel Co | Steelmaking process |
US2733141A (en) * | 1956-01-31 | Pneumatic process for the refining of basic pig iron | ||
US2741554A (en) * | 1955-08-26 | 1956-04-10 | Rinesch Rudolf Franz | Method of refining iron |
US2741555A (en) * | 1951-03-17 | 1956-04-10 | Oesterriechisch Alpine Montang | Process for refining pig iron |
US2811436A (en) * | 1954-02-08 | 1957-10-29 | Heuer Russell Pearce | Process of producing steel |
GB810960A (en) * | 1955-04-28 | 1959-03-25 | Siderurgie Fse Inst Rech | Method for desulphurizing molten pig iron |
US2906616A (en) * | 1955-04-28 | 1959-09-29 | Siderurgie Fse Inst Rech | Method for desulfurizing molten metal and in particular liquid pig iron |
-
1963
- 1963-11-12 US US323087A patent/US3288592A/en not_active Expired - Lifetime
-
1964
- 1964-01-13 GB GB1469/64A patent/GB1028682A/en not_active Expired
- 1964-01-16 DE DE19641303099D patent/DE1303099C2/de not_active Expired
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2733141A (en) * | 1956-01-31 | Pneumatic process for the refining of basic pig iron | ||
US1939638A (en) * | 1931-07-25 | 1933-12-12 | Dwight & Lloyd Metallurg Compa | Refractory material and method of manufacturing |
US2361416A (en) * | 1942-03-04 | 1944-10-31 | Herbert A Reece | Fluxing material for metallurgical furnaces and method of operating said furnaces |
US2741555A (en) * | 1951-03-17 | 1956-04-10 | Oesterriechisch Alpine Montang | Process for refining pig iron |
US2668759A (en) * | 1952-05-22 | 1954-02-09 | Inland Steel Co | Steelmaking process |
US2811436A (en) * | 1954-02-08 | 1957-10-29 | Heuer Russell Pearce | Process of producing steel |
GB810960A (en) * | 1955-04-28 | 1959-03-25 | Siderurgie Fse Inst Rech | Method for desulphurizing molten pig iron |
US2906616A (en) * | 1955-04-28 | 1959-09-29 | Siderurgie Fse Inst Rech | Method for desulfurizing molten metal and in particular liquid pig iron |
US2741554A (en) * | 1955-08-26 | 1956-04-10 | Rinesch Rudolf Franz | Method of refining iron |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3915696A (en) * | 1970-01-08 | 1975-10-28 | Ferdinand Fink | Sintered preformed slag for the steel industry |
US3857698A (en) * | 1971-11-11 | 1974-12-31 | Steetley Ltd | Lime composition for basic oxygen steel-making process |
EP0015396A1 (en) * | 1979-02-07 | 1980-09-17 | Union Carbide Corporation | A method for increasing vessel lining life for basic oxygen furnaces |
WO1981002584A1 (en) * | 1980-03-11 | 1981-09-17 | R Jordan | Carbonaceous fines in an oxygen-blown blast furnace |
EP0107299A1 (en) * | 1982-09-01 | 1984-05-02 | Ivor Gray Nixon | Use of fluxes for refining metals, particularly steel melts |
CN100436618C (zh) * | 2005-07-11 | 2008-11-26 | 台州盛世环境工程有限公司 | 一种用于高温熔融状态下的熔剂 |
CN1800811B (zh) * | 2005-08-24 | 2010-04-28 | 袁家义 | 用于x射线荧光光谱分析的熔剂 |
Also Published As
Publication number | Publication date |
---|---|
GB1028682A (en) | 1966-05-04 |
DE1303099C2 (de) | 1974-07-11 |
DE1303099B (enrdf_load_stackoverflow) | 1973-12-13 |
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