US3265526A - Method of chemically plating base layers with precious metals of the platinum group - Google Patents
Method of chemically plating base layers with precious metals of the platinum group Download PDFInfo
- Publication number
- US3265526A US3265526A US207005A US20700562A US3265526A US 3265526 A US3265526 A US 3265526A US 207005 A US207005 A US 207005A US 20700562 A US20700562 A US 20700562A US 3265526 A US3265526 A US 3265526A
- Authority
- US
- United States
- Prior art keywords
- gas
- temperature
- base
- titanium
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 title claims description 40
- 239000010970 precious metal Substances 0.000 title claims description 40
- 238000000034 method Methods 0.000 title claims description 34
- 238000007747 plating Methods 0.000 title description 22
- 238000010438 heat treatment Methods 0.000 claims description 38
- 238000000576 coating method Methods 0.000 claims description 32
- 239000011248 coating agent Substances 0.000 claims description 28
- 230000008569 process Effects 0.000 claims description 25
- 150000003839 salts Chemical class 0.000 claims description 22
- 239000003638 chemical reducing agent Substances 0.000 claims description 20
- 229910045601 alloy Inorganic materials 0.000 claims description 14
- 239000000956 alloy Substances 0.000 claims description 14
- 230000001464 adherent effect Effects 0.000 claims description 13
- 239000008246 gaseous mixture Substances 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 10
- 229910052697 platinum Inorganic materials 0.000 claims description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 56
- 239000007789 gas Substances 0.000 description 51
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 39
- 239000010936 titanium Substances 0.000 description 38
- 229910052719 titanium Inorganic materials 0.000 description 38
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 37
- 229910052751 metal Inorganic materials 0.000 description 34
- 239000002184 metal Substances 0.000 description 34
- 229910021529 ammonia Inorganic materials 0.000 description 24
- 239000000203 mixture Substances 0.000 description 22
- CDOSHBSSFJOMGT-UHFFFAOYSA-N linalool Chemical compound CC(C)=CCCC(C)(O)C=C CDOSHBSSFJOMGT-UHFFFAOYSA-N 0.000 description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 19
- 239000011521 glass Substances 0.000 description 18
- 230000001603 reducing effect Effects 0.000 description 13
- 239000010410 layer Substances 0.000 description 12
- 239000002904 solvent Substances 0.000 description 11
- 239000001490 (3R)-3,7-dimethylocta-1,6-dien-3-ol Substances 0.000 description 10
- CDOSHBSSFJOMGT-JTQLQIEISA-N (R)-linalool Natural products CC(C)=CCC[C@@](C)(O)C=C CDOSHBSSFJOMGT-JTQLQIEISA-N 0.000 description 10
- 229910052799 carbon Inorganic materials 0.000 description 10
- 229930195733 hydrocarbon Natural products 0.000 description 10
- 150000002430 hydrocarbons Chemical class 0.000 description 10
- 229930007744 linalool Natural products 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- 239000010935 stainless steel Substances 0.000 description 10
- 229910001220 stainless steel Inorganic materials 0.000 description 10
- 150000003841 chloride salts Chemical class 0.000 description 9
- -1 platinum metals Chemical class 0.000 description 9
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 8
- 229910052741 iridium Inorganic materials 0.000 description 7
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 7
- 239000003960 organic solvent Substances 0.000 description 7
- 230000009467 reduction Effects 0.000 description 7
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- 239000002244 precipitate Substances 0.000 description 5
- 229910052703 rhodium Inorganic materials 0.000 description 5
- 239000010948 rhodium Substances 0.000 description 5
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- CLSUSRZJUQMOHH-UHFFFAOYSA-L platinum dichloride Chemical compound Cl[Pt]Cl CLSUSRZJUQMOHH-UHFFFAOYSA-L 0.000 description 3
- 229910052715 tantalum Inorganic materials 0.000 description 3
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 244000178870 Lavandula angustifolia Species 0.000 description 2
- 235000010663 Lavandula angustifolia Nutrition 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 239000010953 base metal Substances 0.000 description 2
- VQLYBLABXAHUDN-UHFFFAOYSA-N bis(4-fluorophenyl)-methyl-(1,2,4-triazol-1-ylmethyl)silane;methyl n-(1h-benzimidazol-2-yl)carbamate Chemical compound C1=CC=C2NC(NC(=O)OC)=NC2=C1.C=1C=C(F)C=CC=1[Si](C=1C=CC(F)=CC=1)(C)CN1C=NC=N1 VQLYBLABXAHUDN-UHFFFAOYSA-N 0.000 description 2
- HQABUPZFAYXKJW-UHFFFAOYSA-N butan-1-amine Chemical compound CCCCN HQABUPZFAYXKJW-UHFFFAOYSA-N 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 150000004820 halides Chemical class 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- 239000001102 lavandula vera Substances 0.000 description 2
- 235000018219 lavender Nutrition 0.000 description 2
- 229910001510 metal chloride Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 229910052762 osmium Inorganic materials 0.000 description 2
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 2
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 2
- SONJTKJMTWTJCT-UHFFFAOYSA-K rhodium(iii) chloride Chemical compound [Cl-].[Cl-].[Cl-].[Rh+3] SONJTKJMTWTJCT-UHFFFAOYSA-K 0.000 description 2
- 229910052707 ruthenium Inorganic materials 0.000 description 2
- DANYXEHCMQHDNX-UHFFFAOYSA-K trichloroiridium Chemical compound Cl[Ir](Cl)Cl DANYXEHCMQHDNX-UHFFFAOYSA-K 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910001260 Pt alloy Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000010617 anise oil Substances 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 150000003842 bromide salts Chemical class 0.000 description 1
- 230000001680 brushing effect Effects 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 150000004694 iodide salts Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002736 metal compounds Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229960001866 silicon dioxide Drugs 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/42—Coating with noble metals
- C23C18/44—Coating with noble metals using reducing agents
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/02—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/42—Coating with noble metals
Definitions
- the present invention relates to a method of chemically plating non-metallic or metallic base layers, such as glass, carbon, stainless steel, iron, titanium and nickel with a precious metal of the platinum group such as platinum, palladium, rhodium, iridium, osmium, ruthenium or alloys thereof.
