US2204651A - Process for refining lead which contains bismuth - Google Patents
Process for refining lead which contains bismuth Download PDFInfo
- Publication number
- US2204651A US2204651A US247660A US24766038A US2204651A US 2204651 A US2204651 A US 2204651A US 247660 A US247660 A US 247660A US 24766038 A US24766038 A US 24766038A US 2204651 A US2204651 A US 2204651A
- Authority
- US
- United States
- Prior art keywords
- lead
- bismuth
- magnesium
- alkali metal
- calcium
- 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 31
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 title description 31
- 238000000034 method Methods 0.000 title description 21
- 238000007670 refining Methods 0.000 title description 11
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 20
- 229910052749 magnesium Inorganic materials 0.000 description 20
- 239000011777 magnesium Substances 0.000 description 20
- 229910052783 alkali metal Inorganic materials 0.000 description 17
- 150000001340 alkali metals Chemical class 0.000 description 17
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 13
- 229910052791 calcium Inorganic materials 0.000 description 13
- 239000011575 calcium Substances 0.000 description 13
- 238000007667 floating Methods 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 238000007711 solidification Methods 0.000 description 8
- 230000008023 solidification Effects 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 5
- 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 4
- 239000000956 alloy Substances 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 4
- 229910052708 sodium Inorganic materials 0.000 description 4
- 239000011734 sodium 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 3
- 230000008030 elimination Effects 0.000 description 2
- 238000003379 elimination reaction Methods 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- -1 bismuth-lead-sodium-magnesium Chemical compound 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 108091001629 crustin Proteins 0.000 description 1
- 230000003292 diminished effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000005065 mining Methods 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
Definitions
- the present invention provides a process for the removal of bismuth from lead which renders the use of calcium unnecessary.
- This new process is based upon the simultaneous action of magnesium and alkali metal which action was the more incapable of being predicted since none of the alkali metals alone produces any elimination of bismuth and magnesium alone only produces a partial elimination of bismuth in alloys containing a high content thereof.
- the process for deb-ismuthizing lead without the aid of calcium 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 alkali metal in suitable quantities and then allowing the metal bath to cool to near its temperature of solidification.
- This floating crust will contain, according to the proportions of magnesium and alkali metal used,
- the lead ordinarily contains an excessof magnesium and alkali metal from which it can be freed by any known treatment, for example, with chlorine.
- themagnesium and alkali metal e. g;, sodium
- theyagnesium and alkali metal may be employed in the state of pure metals or of alloys with lead or with other metals," and by adding successively or simultaneously to the bath of impure metal to be treated.
- the proportion of magnesium or alkali metal utilized may be diminished and this ,,diminution be ,compensatedby an increase of alkali met'algor magnesium taking care always to provide a simultaneous or successive addition of alkali metal andmagnesium; one may thus in particular confer upon the refining process additional advantages such as, for example, minimum costs of the reagents employed, greater ease in the treatment of drosses, etc.
- the lead 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.
- the lead 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 I A lead containing 0.30% of bismuth is treated in the fused state with an' addition of magnesium equal to eight pounds per short ton and an addition of sodium equal to twelve pounds per short ton. After agitation and cooling to the neighborhood of the temperature of solidification, the floating crust is separated. The lead obtained contains only 0.007%, of bismuth.
- the results are remarkable in view of the fact that no substantial reduction of bismuth could have been made in the lead of the examples either with alkali metal or with magnesium, alone.
- I Process for refining lead which contains. bismuth, consisting in adding to the lead-in the molten state magnesium and alkali metal, cooling the metallic bath to the neighborhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected, said process being performed in the absence of calcium.
- Process for debismuthizing lead which comprises mixing magnesium and alkali metal into a molten body of the lead, cooling same to raise a crust having a higher bismuth content than the original lead, and effecting a separation between said crust and the refined lead, said debismuthization being effected without the aid of calcium reagent.
- Process for refining lead with respectto bismuth as a contaminant which comprises subjecting the lead in molten state to the conjoint action of sodium and magnesium, concentrating the bismuth as a bismuth-lead-sodium-magnesium product at a temperature favoring such concentration, and efiecting a separation between said product and the rest of the lead, said process being carried out in the absence of any ei'fective amount of calcium reagent.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented June 18, 1940 PATENT orr ea PRO ESS FOR REFINING LEAD WHICH CONTAINS BISMUTH;
Jesse O. Bettcrton and Yurii E. Lebedeff,
.; K Metuchen, N. J., assignors to; American Smeltl i 1 ing and Refining Company, New York, N. Y.,
a ,ccrporation of New Jersey ticularymetal mixture or alloy and introducing alkali, alkaline earth or rare earth metal reagents therein for the purpose of concentrating one or more of the constituents of theoriginal alloy as v dross or crust which floats upon the molten bath and is readily separated therefrom.
However, early attempts to specifically apply the suggestionto the lead refinery for the removal ofbismuth failed and the advent of any successful, commercialprocesshad to await later discoveries, rjri'anyof which the readerwill find discussed or referred to in an article by applicants appearing in Transactions of the American Ina stitut of" Mining and Metallurgical Engineers,
vol. 121,1pages 205 225 (1936).
Following the discoveries aforementioned, their principles weresoon adapted by various refineries treating thousands of tons annually of lead containing bismuth in the amounts ordinarily encountered which, asis well known, usually range in the neighborhood 'of a few hundredths to afewftenths per cent. In this connection it is highly significant to note that, insofar as applicants are aware, all of the refineries referred to employ calcium as a reagent in debismuthizing such lead.
