WO2005033374A1 - Elektrolyt für die galvanische abscheidung von aluminium-magnesium-legierungen - Google Patents

Elektrolyt für die galvanische abscheidung von aluminium-magnesium-legierungen Download PDF

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Publication number
WO2005033374A1
WO2005033374A1 PCT/EP2004/052113 EP2004052113W WO2005033374A1 WO 2005033374 A1 WO2005033374 A1 WO 2005033374A1 EP 2004052113 W EP2004052113 W EP 2004052113W WO 2005033374 A1 WO2005033374 A1 WO 2005033374A1
Authority
WO
WIPO (PCT)
Prior art keywords
aluminum
magnesium
electrolyte
alkyl
alkyl group
Prior art date
Application number
PCT/EP2004/052113
Other languages
German (de)
English (en)
French (fr)
Inventor
Richard Lisowsky
Klaus-Dieter Mehler
Original Assignee
Aluminal Oberflächentechnik Gmbh & Co. Kg
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Aluminal Oberflächentechnik Gmbh & Co. Kg filed Critical Aluminal Oberflächentechnik Gmbh & Co. Kg
Priority to EP04787118A priority Critical patent/EP1664389A1/de
Priority to JP2006527396A priority patent/JP2007506862A/ja
Priority to US10/573,519 priority patent/US20070108061A1/en
Publication of WO2005033374A1 publication Critical patent/WO2005033374A1/de

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/56Electroplating: Baths therefor from solutions of alloys
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/42Electroplating: Baths therefor from solutions of light metals

