EP3067444B1 - Deposition of decorative palladium iron alloy coatings on metallic substances - Google Patents
Deposition of decorative palladium iron alloy coatings on metallic substances Download PDFInfo
- Publication number
- EP3067444B1 EP3067444B1 EP16156476.0A EP16156476A EP3067444B1 EP 3067444 B1 EP3067444 B1 EP 3067444B1 EP 16156476 A EP16156476 A EP 16156476A EP 3067444 B1 EP3067444 B1 EP 3067444B1
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- EP
- European Patent Office
- Prior art keywords
- palladium
- iron
- electrolyte bath
- alloy
- electrolyte
- 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.)
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- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 title claims description 61
- 229910052763 palladium Inorganic materials 0.000 title claims description 27
- 238000000576 coating method Methods 0.000 title claims description 24
- 229910000640 Fe alloy Inorganic materials 0.000 title claims description 18
- 230000008021 deposition Effects 0.000 title claims description 12
- 239000007769 metal material Substances 0.000 title 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 55
- 239000003792 electrolyte Substances 0.000 claims description 38
- 229910052742 iron Inorganic materials 0.000 claims description 28
- 229910045601 alloy Inorganic materials 0.000 claims description 19
- 239000000956 alloy Substances 0.000 claims description 19
- 229910052751 metal Inorganic materials 0.000 claims description 18
- 239000002184 metal Substances 0.000 claims description 18
- 239000011248 coating agent Substances 0.000 claims description 14
- 238000005260 corrosion Methods 0.000 claims description 14
- 230000007797 corrosion Effects 0.000 claims description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 12
- 239000010949 copper Substances 0.000 claims description 12
- 238000000151 deposition Methods 0.000 claims description 12
- 150000003839 salts Chemical class 0.000 claims description 11
- 239000000080 wetting agent Substances 0.000 claims description 11
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 9
- 229910052802 copper Inorganic materials 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- 229910001252 Pd alloy Inorganic materials 0.000 claims description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims description 7
- 229910002651 NO3 Inorganic materials 0.000 claims description 7
- 238000005299 abrasion Methods 0.000 claims description 7
- 238000005275 alloying Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 239000003381 stabilizer Substances 0.000 claims description 7
- 229910001369 Brass Inorganic materials 0.000 claims description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 6
- 230000001464 adherent effect Effects 0.000 claims description 6
- 229910021529 ammonia Inorganic materials 0.000 claims description 6
- 239000010951 brass Substances 0.000 claims description 6
- KWIUHFFTVRNATP-UHFFFAOYSA-N glycine betaine Chemical compound C[N+](C)(C)CC([O-])=O KWIUHFFTVRNATP-UHFFFAOYSA-N 0.000 claims description 6
- 150000002739 metals Chemical class 0.000 claims description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-K Citrate Chemical compound [O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O KRKNYBCHXYNGOX-UHFFFAOYSA-K 0.000 claims description 5
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 5
- 239000002280 amphoteric surfactant Substances 0.000 claims description 5
- 229910002056 binary alloy Inorganic materials 0.000 claims description 5
- OTYBMLCTZGSZBG-UHFFFAOYSA-L potassium sulfate Chemical compound [K+].[K+].[O-]S([O-])(=O)=O OTYBMLCTZGSZBG-UHFFFAOYSA-L 0.000 claims description 5
- 229910052939 potassium sulfate Inorganic materials 0.000 claims description 5
- 235000011151 potassium sulphates Nutrition 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 4
- -1 alkyl ether sulfonates Chemical class 0.000 claims description 4
- 239000003638 chemical reducing agent Substances 0.000 claims description 4
- 238000005868 electrolysis reaction Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 239000011734 sodium Substances 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 239000011135 tin Substances 0.000 claims description 4
- 229910052725 zinc Inorganic materials 0.000 claims description 4
- 239000011701 zinc Substances 0.000 claims description 4
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 claims description 3
- PMVSDNDAUGGCCE-TYYBGVCCSA-L Ferrous fumarate Chemical compound [Fe+2].[O-]C(=O)\C=C\C([O-])=O PMVSDNDAUGGCCE-TYYBGVCCSA-L 0.000 claims description 3
- OFOBLEOULBTSOW-UHFFFAOYSA-L Malonate Chemical compound [O-]C(=O)CC([O-])=O OFOBLEOULBTSOW-UHFFFAOYSA-L 0.000 claims description 3
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 3
- 239000012670 alkaline solution Substances 0.000 claims description 3
- 125000003118 aryl group Chemical group 0.000 claims description 3
- 229960003237 betaine Drugs 0.000 claims description 3
- 238000005282 brightening Methods 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 150000002191 fatty alcohols Chemical class 0.000 claims description 3
- 150000002941 palladium compounds Chemical class 0.000 claims description 3
- 239000004033 plastic Substances 0.000 claims description 3
- 229920003023 plastic Polymers 0.000 claims description 3
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 claims description 3
- 229940081974 saccharin Drugs 0.000 claims description 3
- 235000019204 saccharin Nutrition 0.000 claims description 3
- 239000000901 saccharin and its Na,K and Ca salt Substances 0.000 claims description 3
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 3
- 235000011152 sodium sulphate Nutrition 0.000 claims description 3
- 229940095064 tartrate Drugs 0.000 claims description 3
- 229910052718 tin Inorganic materials 0.000 claims description 3
- 229910019142 PO4 Inorganic materials 0.000 claims description 2
- 150000003868 ammonium compounds Chemical class 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 150000002505 iron Chemical class 0.000 claims description 2
- 150000002736 metal compounds Chemical class 0.000 claims description 2
- 150000002940 palladium Chemical class 0.000 claims description 2
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 claims description 2
- 235000021317 phosphate Nutrition 0.000 claims description 2
- 150000003871 sulfonates Chemical class 0.000 claims description 2
- PSBDWGZCVUAZQS-UHFFFAOYSA-N (dimethylsulfonio)acetate Chemical compound C[S+](C)CC([O-])=O PSBDWGZCVUAZQS-UHFFFAOYSA-N 0.000 claims 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 claims 1
- 229940117986 sulfobetaine Drugs 0.000 claims 1
- 239000000047 product Substances 0.000 description 13
- 239000010948 rhodium Substances 0.000 description 11
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- 229910052703 rhodium Inorganic materials 0.000 description 10
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 10
- 239000010931 gold Substances 0.000 description 8
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 7
- 229910052737 gold Inorganic materials 0.000 description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 5
- 150000003863 ammonium salts Chemical class 0.000 description 5
- 229910052707 ruthenium Inorganic materials 0.000 description 5
- 239000000243 solution Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 229910000906 Bronze Inorganic materials 0.000 description 3
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 3
- 230000002378 acidificating effect Effects 0.000 description 3
- 239000008367 deionised water Substances 0.000 description 3
- 229910021641 deionized water Inorganic materials 0.000 description 3
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 3
- 231100000206 health hazard Toxicity 0.000 description 3
- 238000010348 incorporation Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 3
- 229910000510 noble metal Inorganic materials 0.000 description 3
- 229910052697 platinum Inorganic materials 0.000 description 3
- 239000010970 precious metal Substances 0.000 description 3
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 2
- PNTWXEIQXBRCPS-CLKGFSLHSA-N Pd-II Natural products C1=CC(=O)OC2=C3[C@H](OC(=O)C(/C)=C/C)[C@H](OC(=O)C(\C)=C\C)C(C)(C)OC3=CC=C21 PNTWXEIQXBRCPS-CLKGFSLHSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 239000010974 bronze Substances 0.000 description 2
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 229910000531 Co alloy Inorganic materials 0.000 description 1
- 229910001229 Pot metal Inorganic materials 0.000 description 1
- 229910000929 Ru alloy Inorganic materials 0.000 description 1
- 229910001128 Sn alloy Inorganic materials 0.000 description 1
- 229910001297 Zn alloy Inorganic materials 0.000 description 1
- YPPQDPIIWDQYRY-UHFFFAOYSA-N [Ru].[Rh] Chemical compound [Ru].[Rh] YPPQDPIIWDQYRY-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 239000002738 chelating agent Substances 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004870 electrical engineering Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910000358 iron sulfate Inorganic materials 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- XSKIUFGOTYHDLC-UHFFFAOYSA-N palladium rhodium Chemical compound [Rh].[Pd] XSKIUFGOTYHDLC-UHFFFAOYSA-N 0.000 description 1
- OYJSZRRJQJAOFK-UHFFFAOYSA-N palladium ruthenium Chemical compound [Ru].[Pd] OYJSZRRJQJAOFK-UHFFFAOYSA-N 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910052714 tellurium Inorganic materials 0.000 description 1
- PORWMNRCUJJQNO-UHFFFAOYSA-N tellurium atom Chemical compound [Te] PORWMNRCUJJQNO-UHFFFAOYSA-N 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
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
- C25D3/56—Electroplating: Baths therefor from solutions of alloys
-
- 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
- C25D3/56—Electroplating: Baths therefor from solutions of alloys
- C25D3/567—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of platinum group metals
-
- 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
- C25D3/20—Electroplating: Baths therefor from solutions of iron
-
- 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
- C25D3/50—Electroplating: Baths therefor from solutions of platinum group metals
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/10—Electroplating with more than one layer of the same or of different metals
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/60—Electroplating characterised by the structure or texture of the layers
- C25D5/605—Surface topography of the layers, e.g. rough, dendritic or nodular layers
- C25D5/611—Smooth layers
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/627—Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/005—Jewels; Clockworks; Coins
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
Definitions
- the present invention is directed to an electrolytic bath composition for depositing white, high-gloss, crack-free, abrasion and corrosion-resistant palladium-iron alloys from alkaline aqueous baths, objects and articles coated with these alloys, and a process for producing the coated objects Items.