The present invention provides a process for the removal of bismuth from lead which renders the use of calcium unnecessary. This new process is based upon the simultaneous action of magnesium and alkali metal which action was the more incapable of being predicted since none of the alkali metals alone produces any elimination of bismuth and magnesium alone only produces a partial elimination of bismuth in alloys containing a high content thereof.
The process for deb-ismuthizing lead without the aid of calcium 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 alkali metal in suitable quantities and then allowing the metal bath to cool to near its temperature of solidification.
There is thus formed a floating crust containing bismuth, magnesium, alkali metal and lead and which is separated from the bath of metal by any known process.
This floating crust will contain, according to the proportions of magnesium and alkali metal used,
Application December 24, 1938,
Serial N0. 247,660
the desired part of the bismuth contained, and up i to substantially the whole of the bismuth content.
After thistreatmentthe lead ordinarily contains an excessof magnesium and alkali metal from which it can be freed by any known treatment, for example, with chlorine.
For putting the process according to the invention into effect, themagnesium and alkali metal, e. g;, sodium, may be employed in the state of pure metals or of alloys with lead or with other metals," and by adding successively or simultaneously to the bath of impure metal to be treated. If desired, the proportion of magnesium or alkali metal utilized may be diminished and this ,,diminution be ,compensatedby an increase of alkali met'algor magnesium taking care always to provide a simultaneous or successive addition of alkali metal andmagnesium; one may thus in particular confer upon the refining process additional advantages such as, for example, minimum costs of the reagents employed, greater ease in the treatment of drosses, etc.
It may be noted that if the lead 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 there are atpre'sent efiicacious 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 greator part of its other impurities before applying the process of the invention for the removal of hismuth.
The invention isillustrated in'the following non-limiting examples? Example I A lead containing 0.30% of bismuth is treated in the fused state with an' addition of magnesium equal to eight pounds per short ton and an addition of sodium equal to twelve pounds per short ton. After agitation and cooling to the neighborhood of the temperature of solidification, the floating crust is separated. The lead obtained contains only 0.007%, of bismuth.
Example II calcium used, the sole debismuthizing reagents being sodium and magnesium in the first example and lithium and magnesium in the second example. The results are remarkable in view of the fact that no substantial reduction of bismuth could have been made in the lead of the examples either with alkali metal or with magnesium, alone.
What is claimed is: I 1. Process for refining lead which contains. bismuth, consisting in adding to the lead-in the molten state magnesium and alkali metal, cooling the metallic bath to the neighborhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected, said process being performed in the absence of calcium. I
2. Process for refining lead which contains bismuth without the aid of calcium, consisting in adding simultaneously to the lead in the molten state magnesium and alkali metal, cooling the metallic bath to the neighborhood 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 without the aid of calcium, consisting in adding successively in either sequence to the lead in the molten state magnesium and alkali metal,
cooling the metallic bath to the neighborhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected. I
4. Process for refining lead which contains bismuth without the aid of calcium,-consisting in adding to the lead in the molten state magnesium and alkali metal in the state of alloys with lead, cooling the metallic bath to the neighborhood 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 without the aid of calcium, consisting in adding to the lead in the molten state magnesium and alkali metal in the state'of alloys with other metals, cooling the metallic bath; to the neighborhood of its solidification point and then separating therefrom the floating crustin which thebismuth has collected. v r
the other.
7. Process for refining lead which contains bismuth, consisting in bringing to simultaneous action on the lead in molten state magnesium and alkali metal, cooling the metallic bath to the neighborhood of its solidification point and then separating therefrom the floating crust in which the bismuth has collected, said process being performed in the absence of calcium.
.8. Process for debismuthizing lead which comprises mixing magnesium and alkali metal into a molten body of the lead, cooling same to raise a crust having a higher bismuth content than the original lead, and effecting a separation between said crust and the refined lead, said debismuthization being effected without the aid of calcium reagent.
9. Process for refining lead containing bismuth a acterized in that the process is performedwithout the addition of calcium to the lead.
10. Process for refining lead with respectto bismuth as a contaminant which comprises subjecting the lead in molten state to the conjoint action of sodium and magnesium, concentrating the bismuth as a bismuth-lead-sodium-magnesium product at a temperature favoring such concentration, and efiecting a separation between said product and the rest of the lead, said process being carried out in the absence of any ei'fective amount of calcium reagent.
JESSE O.'BE1'1ERTON. YURII E. LEBEDEFF.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US247660A US2204651A (en) | 1938-12-24 | 1938-12-24 | Process for refining lead which contains bismuth |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US247660A US2204651A (en) | 1938-12-24 | 1938-12-24 | Process for refining lead which contains bismuth |
Publications (1)
Publication Number | Publication Date |
---|---|
US2204651A true US2204651A (en) | 1940-06-18 |
Family
ID=22935802
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US247660A Expired - Lifetime US2204651A (en) | 1938-12-24 | 1938-12-24 | Process for refining lead which contains bismuth |
Country Status (1)
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US (1) | US2204651A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4039322A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Method for the concentration of alkaline bismuthide in a material also containing molten lead |
US4039323A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Process for the recovery of bismuth |
US4881971A (en) * | 1988-02-03 | 1989-11-21 | Thom Michael J | Refining of lead-debismuthizing |
-
1938
- 1938-12-24 US US247660A patent/US2204651A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4039322A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Method for the concentration of alkaline bismuthide in a material also containing molten lead |
US4039323A (en) * | 1976-04-02 | 1977-08-02 | Asarco Incorporated | Process for the recovery of bismuth |
US4881971A (en) * | 1988-02-03 | 1989-11-21 | Thom Michael J | Refining of lead-debismuthizing |
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