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US3841982A - Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath - Google Patents

Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath Download PDF

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Publication number
US3841982A
US3841982A US00333927A US33392773A US3841982A US 3841982 A US3841982 A US 3841982A US 00333927 A US00333927 A US 00333927A US 33392773 A US33392773 A US 33392773A US 3841982 A US3841982 A US 3841982A
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Prior art keywords
bath
zinc
hydrogen
group
alkyl
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US00333927A
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G Southfield
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OMI International Corp
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Oxy Metal Finishing Corp
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Priority to US00333927A priority Critical patent/US3841982A/en
Priority to NL7304246A priority patent/NL7304246A/xx
Priority to FR7311420A priority patent/FR2180708B1/fr
Priority to DE2318984A priority patent/DE2318984C2/en
Priority to IT49467/73A priority patent/IT983031B/en
Priority to CA169,009A priority patent/CA1009178A/en
Priority to GB1826373A priority patent/GB1387529A/en
Priority to AR247599A priority patent/AR197894A1/en
Priority to JP48042757A priority patent/JPS4917324A/ja
Application granted granted Critical
Publication of US3841982A publication Critical patent/US3841982A/en
Assigned to OXY METAL INDUSTRIES CORPORATION reassignment OXY METAL INDUSTRIES CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). 4-09-74 Assignors: OXY METAL FINISHING CORPORATION
Assigned to HOOKER CHEMICALS & PLASTICS CORP. reassignment HOOKER CHEMICALS & PLASTICS CORP. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: OXY METAL INDUSTRIES CORPORATION
Assigned to OCCIDENTAL CHEMICAL CORPORATION reassignment OCCIDENTAL CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE MARCH 30, 1982. Assignors: HOOKER CHEMICAS & PLASTICS CORP.
Assigned to OMI INTERNATIONAL CORPORATION reassignment OMI INTERNATIONAL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: OCCIDENTAL CHEMICAL CORPORATION
Assigned to MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF reassignment MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: INTERNATIONAL CORPORATION, A CORP OF DE
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    • 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
    • C25D3/22Electroplating: Baths therefor from solutions of zinc