- thermochemically coating a noble metal onto a base is by dissolving salts of precious metals in an Organic solvent, such as acetone, alcohol or glycol, adding an organic reducing agent thereto, such as anise oil or oil of lavender, spreading the resulting mixture over the article to be plated and then heating the article by means of a flame or in a furnace where-.
- Organic solvent such as acetone, alcohol or glycol
- organic reducing agent such as anise oil or oil of lavender
- the adherence of the thus applied precious metal coating can be improved by effecting the platingoperation in an inert atmosphere, e.g. an atmosphere of helium, or by carrying out a secondary heat treatment in such an atmosphere.
- thermochemical methods of plating which are known is that the reduction of the precious metal salts takes place at such a high temperature that, before said temperature is reached, the organic reducing agent which is added has either entirely or largely evaporated. It is true that the reduction can still be effected by means of the carbon originating from carbonization of the reduction agent, e.g. oil of lavender, but experience has shown that in such case, a shinning,
- the principal object of the present invention is to provide certain improved methods for plating a base with precious metal whereby the abovementioned difliculties are obviated.
- a more specific object of the invention is the provision of a method of plating with compounds of precious metals such as iridium, rhodium and platinum, wherein the reduction of said compounds can be effected at temperatures which are many hundreds of degrees lower than those conventionally used whereby the base, e.g. stainless steel, titanium, is not damaged and an improved adherence is obtained.
- the base e.g. stainless steel, titanium
- the present invention involves first cleaning the surface or surfaces of the base to be plated and in the case where the base is a metal, the surface should be degreased and cleaned of rolling mill scale and oxide film in known manner.
- the thus cleaned base is then covered, according to the invention, with a solution of a precious metal salt in an organic solvent and heated in the presence of a reducing agent in a reasonably closed furnace into which a gas having an alkaline reaction is passed.
- a gas having an alkaline reaction is passed.
- There is no necessity for flushing out the furnace with this gas as the process may be carried out in the presence of air or oxygen as long as sufficient alkaline-reacting gas is used (e.g. more than 5% by volume of this gas based on the total atmosphere).
- the reducing agent may be an organic reducing agent which is dissolved or otherwise incorporated into the organic solvent or, if desired, it may be in the form of a gas admixed with the alkaline-reacting gas. Alternatively, a combination of these two reducing means may be used, i.e. some of the reducing agent may be included with the solvent and the balance supplied with the alkaline-reacting gas. Normally a large excess of reducing agent is used, e.g. the four fold excess or more, based on the weight of the precious metal salt, to ensure the complete reduction thereof.
- the article covered with the solution of a precious metal salt is dried and preheated, usually in the range of 250 to 500 C. for 10 seconds to 10 minutes, e.g. 350 C. for 20 seconds and only thereafter the ammonia and the reducing gas are passed into the furnace.
- the solution of the precious metal salt in the solvent can 'be applied to the base layer by brushing or dipping.
- the conditions for heating the thus treated base layer in the presence of the reducing agent and alkaline-reacting gas will vary depending on other factors, e.g. the nature of the base, but usually the temperatures and times selected will correspond with those referred to above in connection with preheating, i.e. 250 to 500 C., not in excess of 600 -C., for from 10 seconds to 10 minutes.
- a thick coating of precious metal is desired and if for said purpose a number of thinner coatings of precious metal are formed, this may be effected at relatively low temperatures, for example, up to 350 C., and the ammonia and reducing gas (if any), may be supplied only during the final treatment which is carried out at the necessary reducing temperature of e.g. 350 C.
- a typical platingsolution may comprise a precious metal chloride dissolved in a mixture of isopropyl alcohol and linalool (e.g. 1 to 5 parts by weight of alcohol and 5 to 1 parts of linalool).
- a solution is used in the following examples but different solvents such as acetone and/or other ketones and alcohols may also be effectively used.
- the reducing agent linalool a anode in electrolytic processes the coated product is preferably subjected to an after-treatment as soon as possible but at any rate within 10 hours after the coating treatment is completed. This after-treatment takes place in an ordinary closed furnace in which the air can circulate to a limited extent.
- the definite heattreatment takes place between 400 and 500 C., but on the Whole, 400 C.
- the time of this treatment depends again on the requirements set for the electrode (anode) subsequently. On the Whole, the longer the heat treatment the more resistent the electrode will become. The minimum duration of this heat treatment is 4 hours, the optimum eflicacy being at 150 hours. An average treatment of hours will, in most cases, give the desired result.
- the coated article may be introduced into the heated furnace, but it is to be preferred to introduce the article into the furnace at room-temperature, and after heating 'it in the furnace during the required time, allowing it to cool to room temperature in the furnace, before removing it.
