EP0183034B1 - Galvanisierverfahren - Google Patents
Galvanisierverfahren Download PDFInfo
- Publication number
- EP0183034B1 EP0183034B1 EP85113105A EP85113105A EP0183034B1 EP 0183034 B1 EP0183034 B1 EP 0183034B1 EP 85113105 A EP85113105 A EP 85113105A EP 85113105 A EP85113105 A EP 85113105A EP 0183034 B1 EP0183034 B1 EP 0183034B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- electrolyte
- electrolyte solution
- guide rail
- coated
- speed
- 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
- 238000000034 method Methods 0.000 title claims abstract description 8
- 238000005246 galvanizing Methods 0.000 title description 2
- 239000003792 electrolyte Substances 0.000 claims abstract description 23
- 239000008151 electrolyte solution Substances 0.000 claims abstract description 21
- 239000000463 material Substances 0.000 claims description 34
- 239000011810 insulating material Substances 0.000 claims description 2
- 125000004122 cyclic group Chemical group 0.000 claims 1
- 230000008021 deposition Effects 0.000 abstract description 4
- 229910052751 metal Inorganic materials 0.000 abstract description 4
- 239000002184 metal Substances 0.000 abstract description 4
- 229910021645 metal ion Inorganic materials 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000009713 electroplating Methods 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 238000013508 migration Methods 0.000 description 3
- 230000005012 migration Effects 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical group [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
Images
Classifications
-
- 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
- C25D7/06—Wires; Strips; Foils
- C25D7/0614—Strips or foils
- C25D7/0685—Spraying of electrolyte
-
- 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
- C25D5/08—Electroplating with moving electrolyte e.g. jet electroplating
Definitions
- the invention relates to a method for applying metallic layers by electroplating onto strip-shaped or rope-shaped materials, the materials to be coated connected to the negative pole of a current source being passed through an electrolyte solution located in a suitable vessel, past an anode connected there to the plusol of the current source. are continuously passed through and the electrolyte solution is moved in the opposite direction to the direction of movement of the material to be coated, and a device for performing this method.
- the electrolyte is also continuously pumped around and renewed, so that there is always an electrolyte solution which has sufficient metal ions, at least in the vessel through which the band-like materials are passed.
- this does not mean that there are also sufficient metal ions in the immediate vicinity of the cathode, that is to say the material to be coated.
- sufficient ions (or anions) are available for the current transport can a corresponding amount of metal be deposited on the cathode or can a good current yield be expected.
- the object of the invention is therefore to increase the very high separation speed of such known systems even further.
- This is achieved in a manner according to the invention by moving the material at a speed above 0.1 m / s and the electrolyte in the opposite direction at a speed above 1 m / s at a Reynolds number above 80,000, so that both the flow speed of the electrolyte as well as the relative speed in the boundary layer between the movement of the material to be coated and that of the electrolyte are in the region of the turbulent flow.
- the turbulent flow thus achieved is certainly directly on the surface of the material to be coated, since this is the starting point or the starting surface for the turbulent flow.
- the decisive factor for this turbulent flow is the Reynolds number, i.e. the ratio of the inertial forces to the toughness forces, the flow speed or the relative speed between the strip-like material and the electrolyte playing the decisive role in this case. It is not decisive that fresh electrolyte solution is always available in the electrolysis bath, i.e. in the vessel containing the electrolytic solution, but that this fresh electrolytic solution with a high number of separable metal ions in the immediate vicinity of the material to be coated, i.e. also in the boundary layer , is available.
- the boundary layer is the layer between the material to be coated and the electrolyte, in which the flow rate of the electrolyte is adjusted the belt speed takes place, i.e. the layer that directly forms the surface of the belt to be coated.
- a turbulent flow also prevails in the boundary layer, which means that the metal ions are not only brought close to the cathode, but are also supported by the turbulent flow, the electron migration to the cathode.
- the boundary layer in the case of turbulent flow is orders of magnitude smaller than in the case of laminar flow, that is to say the high relative speed aimed for according to the invention and the resulting turbulence are decisive for the high separation speed.
- turbulent flow already exists from a Reynolds number that is greater than 2,320. With a Reynolds number, as determined by the invention, of RE 80,000, there is definitely a turbulent flow.
- a device which is characterized by a hollow rail made of insulating material, the free passage cross section of which corresponds approximately to the cross section of the material to be coated, by anodes inserted into the hollow rail and by a ring line connected to the hollow rail and carrying the electrolyte in which a circulation pump is inserted.
- a collection basin for electrolyte liquid can also be inserted into this ring line, to which fresh electrolyte liquid can then always be added in order to maintain the previously determined optimal values.
- the length of the hollow rail is determined according to the layer thickness to be applied, the layer thickness being proportional to the length of the hollow rail at constant speeds and current intensities. The proportionality factor depends on the material; for deposition of palladium under otherwise identical conditions, the length of the hollow rail would have to be about ten times longer than that for coating with silver.
- the anodes can cover the entire inner wall surface of the free passage cross section of such a hollow rail or even only parts thereof.