Definitions

  • X is S- or A is independently selected from the group consisting n is or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of l to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
  • Zincate plating baths have been used as a means of electrodepositing zinc without employing cyanide ions due to the difficulty in disposing of cyanide ions in waste efiluent.
  • Some conventional zinc brighteners produce a bright deposit but only over a narrow current density range.
  • the high current density areas generally resulted in a spongy or burnt deposit. It has been found through the combination of brighteners employed in the present case to obtain not only a bright deposit, but also a deposit over a wide current density area.
  • a method for obtaining a bright zinc electrodeposit over a wide current density area from a zincate electroplating bath by employing a combination of additives, the first being a polyethyleneimine and the second one being a heterocyclic nitrogen containing compound.
  • X is S or I NR,
  • A is independently selected from the group consisting n is 0 or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
  • Zincate plating baths are those which generally contain zinc oxide and caustic, such as sodium hydroxide.
  • the amount of sodium hydroxide that may be employed ranges from 50 to 250 grams/liter, preferably from about to about 200 grams/liter, while the amount of zinc oxide ranges from 5 to 50 grams/liter, preferably from about 8 to about 30 grams/liter.
  • the processing parameters are such that normally atmospheric temperature and pressure is employed, although temperatures up to 55 C. may also be employed, and even more preferably 15 to about 45 C.
  • the cathode current density ranges from about 5 to 25 amps per sq. ft. while the anode current density ranges from about 10 to 35 amps per sq. ft. where the zinc deposition can occur with agitation.
  • agents may also be present in the bath, such as those described in the above patents.
  • suitable agents may be anisaldehyde, glue, polyvinyl alcohol and the glycerol ester of polyvinyl alcohol wherein these alcohols have a molecular weight of 5,000 to 20.- 000.
  • Other polymers that may be employed are gelatin, peptone, and the like.
  • chelating agents or agents which can form a complex with the metal zinc in the bath may also be employed, such as nitrilotriacetic acid and the various alkali metal salts, such as the sodium salt, ethylenediaminetetraacetic acid, and its water soluble salts, such as sodium, and the like.
  • the polyethyleneimine that may be used in the present case has a molecular weight ranging from 1,000 to 400,- 000, preferably 600 to 60,000 where the percentage of primary, secondary and tertiary nitrogen atoms is about 25, 50, and 25% respectively.
  • a zincate bath that may be employed in the present invention is as follows:
  • the bath pH may be adjusted by adding NaOl-I.
  • Some of the nitrogen heterocylic compounds that may be employed in the present invention are as follows.
  • water solubilizing group any substituent on the six membered carbocyclic ring which will improve the water solubility of the compound.
  • Such groups are hydroxy, alkoxy, such as methoxy or ethoxy and the like, carboxy, amino, and the like.
  • R may be other groups which are not detrimental to the electrodeposition of zinc such as chloro, bromo, cyano (CN), nitro and the like.
  • EXAMPLE 1 A zincate plating bath was formulated containing the following components and was used to electrodeposit zinc onto a steel substrate at a cathode current density of ASP and a temperature of 75 F.
  • the initial bath pH is about 14.
  • EXAMPLE 2 Zincate plating bath similar to the above was also prepared but further including 0.1 g./l. of polyvinyl alcohol. A bright zinc deposit was obtained over a broad current density range following the procedure of Example #1.
  • Example 3 The procedure of Example #1 was followed, except that the bath also contained 0.1 grams/liter of anisaldehyde with equivalent results being obtained.
  • Example 4 The procedure of Example #1 was followed, except that the bath also contained 0.1 grams/liter of anisaldehyde and 0.1 grams/liter of polyvinyl alcohol with equivalent results being obtained.
  • An aqueous alkaline electroplating bath comprising inc oxide, alkali metal hydroxide, polyethyleneimine having a molecular weight of from 1,000 to 400,000 and being present in a concentration of 0.2 to grams per liter and a zinc brightening amount of a nitrogen heterocyclic compound of the formula:
  • A is independently selected from the group consisting of 11 is 0 or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is O, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbons, phenyl; and may be joined to form a six membered aromatic carbocyclic ring which may be substituted and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
  • a method of depositing bright zinc from a zincate electroplating bath comprising electrolyzing the bath of Claim 1 for a period of time suflicient to form a bright zinc deposit onto a cathodic surface.
  • a cyanide free alkaline zincate electroplating bath comprising zinc oxide, alkali metal hydroxide, polyethyleneimine having a molecular weight of from 1,000 to 400,000 and being present in a concentration from 0.2 to 100 grams per liter and a zinc brightening amount of a nitrogen heterocyclic compound of the formula:
  • X is S- or l lR and A is independently selected from the group consisting of n is O or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring which may be substituted and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.

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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)

Abstract

1. AN AQUEOUS ALKALINE ELECTROPLATING BATH COMPRISING INC OXIDE, ALKALI METAL HYDROXIDE, POLYETHYLENEIMINE HAVING A MOLECULAR WEIGHT OF FROM 1,000 TO 400,000 AND BEING PRESENT IN A CONCENTRATION OF 0.2 TO 100 GRAMS PER LITER AND A ZINC BRIGHTENING AMOUNT OF A NITROGEN HETEROCYCLIC COMPOUND OF THE FORMULA:

X<(-A=N OR -N(-R3)N-C(-R2)=C(-R1)-)

WHEREIN X IS

-S- OR >N-R3, AND

A IS INDEPENDENTLY SELECTED FROM THE GROUP CONSISTING OF

>C-N(-R3)2; >C=S; -C(=S)-R3; >C=N-R3 AND >CH2

N IS O OR 1; WHEN N IS 0, NITROGEN IS DOUBLY BONDED TO CARBON IN A; WITH THE PROVISO THAT WHEN N IS O, A IS

>C-N(-R3)2; >C-S(R)3 OR >CH2

R1 AND R2 ARE INDEPENDENTLY SELECTED FROM THE GROUP CONSISTING OF HYDROGEN, ALKYL OF 1 TO 4 CARBONS, PHENYL; AND MAY BE JOINED TO FORM A SIX MEMBERED AROMATIC CARBOCYCLIC RING WHICH MAY BE SUBSTITUTED AND R3 IS HYDROGEN, ALKYL OF 1 TO 4 CARBON ATOMS OR PHENYL.

