US1848002A - Anode for iron plating - Google Patents
Anode for iron plating Download PDFInfo
- Publication number
- US1848002A US1848002A US173793A US17379327A US1848002A US 1848002 A US1848002 A US 1848002A US 173793 A US173793 A US 173793A US 17379327 A US17379327 A US 17379327A US 1848002 A US1848002 A US 1848002A
- Authority
- US
- United States
- Prior art keywords
- iron
- anode
- sulphide
- electrolyte
- ferrous
- 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
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title description 58
- 229910052742 iron Inorganic materials 0.000 title description 26
- 238000007747 plating Methods 0.000 title description 6
- 239000003792 electrolyte Substances 0.000 description 13
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 11
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical compound [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 10
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 229960002089 ferrous chloride Drugs 0.000 description 2
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 229910001141 Ductile iron Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 125000001309 chloro group Chemical class Cl* 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- QFXZANXYUCUTQH-UHFFFAOYSA-N ethynol Chemical group OC#C QFXZANXYUCUTQH-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000005445 natural material Substances 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/06—Electrolytic production, recovery or refining of metals by electrolysis of solutions or iron group metals, refractory metals or manganese
Definitions
- My invention relates to the production of anodeswhich are suitable for the production of electrolytic iron which is soft and workable instead of being brittle.
- the essence of my invention is the employment of a control substance as part of or as all of the anode.
- This invention has many advantages besides the reduction of acid development and content, and the consequent diminution of the hydrogen ion concentration as an active factor at the cathode, where the iron is being deposited.
- ferrous sulphide FeS
- FeS ferrous sulphide
- the sulphide may also neutralize sulphur or chlorine acids directly formed, but I believe that its chief function is to prevent the formation of acid which would otherwise resut from the hydrolysis of free ferric chlor1 e.
- a variety of processes may be used in producing the iron sulphide bearing anodes.
- One way will be to employ commercial iron sulphide, which will be mixed in withpieces of various sizes of iron and steel scrap, sheet clippings, borings, or other iron scrap material, in a suitable dish, which may be formed of ingot iron sheets. The dish is then placed in a furnace and heated sufficiently to sinter the mass. If ferrous sulphide is .used, this fusion or sintering will be very rapid; but if the ferric form is employed, I prefer to prolong the heating until all or nearly all of the sulphide is present in the ferrous form.
- the sintered or fused mass can be removed and will be self supporting to a degree suflicient to permit of its being used as an anode.
- I may prefer to use a cast anode member of iron sulphide alone, or a com- .tposite member of iron sulphide and a preformed iron core.
- FusedFeS has a good conductivity, and is quite effective in producing the correct neutrality of electrolyte required for depositing ductile iron.
- Another form of the anode is made by using a dish of iron or steel, and fusing the iron sulphide into it, alone, in which case the dish forms a part of the anode, or the molded block may be removed therefrom and used by itself.
- the iron sulphide may be liquefied by the use of an oxyacetylene torch, and the ferrous oxide of iron, or other iron, stirred into the mass, after which it is permitted to set.
- a solid unitary anode for use in plating iron which contains iron sulphide as an essential ingredient of the unitary mass.
- a solid anode for use in plating iron which contains ferrous sulphide as an essential ingredient, together with iron the several ingredients formlng a unitary, conductive mass.
- An anode for use in platin iron which contains iron sulphide, and iron caring materials held in said sulphide as abinding agent.
- An anode for use in plating iron which is formed -of a mass of iron bearing materials with sintered iron sulphide.
- the sulphide anodes may be used only partof the time, and can be replaced by'iron anodes without sulphide, periodically, during a plating process without having ill effects upon the softness of product.
- the neutralizer would, perhaps, have to be different in composition, and I do not wish to limit my invention to this one substance in its broader ascts. I may without ill effects, in a plating apparatus having a continuous circulatory system for the electrolyte, establish a series of
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
, tile form,
Patented Mar. I 1, 1932 UNITED STATES PATENT T OFFICE JOHN R. CAIN, OF WASHINGTON, DISTRICT or COLUMBIA, ASSIGNOR TO THE RICHARD- soN COMPANY, OF LocKLAN OHIO, A CORPORATION OF OHIO ANODE FOR IRON PLATINU- No Drawing.
My invention relates to the production of anodeswhich are suitable for the production of electrolytic iron which is soft and workable instead of being brittle.
The problem of production of electrolytic iron involves among other things, the fact that past commercial practices have resulted in producing this iron in a brittle, non-ducso far as they have come to my attention.
In a series of experiments aimed at discovering the reasons for this brittleness, and after elimination by such experiments of a number of possible causes, I have discovered thatwith ferrouschloride electrolytes, kept at a temperature close to the boiling point thereof, and controlled as to hydrogen ion content during the electrolytic deposition of metal, that a soft white electrolytic iron will be produced.
In a co-pending application, Serial No. 238,232, I have described an electrolytic process producing soft iron involving the continuous control of the hydrogen ion content of a ferrous electrolyte which is kept at a temperature close to the boiling point thereof during use. My anodes as here claimed are particularly adapted for use in that process.
I do not wish to limit the application of my present invention, which lies in the composition of the anode used by me to maintain the bath free of acid, to the specific type of electrolyte with which it may be employed.
The essence of my invention is the employment of a control substance as part of or as all of the anode. This invention has many advantages besides the reduction of acid development and content, and the consequent diminution of the hydrogen ion concentration as an active factor at the cathode, where the iron is being deposited.
I prefer to use ferrous sulphide (FeS) for the control substance. For one thing, ferric sulphide is an inexpensive natural substance which can be readily fused in a container, and
when so fused, passes readily to the desirableferrolis condition, and can be employed to retain masses of 1ron or steel scrap, and of iron ores and sponge iron. Also, it has the 1927. Serial No. 173,793.
