Process for coating solar collectors
Abstract
Coating a substrate to produce a solar collector is claimed. Coating takes place by means of a combined CVD-PVD process. Also claimed is a solar collector obtained by the proposed method. The coating containing amorphous hydrocarbon or fluorided amorphous hydrocarbon and a metal sputtered from a target (7) consists of different layers with stepped change in the composition and/or at least one layer with at least almost continuously varying concentration. At the same time, the metal concentration close to the substrate (8) is greater than that close to the coating surface.

Term
Term ended
Projected expiry passed 28 March 2016, 10.5 years ago.
- Priority
- Filed
- Published
- Projected expiry
- Today
18 claims: 18 independent, 0 dependent
- 1Method for coating a base or a substrate for producing a solar collector, characterized in that the coating is carried out by means of a combined CVD-PVD process. Verfahren zum Beschichten einer Unterlage bzw. eines Substrates für das Erzeugen eines Sonnenkollektors, dadurch gekennzeichnet, dass das Beschichten mittels eines kombinierten CVD-PVD-Prozesses erfolgt.
- 2Method, in particular according to claim 1, characterized in that the coating is carried out by means of a combined process of plasma-activated gas phase deposition and the sputtering or sputtering of a metal target (7). Verfahren, insbesondere nach Anspruch 1, dadurch gekennzeichnet, dass das Beschichten mittels eines kombinierten Prozesses aus plasmaaktivierter Gasphasendeposition und des Zerstäubens bzw. Sputterns eines Metalltargets (7) erfolgt.
- 3Method, in particular according to one of claims 1 or 2, characterized in that the substrate (8) to be coated or the substrate is kept at a negative electrical potential during the deposition or coating. Verfahren, insbesondere nach einem der Ansprüche 1 oder 2, dadurch gekennzeichnet, dass die zu beschichtende Unterlage (8) bzw. das Substrat während des Abscheidens bzw. des Beschichtens auf einem negativen, elektrischen Potential gehalten wird.
- 4Method, in particular according to one of claims 1 to 3, characterized in that the coating takes place in an evacuated deposition system (1) by combining a high-frequency plasma-activated gas phase deposition of at least one hydrocarbon gas or. fluorinated hydrocarbon gas and the sputtering of a metal target, wherein during the coating by changing the concentration of the hydrocarbon, respectively. fluorinated hydrocarbon, volume flow in an inert gas volume flow in the system, the composition of the coating is changed with increasing layer thickness. Verfahren, insbesondere nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, dass das Beschichten in einer evakuierten Depositionsanlage (1) erfolgt, durch Kombination einer hochfrequenz-plasmaaktivierten Gasphasendeposition von mindestens einem Kohlenwasserstoffgas resp. fluoriertem Kohlenwasserstoffgas und dem Zerstäuben (Sputtern) eines Metalltargets, wobei während des Beschichtens durch Aenderung der Konzentration des Kohlenwasserstoff-, resp. fluorierten Kohlenwasserstoff-, Volumenstromes in einem Inertgasvolumenstrom in der Anlage die Zusammensetzung der Beschichtung bei zunehmender Schichtdicke verändert wird.
- 5Method, in particular according to one of claims 3 or 4, characterized in that the composition in the coating is changed as the coating process progresses, by varying or changing the bias voltage or the negative electrical potential of the substrate or the substrate. Verfahren, insbesondere nach einem der Ansprüche 3 oder 4, dadurch gekennzeichnet, dass die Zusammensetzung in der Beschichtung bei fortschreitendem Beschichtungsvorgang verändert wird, indem die Bias-Spannung bzw. das negative elektrische Potential des Substrates bzw. der Unterlage variiert bzw. verändert wird.
- 6Method, in particular according to one of claims 1 to 5, characterized in that the substrate or the substrate is heated during the coating process. Verfahren, insbesondere nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, dass die Unterlage bzw. das Substrat während des Beschichtungsvorganges geheizt wird.
- 7Method, in particular according to one of claims 1 to 6, characterized in that the metal content in the coating from the substrate or underlay surface to the surface of the coating is adjusted to decrease by at the beginning of the coating process with a lower volume flow of hydrocarbon gas, respectively. fluorinated hydrocarbon gas, which is either increased in steps or continuously during the process and / or by reducing the negative electrical potential or the bias voltage on the substrate or the substrate during the continuous coating process. Verfahren, insbesondere nach einem der Ansprüche 1 bis 6, dadurch gekennzeichnet, dass der Metallgehalt in der Beschichtung von der Substrat- bzw. Unterlageoberfläche zur Oberfläche der Beschichtung abnehmend eingestellt wird, indem zu Beginn des Beschichtungsprozesses mit einem niedrigeren Volumenstrom an Kohlenwasserstoffgas, resp. fluoriertem Kohlenwasserstoffgas, gearbeitet wird, der während des Prozesses entweder stufenartig oder kontinuierlich erhöht wird und/oder indem das negative elektrische Potential bzw. die Bias-Spannung an der Unterlage bzw. dem Substrat während des fortlaufenden Beschichtungsprozesses verringert wird.
- 8Method, in particular according to one of claims 1 to 7, characterized in that a metal sheet, such as for example a copper sheet, is coated as a base in an evacuated deposition system in that a target consisting of chromium or a chromium alloy is broken down on the cathode by means of cathode sputtering or is sputtered and an inert or carrier gas, such as argon, loaded with a hydrocarbon, such as methane, is introduced into the system, high-frequency AC voltage being transmitted to the cathode via capacitive or inductive coupling, and the metal sheet being fed via a DC voltage source a negative potential is held. Verfahren, insbesondere nach einem der Ansprüche 1 bis 7, dadurch gekennzeichnet, dass ein Metallblech, wie beispielsweise ein Kupferblech als Unterlage in einer evakuierten Depositionsanlage beschichtet wird, indem an der Kathode ein aus Chrom oder einer Chromlegierung bestehendes Target mittels Kathodenzerstäubung abgebaut bzw. abgesputtert wird und ein mit einem Kohlenwasserstoff, wie beispielsweise Methan, beaufschlagtes Inert- oder Trägergas, wie beispielsweise Argon, in die Anlage eingeführt wird, wobei hochfrequente Wechselspannung über kapazitive oder induktive Koppelung auf die Kathode übertragen wird, und wobei das Metallblech über eine Gleichspannungsquelle auf einem negativen Potential gehalten wird.
