US1594424A - Method of refining metals - Google Patents
Method of refining metals Download PDFInfo
- Publication number
- US1594424A US1594424A US721125A US72112524A US1594424A US 1594424 A US1594424 A US 1594424A US 721125 A US721125 A US 721125A US 72112524 A US72112524 A US 72112524A US 1594424 A US1594424 A US 1594424A
- Authority
- US
- United States
- Prior art keywords
- caustic
- molten
- dross
- metal
- bath
- 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
- 229910052751 metal Inorganic materials 0.000 title description 16
- 239000002184 metal Substances 0.000 title description 16
- 238000000034 method Methods 0.000 title description 13
- 238000007670 refining Methods 0.000 title description 7
- 150000002739 metals Chemical class 0.000 title description 4
- 239000003518 caustics Substances 0.000 description 24
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000000463 material Substances 0.000 description 11
- 239000012530 fluid Substances 0.000 description 9
- 239000003513 alkali Substances 0.000 description 6
- 239000003153 chemical reaction reagent Substances 0.000 description 6
- 238000007792 addition Methods 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 235000011121 sodium hydroxide Nutrition 0.000 description 5
- 229910052785 arsenic Inorganic materials 0.000 description 4
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 4
- 230000008719 thickening Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 3
- 238000007667 floating Methods 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000002893 slag 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
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/10—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
-
- 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 invention relates to refining and purifying metals and more particularly to methods involving the useor presence of caustic alkali such as caustic soda in the I 5 molten state.
- the molten caustic is'a thin and fluid liquid which floats on the surface of the metal bath much as oil floats on water. So long as the covering of caustic is of considerable depth it may be run off without material difficulty but, as its thickness decreases, it is diflicult to run it off without running off some of the metal. It is also practically impossible tocompletely remove the caustic without removing more or less of the metal, since the last of the caustic floats on the metal bath in detached fugitive patches.
- the molten fluid caustic is also a disagreeable if not a dangerous product to handle since its contact with water may create an explosionwith a scattering of caustic through the air and also because its causticity intensifies a burn beyond that due to its heat.
- con-' rial may conveniently be an inert substance having a high melting point which will form with the molten caustic a mixture which is not fluid at the temperature used.
- the scum or dross may be converted into a practically dry powdery mass which may be scraped from thesurface of the bath. 4
- gredient of the refractory thickening material as, for instance, between the causticcaustic in the material used.
- Theabove method of removing the caustic and drossed impurities from the molten bath' may be used 1n various methods 1nvolvmg a use of caustic whlch results 1n its presence in a fluid molten state on the surface of the bath and has been applied with marked advantage in a method of removing arsenic from antim'onial lead by treatment with caustic soda which is described and claimed in application No. 678,354, filed Nov. 22, 1923, as a continuation of application No. 579,035, filed August 1, 1922.
- caustic soda is added to a bath of the molten alloy at a temperature between 900 degrees and 1000 degrees F.
- the inert stiffening material is added to the scum or dross preparator to its removal and, as above explaine mixes with or absorbs the molten caustic forming therewith and with the dross impurities, a pasty or crusty mass which may be readily removed by scraping or skimming and taking with it prac cally all the fluid caustic without danger and without removal of the metal treated.
- the addition of the 'refractory thickening material may be omitted until the final treatment and removal of the final skim, since the presence of free caustics on the surface of the bath after eachfof the preliminaryskims will not be detrimental.
- caustic alkali reagent is intended to include a reagent com risin caustic alkali 'either alone or mixed with other reagents.
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 Aug. 3, 1926.
1,594,424 PATENT OFFICE. i
JOHN J. MULLIGAN, OF EAST CHICAGO, INDIANA, ASSIGNOR T UNITED STATES SMELTING REFINING & MINING COMPANY, 01: PORTLAND, MAINE, A CORPORATION OF MAINE.
No Drawing.
The invention relates to refining and purifying metals and more particularly to methods involving the useor presence of caustic alkali such as caustic soda in the I 5 molten state.
' on the metal bath. The thickening mate-.