Definitions

  • the invention relates to an electrolyte for the electrodeposition of aluminum-magnesium alloys containing at least one organoaluminum complex compound and a magnesium alkyl compound. 5 Further objects of the invention are a method for producing the electrolyte, a coating method, the use of the electrolyte and an electrolysis kit.
  • Magnesium-aluminum-organic complex compounds have recently been used for the electrolytic deposition of aluminum-magnesium alloys. This is described in WO 00/32847 A1. Interest in the electrolytic coating of metal workpieces with aluminum-magnesium alloys has increased significantly due to the excellent corrosion protection provided by the aluminum-magnesium layers and their ecological harmlessness. For this reason, electroplating with magnesium-15 aluminum-organic electrolytes, which takes place in closed systems at temperatures in the range of 60 - 150 ° C, has gained great technical importance.
  • MAIR 4 complex compounds of the general type MAIR 4 and mixtures thereof in combination with aluminum alkylene AIR 3 have been proposed as particularly suitable eleldrolytes. These are used in the form of their solutions in liquid, aromatic hydrocarbons.
  • M can be an alkali metal such as sodium, potassium, rubidium and cesium, R are alkyl radicals with preferably one, two or four carbon atoms.
  • the systems known hitherto are characterized in that the required magnesium-organic complex compounds are initially not available in the electrolyte and only have to be generated in a trochemically complex manner when the electrolyte is used in situ. So ready-to-use start only organic aluminum compounds but no magnesium compounds.
  • the above-mentioned magnesium-free starting electrolyte is first filled into the electrolysis cells suitable for coating.
  • the required organic magnesium complex is then generated electrochemically by applying a current using separate aluminum and magnesium anodes or an aluminum-magnesium mixed electrode until the concentration of magnesium complex in the electrolyte required for coating is reached.
  • the technical object of the invention is therefore to provide an electrolyte which can be produced as simply, efficiently and inexpensively as possible, which enables the aluminum-magnesium coating process to be introduced commercially and the conditioning phase mentioned above for formation of organic Mg complexes no longer necessary.
  • an electrolyte for the electrodeposition of aluminum-magnesium alloys containing at least one aluminum-organic complex compound of the formula MAIR4 or mixtures thereof and a magnesium alkyl compound, where M is sodium, potassium, rubidium or cesium and R is a C1-C1 0 alkyl group, preferably a C 1 -C 4 -alkyl group.
  • the electrolyte additionally contains an aluminum trialkyl compound.
  • the electrolyte according to the invention can be used for coating materials with aluminum-magnesium alloys without the in-situ generation of magnesium-organic complexes in a time-consuming and cost-intensive conditioning phase before actual coating process is necessary.
  • the magnesium alkyl compound is preferably in one
  • Particularly preferred magnesium alkyl compounds which are used in the electrolyte are selected from the group MgButyl1, 5Octyl0.5, MgButyl1.0Ethyl1, 0, Mgsec-Bu1, 0nButyl1, O or mixtures thereof.
  • Alkyl compounds can preferably be present in an organic solvent.
  • the organic solvent is particularly preferably an aromatic solvent, and solvents such as benzene, toluene or xylene or mixtures thereof can be used here.
  • the magnesium alkyl compounds mentioned have the advantage that they are industrially accessible and can be produced easily and inexpensively compared to the magnesium aluminum-ethyl complexes mentioned above Mg [Al (Et)) 4 ] 2 Electrolytes are made according to the following steps. First, the aluminum-organic complex compound of the formula MAIR4 or a mixture thereof, if appropriate in combination with aluminum trialkyl, is initially introduced. A magnesium alkyl compound is then added as described above. M and R have the same meaning as described above.
  • the metering of the magnesium-alkyl compounds in the manufacture of the electrolyte has the advantage that the necessary concentration of magnesium and aluminum can be set directly, so that the conditioning process described above can be completely dispensed with. It is also possible to add magnesium-alkyl compounds during the coating process in order to maintain the corresponding magnesium concentration which is desired and necessary for the coating.
  • the magnesium-alkyl compounds are added in solution in a hydrocarbon and the aluminum-alkyl complexes are initially introduced in solution in an aromatic hydrocarbon.
  • the hydrocarbon for the aluminum compound is selected from the group i-pentane, n-pentane, hexane, n-hexane, heptane, n-heptane, toluene and xylene.
  • Aluminum-magnesium layers of different concentration sequences of aluminum and magnesium by simply and freely choosing the amount of added magnesium-organic compounds.
  • the corresponding concentration of aluminum-magnesium is determined by the amount added set of magnesium-organic compounds.
  • the electrolyte according to the invention also has the advantage of good conductivity and scatterability.
  • the electrolyte according to the invention makes it possible to work with indifferent anodes which are used in the coating of geometrically complex shaped parts.
  • Indifferent electrodes are those that do not dissolve during the coating process, i.e. do not consist of Al or Mg or their alloys.
  • Mg-organic compounds and Al-organic compounds must therefore be added to the electrolyte solution.
  • the corresponding concentration of aluminum-magnesium is set via the amount of magnesium-organic compounds and aluminum-organic compounds added.
  • Working with indifferent anodes was previously ruled out for the in-situ generation of organic magnesium complexes, as was the generation of layers of different aluminum-magnesium compositions in one operation. This is also not possible using the in-situ method described above with a conditioning step to produce the magnesium concentration in the electrolyte.
  • Another object of the invention is an electrolysis kit for the electrodeposition of aluminum-magnesium alloys on electrically conductive materials or electrically conductive layers, comprising: a) the aluminum-organic complex compounds described above, or aluminum-alkyl compounds of claims 1-3 and 1, 3, 5, 6 and b) a magnesium alkyl compound according to claims 1, 3, 5, 6.
  • the compounds a) and b) are dissolved in an organic solvent.
  • Another object of the invention is a method for coating electrically conductive materials or layers with aluminum-magnesium alloys with the electrolyte according to claims 1-9, wherein during the coating phase, the magnesium-alkyl compound according to claims 1, 3, 5 and 6 is metered in in the desired amount in order to obtain or maintain a desired concentration of magnesium to aluminum
  • Another object of the invention is the use of the electrolyte according to the invention for the production of layers of aluminum alloys on electrically conductive materials or electrically conductive layers.
  • Step 1 The BOMAG ® / heptane solution was adjusted to a content of 0.32 mmol / g after the heptane had been condensed with toluene.
  • 2nd step 55.4 g of an electrolyte of the following composition: 0.8 K [Al (Et) 4 ] + 0.2 Na [Al (Et) 4 ] + 1.17 Al (Et) 3 + 3.85 g of BOMAG / toluene solution were added to 3.85 toluene (approx. 1.0 mol% based on the electrolyte formulation). About 58 g of an electrolyte were obtained.
  • Anode material 2 alloy electrodes AIMg25, 55 x 10 x 5mm
  • Cathode pretreatment degreasing, descaling in an ultrasonic bath with 8% HCI, H 2 O washing, vacuum drying, argon storage.
  • the deposition was started with a current density of 0.05A / dm 2 b. After a few minutes, a light covering can be seen on the parts to be coated. The current density was gradually increased to 3.0 Vdm 2 . The deposition was terminated after a current of 1.499mF corresponding to a layer thickness of 5 ⁇ . The layer is light and silvery.
  • Step 1 The BEM / heptane solution was after the condensation of
  • 2nd step 60.6 g of an electrolyte of the following composition: 0.8 K [Al (Et) 4 ] + 0.2 Na [Al (Et) 4 ] + 1.17 Al (Et) 3 + 3.85 toluene were mixed with 2.0 ml BEM / toluene solution (about 0.9 mol% based on the electrolyte formulation). About 62 g of an electrolyte were obtained.
  • the deposition conditions are as in Example 1.
  • the deposition was started directly with a current density of 2.0 A / dm 2 and was not changed during the entire electrolysis. There was an immediate bright separation of Al / Mg.
  • the deposition was ended after a current of 3.38 mF corresponding to a layer thickness of 11 ⁇ . An excellent, very uniform, silvery layer is obtained, without any visible defects.
  • Step 1 The BEM / isopentane solution is containing
  • 2nd step 70.04 g of an electrolyte of the following composition 0.85 K [Al (Et) 4 ] + 0.15 Na [Al (Et)] + 1.08 Al (Et) 3 + 3, 15 toluene were mixed with 0.5 g BEM / isopentane solution (approx. 0.8 mol% based on the electrolyte formulation).
  • the deposition took place at a current density of 1.0 to 3.0 A / dm 2 .
  • the deposition was terminated after a current of 6.8 mF corresponding to a layer thickness of 20 ⁇ . A very uniform, silvery layer is obtained.
  • the electrolyte is conditioned and ready for use only after this process.

