US2446350A - Electrodeposition of aluminum - Google Patents
Electrodeposition of aluminum Download PDFInfo
- Publication number
- US2446350A US2446350A US524487A US52448744A US2446350A US 2446350 A US2446350 A US 2446350A US 524487 A US524487 A US 524487A US 52448744 A US52448744 A US 52448744A US 2446350 A US2446350 A US 2446350A
- Authority
- US
- United States
- Prior art keywords
- direct current
- aluminum
- alternating current
- current
- electrodeposition
- 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
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
- C25D3/42—Electroplating: Baths therefor from solutions of light metals
- C25D3/44—Aluminium
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/10—Electrodes, e.g. composition, counter electrode
Definitions
- This invention relates to a process for the electrodeposition of aluminum on dissimilar metals.
- Hurley has disclosed that aluminum can be advantageously deposited from and electrolyte comprising (1) an aluminum halide such as aluminum chloride or aluminum bromide and (2) various lower aliphatic pyridinium halides such as N-ethyl pyridinium chloride at temperatures generally above 100 C.
- an aluminum halide such as aluminum chloride or aluminum bromide
- various lower aliphatic pyridinium halides such as N-ethyl pyridinium chloride at temperatures generally above 100 C.
- Wier and Hurley Serial No. 524,486, filed February 29, 1944, it has been disclosed that aluminum can also be deposited on dissimilar metals at room temperature "by utilizing a bath including certain aromatic compounds in addition to the aluminum chloride and the mono-pyridinium mono-halides.
- the magnitude of the alternating current was an approximately sinusoidal function of time and the frequency was about sixty cycles per second.
- a current of this character is usually most conveniently obtained. However, higher or lower frequencies or other alternating current and the type of plate desired.
- the ratio of alternating current to direct current should be increased. Likewise, when thick, non-brittle deposits are to be obtained, the ratio should be increased. The exact value of the ratio is usually not highly critical and can readily be determined for a given set of conditions.
- the direct current and alternating current voltages employed are usually low (of the order of a few volts, usually less than ten volts) and depend upon the several factors mentioned above.
- X-ray examination of plates made in accordance with the present invention shows that when direct current alone is employed, the plates consist of partly oriented, small crystals, whereas when the alternating current is imposed in addition, the plate is composed of larger crystals which are not oriented. It is believed that the improved adherence and other properties of the plates are accounted for in this way.
- a plating mixture was prepared by mixing 2 mols of aluminum chloride (taken as AlCls) and 1 mol of fused ethyl pridinium bromide. After cooling the mixture it was saturated with benzene. About 50 cc. of this solution together with suflicient excess benzene to provide a protective benzene layer about 0.5 cm. in depth was then placed in a cylindrical glass electrolysis cell. This cell was 4.5 cm. in diameter and about 10 cm. high. It was fitted with a cover designed to exclude moisture. The anode was a circular sheet of aluminum fitting against the wall of the cell. The cathodes consisted of suitably cleaned strips of brass 1.34 cm. wide and about 15 cm.
- the direct current voltage was between 0.7 and 0.8 volt.
- the time of electrolysis was 10 minutes in each instance.
- the effect of variation in the root-mean-square value of the alternating current with respect to the direct current on the types of plate is shown in the following table:
- a. process of electroplating with aluminum the step of subjecting an article of a metal from the group consisting of brass, copper and iron, serving as a cathode, simultaneously to an alternating current and a. direct current, passed between said cathode and an aluminum anode and through a fused, anhydrous bath consisting of OTHER REFERENCES Journal of Physical Chemistry, vol. 35 (1931), p. 2289.
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)
- Electroplating And Plating Baths Therefor (AREA)
Description
Patented Aug. 3, 1948 ELECTRODEPOSITION OF ALUMINUM Thomas P. Wier, Jr., Berkeley, Calif., assignor to The William Marsh Rice Institute for the Advancement of Literature, Science and Art, a corporation of Texas No Drawing. Application February 29, 1944, Serial No. 524,487
1 Claim. 1
This invention relates to a process for the electrodeposition of aluminum on dissimilar metals.