- the anodes can only be attached on one side, preferably to coat one side of a strip-shaped material, the strip side facing away from the anodes expediently being covered by a mask attached or traveling in the hollow rail.
- the anodes can also run in the form of strips in the longitudinal direction of the hollow rail in order to produce a coating strip on a strip-shaped material or, of course, also several such strips. Even if the entire surface of the band-shaped material is to be coated, it is advisable to strip the anodes within the
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
- Coating With Molten Metal (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT85113105T ATE54474T1 (de) | 1984-10-31 | 1985-10-16 | Galvanisierverfahren. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19843439750 DE3439750A1 (de) | 1984-10-31 | 1984-10-31 | Galvanisierverfahren |
DE3439750 | 1984-10-31 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0183034A2 EP0183034A2 (de) | 1986-06-04 |
EP0183034A3 EP0183034A3 (en) | 1987-10-28 |
EP0183034B1 true EP0183034B1 (de) | 1990-07-11 |
Family
ID=6249147
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP85113105A Expired - Lifetime EP0183034B1 (de) | 1984-10-31 | 1985-10-16 | Galvanisierverfahren |
Country Status (5)
Country | Link |
---|---|
US (1) | US4721554A (enrdf_load_stackoverflow) |
EP (1) | EP0183034B1 (enrdf_load_stackoverflow) |
JP (1) | JPS61113790A (enrdf_load_stackoverflow) |
AT (1) | ATE54474T1 (enrdf_load_stackoverflow) |
DE (1) | DE3439750A1 (enrdf_load_stackoverflow) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1182782B (it) * | 1985-07-18 | 1987-10-05 | Centro Speriment Metallurg | Perfezionamento nei procedimenti di zincatura elettrolitica |
US4904350A (en) * | 1988-11-14 | 1990-02-27 | International Business Machines Corporation | Submersible contact cell-electroplating films |
DE4430652C2 (de) | 1994-08-29 | 1997-01-30 | Metallglanz Gmbh | Galvanisches Verfahren und Vorrichtung zur Durchführung des Verfahrens sowie dessen Verwendung zum galvanischen oder chemischen Behandeln, insbesondere zum kontinuierlichen Aufbringen metallischer Schichten auf einen Körper |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2370973A (en) * | 1941-11-22 | 1945-03-06 | William C Lang | Method and apparatus for producing coated wire |
US3441494A (en) * | 1963-05-25 | 1969-04-29 | Kokusai Denshin Denwa Co Ltd | Apparatus to deposit a ferromagnetic film on a conductive wire |
US3522166A (en) * | 1967-04-21 | 1970-07-28 | Reynolds Metals Co | Electrical system for anodizing |
SE335038B (enrdf_load_stackoverflow) * | 1968-05-06 | 1971-05-10 | Wennberg Ab C | |
US3644181A (en) * | 1969-07-24 | 1972-02-22 | Sylvania Electric Prod | Localized electroplating method |
US3975242A (en) * | 1972-11-28 | 1976-08-17 | Nippon Steel Corporation | Horizontal rectilinear type metal-electroplating method |
US3865701A (en) * | 1973-03-06 | 1975-02-11 | American Chem & Refining Co | Method for continuous high speed electroplating of strip, wire and the like |
JPS5116236A (en) * | 1974-07-31 | 1976-02-09 | Daiichi Denshi Kogyo | Denkaishorihoho narabini sochi |
US4039398A (en) * | 1975-08-15 | 1977-08-02 | Daiichi Denshi Kogyo Kabushiki Kaisha | Method and apparatus for electrolytic treatment |
LU80496A1 (fr) * | 1978-11-09 | 1980-06-05 | Cockerill | Procede et diopositif pour le depot electrolytique en continu et a haute densite de courant d'un metal de recouvrement sur une tole |
DE2917630A1 (de) * | 1979-05-02 | 1980-11-13 | Nippon Steel Corp | Anordnung zur elektrolytischen verzinkung von walzband |
DE3017079A1 (de) * | 1980-05-03 | 1981-11-05 | Thyssen AG vorm. August Thyssen-Hütte, 4100 Duisburg | Vorrichtung zum elektroplattieren |
JPS5915996B2 (ja) * | 1980-12-03 | 1984-04-12 | 新日本製鐵株式会社 | 連続金属板処理設備における電解処理装置 |
JPS57140890A (en) * | 1981-02-24 | 1982-08-31 | Nippon Kokan Kk <Nkk> | Electric metal plating method for steel strip |
DE3228641A1 (de) * | 1982-07-31 | 1984-02-02 | Hoesch Werke Ag, 4600 Dortmund | Verfahren zur elektrolytischen abscheidung von metallen aus waessrigen loesungen der metallsalze auf stahlband und vorrichtung zur durchfuehrung des verfahrens |
US4434040A (en) * | 1982-09-28 | 1984-02-28 | United States Steel Corporation | Vertical-pass electrotreating cell |
-
1984
- 1984-10-31 DE DE19843439750 patent/DE3439750A1/de active Granted
-
1985
- 1985-10-16 AT AT85113105T patent/ATE54474T1/de not_active IP Right Cessation
- 1985-10-16 EP EP85113105A patent/EP0183034B1/de not_active Expired - Lifetime
- 1985-10-30 JP JP60241781A patent/JPS61113790A/ja active Pending
-
1986
- 1986-10-31 US US06/926,818 patent/US4721554A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
