WO1992021795A1 - TREATING Al SHEET - Google Patents
TREATING Al SHEET Download PDFInfo
- Publication number
- WO1992021795A1 WO1992021795A1 PCT/EP1992/001264 EP9201264W WO9221795A1 WO 1992021795 A1 WO1992021795 A1 WO 1992021795A1 EP 9201264 W EP9201264 W EP 9201264W WO 9221795 A1 WO9221795 A1 WO 9221795A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- sheet
- biased
- bias
- way
- anodic
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41N—PRINTING PLATES OR FOILS; MATERIALS FOR SURFACES USED IN PRINTING MACHINES FOR PRINTING, INKING, DAMPING, OR THE LIKE; PREPARING SUCH SURFACES FOR USE AND CONSERVING THEM
- B41N3/00—Preparing for use and conserving printing surfaces
- B41N3/03—Chemical or electrical pretreatment
- B41N3/034—Chemical or electrical pretreatment characterised by the electrochemical treatment of the aluminum support, e.g. anodisation, electro-graining; Sealing of the anodised layer; Treatment of the anodic layer with inorganic compounds; Colouring of the anodic layer
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/02—Etching
- C25F3/04—Etching of light metals
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S204/00—Chemistry: electrical and wave energy
- Y10S204/09—Wave forms
Definitions
- This invention relates to a method of electrochemically roughening an Al sheet, mainly for use as a lithographic plate support or a capacitor foil.
- Standard techniques for this include: mechanical graining by the use of balls or abrasives or wire brushes; electrochemical graining,
- the aluminium sheet needs to be roughened on a scale of approximately 1 - 15 ⁇ m.
- This invention is concerned with an improvement in the electrochemical graining or roughening technique. It is known to subject the Al go sheet to AC, the current being biased in the anodic direction. It is also known to subject the Al sheet to AC with the current biased in the cathodic direction. Different advantages are claimed for the two alternatives. But neither alternative is effective to
- US Patent 4,561,944 (Fuji) describes a two- step or three-step graining treatment. Al sheet is first mechanically roughened, then optionally chemically etched, and finally electrochemically roughened by means of AC biased on the cathodic side. Because several roughening steps are involved, this treatment is relatively expensive.
- U.S. Patent 4,897,168 describes a process for the production of a roughened aluminium printing plate support by means of a pulsed direct current in an acidic electrolyte. During roughening the plate is mainly anodic. The roughened plate may thereafter be subjected to the cathodic half of the power supply which may exert a cleaning effect.
- the invention provides a method of electrochemically roughening a surface of an Al sheet, by subjecting the sheet in an aqueous electrolyte to the action of an alternating electric current, characterised in that the AC is initially biased in a first way for a time sufficient at least to initiate formation of a first pitting structure on the surface, and is then biased in a second way for a time sufficient at least to initiate formation of a second pitting structure on the surface.
- the Al sheet is subjected to the action of an alternating electric current.
- the wave shape in a graph of voltage against time
- the voltage is usually chosen to be as high as possible, while avoiding localised hot spots, so as to effect treatment in the shortest possible time.
- typical continuous commercial line may operate at 30 to QV and 50-200 A/dm 2 .
- the alternating current is initially biased in a first way, and is then biased in a second way.
- the Al sheet passes from a first region in which its potential is biased in a first way, to a second region in which its potential is biased in a second way.
- the bias may be effected by superimposing a direct current on the alternating current.
- the bias can be effected by any means which ensures that the amount of electricity passed in one half of the AC cycle is different from the amount passed in the other half. For example, one half of the cycle can be made shorter or have a lower voltage than the other.
- a natural bias is set up on the aluminium surface that results from the forward and reverse components of the current being only approximately equal.
- the bias in terms of a direct current superimposed on the alternating current.
- the direct current voltage will most usually be from about 0.25V to about 10V and no more than about 70% of the rms voltage of the alternating current; and this is particularly so when the bias is in a cathodic direction, i.e. the potential of the Al sheet is made more cathodic than would normally be the case.
- 7V AC the inventors have found it convenient to superimpose a DC bias of from +4V to -2V on the alternating current. With commercial production lines operating at 30 - 60V AC, the required DC bias is expected to be somewhat greater.
- the rate of graining is slowed down. More importantly, as the current is biased further and further in the cathodic direction, then the formation of a pitting structure on the surface slows down and eventually stops. In this state, the (mainly) cathodic AC is cleaning the surface of loose debris but is no longer removing metal to form pits.
