US1477099A - Anode for forming percompounds - Google Patents

Anode for forming percompounds Download PDF

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Publication number
US1477099A
US1477099A US583665A US58366522A US1477099A US 1477099 A US1477099 A US 1477099A US 583665 A US583665 A US 583665A US 58366522 A US58366522 A US 58366522A US 1477099 A US1477099 A US 1477099A
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Prior art keywords
anode
percompounds
forming
platinum
tantalum
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Expired - Lifetime
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US583665A
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Baum Gustav
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FIRM OF CHEM FAB WEISSENSTEIN
Firm Of Chemische Fabrik Weissenstein G M B H
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FIRM OF CHEM FAB WEISSENSTEIN
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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
    • C25B1/28Per-compounds

Definitions

  • This invention relates to anodes for forming percompounds, said anodes consisting of tantalum o which the surface is only partly provided with -a platinum coating.
  • anodes of pure platinum have been used. Whereas it is sometimes possible to replace platinum cathodes by other metals, for instance, tungsten or tantalum, it had been quite impossible, to use anything but pure platinum as anodes, since the above named metals, as well as any other metal, are either dissolved in the electrolyte or coated with a layer of oxide whereby the circuit is interrupted.
  • anodes of the said construction can also be used for forming percompounds, since-it isea well known fact that the percompounds are especially sensitive to metal ycontaining catalyzers.
  • the exposure of the surface of tantalum, however, either in the metallic or in oxidized condition has not the slightest injurious effeet on the process of formation and on the condition of the percompounds formed.
  • platinum coating on a tantalum base to such an extent that the whole surface of the tantalum is not coated with platinum is in practice Yconsiderably simpler and cheaper than coating the whole tantalum base with the more expensive platinum.
  • The. coating can, either by electrolysis, or by weldin rolling and the like.
  • a designates a base of tantalum, which may be, for instance, 10mm. in breadth, 500 mm. in length, and 0.2 mm. in thic ness. This piece of tantalum is partly ond is used.
  • anode serves as electrolyzing vessel, a porous cylinder of 200 ccm. as diaphragm.
  • the cathode is formed by a lead ⁇ coil which at the same time serves as a cooling device.
  • 150 ccm. of a saturated solution of ammonium sulfate is used as anolyte (anodic liquid) sulfuric acid of 45 B. as catholte; the temperature remains below 18"A
  • the anode is formed of pure platinum the surface of which is about 2 cm2; the current density during the electrolysis amounts to 1 amp/cm2.
  • the output is 96.4%.
  • vanode being of pure platinum and'havi-ng .an area of .5l cm2 being 1 amp/cm2 60.13%.
  • the anode according to my invention is of high commercial value as it is a perfect substitute for pure platinum.
  • An anode for forming pereompounds, consisting of a tantaluln base portion having its ⁇ surface partially coated with platinum.