- town gas i.e. a gas mixture consisting of 36% CO 35-45% H 10-18% N 12-22% CO, 18-24% CH and 25% heavy hydrocarbons e.g. 5.2% CO 38% H 16.4% N 15.2% C0, 21.2% CH; and 4% heavy hydrocarbons
- town gas i.e. a gas mixture consisting of 36% CO 35-45% H 10-18% N 12-22% CO, 18-24% CH and 25% heavy hydrocarbons e.g. 5.2% CO 38% H 16.4% N 15.2% C0, 21.2% CH; and 4% heavy hydrocarbons
- the furnace It is preferred to so arrange the furnace that the gas introduced cannot 'be ignited by the source of heat. Additionally, it is desirable that the gases introduced, such as, for example, ammonia and town gas are preheated (e.g. from 200 to 500 C.) before they enter the furnace and contact the article to be plated.
- gases introduced such as, for example, ammonia and town gas are preheated (e.g. from 200 to 500 C.) before they enter the furnace and contact the article to be plated.
- the treatment according to the invention can be carried out not only with the precious metals and their alloys mentioned hereinbefore, but also with other precious metals such as palladium, ruthenium, osmium or alloys of said precious metals in any desired ratio.
- the invention provides a technically easily realizable method of converting precious metal compounds into the metallic form at much lower temperatures than hitherto possible to obtain bright metallic coatings which adhere very well to nonmetallic or metallic base layers.
- the coatings formed may be extremely thin or they can be given the desired thickness by a repeated application.
- Products manufactured according to the invention represent a significant advance in all those fields where it is desired to provide thin coatings of precious metals for their properties of corrosion resistance, mechanical strength, good electric contact and conductivity.
- Examples of such products are anodes having a base metal core coated with a thin layer of precious metal. These anodes may be used in electrolytic processes, e.g. brine electrolysis, particularly if the core metal is titanium. Cathodes having a core of stainless steel or nickel coated with precious metal can also be prepared according to the present process for use in electrolytic processes.
- the invention is useful for preparing glass locally coated with precious metal for use in distributing switches in the electronic and in the radio industry; glass coated with alloys of precious metals for use in the optical industry; and carbon, silicagel and like materials coated with precious metals for use as catalysts.
- Example 1 A plate of titanium which had previously been thoroughly cleaned was brushed with a liquid plating mixture composed of 5 cc. of isopropyl alcohol, 5 cc. of linalool and 1 gram of iridium chloride. Thereafter, the thus coated plate of titanium was suspended in a vertical tubular furnace heated to a temperature of about 380 C., and through which a mixture of ammonia gas and town gas was passed, the treatment lasting thirty seconds.
- a liquid plating mixture composed of 5 cc. of isopropyl alcohol, 5 cc. of linalool and 1 gram of iridium chloride.
- the plate of titanium was covered with a coating of metallic iridium having a metallic lustre which adhered to the titanium plate very well.
- the coated plate was eminently suitable as an electrical conductor.
- Two plates of titanium are degreased in any known manner, then placed in chemically pure concentrated hydrochloric acid, and connected to a source of alternating current.
- the current is passed through the liquid at a current density of 5 amps/dm. and a voltage of 1 volt for a period ranging from 1 minute to 1 hour, for example, 15 minutes.
- the plates are allowed to remain in the hydrochloric acid for about 5 minutes.
- the plates are then removed from the bath, rinsed with distilled water, and dried in the air at about 70 C.
- thermo-chemical conversion of the metal salt when coating titanium can be efiectively carried out below 500 C. It will be appreciated from the foregoing that this offers very significant advantages and meets an urgent need in the art. If only ammonia is used (i.e. the town gas is excluded), some improvement over prior techniques is realized because the precipitate on the titanium has a metal gloss whereas without ammonia and town gas, the precipitate, insofar as this is visible, is black. The adherence is poor, however, and the electric conductivity is also appreciably inferior to that obtained when both ammonia (or other alkaline-reacting gas) and town gas are passed through the furnace together. Usually, the proportion of alkalinereacting gas to town gas should fall within the range of '5 to 50% by volume of alkaline-reacting gas based on the total volume of gas, although other proportions may also 'be used.
- the plate After applying the coating of iridium the plate may be subjected to the after-treatment mentioned hereinbefore.
- Example II A glass plate was thoroughly cleaned and subsequently brushed with a mixture made of 10 cc. of isopropyl alcohol and 1 gram of rhodium chloride. The plate covered with this mixture was first dried at a temperature of C. and the dried plate was subsequently suspended in a vertical tubular furnace and heated to a temperature of 390 C. Ammonia and town gas were introduced into the furnace and after 30 seconds a properly adhering lustrous metallic layer of rhodium had deposited on the glass.
- a glass plate brushed with the same mixture was also heated in the furnace without the addition of ammonia and town gas.
- the glass plate was heated up to 810 C (the softening point of the glass) without the black precipitate which was formed changing into an electricity conducting layer having a metallic lustre.
- 810 C the softening point of the glass
- the color of the precipitate was somewhat lilghter, but there was no adherence of the rhodium to the g ass.
- a plate of stainless steel was cleaned in known manner and was subsequently brushed with a mixture composed of 2.5 cc. of isopropyl alcohol, 2.5 cc. of linalool, and 1 gram of platinum chloride.
- This plate was suspended in a vertical tubular furnace through which, as in' the preceding examples, ammonia and town gas were passed after the plate had been heated to 255 C.
- a firmly adhering coating of platinum was obtained on the stainless steel plate.
- a like plate was brushed in the same manner and heated to 310 C. with either the town gas or ammonia omitted, a metal coating was obtained, but the adherence of this coating was poor.