Description

United States Patent Office Patented Oct. 15, 1974 3,841,982 METHOD TO IMPROVE THE BRIGHTNESS OF ZINC FROM AN ALKALINE ZINCATE ELEC- US. Cl. 204-55 R 36 Claims ABSTRACT OF THE DISCLOSURE An aqueous alkaline electroplating bath comprising zinc oxide, alkali metal hydroxide, polyethyleneimine and a zinc brightening amount of a nitrogen heterocyclic compound of the formula:
wherein X is S- or A is independently selected from the group consisting n is or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of l to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
CROSS REFERENCE TO RELATED CASES This case is a continuation-in-part of US. Ser. No. 244,938, filed Apr. 17, 1972, now abandoned.
BACKGROUND OF THE INVENTION Zincate plating baths have been used as a means of electrodepositing zinc without employing cyanide ions due to the difficulty in disposing of cyanide ions in waste efiluent. Previously, it had been difficult to electrodeposit a bright zinc deposit from a zincate bath over a wide current density area. Some conventional zinc brighteners produce a bright deposit but only over a narrow current density range. The high current density areas generally resulted in a spongy or burnt deposit. It has been found through the combination of brighteners employed in the present case to obtain not only a bright deposit, but also a deposit over a wide current density area.
It has also been found that with conventional brigheners relative large amounts are required to obtain brightness while with the components of the present invention relatively less amounts are needed to obtain a bright deposit.
Some zinc brighteners have been described in US. 3,296,105; US. 3,317,412; US. 3,393,135; US. 3,472,743 and German 1,232,800.
SUMMARY OF THE INVENTION A method is described for obtaining a bright zinc electrodeposit over a wide current density area from a zincate electroplating bath by employing a combination of additives, the first being a polyethyleneimine and the second one being a heterocyclic nitrogen containing compound.
DESCRIPTION OF PREFERRED EMBODIMENTS A method is described for obtaining a bright zinc deposit from an alkaline bathpreferably a cyanide free alkaline zincate bath wherein the bath contains polyethyleneimine and a brightening amount of a nitrogen heterocyclic compound of the structure:
wherein X is S or I NR,; and
A is independently selected from the group consisting n is 0 or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
Zincate plating baths are those which generally contain zinc oxide and caustic, such as sodium hydroxide. The amount of sodium hydroxide that may be employed ranges from 50 to 250 grams/liter, preferably from about to about 200 grams/liter, while the amount of zinc oxide ranges from 5 to 50 grams/liter, preferably from about 8 to about 30 grams/liter.
The processing parameters are such that normally atmospheric temperature and pressure is employed, although temperatures up to 55 C. may also be employed, and even more preferably 15 to about 45 C. The cathode current density ranges from about 5 to 25 amps per sq. ft. while the anode current density ranges from about 10 to 35 amps per sq. ft. where the zinc deposition can occur with agitation.
Other agents may also be present in the bath, such as those described in the above patents. Examples of such suitable agents may be anisaldehyde, glue, polyvinyl alcohol and the glycerol ester of polyvinyl alcohol wherein these alcohols have a molecular weight of 5,000 to 20.- 000. Other polymers that may be employed are gelatin, peptone, and the like. In addition, chelating agents or agents which can form a complex with the metal zinc in the bath may also be employed, such as nitrilotriacetic acid and the various alkali metal salts, such as the sodium salt, ethylenediaminetetraacetic acid, and its water soluble salts, such as sodium, and the like.
The polyethyleneimine that may be used in the present case has a molecular weight ranging from 1,000 to 400,- 000, preferably 600 to 60,000 where the percentage of primary, secondary and tertiary nitrogen atoms is about 25, 50, and 25% respectively.
A zincate bath that may be employed in the present invention is as follows:
The bath pH may be adjusted by adding NaOl-I. Some of the nitrogen heterocylic compounds that may be employed in the present invention are as follows.
TNH; s H N N n N s T511 K TNH: H N
' l uHs s =s /N HZN j Tsn s s -sH -s-on3 n l HzN H l CH3 CH3 \FNH mom HzN If 1? H H n N N Ts-orn H H-sn nm N N E N S S H S H 71 1 HzN -N N m B4 --N wherein R is a water solubilizing group.
By water solubilizing group is meant any substituent on the six membered carbocyclic ring which will improve the water solubility of the compound. Such groups are hydroxy, alkoxy, such as methoxy or ethoxy and the like, carboxy, amino, and the like. In addition, R may be other groups which are not detrimental to the electrodeposition of zinc such as chloro, bromo, cyano (CN), nitro and the like.
EXAMPLE 1 A zincate plating bath was formulated containing the following components and was used to electrodeposit zinc onto a steel substrate at a cathode current density of ASP and a temperature of 75 F.
Sodium hydroxide 140 grams/liter; zinc oxide -12 grams/liter; polyethyleneimine (1,200 molecular weight) 2 grams/liter, nitrilotriacetic acid trisodium salt 1 gram/ liter; and Z-amino-benzothiazole 0.03 grams/liter.
