US2030357A - Process of removing tin from columbium alloys - Google Patents
Process of removing tin from columbium alloys Download PDFInfo
- Publication number
- US2030357A US2030357A US71665134A US2030357A US 2030357 A US2030357 A US 2030357A US 71665134 A US71665134 A US 71665134A US 2030357 A US2030357 A US 2030357A
- Authority
- US
- United States
- Prior art keywords
- tin
- columbium
- alloy
- silicon
- alloys
- 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
- 229910045601 alloy Inorganic materials 0.000 title description 33
- 239000000956 alloy Substances 0.000 title description 33
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 title description 27
- 239000010955 niobium Substances 0.000 title description 24
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 title description 23
- 238000000034 method Methods 0.000 title description 12
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 20
- 229910052710 silicon Inorganic materials 0.000 description 20
- 239000010703 silicon Substances 0.000 description 20
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 12
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 5
- 238000002386 leaching Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910000676 Si alloy Inorganic materials 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- LIZIAPBBPRPPLV-UHFFFAOYSA-N niobium silicon Chemical class [Si].[Nb] LIZIAPBBPRPPLV-UHFFFAOYSA-N 0.000 description 2
- 229910021332 silicide Inorganic materials 0.000 description 2
- FVBUAEGBCNSCDD-UHFFFAOYSA-N silicide(4-) Chemical compound [Si-4] FVBUAEGBCNSCDD-UHFFFAOYSA-N 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- JMAHHHVEVBOCPE-UHFFFAOYSA-N [Fe].[Nb] Chemical compound [Fe].[Nb] JMAHHHVEVBOCPE-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Chemical compound CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- -1 steel Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B25/00—Obtaining tin
- C22B25/06—Obtaining tin from scrap, especially tin scrap
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/20—Obtaining niobium, tantalum or vanadium
- C22B34/24—Obtaining niobium or tantalum
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- the present invention relates to a process of treating metallic alloys and more particularly to a process of treating alloys of. columbium forthe removal and" separation of tin.
- columbium ores such as columbite are frequently associated with stanv niferous minerals. If such tin-contaminated ores v are smelted for the production of alloys of co1u m-. bium with-iron, silicon, or other metals, a major portion of the tin content of the ore will ordinarily be recovered in the columbium alloy. For certain uses to which the-columbium alloys are put, notably as a means of. introducing columbium into steel,a high "tin content is often desirable.
- columbium alloys which may be produced by smelting stanniferous columbium oxide ores, by using any suitable reducing agent such as carbon, aluminum, or silicon, may be treated for the elimination of tin.
- the required silicon content of the alloy may be obtained by the reduction of silica, simultaneously with the reduction of the columbite ores, either 10 of silica naturally occurring in the ore, or of silica which may be intentionally added to the ore.
- a silicon-columbium alloy may be obtained by directly alloying a columbium alloy with metallic silicon.
- a leaching agent which has been found to be particularly suitable for the purposes of this invention is hydrochloric acid.
- other acidic agents, and particuwill usually require several hours, depending on the amount of tin to beextracted, the temperature, the concentration of the acid, and the size of the alloy particles being treated. I have found that the tin'can be practically completely extracted when the alloy iscomminuted'sothatthe particles will pass a 20 mesh screen, openmg), the particles being treated with hydrochloric acid of about 11 Baum.
- the acid treatment will frequently dissolve small amounts of some of the alloy constituents other than tin,.
- columbium alloy treated by my process for the elimination of tin may be used directly for adding columbium to other metals, such as steel, or if a lower silicon alloy is desired the silicon may be removed or lowered by any of the conventional refining processes prior to such use.
- Patent No 2,050, 357
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- ing And Chemical Polishing (AREA)
Description
Patented Feb. 11,1936
UNITED STATES PROCESS or REMOVING TIN mom coLU mM ALLOYS Ernest F. Doom, Niagara Falls, N. Y., assignor, by mesne assignments, to Union Carbide and Carbon'Corporation, a corporation of New York No Drawing. Application March 21,
Serial No. 716,651
3 Claims.
The present invention relates to a process of treating metallic alloys and more particularly to a process of treating alloys of. columbium forthe removal and" separation of tin.
