US1549312A - Process of desulphurizing iron and steel and a composition of matter for use in said process - Google Patents
Process of desulphurizing iron and steel and a composition of matter for use in said process Download PDFInfo
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- US1549312A US1549312A US538423A US53842322A US1549312A US 1549312 A US1549312 A US 1549312A US 538423 A US538423 A US 538423A US 53842322 A US53842322 A US 53842322A US 1549312 A US1549312 A US 1549312A
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- Prior art keywords
- metal
- sodium
- hydroxid
- iron
- alkali
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title description 47
- 239000000203 mixture Substances 0.000 title description 31
- 229910052742 iron Inorganic materials 0.000 title description 24
- 238000000034 method Methods 0.000 title description 18
- 229910000831 Steel Inorganic materials 0.000 title description 15
- 239000010959 steel Substances 0.000 title description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 20
- 239000005864 Sulphur Substances 0.000 description 19
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 17
- 229910052783 alkali metal Inorganic materials 0.000 description 16
- 150000001340 alkali metals Chemical class 0.000 description 16
- 239000003153 chemical reaction reagent Substances 0.000 description 15
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 12
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 11
- 229910052751 metal Inorganic materials 0.000 description 11
- 239000002184 metal Substances 0.000 description 11
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 9
- 230000009467 reduction Effects 0.000 description 9
- 238000006722 reduction reaction Methods 0.000 description 9
- 239000011734 sodium Substances 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000004615 ingredient Substances 0.000 description 8
- 229910052708 sodium Inorganic materials 0.000 description 8
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 7
- 229910000029 sodium carbonate Inorganic materials 0.000 description 6
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 6
- 229910001021 Ferroalloy Inorganic materials 0.000 description 5
- 239000004115 Sodium Silicate Substances 0.000 description 5
- 229910000288 alkali metal carbonate Inorganic materials 0.000 description 5
- 150000008041 alkali metal carbonates Chemical class 0.000 description 5
- 239000010410 layer Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 229910052911 sodium silicate Inorganic materials 0.000 description 5
- 229910052914 metal silicate Inorganic materials 0.000 description 3
- 235000019353 potassium silicate Nutrition 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000011876 fused mixture Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 241000134884 Ericales Species 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 239000004111 Potassium silicate Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- KSCFJBIXMNOVSH-UHFFFAOYSA-N dyphylline Chemical compound O=C1N(C)C(=O)N(C)C2=C1N(CC(O)CO)C=N2 KSCFJBIXMNOVSH-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 description 1
- 229910052913 potassium silicate Inorganic materials 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 150000003388 sodium compounds Chemical class 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- -1 sulphur compound Chemical class 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Images
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
- C21C1/00—Refining of pig-iron; Cast iron
- C21C1/02—Dephosphorising or desulfurising
Definitions
- This invention relates to a process of treating iron, steel, ferro-alloys-and copper, for re ucing or eliminating the sulphur content thereof, and to a composition of matter for use in such process, andaims to provide improvements therein.
- the invention provides an improved and. highly effective process of reducing or eliminating the sulphur content in iron, steel, ferro-alloys and copper. It further provides a process which is very simply and readily carried out in' connection. with present operating equipment in general use for producing'iron, steel, etc.
- the invention further provides a process using a class of reagents which are in abundant-supply in the market.
- the invention further provides a composition of matter, which is useful in the above.- mentioned process and which may be put u'pin a form convenient for useand safe for handling.
- sodium hydroxid sodium carbonate, potassium carbonate, potassium hydroxid, and sodium or potassium silicate together with one or more of the preceding.
- asset forthherein may not be used to- 'gether with other substances which do not destroy or materially disadvantageously affeet the desulphurizing .action of said reagents.