DE3439750C2 (enrdf_load_stackoverflow) | 1989-01-05 |
EP0183034A2 (de) | 1986-06-04 |
DE3439750A1 (de) | 1986-04-30 |
JPS61113790A (ja) | 1986-05-31 |
US4721554A (en) | 1988-01-26 |
EP0183034A3 (en) | 1987-10-28 |
ATE54474T1 (de) | 1990-07-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE69923477T2 (de) | Verfahren für ein feuerverzinkungs- und "galvannealing"-prozess in einem aluminium-haltigen zinkbad | |
DE3233010A1 (de) | Verfahren und vorrichtung zum elektroplattieren | |
DE3432821C2 (enrdf_load_stackoverflow) | ||
EP0101429B1 (de) | Verfahren zur elektrolytischen Beschichtung mit einer Metallschicht und gegebenenfalls elektrolytischen Behandlung eines Metallbandes | |
DE3149519A1 (de) | Verfahren und vorrichtung zur galvanisierung /verzinkung) von metallband | |
EP0183034B1 (de) | Galvanisierverfahren | |
DE1928062C3 (de) | Galvanisierzelle | |
DE2753936C2 (enrdf_load_stackoverflow) | ||
DE2156677B2 (de) | Verfahren zur kontinuierlichen elektrolytischen Vorbehandlung von Aluminiumstreifen für das Aufbringen von organischen Überzügen | |
DE3525183C2 (enrdf_load_stackoverflow) | ||
DE69203600T3 (de) | Elektrode für eine elektrolytische zelle, deren gebrauch und verfahren. | |
EP0369983B1 (de) | Verfahren und Vorrichtung zur elektrolytischen Herstellung einer Metallfolie | |
DE2534028C2 (de) | Verfahren zur anodischen Oxidation einer Aluminiumbahn und elektrolytischen Einfärbung der Oxidschicht | |
DE1919365A1 (de) | Verfahren zum Reinigen von Baendern aus Kupferlegierungen | |
EP0142010B1 (de) | Verfahren und Vorrichtung zum elektrolytischen Abscheiden von Metallen | |
CA1165271A (en) | Apparatus and method for plating one or both sides of metallic strip | |
DE3510592A1 (de) | Hochgeschwindigkeits-elektrolysezelle fuer die veredelung von bandfoermigem gut | |
DE8414836U1 (de) | Vorrichtung für die elektrolytische Behandlung metallischer Bänder | |
DE3228641A1 (de) | Verfahren zur elektrolytischen abscheidung von metallen aus waessrigen loesungen der metallsalze auf stahlband und vorrichtung zur durchfuehrung des verfahrens | |
DE3418040A1 (de) | Vorrichtung fuer die elektrolytische behandlung eines metallbandes | |
DE60104107T2 (de) | Verfahren und vorrichtung zur elektrolytischen beschichtung eines metallbandes | |
DE2627837A1 (de) | Elektro-reinigungsverfahren | |
DE2522926B2 (de) | Verfahren zum kontinuierlichen Galvanisieren von langgestrecktem Aluminiummaterial | |
DE3603770C2 (enrdf_load_stackoverflow) | ||
DE68915236T2 (de) | Vorrichtung zur kontinuierlichen elektrolytischen Behandlung von Gegenständen in Form von Draht. |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT BE CH FR GB LI NL SE |
|
PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
RHK1 | Main classification (correction) |
Ipc: C25D 7/06 |
|
AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): AT BE CH FR GB LI NL SE |
|
17P | Request for examination filed |
Effective date: 19871126 |
|
17Q | First examination report despatched |
Effective date: 19881013 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: INOVAN GMBH & CO. KG METALLE UND BAUELEMENTE |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH FR GB LI NL SE |
|
REF | Corresponds to: |
Ref document number: 54474 Country of ref document: AT Date of ref document: 19900715 Kind code of ref document: T |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 19900914 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19900919 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19900920 Year of fee payment: 6 |
|
ET | Fr: translation filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19901029 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19901030 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19901031 Year of fee payment: 6 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19901121 Year of fee payment: 6 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Effective date: 19911016 Ref country code: AT Effective date: 19911016 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19911017 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Effective date: 19911031 Ref country code: CH Effective date: 19911031 Ref country code: BE Effective date: 19911031 |
|
BERE | Be: lapsed |
Owner name: INOVAN G.M.B.H.& CO. K.G. METALLE UND BAUELEMENTE Effective date: 19911031 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Effective date: 19920501 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee | ||
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Effective date: 19920630 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
EUG | Se: european patent has lapsed |
Ref document number: 85113105.2 Effective date: 19920510 |