Naturally occurring columbium ores such as columbite are frequently associated with stanv niferous minerals. If such tin-contaminated ores v are smelted for the production of alloys of co1u m-. bium with-iron, silicon, or other metals, a major portion of the tin content of the ore will ordinarily be recovered in the columbium alloy. For certain uses to which the-columbium alloys are put, notably as a means of. introducing columbium into steel,a high "tin content is often desirable. The removal of the associated tin from columbite prior to smelting is rarely feasible in a commercial manner, when known methods of ore dressing are resorted to, and where a fairly complete removal, of tin is desired. Special chemical treat ments of the ore have been used heretofore, but all of them are relatively expensive.
It is an object of my invention to provide a means of cheaplyand relatively completely re-' moving'tin from columbium alloys.
I have found that if silicon is incorporated in a tin-containing columbium alloy in an amount exceeding a silicon to columbium ratio of about 1 to 6.5, the tin content thereof may be leached out. by means of hydrochloric acid or a similar acid. It appears probable, from my investigations, that when the silicon content of the. alloy is less than this ratio the tin is combined with. the columbium as an acid-insoluble compound. when thesilicon content of the alloy exceeds this} ratio, the tin is in a free or at least in a soluble form. This silicon-columbium ratio roughly corresponds with the silicide CbiSi, and it may well be that the relative afllnity of'columbium for silicon. is greater than the affinity of columbium for tin, so that, when suflicient silicon is' present to form the silicide, the tin is left in a free'or soluble'form. It will be understood, however, that this is merely a theoretical explanation and that this invention does not depend upon the correct- 3 nessof this theory. The presence of other silicide-formingelements in the alloy may alter the minimum ratio of silicon to columbium necessary for the best extraction'of tin. In general I prefer to use somewhat more silicon in the alloy than the ratio shown, this being considered more conducive to an easy solution of the tin. 4
In carrying out my process, columbium alloys which may be produced by smelting stanniferous columbium oxide ores, by using any suitable reducing agent such as carbon, aluminum, or silicon, may be treated for the elimination of tin.
The required silicon content of the alloy may be obtained by the reduction of silica, simultaneously with the reduction of the columbite ores, either 10 of silica naturally occurring in the ore, or of silica which may be intentionally added to the ore. Alternatively; a silicon-columbium alloy may be obtained by directly alloying a columbium alloy with metallic silicon.
The alloy produced by any of the above described processes is then comminuted and treated with a leaching agent. A leaching agent which has been found to be particularly suitable for the purposes of this invention is hydrochloric acid. However, other acidic agents, and particuwill usually require several hours, depending on the amount of tin to beextracted, the temperature, the concentration of the acid, and the size of the alloy particles being treated. I have found that the tin'can be practically completely extracted when the alloy iscomminuted'sothatthe particles will pass a 20 mesh screen, openmg), the particles being treated with hydrochloric acid of about 11 Baum. The acid treatment will frequently dissolve small amounts of some of the alloy constituents other than tin,. such as iron, but -I have found that ifery little, if any, loss of columbium'occurs. The concentration of acid is not critical, as I have employed dilute and concentrated acid with practically equal success. In general, an excess of acid-of fair concentration is to be preferred, as it hastens solution of the tin.
In practicing my invention, three lots of ferrocolumbium-silicon alloy containing varying ratios 7 of silicon to columbium were comminuted to 20 mesh and treated for 36 hours with a solution with two parts of the diluted acid. The results Q,
of this treatment are indicated in the following bium ratio isnearly l to 6.5, a substantial amount table: of the tin is removed by the treatment. With Alloy No.1 I a silicon content below this ratio, as in Alloy No. 1, the tin is completely insoluble, whereas 5 I Bermmat. mm with a higher silicon content, as in Alloy No. 3, 5
went mm the tin is substantially all removed by the acid treatment.
