US2043823A - Anode - Google Patents
Anode Download PDFInfo
- Publication number
- US2043823A US2043823A US2043823DA US2043823A US 2043823 A US2043823 A US 2043823A US 2043823D A US2043823D A US 2043823DA US 2043823 A US2043823 A US 2043823A
- Authority
- US
- United States
- Prior art keywords
- iron
- anode
- sponge
- electrolyte
- metal
- 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
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 128
- 229910052742 iron Inorganic materials 0.000 description 64
- 239000002184 metal Substances 0.000 description 24
- 229910052751 metal Inorganic materials 0.000 description 24
- 239000003792 electrolyte Substances 0.000 description 20
- 239000011248 coating agent Substances 0.000 description 14
- 238000000576 coating method Methods 0.000 description 14
- 239000000463 material Substances 0.000 description 8
- 239000000956 alloy Substances 0.000 description 6
- 229910045601 alloy Inorganic materials 0.000 description 6
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 6
- 239000000969 carrier Substances 0.000 description 6
- 231100000078 corrosive Toxicity 0.000 description 6
- 231100001010 corrosive Toxicity 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- IMBKASBLAKCLEM-UHFFFAOYSA-L Ammonium iron(II) sulfate Chemical compound [NH4+].[NH4+].[Fe+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O IMBKASBLAKCLEM-UHFFFAOYSA-L 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 4
- 229910052753 mercury Inorganic materials 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 238000009736 wetting Methods 0.000 description 4
- NCNCGGDMXMBVIA-UHFFFAOYSA-L Iron(II) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L Iron(II) sulfate Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000000137 annealing Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000001427 coherent Effects 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000004070 electrodeposition Methods 0.000 description 2
- 230000001771 impaired Effects 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 230000000284 resting Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/03—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/02—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form
- C25B11/03—Electrodes; Manufacture thereof not otherwise provided for characterised by shape or form perforated or foraminous
- C25B11/031—Porous electrodes
Definitions
- Fig. I is a diagrammatic view in section of an anode of my present invention in one of its practicable forms
- Fig. II is a view' in section of a portion of the walls of an electrolytic cell, and of the anode of my invention in another permissible form
- Figs. III, IV, and V are views in elevation of the anode of the invention in yet other forms.
- the anode may be formed, to possess the characteristic that it shall consist essentially of iron in finely divided condition.
- a supporting core of magnetic character may carry, magnetically Secured, a surface coating of flnely divided iron, and in such case, as in the progress of the electrolytic operation, it is consumed, the coating may be renewed and built up again by sprinkling fresh supplies of nely divided iron into the electrolyte. such material so sprinkled in will at once be attracted magnetically -to and will constitute renewal of the coating upon the core.
- the core may be permanently magnetic, or it may be rendered magnetic by means of an electric current.
- Fig.' I an anode is shown, consisting of a core i and a coating! of flnely divided iron, and it may be 4 understood that the core is magnetized, and that the coating is held magnetically to it.
- a body 3 of mercury for example, suitably disposed within the cell 4 (spread as a bath upon the bottom of the cell) may carry a skim or coating 5 of flnely divided iron sprinkled upon it. And in this case also the coating may be renewed by sprinkling fresh supplies of finely divided iron into the. cell, while the operation is in progress; for the sprinkled-in iron will sink through the electrolyte and rest upon the surface of'the bath of mercury.
- a plurality of discs or blocks G are shown, which may be understood to be bodies of iron sponge compressed sufllciently to give coherence, but not sufliciently to destroy the characteristic of flnely divided material, large surface area relatively to mass.
- These bodies 6 are shown to be combined andformed into a unitary anode structure by means of strips 'I and 8 of another metal or alloy cast in situ upon them and establishing electrical continuity.
- These uniting strips are formed of a metal or alloy that is inert to the corrosive action of the electrolyte, or substantially so.
- the strips 'l and 8 are dense.
- the metal or alloy of which the strips 1 and 8 are formed be such as to possess when in moiten state the' characteristic of wetting iron. such a metal is lead.
- the strips of relatively inert metal or alioy persist, while the'compressed iron sponge is gradually eaten away by the corrosive action of electrolysis.
- the anode in this embodiment manifestly, there must be replacement of the worn anode.
