EP1743740B1 - Procédé et dispositif pour le traitement de revêtements - Google Patents
Procédé et dispositif pour le traitement de revêtements Download PDFInfo
- Publication number
- EP1743740B1 EP1743740B1 EP05015275A EP05015275A EP1743740B1 EP 1743740 B1 EP1743740 B1 EP 1743740B1 EP 05015275 A EP05015275 A EP 05015275A EP 05015275 A EP05015275 A EP 05015275A EP 1743740 B1 EP1743740 B1 EP 1743740B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- covering
- carrier medium
- granulate
- spray head
- spray
- 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.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 66
- 239000008187 granular material Substances 0.000 claims abstract description 38
- 239000000203 mixture Substances 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 5
- 239000011707 mineral Substances 0.000 claims description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 4
- 239000011521 glass Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 239000003082 abrasive agent Substances 0.000 claims description 3
- 238000009792 diffusion process Methods 0.000 claims description 3
- 239000006004 Quartz sand Substances 0.000 claims description 2
- 239000012634 fragment Substances 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims 2
- 230000003116 impacting effect Effects 0.000 claims 2
- MBDHLQKZIVIDEY-UHFFFAOYSA-N Olivin Natural products COc1cc(C=C(C)/C(=O)c2c(O)cc(O)cc2O)ccc1O MBDHLQKZIVIDEY-UHFFFAOYSA-N 0.000 claims 1
- 230000001133 acceleration Effects 0.000 claims 1
- 229910002092 carbon dioxide Inorganic materials 0.000 claims 1
- 239000001569 carbon dioxide Substances 0.000 claims 1
- PIHTXGRVQBTVRE-KFYAXVMHSA-N olivin Chemical compound OC1=CC(O)=C2C(O)=C(C(=O)[C@H]([C@H]([C@H](OC)C(=O)[C@@H](O)[C@@H](C)O)C3)O)C3=CC2=C1 PIHTXGRVQBTVRE-KFYAXVMHSA-N 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 4
- 239000002609 medium Substances 0.000 description 15
- 239000011248 coating agent Substances 0.000 description 10
- 238000000576 coating method Methods 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000006163 transport media Substances 0.000 description 3
- 238000005422 blasting Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 238000005488 sandblasting Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002223 garnet Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000010450 olivine Substances 0.000 description 1
- 229910052609 olivine Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- -1 sickle Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C1/00—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods
- B24C1/003—Methods for use of abrasive blasting for producing particular effects; Use of auxiliary equipment in connection with such methods using material which dissolves or changes phase after the treatment, e.g. ice, CO2
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C5/00—Devices or accessories for generating abrasive blasts
- B24C5/02—Blast guns, e.g. for generating high velocity abrasive fluid jets for cutting materials
- B24C5/04—Nozzles therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B24—GRINDING; POLISHING
- B24C—ABRASIVE OR RELATED BLASTING WITH PARTICULATE MATERIAL
- B24C7/00—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts
- B24C7/0046—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier
- B24C7/0076—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a gaseous carrier the blasting medium being a liquid stream
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28D—WORKING STONE OR STONE-LIKE MATERIALS
- B28D1/00—Working stone or stone-like materials, e.g. brick, concrete or glass, not provided for elsewhere; Machines, devices, tools therefor
- B28D1/26—Working stone or stone-like materials, e.g. brick, concrete or glass, not provided for elsewhere; Machines, devices, tools therefor by impact tools, e.g. by chisels or other tools having a cutting edge
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04F—FINISHING WORK ON BUILDINGS, e.g. STAIRS, FLOORS
- E04F15/00—Flooring
Definitions
- the invention relates to a method and a device for processing coverings, in particular of floor and stair coverings, of mineral materials with polished surfaces by an abrasive material in the form of granules, which is supplied to the covering with the aid of a support medium under high pressure.
- a method for producing a desired roughness in which a sandblasting material is thrown under high pressure by means of air onto the surface of the covering.
- the sandblasting material is applied uncontrolled on the surface and thereby produces irregular roughening with a strong matting in the surface.
- the object of the invention is therefore to provide a method and a device for the cost-effective manner of producing a non-slip surface on floor and stair coverings, in particular of mineral materials, allows, without any adverse effect on the representative, especially high-gloss, surface is given and meets the future higher requirements of DIN 51130 R9 to R13. Furthermore, it should be achieved that a consistent quality of the treated coating is given and that a reproducibility of a processing result is made possible without difficulty.
- the method for processing coverings is formed by the features of the characterizing part of claim 1.
- the diffusion distance in which the carrier medium is volatilized by the trapped in the spray and the surrounding air with about 70 to 80% and the distance in which the granules are separated from the support medium with about 20 to 30% of the distance between the spray head and the surface to be processed.
- circulating air vortex should be formed on one or both sides in the adjustment direction of the spray.
- the spray jet emerging from the spray head and formed from the carrier medium and the granules should be fanned out in such a way that the granules diffuse diffusely on the coating to be processed in a width of about 10 to 20 cm, preferably with a spray jet diameter of 16 cm.
