US2693445A - Electrolytic method for production of fluorine - Google Patents

Electrolytic method for production of fluorine Download PDF

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Publication number
US2693445A
US2693445A US115456A US11545649A US2693445A US 2693445 A US2693445 A US 2693445A US 115456 A US115456 A US 115456A US 11545649 A US11545649 A US 11545649A US 2693445 A US2693445 A US 2693445A
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United States
Prior art keywords
carbon
fluorine
anode
permeability
electrolyte
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Expired - Lifetime
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US115456A
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English (en)
Inventor
Howell William Norman
Hill Harold
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.)
Imperial Chemical Industries Ltd
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Imperial Chemical Industries Ltd
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/24Halogens or compounds thereof
    • C25B1/245Fluorine; Compounds thereof

Definitions

  • a process for the production of fluorine comprises the electrolysis of substantially drv fused fluorides e. g. of the approximate composition KF.2HF, using as the anode a carbon of permeability not less than 5.
  • a cell suitable for carryin out the invention is shown in the attached drawin which represents a vertical section through the s id cell.
  • Ref rring to the drawing, 1 is a container of mild steel or other suitablv resistant material this container being closed by a lid 2 of similar material.
  • the anode 3 is of carbon of the required per Patented Nov. 2, 1954 meability and is supported by an electrically-conducting rod 6 which passes through the lid 2 and is insulated therefrom by an insulator 4.
  • the said anode is only partially immersed in the electrolyte 9 as illustrated by the drawing.
  • the cathode 5 At a distance from the anode, and wholly or partially surrounding it, is the cathode 5, which may be of mild steel, copper or other material substantially resistant to the electrolyte and products of electrolysis.
  • the cathode is supported by an electrically-conducting rod 7, which rod is insulated from the cell lid through which it passes. Between the anode and cathode is a diaphragm or skirt 8 which depends from the cell lid and dips into the electrolyte 9, thus serving to keep separate the gases evolved at the electrodes. Exits 10 and 11 through the cell lid are provided for the fluorine and hydrogen evolved at the anode and cathode respectively. Heating means not shown are also provided.
  • Example A cell of the kind described was fitted with an anode 13 /2 x 13 /2" x 3" constructed of carbon of permeability 37.5.
  • the electrolyte was of the approximate composition KF.2HF and contained initially less than 0.5% of water.
  • the electrolysis was warmed to about 75 C. and throughout operation was maintained between this temperature and C.
  • the electrolysis was continued for 3,000 hours during which time the HF content of the electrolyte was maintained between 40% and 42% by periodic additions of anhydrous hydrogen fluoride. At the end of 3,000 hours the cell was still giving fluorine of excellent quality and there was no indication of polarisation.
  • a process for the production of fluorine comprising electrolyzing substantially dry mixtures of fused fluorides of the approximate composition KF.2HF, the said electrolysis being effected in a container of suitably resistant material between a cathode of material resistant to the action of the electrolyte, and an anode of porous carbon only partially immersed in said electrolyte, said carbon having a permeability of not less than 5, the unit of permeability being expressed in terms of the number of cubic feet of air which can be passed per square foot of surface through one inch thickness of the carbon per minute under an imposed pressure of two inches of water and removing the generated fluorine from the space above the anode.
  • a process for the production of fluorine comprising electrolyzing in a suitable container substantially dry fused mixtures of fluorides of the approximate composition KF.2HF, the cathode being of material resistant to the action of the electrolyte and the anode being only partially immersed in the said electrolyte and being of carbon of permeability greater than 20, the unit of permeability being expressed in terms of the number of cubic feet of air which can be passed per square foot of surface through a one inch thickness of the carbon per minute under an imposed pressure of two inches of water and removing the generated fluorine from the space above the anode.
US115456A 1948-09-27 1949-09-13 Electrolytic method for production of fluorine Expired - Lifetime US2693445A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB25149/48A GB655098A (en) 1948-09-27 1948-09-27 Improvements in or relating to electrolysis of fluorine salts

Publications (1)

Publication Number Publication Date
US2693445A true US2693445A (en) 1954-11-02

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Family Applications (1)

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US115456A Expired - Lifetime US2693445A (en) 1948-09-27 1949-09-13 Electrolytic method for production of fluorine

Country Status (5)

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US (1) US2693445A (de)
AT (1) AT167844B (de)
DE (1) DE846993C (de)
FR (1) FR996272A (de)
GB (1) GB655098A (de)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2996446A (en) * 1958-01-06 1961-08-15 Ici Ltd Apparatus for the electrolytic production of fluorine
US3000801A (en) * 1958-07-30 1961-09-19 Ici Ltd Process for the electrolytic production of fluorine
US3033767A (en) * 1958-09-02 1962-05-08 Dow Chemical Co Preparation of fluorocarbons
US3320140A (en) * 1963-12-13 1967-05-16 Allied Chem Electrolytic production of fluorine
US4511440A (en) * 1983-12-22 1985-04-16 Allied Corporation Process for the electrolytic production of fluorine and novel cell therefor
CN104532289A (zh) * 2015-01-07 2015-04-22 黎明化工研究设计院有限责任公司 一种电解制氟用阳极

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5623285A (en) * 1979-08-02 1981-03-05 Nobuatsu Watanabe Production of fluorine

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1309148A (en) * 1919-07-08 mighbi
US2194443A (en) * 1937-10-04 1940-03-19 Du Pont Anode for electrolytic cells
US2506438A (en) * 1946-05-14 1950-05-02 Atomic Energy Commission Electrolytic process for production of fluorine
US2540960A (en) * 1946-06-03 1951-02-06 Sidney G Osborne Electrolytic cell
US2592144A (en) * 1948-05-14 1952-04-08 Ici Ltd Process for the electrolytic production of fluorine

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1309148A (en) * 1919-07-08 mighbi
US2194443A (en) * 1937-10-04 1940-03-19 Du Pont Anode for electrolytic cells
US2506438A (en) * 1946-05-14 1950-05-02 Atomic Energy Commission Electrolytic process for production of fluorine
US2540960A (en) * 1946-06-03 1951-02-06 Sidney G Osborne Electrolytic cell
US2592144A (en) * 1948-05-14 1952-04-08 Ici Ltd Process for the electrolytic production of fluorine

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2996446A (en) * 1958-01-06 1961-08-15 Ici Ltd Apparatus for the electrolytic production of fluorine
US3000801A (en) * 1958-07-30 1961-09-19 Ici Ltd Process for the electrolytic production of fluorine
US3033767A (en) * 1958-09-02 1962-05-08 Dow Chemical Co Preparation of fluorocarbons
US3320140A (en) * 1963-12-13 1967-05-16 Allied Chem Electrolytic production of fluorine
US4511440A (en) * 1983-12-22 1985-04-16 Allied Corporation Process for the electrolytic production of fluorine and novel cell therefor
CN104532289A (zh) * 2015-01-07 2015-04-22 黎明化工研究设计院有限责任公司 一种电解制氟用阳极

Also Published As

Publication number Publication date
AT167844B (de) 1951-03-10
GB655098A (en) 1951-07-11
FR996272A (fr) 1951-12-17
DE846993C (de) 1952-08-18

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