- 9Method, in particular according to one of claims 3 to 8, characterized in that the compactness or hardness and density of the layer is increased by a suitable choice of the negative, electrical potential of the substrate during the coating process, as a result of which the aging resistance of the coating can be increased. Verfahren, insbesondere nach einem der Ansprüche 3 bis 8, dadurch gekennzeichnet, dass durch geeignete Wahl des negativen, elektrischen Potentials der Unterlage während des Beschichtungsprozesses die Kompaktheit bzw. Härte und Dichte der Schicht vergrössert wird, wodurch die Alterungsbeständigkeit der Beschichtung erhöht werden kann.
- 10Method, in particular according to one of claims 3 to 9, characterized in that changing the composition produces individual layers which act as diffusion barriers and / or as adhesion promoters within the coating and / or with respect to the substrate to be coated. Verfahren, insbesondere nach einem der Ansprüche 3 bis 9, dadurch gekennzeichnet, dass durch Aenderung der Zusammensetzung einzelne Schichten erzeugt werden, welche als Diffusionsbarrieren und/oder als Haftungsvermittler innerhalb der Beschichtung und/oder gegenüber der zu beschichtenden Unterlage wirken.
- 11Solar collector with optically selective coating, characterized in that the coating, containing amorphous hydrocarbon or fluorinated amorphous hydrocarbon and metal sputtered from a target (7) from different layers with gradually changing composition and / or from at least one layer with an at least almost continuous course of Concentration exists, the metal concentration in the coating close to the base (8) or the substrate is higher than close to the surface of the coating. Sonnenkollektor mit optisch selektiver Beschichtung, dadurch gekennzeichnet, dass die Beschichtung, enthaltend amorphen Kohlenwasserstoff oder fluorierten amorphen Kohlenwasserstoff und von einem Target (7) abgesputtertes Metall aus verschiedenen Lagen mit schrittweise veränderter Zusammensetzung und/oder aus mindestens einer Lage mit einem wenigstens nahezu kontinuierlichen Verlauf der Konzentration besteht, wobei die Metallkonzentration in der Beschichtung nahe an der Unterlage (8) bzw. dem Substrat höher ist als nahe an der Oberfläche der Beschichtung.
- 12Solar collector, in particular according to claim 11, characterized in that the change in the layer composition at the interface of at least two abutting layers is continuous or continuous. Sonnenkollektor, insbesondere nach Anspruch 11, dadurch gekennzeichnet, dass die Aenderung der Schichtzusammensetzung an der Grenzfläche von mindestens zwei aneinanderstossender Schichten stetig bzw. kontinuierlich ist.
- 13Solar collector, in particular according to one of claims 11 or 12, characterized in that the substrate or the base consists of a metal or a metal alloy, or at least has a metallic coating for coating or a coating with a metallic, optical effect. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 oder 12, dadurch gekennzeichnet, dass das Substrat oder die Unterlage aus einem Metall oder einer Metallegierung besteht, oder wenigstens gerichtet zur Beschichtung einen metallenen Ueberzug aufweist oder einen Ueberzug mit metallischer, optischer Wirkung.
- 14Solar collector, in particular according to one of claims 11 or 13, characterized in that the metal incorporated in the coating consists of a so-called carbide former and in the form of metal carbide particles in the hydrocarbon matrix, respectively. fluorinated hydrocarbon matrix is installed. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 oder 13, dadurch gekennzeichnet, dass das in der Beschichtung eingebundene Metall aus einem sogenannten Karbidbildner besteht und in Form von Metallkarbidpartikeln in die Kohlenwasserstoffmatrix resp. fluorierte Kohlenwasserstoffmatrix eingebaut wird.
- 15Solar collector, in particular according to one of claims 11 to 14, characterized in that the metal content decreases from the substrate surface to the collector surface from over 50 atomic percent to <than 30 atomic percent. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 bis 14, dadurch gekennzeichnet, dass der Metallgehalt von der Substratoberfläche zur Kollektoroberfläche von über 50 Atomprozent auf < als 30 Atomprozent abnimmt.
- 16Solar collector, in particular according to one of claims 11 to 15, characterized in that the metal content near the collector surface is <10 atomic percent. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 bis 15, dadurch gekennzeichnet, dass der Metallgehalt nahe der Kollektoroberfläche < 10 Atomprozent beträgt.
- 17Solar collector, in particular according to one of claims 11 to 16, characterized in that one or more layers are provided in or on the coating as diffusion barriers and / or as adhesion promoters. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 bis 16, dadurch gekennzeichnet, dass in oder an der Beschichtung eine oder mehrere Lagen als Diffusionsbarrieren und/oder als Haftungsvermittler vorgesehen sind.
- 18Solar collector, in particular according to one of claims 11 to 17, characterized in that the first layer of the coating covering the base is a diffusion barrier and / or adhesion promoter layer, which mainly consists of chromium carbide. Sonnenkollektor, insbesondere nach einem der Ansprüche 11 bis 17, dadurch gekennzeichnet, dass die die Unterlage überdeckende erste Lage der Beschichtung eine Diffusionsbarriere und/oder Haftungsvermittlerschicht ist, welche überwiegend aus Chromkarbid besteht.
Independent claims18
41 paragraphs, as filed
The present invention relates to a method for coating a base or a substrate for producing a solar collector and a solar collector with an optically selective coating.
In order to achieve a high degree of efficiency in the thermal conversion of solar energy with solar collectors, a solar selective coating of the collectors is essential. This selective surface coating is intended to ensure a high absorption of the incident sunlight and at the same time a small emission of thermal radiation. Since the wavelengths of the electromagnetic waves from the sun and from the thermal radiation are different, the desired selectivity can be achieved by a special course of the reflectivity of the surface. The reflectivity must be as small as possible in the wavelength range of sunlight between approximately 0.3 and 2 µm and as close as possible to 100% in the range of infrared radiation above approximately 2 µm. This reflection profile is usually realized by a thin coating (thickness between 0.1 and 0.2 µm) of a compact, metallic base (usually steel, copper or aluminum). The coating acts as an anti-reflective layer of the reflective base up to wavelengths of 2 µm and is essentially transparent for longer wavelengths, as a result of which the high reflection of the base is retained.