- the adjustment speeds of the pad and the spray head should be coordinated so that the spray acts axially perpendicular to the transport direction of the pad on this.
- the device for processing coverings by means of which this method is advantageously applicable, has the features of the characterizing part of claim 7.
- the guide walls should in this case be arranged approximately parallel to the fanning spray jet of the mixture.
- the spray head and / or the lining to be adjusted against each other in such a way that during its processing a double overlap of the processing surface of the lining is given by the spray.
- the granules should be mixed with a grain size of 0.02 to 2.00 mm grain size of the support medium, and the granules should have a density of at least 1 to 4 grams per cm 3 .
- quartz sand, olivine, garnet, sickle, glass beads, glass splinters or comparable hard components may be used, as the carrier medium may be water, glycol, oil or liquid gases, such as. Carbonic acid, be provided.
- the guarantee is given that the granules strike the pavement at high speed, without this z.
- the granules strike the pavement at high speed, without this z.
- the individual coordinated parameters and process steps namely, the carrier medium between the spray head and the coating is almost completely volatilized, the granules can thus act intensively on the coating and micro crater, which is caused by an anti-slip generate.
- liquid carrier media also has the advantage that a flexible, application-specific and environmentally friendly process for the production of non-slip equipment of smooth, especially polished surfaces, is given. As a result, this method can also be used at different locations. So not just a stationary one Processing of coverings at a place of manufacture possible, but this method can also be used on the move.
- a mixed jet is diffusely ejected from the spray head.
- the mixed jet is outputted conically, so that when a non-moving spray head, a surface is treated or processed with a diameter which is many times greater than the exit diameter of the spray head of the focusing. This is made possible by a short flow channel as focussing unit which adjoins the mixing chamber in which the mixture of the jet is generated. Turbulence in the mixture formed in the mixing chamber is largely retained in the spray, giving a diffused jet exit.
- polished surfaces can thus be machined and designed to be non-slip in a simple and economical manner, without the microcraters which cause this being visible.
- the construction effort required for this is low, yet an above-average work result can be achieved.
- the device shown in Figure 1 and designated 1 is used to process a coating 2, in particular a floor or staircase made of mineral materials, the surface 3 is polished to incorporate into this, as shown in Figure 2, almost invisible microcrater 4 so that the pad 2 is non-slip despite the polished surface 3.
- This is accomplished essentially by bombardment of the lining 2 by a granulate 6, which is supplied to the lining 2 by means of a transport medium 5, for example water, which is ejected together with the granules 6 at high speed from a spray head 11.
- the spray head 11 is arranged here at a defined distance a of about 70 to 130 cm vertically above the lining 2 and consists of a screwed onto the end of a designated for feeding the transport medium 5 tube 13 holder 14, in the one with a nozzle 17th equipped insert 15 is inserted.
- the insert 15 has a mixing chamber 16, in the direction of flow of the transport medium inclined channels 18 for supplying the granules 6 into the mixing chamber 16 open.
- the mixing chamber 16 is followed by a focussing unit 19 formed by a tube piece, which is held by a screwed onto the holder 14 union nut 20. From the spray head 11 thus exits an initially focused spray jet 12, which fanned out after exiting the focusing unit 19.
- the spray head 12 is associated with a casing 21, which is formed by a closed, at a distance from the lining 2 and the spray jet 12 and parallel to this arranged air guide plate 22. In this way, a surrounding air duct 23 is created between the casing 21 and the spray jet 12, 24 arise in the air vortex.
- the carrier medium flows approximately at 2 to 3 times the speed of sound and under a pressure of 1000 to 7000 bar, preferably below 3000 bar, in the mixing chamber 16 of the spray head 11 a. Due to the injector effect, the granulate 6 is sucked into the mixing chamber 16 and the mixture formed from this and the carrier medium 5 is concentrated in the focusing unit 19 to form a spray jet 12 which emerges from the focusing unit 19 at about 1 to 2 times the speed of sound , Upon exiting the spray head 11, the spray jet 12 is fanned out.
- the carrier medium By trapped in the spray 12 and the surrounding air is then volatilized on a diffusion path which corresponds to about 70 to 80% of the distance a, the carrier medium, so that over a distance of about 20 to 30% of the distance a, the granules. 6 is separated from the carrier medium 5.
- the impact of the granules 6 on the pad 2 is thus not affected by the support medium 5, the granules 6 may rather, as shown in Figure 2, in the surface 3 of the pad 2 form a myriad of microcraters 4.
- the spray head 11 and the spray jet 12 can be moved in accordance with Figure 3 with resting pad 2 linearly over this.