In a co-pending application Serial No. 522,375 filed February 14, 1944, Hurley has disclosed that aluminum can be advantageously deposited from and electrolyte comprising (1) an aluminum halide such as aluminum chloride or aluminum bromide and (2) various lower aliphatic pyridinium halides such as N-ethyl pyridinium chloride at temperatures generally above 100 C. In another co-pending application of Wier and Hurley, Serial No. 524,486, filed February 29, 1944, it has been disclosed that aluminum can also be deposited on dissimilar metals at room temperature "by utilizing a bath including certain aromatic compounds in addition to the aluminum chloride and the mono-pyridinium mono-halides. The plates secured by utilizing these bath-s with direct current are brittle and tend to crack, break or flake away from the base, particularly if the article is repeatedly flexed. When using the above mentioned baths, I have discovered that by superimposing a suitable alternating current on the direct current, adherence of the plate to the base metal is increased with the result that the articles can thereafter be worked and bent to shape. Further, the plate secured is more uniform and, in addition, its thickness can be increased. Also, by superimposing a suitable alternating current on the direct current, at the same direct current density the voltage required is lowered somewhat. In addition, higher cathode direct current densities can be used to obtain plates of the same general type as with direct current only. These advantages are obtained without any decrease in cathode current efliciency.
In the experiments whose results are described herein, the magnitude of the alternating current was an approximately sinusoidal function of time and the frequency was about sixty cycles per second. A current of this character is usually most conveniently obtained. However, higher or lower frequencies or other alternating current and the type of plate desired. When it is desired to employ high direct current densities, the ratio of alternating current to direct current should be increased. Likewise, when thick, non-brittle deposits are to be obtained, the ratio should be increased. The exact value of the ratio is usually not highly critical and can readily be determined for a given set of conditions. The direct current and alternating current voltages employed are usually low (of the order of a few volts, usually less than ten volts) and depend upon the several factors mentioned above.
X-ray examination of plates made in accordance with the present invention shows that when direct current alone is employed, the plates consist of partly oriented, small crystals, whereas when the alternating current is imposed in addition, the plate is composed of larger crystals which are not oriented. It is believed that the improved adherence and other properties of the plates are accounted for in this way.
The following example is set forth by way of further illustration of the practice of the present invention, and not by way of limitation:
A plating mixture was prepared by mixing 2 mols of aluminum chloride (taken as AlCls) and 1 mol of fused ethyl pridinium bromide. After cooling the mixture it was saturated with benzene. About 50 cc. of this solution together with suflicient excess benzene to provide a protective benzene layer about 0.5 cm. in depth was then placed in a cylindrical glass electrolysis cell. This cell was 4.5 cm. in diameter and about 10 cm. high. It was fitted with a cover designed to exclude moisture. The anode was a circular sheet of aluminum fitting against the wall of the cell. The cathodes consisted of suitably cleaned strips of brass 1.34 cm. wide and about 15 cm. long; these were immersed to a depth of 3.55 cm. in the bath. The source of direct current was connected across the electrodes and'the source 01 alternating current was connected in parallel with the direct current. The circuits were so arranged as to permit separate variation of the alternating current and of the direct current. The magnitude of the current passing through the cell was an approximately sinusoidal function of time and was symmetrical about a value represented by the direct current. The frequency of the alternating current was approximately cycles per second.
In a series of plating tests, varying amounts of alternating current were superimposed on a constant amount of direct current. The density of direct current at the cathode was 1.20 amps/dun.
3 The direct current voltage was between 0.7 and 0.8 volt. The time of electrolysis was 10 minutes in each instance. The effect of variation in the root-mean-square value of the alternating current with respect to the direct current on the types of plate is shown in the following table:
5 being about two to three times the value of the direct current.
THOMAS P. WIER, JR.
. I Type assurances omen o U gg y plate with small brown 10 The following references are of record in the 1.0 man till 5 signs a? plate secured. when 519 of his patent: 1.5 r ncizfily shfiy E white. Not UNITED STATES PATENTS muc apparent p ysical change, but no brown coloration. Number Name Date 33%; mwhat 15 1,567,791 Duhme D c, 29, 1925 Uniiorm white deposit, not uc 1,785,389 Piersol Dec, 16, 1930 1,911,122 Keyes et al. May 23, 1933 1,939,397 Keyes et a1. Dec. 12, 1933 Satisfactory plates on other metals such as iron Mathers t all g and copper were also made, using this process.
I claim:
In a. process of electroplating with aluminum, the step of subjecting an article of a metal from the group consisting of brass, copper and iron, serving as a cathode, simultaneously to an alternating current and a. direct current, passed between said cathode and an aluminum anode and through a fused, anhydrous bath consisting of OTHER REFERENCES Journal of Physical Chemistry, vol. 35 (1931), p. 2289.