In order to meet the optical requirements for the coating, it is advantageous to design the structure of the coating in such a way that it also has metallic properties directly on the metallic base and becomes increasingly dielectric, ie more insulating, as the thickness increases. For this reason, materials that consist of a mixture of an insulator and a metal are suitable for the coating. In the so-called cermet, desired optical properties can be set via the proportions of the insulating and the metallic component. The entire coating can then be built up either from different layers with a composition that is changed step by step or from a single layer with a continuous course of the concentration.
So far, the selective coatings have mostly been applied galvanically in the commercially available collectors. However, the wet chemical methods have the disadvantage that acid residues which are harmful to the environment can occur during production and the reproducibility of the layer properties is not always guaranteed. These disadvantages can be avoided with more modern vacuum separation methods, such as cathode sputtering. In conventional sputtering, an inert gas is supplied to a vacuum chamber, which is equipped with a cathode, an anode and the substrate to be coated, and a certain working pressure (usually between 0.1 Pa and 10 Pa) is set. By applying a direct voltage (DC) or a high-frequency alternating voltage (RF) between the cathode and the anode, a plasma ignites, from which ions are extracted and accelerated to the cathode. The energetic ions hitting the cathode knock (sputter) atoms out of the cathode surface, which is provided with a target made of a specific material. The sputtered atoms finally form a coating on the substrate. If this method is expanded, reactive sputtering, a reactive gas (e.g. O<sub>2</sub>, N<sub>2</sub> or H<sub>2</sub>) fed. Chemical reactions can then take place between components of the reactive gas and the target material and compounds can be built into the layer. Magnets are often attached to the cathode so that the plasma is enclosed in the magnetic field and concentrated in front of the target. In this case one speaks of magnetron sputtering.
G. Harding et al, Method of and apparatus for reactively sputtering a graded surface coating onto a substrate, United States Patent 4,309,261 dated January 5, 1982, describes a reactive DC sputter deposit method and system for the evacuated tube collectors with a Coating insulator-metal mixture and continuous concentration curve. Using amorphous hydrocarbon as the insulator and stainless steel as the metal, these tube collectors are manufactured by the company Shiroky, Japan and are commercially sold, for example, by the company Cuenod, Satigny, GE.
Regarding the state of the art, reference is made to the following references:<ul id="ul0001" list-style="dash"><li>RA Haefer, Surface and Thin Film Technology, Part I Coatings of Surfaces, Springer-Verlag, Berlin, Heidelberg, New York, 1987.</li><li>CP Klages, R. Memming, Microstructure and physical properties of metal-containing hydrogenated carbon films, in Properties and characterization of amorphous carbon films, Materials Science Forum Vols. 52 & 53 (1989), Trans. Tech. Publications, Aedermannsdorf, pages 609-644.</li><li>B. Carlsson et al., Accelarated Life Testing of Solar Energy Materials, Case study of some selective solar absorber coating materials for DHW Systems, A Report of Task X Solar Materials Research and Development, February 1994, IEA International Energy Agency.</li></ul>
For the rest, reference is made to various brochures from solar collector companies.
Since the price of evacuated tube collectors is high and their maintenance is complicated, it is desirable to also use coatings produced by vacuum technology in the cheaper and simple flat collectors. In the case of flat-plate collectors, however, in addition to the requirements for optical selectivity, there is also a very high level of aging resistance, because these are subject to very corrosive environmental conditions. The collector coating must withstand both high temperatures (typically around 60 ° C, peak values up to 200 ° C) and moisture in air so that there is no intolerable decrease in efficiency within a period of at least 25 years. The coating material produced by the Harding method is not sufficiently stable under these conditions. But even the stability of the layer material alone is not enough. In combination with the collector plate, additional aging mechanisms occur that limit the lifespan of a collector. For example, the metal from which the collector plate is made can diffuse through the coating, reach the surface and oxidize. The risk of such diffusion is particularly great in the case of rolled sheets, which are common in industrial applications. On these there are up to a few µm deep rolling grooves, the edges of which are only incompletely covered by the coating. Diffusion therefore preferably takes place at these edges.
It is therefore an object of the present invention to create vacuum-coated collectors with sufficient durability and high optical selectivity.
The object of the invention is achieved by means of a method according to the wording of claim 1.
A method for coating a substrate for the production of a solar collector is proposed, in that a process from RF plasma-activated gas phase deposition of a hydrocarbon gas or. fluorinated hydrocarbon gas is combined with the sputtering of a metal target. It is important for the aging resistance of the layers that the substrate or the substrate is kept at a negative electrical potential (bias) during the deposition. In addition, it proves to be particularly advantageous for stability at high temperatures in air if the substrate or the coating is heated during the manufacturing process.
Further preferred embodiment variants of the method according to the invention are characterized in the dependent claims 2 to 10.
The solar collector produced according to the invention with a selective coating is characterized by the wording according to claim 11.
The coating of the solar collector produced according to the invention contains amorphous hydrocarbon, respectively. fluorinated amorphous hydrocarbon and metal sputtered from a target, the coating consisting of different layers with gradually changing composition and / or of at least one layer with an at least almost continuous course of the concentration, the metal concentration in the coating close to the base or the substrate surface is higher than close to the surface of the coating or the solar collector. It is also possible for individual layers to act as diffusion barriers and / or adhesion promoters. Such a diffusion barrier or adhesion promoter layer can be the first, metal-rich layer lying directly on the base. It is technologically advantageous that for the creation of these diffusion barriers or Adhesion promoter layers no additional coating methods are necessary. In the case of different layers with different layer compositions, it can also be advantageous if the composition at the respective layer boundary layers does not change abruptly but continuously.
Further preferred embodiment variants of the solar collector proposed according to the invention are characterized in the dependent claims 12 to 17.
The invention will now be explained in more detail with reference to the accompanying figures and exemplary embodiments.