Metal refining methods have heretofore been proposed or used in which molten v,Inet-al is treated. with caustic alkali either.
alone or mixed with other reagents and in which the impurities rise with the freecaustic to the surface of the metal in the form of a more or less fluid dross which must be removed. The molten caustic is'a thin and fluid liquid which floats on the surface of the metal bath much as oil floats on water. So long as the covering of caustic is of considerable depth it may be run off without material difficulty but, as its thickness decreases, it is diflicult to run it off without running off some of the metal. It is also practically impossible tocompletely remove the caustic without removing more or less of the metal, since the last of the caustic floats on the metal bath in detached fugitive patches. The molten fluid caustic is also a disagreeable if not a dangerous product to handle since its contact with water may create an explosionwith a scattering of caustic through the air and also because its causticity intensifies a burn beyond that due to its heat.
The present invention provides for con-' rial may conveniently be an inert substance having a high melting point which will form with the molten caustic a mixture which is not fluid at the temperature used.
Materials of this character which have been successfully used include ordinary building cement, crushed fire brick, crushed lead blast furnace slag ground commercial fire clay, and sand. suflicient quantity of a material of this character is scattered over the dross preparatoryto its removal and serves to thicken the molten caustic to a pasty mass which may be readily scraped or sklmmedfrom the surface of the bath. By
METHOD OF REFINING META-LS.
Application filed-June 19, -1924. Serial No. 721,125.
the addition of an excess of the refractory materials, the scum or dross may be converted into a practically dry powdery mass which may be scraped from thesurface of the bath. 4
While possibly there may be some chemical action between the caustic and some in-.
gredient of the refractory thickening material, as, for instance, between the causticcaustic in the material used.
Theabove method of removing the caustic and drossed impurities from the molten bath'may be used 1n various methods 1nvolvmg a use of caustic whlch results 1n its presence in a fluid molten state on the surface of the bath and has been applied with marked advantage in a method of removing arsenic from antim'onial lead by treatment with caustic soda which is described and claimed in application No. 678,354, filed Nov. 22, 1923, as a continuation of application No. 579,035, filed August 1, 1922. In
this method caustic soda is added to a bath of the molten alloy at a temperature between 900 degrees and 1000 degrees F. and
is thoroughly stirred into or mixed withthe molten bath, the agitation being continued until the caustic is practically spent, and the dross or scum thus formed is then removed. ;In applying the present invention to this process, the inert stiffening material is added to the scum or dross preparator to its removal and, as above explaine mixes with or absorbs the molten caustic forming therewith and with the dross impurities, a pasty or crusty mass which may be readily removed by scraping or skimming and taking with it prac cally all the fluid caustic without danger and without removal of the metal treated. If the arsenic is removed by successive fractional additions of caustic soda, the addition of the 'refractory thickening material may be omitted until the final treatment and removal of the final skim, since the presence of free caustics on the surface of the bath after eachfof the preliminaryskims will not be detrimental.
The term caustic alkali reagent is intended to include a reagent com risin caustic alkali 'either alone or mixed with other reagents.
What is claimed is':
1. Inn method of refining metals which consists in subjecting molten metal to treatment with a caustic alkali reagent to dross the impurities therein, the addition to the floating dross preparatory to its removal of a material which thickens the fluid caustic therein.
2. In a .method of refining metals comprising subjecting molten metal to treatment with a caustic alkali reagent to dross the impurities therein, adding to the floating' dross an inert material to thicken the molten caustic therein, and removing the non-fluid mixture thus formed.
3. The method of removing molten caustie and drossedimpurities from-the surface of a molten metal which consists in absorbing the fluid caustic by the addition of a thickening material and removing the nonfiuid mixture thus formed.
4 The method of removing arsenic from antimonial .lead which consists in treating the molten metal with caustic soda to dross the arsenic, adding to the dross a material JOHN J. MULLIGAN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US721125A US1594424A (en) | 1924-06-19 | 1924-06-19 | Method of refining metals |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US721125A US1594424A (en) | 1924-06-19 | 1924-06-19 | Method of refining metals |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1594424A true US1594424A (en) | 1926-08-03 |
Family
ID=24896634
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US721125A Expired - Lifetime US1594424A (en) | 1924-06-19 | 1924-06-19 | Method of refining metals |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1594424A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2543041A (en) * | 1949-04-12 | 1951-02-27 | Meyer Metallurg Corp | Process for refining lead and its alloys |
-
1924
- 1924-06-19 US US721125A patent/US1594424A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2543041A (en) * | 1949-04-12 | 1951-02-27 | Meyer Metallurg Corp | Process for refining lead and its alloys |
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