US497621A - Officex - Google Patents
Officex Download PDFInfo
- Publication number
- US497621A US497621A US497621DA US497621A US 497621 A US497621 A US 497621A US 497621D A US497621D A US 497621DA US 497621 A US497621 A US 497621A
- Authority
- US
- United States
- Prior art keywords
- tin
- bath
- chloride
- iron
- plate
- 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
- 229910052718 tin Inorganic materials 0.000 description 54
- ATJFFYVFTNAWJD-UHFFFAOYSA-N tin hydride Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 54
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 44
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 42
- 229910052742 iron Inorganic materials 0.000 description 22
- 238000000034 method Methods 0.000 description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 18
- 239000005028 tinplate Substances 0.000 description 18
- XPPKVPWEQAFLFU-UHFFFAOYSA-J Pyrophosphate Chemical compound [O-]P([O-])(=O)OP([O-])([O-])=O XPPKVPWEQAFLFU-UHFFFAOYSA-J 0.000 description 16
- 229940048084 Pyrophosphate Drugs 0.000 description 16
- 235000011180 diphosphates Nutrition 0.000 description 16
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 16
- 239000011734 sodium Substances 0.000 description 16
- 229910052708 sodium Inorganic materials 0.000 description 16
- 235000011121 sodium hydroxide Nutrition 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 229940037003 alum Drugs 0.000 description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 238000000151 deposition Methods 0.000 description 10
- 238000005868 electrolysis reaction Methods 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 238000005554 pickling Methods 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000000137 annealing Methods 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 239000002659 electrodeposit Substances 0.000 description 4
- 150000002739 metals Chemical class 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 241000276489 Merlangius merlangus Species 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 150000001805 chlorine compounds Chemical class 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000004070 electrodeposition Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 239000011121 hardwood Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 230000001788 irregular Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000007517 polishing process Methods 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/30—Electroplating: Baths therefor from solutions of tin
Definitions
- My invention involves the use of an aqueous electrolytic bath of special composition and at a comparatively high temperature.
- the compound thus produced constitutes my electrolytic tin bath, and while the same may be used at ordinary temperature, I have found that a considerable advantage is secured when the bath'is heated to a temperature of 150" Fahrenheit and more. tages secured by the elevated temperature of the bath is that its conductivity is thereby increased and that for this reason the electromotive force of the current employed need not be so high as when the bath is cold. The lower the electro-motive force of the electric current employed, the greater is the density and the more uniform is the thickness of the iron is moved about in the bath or the bath is agitated. The sheet iron is then removed and washed in water and is then annealed in the ordinary manner. After annealing the sheets are passed between smooth polished One of the advan- 7 have been removed.
- the sheet 5 rolls, whereby they are made smooth and receive a bright finish.
- the plates become again superficially oxidized, and this oxide is now removed by immersion of the plates in a solution of one part of hydrochloric acid to twenty parts of water.
- the plates are left from ten to fifteen minutes. They are then withdrawn and are placed in clear running water and are scoured by scratch brushes, or otherwise.
- the electro-deposit is produced in the ordinary manner, using cast tin anodes and a uniform current from. any suitable source and preferably of low electro-motive force. This is quite practicable when the bath is heated and maintained hot as above described. A layer of any desired thickness of tin may be deposited, and if the bath is sufficiently hot and the electro-motivc force of the current sufliciently low, the deposit is very uniform and shows very little, if any,
- the sheets are withdrawn from the electrolytic bath and are passed first through cold water, then through hot water, and are then dried in coarse, hard wood sawdust, and then polished with flannel and whiting, or by any other convenient means.
- tin plate which consists in pickling sheet iron'or steel, and then depositing tin upon the same by the electrolysis of an aqueous electrolytic bath, containing ammoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
- tin plate which consists in depositing tin upon pickled sheet iron or steel by the electrolysis of a hot aqueous electrolytic bath,containing aminoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
- An electrolytic tinning bath composed of water, ammoniacal alum, chloride of tin, pyrophosphate of sodium, and caustic soda, substantially as described.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
Description
- LOUIS ARONSON; OF
UNITED STAT S PATENT FFrcE.
NEW YORK, Y., ASSIGNOR orbits-HALF To JAMES H.'HOFEMAN,OF SAME PLACE.
PROCESS OF IELEIVCTRO-TIN-PLATIJNG."
srncrmcmrron'forming part a. Letters Patent N .497,e2'1, dated 'May 16, 1893.
llpplicatlon filed January 31, 1893. Serial No. 460,446. (No specimens-l I adapted to such manufacture.
' deposition, it has heretofore been found that In the production of tin-plate by electro the tin deposited upon the iron did not adhere to the latter with sufficient tenacity to allow the plate to be worked into articles of merchandise. The tin would peel off in flakes,
more especially, when the plate was bent an-' gularly, thus leaving irregular patches of the iron exposed and subject to the corroding infiuenee of the atmosphere orof other agencies which would come into contact with the plate. It was also found that electrically deposited tin was very much softer than ordinary com- I mercial tin, and aportion of it would rub ofi in the polishing process to which such plates should be subjected after the electrical deposit has been made. For these reasons, electro-plated tin-plate, although considerably cheaper than the ordinary tin-plate, has not come into use.
