US692688A - Apparatus for producing fluorin. - Google Patents

Apparatus for producing fluorin. Download PDF

Info

Publication number
US692688A
US692688A US3609300A US1900036093A US692688A US 692688 A US692688 A US 692688A US 3609300 A US3609300 A US 3609300A US 1900036093 A US1900036093 A US 1900036093A US 692688 A US692688 A US 692688A
Authority
US
United States
Prior art keywords
anode
fluorin
electrolyte
cell
walls
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
US3609300A
Inventor
Maurice Meslans
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to US3609300A priority Critical patent/US692688A/en
Application granted granted Critical
Publication of US692688A publication Critical patent/US692688A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/16Electric current supply devices, e.g. bus bars

Definitions

  • My invention enables this gas to be conveyed out of the apparatus, only allowing it to encounter metallic walls, o n which it has no action or onlya temporary action, the substance formed protecting the real casing, as will be hereinafter explained.'
  • I utilize materials having as a base organic products.
  • I employ for separating the anode and cathode spaces, and consequently the hydrogen gas and fluorin, a box having walls of copper containing the anode.
  • This cell or box is connected with the positivepole, and its walls are coated from the commencement of the electrolysis with a layer of fluorid of copper, forming a bad conducting covering, which enables them to act in an absolutely indierent manner.
  • Figures l and 2 are vertical, longitudinal, and transverse sections, respectively, of an apparatus for production on a large scale.
  • Fig. 3 also shows aver-tical section of an apparatus of the same kindfor production on a smaller scale.
  • ct is a metallic vessel constituting the cathode-cell and containing the electrolyte, a mixture of anhydrous hydrofluoric acid and a metallic fluorid. It is closed by a lid b with a joint p of materials having organic products as a base.
  • caoutchouc for the insulating -joints
  • anhydrous hydrofluoric acid containing about twenty-five per cent. of fluorhydra-te or fluorid of potassium.
  • a suitable number of anode-cells d are arranged, placed parallel to one another, and the cathode-space contained between the two receptacles d is divided into two parts by intermediate walls or partitions.
  • c indicates the cathodes, and e the anodes.
  • the cells d are supported by two tubes g and Z in communication with the anode-cell and connected with the positive pole. They are mounted on the lid b and electrically insulated from this latter by Washers j of material having a base oforganic substance forming a tight joint.
  • the tube g serves for the diswhich is usually closed by a screw-stopper Z', serves when the generation is stopped for expelling the ijluorin before opening the apparatus.
  • a third tube t' also mounted on the lid b, communicates with the cathode-cell and serves for discharging the hydrogen.
  • the cathodes c are connected with the negative pole by the walls of the receptacle a, and the current is brought to the anodes e by the pipes g and Z and by the walls of the anode'- cell, which are of suitably-selected metal, as is hereinbet'ore specified.
  • the cells cl above the level of the electrolyte are closed boxes, except at the outlets g, while below the level of the electrolyte the side walls of the cells consist of thin strips d of a V-section arranged one beneath the other, the opening turned upward and fixed on the end walls. This arrangement assists in maintaining the separation of the gases and offers little resistance to the passage of the current.
  • the whole apparatus may be immersed in a refrigcrating-tank, and a current of refrigerating liquid may be created in the hollow boxes e', carrying the anodes, by means of pipes g' and Z2, arranged within the pipes g and Z and communicating with an external reservoir.
  • These pipes which are of the same metal as the anode-cell, also serve to convey electric current to the anode e.
  • FIG. 3 which shows the arrangement for production on a small scale, the same letters are employed for indicating the like parts as in Figs. l and 2.
  • This apparatus comprises only a single anode-cell, the wall of which beneath the level of the electrolyte is simply provided at d with perforations of any suitable dimensions; but above the level of the electrolyte the cell is closed, except at the pipe g.
  • the apparatus is immersed in a refrigeratingtank m and is supported by an ebonite plate o. It is surmounted by a refrigerator u, in which the pipes g and 1l coil spirally before emerging from the apparatus.
  • the object of this arrangement is to avoid the carrying off of hydrofluoric acid by condensing it, so that it falls back in liquid form into the apparatus.
  • This arrangement of a condensing-refrigerator is applicable to the different forms of the apparatus whether large or small.
  • the small apparatus does not pos sess a pipe for expelling the iiuorin after each operation.
  • this latter is constructed as a ring fitted on a tube e2, firmly attached to the cover b and in which the liquid contained in the refrigerator il, can circulate.
  • An apparatus for the manufacture of fluorin by electrolysis and provided with a partition wholly of metal separating the anode and cathode cells, and having openings through it only below the normal level of the electrolyte, said partition being electrically connected with the anode and being of a metal having the described property of forming on its surface a layer of insulating fluorid, all substantially as set forth.
  • An apparatus for the manufacture of liuorin by electrolysis and provided with a copper partition separating the anode and cathode cells, said partition being electrically connected with the anode and having openings below the normal level of the electrolyte but being imperforate above, all as and for the purpose described.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

