EP1654404B1 - Elektrophoretisches verfahren zur herstellung von keramischen strukturen - Google Patents
Elektrophoretisches verfahren zur herstellung von keramischen strukturen Download PDFInfo
- Publication number
- EP1654404B1 EP1654404B1 EP04741370.3A EP04741370A EP1654404B1 EP 1654404 B1 EP1654404 B1 EP 1654404B1 EP 04741370 A EP04741370 A EP 04741370A EP 1654404 B1 EP1654404 B1 EP 1654404B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- ceramic
- deposited
- suspension
- particle size
- ceramic structures
- 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.)
- Not-in-force
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D13/00—Electrophoretic coating characterised by the process
- C25D13/02—Electrophoretic coating characterised by the process with inorganic material
Definitions
- dry pressing powder-technological injection molding, hot casting, slip casting, film casting, electrophoretic deposition from powder suspensions and further processes with subsequent sintering are used as the production process.
- feedstocks are used for shaping, which consist of ceramic powders and binders, dispersants and lubricants for improving the processability.
- additives are added to the powders only in volume fractions of a few percent.
- binders, dispersants, lubricants, polymers, waxes and suspension liquids such as water and alcohol are added.
- the powder fractions are from 30 to 70 percent by volume.
- the volume fractions of the ceramic powder may be in the range of about 5 to 50%.
- powders are used which are present as so-called monomodal powders in a relatively broad distribution, which frequently follow normal distributions, logarithmic normal distributions or so-called Rosin-Rammler distributions. Partly also powders are used, which are in the form of complex multimodal distributions.
- an electric field which causes a largely particle-size-independent particle velocity in the direction of the electric field is superposed on a field which effects a particle-size-dependent particle velocity.
- the particle size-dependent sedimentation is suitable either in a constant, location-independent gravitational field (gravity sedimentation) or in a variable and location-dependent gravitational field (centrifugation). This is in contrast to the usual electrophoresis, in which by suitable means such.
- the special arrangement of the electrodes and in particular by stirring the suspension which is undesirable for certain applications effective gravitational force, which results from the gravitational field of the earth, is turned off.
- a critical particle size r c results for each electric field strength E and for each acceleration b in the gravitational field at which the effects of both fields cancel each other out and the particle floats. All particles with r > r c move in the direction of the gravitational field, all particles with r ⁇ r c move in the direction of the electric field.
- E and the acceleration b for example by varying the rotational speed in a centrifuge
- a fraction of the suspended particles in the gravitational field is deposited on the upper electrode.
- the fraction deposited in the form of a ceramic structure is generally distinguished by the fact that its particle size distribution differs from the particle size distribution of the suspension, which is not the case in conventional electrophoresis. Since the finer particles are preferably deposited, the particle size distribution of the ceramic structure has lower values than the particle size distribution of the suspension.
- an influencing of the particle size distribution to be separated can be achieved by freely selecting not only the absolute value, but also the time at which the electric field is superimposed by the gravity sedimentation. By varying the electric field strength, the respectively desired limit of the separated size fraction can thus be set.
- a particularly preferred embodiment of the invention results from the superimposition of a variable in its absolute value electric field with a variable in its absolute gravitational field, as in particular the centrifugation, in which centrifugal forces (centrifugal forces) occur.
- the gravitational field generated thereby is directed outward with respect to the axis of rotation of the centrifuge.
- the fine fraction of the suspension in the form of a ceramic layer is deposited on the inner electrode according to the invention.
- the present invention is also applicable to suspensions (dispersions) consisting of particles of different composition. If such particle mixtures differ in their specific electrical charge, their electrophoretic mobilities and their electrophoretic deposition rates are different. If such particle mixtures differ in their density, their sedimentation rates are different in the gravitational or in the centrifugal force field, because in both cases the sedimentation velocity according to Equation 2 is proportional to the difference between the density of the particles and the density of the liquid of the suspension.
- the inventive method is not only suitable for the production of layers in which the particle size distribution or in the presence of several different powders, the composition is variable within wide limits, but also for Separation of suspensions with an extended range of variation compared to pure sedimentation or centrifugation techniques.
- an Al 2 O 3 layer was prepared.
- the counter electrode and the substrate were arranged horizontally, ie both surfaces of the electrode pair were aligned perpendicular to the direction of the gravitational field.
- the roughness depth was visually examined with the aid of a surface measuring device (FRT Microglider).
- FRT Microglider a surface measuring device
- an additional layer was also prepared, in the deposition of which the sedimentation was suppressed according to the prior art by stirring the suspension and the electrodes were arranged vertically.
- an SiO 2 layer was produced. Counter electrode and substrate were arranged horizontally. In order to show that increasingly finer particles are precipitated by sedimentation, the surface roughness was optically investigated with the help of a surface measuring device (FRT Microglider). For comparison, an additional layer was also prepared, in the deposition of which the sedimentation was suppressed according to the prior art by stirring the suspension and the electrodes were arranged vertically.