Chemical Abstracts, vol. 32, No. 18, Sept. 20,
25 1938, Col. 6956.
Elektrochemie Nichtwassriger Losungen by Paul Walden, pp. 194, 200, 239.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US524487A US2446350A (en) | 1944-02-29 | 1944-02-29 | Electrodeposition of aluminum |
GB19811/44A GB595790A (en) | 1944-02-29 | 1944-10-13 | Improvements in protected anodes for continuous electroplating processes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US524487A US2446350A (en) | 1944-02-29 | 1944-02-29 | Electrodeposition of aluminum |
Publications (1)
Publication Number | Publication Date |
---|---|
US2446350A true US2446350A (en) | 1948-08-03 |
Family
ID=24089412
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US524487A Expired - Lifetime US2446350A (en) | 1944-02-29 | 1944-02-29 | Electrodeposition of aluminum |
Country Status (2)
Country | Link |
---|---|
US (1) | US2446350A (en) |
GB (1) | GB595790A (en) |
Cited By (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2692850A (en) * | 1951-11-02 | 1954-10-26 | Battelle Development Corp | Aluminum electroforming |
US2939824A (en) * | 1957-07-26 | 1960-06-07 | Kaiser Aluminium Chem Corp | Method and apparatus for the production of aluminum |
US4463072A (en) * | 1983-11-30 | 1984-07-31 | Allied Corporation | Secondary batteries containing room-temperature molten 1,2,3-trialkylimidazolium halide non-aqueous electrolyte |
US4463071A (en) * | 1983-11-30 | 1984-07-31 | Allied Corporation | Secondary batteries using room-temperature molten non-aqueous electrolytes containing 1,2,3-trialkylimidazolium halides or 1,3-dialkylimidazolium halide |
US4747916A (en) * | 1987-09-03 | 1988-05-31 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and process for the same |
WO1989000616A1 (en) * | 1987-07-13 | 1989-01-26 | Nisshin Steel Co., Ltd. | Process for electroplating metal plate with aluminum |
US4904355A (en) * | 1988-04-26 | 1990-02-27 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and plating process making use of the bath |
US4906342A (en) * | 1988-04-26 | 1990-03-06 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and plating process making use of the bath |
US5041194A (en) * | 1989-05-18 | 1991-08-20 | Mitsubishi Petrochemical Co., Ltd. | Aluminum electroplating method |
US5074973A (en) * | 1989-05-23 | 1991-12-24 | Nisshin Steel Co. Ltd. | Non-aqueous electrolytic aluminum plating bath composition |
US5827602A (en) * | 1995-06-30 | 1998-10-27 | Covalent Associates Incorporated | Hydrophobic ionic liquids |
US20040238352A1 (en) * | 2000-10-20 | 2004-12-02 | The University Of Alabama | Production, refining and recycling of lightweight and reactive metals in ionic liquids |
WO2004106288A2 (en) | 2003-06-02 | 2004-12-09 | Merck Patent Gmbh | Ionic liquids containing guanidinium cations |
US20060169590A1 (en) * | 2003-03-04 | 2006-08-03 | Hebditch David J | Process for separating metals |
DE102008014028A1 (en) | 2008-03-13 | 2009-09-17 | Doris Dr. Kunz | Preparing imidazolium salts, preferably 1,3-disubstiuted imidazolium salts, useful e.g. as precursors of N-heterocyclic carbenes, comprises reducing 1,3-disubstituted-2-alkoxyimidazolium salts with hydrides and/or hydride donors |
US20090242409A1 (en) * | 2008-03-31 | 2009-10-01 | Nec Electronics Corporation | Plating method, semiconductor device manufacturing method and plate processing system |
DE102008031480A1 (en) | 2008-07-03 | 2010-01-07 | Merck Patent Gmbh | Salts containing a Pyrimidincarbonsäure derivative |
US9631290B2 (en) | 2011-10-07 | 2017-04-25 | The Board Of Regents Of The Nevada System Of Higher Education On Behalf Of The University Of Nevada, Las Vegas | Room temperature electrodeposition of actinides from ionic solutions |
US10422048B2 (en) | 2014-09-30 | 2019-09-24 | The Board Of Regents Of The Nevada System Of Higher Education On Behalf Of The University Of Nevada, Las Vegas | Processes for recovering rare earth elements |
