US1197137A - Method of reducing metals. - Google Patents

Method of reducing metals. Download PDF

Info

Publication number
US1197137A
US1197137A US73971013A US1913739710A US1197137A US 1197137 A US1197137 A US 1197137A US 73971013 A US73971013 A US 73971013A US 1913739710 A US1913739710 A US 1913739710A US 1197137 A US1197137 A US 1197137A
Authority
US
United States
Prior art keywords
sodium
pressure
compounds
electrolyte
metals
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
Application number
US73971013A
Inventor
Robert J Mcnitt
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Roessler and Hasslacher Chemical Co
Original Assignee
Roessler and Hasslacher Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Roessler and Hasslacher Chemical Co filed Critical Roessler and Hasslacher Chemical Co
Priority to US73971013A priority Critical patent/US1197137A/en
Priority to US27474A priority patent/US1214808A/en
Application granted granted Critical
Publication of US1197137A publication Critical patent/US1197137A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00Electrolytic production of organic compounds
    • C25B3/20Processes
    • C25B3/23Oxidation

Definitions

  • a method of reducing metallic sodium from its compounds by electrolysis consisting in raising the boiling point of the sodium by pressure of a gas generated by and compressed during the reduction process, on the molten electrolyte while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure.

Description

R. J. McNITT.
METHOD OF REDUCING METALS.
APPLICATION FILED JAN. 2. 1913.
Patented Sept. 5, 1916.
wmma INVENTOR.
WITNESSES W Lr I? 017W t1 ti ROBERT J. MGNITT, OF PERTH AIVIBOY, NEW JERSEY, ASSIGNOR TO THE ROESSLER, & HASSLACHER CHEMICAL (30., OF NEW YORK, Y., A CORPORATION OF NEW YORK.
Mn'rnon or REDUCING METALS.
mower.
Application filed January 2, 1913.
To all whom it may concern Be it known that 1, ROBERT J. MoNrr'r, a citizen of the United States of America, residing at Perth Amboy, Middlese-x county, New Jersey, have invented a certain new and useful Method of Reducing Metals, of which the following is aspecification.
My invention relates to a new and useful method of reducing metals from compounds containing the same and it refers particularly to the reduction of metals from their compounds by electrolyzing the same under pressure.
The reduction of metals by electrolysis has been long practised by many processes, but in all cases the electrolysis has been carried on under pressures substantially equal to the atmospheric pressure. Now I have found that by carrying on the electrolysis under greater pressures than atmospheric pressure, the reduction is more complete and results in more economical separation.
Furthermore, whereas it has been found impossible to continuously and. economically reduce many metals by electrolysis by the processes and apparatus heretofore proposed. l have found that by the practice of my invention this may be most satisfactorily accomplished.
I By way of illustrating my invention, I may cite as an example, the reduction of metallic sodium from molten sodium chlorid by electrolysis under pressure. Among those familiar with this art it is considered to be impossible to separate metallic sodium from molten sodium chlorid at temperatures in the neighborhood of the melting point of this compound which is in the vicinity of the boiling point of sodium, so that the high volatility of the sodium metal at the former temperature gives ,rise to various difiicillties. I find however that by carrying on electrolysis under a pressure of 900 mm. mercury, while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure, the boiling point of the liberated metal is raised approximately 100 C. and thelatter may be easily collected. i
I shall-explain my invention in connection with the accompanying drawing, which is a vertical longitudinal section showing in rather a diagrammatic way one form of elec trical apparatus suitable for the purpose.
A indicates an anode of graphite or other Specification of Letters Patent.
I Patented Sept. 5, 1916..
Serial No. 739,710.
suitable material which is electrically connected with conductors B extending through the external walls of the furnace. A cathode C, of any suitable material, is shown as connected on its lower side with a conductor D extending through the bottom of the furnace. The walls of the furnace are shown as formed of steel-plates E lined on the inside with a thin layer of asbestos F and the remaining spacebetween said walls and the rear sides of the electrodes and above the anodes is filled with a suitable material such as brickworlLG preferably fire clay brick. The working chamber of the furnace extends from the bottom X up to cover H.
Z indicates a bell of any suitable material, shown as somewhat larger in its lateral extension than cathode C.
K represents a diaphragm of perforated metal, extending downward from the lower rim of the bell Z and hanging between the anode and cathode surfaces.
The lower rim of bell Z is shown as terminating a short distance from the upper edge of the cathode C.
Z indicates a tube connected to the upper part of bell Z and passing through a cover H. Tube Z is connected by pipe L with pipe M, provided with a valve M. A pipe N is shown as branching off from tube Z and connecting to a vessel 0, provided with a Valve 0'. vessel 0 serving as a receiver.
A pipe P, provided with a valve P, conducts away the gases generated in the process and another pipe Q, of suitable diameter and provided with a suitable cover, serves for charging the metallic compound, as for instance sodium chlorid, into the furnace. A pressure gage R, carried by the cover H, serves for indicating the pressure exerted on the contents of the furnace.
lln carrying out my method of reducing metals from their compounds by electrolyzing the same under pressure I prefer to charge the apparatus, described above, with molten sodium chlorid until it approximately reaches somewhat below branchpipe N so that the lower .ends of both pipes M and Q are submerged somewhat in the liquid electrolyte. Immediately after charging in the molten sodium-chlorid I open valve M and admit some inert gas, such as producer gas, through pipes M and L in such quantities as to exert pressure on the electrolyte within the working chamber and I then pass the electric current through the furnace to start the electrolysis for the reduction of the sodium metal at the cathode C, Valve P is then opened just enough to throttle the escaping chlorin gas thus maintaining the pressure exerted on the electrolyte. It is obvious that the chlorin will pass freely through the electrolyte and out through pipe P and valve P, whereas the path of the sodium, after being separated at the cathode, is so directed that the sodium rises and is collected within bell Z. As the continuous electrolysis constantly increases the volume of the metallic sodium within the bell, owing to the difi'erence in the specific gravity of the respective liquids, the sodium rises in the bell and finally overflows through pipe N into receiver 0.