- the electrolytes are out JP, 2001-192885, A are also based on ammonium salts and contain additional brighteners and possibly different alloying metals such as iron or tellurium.
- JP, 2001-181887, A describes palladium-iron alloy baths which are also based on ammonium salts, and additionally contain EDTA.
- strong chelating agents are generally undesirable in electrolytes since they introduce difficulties in wastewater treatment.
- JP, 10-046384, A describes palladium alloy baths for the electronics industry. Iron as alloying metal is mentioned, the electrolytes are based on ammonium salts. The examples, however, relate only to palladium-cobalt alloys. Alloys of palladium-iron, palladium-nickel, palladium-rhodium and palladium-ruthenium should be produced in the same way.
- DE2657925 describes ammonia-free, semi-glossy to bright palladium and palladium alloy baths for electrical engineering, but iron is not mentioned as alloying metal.
- EP 1396559A1 is an electrolytic bath for the cathodic deposition of binary alloys to form white, corrosion-resistant, crack-free and (high) glossy coatings on at least on their surface metallic or electrically conductive or conductive coated objects known which bath as alloying metals at least one palladium compound as the primary metal and contains at least one iron compound as secondary metal, and for the deposition of a Pd / Fe alloy having a content in the range of 5 to 15 wt% Fe - as an aqueous alkaline solution having a pH of 7.5 to 9 and as essential other components at least one wetting agent from the group of amphoteric surfactants and additionally contains at least one of the usual in palladium baths contained gloss additives and conductive salts, pH stabilizers and voltage reducer, wherein the electrolyte bath has a content of palladium of 0.5 to 15 g / l and of iron from 0.2 to 2 g / l au f réelle.
- the object of the present invention to develop baths from which high gloss, binary palladium-iron alloys can be deposited without any addition of other metals and.
- the alloy baths during operation should not present an odor nuisance or health hazard through the release of irritating gases or vapors, and moreover contain no strong complexing agents such as EDTA or NTA, which would cause problems in wastewater treatment.
- the production is to be cheapened by the use of such alloy baths, and resources of the expensive palladium are spared.
- Such alloys are therefore particularly well suited for any metallic white decorative coating, e.g. of costume jewelery, but also for industrial applications, especially in the electronics industry.
- the baths contain 0.5-15 g / l of palladium, 0.2-2 g / l of iron, conductive salts, brighteners and wetting agents. It is possible to deposit layer thicknesses> 5 ⁇ high gloss, crack-free.
- the corrosion resistance is comparable to pure palladium, the abrasion resistance is better than pure palladium.
- the invention relates to a novel electrolyte bath for the cathodic deposition of binary alloys with the formation of white, corrosion-resistant, crack-free and (high) glossy coatings on at least metallic or electrically conductive or conductively coated objects on its surface, which bath contains at least one palladium compound as alloying metals.
- a palladium salt as a primary metal and at least one iron compound, in particular an iron salt, as a secondary metal, which for the deposition of a Pd / Fe alloy with a content in the range of 5 to 15 wt% Fe - as an aqueous, alkaline solution with a pH value of 7.5 to 9, and in addition to the metal compounds mentioned as essential further components at least one wetting agent from the group of amphoteric surfactants, and at least one brightener and conductive salts, pH stabilizers and voltage reducer, wherein the electrolyte bath a Content of P alladium of 0.5 to 15 g / l and iron of 0.2 to 2 g / l and is free of ammonia and ammonium compounds.
- the new electrolyte bath is characterized in that it contains betaines and sulfobetaines in quantities of 0.5-2 g / l as wetting agents from the group of the amphoteric surfactants, and aromatic N-heterocycles substituted as brightening agents, and as stress relievers saccharin or organic sulfonates, and as conductive salts and / or pH stabilizers, sodium or potassium sulfate, chloride, nitrate, citrate, tartrate, or malonate.
- the pH of the new alloy bath should be maintained in the range of 7.5 - 9, since at lower pH values (approximately between 7 and 7.5) the incorporation rates of iron decrease. At higher pH values (approximately between 9 and 10), burns occur in the high current density range.
- the pH is advantageously adjusted by means of sodium or potassium hydroxide.
- the iron content of the deposited alloy at 5-15 wt .-% Fe since at incorporation rates> 15 wt .- Fe Fe the layers are cracked, and at incorporation rates ⁇ 5% by weight, the deposition receives a milky appearance.
- palladium in divalent form for example as palladium chloride, sulfate or nitrate, and iron as iron sulfate, chloride, nitrate or citrate are present in the electrolyte bath.
- an electrolyte bath which is characterized in that it has a content of palladium of 2 to 8 g / l, and more preferably of 4 to 6 g / l and of iron preferably 0.5 to 1 Contains 5 g / l.
- conductive salts and pH stabilizers such as sodium or potassium sulfate, - nitrate, chloride, citrate, tartrate, or malonate, and further as wetting agents alkyl ether sulfonates, alkyl ether phosphates or fatty alcohol alkoxylates. All conductive salts or pH stabilizers used in the invention are sodium or potassium salts.
- the total thickness of the binary palladium-iron coating to be achieved in the context of the invention is in each case 0.1 to 5 ⁇ m, in particular approximately 0.5 to 3 ⁇ m, depending on the field of use.
- a further, electrodeposited final layer of gold and / or another noble metal such as, in particular, rhodium, platinum, ruthenium or an alloy of the same, can be arranged, by means of which the already high usability and the gloss of the coating is still increased.
- an adherent gold adherent intermediate layer adhered thereto may be disposed on the palladium-iron overlay and an electrolytically deposited, adherent final layer of gold and / or another thereon Noble metal, in particular rhodium, platinum, ruthenium or an alloy of the same.