It is the object of my invention to overcome these difficulties and to produce tinplate by electro deposition, in which the tin shall adhere to the iron or other base, with the same tenacity as it does in the ordinary tin-plate, and in which the tin shall be as denseand hard, if not denser and harder than on the ordinary tin plate.
, My invention involves the use of an aqueous electrolytic bath of special composition and at a comparatively high temperature.
. I It also involves the practice of a peculiar pickling process for preparing sheet iron for the reception of the electro deposit of tin. All this will more fully appear from the following detail description, which is intended to be sufficiently full and clear to enable others skilled in the art to practice the invention.
I prepare the electrolytic tin bath as fol-.
lows: Onepeund of ammoniacalalum is dissolved in five gallons of water, and to this solution are added four to eight ounces of chloride of tin; only a portion of this chloride of tin will be dissolved,another portion' -ietnaining suspended and eventually accumulating at the bottom. To this compound are added eight ounces of pyro-phosphate of sodium, which produces a considerable precipitate. The fluid is then stirred and caustic soda is added in small quantities until the precipitate together withthe undissolved portion of the chloride of tin is taken up. If more than eight ounces of chloride of tin are used, a proportionately greater amount of pyro-phosphate of sodium must be used. The compound thus produced constitutes my electrolytic tin bath, and while the same may be used at ordinary temperature, I have found that a considerable advantage is secured when the bath'is heated to a temperature of 150" Fahrenheit and more. tages secured by the elevated temperature of the bath is that its conductivity is thereby increased and that for this reason the electromotive force of the current employed need not be so high as when the bath is cold. The lower the electro-motive force of the electric current employed, the greater is the density and the more uniform is the thickness of the iron is moved about in the bath or the bath is agitated. The sheet iron is then removed and washed in water and is then annealed in the ordinary manner. After annealing the sheets are passed between smooth polished One of the advan- 7 have been removed. By preference the sheet 5 rolls, whereby they are made smooth and receive a bright finish. In the annealing process the plates become again superficially oxidized, and this oxide is now removed by immersion of the plates in a solution of one part of hydrochloric acid to twenty parts of water. In this diluted acid bath the plates are left from ten to fifteen minutes. They are then withdrawn and are placed in clear running water and are scoured by scratch brushes, or otherwise. The plates'are now ready to be received in the electrolytic bath above described. The electro-deposit is produced in the ordinary manner, using cast tin anodes and a uniform current from. any suitable source and preferably of low electro-motive force. This is quite practicable when the bath is heated and maintained hot as above described. A layer of any desired thickness of tin may be deposited, and if the bath is sufficiently hot and the electro-motivc force of the current sufliciently low, the deposit is very uniform and shows very little, if any,
granulation. It adheres tenaciously to the iron and and is very hard.
When a suflicient deposit has been produced, the sheets are withdrawn from the electrolytic bath and are passed first through cold water, then through hot water, and are then dried in coarse, hard wood sawdust, and then polished with flannel and whiting, or by any other convenient means.
It is evident, that by this process not only tin plate, but a. great variety of other articles may be made; nor is the process confined to the tinning of iron or steel, but is applicable to the tinning, of a variety of other metals, which may be prepared, for the bath in any desired manner.
The proportions of the ingredients composing the electrolytic bath may be varied with out departing from my invention.
Other metals than iron may be tinned by.
means of my electrolytic bath and by the general procedure hereinbefore described, except that the pickling process must be adapted to the metal.
Having now fully described my invention,
I claim and desire to secure by Letters Paten l. The process of tinning metallic articles, which consists in depositing tin upon such articles, by the electrolysis of an aqueous electrolytic bath, containing ammoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
2. The process of tinning metallic articles, which consists in depositing tin upon such articles by the electrolysis of a hot aqueous electrolytic bath, containing ammoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
3. The process of tinning metallic articles, which consists in depositing tin upon such article from a hot aqueous bath, containing ammoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, by the passage therethrough and between tin anodes and the article of a current of electricity of low tension, substantially as described.
4. The process of making tin plate, which consists in pickling sheet iron'or steel, and then depositing tin upon the same by the electrolysis of an aqueous electrolytic bath, containing ammoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
5. The process of making tin plate, which consists in depositing tin upon pickled sheet iron or steel by the electrolysis of a hot aqueous electrolytic bath,containing aminoniacal alum, chloride of tin, pyro-phosphate of sodium and caustic soda, substantially as described.
- 6. An electrolytic tinning bath composed of water, ammoniacal alum, chloride of tin, pyrophosphate of sodium, and caustic soda, substantially as described.
In testimony whereof I have signed my name to this specification in the presence of two subscribing witnesses.
LOUIS ARONSQN. Witnesses:
UHR. STRAUS, J AS. H. HOFFMAN.
Publications (1)
Publication Number | Publication Date |
---|---|
US497621A true US497621A (en) | 1893-05-16 |
Family
ID=2566459
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US497621D Expired - Lifetime US497621A (en) | Officex |
Country Status (1)
Country | Link |
---|---|
US (1) | US497621A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434290A (en) * | 1941-03-05 | 1948-01-13 | Carnegie Illinois Steel Corp | Electrolytic tin plate |
-
0
- US US497621D patent/US497621A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2434290A (en) * | 1941-03-05 | 1948-01-13 | Carnegie Illinois Steel Corp | Electrolytic tin plate |
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