US1551615A - Process of reducing alumina - Google Patents
Process of reducing alumina Download PDFInfo
- Publication number
- US1551615A US1551615A US758865A US75886524A US1551615A US 1551615 A US1551615 A US 1551615A US 758865 A US758865 A US 758865A US 75886524 A US75886524 A US 75886524A US 1551615 A US1551615 A US 1551615A
- Authority
- US
- United States
- Prior art keywords
- furnace
- sodium
- aluminum
- alkali metal
- vapor
- 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
- 238000000034 method Methods 0.000 title description 12
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 13
- 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 10
- 229910052783 alkali metal Inorganic materials 0.000 description 9
- 229910052708 sodium Inorganic materials 0.000 description 9
- 239000011734 sodium Substances 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 150000001340 alkali metals Chemical class 0.000 description 5
- -1 alkali metal salt Chemical class 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 230000004927 fusion Effects 0.000 description 4
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 3
- 229910001948 sodium oxide Inorganic materials 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 241000692870 Inachis io Species 0.000 description 1
- 241000283986 Lepus Species 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- ANBBXQWFNXMHLD-UHFFFAOYSA-N aluminum;sodium;oxygen(2-) Chemical compound [O-2].[O-2].[Na+].[Al+3] ANBBXQWFNXMHLD-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L sodium carbonate Substances [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 150000003388 sodium compounds Chemical class 0.000 description 1
- MBEGFNBBAVRKLK-UHFFFAOYSA-N sodium;iminomethylideneazanide Chemical compound [Na+].[NH-]C#N MBEGFNBBAVRKLK-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
- C22B21/00—Obtaining aluminium
- C22B21/04—Obtaining aluminium with alkali metals earth alkali metals included
Definitions
- This invention relates to a process for making metallic aluminum in a blast furnace, and has for its object to producethis metal in a manner more expeditious and less (postly than has been heretofore propose With these objects in view, the invention consists in the novel steps and combinations of steps more fully hereinafter disclosed and particularly pointed out in the claims.
- the furnace charge consists of coke or charcoal alumina and a commercial oxygen containing alkali metal salt, such as a carbonate or aluminate of Application filed December 30, 1924. Serial No. 758,865.
- reaction zone of the furnace in an atmosphere positively devoid of free oxygen or carbon dioxide, and a bed of white hot free carbon is constantly maintained in a localized fusion zone.
- the alkali metal salt which for example may be sodium or potassium carbonate, is decomposed substantially as follows If sodium aluminate is employed as the salt-of sodium, the reaction becomes Elemental sodium is not exclusively pro pokerd however, as under the conditions of the reaction, more or less sodium carbide, Na C, and sodium cyanamid, Na CN,, are
- the deposited sodium oxide is carried down with the furnace burden, to the hot localizel fusion zone of the furnace, where the reactions are repeated, thus constituting a cycle, and in consequence the vapor of such metallic sodlum and sodium compounds m the high temperature zone of the furnace becomes increasingly concentrated, until the partial pressure of such vapor becomes such
- the furnace charge then begins to produce metallic aluminum, and sodium oxide. But this oxide is reduced as fast as it is formed, and the cycle continues Without the addition of any more of the initial alkali metal salt than is necessary to compensate for operating losses.
- the furnace burden will be so proportioned as will accomplish a smelting of the particular compounds used. Also it will be understood that the top temperatures will be maintained sufficiently low to effect 'a condensation of the sublimate on the charge material and thus prevent the escape of the,
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Sept. 1, 1925.
UNITED STATES PATENT OFFICE.
CHARLES E. PARSONS, OF NEW YORK, N. Y., AND SAMUEL PEACOCK, OF WHEELING,
WEST VIRGINIA, ASSIGNORS T0 METAL RESEARCH CORPORATION, OF NEW YORK,
N. Y., A CORPORATION OF DELAWARE.
PROCESS OF REDUCING ALUMINA.
No Drawing.
To all whom it may concern:
Be it known that we, CHAR ES E. PansoNs, a citizen of the United States, residing at New York, in the county of New York and State of New York, and SAMUEL PEA- COCK, a citizen of the United States, residing at Wheeling, in the county of Ohio and State ofWest Virginia, have invented certain new and useful Improvements in Processes of Reducing Alumina; and we do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to a process for making metallic aluminum in a blast furnace, and has for its object to producethis metal in a manner more expeditious and less (postly than has been heretofore propose With these objects in view, the invention consists in the novel steps and combinations of steps more fully hereinafter disclosed and particularly pointed out in the claims.
It is well known that all efforts to reduce aluminum oxide (A1 0 by carbon in -a fuel fed furnace have heretofore been failures largely due'to the fact that the reaction,
is strongly endothermic, and therefore absorbs such a quantity of heat that the reacting constituents are cooled so rapidly below their reacting temperatures that a commercial process has never been attained. This process, on the other hand, avoids the above objection by dividing the reducing hase into two different procedures. That is, an intermediate reactionis employed by means of which the energy consumed is divided into two different reducing eflects either of which can be re lated by means readily available, and each,of which can be carried out in periods of time sufiiciently short to be commercially feasible.