- the intermediate layer of adhesive gold may have a thickness of 0.05 to 0.3 microns.
- the coated new objects or articles can be coated with a final layer of an alloy formed with rhodium and ruthenium, preferably in the weight% ratio of (70 to 90) to (30 to 10), in particular of about 80 to 20 his. It is the object of the present invention to adjust the concentration of the metal salts, wetting agents, brighteners and the additional ingredients in the mold and to vary within the weight ratios according to the invention so that the electrolyte solution is clear and remains, so that no metal salts precipitate, and that just according to the invention desired, shiny, adherent, crack-free, abrasion and corrosion resistant layers or coatings are deposited.
- the working temperature of the electrolyte baths according to the invention is between 35 and 75 ° C.
- the current density can be set to between 0.01 and 10 amps / dm 2 , depending on the type of coating system.
- current densities between 0.05 and 0.50 A / dm 2 are particularly preferred.
- insoluble anodes When using the electrolyte baths according to the invention, various insoluble anodes can be used.
- insoluble anodes those of a material selected from the group consisting of platinum-plated titanium and iridium-transition metal mixed oxide or combinations of these materials may be used, with platinized titanium anodes being preferred.
- the production of the objects or articles coated according to the invention is usually carried out as follows: On a respective base material, for example consisting of brass, zinc, iron, steel or their alloys or other materials made conductive at least on its surface is either directly or on a previously applied copper undercoat, deposited from cyanide or non-cyanidic alkaline and / or from acidic copper baths, the new binary palladium-iron alloy is deposited either directly or on Cu / Sn / Zn alloy of cyanide bronze baths applied there.
- This palladium-iron alloy is in itself a final layer. However, it can be further coated by methods known per se. Other coatings may, as mentioned above, be gold-containing or other noble metal-containing layers, such as those of rhodium, platinum, ruthenium or their alloys.
- the base material is first copper-plated, then coated with palladium and finally receives the desired finish by coating with gold, rhodium or other precious metals or their alloys.
- a thickness of the palladium layer of about 0.5-5 microns is recommended. Usually a layer thickness of about 1 ⁇ m is considered sufficient.
- rhodium-ruthenium alloy instead of a rhodium final layer. If, for example, an alloy in the ratio by weight of rhodium to ruthenium of 80:20 is deposited as the final layer, in addition to the savings in the intermediate layers mentioned above, 20% of the very expensive rhodium would be saved.
- the invention further relates to a per se conventional method for cathodic deposition of the binary alloys according to the invention with an Fe content of 5-15% by weight on at least on their surface metallic or electrically conductive or conductive coated objects or articles using the electrolyte according to the invention ,
- the corrosion resistance of the palladium-iron alloy in comparison with a coating of a pure palladium electrolyte (Gapal TS, product of Garhöfer GesmbH), produced on the same base material in the SO 2 test is equally good.
- a brass disc in the palladium-iron electrolyte of example 1 and a brass disc in a pure palladium electrolyte (Gapal TS, product of Garhöfer GesmbH) were coated with 2 .mu.m. Ansch manend both discs were abraded. The pure palladium was rubbed much earlier than the palladium-iron alloy.
- a jewelery blank made of die-cast zinc is electrolytically degreased in a weakly alkaline cyanide-free cleaner (degreasing 1018, product of the company Ing. W. Garhöfer GesmbH) at 25 ° C. for 30 seconds at 10 A / dm 2 .
- a weakly alkaline cyanide-free cleaner degreasing 1018, product of the company Ing. W. Garhöfer GesmbH
- the jewelry blank is rinsed in deionized water and in an alkaline cyanide Vorkupferbad with 22 g / l Cu and 34 g / l KCN ("Cuproga", product of the company Ing. W. Garhöfer GesmbH) were 5 microns of copper at 1 A / dm 2 and 50 ° C deposited.
- the pre-coppered jewelry blank is then dekapiert in 5% sulfuric acid solution for 30 s and in an acidic copper bath with 50 g / l Cu and 60 g / l sulfuric acid ("IWG Cu 550", product of the company Ing. W. Garhöfer GesmbH) 15 ⁇ m copper leveling and high gloss deposited at 4 A / dm 2 and 25 ° C.
- the thus coppered part is rinsed and pre-immersed in a 10% KCN solution.
- the galvanized part of the jewelry performed just as well in the corrosion tests as a jewelery part coated with pure palladium using the same process.
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Description
Die vorliegende Erfindung ist auf eine Elektrolytbadzusammensetzung zur Abscheidung weißer, hochglänzender, rissfreier, abriebs- und korrosionsbeständiger Palladium-Eisenlegierungen aus alkalischen wässrigen Bädern gerichtet, weiters auf Objekte und Artikel, welche mit diesen Legierungen beschichtet sind sowie auf ein Verfahren zur Herstellung der beschichteten Objekte und Artikel.The present invention is directed to an electrolytic bath composition for depositing white, high-gloss, crack-free, abrasion and corrosion-resistant palladium-iron alloys from alkaline aqueous baths, objects and articles coated with these alloys, and a process for producing the coated objects Items.
Methoden zur Abscheidung von Palladium-Eisenlegierungen aus wässrig alkalischen Elektrolyten sind aus dem AiF Forschungsvorhaben Nr. 10302 N des Forschungsinstitutes für Edelmetalle und Metallchemie Schwäbisch Gmünd, "Galvanische Abscheidung von Palladium-Eisen-Legierungsüberzügen für funktionelle Anwendungen und deren Charakterisierung" bekannt. Jedoch konnten mit einem dort beschriebenen Elektrolyten unter den dort beschriebenen Bedingungen keine hochglänzenden Legierungen abgeschieden werden. Außerdem basiert der beschriebene Elektrolyt auf Ammoniumsalzen, der pH-Wert wird mit Ammoniak eingestellt. Bei Elektrolyttemperaturen von 55 °C muss daher ständig Ammoniak nachgeliefert werden, um den pH-Wert konstant zu halten, außerdem entstehen dadurch enorme Geruchs- und Gesundheitsbelästigungen für die Betreiber solcher Bäder.Methods for the deposition of palladium-iron alloys from aqueous alkaline electrolytes are known from the AiF research project No. 10302 N of the Research Institute for Precious Metals and Metal Chemistry Schwäbisch Gmünd, "Galvanic deposition of palladium-iron alloy coatings for functional applications and their characterization". However, with the electrolyte described there, no high-gloss alloys could be deposited under the conditions described there. In addition, the electrolyte described is based on ammonium salts, the pH is adjusted with ammonia. At electrolyte temperatures of 55 ° C, therefore, ammonia must be constantly replenished in order to keep the pH constant, and in addition there are enormous odor and health nuisances for the operators of such baths.
Die Elektrolyte die aus
Aus der
Auch die
Es ist Ziel der gegenwärtigen Erfindung, Bäder zu entwickeln, aus denen hochglänzende, binäre Palladium-Eisen-Legierungen ohne jeglichen Zusatz von weiteren Metallen und abgeschieden werden können. Insbesondere sollen die Legierungsbäder beim Betrieb keine Geruchsbelästigung oder Gesundheitsgefahr durch die Freisetzung von reizenden Gasen oder Dämpfen darstellen und darüber hinaus keine starken Komplexbildner wie EDTA oder NTA enthalten, die Probleme bei der Abwasserbehandlung hervorrufen würden.
Zusätzlich soll die Produktion durch den Einsatz derartiger Legierungsbäder verbilligt werden, und Ressourcen des teuren Palladiums geschont werden.