It shows:<dl id="dl0001"><dt>Fig. 1</dt><dd>for example, a trained deposition facility, while</dd><dt>Fig. 2</dt><dd>shows the time course of deposition parameters with reference to embodiment 3.</dd></dl>
A deposition system with its essential components is shown schematically and in a highly simplified manner in FIG. 1 is the vacuum housing of the system and 2 is the pump system necessary to maintain the vacuum. 3 and 4 provide the supply lines for the inert gas, respectively. Hydrocarbon gas resp. fluorinated hydrocarbon gas, the inflow of which is controlled by suitable control and measuring devices. 5 is the power supply for the high-frequency AC voltage, which is transmitted to the cathode 6 via capacitive or inductive coupling. It is possible, but not absolutely necessary, to design the cathode as a magnetron. The metal target 7 is located on the cathode, which can consist of pure metals but also metal alloys. 8 represents the base to be coated, usually the collector plate. The substrate is heated with a heater 9 during the coating process and is kept at a negative electrical potential (bias) via a DC voltage source 10. In this arrangement, the vacuum chamber walls represent the anode.
In the case of the substrate to be coated, however, instead of a metal collector plate, for example, a suitable polymer material can also be selected, which for example has a metal coating or at least a coating with metallic properties or a coating whose optical effect corresponds to that of a metallic coating.
Examples of possible combinations of hydrocarbon gases, fluorinated hydrocarbon gas and metal targets are listed in Table 1 below: <tables id="tabl0001" num="0001"><table frame="all"><title>Table 1</title><tgroup cols="2" colsep="1" rowsep="1"><colspec colnum="1" colname="col1" colwidth="78.75mm" /><colspec colnum="2" colname="col2" colwidth="78.75mm" /><thead valign="top"><row><entry namest="col1" nameend="col2" align="center">For example, possible material combinations of hydrocarbon gas, fluorinated hydrocarbon gas and metal target.</entry></row><row><entry namest="col1" nameend="col1" align="center">Hydrocarbon gas, respectively. fluorinated hydrocarbon gas</entry><entry namest="col2" nameend="col2" align="center">Metal target</entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">methane</entry><entry namest="col2" nameend="col2" align="left">chrome</entry></row><row><entry namest="col1" nameend="col1" align="left">acetylene</entry><entry namest="col2" nameend="col2" align="left">chrome</entry></row><row><entry namest="col1" nameend="col1" align="left">methane</entry><entry namest="col2" nameend="col2" align="left">titanium</entry></row><row><entry namest="col1" nameend="col1" align="left">acetylene</entry><entry namest="col2" nameend="col2" align="left">titanium</entry></row><row><entry namest="col1" nameend="col1" align="left">Difluoromethane</entry><entry namest="col2" nameend="col2" align="left">chrome</entry></row><row><entry namest="col1" nameend="col1" align="left">Difluoromethane</entry><entry namest="col2" nameend="col2" align="left">titanium</entry></row><row><entry namest="col1" nameend="col1" align="left">Tetrafluoromethane</entry><entry namest="col2" nameend="col2" align="left">chrome</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Tetrafluoromethane</entry><entry namest="col2" nameend="col2" align="left">titanium</entry></row></tbody></tgroup></table></tables>
The material that is deposited in this coating process consists of amorphous hydrocarbon (also called aC: H or diamond-like carbon in the literature) or fluorinated hydrocarbon (aC: H: F) and metal sputtered from the target. If the metal consists of a carbide former, it is up to very high metal concentrations (typically more than 50 atomic percent) in the form of metal carbide particles in the amorphous hydrocarbon matrix or. fluorinated hydrocarbon matrix installed. About the proportions of hydrocarbon gas, respectively. fluorinated hydrocarbon gas and inert gas, the metal content of a deposited layer can be adjusted. The aging stability of the coating depends on the stability of the metal carbide and the amorphous hydrocarbon matrix respectively. fluorinated hydrocarbon matrix. It is also important that no undesired diffusion processes of substrate material in and through the coating nor of coating material take place in the substrate. Especially in a humid atmosphere, the adhesion of the coating to the substrate proves to be an essential parameter for the aging resistance.
Due to the negative electrical potential of the base, the maximum energy with which ions extracted from the plasma hit the growing layer can be set. As is also known for pure amorphous hydrocarbon films, ion bombardment leads to a densification of the layer. This allows the hardness and density of the layers to be increased and the formation of pores to be restricted. Thus, with a suitable bias voltage or suitable, negative, electrical potential significantly improve the aging resistance of the coating. By varying the negative electrical potential or the bias voltage of the substrate or the substrate, the composition of the coating can also be influenced, as an increase in the metal concentration in the coating can be achieved with an increased, negative, electrical potential. By heating the underlay, the incorporation of weakly bound hydrogen into the amorphous hydrocarbon matrix, respectively. fluorinated hydrocarbon matrix reduced.
The coating, consisting of the various layer layers, or having an essentially continuous course of the concentration, is selected such that a selective reflection profile is achieved and, in addition, individual layers or areas of the coating act as diffusion barriers and adhesion promoters.
On the basis of concrete examples, it will be shown how optically selective coatings with high aging resistance can be produced using the described method. In the following examples, the layers can be further improved with regard to their optical characteristics by an optimal choice of layer thickness and composition. The vacuum apparatus in which the sheets have been placed is at a final pressure of approximately 1 × 10 before coating<sup>-4</sup>Pa has been evacuated. We worked with methane and argon as process gas and a chrome target. The target with a diameter of 90mm was attached to a magnetron and was powered by a capacitive coupling from an RF power supply (13.56MHz and 200W). During the coating, the sheet was kept at an electrical potential of -200V. The other coating parameters are listed in the individual examples.
In order to characterize the resistance to aging, the coatings were accelerated aged by the SPF solar energy testing and research institute at the Intercantonal Technical Center in Rapperswil in artificial environments that simulate a multiple of the natural load.
