US2022064814A1PendingUtilityA1

Zinc electrolyte devoid of boric acid and ammonium for the electrodeposition of zinc coatings

Assignee: DR LNG MAX SCHLOETTER GMBH & CO KGPriority: Dec 12, 2018Filed: Dec 9, 2019Published: Mar 3, 2022
Est. expiryDec 12, 2038(~12.4 yrs left)· nominal 20-yr term from priority
C25D 3/565C25D 3/22C25D 5/48C25D 5/50C25D 21/14
27
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Claims

Abstract

The invention relates to an aqueous electrolyte devoid of boric acid and ammonium for the electrodeposition of zinc coatings and to a method for producing such an electrolyte. The electrolyte comprises (a) Zn 2+ in a concentration of 15 to 70 g/L; (b) Cl − in a concentration of 100 to 200 g/L; (c) K + and/or Na + in a total concentration of 0.75 to 6.0 mol/L; (d) acetate in a concentration of 5.0 to 45 g/L; (e) glycine and/or alanine in a total concentration of 0.5 to 30 g/L; and (f) water. The electrolyte has a pH of 4.5 to 6.5. In a preferred variant, the electrolyte contains (g) nicotinic acid and/or (h) ethoxylated thiodiglycol. The invention also relates to a method for producing a component having a zinc coating, which uses the electrolyte.

Claims

exact text as granted — not AI-modified
1 . An aqueous electrolyte devoid of boric acid and ammonium for the electrodeposition of zinc coatings, comprising:
 (a) Zn 2+  in a concentration of 15 to 70 g/L;   (b) Cl −  in a concentration of 100 to 200 g/L;   (c) K +  and/or Na +  in a total concentration of 0.75 to 6.0 mol/L;   (d) acetate in a concentration of 5.0 to 45 g/L;   (e) glycine and/or alanine in a total concentration of 0.5 to 30 g/L; and   (f) water;   wherein the electrolyte has a pH of 4.5 to 6.5.   
     
     
         2 . The electrolyte according to  claim 1 , wherein the concentration of Zn 2+  in the electrolyte is 20 to 60 g/L, preferably 25 to 50 g/L, more preferably 30 to 40 g/L and most preferably 35 g/L. 
     
     
         3 . The electrolyte according to  claim 1 , wherein the concentration of Cl −  in the electrolyte is 120 to 190 g/L, preferably 130 to 180 g/L and more preferably 160 g/L. 
     
     
         4 . The electrolyte according to  claim 1 , wherein the electrolyte contains K +  and the concentration of K +  is 0.75 to 6.0 mol/L, preferably 2.7 to 4.8 mol/L and more preferably 3.3 to 4.1 mol/L. 
     
     
         5 . The electrolyte according to  claim 1 , wherein the concentration of acetate in the electrolyte is 7.5 to 30 g/L, preferably 10 to 20 g/L, most preferably 12 g/L. 
     
     
         6 . The electrolyte according to  claim 1 , wherein the total concentration of glycine and/or alanine in the electrolyte is in the range of 0.5 to 20 g/L, preferably 1.0 to 10 g/L, more preferably 1.5 to 5 g/L and most preferably 2.5 g/L. 
     
     
         7 . The electrolyte according to  claim 1 , wherein the electrolyte contains
 (a) Zn 2+  in a concentration of 20 to 60 g/L;   (b) Cl −  in a concentration of 120 to 190 g/L;   (c) K +  in a concentration of 2.7 to 4.8 mol/L and 0 to 0.5 mol/L Nat;   (d) acetate in a concentration of 7.5 to 30 g/L; and   (e) glycine and/or alanine in a total concentration of 0.5 to 20 g/L.   
     
     
         8 . The electrolyte according to  claim 1 , wherein the electrolyte additionally contains (g) nicotinic acid in a concentration of 0.01 to 2.0 g/L, preferably 0.05 to 1.0 g/L, more preferably 0.08 to 0.5 g/L, most preferably 0.1 g/L. 
     
     
         9 . The electrolyte according to  claim 1 , wherein the electrolyte additionally contains (h) ethoxylated thiodiglycol, with an average of at least 20 structural units derived from ethylene oxide, in a concentration of 0.3 to 10 g/L, preferably 0.5 to 5 g/L, more preferably 1.0 to 3.5 g/L and most preferably 2.1 g/L. 
     
     
         10 . The electrolyte according to  claim 1 , wherein the electrolyte contains
 (g) nicotinic acid in a concentration of 0.05 to 1.0 g/L, and/or   (h) ethoxylated thiodiglycol, with an average of at least 20 structural units derived from ethylene oxide, in a concentration of 0.5 to 5 g/L.   
     
     
         11 . A method for producing an aqueous electrolyte according to  claim 1 , comprising the steps of:
 A) forming an aqueous solution of
 (a′) zinc chloride and/or zinc acetate; 
 (b′) potassium chloride and/or sodium chloride; 
 (c′) at least one of potassium acetate, sodium acetate and acetic acid; 
 (d′) at least one from the group consisting of glycine, a salt thereof, alanine and a salt thereof; and 
 (e′) optionally nicotinic acid or a salt thereof; and 
 (f′) optionally ethoxylated thiodiglycol, with an average of at least 20 structural units derived from ethylene oxide; and 
   B) optionally setting the pH to 4.5 to 6.5 by adding hydrochloric acid or by adding potassium hydroxide and/or sodium hydroxide, which can be added as solids or in the form of an aqueous solution.   
     
     
         12 . A method for producing a component having a zinc coating, comprising the electrodeposition of zinc on a metal component from an electrolyte according to  claim 1 . 
     
     
         13 . The method according to  claim 12 , wherein the metal component comprises or consists of iron or an iron alloy. 
     
     
         14 . The method according to  claim 12 , wherein deposition occurs at a temperature of 20 to 50° C., preferably 25 to 40° C., and
 a current density of 0.2 to 10 A/dm 2 , preferably 0.5 to 6 A/dm 2 , is used for the deposition. 
 
     
     
         15 . The method according to  claim 12 , wherein after the electrodeposition the component having a zinc coating is subjected to a passivation treatment. 
     
     
         16 . The method according to  claim 12 , wherein after the electrodeposition the component having a zinc coating is annealed, optionally before or after a passivation treatment.

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