Eine Kostenersparnis von etwa 15% beim Einsatz derartiger Legierungsbäder im Vergleich zu Reinpalladiumbädern ergibt sich zum einen aus der geringeren Dichte der abgeschiedenen Palladium-Eisen-Legierung, zum anderen aus geringeren Ausschleppungsverlusten von Edelmetall, da Reinpalladiumbäder meist etwa mit einer Palladiumkonzentration von 10 g/l Palladium arbeiten, das Palladium-Eisen-Legierungsbad vorliegender Erfindung jedoch mit etwa der halben Konzentration auskommen kann.It is the object of the present invention to develop baths from which high gloss, binary palladium-iron alloys can be deposited without any addition of other metals and. In particular, the alloy baths during operation should not present an odor nuisance or health hazard through the release of irritating gases or vapors, and moreover contain no strong complexing agents such as EDTA or NTA, which would cause problems in wastewater treatment.
In addition, the production is to be cheapened by the use of such alloy baths, and resources of the expensive palladium are spared.
A cost saving of about 15% when using such alloy baths in comparison to pure palladium baths results on the one hand from the lower density of the deposited palladium-iron alloy, on the other hand from lower Ausleppungsverlusten of precious metal, since pure palladium baths usually about with a palladium concentration of 10 g / l Palladium work, but the palladium-iron alloy bath of the present invention can get by with about half the concentration.
Derartige Legierungen eignen sich daher besonders gut für jegliche metallisch weiße, dekorative Beschichtung, z.B. von Modeschmuck, aber durchaus auch für industrielle Anwendungen, wie insbesondere in der Elektronikindustrie.Such alloys are therefore particularly well suited for any metallic white decorative coating, e.g. of costume jewelery, but also for industrial applications, especially in the electronics industry.
Gemäß vorliegender Erfindung enthalten die Bäder 0,5-15 g/l Palladium, 0,2-2 g/l Eisen, Leitsalze, Glanzzusätze und Netzmittel. Es können Schichtdicken >5 µ hochglänzend, rissfrei abgeschieden werden. Die Korrosionsbeständigkeit ist vergleichbar mit Reinpalladium, die Abriebbeständigkeit ist besser als Reinpalladium.In the present invention, the baths contain 0.5-15 g / l of palladium, 0.2-2 g / l of iron, conductive salts, brighteners and wetting agents. It is possible to deposit layer thicknesses> 5 μ high gloss, crack-free. The corrosion resistance is comparable to pure palladium, the abrasion resistance is better than pure palladium.
Die Erfindung betrifft ein neues Elektrolytbad für das kathodische Abscheiden von binären Legierungen unter Bildung von weißen, korrosionsbeständigen, rissfreien und (hoch)glänzenden Überzügen auf zumindest an ihrer Oberfläche metallischen bzw. elektrisch leitfähigen oder leitfähig beschichteten Objekten, welches Bad als Legierungsmetalle zumindest eine Palladiumverbindung, insbesondere ein Palladiumsalz, als Primärmetall und zumindest eine Eisenverbindung, insbesondere ein Eisensalz, als Sekundärmetall enthält, welches für die Abscheidung einer Pd/Fe-Legierung mit einem Gehalt im Bereich von 5 bis 15 Gew-% Fe - als wässerige, alkalische Lösung mit einem pH-Wert von 7,5 bis 9, vorliegt und außer den genannten Metall-Verbindungen als wesentliche weitere Komponenten zumindest ein Netzmittel aus der Gruppe der amphoteren Tenside, und mindestens einen Glanzzusatz sowie Leitsalze, pH-Stabilisatoren und Spannungsverminderer enthält, wobei das Elektrolytbad einen Gehalt an Palladium von 0,5 bis 15 g/l und an Eisen von 0,2 bis 2 g/l aufweist und frei von Ammoniak und Ammoniumverbindungen ist. Das neue Elektrolytbad ist dadurch gekennzeichnet, dass es als Netzmittel aus der Gruppe der amphoteren Tenside Betaine und Sulfobetaine in Mengen von 0,5-2 g/l enthält, und als Glanzmittel substituierte aromatische N-Heterocyclen, und als Spannungsverminderer Saccharin oder organische Sulfonate, und als Leitsalze und/oder pH-Stabilisatoren Natrium- oder Kaliumsulfat, - chlorid, -nitrat, -citrat, -tartrat, oder -malonat, enthält.The invention relates to a novel electrolyte bath for the cathodic deposition of binary alloys with the formation of white, corrosion-resistant, crack-free and (high) glossy coatings on at least metallic or electrically conductive or conductively coated objects on its surface, which bath contains at least one palladium compound as alloying metals. in particular a palladium salt, as a primary metal and at least one iron compound, in particular an iron salt, as a secondary metal, which for the deposition of a Pd / Fe alloy with a content in the range of 5 to 15 wt% Fe - as an aqueous, alkaline solution with a pH value of 7.5 to 9, and in addition to the metal compounds mentioned as essential further components at least one wetting agent from the group of amphoteric surfactants, and at least one brightener and conductive salts, pH stabilizers and voltage reducer, wherein the electrolyte bath a Content of P alladium of 0.5 to 15 g / l and iron of 0.2 to 2 g / l and is free of ammonia and ammonium compounds. The new electrolyte bath is characterized in that it contains betaines and sulfobetaines in quantities of 0.5-2 g / l as wetting agents from the group of the amphoteric surfactants, and aromatic N-heterocycles substituted as brightening agents, and as stress relievers saccharin or organic sulfonates, and as conductive salts and / or pH stabilizers, sodium or potassium sulfate, chloride, nitrate, citrate, tartrate, or malonate.
Der pH-Wert des neuen Legierungsbades soll im Bereich 7,5 - 9 gehalten werden, da bei niedrigeren pH-Werten (etwa zwischen 7 und 7,5) die Einbauraten an Eisen sinken. Bei höheren pH-Werten (etwa zwischen 9 und 10) kommt es zu Anbrennungen im hohen Stromdichtebereich. Der pH-Wert wird vorteilhafterweise mittels Natrium- oder Kaliumhydroxid eingestellt.The pH of the new alloy bath should be maintained in the range of 7.5 - 9, since at lower pH values (approximately between 7 and 7.5) the incorporation rates of iron decrease. At higher pH values (approximately between 9 and 10), burns occur in the high current density range. The pH is advantageously adjusted by means of sodium or potassium hydroxide.
Gemäß vorliegender Erfindung liegt der Eisengehalt der abgeschiedenen Legierung bei 5-15 Gew.-% Fe, da bei Einbauraten >15 Gew.-% Fe die Schichten rissig werden, und bei Einbauraten <5 Gew-% die Abscheidung ein milchiges Aussehen erhält.
Im Rahmen der vorliegenden Erfindung hat es sich als vorteilhaft erwiesen, wenn Palladium in zweiwertiger Form, z.B. als Palladiumchlorid, -sulfat oder -nitrat, und Eisen als Eisen-sulfat, -chlorid, -nitrat oder -citrat im Elektrolytbad vorliegen.
Demgemäß ist für die Abscheidung eines Überzugs ein Elektrolytbad vorteilhafterweise vorgesehen, das sich dadurch auszeichnet, dass es einen Gehalt Palladium von 2 bis 8 g/l, und besonders bevorzugt von 4 bis 6 g/l aufweist und an Eisen bevorzugt 0,5 bis 1,5 g/l enthält.
Weiters enthalten sind Leitsalze sowie pH-Stabilisatoren wie Natrium- oder Kaliumsulfat, - nitrat, -chlorid, -citrat, -tartrat, oder -malonat, und weiters als Netzmittel Alkylethersufonate, Alkyletherphosphate oder Fettalkoholalkoxylate.
Alle in der Erfindung verwendeten Leitsalze bzw. pH-Stabilisatoren sind Natrium- oder Kaliumsalze. Beim Einsatz von Ammoniak bzw. Ammoniumsalzen bei erhöhten Temperaturen von etwa 50°C wird ständig Ammoniak ausgetrieben. Dadurch verstellt sich der pH-Wert des Bades ständig und ein kontinuierliches Arbeit ist deutlich erschwert.