After plating rod like structures in a typical barrel plating apparatus for 25-30 minutes a uniform bright zinc deposit of 0.2-0.3 mil thickness was obtained. The initial bath pH is about 14.
EXAMPLE 2 Zincate plating bath similar to the above was also prepared but further including 0.1 g./l. of polyvinyl alcohol. A bright zinc deposit was obtained over a broad current density range following the procedure of Example #1.
EXAMPLE 3 The procedure of Example #1 was followed, except that the bath also contained 0.1 grams/liter of anisaldehyde with equivalent results being obtained.
EXAMPLE 4 The procedure of Example #1 was followed, except that the bath also contained 0.1 grams/liter of anisaldehyde and 0.1 grams/liter of polyvinyl alcohol with equivalent results being obtained.
EXAMPLE 5 A cyanide free alkaline zincate bath was formulated as follows:
G./l. NaOH 140 ZnO 15 Z-mercaptobenzothiazole 0.03 polyethyleneimine (1200 molecular wt.) 3
Following the procedure of Example #1 equivalently good results were obtained.
What is claimed is:
1. An aqueous alkaline electroplating bath comprising inc oxide, alkali metal hydroxide, polyethyleneimine having a molecular weight of from 1,000 to 400,000 and being present in a concentration of 0.2 to grams per liter and a zinc brightening amount of a nitrogen heterocyclic compound of the formula:
i 3)n wherein X is -S- or I!\IR3; and
A is independently selected from the group consisting of 11 is 0 or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is O, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbons, phenyl; and may be joined to form a six membered aromatic carbocyclic ring which may be substituted and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
2. The bath of Claim 1 wherein R and R are joined to form a six membered aromatic carbocyclic ring.
3. The bath of Claim 2 wherein the carbocyclic ring is substituted by an amino group.
4. The bath of Claim 2 wherein the carbocyclic ring is substituted by a bath solubilizing group.
5. The bath of Claim 1 wherein the nitrogen heterocyclic compound is present in an amount ranging from about 0.005 to about 5 grams/ liter.
6. The bath of Claim 1 wherein X is S.
7. The bath of Claim 1 wherein X is -I IRa.
'8. The bath of Claim 1 wherein A is 9. The bath of Claim 1 wherein A is 10. The bath of Claim 1 wherein A is 11. The bath of Claim 1 wherein A is 12. The bath of Claim 1 wherein n is 0.
13. The bath of Claim 1 wherein R is hydrogen.
1-4. The bath of Claim 1 wherein R and R are hydrogen.
15. The bath of Claim 1 wherein the nitrogen heterocyclic compound is aminobenzothiazole.
16. The bath of Claim 1 wherein the nitrogen heterocyclic compound is an amino-2-mercaptobenzothiazole.
17. The bath of Claim 1 wherein the nitrogen heterocyclic compound is 2-imino, 3-a1kyl benzothiazole.
18. A method of depositing bright zinc from a zincate electroplating bath comprising electrolyzing the bath of Claim 1 for a period of time suflicient to form a bright zinc deposit onto a cathodic surface.
19. The method of Claim 18 wherein R and R are joined to form a six membered aromatic carbocyclic ring.
20. The method of Claim 19 wherein the carbocyclic ring is substituted by an amino group.
21. The method of Claim 19 wherein the carbocyclic ring is substituted by a bath solubilizing group.
22. The method of Claim 18 wherein the nitrogen heterocyclic compound is present in an amount ranging from about 0.005 to about 5 grams/ liter.
23. The method of Claim 18 wherein X is S.
24. The method of Claim 18 wherein X is ALB.
'25. The method of Claim 18 wherein A is J a)z- 26. The method of Claim 18 wherein A is 27. The method of Claim 18 wherein A is -.iJ-s (R3). 28. The method of Claim 18 wherein A is 29. The method of Claim 18 wherein n is 0.
30. The method of Claim 18 wherein R is hydrogen.
31. The method of Claim 18 wherein R and R are hydrogen.
32. The method of Claim 18 wherein the nitrogen heterocyclic compound is aminobenzothiazole.
33. The method of Claim 18 wherein the nitrogen heterocyclic compound is an amino2-mercaptobenzothiazole.
34. The method of Claim 18 wherein the nitrogen heterocyclic compound is 2-imino, 3'alkyl benzothiazole.
35. The method of Claim 18 wherein the cathodic surface is metallic.
36. A cyanide free alkaline zincate electroplating bath comprising zinc oxide, alkali metal hydroxide, polyethyleneimine having a molecular weight of from 1,000 to 400,000 and being present in a concentration from 0.2 to 100 grams per liter and a zinc brightening amount of a nitrogen heterocyclic compound of the formula:
wherein X is S- or l lR and A is independently selected from the group consisting of n is O or 1; when n is 0, nitrogen is doubly bonded to carbon in A; with the proviso that when n is 0, A is R and R are independently selected from the group consisting of hydrogen, alkyl of 1 to 4 carbon atoms, phenyl; and may be joined to form a six membered aromatic carbocyclic ring which may be substituted and R is hydrogen, alkyl of 1 to 4 carbon atoms or phenyl.
References Cited UNITED STATES PATENTS 2,853,444 9/1958 Pye et a1 204- R X 2,892,760 6/1959 Giindel et a1 204-44 3,267,010 8/ 1966 Creutz et a1 20452 R 3,672,971 6/1972 Senge et al. 204-55 R 3,723,263 3/ 1973 Rosenberg 204-55 R FOREIGN PATENTS 1,243,488 6/1967 Germany 204-55 R 1,263,445 3/ 196 8 Germany 20455 R a GERALD L. KAPLAN, Primary Examiner

