DE825597C - Process for anodic nickel removal - Google Patents

Process for anodic nickel removal

Info

Publication number
DE825597C
DE825597C DEC2148A DEC0002148A DE825597C DE 825597 C DE825597 C DE 825597C DE C2148 A DEC2148 A DE C2148A DE C0002148 A DEC0002148 A DE C0002148A DE 825597 C DE825597 C DE 825597C
Authority
DE
Germany
Prior art keywords
anodic
nickel
nickel removal
baths
anodic nickel
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
Application number
DEC2148A
Other languages
German (de)
Inventor
Rolf Brandenburger
Dr-Ing Alexander Pollack
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gerhard Collardin GmbH
Original Assignee
Gerhard Collardin GmbH
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 Gerhard Collardin GmbH filed Critical Gerhard Collardin GmbH
Priority to DEC2148A priority Critical patent/DE825597C/en
Application granted granted Critical
Publication of DE825597C publication Critical patent/DE825597C/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F5/00Electrolytic stripping of metallic layers or coatings

Landscapes

  • 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)

Description

Verfahren zum anodischen Entnickeln Es sind verschiedene Verfahren bekannt, um Nickelüberzüge auf chemischem oder elektrochemischem Wege abzulösen. Im ersten Fall verwendet man dazu meist Gemische von Schwefelsäure und Salpetersäure, während man anodisch in Schwefelsäure von etwa 55° Be mit 2 bis 6 Volt und q bis 8 Amp./qdm entnickelt.Methods of anodic nickel removal There are several methods known to remove nickel coatings chemically or electrochemically. In the first case, mixtures of sulfuric acid and nitric acid are usually used, while anodic in sulfuric acid of about 55 ° Be with 2 to 6 volts and q to 8 Amp./qdm removed.

Der Hauptnachteil der elektrolytischen Entnirklungsbäder besteht darin, daß nach der Entnicklung das Grundmetall angegriffen wird. Die zu entnickelnden Gegenstände müssen daher, sobald der Nickelüberzug abgezogen ist, aus dem Bade herausgenommen werden. Da die Nickelschichten aber niemals gleichmäßig stark sind und zum Teil schneller, zum Teil langsamer abgelöst werden, läßt sich ein Angriff des Grundmetalls niemals ganz unterbinden. Man hat daher schon vielfach versucht, das Grundmetall durch Zusätze verschiedener Art zu schützen. Vorgeschlagen hat man dazu beispielsweise Neutralsalze wie Natrium- oder Aluminiumsulfat oder auch arsenige Säure. Während die neutralen Salze wenig wirksam sind, besteht beim Zusatz von arseniger Säure die Gefahr der Bildung von Arsenwasserstoff, der äußerst giftig ist und das Arbeiten mit solchen Bädern sehr unbequem macht. Auch das ebenfalls vorgeschlagene anodische Albziehen in Natriumnitratlösung ist infolge der Entwicklung giftiger Stickoxyde zu verwerfen.The main disadvantage of electrolytic removal baths is that that after the development of nickel, the base metal is attacked. The ones to be unsnickled Objects must therefore be removed from the bath as soon as the nickel coating is removed will. Since the nickel layers are never evenly thick and partly be removed faster, sometimes more slowly, the base metal can be attacked never stop completely. Therefore, many attempts have been made to find the base metal to protect with additives of various kinds. For example, one has proposed this Neutral salts such as sodium or aluminum sulfate or arsenic acid. While the neutral salts are not very effective, if arsenic acid is added the risk of the formation of arsine, which is extremely toxic and working makes having such baths very uncomfortable. Also the anodic one that is also proposed Sleeping in sodium nitrate solution is due to the development of toxic oxides of nitrogen to discard.