Außerdem kommt es zu einer ständigen Geruchsbelästigung und Gesundheitsgefahr für die Bediener des Elektrolyten.
Weiters werden im Elektrolyten der vorliegenden Erfindung organische Säuren oder Salze nicht verwendet, die beim Betrieb des Bades mit erhöhter Temperatur Dämpfe freisetzen, die zu einer Geruchsbelästigung und/oder Gesundheitsgefahr für die Bediener des Elektrolyten führen können, z.B. Propionsäure/Propionate, Essigsäure/Acetate.
Die verschiedenen vorteilhaften erfindungsgemäßen bzw. erfindungsgemäß eingesetzten Elektrolytbäder sind im Einzelnen in den Ansprüchen 2 bis 4 beschrieben.
Auf Basis der vorliegenden Erfindung lassen sich Objekte bzw. Artikel, insbesondere Schmuck- bzw. Dekorartikel, sowie elektrotechnische bzw. elektronische Komponenten und Bauteile aus einem bevorzugterweise physiologisch verträglichen Metall, insbesondere aus Messing, Zink, Zinn, Eisen oder Stahl, oder aus Legierungen derselben oder aber aus einem leitfähig ausgerüsteten Kunststoff mit einem aus einem wie oben genannten Elektrolytbad abgeschiedenen Überzug aus einer binären Legierung aus Palladium und Eisen, in welcher das Eisen mit einem Gehalt von 5 bis 12 Gew-% vorliegt, herstellen.
Die im Rahmen der Erfindung üblicherweise zu erreichende Gesamtdicke der binären Palladium-Eisen-Beschichtung beträgt- jeweils abhängig vom Einsatzgebiet - 0,1 bis 5 µm, insbesondere etwa 0,5 bis 3 µm.
Auf der Palladium-Eisen-Beschichtung kann außen eine auf derselben festhaftende weitere, elektrolytisch abgeschiedene Finalschicht aus Gold und/oder aus einem anderem Edelmetall, wie insbesondere aus Rhodium, Platin, Ruthenium oder aus einer Legierung aus denselben, angeordnet werden, durch welche die an sich schon hohe Gebrauchsfähigkeit und der Glanz des Überzugs noch gesteigert wird.
Für weitere Verbesserungen der neuen Überzüge der genannten Objekte bzw. Artikel kann auf dem Palladium-Eisen-Überzug eine auf demselben festhaftende, elektrolytisch abgeschiedene Zwischenschicht aus Haftgold angeordnet werden, und auf dieser eine elektrolytisch abgeschiedene, haftfeste Finalschicht aus Gold und/oder aus einem anderem Edelmetall, wie insbesondere Rhodium, Platin, Ruthenium oder aus einer Legierung aus denselben.
Die Zwischenschicht aus Haftgold kann eine Dicke von 0,05 bis 0,3 µm aufweisen.
Weiters können die beschichteten neuen Objekte bzw. Artikel mit einer Finalschicht aus einer mit Rhodium und Ruthenium, vorzugsweise im Gew.-%-Verhältnis von (70 bis 90) zu (30 bis 10), insbesondere von etwa 80 zu 20, gebildeten Legierung beschichtet sein.
Es ist das Ziel der vorliegenden Erfindung die Konzentration der Metallsalze, Netzmittel, Glanzzusätze und der zusätzlichen Inhaltsstoffe in der Form einzustellen und im Rahmen der erfindungsgemäßen Gewichts-Verhältnisse so zu variieren, dass die Elektroytlösung klar ist und bleibt, dass also keine Metallsalze ausfallen, und dass eben die erfindungsgemäß angestrebten, glänzenden, festhaftenden, rissfreien, abriebs- und korrosionsbeständigen Schichten bzw. Überzüge abgeschieden werden.
Das Verfahren zur Herstellung von mit einer weißen Beschichtung bzw. mit einem derartigen korrosionsbeständigen, rissfreien, hochabrieb- und haftfesten, glänzenden Überzug versehenen Objekten bzw. Artikeln aus der Gruppe Schmuck- bzw. Dekorartikel, aus der Gruppe elektrotechnische bzw. elektronische Komponenten und Bauteile aus Messing, Zink, Zinn, Eisen oder Stahl oder aus deren Legierungen oder aber aus einem leitfähig ausgerüsteten Kunststoff, wobei, vorzugsweise auf einer auf der Oberfläche des Objekt- bzw. Artikel-Rohlings befindlichen metallischen Untergrundschicht, insbesondere aus Kupfer, eine Pd/Fe-Legierung abgeschieden wird, ist dadurch gekennzeichnet, dass die zu beschichtenden Objekte bzw. Artikel, gegebenenfalls nach einer Grundbeschichtung mit Kupfer, mittels Elektrolyse in einem Elektrolytbad gemäß einem der Ansprüche 1 bis 4 bei Temperaturen von 35 bis 75°C und Stromdichten von 0,1 bis 10 A/dm2, insbesondere von 0,2 bis 5 A/dm2, unter Einsatz von zumindest einer unlöslichen Anode der Elektrolyse unterworfen werden.
Im Zuge des Verfahrens zur elektrolytischen Aufbringung der neuen binären Palladium-Eisen-Legierungen auf die jeweiligen Grundmaterialien werden die zu beschichtenden Gegenstände, Objekte oder Artikel in das jeweilige, erfindungsgemäße Elektrolytbad getaucht und dort als Kathode geschaltet.
Die Arbeitstemperatur der erfindungsgemäßen Elektrolytbäder liegt zwischen 35 und 75 °C. Die Stromdichte kann auf zwischen 0,01 und 10 Ampere/dm2 eingestellt werden, jeweils abhängig von der Art der Beschichtungsanlage.
So werden in Trommelbeschichtungsverfahren Stromdichten zwischen 0,05 und 0,50 A/dm2 besonders bevorzugt. In Gestellbeschichtungsverfahren wählt man bevorzugt Stromdichten zwischen 0,2 und 10 A/dm2, besonders bevorzugt 0,2 bis 5 A/dm2.
Beim Einsatz der erfindungsgemäßen Elektrolytbäder können verschiedene unlösliche Anoden eingesetzt werden.
Als unlösliche Anoden können solche aus einem Material aus der Gruppe platiniertes Titan und Iridium-Übergangsmetall-Mischoxid oder Kombinationen dieser Materialien eingesetzt werden, wobei platinierte Titananoden bevorzugt sind.
Die Herstellung der erfindungsgemäß beschichteten Objekte bzw. Artikel erfolgt üblicherweise folgendermaßen:
Auf einem jeweiligen Grundmaterial, beispielsweise bestehend aus Messing, Zink, Eisen, Stahl bzw. deren Legierungen oder auch anderen zumindest auf ihrer Oberfläche leitfähig gemachten Materialien wird entweder direkt oder auf eine dort vorher aufgebrachte Kupfer- Unterschicht, abgeschieden aus cyanidischen oder nicht cyanidischen alkalischen und/oder aus sauren Kupferbädern, wird entweder direkt oder auf dort aufgebrachte Cu/Sn/Zn-Legierung aus cyanidischen Bronzebädern die neue binäre Palladium-Eisen-Legierung abgeschieden.According to the present invention, the iron content of the deposited alloy at 5-15 wt .-% Fe, since at incorporation rates> 15 wt .- Fe Fe the layers are cracked, and at incorporation rates <5% by weight, the deposition receives a milky appearance.
In the context of the present invention, it has proved to be advantageous if palladium in divalent form, for example as palladium chloride, sulfate or nitrate, and iron as iron sulfate, chloride, nitrate or citrate are present in the electrolyte bath.