- a convenient way of measuring bias is to plot the potential of the Al sheet, or alternatively the alternating current applied to the electrodes, against time, and compare the areas under the curves on each side of the zero (potential or current) line. With no bias, the areas are equal. With a bias, the areas are unequal. It is preferred that the bias be of limited extent, particularly in the cathodic direction, such that the ratio of the areas is no greater than about 3:1.
- the method of this invention involves biasing the AC, for a time sufficient at least to initiate formation of a pitting structure on the Al surface. For the above reason, this time may depend on the extent of the bias.
- the alternating current be initially biased in an anodic direction, and then biased in a cathodic direction.
- the AC may be initially biased in a cathodic direction and then biased in an anodic direction.
- the initial bias may be by a relatively larger direct current in the anodic direction and the second bias may be by a relatively smaller direct current also in the anodic direction.
- the statement that the AC is biased in a particular way includes the possibility of applying no bias at all in one part of the electrochemical roughening operation.
- the invention also includes the possibility of changing the bias more than once, e.g.
- the initial bias is continued for a time sufficient at least to initiate formation of a first pitting structure on the surface.
- the AC is then biased in the second way for a time sufficient at least to initiate formation of a second pitting structure on the surface of the Al sheet.
- the pitting structure is a function of the DC bias. When the initial DC bias is in an anodic direction, a period of from 1 to 15 seconds is likely to be sufficient to initiate and grow pits in a relatively coarse structure on the surface of the Al sheet.
- the aqueous electrolyte used in the method of this invention can be one used in conventional electrochemical roughening processes. Electrolytes based on nitric acid are preferred, but those based on hydrochloric acid are also possible. In a nitric acid electrolyte, an initial anodic bias forms relatively large pits, and a subsequent cathodic bias allows the subsequent fine pitting to decorate the bases of the large pits. Conventional additives to such electrolytes include boric acid with nitric acid, and acetic, tartaric, formic and other organic acids with hydrochloric acid. Electrolyte concentration is preferably in the range 1-250 g/1, preferably 5-100 g/1, and electrolyte temperature is preferably from 20-60'C. Temperature has only a small influence on graining speed.
- Al sheet is used herein to include sheets of pure aluminium and of alloys containing a major proportion of aluminium. Alloys conventionally used to make lithographic plate supports by electrochemical roughening, are suitable for use. The method of this invention should make it possible to use other Al alloys, e.g. those containing Ti, which have desirable properties (resistance to bake softening) but which are difficult to electrograin under conventional conditions by virtue of forming a protective surface film. Suitable alloys are found in the 1000, 3000, 5000 and 6000 series, e.g. 1050A of the Aluminum Association designation.
- Electrograining equipment comprises a series of baths containing electrolyte, each supplied with one electrode generally of graphite; or a single elongated bath of electrolyte containing a series of electrodes.
- a strip of Al sheet is passed continuously through the electrolyte and successively facing the electrodes.
- the strip may be contacted by a conducting roll and also passes through the electrolyte facing one or more counter-electrodes.
- barriers are provided between the electrodes to prevent short- circuiting through the electrolyte.
- the electrodes may be connected in one or more pairs, with alternating current passing from a first electrode to the Al sheet and thence to the second electrode- Where a direct current is superimposed on this AC circuit, the first electrode may be biased in a cathodic direction (so that the adjacent portion of the Al sheet is anodically biased) with the second electrode being correspondingly biased in an anodic direction.
- the AC is supplied in three separate phases R, S and T, it may be convenient to provide two pairs of electrodes in series R-S and T-R, with the first"electrode of each pair being cathodically biased.
- Other combinations e.g. RST or RSTR can be used.
- the DC bias can be changed on each electrode individually in a cascade or even in a more variable manner.
- the treated sheets are suitable as supports for lithographic plates, by virtue of having an average roughness R 3* (measured by an optical technique) in the range 0.5 ⁇ m to 2.5 ⁇ m depending on intended use.
- the lithographic plate supports may be further treated in a conventional way, e.g. by anodic oxidation, treatment with alkali metal silicates or cellulose derivatives, etc. Then a photosensitive layer is applied, and the plate is ready for use. To further speed up the electrograining process, it is possible to clean the metal surface by briefly applying, either a short burst of imposed DC, or ultrasound.