Patented Feb. 4, |902.
M. MEsL'ANs. APPARATUS FUR PBUDUCING FLUURIN.
(Application Bled Nov. 10, 1900.)
(No liludenf4 (lx/ef MesL/INS WITNESSES UNITED STATES PATENT OFFICE.
MAURICE MESLANS, OF PARIS, FRANCE.
APPARATUS l-IOR PRODUCING FLUOR|N.
SPECIFICATION formingpart of Letters Patent No. 692,688, dated February 4, 1902. Application filed November 10. 1900. Serial No. 36.093. (No model.)
To all whom it may' concern: j
Be it known that I, MAURICE MEsLANs, Va citizen of` the Republic of France, and a resident of Paris, France, have invented an Im?" proved Apparatus for Producing Fluorin, ofv Whiclr'the following is a full, clear, and exact The present invention relates to an appa ratus which enables fluorin to be made on an industrial scale. 1
The manufacture of fluorin presents three serious difcultieswhich must be overcome. These difficulties consist, first, in the action of hydroiluoric acid and fluorin on the joints intended to insure the tightness of the apparatus and on the insulating Washers or fittings in the case `of electrical apparatus second, in the phenomenon of counter-electrolysis due to the metallic partitions or Walls of the apparatus, and, third, inthe great resistance of the layer of electrolyte in a U-shaped tube. As regards the first difficulty, the action of hydroiiuoric acid necessitates the exclusion of insulating mineral products, with the exception of tiuor-spar,which itself disintegrates rapidly, while the action of iluorin necessitates the exclusion of products having an inorganic base, such as sulfur and the like. In order to overcome this difficulty, I have con-` structed my apparatus with a view to dispensing with the presence of insulating parts and joints in the anode-cell, where the iiuorin is formed. My invention enables this gas to be conveyed out of the apparatus, only allowing it to encounter metallic walls, o n which it has no action or onlya temporary action, the substance formed protecting the real casing, as will be hereinafter explained.' For the joints of the cathode-cell, `where thevapors of hydrotiuoric acid are formed, I utilize materials having as a base organic products.
With the object of avoiding the effects of counter-electrolysis, which diminish the yield of fluorin, I employ for separating the anode and cathode spaces, and consequently the hydrogen gas and fluorin, a box having walls of copper containing the anode. This cell or box is connected with the positivepole, and its walls are coated from the commencement of the electrolysis with a layer of fluorid of copper, forming a bad conducting covering, which enables them to act in an absolutely indierent manner.
Naturally any other suitable metal having the property which has just been mentioned the electrodes and by the diminution of the j thickness of the layer of electrolyte which the current has to traverse.
In the accompanying drawings, Figures l and 2 are vertical, longitudinal, and transverse sections, respectively, of an apparatus for production on a large scale. Fig. 3 also shows aver-tical section of an apparatus of the same kindfor production on a smaller scale.
In Figs. l and 2, ct is a metallic vessel constituting the cathode-cell and containing the electrolyte, a mixture of anhydrous hydrofluoric acid and a metallic fluorid. It is closed by a lid b with a joint p of materials having organic products as a base. I prefer to employ caoutchouc for the insulating -joints For the electrolyte I prefer anhydrous hydrofluoric acid containing about twenty-five per cent. of fluorhydra-te or fluorid of potassium. In the receptacle a a suitable number of anode-cells d are arranged, placed parallel to one another, and the cathode-space contained between the two receptacles d is divided into two parts by intermediate walls or partitions. c indicates the cathodes, and e the anodes. The cells d are supported by two tubes g and Z in communication with the anode-cell and connected with the positive pole. They are mounted on the lid b and electrically insulated from this latter by Washers j of material having a base oforganic substance forming a tight joint.
charge of the iiuorin formed, and the other, Z,
IDO
The tube g serves for the diswhich is usually closed by a screw-stopper Z', serves when the generation is stopped for expelling the ijluorin before opening the apparatus. A third tube t', also mounted on the lid b, communicates with the cathode-cell and serves for discharging the hydrogen. The cathodes c are connected with the negative pole by the walls of the receptacle a, and the current is brought to the anodes e by the pipes g and Z and by the walls of the anode'- cell, which are of suitably-selected metal, as is hereinbet'ore specified. The cells cl above the level of the electrolyte are closed boxes, except at the outlets g, while below the level of the electrolyte the side walls of the cells consist of thin strips d of a V-section arranged one beneath the other, the opening turned upward and fixed on the end walls. This arrangement assists in maintaining the separation of the gases and offers little resistance to the passage of the current.
Vith the object ot' cooling tbe electrodes the whole apparatus may be immersed in a refrigcrating-tank, and a current of refrigerating liquid may be created in the hollow boxes e', carrying the anodes, by means of pipes g' and Z2, arranged within the pipes g and Z and communicating with an external reservoir. These pipes, which are of the same metal as the anode-cell, also serve to convey electric current to the anode e.
In Fig. 3, which shows the arrangement for production on a small scale, the same letters are employed for indicating the like parts as in Figs. l and 2. This apparatus comprises only a single anode-cell, the wall of which beneath the level of the electrolyte is simply provided at d with perforations of any suitable dimensions; but above the level of the electrolyte the cell is closed, except at the pipe g. The apparatus is immersed in a refrigeratingtank m and is supported by an ebonite plate o. It is surmounted by a refrigerator u, in which the pipes g and 1l coil spirally before emerging from the apparatus. The object of this arrangement is to avoid the carrying off of hydrofluoric acid by condensing it, so that it falls back in liquid form into the apparatus. This arrangement of a condensing-refrigerator is applicable to the different forms of the apparatus whether large or small.
The small apparatus of course does not pos sess a pipe for expelling the iiuorin after each operation.
To cool the anode, this latter is constructed as a ring fitted on a tube e2, firmly attached to the cover b and in which the liquid contained in the refrigerator il, can circulate.
I claim as my inventionl. An apparatus for the manufacture of fluorin by electrolysis and provided with a partition wholly of metal separating the anode and cathode cells, and having openings through it only below the normal level of the electrolyte, said partition being electrically connected with the anode and being of a metal having the described property of forming on its surface a layer of insulating fluorid, all substantially as set forth.
2. An apparatus for the manufacture of liuorin by electrolysis and provided with a copper partition separating the anode and cathode cells, said partition being electrically connected with the anode and having openings below the normal level of the electrolyte but being imperforate above, all as and for the purpose described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
MAURICE MESLANS.
Vitnesses:
JOSEPH DELAGE,
EDWARD P. MACLEAN.
US3609300A 1900-11-10 1900-11-10 Apparatus for producing fluorin. Expired - Lifetime US692688A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US3609300A US692688A (en) 1900-11-10 1900-11-10 Apparatus for producing fluorin.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US3609300A US692688A (en) 1900-11-10 1900-11-10 Apparatus for producing fluorin.