Accordingly, for the deposition of a coating, an electrolyte bath is advantageously provided, which is characterized in that it has a content of palladium of 2 to 8 g / l, and more preferably of 4 to 6 g / l and of iron preferably 0.5 to 1 Contains 5 g / l.
Further included are conductive salts and pH stabilizers such as sodium or potassium sulfate, - nitrate, chloride, citrate, tartrate, or malonate, and further as wetting agents alkyl ether sulfonates, alkyl ether phosphates or fatty alcohol alkoxylates.
All conductive salts or pH stabilizers used in the invention are sodium or potassium salts. When using ammonia or ammonium salts at elevated temperatures of about 50 ° C, ammonia is constantly expelled. As a result, the pH of the bath constantly adjusted and continuous work is much more difficult.
In addition, there is a constant odor nuisance and health hazard for the operator of the electrolyte.
Furthermore, in the electrolyte of the present invention, organic acids or salts are not used which release vapors during operation of the bath at elevated temperature, which can lead to an odor nuisance and / or health hazard for the operators of the electrolyte, for example propionic acid / propionates, acetic acid / acetates.
The various advantageous electrolyte baths according to the invention or used according to the invention are described in detail in claims 2 to 4.
On the basis of the present invention, objects or articles, in particular jewelery or decorative articles, as well as electrotechnical or electronic components and components of a preferably physiologically acceptable metal, in particular brass, zinc, tin, iron or steel, or alloys thereof or a conductive plastic with one of the above said coating deposited from a binary alloy of palladium and iron, in which the iron is present at a level of from 5 to 12% by weight.
The total thickness of the binary palladium-iron coating to be achieved in the context of the invention is in each case 0.1 to 5 μm, in particular approximately 0.5 to 3 μm, depending on the field of use.
On the outside of the palladium-iron coating, a further, electrodeposited final layer of gold and / or another noble metal, such as, in particular, rhodium, platinum, ruthenium or an alloy of the same, can be arranged, by means of which the already high usability and the gloss of the coating is still increased.
For further improvements of the novel coatings of said articles, an adherent gold adherent intermediate layer adhered thereto may be disposed on the palladium-iron overlay and an electrolytically deposited, adherent final layer of gold and / or another thereon Noble metal, in particular rhodium, platinum, ruthenium or an alloy of the same.
The intermediate layer of adhesive gold may have a thickness of 0.05 to 0.3 microns.
Furthermore, the coated new objects or articles can be coated with a final layer of an alloy formed with rhodium and ruthenium, preferably in the weight% ratio of (70 to 90) to (30 to 10), in particular of about 80 to 20 his.
It is the object of the present invention to adjust the concentration of the metal salts, wetting agents, brighteners and the additional ingredients in the mold and to vary within the weight ratios according to the invention so that the electrolyte solution is clear and remains, so that no metal salts precipitate, and that just according to the invention desired, shiny, adherent, crack-free, abrasion and corrosion resistant layers or coatings are deposited.
The process for the production of objects with a white coating or with such a corrosion-resistant, crack-free, highly abrasion-resistant and adherent, glossy coating from the group jewelry or decorative items, from the group of electrical or electronic components and components Brass, zinc, tin, iron or steel or of their alloys or else of a conductively equipped plastic, wherein, preferably on a metallic background layer, in particular of copper, located on the surface of the object or article blank, a Pd / Fe Alloy is deposited, is characterized in that the objects to be coated or articles, optionally after a base coat with copper, by electrolysis in an electrolyte bath according to one of claims 1 to 4 at temperatures of 35 to 75 ° C and current densities of 0.1 to 10 A / dm 2 , in particular from 0.2 to 5 A / dm 2 , are subjected to the use of at least one insoluble anode of the electrolysis.
In the course of the process for electrolytic application of the new binary palladium-iron alloys to the respective base materials to be coated objects, objects or articles are immersed in the respective inventive electrolyte bath and switched there as a cathode.
The working temperature of the electrolyte baths according to the invention is between 35 and 75 ° C. The current density can be set to between 0.01 and 10 amps / dm 2 , depending on the type of coating system.
Thus, in drum coating processes, current densities between 0.05 and 0.50 A / dm 2 are particularly preferred. In rack coating processes, preference is given to choosing current densities between 0.2 and 10 A / dm 2 , particularly preferably 0.2 to 5 A / dm 2 .
When using the electrolyte baths according to the invention, various insoluble anodes can be used.
As insoluble anodes, those of a material selected from the group consisting of platinum-plated titanium and iridium-transition metal mixed oxide or combinations of these materials may be used, with platinized titanium anodes being preferred.
The production of the objects or articles coated according to the invention is usually carried out as follows:
On a respective base material, for example consisting of brass, zinc, iron, steel or their alloys or other materials made conductive at least on its surface is either directly or on a previously applied copper undercoat, deposited from cyanide or non-cyanidic alkaline and / or from acidic copper baths, the new binary palladium-iron alloy is deposited either directly or on Cu / Sn / Zn alloy of cyanide bronze baths applied there.
Diese Palladium-Eisen-Legierung ist an sich eine End- bzw. Finalschicht. Sie kann aber nach an sich bekannten Verfahren weiter beschichtet werden. Weitere Beschichtungen können, wie schon oben erwähnt, goldhaltige oder andere edelmetallhaltige Schichten, wie solche aus Rhodium, Platin, Ruthenium oder deren Legierungen sein.This palladium-iron alloy is in itself a final layer. However, it can be further coated by methods known per se. Other coatings may, as mentioned above, be gold-containing or other noble metal-containing layers, such as those of rhodium, platinum, ruthenium or their alloys.
Aus dem Stand der Technik ist - ergänzend zu den schon eingangs genannten Dokumenten - an sich bekannt, dass Palladium als Nickelersatz, als Diffusionssperre und als Korrosionsschutz eingesetzt wird. Bei diesen Produkten wird das Grundmaterial zuerst verkupfert, anschließend mit Palladium beschichtet und erhält zuletzt das gewünschte Finish durch Beschichtung mit Gold, Rhodium oder anderen Edelmetallen oder deren Legierungen.
Um einen ausreichenden Korrosionsschutz zu schaffen, wird eine Dicke der Palladiumschicht von etwa 0,5-5 µm empfohlen. Meist wird eine Schichtdicke von etwa 1µm als ausreichend betrachtet.From the prior art is - in addition to the documents already mentioned - known per se that palladium is used as a nickel substitute, as a diffusion barrier and as corrosion protection. In these products, the base material is first copper-plated, then coated with palladium and finally receives the desired finish by coating with gold, rhodium or other precious metals or their alloys.
In order to provide sufficient corrosion protection, a thickness of the palladium layer of about 0.5-5 microns is recommended. Usually a layer thickness of about 1 μm is considered sufficient.
Gemäß vorliegender Erfindung wurde gefunden, dass das Aufbringen einer gleich dicken Palladium-Legierungsschichte zu gleich guten Korrosionsergebnissen führt, wie sie bei rein-palladiumbeschichteten Grundmaterialien erzielt werden, die Abriebsbeständigkeit jedoch besser ist. Die Kostenersparnis beträgt allein aufgrund der geringeren Dichte ca. 15%.According to the present invention, it has been found that the application of an equally thick palladium alloy layer leads to equally good corrosion results as are achieved in pure palladium-coated base materials, but the abrasion resistance is better. The cost savings alone is about 15% due to the lower density.