- Example IV Thoroughly cleaned tantalum was brushed with a mixture of 0.5 gram of iridium chloride and 1 gram of platinum chloride in cc. of isopropyl alcohol and 10 cc. of linalool.
- the metals precipirated as .an alloy containing 70% of platinum and 30% of iridium and a complete conversion and good adherence were obtained.
- good results could not be obtained even at temperatures above 800 C.
- Example V Thoroughly cleaned titanium was brushed with a mixture of a total of 1 gram of platinum chloride and rhodium chloride in a proportion of 2:1 in 10 cc. of isopropyl alcohol. When the titanium was placed in a furnace heated to 350 C. and town gas and ammonia were passed through the furnace as in the preceding examples, complete conversion to an alloy of 70% of platinum and 30% of rhodium was obtained. Strong adherence of the alloy to the titanium was obtained.
- Example VI Activated carbon was first thoroughly freed of dust and subsequently sprayed with a mixture of 20 cc. of isopropyl alcohol, 20 cc. of linalool and 1 gm. of palladium chloride. This carbon was heated to 260 C. in a furnace into which ammonia was passed and a firmly adhering metallic impregnation was obtained. When similarly sprayed carbon was heated but the ammonia was omitted, it was necessary to heat the carbon up to 430 C. to convert the palladium chloride, and this temperature impaired the mechanical strength and the activity of the carbon. In contrast, the palladium impregnated activated carbon obtained by heating the carbon to 260 C., in an atmosphere of ammonia formed an excellent catalyst mass.
- a process for coating a base with a precious metal selected from the group consisting of platinum and alloys thereof which consists essentially of the steps of applying to said base a reducible salt of at least one of said precious metals, and heating said base in a gaseous mixture consisting essentially of a gaseous reducing agent and a gas having an alkaline reaction, said heating being at a temperature sufiicient to reduce said precious metal salt and form a firmly adherent coating of platinum metal on said base, said temperature being above the temperature at which the salt decomposes and below the temperature at which the base will be damaged.
- a process for coating a base with a precious metal selected from the group consisting of platinum and alloys thereof which consists essentially of the steps of applying to said base an organic solvent solution of a reducible salt of at least one of said precious metals, drying the solution to form the dried salt, heating the base in a gaseous mixture consisting essentially of a gaseous reducing agent and a gas having an alkaline reaction, said heating being at a temperature sufiicient to reduce said precious metal salt and form a firmly adherent coating of platinum metal on said base, said temperature being above the temperature at which the salt decomposes and below the temperature at which the base will be damaged.
- a .process for plating titanium with a platinum group metal which consistsessentially of the steps of covering a surface of said titanium with a solution of a chloride of at least one platinum group metal in an organic solvent therefor, heating said titanium to remove the solvent and then continuing the heating in the presence of an organic reducing agent, in a gaseous mixture consisting essentially'of ammonia gas and a hydrocarbon containing reducing gas above a decomposition temperature for the chloride salt and below about 500 C. whereupon said chloride is reduced and a lustrous, adherent coating of the platinum group metal is deposited on said titanium.
- a process'for plating titanium with a platinum group metal which consists essentially of the stepsof covering a surface of said titanium with a solution of a chloride of at least one platinum group metal in an organic solvent therefor, heating said titanium to remove the solvent and then continuing the heating in the presence of an organic reducing agent in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature above the decomposition temperature of the chloride salt and below about 500 C. whereupon said chloride is reduced and a lustrous, adherent coating of the platinum group metal is deposited on said titanium, and within 10 hours completing the process by heating the plated titanium in air at a temperature ranging from 400 to 500 C. for a period of from 4 to 15 0 hours.
- a process for plating titanium with at least one platinum group metal which consists essentially of the step of covering a surface of said titanium with a plating mixture composed of isopropyl alcohol, linalool and a chloride salt of the platinum group metals, heating said titanium to remove the solvent and then continuing the heating in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature of about 380 C. for 30 seconds, whereupon said chloride is reduced and a lustrous, adherent coating of the platinum group metal is deposited on said titanium.
- a process for plating titanium with an alloy of platinum group metals which consists essentially of the steps of covering a surface of said titanium with a plating mixture composed of isopropyl alcohol and a mixture of chloride salts of the platinum group metals, heating said titanium to remove the solvent and then continuing the heating in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature of 350 C., whereupon said chlorides are reduced and a lustrous, adherent coating of an alloy of the platinum group metals is deposited on said titamum.
- a process for plating glass with a platinum group metal which consists essentially of the steps of covering a surface of the glass with a plating mixture composed of isopropyl alcohol and a chloride salt of the platinum group metals, heating said glass to remove the solvent and then continuing heating the glass plate in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature of 390 C. for 30 seconds, whereupon said chloride is re Jerusalem and a lustrous, adherent coating of an alloy of the platinum group metal is deposited on said glass.
- a process for plating stainless steel with a platinum group metal which consists essentially of the steps of covering a surface of the stainless steel with a plating mixture composed of isopropyl alcohol, linalool, and a chloride salt of the platinum group metals, heating said stainless steel to remove the solvent and then continuing heating the stainless steel in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature of 255 C., whereupon said chloride is reduced and a lustrous, adherent coating of the platinum group metal is deposited on said stainless steel.
- a process for impregnating activated carbon with a platinum group metal which consists essentially of the steps of spraying a surface of said carbon with a plating mixture composed of isopropyl alcohol, linalool and a chloride salt of the platinum group metals, heating said carbon to remove the solvent and then continuing heating the activated carbon in the presence of ammonia at a temperature of 260 C., whereupon said chloride is reduced and an adherent metallic impregnation of activated carbon is obtained.