Es hat sich nun überraschenderweise 'herausgestellt, daß das Grundmaterial nicht oder nur sehr wenig angegriffen wird, wenn man den Entnicklungsbädern als sog. Inhiibitoren !bekannte Stoffe anorganischer oder organischer Art allein oder im Gemisch miteinander zusetzt. Es sind dies z. B. Chromate, Phosphate, Silicate und ähnliche als anorganische Hexamethylentetramin, Pyridin, Chinolin, Thioharnstoffverbindungen und andere Stoffe mit ähnlichen Eigenschaften als organische Inhibitoren. Es ist zwar bekannt, daß diese Stoffe die Korrosion von Metallen vermindern, es war aber keineswegs vorauszusehen, daß sie auch die anodische Auflösung der Metalle nach der anodischen Ablösung von Nickelschichten unterbinden.It has now surprisingly been found that the base material not, or only very little, attacked if one considers the development baths So-called inhibitors! known substances of an inorganic or organic nature alone or in the Mixture added together. There are z. B. Chromates, phosphates, Silicates and the like as inorganic hexamethylenetetramine, pyridine, quinoline, Thiourea compounds and other substances with properties similar to organic ones Inhibitors. It is known that these substances reduce the corrosion of metals, but it was by no means to be foreseen that they would also dissolve the metals anodically after the anodic detachment of nickel layers.

Durch Verwendung der Zusätze gemäß vorliegender Erfindung wird es auch möglich, die Bäder auf höhere Temperaturen zu erhitzen und höhere Spannungen und Stromdichten als üblich anzuwenden. Es wird beispielsweise möglich, mit 8 .bis io Volt und io bis 15 Amp./qdm bei 3o bis 40° zu entnickeln, ohne daß ein Angriff des Grundmetalls zu befürchten ist. In den Bädern gemäß vorliegender Erfindung können auch ohne weiteres Eisenkathoden verwendet werden oder auch eiserne Bad'behälter, die als Kathoden geschaltet werden, so daß sich die Verwendung besonderer Kathoden erübrigt.By using the additives of the present invention, it becomes also possible to heat the baths to higher temperatures and higher voltages and current densities as usual to apply. It is possible, for example, with 8 .bis io volts and io to 15 amps / sqdm at 3o to 40 ° without an attack of the base metal is to be feared. In the baths according to the present invention can iron cathodes can also be used without further ado or iron bath containers, which are connected as cathodes, so that the use of special cathodes unnecessary.

Claims (2)

PATENTANSPRÜCHE: i. Verfahren zum anodischen Entnickeln, vorzugsweise in Schwefelsäurelösungen, dadurch gekennzeichnet, daß man den Bädern oder den zu ihrer Herstellung dienenden Salzen, z. B. Bisulfaten, Hemmstoffe anorganischer oder organischer Art, wie Chromate, Phosphate, Silicate und ähnliche oder Hexamethylentetramin, Pyridin, Chinolin, Thioharnstoffverbindungen und ähnliche allein oder im Gemisch miteinander zusetzt. PATENT CLAIMS: i. Process for anodic nickel removal, preferably in sulfuric acid solutions, characterized in that the baths or the salts used for their preparation, e.g. B. bisulfates, inhibitors of inorganic or organic nature, such as chromates, phosphates, silicates and the like, or hexamethylenetetramine, pyridine, quinoline, thiourea compounds and the like, alone or in admixture with one another. 2. Verfahren nach Anspruch i, dadurch gekennzeichnet, daß die Entnicklung bei höheren Temperaturen durchgeführt wird.2. The method according to claim i, characterized in that the Development of nickel is carried out at higher temperatures.
DEC2148A 1950-09-14 1950-09-14 Process for anodic nickel removal Expired DE825597C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEC2148A DE825597C (en) 1950-09-14 1950-09-14 Process for anodic nickel removal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEC2148A DE825597C (en) 1950-09-14 1950-09-14 Process for anodic nickel removal

Publications (1)

Publication Number Publication Date
DE825597C true DE825597C (en) 1951-12-20

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
DEC2148A Expired DE825597C (en) 1950-09-14 1950-09-14 Process for anodic nickel removal

Country Status (1)

Country Link
DE (1) DE825597C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1301185B (en) * 1967-04-27 1969-08-14 Dillenberg Bergische Metall Bath for the electrolytic removal of galvanic deposits from ferrous basic bodies

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1301185B (en) * 1967-04-27 1969-08-14 Dillenberg Bergische Metall Bath for the electrolytic removal of galvanic deposits from ferrous basic bodies

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