Example 1:
Process for producing a two-layer layer:
A two-ply layer was made using the parameters listed in Table 2. Technical copper sheet with a typical average roughness (RMS roughness) of about 0.10 µm was used as a base. The first layer shows directly the substrate or the copper sheet, covering a metal content of 54 atomic percent chromium, while layer 2, forming the surface of the collector, has a metal content of 32 atomic percent chromium. It is therefore essential for the selective coating to design the metal content of the layer in such a way that it has a high metal concentration in the range of approx. 40-60 atom percent at the border to the metallic base or the substrate and a small metal content on the surface of the collector owns. This means that the metal on the substrate surface is almost completely carbidized and the proportion of the hydrocarbon matrix is small; On the other hand, the hydrocarbon matrix is almost exclusively present on the layer surface of the collector. The first, metal-rich layer, consisting almost entirely of chromium carbide, further serves as an adhesion promoter between the coating and the metallic base to be coated.
The two-layer layer produced in accordance with Table 2 was accelerated aged in air at 150 ° C. for 150 hours in order to characterize the stability at high temperatures in air. A solar absorption capacity of 66.5% and a thermal emissivity of 10.9% (at an assumed collector temperature of 100 ° C) were determined from the reflection curve before the aging treatment. After the thermal treatment, the solar absorptivity even improved to 71.6% and the thermal emissivity deteriorated only slightly and rose to a value of 12.0%. Since both these integral key figures and the reflection profile of the collector coating remained essentially constant during accelerated aging at 300 ° C in air, it can be concluded that the coating would have a very long service life at the operating temperatures usual in flat collectors. The great stability of the collector surface has two causes. On the one hand, each of the individual layers is very stable and hard. If a layer is deposited on a silicon single crystal surface, it cannot be scratched with a steel tip. On the other hand, the first layer, which is very rich in metal, i.e. has a high proportion of chromium carbide, acts as a barrier against the diffusion of copper. Atomic force microscopic examinations of layers produced under these conditions showed that the surfaces are very flat and have no pores. As a result, no copper can diffuse from the substrate along pores to the layer surface. In addition, since the chromium carbide crystallites have diameters of only a few nanometers, the situation is quasi amorphous. In contrast to fine crystalline layers, there is no grain boundary diffusion. The thickness of the first layer was adapted to the roughness of the copper sheet used so that the edges of the rolling grooves are adequately covered.<tables id="tabl0002" num="0002"><table frame="all"><title>Table 2</title><tgroup cols="3" colsep="1" rowsep="1"><colspec colnum="1" colname="col1" colwidth="52.50mm" /><colspec colnum="2" colname="col2" colwidth="52.50mm" /><colspec colnum="3" colname="col3" colwidth="52.50mm" /><thead valign="top"><row><entry namest="col1" nameend="col3" align="center">Coating parameters for the individual layers of the selective coating according to embodiment 1.</entry></row><row><entry namest="col1" nameend="col1" align="left">Coating parameters</entry><entry namest="col2" nameend="col2" align="right">Location 1</entry><entry namest="col3" nameend="col3" align="right">Location 2</entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">Argon volume flow [sccm]</entry><entry namest="col2" nameend="col2" align="char" char=",">40</entry><entry namest="col3" nameend="col3" align="char" char=",">40</entry></row><row><entry namest="col1" nameend="col1" align="left">Methane volume flow [sccm]</entry><entry namest="col2" nameend="col2" align="char" char=",">1,0</entry><entry namest="col3" nameend="col3" align="char" char=",">1,5</entry></row><row><entry namest="col1" nameend="col1" align="left">Pressure [Pa]</entry><entry namest="col2" nameend="col2" align="char" char=",">0,8</entry><entry namest="col3" nameend="col3" align="char" char=",">2,6</entry></row><row><entry namest="col1" nameend="col1" align="left">Substrate temperature [° C]</entry><entry namest="col2" nameend="col2" align="char" char=",">200</entry><entry namest="col3" nameend="col3" align="char" char=",">200</entry></row><row><entry namest="col1" nameend="col1" align="left">Metal content [atomic percent chromium]</entry><entry namest="col2" nameend="col2" align="char" char=",">54</entry><entry namest="col3" nameend="col3" align="char" char=",">32</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Thickness [µm]</entry><entry namest="col2" nameend="col2" align="char" char=",">0,056</entry><entry namest="col3" nameend="col3" align="char" char=",">0,055</entry></row></tbody></tgroup></table></tables>
Example 2:
Production of a three-layer layer:
The optical efficiency of the collector coating can be further improved by an additional third layer, which has an even lower metal content of <10 atomic percent metal. Table 3 lists the parameters with which aC: H / Cr three-layer layers were produced, which had a solar absorptivity α before the aging treatments<sub>S</sub> of about 89% and a thermal emissivity ε<sub>100 ° C</sub> of about 14% (see Table 4). Technical copper sheet with a typical mean roughness (RMS roughness) of 0.10 µm was used as the backing.<tables id="tabl0003" num="0003"><table frame="all"><title>Table 3</title><tgroup cols="4" colsep="1" rowsep="1"><colspec colnum="1" colname="col1" colwidth="39.37mm" /><colspec colnum="2" colname="col2" colwidth="39.37mm" /><colspec colnum="3" colname="col3" colwidth="39.37mm" /><colspec colnum="4" colname="col4" colwidth="39.37mm" /><thead valign="top"><row><entry namest="col1" nameend="col4" align="center">Parameters for the individual layers of the selective coating according to embodiment 2.</entry></row><row><entry namest="col1" nameend="col1" align="left">parameter</entry><entry namest="col2" nameend="col2" align="left">Location 1</entry><entry namest="col3" nameend="col3" align="left">Location 2</entry><entry namest="col4" nameend="col4" align="center">Location 3</entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="left">Argon volume flow [sccm]</entry><entry namest="col2" nameend="col2" align="char" char=",">40</entry><entry namest="col3" nameend="col3" align="char" char=",">40</entry><entry namest="col4" nameend="col4" align="char" char=",">40</entry></row><row><entry namest="col1" nameend="col1" align="left">Methane volume flow [sccm]</entry><entry namest="col2" nameend="col2" align="char" char=",">1,0</entry><entry namest="col3" nameend="col3" align="char" char=",">1,75</entry><entry namest="col4" nameend="col4" align="char" char=",">4,0</entry></row><row><entry namest="col1" nameend="col1" align="left">Pressure [Pa]</entry><entry namest="col2" nameend="col2" align="char" char=",">0,8</entry><entry namest="col3" nameend="col3" align="char" char=",">2,8</entry><entry namest="col4" nameend="col4" align="char" char=",">3,2</entry></row><row><entry namest="col1" nameend="col1" align="left">Substrate temperature [° C]</entry><entry namest="col2" nameend="col2" align="char" char=",">200</entry><entry namest="col3" nameend="col3" align="char" char=",">200</entry><entry namest="col4" nameend="col4" align="char" char=",">200</entry></row><row><entry namest="col1" nameend="col1" align="left">Metal content [atomic percent chrome]</entry><entry namest="col2" nameend="col2" align="char" char=",">54</entry><entry namest="col3" nameend="col3" align="char" char=",">24</entry><entry namest="col4" nameend="col4" align="char" char=",">5</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="left">Thickness [µm]</entry><entry namest="col2" nameend="col2" align="char" char=",">0,056</entry><entry namest="col3" nameend="col3" align="char" char=",">0,080</entry><entry namest="col4" nameend="col4" align="char" char=",">0,050</entry></row></tbody></tgroup></table></tables>
Accelerated aging tests were carried out on these three-layer layers in a humid atmosphere (samples 1 and 2) and under UV radiation (samples 3 and 4). As shown in Table 4, none of the treatments resulted in a significant deterioration in the optical indicators. The moisture treatments are characterized by the duration of the treatment and the air temperature / relative humidity / sample temperature. Even during 70 hours in the extremely corrosive conditions of an 85 ° C hot air atmosphere with 95% relative humidity and a sample temperature of 80 ° C, the key figures of sample 2 did not deteriorate. Since the temperature of the samples is below the air temperature, the samples are completely covered with condensation water during the aging treatment. In addition to the low porosity of the layers and thus low permeability to water, the fact that the properties of these coatings are not deteriorated by the influence of moisture is due to the adhesion imparted by the first, metal-rich layer.