I do not wish to be bound to the correctness thereof, since the reactions in the baths used as electrolytes by me, are not easy to trace.
I will, in the description of a typical example of my invention, however, refer to my theory of reactions, and of cause and effect,,with the understanding that there may be other factors entering into the explanation of the surprising results obtained, which factors I have not as yet determined. f
-With the aim of producing a deposit of soft and ductile electrolytic iron upon a suitable cathode, in my typical example, I employ .a cathode in the form of a sheet of electrolytic iron of the type produced by me, or
resulting from annealing and pickling of electrolytic iron produced by other processes. I employ as an electrolyte a bath of ferrous chloride in water, having 100 grams of iron per liter. This is not as concentrated a solution as I could use with ood results, but will suflice for excellent wof'k This electrolyte I maintain at between 90 and 95 degrees Centigrade, and I also provide for filtering the electrolyte during use, for reasons to be explained.
If an anode of iron were used, it would be necessary to add ferroussulphide or some other neutralizer or conditioner to the bath, from time to time to obtain the efiects that I obtain, and it is the object of my invention to provide an anode which automatically takes care at least in part of the iron sulphide addition, and continuously.
S. The sulphide may also neutralize sulphur or chlorine acids directly formed, but I believe that its chief function is to prevent the formation of acid which would otherwise resut from the hydrolysis of free ferric chlor1 e.
A variety of processes may be used in producing the iron sulphide bearing anodes. One way will be to employ commercial iron sulphide, which will be mixed in withpieces of various sizes of iron and steel scrap, sheet clippings, borings, or other iron scrap material, in a suitable dish, which may be formed of ingot iron sheets. The dish is then placed in a furnace and heated sufficiently to sinter the mass. If ferrous sulphide is .used, this fusion or sintering will be very rapid; but if the ferric form is employed, I prefer to prolong the heating until all or nearly all of the sulphide is present in the ferrous form. If it is not desired to use the dish as a part of the anode, the sintered or fused mass can be removed and will be self supporting to a degree suflicient to permit of its being used as an anode. I may prefer to use a cast anode member of iron sulphide alone, or a com- .tposite member of iron sulphide and a preformed iron core. FusedFeS has a good conductivity, and is quite effective in producing the correct neutrality of electrolyte required for depositing ductile iron.
So far I have not obtained effective results where the electrolyte is used cold.
Another form of the anode is made by using a dish of iron or steel, and fusing the iron sulphide into it, alone, in which case the dish forms a part of the anode, or the molded block may be removed therefrom and used by itself. Or I ma make a composite anode including oxides 0 iron thus: The iron sulphide may be liquefied by the use of an oxyacetylene torch, and the ferrous oxide of iron, or other iron, stirred into the mass, after which it is permitted to set.
ing iron which consists of fused ferrous sulphide.
2. A solid unitary anode for use in plating iron which contains iron sulphide as an essential ingredient of the unitary mass.
3. A solid anode for use in plating iron which contains ferrous sulphide as an essential ingredient, together with iron the several ingredients formlng a unitary, conductive mass.
4. An anode for use in platin iron which contains iron sulphide, and iron caring materials held in said sulphide as abinding agent.
5. An anode for use in plating iron which is formed -of a mass of iron bearing materials with sintered iron sulphide.
' JOHN R. CAIN.
I find that the conditioning of the electrolyte by the use of sulphide of iron in the anode itself, is much preferable to the use of same as other than part of the anode. The electrolyte not only becomes more quickly conditioned, but also keeps the proper hydrogen ion concentration longer after the conditioner has been removed.
I find also that the sulphide anodes may be used only partof the time, and can be replaced by'iron anodes without sulphide, periodically, during a plating process without having ill effects upon the softness of product.
With another electrolyte the neutralizer would, perhaps, have to be different in composition, and I do not wish to limit my invention to this one substance in its broader ascts. I may without ill effects, in a plating apparatus having a continuous circulatory system for the electrolyte, establish a series of
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US173793A US1848002A (en) | 1927-03-08 | 1927-03-08 | Anode for iron plating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US173793A US1848002A (en) | 1927-03-08 | 1927-03-08 | Anode for iron plating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1848002A true US1848002A (en) | 1932-03-01 |
Family
ID=22633511
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US173793A Expired - Lifetime US1848002A (en) | 1927-03-08 | 1927-03-08 | Anode for iron plating |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1848002A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4454015A (en) * | 1982-09-27 | 1984-06-12 | Aluminum Company Of America | Composition suitable for use as inert electrode having good electrical conductivity and mechanical properties |
| US4584172A (en) * | 1982-09-27 | 1986-04-22 | Aluminum Company Of America | Method of making composition suitable for use as inert electrode having good electrical conductivity and mechanical properties |
| WO2019057431A1 (en) * | 2017-09-19 | 2019-03-28 | Siemens Aktiengesellschaft | CO2-FREE ELECTROCHEMICAL MANUFACTURE OF METALS AND ALLOYS THEREOF |
-
1927
- 1927-03-08 US US173793A patent/US1848002A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4454015A (en) * | 1982-09-27 | 1984-06-12 | Aluminum Company Of America | Composition suitable for use as inert electrode having good electrical conductivity and mechanical properties |
| US4584172A (en) * | 1982-09-27 | 1986-04-22 | Aluminum Company Of America | Method of making composition suitable for use as inert electrode having good electrical conductivity and mechanical properties |
| WO2019057431A1 (en) * | 2017-09-19 | 2019-03-28 | Siemens Aktiengesellschaft | CO2-FREE ELECTROCHEMICAL MANUFACTURE OF METALS AND ALLOYS THEREOF |
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