It is obvious many changes may be made in the process described above without departing from the spirit of my invention; one such change, for instance, consists in carrying on the electrolysis under the hydrostatic pressure due to a high column of fluid which may consist in part or whole of the molten electrolytic compounds, instead of creating the pressure by means of gases. Such change constitutes only one illustrative modification of the method described and comes within the scope of my invention, inasmuch as it does not bring about a change of material conditions in regard to the chemical or physical sides of the invention. It is further obvious that many other changes may be made, as for instance charging the metallic compound in a solid instead of in a molten state; modifying the form and construction of the bell Z as to allow the introduction of cathode C and its conductor D from the top instead of through the bottom or making other changes in the relative position of the electrodes without in the least interfering with the working of the process as described.
The application of gas for exerting pressure on the electrolyte makes it essential that the gas fulfil certain conditions; first of all any gas used as an auxiliary should be reasonably dry; it is desirable furthermore that it be inert as well to the chlorin gas as to the metal separated at the cathode.
I Wish also to state that the electric furnace may be built in either square or round shape and that the various material parts as for instance the electrodes, may most readily be adapted to fit eithershape. The apparatus described is one of the forms which is well suited for the reduction of metallic sodium from its compounds, preferably sodium chlorid, said reduction of metallic sodium being heredescribed simply as an example of my method of reducing metals.
The apparatus is'not claimed in connection with this application, as I reserve the same as the subject-matter of another application for patent to be hereafter filed.
What I claim and desire to secure by Letters Patent is: l. A method of reducing metallic compounds to their metals by electrolysis consisting in raising the boiling point of said metals by pressure on the molten electrolyte while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure.
2. A method of reducing metallic compounds to their metals by electrolysis consisting in raising the boiling point of said metals by pressure of a compressed gas on the molten electrolyte while maintaining the temperature of the electrolyte below its boil ing point at atmospheric pressure.
3. A method of reducing metallic compounds to their metals by electrolysis consisting in applying pressure to the metallic compounds forming the electrolyte, by means of compressed inert gas and then electrolyzing the metallic compounds while under pressure.
i. A method of reducing metallic compounds to their metals by electrolysis consisting in raising the boiling point of said metals by pressure of a gas generated by and compressed during the reduction process, on the molten electrolyte while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure.
5. A method of reducing metallic compounds to their metals by electrolysis con sisting in exerting pressure on the metallic compounds forming the electrolyte, by means of both a compressed inert gas admitted to the furnace and a gas generated by and compressed duringthe reduction process and then electrolyzing the metallic compounds while under pressure.
6. A method of reducing metallic compounds to their metals by electrolysis consisting in providing in an electrolytic chamber said metallic compounds in a fluid state, applying pressure to the metallic compounds by means of compressed gas, passing the electric current through the bath of metallic compounds, separating the products generated at the electrodes as desired and controlling the applied pressure by means of gases liberated by the process and gases admitted from without.
7. A method of reducing metallic sodium from its compounds by electrolysis consisting in raising the boiling point of the sodium by pressure on the molten electrolyte while maintaining the ten'iperature of the electrolyte below its boiling point at atmospheric pressure.
8. A method of reducing metallic sodium from its compounds by electrolysis consisting in raising the boiling point of the someme? dium by pressure of a compressed gas on the molten electrolyte while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure.
9. A method of reducing metallic sodium from its compounds by electrolysis consist ing in applying pressure to the sodium compound forming the electrolyte, by means of a compressed inert gas and electrolyzing the sodium compound While under pressure.
10. A method of reducing metallic sodium from its compounds by electrolysis consisting in raising the boiling point of the sodium by pressure of a gas generated by and compressed during the reduction process, on the molten electrolyte while maintaining the temperature of the electrolyte below its boiling point at atmospheric pressure.
11. A method of reducing metallic sodium from its compounds by electrolysis consisting in exerting pressure on the sodium compound forming the electrolyte, by means of both a compressed, inert gas and a gas generated by and compressed during the reduction, and electrolyzing the sodium compound while under pressure.
12. A method of reducing metallic so dium from its compounds by electrolysis consisting in providing in an electrolytic chamber said sodium compounds in a fluid state, applying pressure to the sodium compounds by means of compressed gas, passing the electric current through the bath of the sodium compounds, separating the products generated at the electrodes as desired and controlling the applied pressure by means of gases liberated by the process and gases admitted from without.
In testimony whereof I have signed this specification in the presence of two subscribing witnesses.
v v ROBERT J. MGNITT. Witnesses: I
HERBERT PHILIPP, OTTO K. ZWIN-GENBERGER.
US73971013A 1913-01-02 1913-01-02 Method of reducing metals. Expired - Lifetime US1197137A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US73971013A US1197137A (en) 1913-01-02 1913-01-02 Method of reducing metals.
US27474A US1214808A (en) 1913-01-02 1915-05-12 Method of reducing metals.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US73971013A US1197137A (en) 1913-01-02 1913-01-02 Method of reducing metals.

