US2133327A - Process for refining lead which contains bismuth - Google Patents
Process for refining lead which contains bismuth Download PDFInfo
- Publication number
- US2133327A US2133327A US177301A US17730137A US2133327A US 2133327 A US2133327 A US 2133327A US 177301 A US177301 A US 177301A US 17730137 A US17730137 A US 17730137A US 2133327 A US2133327 A US 2133327A
- Authority
- US
- United States
- Prior art keywords
- bismuth
- lead
- potassium
- magnesium
- refining
- 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
- 229910052797 bismuth Inorganic materials 0.000 title description 30
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 title description 30
- 238000000034 method Methods 0.000 title description 14
- 238000007670 refining Methods 0.000 title description 10
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 18
- 239000011777 magnesium Substances 0.000 description 18
- 229910052749 magnesium Inorganic materials 0.000 description 18
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 17
- 239000011591 potassium Substances 0.000 description 17
- 229910052700 potassium Inorganic materials 0.000 description 17
- 238000001816 cooling Methods 0.000 description 9
- 238000007711 solidification Methods 0.000 description 7
- 230000008023 solidification Effects 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 4
- 239000000956 alloy Substances 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 238000000926 separation method Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 108091001629 crustin Proteins 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C22B13/00—Obtaining lead
- C22B13/06—Refining
-
- 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
- C22B13/00—Obtaining lead
- C22B13/06—Refining
- C22B13/08—Separating metals from lead by precipitating, e.g. Parkes process
Definitions
- the process which forms the subject of the present invention thus consists essentially in adding to lead which contains bismuth and which has been previously molten, magnesium and potassium in suitable quantities and then allowing the metal bath to cool' to near its temperature of solidi'lcation.
- This floating crust will contain, according to the proportions of magnesium and potassium used, the desired part of the bismuth contained, and up to the whole of the bismuth content, the bismuth content of the fused metallic lead being thus able practically to be brought to 0.001%.
- the lead After this treatment the lead always contains an excess of magnesium and potassium from which it can be freed by any known treatment for example with chlorine or water vapour.
- the magnesium and potassium may be employed in the state of pure metals or of alloys with lead or with other metals, and be added successively or simulteously to the bath of impure metal to be trea v If desired the proportion of magnesium or potassium utilized maybe diminished and this diminution be compensatedby an increase of potassium or magnesium taking care always to provide a simultaneous or successive addition of potassiumand magnesium; one may thus in particular confer upon the refining process additional advantages such for example as minimum cost of the reagents employed, greater ease in the treatment of the dresses, etc.
- thelead from which the bismuth isto be removed contains, besides bismuth, other impurities these may be partly or wholly contained in the dross with the bismuth.
- Example 1 A lead containing 1350 grams of bismuth per metric ton is treated in the fused state with an addition of magnesium equal to 1520 grams per metric ton and an addition oil potassium equal to 975 grams per metric ton. After agitation and cooling to the neighbourhood of the temperature of solidification, the floating crust is separated. The lead obtained only contains 130 grams of bismuth per metric ton.
- Example 2 A lead containing 590 grams of bismuth pe metric ton is treated as above with an addition of magnesium equal to 2220 grams per metric ton and an addition of potassium equal to 1240 grams per metric ton. After, cooling and separation of the'floating crust the lead obtained only contains'14 grams of bismuth per metric ton.
- H lead which contains bismuth, consisting in adding simultaneously to the lead in the molten state magnesium and potassium, cooling the metallic bath ,to the neighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
- Process for refining lead which contains bismuth consisting in adding to the lead in the molten state magnesium and potassium in the state of alloys with other metals, cooling the metallic bath to theneighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
Description
Patented a. 18, 1938 V UNITED STATES PATENT OFFICE PROCESS FOR REFINING LEAD'WHICH CON- TAINS BISMUTH Leon Eugene Jollivet, Marseille LEstaque, France, minor to Socit Miniere ct Mtallurgique de Penarroya, Paris, France France, a corporation of No Drawing. Application November 30, 1937, Serial No. 177,301. In France January 11, 1937 7 Claims. (01. 75-63) duces a partial elimination of bismuth in alloys v containing a high contentthereof.
The process which forms the subject of the present invention thus consists essentially in adding to lead which contains bismuth and which has been previously molten, magnesium and potassium in suitable quantities and then allowing the metal bath to cool' to near its temperature of solidi'lcation.
There is thus formed'a floating crust containing bismuth, magnesium, potassium and lead and which is separated from the bath of metal by any known process. I
This floating crust will contain, according to the proportions of magnesium and potassium used, the desired part of the bismuth contained, and up to the whole of the bismuth content, the bismuth content of the fused metallic lead being thus able practically to be brought to 0.001%.
After this treatment the lead always contains an excess of magnesium and potassium from which it can be freed by any known treatment for example with chlorine or water vapour.
For putting the process according to the invention into eflect, the magnesium and potassium may be employed in the state of pure metals or of alloys with lead or with other metals, and be added successively or simulteously to the bath of impure metal to be trea v If desired the proportion of magnesium or potassium utilized maybe diminished and this diminution be compensatedby an increase of potassium or magnesium taking care always to provide a simultaneous or successive addition of potassiumand magnesium; one may thus in particular confer upon the refining process additional advantages such for example as minimum cost of the reagents employed, greater ease in the treatment of the dresses, etc.