- cious metal selected from the group consisting of platinum and alloys thereof, which consists essentially of the steps of applying to the base a reducible salt of at least one of said precious metals, and heating said base in a gaseous mixture consisting essentially of a gaseous reducing agent and a gas having an alkaline reaction, said heating being at a temperature suificient to reduce said precious metal salt and form a firmly adherent coating of precious metal on said base, said temperature being above the temperature at which the salt decomposes and below the temperature at which the precious metal begins to diffuse into the metal of the base.
- a process for plating glass with a platinum group metal which consists essentially of the steps of covering a surface of the glass with a plating mixture comprised of isopropyl alcohol and a chloride salt of the platinum group metals, heating said plate to remove the solvent and then continuing heating the glass in a gaseous mixture consisting essentially of ammonia gas and a hydrocarbon containing reducing gas at a temperature sufficient to reduce the chloride salt and form a firm, lustrous, adherent coating of the metal on the glass, said temperature being above the temperature at which the salt decom poses and below a temperature at which the glass will soften.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Catalysts (AREA)
- Chemically Coating (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB24442/61A GB964913A (en) | 1961-07-06 | 1961-07-06 | A method of chemically plating base layers with precious metals |
Publications (1)
Publication Number | Publication Date |
---|---|
US3265526A true US3265526A (en) | 1966-08-09 |
Family
ID=10211798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US207005A Expired - Lifetime US3265526A (en) | 1961-07-06 | 1962-07-02 | Method of chemically plating base layers with precious metals of the platinum group |
Country Status (6)
Country | Link |
---|---|
US (1) | US3265526A (de) |
CH (1) | CH405870A (de) |
DE (1) | DE1446095B2 (de) |
DK (1) | DK105679C (de) |
FI (1) | FI41333C (de) |
GB (1) | GB964913A (de) |
Cited By (41)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3470019A (en) * | 1965-02-04 | 1969-09-30 | Matthey Bishop Inc | Platinum coating composition,process and platinum-coated materials |
US3489602A (en) * | 1965-05-25 | 1970-01-13 | Hughes Aircraft Co | Method of impregnating porous tungsten and resulting article |
US3547685A (en) * | 1968-08-21 | 1970-12-15 | Atomic Energy Commission | Method of inhibiting the corrosion of tantalum by liquid lithium |
US3622367A (en) * | 1970-03-24 | 1971-11-23 | Mobil Oil Corp | Contact deposition of platinum and other metals |
US3635761A (en) * | 1970-05-05 | 1972-01-18 | Mobil Oil Corp | Electroless deposition of metals |
US3653953A (en) * | 1970-01-26 | 1972-04-04 | North American Rockwell | Nonaqueous electroless plating |
US3850668A (en) * | 1972-06-05 | 1974-11-26 | Johnson Matthey Co Ltd | Impregnation of graphite with ruthenium compounds |
US3857724A (en) * | 1971-08-20 | 1974-12-31 | Ibm | Primer for electroless plating |
US4203810A (en) * | 1970-03-25 | 1980-05-20 | Imi Marston Limited | Electrolytic process employing electrodes having coatings which comprise platinum |
US4349581A (en) * | 1980-02-13 | 1982-09-14 | Permelec Electrode Ltd. | Method for forming an anticorrosive coating on a metal substrate |
US4655900A (en) * | 1986-03-10 | 1987-04-07 | Beckman Industrial Corporation | Method for treating electrodes and improved electrochemical cell |
US4708888A (en) * | 1985-05-07 | 1987-11-24 | Eltech Systems Corporation | Coating metal mesh |
US4783246A (en) * | 1987-12-01 | 1988-11-08 | Eltech Systems Corporation | Bipolar rapid pass electrolytic hypochlorite generator |
US4798715A (en) * | 1988-02-05 | 1989-01-17 | Eltech Systems Corporation | Producing chlorine dioxide from chlorate salt |
US4936971A (en) * | 1988-03-31 | 1990-06-26 | Eltech Systems Corporation | Massive anode as a mosaic of modular anodes |
US4985071A (en) * | 1987-05-20 | 1991-01-15 | Matsushita Electric Industrial Co., Ltd. | Process for producing a base metal thin film and an electronic device using the same |
US5004626A (en) * | 1986-10-27 | 1991-04-02 | Huron Technologies, Inc. | Anodes and method of making |
US5188721A (en) * | 1989-02-10 | 1993-02-23 | Eltech Systems Corporation | Plate anode having bias cut edges |
US5314601A (en) * | 1989-06-30 | 1994-05-24 | Eltech Systems Corporation | Electrodes of improved service life |
US5324407A (en) * | 1989-06-30 | 1994-06-28 | Eltech Systems Corporation | Substrate of improved plasma sprayed surface morphology and its use as an electrode in an electrolytic cell |