- the iron sponge may be compressed upon a supporting grid or carrier of another metal
- Fig. IV in which in dotted lines a body 9 of iron sponge is shown to be shaped'- and compressed upon a grid o, 'that may be understood to be formed of denser iron.
- the ,iron sponge may be given coherence by compression within a thin cylinder of a metal This is l2 that may be understood to be a body of compressed iron sponge. Within the body !2, in turn, is incorporated a supporting and electrically conducting carrier I 3.
- the electroiyte will as operation progresses be found to have a relatively constant pH value; the pH value will be found to range from 6 to '7. And within that range electrolysis progresses successfully and the deposit is such in character as to be useful.
- a deposited sheet for example, may be successfully removed from a stripping cathode, and brought by annealing to serviceable condition.
- An anode for an electrolytic cell consisting of finely divided iron held magnetically upon the surface of a supportingbody of magnetic character.
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- 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 June 9, 1936 PATENT 'OFFICE ANODE John L. Young, Pittsb'gh, Pa., assignor to National Radiato' Corporation, a corporation of Maryland Application November 1, 1934, Serial No. !50,929 2 Claims. (l. Zoi-4) This invention relates to electrolytic cells for the deposit of metals. I have developed it in making deposit of iron, and in that particular application I shall describe it. I
In the accompanying drawing Fig. I is a diagrammatic view in section of an anode of my present invention in one of its practicable forms; Fig. II is a view' in section of a portion of the walls of an electrolytic cell, and of the anode of my invention in another permissible form; and Figs. III, IV, and V are views in elevation of the anode of the invention in yet other forms.
It has heretofore been proposed to make electrolytic deposit of iron from a solution of a ferrous salt, typically ferrous ammonium sulphate, as an electrolyte, using an iron anode; but the proposal has been attended with practical difliculties not heretofore successfully overcome. As the operation progresses the electrolyte tends to .become increasingly acid in character, with the conversion of the dissolved ferrous ammonium sulphate to ferric salt, and the iron deposit upon the cathode tends to become so brittle as to be useless. The proposal has been made to correct 25 this tendency by maintaining iron sponge in suspension in the electrolyte; but the proposal leads to other difficulties. The bulk of the sponge iron is lost in an undeslred precipitate of ferrous hydroxide, and the deposit on the cathode tends to become rough, and in that respect of impaired utility. And it has not 'been found practically possible so to maintain the pH value of the bath within the limited range essential to practical success. V
I have discovered that if iron sponge be employed, not as a substance Suspended in and distributed through the body of electrolyte, but as the anode itself, the pH value of the electrolyte may be maintained within the requisite range, and a successful and practical deposit obtained.
While I do not wish to limit my invention by theoretical considerations, I have reason to believe that my practical success, in contrast to the 4 impracticability of prior proposals, is due to the fact that, whereas the substance of the iron anode as heretofore employed has been accessible to the electrolyte over surface areas that were small relatively to the mass of metal consumed, with -an anode of iron sponge the substance of the anode is accessible over surface areas that are large relatively to the mass consumed. I, therefore, find the essential character of the anode of my invention to be the flnely divided condition of the iron of which it is constituted.
There are various ways in which the anode may be formed, to possess the characteristic that it shall consist essentially of iron in finely divided condition. In one embodiment of the invention a supporting core of magnetic character may carry, magnetically Secured, a surface coating of flnely divided iron, and in such case, as in the progress of the electrolytic operation, it is consumed, the coating may be renewed and built up again by sprinkling fresh supplies of nely divided iron into the electrolyte. such material so sprinkled in will at once be attracted magnetically -to and will constitute renewal of the coating upon the core. The core may be permanently magnetic, or it may be rendered magnetic by means of an electric current. In Fig.' I an anode is shown, consisting of a core i and a coating! of flnely divided iron, and it may be 4 understood that the core is magnetized, and that the coating is held magnetically to it.
Again, advantage may be taken of the fact that certain metals in molten state have the characteristic of wetting iron, in order to form an anode of the character indicated. This is illustrated in Fig. II. A body 3 of mercury, for example, suitably disposed within the cell 4 (spread as a bath upon the bottom of the cell) may carry a skim or coating 5 of flnely divided iron sprinkled upon it. And in this case also the coating may be renewed by sprinkling fresh supplies of finely divided iron into the. cell, while the operation is in progress; for the sprinkled-in iron will sink through the electrolyte and rest upon the surface of'the bath of mercury.