The radiation tests can be used to check whether the aC: H / Cr collector coating is sensitive to UV radiation. (A UV400F lamp from Dr. Hönle was used for the UV test. With this lamp, 3.5 times the UV-A radiation and 6.5 times the UV-B radiation were compared to the samples the daylight spectrum D65). During the UV resistance test, sample 3 was cooled to 50 ° C and sample 4 was not cooled. The latter warmed up to a temperature of 75 ° C. The solar UV radiation is reduced by the glass cover that is common in flat-plate collectors, but it could not be excluded from the outset that photochemical reactions adversely affect the optical properties of the aC: H / Cr coatings. However, the investigations show that there is no significant change in the optical properties as a result of UV radiation. It can therefore be concluded that a significant degradation of the selective properties is not to be expected under either condensation or UV exposure. <tables id="tabl0004" num="0004"><table frame="all"><title>Table 4</title><tgroup cols="6" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="26.25mm" /><colspec colnum="2" colname="col2" colwidth="26.25mm" /><colspec colnum="3" colname="col3" colwidth="26.25mm" /><colspec colnum="4" colname="col4" colwidth="26.25mm" /><colspec colnum="5" colname="col5" colwidth="26.25mm" /><colspec colnum="6" colname="col6" colwidth="26.25mm" /><thead valign="top"><row rowsep="1"><entry namest="col1" nameend="col6" align="center">Solar absorption level α<sub>S</sub> and thermal emissivity ε<sub>100 ° C</sub> of three-layer layers according to embodiment 2 before and after various aging treatments</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" rowsep="0" align="center">sample</entry><entry namest="col2" nameend="col3" align="left">unaged</entry><entry namest="col4" nameend="col4" rowsep="0" align="center">treatment</entry><entry namest="col5" nameend="col6" align="center">aged</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" /><entry namest="col2" nameend="col2" align="left">α<sub>S</sub></entry><entry namest="col3" nameend="col3" align="center">ε<sub>100 ° C</sub></entry><entry namest="col4" nameend="col4" /><entry namest="col5" nameend="col5" align="center">α<sub>S</sub></entry><entry namest="col6" nameend="col6" align="center">ε<sub>100 ° C</sub></entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="right">1</entry><entry namest="col2" nameend="col2" align="char" char=",">89,3%</entry><entry namest="col3" nameend="col3" align="char" char=",">14,8%</entry><entry namest="col4" nameend="col4" align="center">200h at 60 ° C / 95% / 55 ° C</entry><entry namest="col5" nameend="col5" align="char" char=",">88,7%</entry><entry namest="col6" nameend="col6" align="char" char=",">13,3%</entry></row><row><entry namest="col1" nameend="col1" align="right">2</entry><entry namest="col2" nameend="col2" align="char" char=",">89,2%</entry><entry namest="col3" nameend="col3" align="char" char=",">14,4%</entry><entry namest="col4" nameend="col4" align="center">70h at 85 ° C / 95% / 80 ° C</entry><entry namest="col5" nameend="col5" align="char" char=",">89,4%</entry><entry namest="col6" nameend="col6" align="char" char=",">13,1%</entry></row><row><entry namest="col1" nameend="col1" align="right">3</entry><entry namest="col2" nameend="col2" align="char" char=",">88,7%</entry><entry namest="col3" nameend="col3" align="char" char=",">13,2%</entry><entry namest="col4" nameend="col4" align="center">86h UV at 50 ° C</entry><entry namest="col5" nameend="col5" align="char" char=",">89,0%</entry><entry namest="col6" nameend="col6" align="char" char=",">13,1%</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="right">4</entry><entry namest="col2" nameend="col2" align="char" char=",">88,9%</entry><entry namest="col3" nameend="col3" align="char" char=",">13,0%</entry><entry namest="col4" nameend="col4" align="center">86h UV at 75 ° C</entry><entry namest="col5" nameend="col5" align="char" char=",">88,9%</entry><entry namest="col6" nameend="col6" align="char" char=",">13,1%</entry></row></tbody></tgroup></table></tables>
Example 3:
Production of quasi-continuous three-layer layers
In order to further increase the degree of solar absorption, aC: H / Cr three-layer coatings were produced in which the metal content of the individual layers merges almost continuously. In the exemplary embodiments listed above, the target was conditioned to the new parameters for several minutes between the deposition of the individual layers without coating the substrate during this time. In contrast, with quasi-continuous three-layer coating, the substrate is also coated immediately after a parameter change. Since the target only returns to a stable state after a change in parameters, in which the deposition and re-sputtering of hydrocarbon on the target surface is balanced, the layer composition does not change suddenly, but continuously. The exact time course of the deposition parameters methane volume flow and pressure is shown in FIG. 2. The vertical dashed line at a time of 14 min indicates a conditioning phase (10 min duration). During the entire deposition, the argon volume flow is 40 sccm and the substrate temperature is 300 ° C. The structure of the resulting coating can be roughly described as a sequence of three homogeneous layers. The first layer consists of an approximately 0.028 µm thick chromium carbide-rich intermediate layer (54 atom percent chromium), which acts as a diffusion barrier and an adhesion promoter. Given the low surface roughness of the mechanically polished copper substrates used in these samples, this thickness is sufficient to suppress preferential diffusion along the rolling grooves of the sheet (RMS roughness of 0.07 µm). The second layer consists of an approximately 0.060 µm thick aC: H / Cr layer with 15 atomic percent chromium and the last layer consists of a 0.072 µm thick, pure aC: H cover layer. The degree of solar absorption of the quasi-continuous three-layer layers is about 92%, the thermal emissivity is 8.6% (see Table 5).