US5421968A (en) * | 1985-05-07 | 1995-06-06 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US5423961A (en) * | 1985-05-07 | 1995-06-13 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US5451307A (en) * | 1985-05-07 | 1995-09-19 | Eltech Systems Corporation | Expanded metal mesh and anode structure |
US5454925A (en) * | 1994-05-03 | 1995-10-03 | Eltech Systems Corporation | Repair of mesh electrode spaced from electrode pan |
US5464519A (en) * | 1993-12-02 | 1995-11-07 | Eltech Systems Corporation | Refurbished electrode having an inner plate and outer envelope electrode |
US5545262A (en) * | 1989-06-30 | 1996-08-13 | Eltech Systems Corporation | Method of preparing a metal substrate of improved surface morphology |
US5584975A (en) * | 1995-06-15 | 1996-12-17 | Eltech Systems Corporation | Tubular electrode with removable conductive core |
US5653857A (en) * | 1995-11-29 | 1997-08-05 | Oxteh Systems, Inc. | Filter press electrolyzer electrode assembly |
US5753098A (en) * | 1996-04-22 | 1998-05-19 | Excel Technologies International Corp. | Cylindrical electrolyzer assembly and method |
US5804053A (en) * | 1995-12-07 | 1998-09-08 | Eltech Systems Corporation | Continuously electroplated foam of improved weight distribution |
US5879817A (en) * | 1994-02-15 | 1999-03-09 | Eltech Systems Corporation | Reinforced concrete structure |
US6051117A (en) * | 1996-12-12 | 2000-04-18 | Eltech Systems, Corp. | Reticulated metal article combining small pores with large apertures |
US6527939B1 (en) | 1999-06-28 | 2003-03-04 | Eltech Systems Corporation | Method of producing copper foil with an anode having multiple coating layers |
US20070068814A1 (en) * | 2002-05-09 | 2007-03-29 | Marshall Orange S | Electro-osmotic pulse (EOP) treatment system and method of use therefor |
US20070135299A1 (en) * | 2005-12-12 | 2007-06-14 | Jong Hyun Lee | Method for preparation of highly dispersed supported platinum catalyst |
US20080274372A1 (en) * | 2005-06-15 | 2008-11-06 | Danfoss A/S | Corrosion Resistant Object Having an Outer Layer of a Precious Metal |
US20100044219A1 (en) * | 2003-05-07 | 2010-02-25 | Eltech Systems Corporation | Smooth Surface Morphology Chlorate Anode Coating |
CN102943300A (zh) * | 2012-11-02 | 2013-02-27 | 苏州宝联重工股份有限公司 | 热分解法涂层的电镀极板及其方法 |
US8580091B2 (en) | 2010-10-08 | 2013-11-12 | Water Star, Inc. | Multi-layer mixed metal oxide electrode and method for making same |
CN110621806A (zh) * | 2017-05-18 | 2019-12-27 | 日本高纯度化学株式会社 | 化学镀铂液和使用该化学镀铂液得到的铂覆膜 |
US11668017B2 (en) | 2018-07-30 | 2023-06-06 | Water Star, Inc. | Current reversal tolerant multilayer material, method of making the same, use as an electrode, and use in electrochemical processes |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0243302B1 (de) * | 1986-04-17 | 1992-01-22 | Eltech Systems Corporation | Elektrode mit Platinmetallkatalysator in der Oberflächenschicht und ihre Verwendung |
GB2242203A (en) * | 1990-03-21 | 1991-09-25 | Johnson Matthey Plc | Catalyst material comprising platinum alloy supported on carbon |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1236383A (en) * | 1916-05-31 | 1917-08-07 | Frank A Fahrenwald | Process of coating tungsten or molybdenum with noble metals. |
US1583268A (en) * | 1920-06-10 | 1926-05-04 | Bart Blasius | Method of forming reflecting surfaces |
US1954353A (en) * | 1930-03-15 | 1934-04-10 | Du Pont | Material for decorating surfaces |
US2285277A (en) * | 1939-11-08 | 1942-06-02 | Du Pont | Noble metal catalyst and process of preparing same |
US2328101A (en) * | 1941-01-28 | 1943-08-31 | Baker & Co Inc | Method of providing adherent metal coatings on surfaces |
US2511472A (en) * | 1947-09-19 | 1950-06-13 | George J Kmecik | Method of applying metallic coatings on nonmetallic materials |
US2873216A (en) * | 1956-03-21 | 1959-02-10 | Philco Corp | Method of chemically plating metals |
US2915406A (en) * | 1958-03-03 | 1959-12-01 | Int Nickel Co | Palladium plating by chemical reduction |
US2979424A (en) * | 1953-09-17 | 1961-04-11 | Owens Corning Fiberglass Corp | Metal coated glass fibers and method of making them |
US3112215A (en) * | 1959-10-09 | 1963-11-26 | Lonza Ag | Preparation of catalytically active coatings |
US3117023A (en) * | 1962-01-03 | 1964-01-07 | Ionics | Method of making a non-corroding electrode |
US3133829A (en) * | 1959-02-02 | 1964-05-19 | Du Pont | Method of applying protective coatings to metals |
-
1961
- 1961-07-06 GB GB24442/61A patent/GB964913A/en not_active Expired
-
1962
- 1962-07-02 US US207005A patent/US3265526A/en not_active Expired - Lifetime
- 1962-07-04 CH CH805662A patent/CH405870A/de unknown
- 1962-07-04 DE DE19621446095 patent/DE1446095B2/de active Pending
- 1962-07-05 DK DK301362AA patent/DK105679C/da active
- 1962-07-06 FI FI621298A patent/FI41333C/fi active
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1236383A (en) * | 1916-05-31 | 1917-08-07 | Frank A Fahrenwald | Process of coating tungsten or molybdenum with noble metals. |