Description

Dees;l l 1923.
G. BAUM` ANDE FOR FORMING PERCOMPOUNDS Filed Aug. 22 1922 Flai Z'fpurn,
Patented Dec. 11, 1923.
FBBIK WEISSEN STEIN orifice.
or' cnnmscnn G. M. B. H., OF GABINTHIA, AUSTRIA.
NODE ron FonmNG PEaconroUNns.
Application :tiledv August 22, 1922. Serial No. 588,665.
To all 'wiwm z't 'may concern.' i
Be it known that I, GUs'rAv BAUM, a citizen of the Republic of Austria, and residing at Weissenstein ob der Drau, Carinthia, Austria, have invented certain new and useful Improvements in Anodes for Forming Percompounds; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the Aart to which it appertains to make and use the same.
This invention relates to anodes for forming percompounds, said anodes consisting of tantalum o which the surface is only partly provided with -a platinum coating.
or 'making percompounds heretofore, anodes of pure platinum have been used. Whereas it is sometimes possible to replace platinum cathodes by other metals, for instance, tungsten or tantalum, it had been quite impossible, to use anything but pure platinum as anodes, since the above named metals, as well as any other metal, are either dissolved in the electrolyte or coated with a layer of oxide whereby the circuit is interrupted.
I have, however, shown that it is possible to avoid the above mentioned drawback and to obtain suitable anodes for forming percompounds by manufacturing anodes ofl a tantalum base and providin this base with a relatively small surface o? platinum coating which serves for transmitting` the current from the tantalum to the electrolyte.
It is surprising that anodes of the said construction can also be used for forming percompounds, since-it isea well known fact that the percompounds are especially sensitive to metal ycontaining catalyzers. The exposure of the surface of tantalum, however, either in the metallic or in oxidized condition has not the slightest injurious effeet on the process of formation and on the condition of the percompounds formed.
The use of platinum coating on a tantalum base to such an extent that the whole surface of the tantalum is not coated with platinum is in practice Yconsiderably simpler and cheaper than coating the whole tantalum base with the more expensive platinum. The. coating can, either by electrolysis, or by weldin rolling and the like.
t e. accompanying drawings an.` anode hammering,
for example, be eifected -b an anode o tantalum according front view by way of example. l
a designates a base of tantalum, which may be, for instance, 10mm. in breadth, 500 mm. in length, and 0.2 mm. in thic ness. This piece of tantalum is partly ond is used.
Examples.
to the" invention is illustrated in 1. (a.) A cylindrical cell of 600 ccm.
serves as electrolyzing vessel, a porous cylinder of 200 ccm. as diaphragm. The cathode is formed by a lead `coil which at the same time serves as a cooling device. 150 ccm. of a saturated solution of ammonium sulfate is used as anolyte (anodic liquid) sulfuric acid of 45 B. as catholte; the temperature remains below 18"A The anode is formed of pure platinum the surface of which is about 2 cm2; the current density during the electrolysis amounts to 1 amp/cm2. The output is 96.4%.
(b.) The same apparatus is used and the same conditions are maintained, when the platinum anode is substituted by an anode of tantalum, partly coated withplatinum. The output 1s 95%, that is to say the result is practically equal to that obtalned witha platinum anode.
2. (a.) The cylindrical cell, diaphragm 'and lead vcoil are the same as in the above described example. As electrolytev I use sulfuric acid of 45 B., the contents of the anodic cell being 150 ccm. The temperature variesbetween 18 and 20. C. The
vanodebeing of pure platinum and'havi-ng .an area of .5l cm2 being 1 amp/cm2 60.13%.
(b'.)\ If the latinumA anode is substituted partly coated With p atinum and it 4the e' conditions are maintained the output amounts to 60.55%. t
and the current density the output amounts to nos From the above it may be seen that "the anode according to my invention is of high commercial value as it is a perfect substitute for pure platinum.
I claim: l
1. An anode, for forming pereompounds, consisting of a tantaluln base portion having its` surface partially coated with platinum.
2. An anode for forming pereompounds,
consisting of a tantalum base portion having its surface partially covered with a coat: ing of platinum Welded thereto.
In testimony thatfI claim the foregoing as my invention, I have signed my name.
GUSTAV BAUM.
Witnesses:
ING. CHEM. J. RUMPLER, ING. En. Pnos'z.
US583665A 1922-07-07 1922-08-22 Anode for forming percompounds Expired - Lifetime US1477099A (en)

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GB18740/22A GB198246A (en) 1922-07-07 1922-07-07 Anodes for forming percompounds

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DE (1) DE386514C (en)
FR (1) FR552982A (en)
GB (1) GB198246A (en)

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434731A (en) * 1943-11-16 1948-01-20 Baker & Co Inc Platinum sheet electrode
US2795541A (en) * 1951-12-22 1957-06-11 Degussa Electrolytic production of percompounds
US2868711A (en) * 1955-08-10 1959-01-13 Pennsalt Chemicals Corp Electrolytic cell
US2929769A (en) * 1955-07-07 1960-03-22 Isaac L Newell Electroplating anode
US2955999A (en) * 1957-09-04 1960-10-11 Ionics Self-rectifying electrodialysis unit
US2998359A (en) * 1958-11-25 1961-08-29 Engelhard Ind Inc Method for preparing anodes for cathodic protection systems
US3010891A (en) * 1959-04-15 1961-11-28 Engelhard Ind Inc Trailing anode for cathodic protection systems
US3022242A (en) * 1959-01-23 1962-02-20 Engelhard Ind Inc Anode for cathodic protection systems
US3038849A (en) * 1958-10-07 1962-06-12 Herman S Preiser Insoluble trailing anode for cathodic protection of ships
US3055821A (en) * 1960-03-07 1962-09-25 Olin Mathieson Diaphragmless monopolar elecrolytic cell
US3081252A (en) * 1959-09-30 1963-03-12 Chemionics Engineering Lab Inc Pipe plug anode
US3096272A (en) * 1957-10-24 1963-07-02 Amalgamated Curacao Patents Co Noble metal coated titanium electrode and method of making and using it
US3102086A (en) * 1957-07-26 1963-08-27 Ici Ltd Method of improving the corrosion resistance of titanium metals
US3118828A (en) * 1957-07-17 1964-01-21 Ici Ltd Electrode structure with titanium alloy base
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications
US3222270A (en) * 1958-03-18 1965-12-07 Ici Ltd Multi-electrolytic cells
US3236756A (en) * 1957-04-09 1966-02-22 Amalgamated Curacao Patents Co Electrolysis with precious metalcoated titanium anode
US3291714A (en) * 1961-01-13 1966-12-13 Ici Australia Ltd Electrodes
US3313721A (en) * 1958-12-31 1967-04-11 Englehard Ind Inc Dish-shaped anode
US4052271A (en) * 1965-05-12 1977-10-04 Diamond Shamrock Technologies, S.A. Method of making an electrode having a coating containing a platinum metal oxide thereon
US4175021A (en) * 1978-03-06 1979-11-20 C. E. Equipment Co., Inc. Apparatus for preventing end effect in anodes
US4210508A (en) * 1975-12-15 1980-07-01 Gustav Bergson Electrolytic hygrometer improvement
US4401540A (en) * 1980-10-29 1983-08-30 C.E. Equipment Co., Inc. Apparatus for reducing end effect in anodes