Using three samples (samples 5 to 7), which were produced according to the profile in FIG. 2, it was estimated whether the aC: H / Cr coatings could meet the qualification criteria of the International Energy Agency IEA (see list of references). A collector coating is considered qualified if, within 25 years, the optical key figures α in a standard collector<sub>S</sub> and ε<sub>100 ° C</sub> expected to change so little that the criterion<maths id="math0001" num=""><math display="block"><mrow><msub><mrow><mtext>-Δ α</mtext></mrow><mrow><mtext>S</mtext></mrow></msub><msub><mrow><mtext> + 0.25 Δε</mtext></mrow><mrow><mtext>100 ° C</mtext></mrow></msub><mtext> ≦ 5%</mtext></mrow></math><img file="EP0736612A2_D0001.tif" /></maths> remains fulfilled. In order to investigate the kinematics of the aging processes, the samples were annealed at various elevated temperatures until they failed, that is, until the qualification criterion was no longer met. Table 5 shows the key figures of samples 5 to 7 and the lifetimes when tempering in air.<tables id="tabl0005" num="0005"><table frame="all"><title>Table 5</title><tgroup cols="5" colsep="1" rowsep="0"><colspec colnum="1" colname="col1" colwidth="31.50mm" /><colspec colnum="2" colname="col2" colwidth="31.50mm" /><colspec colnum="3" colname="col3" colwidth="31.50mm" /><colspec colnum="4" colname="col4" colwidth="31.50mm" /><colspec colnum="5" colname="col5" colwidth="31.50mm" /><thead valign="top"><row rowsep="1"><entry namest="col1" nameend="col5" align="center">Solar absorption level α<sub>S</sub> and thermal emissivity ε<sub>100 ° C</sub> quasi-continuous three-layer layers according to embodiment 3 before the annealing treatment and their service life at elevated temperature</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="center">sample</entry><entry namest="col2" nameend="col2" align="center">α<sub>S</sub></entry><entry namest="col3" nameend="col3" align="center">ε<sub>100 ° C</sub></entry><entry namest="col4" nameend="col4" align="center">temperature</entry><entry namest="col5" nameend="col5" align="center">lifespan</entry></row></thead><tbody valign="top"><row><entry namest="col1" nameend="col1" align="right">5</entry><entry namest="col2" nameend="col2" align="char" char=",">91,8%</entry><entry namest="col3" nameend="col3" align="char" char=",">8,4%</entry><entry namest="col4" nameend="col4" align="right">250 ° C</entry><entry namest="col5" nameend="col5" align="right">80 .... 120h</entry></row><row><entry namest="col1" nameend="col1" align="right">6</entry><entry namest="col2" nameend="col2" align="char" char=",">91,8%</entry><entry namest="col3" nameend="col3" align="char" char=",">8,8%</entry><entry namest="col4" nameend="col4" align="right">300 ° C</entry><entry namest="col5" nameend="col5" align="right"><20h</entry></row><row rowsep="1"><entry namest="col1" nameend="col1" align="right">7</entry><entry namest="col2" nameend="col2" align="char" char=",">91,8%</entry><entry namest="col3" nameend="col3" align="char" char=",">8,6%</entry><entry namest="col4" nameend="col4" align="right">220 ° C</entry><entry namest="col5" nameend="col5" align="right">> 280h</entry></row></tbody></tgroup></table></tables>
The lifespan of the quasi-continuous three-layer layers is between 80 and 120h at 250 ° C, less than 20h at 300 ° C and more than 280h at 220 ° C. Based on time transformation functions, it can be concluded that the service life under the thermal loads in a standard collector should be at least 25 years. The coating thus fulfills the qualification criteria of the IEA.
The deposition system shown for example in FIG. 1 and the exemplary embodiments 1, 2 and 3 are examples in order to explain the invention in more detail and to make it understandable. Of course, the invention is not limited to the system shown and the exemplary embodiments. So instead of methane other hydrocarbon gases resp. fluorinated hydrocarbon gases are used, and other metals can be used in place of chromium to be included in the coating. Finally, a copper sheet does not necessarily have to be used as a substrate or base, but other metals or metal alloys can also be used, or non-metallic substrates which have a metal coating or a coating with an optical effect corresponding to that of a metallic surface.
It is essential to the invention that plasma-activated gas phase deposition is combined with an atomization process and negative substrate potential when coating a substrate or a base for producing a solar collector.