Claims (1)

1. AN AQUEOUS ALKALINE ELECTROPLATING BATH COMPRISING INC OXIDE, ALKALI METAL HYDROXIDE, POLYETHYLENEIMINE HAVING A MOLECULAR WEIGHT OF FROM 1,000 TO 400,000 AND BEING PRESENT IN A CONCENTRATION OF 0.2 TO 100 GRAMS PER LITER AND A ZINC BRIGHTENING AMOUNT OF A NITROGEN HETEROCYCLIC COMPOUND OF THE FORMULA:
US00333927A 1972-04-17 1973-02-20 Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath Expired - Lifetime US3841982A (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
US00333927A US3841982A (en) 1972-04-17 1973-02-20 Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath
NL7304246A NL7304246A (en) 1972-04-17 1973-03-27
FR7311420A FR2180708B1 (en) 1972-04-17 1973-03-29
DE2318984A DE2318984C2 (en) 1972-04-17 1973-04-14 Aqueous alkaline bath and process for the deposition of shiny zinc coatings
CA169,009A CA1009178A (en) 1972-04-17 1973-04-16 Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath
GB1826373A GB1387529A (en) 1972-04-17 1973-04-16 Method to improve the brightness of zinc from an alkaline zincate electrode-position bath
IT49467/73A IT983031B (en) 1972-04-17 1973-04-16 METHOD FOR STORING BRIGHT ZINC ELECTROLYTES AND BATHROOMS USED IN IT
AR247599A AR197894A1 (en) 1972-04-17 1973-04-17 AQUEOUS ALKALINE ELECTROPLATE BATH
JP48042757A JPS4917324A (en) 1972-04-17 1973-04-17