- sodium hydroxld as the reagent,
- the alkali-metal reagent is brought into 4 the reaction upon the sulphur in the metal v contact with the molten iron, steel, etc. in
- any suitable or known manner practiced in metallurgy but is conveniently placed or dumped-onto the surface bf the metal con- I tained in an ordinary ladle, crucible, converter, hearth, or the like. Any overlying slag, so far as possible, is removed from the surface of the molten metalf A-complete covering of the surface of ,the" metal with the desulphurizing material will give the greatest efficiency.
- the heat of the metal will dissociate the sodium hydro-xid, which will breakup into-sodium oxid and water vapor which will be evolved. The. sodium hydroxid will bemelted to afluid consisan alkali-metal silicate.
- Fig. 1 the molten metal (designated by reference letter A) is illustrated as being contained in a ladle B.
- G designates the surface layer of liquid sodium hydroxid.
- the two or mixed reagents are preferably fused into cakes of a regular 'size, and for comfort and safety in handlin where one of the ingredients may be caustlc, and for preserving the condition 40 of the mixture where oneof the ingredients may be hygroscopic, the mixture may be covered 1n any suitable manner, as by a box,
- Fig. 2 which illustrates a form of the com osition of matter comprising the alkali-metal reagent and theal.-
- the letter M designates a cake conslstmg of a fused mixture of said 4 ingredients
- Q designates a coating or paraifine wax covering said cake.
- ture to a ton of iron is used, depending on the sulphur content and the amount of sulphur desired to be removed. .
- the carbonate is used in the place of the hydroxid, or where potassium is used in the place of sodium, the amount to be used may be calculated'on the basis of the Na,() content of the sadium hydroxid.
- the alkali-metal silicate when used alone will act" to reduce the sulphur content of iron, steel, etc., but this per cent. of reduc tion is small 'as compared with sodium-hydroxid and sodium carbonate, showing about a 14% reduction.
- t at the carbonate 7 beside reducing the volatility of the hy-' droxid has other beneficial roperties such asfreducing the 'tendency'o the hydroxid to act on the silicon. in the iron, and that the silicate also has other pro rties, such as reducing the volatility of t e hydroxid.
- the desulp mferior to what has been found to be much I it is when the reagent at a thin or fluid consistency.
- the process may be carried out by various other procedures than that specifically de-- scribed.
- a process of treating iron, steel, ferroalloys, and copper for diminishin .or eliminating the sulphur content thereo comprising treating the molten metal with a mixture of alkali-metal hydroxid and alkalimetal carbonate, the carbonate being present in an amount to reduce the volatilization of the hydroxid.
- a rocess according to claim 1 in which an alka i-metal silicate is contained in the mixture of hydroxid and carbonate, the silicate binding the other ingredients of the mixture prior to melting.
- a process of treating iron, steel,ferro alloys, and copper for diminishin or eliminating the sulphur content thereo comprising treating the molten metal with a mixture of an alkali-metal silicate, and at least one of the following: alkali-metal hydroxi-d, alkali-metal carbonate; said silicate binding the other ingredients of the mixture prior to melting.
- Aprocess according to claim 3 further characterized by the silicate being present inthe proportion of substantially 10%, and
- composition of matter for use in desulphurizing iron, steel, ferro-alloys, and copper consisting of an alkali-metal silicate and at least one of the following: alkalimetal hydroxid, alkali-metal carbonate, the silicate binding the other ingredients of the mixture.
- composition of matter according to claim 9 further characterized by the alkalimetal silicate being representatively in the proportion of 5 to 15% and the alkali-metal hydroxid, or carbonate, or mixture, from 85 to 95%.
- composition of matter according to claim 9 further characterized by the alkalimetal silicate being substantially in the prosigned our names.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Description
' Patented Aug. 11-, 1925.
UNITED STATE-S,
PATENT oilce.
I DANIEL nmoxsoit, or nnooxmm, unw'yonx, .rosnrn n. sums, or nnoomrmnn,
AND FREDERICK CO'NLIN; F WESTFIELD, NEWRTERSEY, ASSIGNORS TO SAID JACK- SON, SAID SEARS, AND JOHN T. PRATT, OF NEW YORK, N. Y., AS JOINT TRUSTEES.