US11142841B2 (en) | 2019-09-17 | 2021-10-12 | Consolidated Nuclear Security, LLC | Methods for electropolishing and coating aluminum on air and/or moisture sensitive substrates |
EP3904562A1 (en) * | 2020-04-30 | 2021-11-03 | The Boeing Company | Multiple-layer electroplated aluminum coatings over steel substrates and deposition method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1567791A (en) * | 1924-11-01 | 1925-12-29 | Siemens Ag | Electrolytic production of metals |
US1785389A (en) * | 1929-01-14 | 1930-12-16 | Robert J Piersol | Process for controlling electroplating |
US1911122A (en) * | 1929-08-13 | 1933-05-23 | Ellis Foster Co | Process for the electrodeposition of aluminum from its compounds |
US1939397A (en) * | 1929-04-12 | 1933-12-12 | Ellis Foster Co | Process of electrodeposition of aluminum |
US2170375A (en) * | 1937-05-10 | 1939-08-22 | Frank C Mathers | Electrodeposition of aluminum |
-
1944
- 1944-02-29 US US524487A patent/US2446350A/en not_active Expired - Lifetime
- 1944-10-13 GB GB19811/44A patent/GB595790A/en not_active Expired
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1567791A (en) * | 1924-11-01 | 1925-12-29 | Siemens Ag | Electrolytic production of metals |
US1785389A (en) * | 1929-01-14 | 1930-12-16 | Robert J Piersol | Process for controlling electroplating |
US1939397A (en) * | 1929-04-12 | 1933-12-12 | Ellis Foster Co | Process of electrodeposition of aluminum |
US1911122A (en) * | 1929-08-13 | 1933-05-23 | Ellis Foster Co | Process for the electrodeposition of aluminum from its compounds |
US2170375A (en) * | 1937-05-10 | 1939-08-22 | Frank C Mathers | Electrodeposition of aluminum |
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2692850A (en) * | 1951-11-02 | 1954-10-26 | Battelle Development Corp | Aluminum electroforming |
US2939824A (en) * | 1957-07-26 | 1960-06-07 | Kaiser Aluminium Chem Corp | Method and apparatus for the production of aluminum |
US4463072A (en) * | 1983-11-30 | 1984-07-31 | Allied Corporation | Secondary batteries containing room-temperature molten 1,2,3-trialkylimidazolium halide non-aqueous electrolyte |
US4463071A (en) * | 1983-11-30 | 1984-07-31 | Allied Corporation | Secondary batteries using room-temperature molten non-aqueous electrolytes containing 1,2,3-trialkylimidazolium halides or 1,3-dialkylimidazolium halide |
WO1989000616A1 (en) * | 1987-07-13 | 1989-01-26 | Nisshin Steel Co., Ltd. | Process for electroplating metal plate with aluminum |
US4966660A (en) * | 1987-07-13 | 1990-10-30 | Nisshin Steel Co., Ltd. | Process for electrodeposition of aluminum on metal sheet |
US4747916A (en) * | 1987-09-03 | 1988-05-31 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and process for the same |
US4904355A (en) * | 1988-04-26 | 1990-02-27 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and plating process making use of the bath |
US4906342A (en) * | 1988-04-26 | 1990-03-06 | Nisshin Steel Co., Ltd. | Plating bath for electrodeposition of aluminum and plating process making use of the bath |
US5041194A (en) * | 1989-05-18 | 1991-08-20 | Mitsubishi Petrochemical Co., Ltd. | Aluminum electroplating method |
US5074973A (en) * | 1989-05-23 | 1991-12-24 | Nisshin Steel Co. Ltd. | Non-aqueous electrolytic aluminum plating bath composition |
US5827602A (en) * | 1995-06-30 | 1998-10-27 | Covalent Associates Incorporated | Hydrophobic ionic liquids |
US20040238352A1 (en) * | 2000-10-20 | 2004-12-02 | The University Of Alabama | Production, refining and recycling of lightweight and reactive metals in ionic liquids |
US7347920B2 (en) | 2000-10-20 | 2008-03-25 | The Board Of Trustees Of The University Of Alabama | Production, refining and recycling of lightweight and reactive metals in ionic liquids |
US20060169590A1 (en) * | 2003-03-04 | 2006-08-03 | Hebditch David J | Process for separating metals |
WO2004106288A2 (en) | 2003-06-02 | 2004-12-09 | Merck Patent Gmbh | Ionic liquids containing guanidinium cations |