US1583268A (en) * | 1920-06-10 | 1926-05-04 | Bart Blasius | Method of forming reflecting surfaces |
US1954353A (en) * | 1930-03-15 | 1934-04-10 | Du Pont | Material for decorating surfaces |
US2285277A (en) * | 1939-11-08 | 1942-06-02 | Du Pont | Noble metal catalyst and process of preparing same |
US2328101A (en) * | 1941-01-28 | 1943-08-31 | Baker & Co Inc | Method of providing adherent metal coatings on surfaces |
US2511472A (en) * | 1947-09-19 | 1950-06-13 | George J Kmecik | Method of applying metallic coatings on nonmetallic materials |
US2979424A (en) * | 1953-09-17 | 1961-04-11 | Owens Corning Fiberglass Corp | Metal coated glass fibers and method of making them |
US2873216A (en) * | 1956-03-21 | 1959-02-10 | Philco Corp | Method of chemically plating metals |
US2915406A (en) * | 1958-03-03 | 1959-12-01 | Int Nickel Co | Palladium plating by chemical reduction |
US3133829A (en) * | 1959-02-02 | 1964-05-19 | Du Pont | Method of applying protective coatings to metals |
US3112215A (en) * | 1959-10-09 | 1963-11-26 | Lonza Ag | Preparation of catalytically active coatings |
US3117023A (en) * | 1962-01-03 | 1964-01-07 | Ionics | Method of making a non-corroding electrode |
Cited By (53)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3470019A (en) * | 1965-02-04 | 1969-09-30 | Matthey Bishop Inc | Platinum coating composition,process and platinum-coated materials |
US3489602A (en) * | 1965-05-25 | 1970-01-13 | Hughes Aircraft Co | Method of impregnating porous tungsten and resulting article |
US3547685A (en) * | 1968-08-21 | 1970-12-15 | Atomic Energy Commission | Method of inhibiting the corrosion of tantalum by liquid lithium |
US3653953A (en) * | 1970-01-26 | 1972-04-04 | North American Rockwell | Nonaqueous electroless plating |
US3622367A (en) * | 1970-03-24 | 1971-11-23 | Mobil Oil Corp | Contact deposition of platinum and other metals |
US4203810A (en) * | 1970-03-25 | 1980-05-20 | Imi Marston Limited | Electrolytic process employing electrodes having coatings which comprise platinum |
US3635761A (en) * | 1970-05-05 | 1972-01-18 | Mobil Oil Corp | Electroless deposition of metals |
US3857724A (en) * | 1971-08-20 | 1974-12-31 | Ibm | Primer for electroless plating |
US3850668A (en) * | 1972-06-05 | 1974-11-26 | Johnson Matthey Co Ltd | Impregnation of graphite with ruthenium compounds |
US4349581A (en) * | 1980-02-13 | 1982-09-14 | Permelec Electrode Ltd. | Method for forming an anticorrosive coating on a metal substrate |
US6254743B1 (en) | 1985-05-07 | 2001-07-03 | Eltech Systems Corporation | Expanded titanium metal mesh |
US5639358A (en) * | 1985-05-07 | 1997-06-17 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US4708888A (en) * | 1985-05-07 | 1987-11-24 | Eltech Systems Corporation | Coating metal mesh |
US5451307A (en) * | 1985-05-07 | 1995-09-19 | Eltech Systems Corporation | Expanded metal mesh and anode structure |
US5759361A (en) * | 1985-05-07 | 1998-06-02 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US5421968A (en) * | 1985-05-07 | 1995-06-06 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US5423961A (en) * | 1985-05-07 | 1995-06-13 | Eltech Systems Corporation | Cathodic protection system for a steel-reinforced concrete structure |
US4655900A (en) * | 1986-03-10 | 1987-04-07 | Beckman Industrial Corporation | Method for treating electrodes and improved electrochemical cell |
US5004626A (en) * | 1986-10-27 | 1991-04-02 | Huron Technologies, Inc. | Anodes and method of making |
US4985071A (en) * | 1987-05-20 | 1991-01-15 | Matsushita Electric Industrial Co., Ltd. | Process for producing a base metal thin film and an electronic device using the same |
US4783246A (en) * | 1987-12-01 | 1988-11-08 | Eltech Systems Corporation | Bipolar rapid pass electrolytic hypochlorite generator |
US4798715A (en) * | 1988-02-05 | 1989-01-17 | Eltech Systems Corporation | Producing chlorine dioxide from chlorate salt |
US4936971A (en) * | 1988-03-31 | 1990-06-26 | Eltech Systems Corporation | Massive anode as a mosaic of modular anodes |
US5188721A (en) * | 1989-02-10 | 1993-02-23 | Eltech Systems Corporation | Plate anode having bias cut edges |
US5578176A (en) * | 1989-06-30 | 1996-11-26 | Eltech Systems Corporation | Method of preparing electrodes of improved service life |
US6071570A (en) * | 1989-06-30 | 2000-06-06 | Eltech Systems Corporation | Electrodes of improved service life |
US5545262A (en) * | 1989-06-30 | 1996-08-13 | Eltech Systems Corporation | Method of preparing a metal substrate of improved surface morphology |
US5314601A (en) * | 1989-06-30 | 1994-05-24 | Eltech Systems Corporation | Electrodes of improved service life |
US5324407A (en) * | 1989-06-30 | 1994-06-28 | Eltech Systems Corporation | Substrate of improved plasma sprayed surface morphology and its use as an electrode in an electrolytic cell |
US5672394A (en) * | 1989-06-30 | 1997-09-30 | Eltech Systems Corporation | Electrodes of improved service life |