It should be noted that if thelead from which the bismuth isto be removed contains, besides bismuth, other impurities these may be partly or wholly contained in the dross with the bismuth.
However as at present there are eflicacious means for the separation of these other current impurities from impure lead, it may be more economical to separate from the lead to be treated the greater part of its other impurities before applying the process of the invention for the removal of bismuth. I
The-invention is illustrated in the following non-limiting examples.
Example 1 A lead containing 1350 grams of bismuth per metric ton is treated in the fused state with an addition of magnesium equal to 1520 grams per metric ton and an addition oil potassium equal to 975 grams per metric ton. After agitation and cooling to the neighbourhood of the temperature of solidification, the floating crust is separated. The lead obtained only contains 130 grams of bismuth per metric ton.
v I Example 2 A lead containing 590 grams of bismuth pe metric ton is treated as above with an addition of magnesium equal to 2220 grams per metric ton and an addition of potassium equal to 1240 grams per metric ton. After, cooling and separation of the'floating crust the lead obtained only contains'14 grams of bismuth per metric ton.
What I claim is:
'1. Process for refining .lead which contains bismuth, consisting in adding to the lead in the molten state magnesium and potassium, cooling the metallic bath to the neighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
2. Process for refining H lead which contains bismuth, consisting in adding simultaneously to the lead in the molten state magnesium and potassium, cooling the metallic bath ,to the neighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
3. Process for refining lead which contains bismuth, consisting in adding successively in either sequence to the lead in the molten state magnesium and potassium, cooling the metallic bath to the neighbourhood of its soli'dflcation point and then separating therefrom the floating crust in which the bismuth has collected. 7
4. Process for refining lead which contains bismuth, consisting in adding to the lead in the molten state magnesium and potassium. in the state of alloys with lead, cooling the metallic bath to the neighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
5. Process for refining lead which contains bismuth, consisting in adding to the lead in the molten state magnesium and potassium in the state of alloys with other metals, cooling the metallic bath to theneighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected.
6. Process for refining lead which contains bismuth consisting in adding to the lead in the molten state magnesium and potassium, cooling the metallic bath to the neighbourhood of its 1 solidification point, and then separating therefrom the floating crustin which the bismuth has collected, the proportions of magnesium and potassium being coordinated in the sense that the proportion of one may be varied within certain limits, this variation being compensated by a corresponding variation in the opposite sense in the proportion of the other. r
7. Process for refining lead which contains bismuth, consisting in bringing to simultaneous action on the lead in molten state magnesium and potassium, cooling the metallic bath to the neighbourhood of its solidification point and then separating therefrom the floating crust in which the bismuth has'collected.
LEON EUGENE JOLLIVET.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR2133327X | 1937-01-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
US2133327A true US2133327A (en) | 1938-10-18 |
Family
ID=9684011
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US177301A Expired - Lifetime US2133327A (en) | 1937-01-11 | 1937-11-30 | Process for refining lead which contains bismuth |
Country Status (1)
Country | Link |
---|---|
US (1) | US2133327A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2683085A (en) * | 1949-09-14 | 1954-07-06 | Metallgesellschaft Ag | Process for the recovery of metals or metal alloys from iron clad therewith |
US4039323A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Process for the recovery of bismuth |
US4039322A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Method for the concentration of alkaline bismuthide in a material also containing molten lead |
US5041160A (en) * | 1988-05-20 | 1991-08-20 | Timminco Limited | Magnesium-calcium alloys for debismuthizing lead |
US5143693A (en) * | 1988-05-20 | 1992-09-01 | Timminco Limited | Magnesium-calcium alloys for debismuthizing lead |
US20060096107A1 (en) * | 2004-11-05 | 2006-05-11 | Hickey James K | Lay out line |
US7469482B2 (en) | 2004-11-05 | 2008-12-30 | Studline Tool Company | Lay out line |
-
1937
- 1937-11-30 US US177301A patent/US2133327A/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2683085A (en) * | 1949-09-14 | 1954-07-06 | Metallgesellschaft Ag | Process for the recovery of metals or metal alloys from iron clad therewith |
US4039323A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Process for the recovery of bismuth |
US4039322A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Method for the concentration of alkaline bismuthide in a material also containing molten lead |
US5041160A (en) * | 1988-05-20 | 1991-08-20 | Timminco Limited | Magnesium-calcium alloys for debismuthizing lead |
US5143693A (en) * | 1988-05-20 | 1992-09-01 | Timminco Limited | Magnesium-calcium alloys for debismuthizing lead |
US20060096107A1 (en) * | 2004-11-05 | 2006-05-11 | Hickey James K | Lay out line |
US7231722B2 (en) | 2004-11-05 | 2007-06-19 | Stud Line Tool Company | Lay out line |
US7469482B2 (en) | 2004-11-05 | 2008-12-30 | Studline Tool Company | Lay out line |
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