- Electrochemical graining can be effected as quickly or more quickly than by conventional techniques, and with improved control over surface micro ⁇ tructure. - It is possible to make several different kinds of litho plate support on the same line and using the same electrolyte, merely by altering the extent or the timing of the imposed DC bias.
- Al alloys that cannot be electrochemically grained by conventional means.
- high Ti alloys are desired for their improved bake softening properties but are difficult to electrograin. This difficulty should be overcome by the DC bias technique herein described.
- the method of this invention, involving biased alternating current may be used to electrochemically roughen capacitor foil in the same way as litho sheet and gives rise to the same advantages.
- aluminium sheet in the form of a continuous strip 10 is passed continuously under a pair of graphite electrodes 12, 14.
- the strip and the electrodes are immersed in a bath of electrolyte not shown.
- Applied to the electrodes is an alternating current from a power source 16.
- a direct current from a further power source comprising a negative terminal 18 and a positive terminal 20.
- a small plot of the potential of the strip at that point against time The line of the time axis represents zero potential. It can be seen that the areas under the curves above this horizontal line are larger than those below it; thus the aluminium strip is anodically biased at this point.
- a corresponding plot under the electrode 14 shows that the aluminium strip is cathodically biased at that point. The whole operation is performed in a single bath and is symmetrical.
- the aluminium strip is again shown as 10, with jinks at 22 and 24 to indicate passage from one bath of electrolyte to another.
- the aluminium strip passes through a cleaning bath 26, with no external power supply; a graining - 1 1
- a power supply 38 supplies alternating current to electrodes 30 and 32.
- a further power supply 40 superimposes a direct current on that alternating current.
- Further power supplies 42 and 44 supply respectively alternating and direct current between electrodes 32 and 36.
- the aluminium strip is anodically biased below electrode 30; cathodically biased below electrode 32; and anodically biased again below electrode 36.
- the extent of cathodic bias is greater than the extent of anodic bias.
- FIG. 3 shows a similar system.
- the aluminium strip 10 passes through a cleaning bath 26 containing an electrode 46; an electrograining bath 28 containing electrodes 48 and 50; and an anodising bath with no power source shown.
- Power sources 52 and 54 impose alternating current and direct current respectively on electrodes 46 and 48.
- Power sources 56 and 58 impose alternating current and direct current respectively on electrodes 48 and 50.
- the result is that the aluminium strip is anodically biased under the electrode 48 and cathodically biased under the electrode 50.
- the extent of anodic bias is greater than the extent of cathodic bias in the graining bath.
- the balance of cathodic bias is used up in the cleaning bath 26.
- Figures 2 and 3 show how the anodic and cathodic bias of the aluminium strip in the electrograining bath (or baths) can each be varied independently of the other.
- Example 1 illustrates the invention. Examples 1 and 2 provide background data. Example 1
- the alloy used was AA1050A (Fe, 0.38; Si,
- Samples were grained in a laboratory cell that had been shown to produce surfaces similar to those produced commercially.
- the electrolyte was 1% nitric acid.
- the voltage applied was 7V AC and the electrode spacing was
- Example 2 Experiments were performed as in Example 1 but using a 1.5 wt% hydrochloric acid electrolyte and 11.5V.
- the following table relates DC bias to time required for electrograining (taken as the time taken
- Example 1 the time required for electrograining is substantially reduced by increasing the anodic bias.
- An anodic bias gave deeper single pits resulting from cubic attack, while a cathodic bias gave normal graining. In this case, the boundary between the two graining regimes appeared to be in the region of -2 to 0V.
- Example 3 This experiment was performed uving a nitric acid electrolyte under the conditions of Example 1. But the imposed DC bias was changed once during the electrograining operation. Specifically, the sample was treated for 4 seconds with a 7V alternating current on which was superimposed a 1V DC bias, the sample being biased in the anodic direction. Then the direct current was reversed, so that the sample was biased by 1V in a cathodic direction, and electrochemical roughening continued for a f rther 11 seconds. The treated sample had a microstructure completely covered with pits, comprising a mixture of larger pits around 10 ⁇ m average diameter, and a superimposed structure of smaller pits, and was very suitable for use as a lithographic plate support. It should be noted that treatment was effected in 15 seconds, and the charge
- Example 1 shows, there is no single set of conditions by which treatment can be effected in less than about
- the surface was similar to that produced in unassisted
- the roughness of the sample grained without superimposing a bias had a centre line average roughness (R 3.) of 1.48 ⁇ m and the sample grained in this example had a R 3_. of 1.45 ⁇ m.