US5435896A (en) * | 1989-06-30 | 1995-07-25 | Eltech Systems Corporation | Cell having electrodes of improved service life |
US5619793A (en) * | 1993-12-02 | 1997-04-15 | Eltech Systems Corporation | Method of refurbishing a plate electrode |
US5783053A (en) * | 1993-12-02 | 1998-07-21 | Eltech Systems Corporation | Combination inner plate and outer envelope electrode |
US5464519A (en) * | 1993-12-02 | 1995-11-07 | Eltech Systems Corporation | Refurbished electrode having an inner plate and outer envelope electrode |
US5879817A (en) * | 1994-02-15 | 1999-03-09 | Eltech Systems Corporation | Reinforced concrete structure |
US5454925A (en) * | 1994-05-03 | 1995-10-03 | Eltech Systems Corporation | Repair of mesh electrode spaced from electrode pan |
US5584975A (en) * | 1995-06-15 | 1996-12-17 | Eltech Systems Corporation | Tubular electrode with removable conductive core |
US5653857A (en) * | 1995-11-29 | 1997-08-05 | Oxteh Systems, Inc. | Filter press electrolyzer electrode assembly |
US5804053A (en) * | 1995-12-07 | 1998-09-08 | Eltech Systems Corporation | Continuously electroplated foam of improved weight distribution |
US5753098A (en) * | 1996-04-22 | 1998-05-19 | Excel Technologies International Corp. | Cylindrical electrolyzer assembly and method |
US6051117A (en) * | 1996-12-12 | 2000-04-18 | Eltech Systems, Corp. | Reticulated metal article combining small pores with large apertures |
US6527939B1 (en) | 1999-06-28 | 2003-03-04 | Eltech Systems Corporation | Method of producing copper foil with an anode having multiple coating layers |
US20070068814A1 (en) * | 2002-05-09 | 2007-03-29 | Marshall Orange S | Electro-osmotic pulse (EOP) treatment system and method of use therefor |
US7935236B2 (en) | 2002-05-09 | 2011-05-03 | The United States Of America As Represented By The Secretary Of The Army | Electro-osmotic pulse (EOP) treatment method |
US20100044219A1 (en) * | 2003-05-07 | 2010-02-25 | Eltech Systems Corporation | Smooth Surface Morphology Chlorate Anode Coating |
US8142898B2 (en) | 2003-05-07 | 2012-03-27 | De Nora Tech, Inc. | Smooth surface morphology chlorate anode coating |
US20080274372A1 (en) * | 2005-06-15 | 2008-11-06 | Danfoss A/S | Corrosion Resistant Object Having an Outer Layer of a Precious Metal |
US20070135299A1 (en) * | 2005-12-12 | 2007-06-14 | Jong Hyun Lee | Method for preparation of highly dispersed supported platinum catalyst |
US7557057B2 (en) * | 2005-12-12 | 2009-07-07 | Hyundai Motor Company | Method for preparation of highly dispersed supported platinum catalyst |
US8580091B2 (en) | 2010-10-08 | 2013-11-12 | Water Star, Inc. | Multi-layer mixed metal oxide electrode and method for making same |
CN102943300A (zh) * | 2012-11-02 | 2013-02-27 | 苏州宝联重工股份有限公司 | 热分解法涂层的电镀极板及其方法 |
CN110621806A (zh) * | 2017-05-18 | 2019-12-27 | 日本高纯度化学株式会社 | 化学镀铂液和使用该化学镀铂液得到的铂覆膜 |
US11668017B2 (en) | 2018-07-30 | 2023-06-06 | Water Star, Inc. | Current reversal tolerant multilayer material, method of making the same, use as an electrode, and use in electrochemical processes |
Also Published As
Publication number | Publication date |
---|---|
CH405870A (de) | 1966-01-15 |
GB964913A (en) | 1964-07-29 |
DK105679C (da) | 1966-10-24 |
DE1446095A1 (de) | 1968-11-21 |
DE1446095B2 (de) | 1970-02-05 |
FI41333C (fi) | 1969-10-10 |
FI41333B (de) | 1969-06-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3265526A (en) | Method of chemically plating base layers with precious metals of the platinum group | |
US4140813A (en) | Method of making long-term electrode for electrolytic processes | |
US3864163A (en) | Method of making an electrode having a coating containing a platinum metal oxide thereon | |
AU657248B2 (en) | Electrodes of improved service life | |
US4349581A (en) | Method for forming an anticorrosive coating on a metal substrate | |
US3470019A (en) | Platinum coating composition,process and platinum-coated materials | |
US3684543A (en) | Recoating of electrodes | |
US2987453A (en) | Method of electrodepositing chromium | |
US3174917A (en) | Method of making tin plate | |
US2085543A (en) | Process for coating metals | |
JPS6013074B2 (ja) | 電解用陰極及びその製造法 | |
US3213004A (en) | Surface preparation of platinum group metals for electrodeposition | |
US1971761A (en) | Protection of metals | |
JPH02200790A (ja) | 電解用電極 | |
US2305539A (en) | Electrode | |
JPS5813629B2 (ja) | 海水電解用陰極 | |
USRE28820E (en) | Method of making an electrode having a coating containing a platinum metal oxide thereon | |
JPH02190491A (ja) | 電解用電極 | |
US2971899A (en) | Method of electroplating aluminum | |
JPS6142796B2 (de) | ||
US2859132A (en) | Gas plating using nitrous oxide | |
US3503799A (en) | Method of preparing an electrode coated with a platinum metal | |
US2888387A (en) | Electroplating | |
US3668005A (en) | Process for the coating of electrodes | |
US3445351A (en) | Process for plating metals |