Publications (1)

Publication Number Publication Date
US692688A true US692688A (en) 1902-02-04

Family

ID=2761227

Family Applications (1)

Application Number Title Priority Date Filing Date
US3609300A Expired - Lifetime US692688A (en) 1900-11-10 1900-11-10 Apparatus for producing fluorin.

Country Status (1)

Country Link
US (1) US692688A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2465747A (en) * 1945-04-30 1949-03-29 Rca Corp Apparatus for electroplating metal
US2568844A (en) * 1944-10-14 1951-09-25 Du Pont Process and apparatus for the electrolytic production of fluorine
US2621155A (en) * 1949-10-08 1952-12-09 Du Pont Cathode structure
US2739115A (en) * 1952-06-19 1956-03-20 Pennsylvania Salt Mfg Co Fluorine cell

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2568844A (en) * 1944-10-14 1951-09-25 Du Pont Process and apparatus for the electrolytic production of fluorine
US2465747A (en) * 1945-04-30 1949-03-29 Rca Corp Apparatus for electroplating metal
US2621155A (en) * 1949-10-08 1952-12-09 Du Pont Cathode structure
US2739115A (en) * 1952-06-19 1956-03-20 Pennsylvania Salt Mfg Co Fluorine cell

Similar Documents

Publication Publication Date Title
US692688A (en) Apparatus for producing fluorin.
US368608A (en) peybusson
US3930980A (en) Electrolysis cell
US4059495A (en) Method of electrolyte feeding and recirculation in an electrolysis cell
US2629688A (en) Electrolytic apparatus for production of magnesium
US1074988A (en) Apparatus for electrolysis of fused alkali chlorids.
US1547362A (en) Apparatus for the electrolysis of water
US587437A (en) Ferdinand hurter
US3832300A (en) Bipolar diaphragm electrolyzer with cathode waves in horizontal plane
US984905A (en) Process and apparatus for the electrolytic decomposition of alkaline salts.
US2154830A (en) Electrolytic cell
NO141759B (en) ANALOGY PROCEDURE FOR THE PREPARATION OF THERAPEUTICALLY EFFECTIVE PENICILLINES
US666387A (en) Apparatus for producing alkali, electricity, and hydrogen from alkali-metal amalgam.
US712218A (en) Electrolytic cell.
US1485461A (en) Electrolytic cell
US1296046A (en) Electrolytic cell.
US2624703A (en) Electrolytic fluorine cell
US1185407A (en) Electrolytic cell.
US4107006A (en) Electrolysis cell
US512266A (en) Emile andreoli
US1186937A (en) Electrolytic apparatus.
US2370086A (en) Electrolytic alkali halogen cells
US826435A (en) Extracting metals by electrolytic means from ores.
US612009A (en) Giovanni battista baldo
US1720995A (en) Electrolytic cell