Will man die Produkte besonders effizient herstellen, kann man statt einer Rhodium-Finalschicht eine Rhodium-Ruthenium-Legierung abscheiden. Scheidet man als Finalschicht beispielsweise eine Legierung im Gew.-Verhältnis Rhodium zu Ruthenium von 80:20 ab, würde man zusätzlich zu der Ersparnis bei den wie oben genannten Zwischenschichten noch 20 % des an sich sehr teuren Rhodiums einsparen.If you want to produce the products particularly efficient, you can deposit a rhodium-ruthenium alloy instead of a rhodium final layer. If, for example, an alloy in the ratio by weight of rhodium to ruthenium of 80:20 is deposited as the final layer, in addition to the savings in the intermediate layers mentioned above, 20% of the very expensive rhodium would be saved.
Die Erfindung betrifft weiters ein an sich übliches Verfahren zum kathodischen Abscheiden der erfindungsgemäßen binären Legierungen mit einem Fe-Gehalt von 5-15 Gew-% auf zumindest an ihrer Oberfläche metallischen bzw. elektrisch leitfähigen oder leitfähig beschichteten Objekten bzw. Artikeln unter Einsatz des erfindungsgemäßen Elektrolytbads.The invention further relates to a per se conventional method for cathodic deposition of the binary alloys according to the invention with an Fe content of 5-15% by weight on at least on their surface metallic or electrically conductive or conductive coated objects or articles using the electrolyte according to the invention ,
Anhand der folgenden, nicht einschränkend zu verstehenden Beispiele wird die Erfindung näher erläutert:Reference to the following, non-limiting examples, the invention is explained in more detail:
- 4 g/l Pd aus Pd-II-chlorid4 g / l Pd of Pd-II chloride
- 0,6 g/l Fe aus Fe-III-sulfat0.6 g / l Fe of Fe-III sulfate
- 80 g/l Kaliumsulfat80 g / l potassium sulfate
- 40 g/l Zitronensäure40 g / l citric acid
- 1 g/l Netzmittel PF (Betain, Produkt der Fa. Ing. W. Garhöfer GesmbH)1 g / l wetting agent PF (betaine, product of the company Ing. W. Garhöfer GesmbH)
Die Korrosionsbeständigkeit der Palladium-Eisen-Legierung im Vergleich mit einem Überzug aus einem Reinpalladium-Elektrolyten (Gapal TS, Produkt der Fa. Garhöfer GesmbH), produziert auf jeweils gleichem Grundmaterial im SO2-Test ist gleich gut.The corrosion resistance of the palladium-iron alloy in comparison with a coating of a pure palladium electrolyte (Gapal TS, product of Garhöfer GesmbH), produced on the same base material in the SO 2 test is equally good.
Es wurden jeweils eine Messingscheibe in dem Palladium-Eisen-Elektrolyt aus Bespiel 1 und eine Messingscheibe in einem Reinpalladium-Elektrolyten (Gapal TS, Produkt der Fa. Garhöfer GesmbH) mit 2µm beschichtet. Anschießend wurden beide Scheiben abgerieben. Das Reinpalladium war deutlich früher durchgerieben als die Palladium-Eisen-Legierung.In each case, a brass disc in the palladium-iron electrolyte of example 1 and a brass disc in a pure palladium electrolyte (Gapal TS, product of Garhöfer GesmbH) were coated with 2 .mu.m. Anschießend both discs were abraded. The pure palladium was rubbed much earlier than the palladium-iron alloy.
- 4 g/l Pd aus Pd-II-chlorid4 g / l Pd of Pd-II chloride
- 0,6 g/l Fe aus Fe-III-sulfat0.6 g / l Fe of Fe-III sulfate
- 80 g/l Kaliumsulfat80 g / l potassium sulfate
- 40 g/l Zitronensäure40 g / l citric acid
- 1 g/l Netzmittel PF (Betain, Produkt der Fa. Ing. W. Garhöfer GesmbH)1 g / l wetting agent PF (betaine, product of the company Ing. W. Garhöfer GesmbH)
- 0,1 g/l Fettalkoholethoxylat0.1 g / l fatty alcohol ethoxylate
- 2 g/l Saccharin2 g / l saccharin
- 2 ml/l Glanzmittel: "Brightener PF" (Gemisch substituierter aromatischer N-Heterocyclen, , Produkt der Fa. Ing. W. Garhöfer GesmbH)2 ml / l brightener: Brightener PF (mixture of substituted aromatic N-heterocycles, product of the company Ing. W. Garhöfer GesmbH)
- pH-Wert: 8,0 eingestellt mittels KOHpH value: 8.0 adjusted by means of KOH
Ein Schmuckrohling aus Zinkdruckguß wird in einem schwach alkalischen cyanidfreien Reiniger, (Entfettung 1018, Produkt der Fa. Ing. W. Garhöfer GesmbH) bei 25 °C 30s lang bei 10 A/dm2 elektrolytisch entfettet.A jewelery blank made of die-cast zinc is electrolytically degreased in a weakly alkaline cyanide-free cleaner (degreasing 1018, product of the company Ing. W. Garhöfer GesmbH) at 25 ° C. for 30 seconds at 10 A / dm 2 .
Anschließend wird der Schmuckrohling in deionisiertem Wasser gespült und in einem alkalisch cyanidischen Vorkupferbad mit 22 g/l Cu und 34 g/l KCN ("Cuproga", Produkt der Fa. Ing. W. Garhöfer GesmbH) wurden 5µm Kupfer bei 1 A/dm2 und 50 °C abgeschieden.Subsequently, the jewelry blank is rinsed in deionized water and in an alkaline cyanide Vorkupferbad with 22 g / l Cu and 34 g / l KCN ("Cuproga", product of the company Ing. W. Garhöfer GesmbH) were 5 microns of copper at 1 A / dm 2 and 50 ° C deposited.
Der vorverkupferte Schmuckrohling wird dann in 5%iger Schwefelsäurelösung 30 s lang dekapiert und in einem sauren Kupferbad mit 50 g/l Cu und 60 g/l Schwefelsäure ("IWG Cu 550", Produkt der Fa. Ing. W. Garhöfer GesmbH) werden 15µm Kupfer einebnend und hochglänzend bei 4 A/dm2 und 25 °C abgeschieden. Der so verkupferte Teil wird gespült und in einer 10% KCN-Lösung vorgetaucht.The pre-coppered jewelry blank is then dekapiert in 5% sulfuric acid solution for 30 s and in an acidic copper bath with 50 g / l Cu and 60 g / l sulfuric acid ("IWG Cu 550", product of the company Ing. W. Garhöfer GesmbH) 15μm copper leveling and high gloss deposited at 4 A / dm 2 and 25 ° C. The thus coppered part is rinsed and pre-immersed in a 10% KCN solution.
Hierauf werden aus einem Bronzeelektroytbad ("Weissbronze CT 15 LF, Produkt der Fa. Ing. W. Garhöfer GesmbH) 2µm Bronzelegierung bei 60 °C und 1 A/dm2 innerhalb von 10 min aus dem Elektrolyten abgeschieden. Danach wird in deionisierem Wasser gespült und in 5%iger Schwefelsäurelösung dekapiert. 2 μm of bronze alloy are then removed from the electrolyte within a period of 10 minutes from a bronze electrolytic bath (Weissbronze CT 15 LF, product of the company Ing. W. Garhöfer GesmbH) and then rinsed in deionized water and decanted in 5% sulfuric acid solution.
Hierauf werden aus einem Palladium-Eisen-Elektroytbad gemäß vorliegender Erfindung 2µm Palladium-Eisen der Zusammensetzung Palladium: 90,3 %, Eisen: 9,7 %, bei 50 °C, und 1 A/dm2 innerhalb von 10 min aus dem Elektrolytbad abgeschieden.Then from a palladium-iron-Elektroytbad according to the present invention 2μm palladium-iron of the composition palladium: 90.3%, iron: 9.7%, at 50 ° C, and 1 A / dm 2 within 10 minutes from the electrolyte bath deposited.