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US24493872A 1972-04-17 1972-04-17
US00333927A US3841982A (en) 1972-04-17 1973-02-20 Method to improve the brightness of zinc from an alkaline zincate electrodeposition bath

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JP (1) JPS4917324A (en)
AR (1) AR197894A1 (en)
CA (1) CA1009178A (en)
DE (1) DE2318984C2 (en)
FR (1) FR2180708B1 (en)
GB (1) GB1387529A (en)
IT (1) IT983031B (en)
NL (1) NL7304246A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5084542A (en) * 1990-05-31 1992-01-28 E. I. Du Pont De Nemours And Company Epoxy/isocyanate crosslinked coatings containing 1,3-disubstituted imidazole-2-thione catalysts
US6656606B1 (en) 2000-08-17 2003-12-02 The Westaim Corporation Electroplated aluminum parts and process of production
WO2013056996A1 (en) * 2011-10-19 2013-04-25 Basf Se Formulations, use thereof as or to produce dishwashing detergents, and production thereof
CN103842559A (en) * 2011-10-04 2014-06-04 杰富意钢铁株式会社 Production method for zinc-electroplated steel sheets

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5332771B2 (en) * 1973-12-10 1978-09-09

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1480997A (en) * 1966-05-25 1967-05-12 Schering Ag Alkaline zincic brightening bath, free of cyanides
DE1935821B2 (en) * 1969-07-15 1972-03-16 Riedel & Co, 4800 Bielefeld PROCESS FOR THE PRODUCTION OF A GLOSS ADDITIVE FOR ALKALINE CYANIDE-FREE ZINC BATHS

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5084542A (en) * 1990-05-31 1992-01-28 E. I. Du Pont De Nemours And Company Epoxy/isocyanate crosslinked coatings containing 1,3-disubstituted imidazole-2-thione catalysts
US6656606B1 (en) 2000-08-17 2003-12-02 The Westaim Corporation Electroplated aluminum parts and process of production
US6692630B2 (en) 2000-08-17 2004-02-17 The Westaim Corporation Electroplated aluminum parts and process for production
CN103842559A (en) * 2011-10-04 2014-06-04 杰富意钢铁株式会社 Production method for zinc-electroplated steel sheets
CN103842559B (en) * 2011-10-04 2016-11-09 杰富意钢铁株式会社 Manufacturing method of electrogalvanized steel sheet
WO2013056996A1 (en) * 2011-10-19 2013-04-25 Basf Se Formulations, use thereof as or to produce dishwashing detergents, and production thereof
US8574374B2 (en) 2011-10-19 2013-11-05 Basf Se Formulations, their use as or for producing dishwashing compositions and their preparation
KR20140088566A (en) * 2011-10-19 2014-07-10 바스프 에스이 Formulations, use thereof as or to produce dishwashing detergents, and production thereof
RU2607085C2 (en) * 2011-10-19 2017-01-10 Басф Се Compositions, use thereof as or for preparing agents for dish washing and preparation thereof
KR101884618B1 (en) 2011-10-19 2018-08-02 바스프 에스이 Formulations, use thereof as or to produce dishwashing detergents, and production thereof

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FR2180708B1 (en) 1977-04-29
GB1387529A (en) 1975-03-19
DE2318984C2 (en) 1982-11-11
CA1009178A (en) 1977-04-26
AR197894A1 (en) 1974-05-15
NL7304246A (en) 1973-10-19
IT983031B (en) 1974-10-31
DE2318984A1 (en) 1973-11-08
JPS4917324A (en) 1974-02-15
FR2180708A1 (en) 1973-11-30

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