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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)
  • Electroplating And Plating Baths Therefor (AREA)
  • Electroplating Methods And Accessories (AREA)
PCT/EP2004/052113 2003-09-27 2004-09-09 Elektrolyt für die galvanische abscheidung von aluminium-magnesium-legierungen WO2005033374A1 (de)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP04787118A EP1664389A1 (de) 2003-09-27 2004-09-09 Elektrolyt f r die galvanische abscheidung von aluminium-mag nesium-legierungen
JP2006527396A JP2007506862A (ja) 2003-09-27 2004-09-09 アルミニウム−マグネシウム合金の電着用電解質
US10/573,519 US20070108061A1 (en) 2003-09-27 2004-09-09 Electrolyte for the galvanic deposition of aluminum-magnesium alloys

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP03021877.0 2003-09-27
EP03021877A EP1518945A1 (de) 2003-09-27 2003-09-27 Elektrolyt für die galvanische Abscheidung von Aluminium-Magnesium-Legierungen

Publications (1)

Publication Number Publication Date
WO2005033374A1 true WO2005033374A1 (de) 2005-04-14

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PCT/EP2004/052113 WO2005033374A1 (de) 2003-09-27 2004-09-09 Elektrolyt für die galvanische abscheidung von aluminium-magnesium-legierungen

Country Status (7)

Country Link
US (1) US20070108061A1 (zh)
EP (2) EP1518945A1 (zh)
JP (1) JP2007506862A (zh)
KR (1) KR20060090816A (zh)
CN (1) CN1860257A (zh)
RU (1) RU2347857C2 (zh)
WO (1) WO2005033374A1 (zh)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1524336A1 (de) * 2003-10-18 2005-04-20 Aluminal Oberflächtentechnik GmbH & Co. KG Mit einer Aluminium-/Magnesium-Legierung beschichtete Werkstücke
CN103334132B (zh) * 2013-07-17 2016-05-25 沈阳大学 室温电沉积制备铝镁合金膜的方法
CN103510136B (zh) * 2013-09-22 2015-08-19 电子科技大学 一种在超细钨丝表面电沉积铝镁合金薄膜的方法
CN106435706B (zh) * 2015-08-04 2019-02-26 张无量 镁制血管支架的电化学抛光方法
US11111591B2 (en) * 2017-06-01 2021-09-07 Lumishield Technologies Incorporated Methods and compositions for electrochemical deposition of metal rich layers in aqueous solutions
CN113846353B (zh) * 2021-10-13 2023-03-28 东北大学 一种使用极性非质子有机溶剂制备铝镁合金的方法

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1365009A (en) * 1971-05-07 1974-08-29 Siemens Ag Electrolytic aluminising of shaped metal articles
US4778575A (en) * 1988-01-21 1988-10-18 The United States Of America As Represented By The United States Department Of Energy Electrodeposition of magnesium and magnesium/aluminum alloys
WO2000032847A2 (de) * 1998-12-01 2000-06-08 Studiengesellschaft Kohle Mbh Aluminiumorganische elektrolyte und verfahren zur elektrolytischen beschichtung mit aluminium oder aluminium-magnesium-legierungen
WO2002088434A1 (en) * 2001-04-30 2002-11-07 Alumiplate Incorporated Aluminium electroplating formulations

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3028319A (en) * 1960-02-01 1962-04-03 Ethyl Corp Manufacture of magnesium organo compounds
US7250102B2 (en) * 2002-04-30 2007-07-31 Alumiplate Incorporated Aluminium electroplating formulations

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1365009A (en) * 1971-05-07 1974-08-29 Siemens Ag Electrolytic aluminising of shaped metal articles
US4778575A (en) * 1988-01-21 1988-10-18 The United States Of America As Represented By The United States Department Of Energy Electrodeposition of magnesium and magnesium/aluminum alloys
WO2000032847A2 (de) * 1998-12-01 2000-06-08 Studiengesellschaft Kohle Mbh Aluminiumorganische elektrolyte und verfahren zur elektrolytischen beschichtung mit aluminium oder aluminium-magnesium-legierungen
WO2002088434A1 (en) * 2001-04-30 2002-11-07 Alumiplate Incorporated Aluminium electroplating formulations

Also Published As

Publication number Publication date
RU2347857C2 (ru) 2009-02-27
RU2006116263A (ru) 2007-11-27
EP1518945A1 (de) 2005-03-30
KR20060090816A (ko) 2006-08-16
CN1860257A (zh) 2006-11-08
EP1664389A1 (de) 2006-06-07
JP2007506862A (ja) 2007-03-22
US20070108061A1 (en) 2007-05-17

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