I have found that iron sponge compressed sufficiently to form a coherent mass of permanent shape will still retain its finely divided character to sumcient extent, and will be found effective in the electrolytic operation. Accordingly, another way of 'forming a practicable electrode is to compress iron sponge to suitable shape and size and to mount the compressed body or bodies (for, conveniently, a plurality of smaller units will thus be built together) upon a carrier that is at once a conductor and is more inert than is the body of compressed sponge to the corrosive action of the electrolyte. In Flg. III a plurality of discs or blocks G are shown, which may be understood to be bodies of iron sponge compressed sufllciently to give coherence, but not sufliciently to destroy the characteristic of flnely divided material, large surface area relatively to mass. These bodies 6 are shown to be combined andformed into a unitary anode structure by means of strips 'I and 8 of another metal or alloy cast in situ upon them and establishing electrical continuity. These uniting strips are formed of a metal or alloy that is inert to the corrosive action of the electrolyte, or substantially so. They are inert, relatively to the bodies of iron sponge, both by virtue of the material of which they are composed and by virtue of the condition of the material: while the bodies 6 are of spongy condition, the strips 'l and 8 are dense. Although it is not requisite, it is advantageous that the metal or alloy of which the strips 1 and 8 are formed be such as to possess when in moiten state the' characteristic of wetting iron. such a metal is lead. In operation the strips of relatively inert metal or alioy persist, while the'compressed iron sponge is gradually eaten away by the corrosive action of electrolysis. In the use of the anode in this embodiment, manifestly, there must be replacement of the worn anode.
` Again, the iron sponge may be compressed upon a supporting grid or carrier of another metal, the
compression being sufficient to efl'ect mechanical union and integration and electrical continuit'y, but insuflicient to destroy the characteristic advantage of iron sponge described above. illustrated in Fig. IV, in which in dotted lines a body 9 of iron sponge is shown to be shaped'- and compressed upon a grid o, 'that may be understood to be formed of denser iron.
The ,iron sponge may be given coherence by compression within a thin cylinder of a metal This is l2 that may be understood to be a body of compressed iron sponge. Within the body !2, in turn, is incorporated a supporting and electrically conducting carrier I 3.
Proceeding with an anode of finly divided iron, the electroiyte will as operation progresses be found to have a relatively constant pH value; the pH value will be found to range from 6 to '7. And within that range electrolysis progresses successfully and the deposit is such in character as to be useful. A deposited sheet, for example, may be successfully removed from a stripping cathode, and brought by annealing to serviceable condition. e
I claim as my invention:
1. A soluble anode for' metallic electro-deposition 'consisting of nely divided metal resting upon the surface of a supporting body of another metal in liquid state.
2. An anode for an electrolytic cell consisting of finely divided iron held magnetically upon the surface of a supportingbody of magnetic character.
J OI-IN L. YOUNG.
Publications (1)
Publication Number | Publication Date |
---|---|
US2043823A true US2043823A (en) | 1936-06-09 |
Family
ID=3427948
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US2043823D Expired - Lifetime US2043823A (en) | Anode |
Country Status (1)
Country | Link |
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US (1) | US2043823A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2467852A (en) * | 1944-03-23 | 1949-04-19 | Houdaille Hershey Corp | Electrolytic sheet metal anode |
US4540477A (en) * | 1983-05-27 | 1985-09-10 | Olin Corporation | Apparatus for producing acicular or equiaxed iron or iron alloy particles |
WO1994007543A3 (en) * | 1992-10-06 | 1994-05-26 | Kew Import/Exort Inc. | Sharps destruction apparatus |
-
0
- US US2043823D patent/US2043823A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2467852A (en) * | 1944-03-23 | 1949-04-19 | Houdaille Hershey Corp | Electrolytic sheet metal anode |
US4540477A (en) * | 1983-05-27 | 1985-09-10 | Olin Corporation | Apparatus for producing acicular or equiaxed iron or iron alloy particles |
WO1994007543A3 (en) * | 1992-10-06 | 1994-05-26 | Kew Import/Exort Inc. | Sharps destruction apparatus |
US5441622A (en) * | 1992-10-06 | 1995-08-15 | Kew Import/Export, Inc. | Sharps destruction apparatus |
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