- Example 6 Another experiment was carried out in a similar manner to that described in Example 5 but with the anodic and cathodic biases applied for equal times-. namely 4 seconds.
- the charge density was
- the 3103 material again exhibited a similar surface to the above but had less plateau thus causing the pits to have thinner side walls and leading to a satisfactory more open structure.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Printing Plates And Materials Therefor (AREA)
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69216089T DE69216089T2 (en) | 1991-06-06 | 1992-06-05 | TREATMENT OF ALUMINUM SHEETS |
US08/157,071 US5449441A (en) | 1991-06-06 | 1992-06-05 | Electrochemically roughening aluminum sheet |
JP4510708A JPH06507678A (en) | 1991-06-06 | 1992-06-05 | Processing of A1 sheet |
EP92911798A EP0586504B1 (en) | 1991-06-06 | 1992-06-05 | TREATING Al SHEET |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB919112211A GB9112211D0 (en) | 1991-06-06 | 1991-06-06 | Treating a1 sheet |
GB9112211.9 | 1991-06-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1992021795A1 true WO1992021795A1 (en) | 1992-12-10 |
Family
ID=10696220
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1992/001264 WO1992021795A1 (en) | 1991-06-06 | 1992-06-05 | TREATING Al SHEET |
Country Status (7)
Country | Link |
---|---|
US (1) | US5449441A (en) |
EP (1) | EP0586504B1 (en) |
JP (1) | JPH06507678A (en) |
AU (1) | AU1905392A (en) |
DE (1) | DE69216089T2 (en) |
GB (1) | GB9112211D0 (en) |
WO (1) | WO1992021795A1 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030032879A1 (en) * | 1997-07-07 | 2003-02-13 | Steven Quay | Microbubble formation using ultrasound |
US6195251B1 (en) * | 1997-10-29 | 2001-02-27 | Asahi Glass Company Ltd. | Electrode assembly and electric double layer capacitor having the electrode assembly |
US7078154B2 (en) * | 2001-07-06 | 2006-07-18 | Fuji Photo Film Co., Ltd. | Presensitized plate |
US20030047464A1 (en) * | 2001-07-27 | 2003-03-13 | Applied Materials, Inc. | Electrochemically roughened aluminum semiconductor processing apparatus surfaces |
KR100559933B1 (en) * | 2002-11-29 | 2006-03-13 | 엘에스전선 주식회사 | Low Roughness Copper Foil Electropolishing Method And Electropolishing Device Thereof And Copper Foil Thereof |
EP2077949B1 (en) * | 2006-03-31 | 2015-09-30 | Aludium Transformación de Productos, S.L.U. | Manufacturing process to produce litho sheet |
US8023250B2 (en) * | 2008-09-12 | 2011-09-20 | Avx Corporation | Substrate for use in wet capacitors |
US8279585B2 (en) | 2008-12-09 | 2012-10-02 | Avx Corporation | Cathode for use in a wet capacitor |
JP2013049259A (en) * | 2011-07-29 | 2013-03-14 | Fujifilm Corp | Method and apparatus for electrolytic surface roughening treatment, and method and apparatus for manufacturing planographic printing plate precursor |
CN113699573A (en) * | 2020-05-20 | 2021-11-26 | 苹果公司 | Non-aqueous aluminum anodization |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1621187A1 (en) * | 1967-03-15 | 1971-06-03 | Elektronische Bauelemente Veb | Process for electrolytic etching of metal surfaces, especially aluminum foils |
EP0291760A2 (en) * | 1987-05-12 | 1988-11-23 | Hoechst Aktiengesellschaft | Printing plate supports and process and apparatus for their manufacture |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3217499A1 (en) * | 1982-05-10 | 1983-11-10 | Hoechst Ag, 6230 Frankfurt | METHOD FOR ELECTROCHEMICALLY Roughening ALUMINUM FOR PRINTING PLATE CARRIERS |
DE3217552A1 (en) * | 1982-05-10 | 1983-11-10 | Hoechst Ag, 6230 Frankfurt | METHOD FOR ELECTROCHEMICALLY Roughening ALUMINUM FOR PRINTING PLATE CARRIERS |
JPS59227494A (en) * | 1983-06-09 | 1984-12-20 | Fuji Photo Film Co Ltd | Manufacture of support for lithographic plate |
US4545875A (en) * | 1984-08-06 | 1985-10-08 | Polychrome Corporation | Electrolytic graining |
JPH0729507B2 (en) * | 1987-10-30 | 1995-04-05 | 富士写真フイルム株式会社 | Method for producing aluminum support for printing plate |