Publications (1)

Publication Number Publication Date
US1197137A true US1197137A (en) 1916-09-05

Family

ID=3265081

Family Applications (1)

Application Number Title Priority Date Filing Date
US73971013A Expired - Lifetime US1197137A (en) 1913-01-02 1913-01-02 Method of reducing metals.

Country Status (1)

Country Link
US (1) US1197137A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2690421A (en) * 1943-03-06 1954-09-28 William C Lilliendahl Electrolytic production of uranium powder
US2773826A (en) * 1944-02-07 1956-12-11 Norman C Beese Electrolytic apparatus for the recovery of rare refractory metals
US2951021A (en) * 1952-03-28 1960-08-30 Nat Res Corp Electrolytic production of titanium
US3453187A (en) * 1965-09-23 1969-07-01 Timax Associates Apparatus and process for reduction of hydrogen chloride

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2690421A (en) * 1943-03-06 1954-09-28 William C Lilliendahl Electrolytic production of uranium powder
US2773826A (en) * 1944-02-07 1956-12-11 Norman C Beese Electrolytic apparatus for the recovery of rare refractory metals
US2951021A (en) * 1952-03-28 1960-08-30 Nat Res Corp Electrolytic production of titanium
US3453187A (en) * 1965-09-23 1969-07-01 Timax Associates Apparatus and process for reduction of hydrogen chloride

Similar Documents

Publication Publication Date Title
GB880838A (en) Improvements in or relating to electrolytic cells
US1197137A (en) Method of reducing metals.
FR2542326A1 (en) TANK OF ALUMINUM REFINING BY ELECTROLYSIS
US4298587A (en) Silicon purification
US995476A (en) Electrolytic process.
JP2004052003A (en) Method and apparatus for producing niobium powder or tantalum powder
US1214808A (en) Method of reducing metals.
US1299947A (en) Electrolysis of fused electrolytes.
US2073631A (en) Metal recovery
US809089A (en) Process of making caustic alkali.
US2758831A (en) Lined metal reduction apparatus
US2913382A (en) Method for producing metals electrolytically
US1534319A (en) Refining aluminum electrolytically with fused electrolytes
US1567318A (en) Method of making metallic magnesium
US2539743A (en) Electrolytic refining of impure aluminum
US1336281A (en) Process and apparatus for the electrolytic decomposition of chlorids
US4686025A (en) Apparatus for the production of a metal by electrolyzing halides in a molten salt bath, by a simultaneous continuous double deposit
US2291644A (en) Apparatus for electrolysis of fused electrolytes
US984905A (en) Process and apparatus for the electrolytic decomposition of alkaline salts.
US1186937A (en) Electrolytic apparatus.
US735464A (en) Electrolytic diaphragm.
US2904491A (en) Apparatus for producing refractory metal
US830051A (en) Apparatus for the electrolytic extraction of metals.
US1043154A (en) Electrolytic production of light metals.
US715625A (en) Process of obtaining metallic aluminium or other metals by electrolysis.