Der so erhaltene Schmuckteil wird nach erneutem Spülen und Säuretauchen mit 0,1 µm Haftgold aus einem schwach sauren Elektrolyten mit 2,5 g/l Au ("MC 218", Produkt der Fa. Ing. W. Garhöfer GesmbH) bei 1,5 A/dm2 und 35 °C versehen. Dann wird sorgfältig in demineralisiertem Wasser gespült, in 5%iger Schwefelsäurelösung dekapiert und mit 0,2µm Rhodium aus einem Elektrolyten mit 2 g/l Rh und 50 g/l Schwefelsäure ("Rhodium C2", Produkt der Fa. Ing. W. Garhöfer GesmbH) bei 3V und 35 °C rhodiniert.After renewed rinsing and acid immersion with 0.1 μm adhesive gold from a weakly acidic electrolyte with 2.5 g / l Au ("MC 218", product of the company Ing. W. Garhöfer GesmbH), the jewelery thus obtained is 1.5 A / dm 2 and 35 ° C provided. Then rinsed thoroughly in demineralized water, dekapiert in 5% sulfuric acid solution and 0.2 .mu.m rhodium from an electrolyte with 2 g / l Rh and 50 g / l sulfuric acid ("rhodium C2", product of the company Ing. W. Garhöfer GesmbH) rhodinated at 3V and 35 ° C.
Abschließend wurde der galvanisierte Teil in deionisiertem Wasser gespült und getrocknet.Finally, the galvanized part was rinsed in deionized water and dried.
Der auf diese Weise erhaltene, galvanisierte Schmuckteil bzw. dessen Oberfläche war rein weiß und hochglänzend.The obtained in this way, galvanized jewelry or its surface was pure white and high gloss.
Der galvanisierte Schmuckteil schnitt in den Korrosionstests gleich gut ab wie ein nach dem gleichen Verfahren, aber mit Reinpalladium beschichteter Schmuckteil.The galvanized part of the jewelry performed just as well in the corrosion tests as a jewelery part coated with pure palladium using the same process.
Claims (5)
- Electrolyte bath for the cathodic deposition of binary alloys with the formation of white, corrosion-resistant, crack-free and (highly) glossy coatings on objects that are at least on their surface metallic or electrically conductive or conductively coated, which bath contains as alloying metals at least one palladium compound, in particular a palladium salt, as primary metal and at least one iron compound, in particular an iron salt, as secondary metal, which for the deposition of a Pd/Fe alloy with a content in the range 5 to 15 % by weight Fe is present as an aqueous, alkaline solution with a pH value from 7.5 to 9, and in addition to said metal compounds contains as essential further components at least one wetting agent from the group of amphoteric surfactants, and at least one brightening agent as well as conductive salts, pH stabilisers and voltage reducers, wherein the electrolyte bath has a content of palladium from 0.5 to 15 g/l and of iron from 0.2 to 2 g/l and is free of ammonia and ammonium compounds, characterised in that
it contains as wetting agent from the group of amphoteric surfactants betaine and sulfobetaine in quantities from 0.5-2 g/l, and contains as brightening agent substituted aromatic N-heterocycles, as voltage reducers saccharin or organic sulfonates, and as conductive salts and/or pH stabilisers sodium or potassium sulfate, chloride, nitrate, citrate, tartrate, or malonate. - Electrolyte bath according to claim 1, characterized in that the electrolyte bath has a content of palladium from 2 to 8 g/l, and preferably from 4 to 6 g/l, and of iron from 0.5 to 1.5 g/l.
- Electrolyte bath according to Claim 1 or 2, characterized in that the alloying metals contained therein are present as palladium in divalent form, as palladium chloride, sulfate or nitrate, and iron as iron (III) sulphate, chloride, nitrate or citrate.
- Electrolyte bath according to any one of claims 1 to 3, characterized in that it contains as further wetting agents alkyl ether sulfonates, alkyl ether phosphates or fatty alcohol alkoxylates.
- A process for the production of objects or articles selected from the group of jewellery or decorative articles, from the group of electrotechnical or electronic components and components of brass, zinc, tin, iron or steel or their alloys, or of conductive plastics material, which objects or articles have a white coating or a corrosion-resistant, crack-free, highly abrasion-resistant and adherent, glossy coating of that kind, wherein a Pd/Fe alloy is deposited, preferably on a metallic base layer, in particular of copper, located on the surface of the object or article blank, characterised in that the article or object to be coated, optionally after base coating with copper, is subjected to electrolysis utilising at least one insoluble anode, by electrolysis in an electrolyte bath according to any one of claims 1 to 4 at temperatures from 35 to 75°C and current densities from 0.1 to 10 A/dm2, in particular from 0.2 to 5 A/dm2.
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AT522158B1 (en) * | 2019-05-03 | 2020-09-15 | Iwg Ing W Garhoefer Ges M B H | Coating system for application by galvanic deposition on a blank |
US10612149B1 (en) | 2019-09-05 | 2020-04-07 | Chow Sang Sang Jewellery Company Limited | Platinum electrodeposition bath and uses thereof |
AT523922B1 (en) * | 2020-09-08 | 2022-01-15 | Iwg Ing W Garhoefer Ges M B H | Electrolyte bath for palladium-ruthenium coatings |
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FR2364980A1 (en) * | 1976-09-17 | 1978-04-14 | Parker Ste Continentale | Electrodeposition of palladium alloys for jewellery - or protective coatings, using bath contg. organic cpds. and brighteners |
DE2657925A1 (en) | 1976-12-21 | 1978-06-22 | Siemens Ag | AMMONIA-FREE, AQUATIC BATH FOR GALVANIC DEPOSITION OF PALLADIUM OR. PALLADIUM ALLOYS |
DE2906783A1 (en) * | 1979-02-22 | 1980-10-16 | Degussa | Pretreatment of light metals before electroplating in aq. solns. - where substrates are first coated with palladium alloy contg. cobalt and/or iron, to ensure adhesion of plating |
DE19512888A1 (en) * | 1995-04-06 | 1996-10-10 | Vacuumschmelze Gmbh | Process for the electrolytic coating of rare earth permanent magnets with minimal surface damage |
JPH1046384A (en) | 1996-05-10 | 1998-02-17 | Lucent Technol Inc | Palladium alloy plating bath |
US6251249B1 (en) * | 1996-09-20 | 2001-06-26 | Atofina Chemicals, Inc. | Precious metal deposition composition and process |
WO2002103084A1 (en) * | 1999-10-27 | 2002-12-27 | Kojima Chemicals Co., Ltd | Palladium plating solution |
JP3601005B2 (en) | 1999-10-27 | 2004-12-15 | 小島化学薬品株式会社 | Palladium plating solution |
JP3208131B2 (en) | 1999-12-24 | 2001-09-10 | 株式会社ビクトリア | Palladium / iron alloy plating solution and palladium alloy plating substrate |
WO2007076898A1 (en) * | 2006-01-06 | 2007-07-12 | Enthone Inc | Electrolyte and process for depositing a matt metal layer |
EP2283170B1 (en) * | 2008-05-07 | 2012-04-25 | Umicore Galvanotechnik GmbH | Pd and pd-ni electrolyte baths |
DE502008001789D1 (en) * | 2008-11-21 | 2010-12-23 | Umicore Galvanotechnik Gmbh | Precious metal-containing layer sequence for decorative articles |
DE102009055828A1 (en) * | 2008-12-19 | 2010-07-01 | Merck Patent Gmbh | Preparing metal coated particles, useful e.g. in lacquers, colors, inks, pigment mixtures, comprises electrochemical metal deposition of metals on the particle substrate, whose surface is electrically conductive or semi-conductive |
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