' successor .nnsunrmimzme men AND swam; AND A oomrosrrrou OF'IlEATTER non; use IN sun rnocnss.
To all whom,- z't-may concern: I
Application filed February 22, 1922. Serial m. 538,423.
Be it known that we, -DANIEL D. J ACKSON, residingin the-borough of Brooklyn, city and State of New York, JosErH D. SEARS, residing in 'Bloomfield, 'county of Essex, and State .of New Jersey, and FREDERICK CONL'IN, residing in Westfield,- county of Union, State of New Jersey, citizens of the United States of America, have invented certain nwQ-and useful Improvements in Processes of -Desulphurizing Iron and Steel and a Composition of Matter for Use in Said Processes, of which the following isa specification. A r
This invention relates to a process of treating iron, steel, ferro-alloys-and copper, for re ucing or eliminating the sulphur content thereof, and to a composition of matter for use in such process, andaims to provide improvements therein.
y The inventionprovides an improved and. highly effective process of reducing or eliminating the sulphur content in iron, steel, ferro-alloys and copper. It further provides a process which is very simply and readily carried out in' connection. with present operating equipment in general use for producing'iron, steel, etc.
. The invention further provides a process using a class of reagents which are in abundant-supply in the market. I
The invention further provides a composition of matter, which is useful in the above.- mentioned process and which may be put u'pin a form convenient for useand safe for handling.
- V A specifioapplication of the process and a form in whichthe composition of matter may be embodied are illustrated in Figures 1 and 2 respeotivelyof the accompanying drawing. f According to our discovery and researches, sulphur, found as an impurity in iron, steel,
1 etc., can be virtually eliminated, or its content iniiron, steel, etc., substantially reduced by treating the molten metal containing the sulphur, with certain mixtures of alkali- -metal comp'ounds,which unite or combine with the sulphur compound of the iron. A
been found to give good results in reducing the sulphur contentof iron and steel.
-Among these substances may be mentioned sodium hydroxid, sodium carbonate, potassium carbonate, potassium hydroxid, and sodium or potassium silicate together with one or more of the preceding.
Our researches and discoveries have also shown that the sodium compounds, in combination with sodium silicate, give a decidedly superior desulphurizing action.
Our researches and discoveries have also shown that mixtures. of alkali-metal hydroxids and carbonates indiscriminately with other substanoes, instances of which are found in prior art patents, do" not have an action which can be regarded as of significant or technical importance.
It is not intended to beintlicated herein, however, that the alkali-metal compounds, or. their mixtures with alkali-metal sllicates,
asset forthherein, may not be used to- 'gether with other substances which do not destroy or materially disadvantageously affeet the desulphurizing .action of said reagents. Using sodium hydroxld as the reagent,
would probably be- The alkali-metal reagent is brought into 4 the reaction upon the sulphur in the metal v contact with the molten iron, steel, etc. in
any suitable or known manner practiced in metallurgy, but is conveniently placed or dumped-onto the surface bf the metal con- I tained in an ordinary ladle, crucible, converter, hearth, or the like. Any overlying slag, so far as possible, is removed from the surface of the molten metalf A-complete covering of the surface of ,the" metal with the desulphurizing material will give the greatest efficiency. The heat of the metal "will dissociate the sodium hydro-xid, which will breakup into-sodium oxid and water vapor which will be evolved. The. sodium hydroxid will bemelted to afluid consisan alkali-metal silicate.
5 the mass into contact with the liquid layer of the sodium hydroxid onthe surface thereof, thereby reacting with the sodium oxid to form sodium sulphide, and probably some one or more oxy-sulphur sodium compounds, which enter therslag produced by the treatment.