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL248510A (en) * 1959-02-18

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434731A (en) * 1943-11-16 1948-01-20 Baker & Co Inc Platinum sheet electrode
US2795541A (en) * 1951-12-22 1957-06-11 Degussa Electrolytic production of percompounds
US2929769A (en) * 1955-07-07 1960-03-22 Isaac L Newell Electroplating anode
US2868711A (en) * 1955-08-10 1959-01-13 Pennsalt Chemicals Corp Electrolytic cell
US3236756A (en) * 1957-04-09 1966-02-22 Amalgamated Curacao Patents Co Electrolysis with precious metalcoated titanium anode
US3278404A (en) * 1957-07-17 1966-10-11 Ici Ltd Method and apparatus for cathodic protection
US3118828A (en) * 1957-07-17 1964-01-21 Ici Ltd Electrode structure with titanium alloy base
US3102086A (en) * 1957-07-26 1963-08-27 Ici Ltd Method of improving the corrosion resistance of titanium metals
US2955999A (en) * 1957-09-04 1960-10-11 Ionics Self-rectifying electrodialysis unit
US3096272A (en) * 1957-10-24 1963-07-02 Amalgamated Curacao Patents Co Noble metal coated titanium electrode and method of making and using it
US3222270A (en) * 1958-03-18 1965-12-07 Ici Ltd Multi-electrolytic cells
US3038849A (en) * 1958-10-07 1962-06-12 Herman S Preiser Insoluble trailing anode for cathodic protection of ships
US2998359A (en) * 1958-11-25 1961-08-29 Engelhard Ind Inc Method for preparing anodes for cathodic protection systems
US3313721A (en) * 1958-12-31 1967-04-11 Englehard Ind Inc Dish-shaped anode
US3022242A (en) * 1959-01-23 1962-02-20 Engelhard Ind Inc Anode for cathodic protection systems
US3133872A (en) * 1959-03-10 1964-05-19 Chemionics Engineering Lab Inc Anode for electrochemical applications
US3010891A (en) * 1959-04-15 1961-11-28 Engelhard Ind Inc Trailing anode for cathodic protection systems
US3081252A (en) * 1959-09-30 1963-03-12 Chemionics Engineering Lab Inc Pipe plug anode
US3055821A (en) * 1960-03-07 1962-09-25 Olin Mathieson Diaphragmless monopolar elecrolytic cell
US3291714A (en) * 1961-01-13 1966-12-13 Ici Australia Ltd Electrodes
US4052271A (en) * 1965-05-12 1977-10-04 Diamond Shamrock Technologies, S.A. Method of making an electrode having a coating containing a platinum metal oxide thereon
US4210508A (en) * 1975-12-15 1980-07-01 Gustav Bergson Electrolytic hygrometer improvement
US4175021A (en) * 1978-03-06 1979-11-20 C. E. Equipment Co., Inc. Apparatus for preventing end effect in anodes
US4401540A (en) * 1980-10-29 1983-08-30 C.E. Equipment Co., Inc. Apparatus for reducing end effect in anodes

Also Published As

Publication number Publication date
FR552982A (en) 1923-05-11
DE386514C (en) 1923-12-10
GB198246A (en) 1923-05-31

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