In carrying out this process, an ordinary blast furnace of the type used in iron smelting, is employed. The furnace charge consists of coke or charcoal alumina and a commercial oxygen containing alkali metal salt, such as a carbonate or aluminate of Application filed December 30, 1924. Serial No. 758,865.
reaction zone of the furnace, in an atmosphere positively devoid of free oxygen or carbon dioxide, and a bed of white hot free carbon is constantly maintained in a localized fusion zone.
Under such conditions the alkali metal salt, which for example may be sodium or potassium carbonate, is decomposed substantially as follows If sodium aluminate is employed as the salt-of sodium, the reaction becomes Elemental sodium is not exclusively pro duced however, as under the conditions of the reaction, more or less sodium carbide, Na C, and sodium cyanamid, Na CN,, are
also formed. These products sublime in the furnace when formed in the high temperature zone thereof, and together with the elemental sodium, rise with the gaseous reaction products until they reach the upper part of the shaft, at a temperature of about 600 (1, when they are condensed upon the relatively cool furnace burden, and are' more or less oxidized by the. interaction of the combustion gases, substantially in accordance'with the following equations:
The deposited sodium oxide is carried down with the furnace burden, to the hot localizel fusion zone of the furnace, where the reactions are repeated, thus constituting a cycle, and in consequence the vapor of such metallic sodlum and sodium compounds m the high temperature zone of the furnace becomes increasingly concentrated, until the partial pressure of such vapor becomes such When the sodium, and sodium salts thus produced in the furnace become concentrated cumulatively in the high temperature zone, after the full cycle of reactions is established, the furnace charge then begins to produce metallic aluminum, and sodium oxide. But this oxide is reduced as fast as it is formed, and the cycle continues Without the addition of any more of the initial alkali metal salt than is necessary to compensate for operating losses.
Of course, since various alkali-aluminum compounds may be employed in this process, the furnace burden will be so proportioned as will accomplish a smelting of the particular compounds used. Also it will be understood that the top temperatures will be maintained sufficiently low to effect 'a condensation of the sublimate on the charge material and thus prevent the escape of the,
same.
What is claimed is 1. The process of producing metallic aluminum in a fuel-fed furnace which consists in providing a charge containing carbon, a sodium oxide producing salt, and alumina; igniting said charge to reduce the sodium salt in said furnace continuing the operation until said sodium attacks said aluminum oxemme ide to produce metallic aluminum; and recovering the latter,
2. The process of producing metallic aluminum in a fuel-fed furnace which consists in providing a charge containing carbon, an alkali metal producing salt, and alumina; igniting said charge to reduce the alkali metal salt in said furnace; continuing the operation until said alkali metal attacks said aluminum oxide to produce metallic aluminum; and recovering the latter.
3. The process of producing metallic aluminum in a blast furnace which consists in providing a furnace charge containing carbon, and sodium and aluminum combined with oxygen; maintaining free carbon and a reducing atmosphere in the fusion zone of said furnace to cause said sodium to be liberated in the form of vapor, maintaining a top temperature low enough to cause said vapor to condense on the down coming charge material; continuing the operation until the sodium vapor is sufficiently superheated to reduce said aluminum oxide; and segregating out the metallic aluminum thus formed.
4. The process of producing metallic aluminum in a blast furnace which consists'in providing a furnace charge containing carbon, and an alkali metal and aluminum combined with oxygen; maintaining free carbon and a reducing atmosphere in the fusion zone of said furnace to cause said alkali metal to be liberated in the form of vapor, maintaining a top temperature low enough to cause said vapor to condense on the down coming charge material; continuing the operation until the alkali metal metal vapor is sufiiciently superheated to reduce said aluminum oxide; and segregating out the metallic aluminum thus formed.
In testimony whereof we afiix our signatures.
CHARLES E. PARSONS. SAMUEL PEACOGK.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US758865A US1551615A (en) | 1924-12-30 | 1924-12-30 | Process of reducing alumina |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US758865A US1551615A (en) | 1924-12-30 | 1924-12-30 | Process of reducing alumina |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1551615A true US1551615A (en) | 1925-09-01 |
Family
ID=25053391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US758865A Expired - Lifetime US1551615A (en) | 1924-12-30 | 1924-12-30 | Process of reducing alumina |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1551615A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3009778A (en) * | 1956-07-31 | 1961-11-21 | Pechiney Prod Chimiques Sa | Alumina manufacture in low-stack blast furnace |
| US3661562A (en) * | 1970-12-07 | 1972-05-09 | Ethyl Corp | Reactor and method of making aluminum-silicon alloys |
| US3661561A (en) * | 1970-08-03 | 1972-05-09 | Ethyl Corp | Method of making aluminum-silicon alloys |
-
1924
- 1924-12-30 US US758865A patent/US1551615A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3009778A (en) * | 1956-07-31 | 1961-11-21 | Pechiney Prod Chimiques Sa | Alumina manufacture in low-stack blast furnace |
| US3661561A (en) * | 1970-08-03 | 1972-05-09 | Ethyl Corp | Method of making aluminum-silicon alloys |
| US3661562A (en) * | 1970-12-07 | 1972-05-09 | Ethyl Corp | Reactor and method of making aluminum-silicon alloys |
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