In the drawing, Fig. 1 the molten metal (designated by reference letter A) is illustrated as being contained in a ladle B. G designates the surface layer of liquid sodium hydroxid.
In experiments on iron, using'a mixture of sodium hydroxid and sodium carbonate (equal parts) as the desulphurizing reagent, spread out as a liquid la er on the surface of the molten iron, a re uction as high as 67% of the sulphur contained in the iron has been obtained,at a single treatment, via, a reduction from 146% S. to 048% S.
3 It has been further discovered that a bet; ter result in reducing the sulphur content of iron, steel, etc.,' by the use of the reagents hereinbefore mentioned, may be obtained by' using said reagents concurrently with reagent and the alkali-metal silicate .are conveniently mixed, and the mixture used in 'the same manner'as the use of the alkalimetalreagent has been described. For convenience in handling, the two or mixed reagents are preferably fused into cakes of a regular 'size, and for comfort and safety in handlin where one of the ingredients may be caustlc, and for preserving the condition 40 of the mixture where oneof the ingredients may be hygroscopic, the mixture may be covered 1n any suitable manner, as by a box,
'. or by-a coating of parafline.
In the drawing, Fig. 2, which illustrates a form of the com osition of matter comprising the alkali-metal reagent and theal.-
ali-metal silicate, the letter M designates a cake conslstmg of a fused mixture of said 4 ingredients, and Q designates a coating or paraifine wax covering said cake.
With a mixture of sodium h droxid' and sodlum silicate (solid water g ass) spread out as a liquid-layer on the surface of the molten metal, the sulphur content of iron has been reduced as much as 97% at a single treatment, yi'z, a reduction from ;114% S. to 004% S. Amixture of from 85-95% sodium hydroxid to from 545% sodium 811163136 has 'ven best results in use,
the highest reduction of sulphur having ture ofsOdiumparbonate, and sodium sili- The alkali-metal cate spread out as a liquid layer on the surface of the moltenmetal, the sul hur content of the-iron has been reduc as much. as 68% at a single treatment, viz, a reduction from 158% S. to 05% S. In experiments upon iron, using a mixture of sodium liydroxid, sodium carbonate, and sodium silicate in the proportions of 90% sodium hydroxi'd, and sodium carbonate, and 10% sodium silicate, as the desulphurizing reagent spread out as a liquid layer on the surface of. the molten iron, a reduction as highas' has been a single treatment.
With a mixture of sodium hydroxid (90%) and sodium silicate (10%) used on copper (Lake copper) the sulphur content has been reduced as much as 91% at a single treatment, viz, a reduction from .117 S.
Usually from '10to 25 pounds of this mixobtained, at
ture to a ton of iron is used, depending on the sulphur content and the amount of sulphur desired to be removed. .Where the carbonate is used in the place of the hydroxid, or where potassium is used in the place of sodium, the amount to be used may be calculated'on the basis of the Na,() content of the sadium hydroxid.
Gorrespondin" results in foundry practice have been (itained by using the abovementioned reagents and mixtures thereof with silicates (water glass).
The alkali-metal silicate when used alone will act" to reduce the sulphur content of iron, steel, etc., but this per cent. of reduc tion is small 'as compared with sodium-hydroxid and sodium carbonate, showing about a 14% reduction.
The conjoint use of the alkali-metal silicate (Water glass) with another alkalimetal reagent such as sodium hydroxid or carbonate, in the proportions previously.
designated, givesthe best results, as the sulphur reduction in such case issuperior to that obtained by any of the alkali-metal reagents alone. v 1 The mixture of alkali-metal hydroxid' and alkali-metal carbonate is less volatile when heated on the molten bath than hydroxid alone, produces a less watery layer or sla on the surface of the metal than hydroxid alone, and melts more quickly than carbon-- ate alone. mainly as a' binder of the other ingredient or ingredients of themixture and to thereby The alkali-metal silicate is used promote the quick meltin of the mixture. g It is to be understood t at the carbonate 7 beside reducing the volatility of the hy-' droxid, has other beneficial roperties such asfreducing the 'tendency'o the hydroxid to act on the silicon. in the iron, and that the silicate also has other pro rties, such as reducing the volatility of t e hydroxid.