- An ethanolic SiO 2 suspension (d 50 15 ⁇ m) having a solids content of 5% by volume and a dispersant content of 2% by mass, based on the mass of the powder, was prepared. The layers were deposited from this suspension under the following conditions: Without stirring Without stirring With stirring (200 rpm) electrode assembly horizontal horizontal vertical tension 50V 10 v 50V average roughness 1.20 ⁇ m 0.12 ⁇ m 1.17 ⁇ m
- an Al 2 O 3 layer was prepared.
- the electrodes were arranged horizontally.
- the electrophoretic deposition was carried out on the upper electrode.
- the particle size distribution was determined optically in the suspension and in the layer with a laser granulometer.
- an ethanolic Al 2 O 3 suspension having a solids content of 30% by volume and a dispersant content of 2% by mass, based on the mass of the powder, was prepared.
- the electrode spacing was 13 mm. In each case four profiles were examined in one shift. Indicated is the mean. There was a significant reduction in the roughness depth with superimposed sedimentation.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Compositions Of Oxide Ceramics (AREA)
- Electrostatic Separation (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10337688A DE10337688B3 (de) | 2003-08-16 | 2003-08-16 | Verfahren zur Herstellung von keramischen Strukturen und nach diesem Verfahren hergestellte keramische Strukturen |
PCT/EP2004/008768 WO2005019505A1 (de) | 2003-08-16 | 2004-08-05 | Verfahren zur herstellung von keramischen strukturen |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1654404A1 EP1654404A1 (de) | 2006-05-10 |
EP1654404B1 true EP1654404B1 (de) | 2013-10-09 |
Family
ID=34201583
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04741370.3A Not-in-force EP1654404B1 (de) | 2003-08-16 | 2004-08-05 | Elektrophoretisches verfahren zur herstellung von keramischen strukturen |
Country Status (5)
Country | Link |
---|---|
US (1) | US20070221500A1 (ja) |
EP (1) | EP1654404B1 (ja) |
JP (1) | JP2007502912A (ja) |
DE (1) | DE10337688B3 (ja) |
WO (1) | WO2005019505A1 (ja) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030012985A1 (en) | 1998-08-03 | 2003-01-16 | Mcalister Roy E. | Pressure energy conversion systems |
DE102008036661A1 (de) | 2008-08-06 | 2010-02-11 | Forschungszentrum Karlsruhe Gmbh | Verfahren zur Herstellung von oxidischer Zahnkeramik |
US8329219B2 (en) * | 2009-12-22 | 2012-12-11 | Cook Biotech Incorporated | Methods for producing ECM-based biomaterials |
US9377105B2 (en) | 2013-03-12 | 2016-06-28 | Mcalister Technologies, Llc | Insert kits for multi-stage compressors and associated systems, processes and methods |
US8838367B1 (en) | 2013-03-12 | 2014-09-16 | Mcalister Technologies, Llc | Rotational sensor and controller |
US9255560B2 (en) | 2013-03-15 | 2016-02-09 | Mcalister Technologies, Llc | Regenerative intensifier and associated systems and methods |
WO2014144581A1 (en) | 2013-03-15 | 2014-09-18 | Mcalister Technologies, Llc | Internal combustion engine and associated systems and methods |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3023910A (en) * | 1957-01-24 | 1962-03-06 | Shirley E Schless | Support for sliding shelves |
US3791577A (en) * | 1972-08-08 | 1974-02-12 | J Lacher | Centrifuge and rotating discharge means therefor |
US3929596A (en) * | 1972-10-02 | 1975-12-30 | Toyo Kogyo Co | Electrodeposition of wear resistant and oil retentive nickel coatings and article having such a coating |
US4026780A (en) * | 1976-04-05 | 1977-05-31 | Rca Corporation | Method and apparatus for cataphoretic deposition |
US4459327A (en) * | 1979-08-24 | 1984-07-10 | Kennecott Corporation | Method for the production of copper-boron carbide composite |
CA2007501A1 (en) * | 1989-02-01 | 1990-08-01 | Jau-Ho Jean | Process for the electrophoretic deposition of barrier coatings on precious metals |
DE10013092C2 (de) * | 2000-03-17 | 2002-01-24 | Haenel & Co Altstaetten | Lagerregal |
CA2418138A1 (en) * | 2003-01-29 | 2004-07-29 | Eugenia Kumacheva | Method of colloid crystal growth on patterned surfaces |
-
2003
- 2003-08-16 DE DE10337688A patent/DE10337688B3/de not_active Expired - Fee Related
-
2004
- 2004-08-05 JP JP2006523561A patent/JP2007502912A/ja active Pending
- 2004-08-05 WO PCT/EP2004/008768 patent/WO2005019505A1/de active Application Filing
- 2004-08-05 US US10/568,288 patent/US20070221500A1/en not_active Abandoned
- 2004-08-05 EP EP04741370.3A patent/EP1654404B1/de not_active Not-in-force
Also Published As
Publication number | Publication date |
---|---|
JP2007502912A (ja) | 2007-02-15 |
WO2005019505A1 (de) | 2005-03-03 |
DE10337688B3 (de) | 2005-03-17 |
EP1654404A1 (de) | 2006-05-10 |
US20070221500A1 (en) | 2007-09-27 |
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