4 sheets
Sheet 1 Sheet 2 Sheet 3 Sheet 4
Every citation, both ways
| Document | Relation | Office | Cited during |
|---|---|---|---|
| WO03048406A3 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| DE10159907B4 | Cited by | Germany | Search report |
| EP1887293A2 | Cited by | European Patent Office (EPO) | Search report |
| WO9846947A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO03048406A2 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO2009140051A3 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO9914390A3 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| EP1887293A3 | Cited by | European Patent Office (EPO) | Search report |
| AU2002352216B2 | Cited by | Australia | Search report |
| WO2009140051A2 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| DE10159907A1 | Cited by | Germany | Search report |
| WO0244629A1 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO9914390A2 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| WO9914390A3 | Cited by | World Intellectual Property Organization (WIPO) | International search |
| US6171454B1 | Cited by | United States of America | Applicant |
| US4309261A | Cites | United States of America | Search report |
7 members in 3 offices
Priority claims5
| Document | Office | Kind | Date |
|---|---|---|---|
| 100895 | Switzerland | – | |
| 100895 | Switzerland | A | |
| 100895 | Switzerland | A | |
| 100895 | – | – | – |
| CH19950001008 | – | – | – |
Members7
| Document | Office | Kind | |
|---|---|---|---|
| EP0736612A2This record | European Patent Office (EPO) | A2 | |
| EP0736612A3 | European Patent Office (EPO) | A3 | |
| EP0736612B1 | European Patent Office (EPO) | B1 | |
| AT270720T | Austria | T | |
| ATE270720T1 | Austria | T1 | |
| DE59611031D1 | Germany | D1 | |
| EP0736612B2 | European Patent Office (EPO) | B2 |
50 legal events, as 4 offices reported them to INPADOC
Over the term
Point at a mark for the eventEvents
| Event | Code | Office | |
|---|---|---|---|
| ExpiryMK07 | MK07 | AT | |
| Patent ceasedCeasedPL | PL | CH | |
| Expiry of rightR071 | R071 | DE | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Annual fee paid to national office [announced via postgrant information from national office to epo]GrantedPGFP | PGFP | EP | |
| Modification of the scope of the patentAUFRECHTERHALTUNG DES PATENTES IN GEAENDERTER FORMAEN | AEN | CH | |
| Patent maintained in amended form27A | 27A | EP | |
| Designated contracting statesAK | AK | EP | |
| Patent maintained in amended formORIGINAL CODE: 0009272PUAH | PUAH | EP | |
| Information on the status of an ep patent application or granted ep patentGrantedSTATUS: PATENT MAINTAINED AS AMENDEDSTAA | STAA | EP | |
| Opposition filed (corrected)OppositionR26 | R26 | EP | |
| Opposition data, opponent's data or that of the opponent's representative modifiedOppositionORIGINAL CODE: 0009299OPPOPLAB | PLAB | EP | |
| Name/firm changedPFA | PFA | CH | |
| Reply of patent proprietor to notice(s) of opposition receivedOppositionORIGINAL CODE: EPIDOSNOBS3PLBB | PLBB | EP | |
| Information modified related to communication of a notice of opposition and request to file observations + time limitOppositionORIGINAL CODE: EPIDOSCOBS2PLAF | PLAF | EP | |
| Opposition filed (corrected)OppositionR26 | R26 | EP | |
| Opposition filedOpposition26 | 26 | EP | |
| Opposition data, opponent's data or that of the opponent's representative modifiedOppositionORIGINAL CODE: 0009299OPPOPLAB | PLAB | EP | |
| Examination of admissibility of opposition: information related to despatch of communication + time limit deletedOppositionORIGINAL CODE: EPIDOSDOPE2PLAQ | PLAQ | EP | |
| Examination of admissibility of opposition: information related to receipt of reply deletedOppositionORIGINAL CODE: EPIDOSDOPE4PLAR | PLAR | EP | |
| Notice of opposition and request to file observation + time limit sentOppositionORIGINAL CODE: EPIDOSNOBS2PLAX | PLAX | EP | |
| Unpublished change to opponent dataORIGINAL CODE: EPIDOS OPPOPLBQ | PLBQ | EP | |
| Opposition filedOppositionORIGINAL CODE: 0009260PLBI | PLBI | EP | |
| Examination of admissibility of opposition: information related to despatch of communication + time limit deletedOppositionORIGINAL CODE: EPIDOSDOPE2PLAQ | PLAQ | EP | |
| Unpublished change to opponent dataORIGINAL CODE: EPIDOS OPPOPLBQ | PLBQ | EP | |
| Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents actLapsedNLV1 | NLV1 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| Corresponds to:REF | REF | EP | |
| European patent takes effect as a national patent in ch/liEP | EP | CH | |
| New agentNV | NV | CH | |
| Designated contracting statesAK | AK | EP | |
| Lapsed in a contracting state [announced via postgrant information from national office to epo]LapsedPG25 | PG25 | EP | |
| (expected) grantORIGINAL CODE: 0009210GRAA | GRAA | EP | |
| Grant fee paidORIGINAL CODE: EPIDOSNIGR3GRAS | GRAS | EP | |
| Despatch of communication of intention to grant a patentORIGINAL CODE: EPIDOSNIGR1GRAP | GRAP | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| Party data changed (applicant data changed or rights of an application transferred)RAP1 | RAP1 | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| Information on inventor provided before grant (corrected)RIN1 | RIN1 | EP | |
| First examination report despatched17Q | 17Q | EP | |
| Request for examination filed17P | 17P | EP | |
| Designated contracting statesAK | AK | EP | |
| Search report despatchedORIGINAL CODE: 0009013PUAL | PUAL | EP | |
| Designated contracting statesAK | AK | EP | |
| Public reference made under article 153(3) epc to a published international application that has entered the european phaseORIGINAL CODE: 0009012PUAI | PUAI | EP |
Numbers
- Publication
- 0736612
- Publication, DOCDB
- 0736612
- Publication, EPODOC
- EP0736612
- Application
- 96104926
- Application, DOCDB
- 96104926
- Application, EPODOC
- EP19960104926
Titles3
- German
- Verfahren zur Beschichtung von Sonnenkollektoren
- English
- Process for coating solar collectors
- French
- Procédé pour le revêtement de collecteurs solaires
Classification
- CPC, 6
- C23C16/50
- C23C14/0057
- C23C14/06
- C23C16/30
- Y02E10/40
- F24S70/225
- IPC, 5
- C23C14 00
- C23C14 06
- C23C16 30
- C23C16 50
- F24J2 48
Designated states7
- Contracting states, 7
- Austria
- Switzerland
- Germany
- Denmark
- Liechtenstein
- Netherlands (Kingdom of the)
- Sweden