.Where the {alkali metalreagent, either alone or associated with analkali-metal silicate, is used with other substances which to a thin or urizing action fluid consistency, the desulp mferior to what has been found to be much I it is when the reagent at a thin or fluid consistency.
The process may be carried out by various other procedures than that specifically de-- scribed.
Claims to the mixture of sodium hydroxid and sodium carbonate, and to the fused mixture thereof, and to the process of desulphurizing with this mixture, are contained in our copending application Serial No. 631,925, filed April 13, 1923.
What is claimed'is:-
1. A process of treating iron, steel, ferroalloys, and copper for diminishin .or eliminating the sulphur content thereo comprising treating the molten metal with a mixture of alkali-metal hydroxid and alkalimetal carbonate, the carbonate being present in an amount to reduce the volatilization of the hydroxid.
2. A rocess according to claim 1 in which an alka i-metal silicate is contained in the mixture of hydroxid and carbonate, the silicate binding the other ingredients of the mixture prior to melting. a
3. A process of treating iron, steel,ferro alloys, and copper for diminishin or eliminating the sulphur content thereo comprising treating the molten metal with a mixture of an alkali-metal silicate, and at least one of the following: alkali-metal hydroxi-d, alkali-metal carbonate; said silicate binding the other ingredients of the mixture prior to melting. v
4. A process according to claim 3, further characterizeddiy the silicate being present in the proportion of 515% and the alkalimetal hydroxid, or carbonate, or mixture of hydroxid and carbonate, from 85-95%.
5'. Aprocess according to claim 3, further characterized by the silicate being present inthe proportion of substantially 10%, and
the alkali-metal hydroxid, or carbonate, or mixtur of hydroxid and carbonate, 90%.
6. A process according to claim 1, further the lngredlents being presulphurizing iron, steel, ferro-alloys, and copper, consisting of alkali-metal hydroxid and I alkali-metal carbonate, the carbonate being resent in an amount to reduce the volatillzation of the hydroxid at the temperatures of molten metal.
9. A composition of matter for use in desulphurizing iron, steel, ferro-alloys, and copper, consisting of an alkali-metal silicate and at least one of the following: alkalimetal hydroxid, alkali-metal carbonate, the silicate binding the other ingredients of the mixture. I
10. A composition of matter according to claim 9, further characterized by the alkalimetal silicate being representatively in the proportion of 5 to 15% and the alkali-metal hydroxid, or carbonate, or mixture, from 85 to 95%.
'11. A composition of matter according to claim 9, further characterized by the alkalimetal silicate being substantially in the prosigned our names.
DANIEL D. JACKSON. J OSEPHD SEARS. FREDERICK CONLIN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US538423A US1549312A (en) | 1922-02-22 | 1922-02-22 | Process of desulphurizing iron and steel and a composition of matter for use in said process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US538423A US1549312A (en) | 1922-02-22 | 1922-02-22 | Process of desulphurizing iron and steel and a composition of matter for use in said process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1549312A true US1549312A (en) | 1925-08-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US538423A Expired - Lifetime US1549312A (en) | 1922-02-22 | 1922-02-22 | Process of desulphurizing iron and steel and a composition of matter for use in said process |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1549312A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2730442A (en) * | 1951-04-06 | 1956-01-10 | Thill Arthur | Method of dephosphorizing and refining thomas and bessemer steels |
-
1922
- 1922-02-22 US US538423A patent/US1549312A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2730442A (en) * | 1951-04-06 | 1956-01-10 | Thill Arthur | Method of dephosphorizing and refining thomas and bessemer steels |
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