The columbium alloy treated by my process for the elimination of tin may be used directly for adding columbium to other metals, such as steel, or if a lower silicon alloy is desired the silicon may be removed or lowered by any of the conventional refining processes prior to such use.
Alloy No.2 I What I claim is: 1. The process of removing tin from columbium 15 Before treat- Aitertreatalloys which comprises introducing silicon into said alloys in an amount at least equivalent to that required to provide a ratio of silicon to columbium satisfying the formula CbzSi, and treating said alloys with aqueous hydrochloric acid.
2. The process of reducing the proportion of tin in tin containing columbium alloys, which comprises introducing silicon into such alloy in Largely iron lto columbium ratio of about 1 to 6.5, comminuting Before treat- Altertm tthe silicon-containing alloy and leaching it with a solution of hydrochloric acid.
3. The process of reducing the proportion of 40.42% tin which is contained in an iron-columbium {2 alloy, which comprises introducing silicon into g3: said alloy in a'iatio of about 1 to 6.5, comminutl mg ing the alloy, and leaching it with aqueous hydrochloric acid.
' ERNEST F. DOOM. It will be noted that where the silicon-colum- CERTIFICATE OF CORRECTION.
Patent No. 2,050,' 357. I February 11, 1936.
ERNEST F. DOOM. a
It is hereby certified that errorappears in the printed specification of the above numbered patent requiring correction as follows: Page 1 first column, line 14,, 'for "desirable read undesirable; and that the said Letters Patent should be read with this correction 'therein that the same may conform to the record of the case in the Patent Office.
, Signed and sealed this 17th day March, A. D. 1936.
Leslie Frazer (Seal) 4 Acting Commissioner of" Patents 5 Alloy No. 3 an amount at least equivalent to a silicon to 25 CERTIFICATE or CORRECTION.
Patent No 2,050, 357.
ERNEST F. DOOM. A
It is hereby certified that error in the printed specifioation of the above numbered patent requiring correction as follows: Page 1, first column, line 14, 'for "desirable" read undesirable; and that the sai Letiers tion 'therein' that the same may conform Patent should be read with this correc to, the record of the case in the Patent Office/ Signed and sealed this 17th day March, A. D. 1936.
appears Leslie Frazer (Seal) Acting Commissioner of Patents February 11-, 1936.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US71665134 US2030357A (en) | 1934-03-21 | 1934-03-21 | Process of removing tin from columbium alloys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US71665134 US2030357A (en) | 1934-03-21 | 1934-03-21 | Process of removing tin from columbium alloys |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2030357A true US2030357A (en) | 1936-02-11 |
Family
ID=24878868
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US71665134 Expired - Lifetime US2030357A (en) | 1934-03-21 | 1934-03-21 | Process of removing tin from columbium alloys |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2030357A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2905549A (en) * | 1957-10-14 | 1959-09-22 | Fansteel Metallurgical Corp | Method of recovering refractory metals |
| US2905550A (en) * | 1957-10-14 | 1959-09-22 | Fansteel Metallurgical Corp | Recovery of refractory metals |
| US2905548A (en) * | 1957-09-06 | 1959-09-22 | Fansteel Metallurgical Corp | Method of recovering tantalum and columbium |
| US3862836A (en) * | 1972-05-18 | 1975-01-28 | Molybdenum Corp | Removal of lead from columbium mineral concentrate |
-
1934
- 1934-03-21 US US71665134 patent/US2030357A/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2905548A (en) * | 1957-09-06 | 1959-09-22 | Fansteel Metallurgical Corp | Method of recovering tantalum and columbium |
| US2905549A (en) * | 1957-10-14 | 1959-09-22 | Fansteel Metallurgical Corp | Method of recovering refractory metals |
| US2905550A (en) * | 1957-10-14 | 1959-09-22 | Fansteel Metallurgical Corp | Recovery of refractory metals |
| US3862836A (en) * | 1972-05-18 | 1975-01-28 | Molybdenum Corp | Removal of lead from columbium mineral concentrate |
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