DE102008014028A1 (en) | 2008-03-13 | 2009-09-17 | Doris Dr. Kunz | Preparing imidazolium salts, preferably 1,3-disubstiuted imidazolium salts, useful e.g. as precursors of N-heterocyclic carbenes, comprises reducing 1,3-disubstituted-2-alkoxyimidazolium salts with hydrides and/or hydride donors |
US20090242409A1 (en) * | 2008-03-31 | 2009-10-01 | Nec Electronics Corporation | Plating method, semiconductor device manufacturing method and plate processing system |
US20110152292A1 (en) * | 2008-07-03 | 2011-06-23 | Merck Patent Gesellschaft | Salts comprising a pyrimidinecarboxylic acid derivative for cosmetic use |
DE102008031480A1 (en) | 2008-07-03 | 2010-01-07 | Merck Patent Gmbh | Salts containing a Pyrimidincarbonsäure derivative |
US9631290B2 (en) | 2011-10-07 | 2017-04-25 | The Board Of Regents Of The Nevada System Of Higher Education On Behalf Of The University Of Nevada, Las Vegas | Room temperature electrodeposition of actinides from ionic solutions |
US10422048B2 (en) | 2014-09-30 | 2019-09-24 | The Board Of Regents Of The Nevada System Of Higher Education On Behalf Of The University Of Nevada, Las Vegas | Processes for recovering rare earth elements |
US11142841B2 (en) | 2019-09-17 | 2021-10-12 | Consolidated Nuclear Security, LLC | Methods for electropolishing and coating aluminum on air and/or moisture sensitive substrates |
US11459658B2 (en) | 2019-09-17 | 2022-10-04 | Consolidated Nuclear Security, LLC | Methods for electropolishing and coating aluminum on air and/or moisture sensitive substrates |
EP3904562A1 (en) * | 2020-04-30 | 2021-11-03 | The Boeing Company | Multiple-layer electroplated aluminum coatings over steel substrates and deposition method |
US11661665B2 (en) | 2020-04-30 | 2023-05-30 | The Boeing Company | Aluminum and aluminum alloy electroplated coatings |
Also Published As
Publication number | Publication date |
---|---|
GB595790A (en) | 1947-12-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2446350A (en) | Electrodeposition of aluminum | |
US3193485A (en) | Electrolytic treatment of aluminium for increasing the effective surface | |
US4417954A (en) | Electrolyte for the electrodeposition of aluminum | |
Verdieck et al. | The Electrochemistry of Baths of Fused Aluminum Halides. I. Aluminum as a Reference Electrode. | |
US3554881A (en) | Electrochemical process for the surface treatment of titanium,alloys thereof and other analogous metals | |
Toschev et al. | Electrolytic nucleation of cadmium | |
IT978581B (en) | METALLIC ANODES WITH REDUCED ANODIC SURFACE FOR ELECTROLYSIS PROCESSES USING LOW DENSITY OF CATHODIC CURRENT | |
US2170375A (en) | Electrodeposition of aluminum | |
McCullough et al. | The Crystal Structure of Diphenylselenium Dichloride1 | |
US3528894A (en) | Method of electrodepositing corrosion resistant coating | |
US1735878A (en) | Device for measuring the current densities of galvanic baths | |
Haurpin | Polarization in an aluminum reduction cell | |
CN103748269B (en) | Copper plating bath | |
US3691049A (en) | Wire and strip line electroplating | |
Blum et al. | General principles and methods of electroplating | |
Wesley et al. | Cathode Potential, Efficiency and Throwing Power of Nickel Plating Solutions | |
Juchniewicz | The influence of alternating current on the anodic behaviour of platinum | |
US3759801A (en) | Electrolysis bath and process for electrolytically coloring anodized aluminum | |
Green et al. | A New Method for the Determination of the Zero Charge Point of Metal Electrodes | |
Toifur et al. | The Effect of Deposition Time on the Voltage Range and Sensitivity of Cu/Ni as Low-Temperature Sensor Resulted from Electroplating Assisted by a Transverse Magnetic Field | |
US3954571A (en) | Wire and strip line electroplating | |
Mazza | Influence of long time polarization on anodic breakdown of titanium in concentrated NaCl solutions | |
US2741586A (en) | Electroplating metals | |
Ukshe et al. | The electrical double layer in molten halides | |
Cromer | Least-Squares Refinement of the Structure of Tetramethylpyrazine |