US5264110A (en) * | 1990-03-06 | 1993-11-23 | Dupont-Howson Ltd. Of Coal Road | Electrolytic square wave graining |
-
1991
- 1991-06-06 GB GB919112211A patent/GB9112211D0/en active Pending
-
1992
- 1992-06-05 JP JP4510708A patent/JPH06507678A/en active Pending
- 1992-06-05 AU AU19053/92A patent/AU1905392A/en not_active Abandoned
- 1992-06-05 DE DE69216089T patent/DE69216089T2/en not_active Expired - Fee Related
- 1992-06-05 EP EP92911798A patent/EP0586504B1/en not_active Expired - Lifetime
- 1992-06-05 WO PCT/EP1992/001264 patent/WO1992021795A1/en active IP Right Grant
- 1992-06-05 US US08/157,071 patent/US5449441A/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1621187A1 (en) * | 1967-03-15 | 1971-06-03 | Elektronische Bauelemente Veb | Process for electrolytic etching of metal surfaces, especially aluminum foils |
EP0291760A2 (en) * | 1987-05-12 | 1988-11-23 | Hoechst Aktiengesellschaft | Printing plate supports and process and apparatus for their manufacture |
Also Published As
Publication number | Publication date |
---|---|
JPH06507678A (en) | 1994-09-01 |
GB9112211D0 (en) | 1991-07-24 |
DE69216089T2 (en) | 1997-04-03 |
EP0586504B1 (en) | 1996-12-18 |
DE69216089D1 (en) | 1997-01-30 |
AU1905392A (en) | 1993-01-08 |
US5449441A (en) | 1995-09-12 |
EP0586504A1 (en) | 1994-03-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0659909B1 (en) | Electrochemical graining method | |
EP0181173B1 (en) | Anodic aluminium oxide film and method of forming it | |
US5449441A (en) | Electrochemically roughening aluminum sheet | |
JPH0379799A (en) | Production of aluminum base for printing plate | |
Terryn et al. | AC electrograining of aluminium | |
Amor et al. | The mechanism of electrograining aluminium sheet in nitric/boric acid electrolyte | |
JPH07138687A (en) | Aluminum alloy base material for planographic printing plate | |
JPH01118489A (en) | Method of manufacturing aluminum support for print | |
EP1409773A1 (en) | Aluminium alloy sheet with roughened surface | |
JPH01148592A (en) | Production of aluminum base for printing plate | |
JP3582048B2 (en) | Electrolytic surface roughening method and photosensitive lithographic printing plate | |
US5651871A (en) | Process for graining and anodizing a metal plate | |
WO1992022688A1 (en) | TREATING Al SHEET | |
US4735696A (en) | Method of electrolytically graining aluminum metal sheets suitable for lithographic plate supports | |
JPH02240292A (en) | Anodic oxidation of aluminum material with superior corrosion resistance | |
EP0958412B1 (en) | Treating aluminium workpieces | |
SU1713990A2 (en) | Method of micro-arc anodizing of metals and alloys | |
JPH07132689A (en) | Aluminum alloy substrate for lithographic plate | |
US5213666A (en) | Method of preparing support for printing plate | |
JP2614112B2 (en) | Electrolytic treatment of aluminum support for printing plate | |
JPH0382800A (en) | Electrolytic treatment | |
JP3162115B2 (en) | Continuous electrolytic surface roughening method for aluminum support for offset printing plate | |
JPS63176188A (en) | Method for removing smut of printing base material | |
JP2000318338A (en) | Manufacture of printing plate | |
JPS63307990A (en) | Production of base for printing plate |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AT AU BB BG BR CA CH DE DK ES FI GB HU JP KP KR LK LU MG MW NL NO PL RO RU SD SE US |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE BF BJ CF CG CH CI CM DE DK ES FR GA GB GN GR IT LU MC ML MR NL SE SN TD TG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1992911798 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 08157071 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 1992911798 Country of ref document: EP |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
NENP | Non-entry into the national phase |
Ref country code: CA |
|
WWG | Wipo information: grant in national office |
Ref document number: 1992911798 Country of ref document: EP |