- the reversal of the direction of movement of the spray head 11 should in this case take place laterally next to the lining 2, and should be given during the processing of the covering an overlap of the spray jet 12.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Mining & Mineral Resources (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
- Floor Finish (AREA)
- Container Filling Or Packaging Operations (AREA)
- Details Of Indoor Wiring (AREA)
- Lining Or Joining Of Plastics Or The Like (AREA)
- Housing For Livestock And Birds (AREA)
- Catching Or Destruction (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
Claims (13)
- Procédé de traitement de recouvrements (2), en particulier des recouvrements de planchers et d'escaliers en matériau minéral aux surfaces polies (3), moyennant un matériau abrasif sous la forme de granulé (6) appliqué à l'aide d'un milieu support (5) sous pression élevée sur le recouvrement (2), le milieu support (5) étant introduit dans une chambre de mélange d'une tête de pulvérisation (11), le granulé (6) étant dirigé dans la chambre de mélange (16) vers le milieu support (5) et le mélange qui en résulte, étant ensuite accéléré dans une unité de focalisation (19) sous la forme d'un jet de pulvérisation (12), le jet de pulvérisation (12) formé par le milieu support (5) et le granulé (6) étant dispersé après être sorti de l'unité de focalisation (19), et la distance (a) entre la tête de pulvérisation (11) et le recouvrement à traiter (2) et/ou la pression de refoulement du milieu support (5) étant réglées tel qu'avant d'entrer en contact avec le recouvrement (2), le milieu support (5) est séparé du granulé (6) et au moins partiellement volatilisé par l'air contenu dans et celui entourant le jet de pulvérisation (12),
caractérisé en ce que
le milieu support (5) est introduit avec 2 à 3 fois la vitesse du son et sous une pression de 1000 à 7000 bars, de préférence env. 3000 bars, dans la chambre de mélange de la tête de pulvérisation (11), que l'accélération a lieu à une vitesse de flux de 1 à 2 fois la vitesse du son et où la distance (a) entre la tête de pulvérisation (11) et le recouvrement à traiter (2) est réglée à 70-130 cm, de sorte que le granulé (6) agit de manière diffuse sur le recouvrement (2) et qu'il est pratiqué dans sa surface (3) une multitude de microcratères (4) qui, à une distance d'observation d'env. 150 cm, ne sont plus visibles à l'oeil humain. - Procédé d'après la revendication 1,
caractérisé en ce que
le trajet de diffusion, sur lequel le milieu support (5) est volatilisé par l'air contenu dans et celui entourant le jet de pulvérisation (12), correspond à env. 70-80 %, et le trajet, sur lequel le granulé (6) est séparé du milieu support (5), correspond à env. 20-30 % de la distance (a) entre la tête de pulvérisation (11) et le recouvrement à traiter (2). - Procédé d'après les revendications 1 ou 2,
caractérisé en ce que
dans la tête de mélange (16), le granulé (6) est aspiré par le milieu support (5) moyennant un ou plusieurs canaux (18) inclinés de préférence en direction du flux du milieu support (5), dans la tête de mélange (16). - Procédé d'après une des revendications 1 à 3,
caractérisé en ce que
sur un ou sur les deux côtés, il est formé des tourbillons d'air (24) circulant en direction du réglage du jet de pulvérisation (12). - Procédé d'après une des revendications 1 à 4,
caractérisé en ce que
le jet de pulvérisation (12) sortant de la tête de pulvérisation (11) et formé par le milieu support (5) et le granulé (6) est dispersé de sorte que le granulé (6) atteint le recouvrement à traiter (2) de manière diffuse sur une largeur de 10 à 20 cm, de préférence avec un diamètre du jet de pulvérisation de 16 cm. - Procédé d'après une des revendications 1 à 5,
caractérisé en ce que
dans le cas d'un recouvrement (2) déplacé continuellement dans une direction de transport (T), la tête de pulvérisation (11) se laisse déplacer ou osciller transversalement à celui-ci et que les vitesses de réglage du recouvrement (2) et de la tête de pulvérisation (11) se laissent adapter l'une à l'autre de sorte que le jet de pulvérisation (12) agit perpendiculairement à l'axe de la direction de transport (T) du recouvrement (2). - Dispositif (1) de traitement de recouvrements (2), en particulier des recouvrements de planchers et d'escaliers en matériau minéral aux surfaces polies (3), moyennant un matériau abrasif sous la forme de granulé (6) appliqué à l'aide d'un milieu support (5) sous pression élevée sur le recouvrement (2), où, au-dessus du recouvrement à traiter (2), il est disposé une tête de pulvérisation (11) munie d'une chambre de mélange (16) permettant de faire pénétrer le granulé (6) dans le milieu support (5) et de le focaliser pour former un jet de pulvérisation (12), la distance (a) entre la tête de pulvérisation (11) et le recouvrement à traiter (2) étant réglée tel qu'avant d'entrer en contact avec le recouvrement (2), le milieu support (5) est séparé du granulé (6) et au moins partiellement volatilisé par l'air contenu dans et celui entourant le jet de pulvérisation (12),
caractérisé en ce que
la tête de pulvérisation (11) est disposée à une distance (a) d'entre 70 et 130 cm au-dessus du recouvrement à traiter (2), de sorte que le granulé (6) agit de manière diffuse sur le recouvrement (2) et qu'il est pratiqué dans sa surface (3) une multitude de microcratères (4) qui, à une distance d'observation d'env. 150 cm, ne sont plus visibles à l'oeil humain et que, sur un ou sur les deux côtés du jet de pulvérisation (12), il est prévu en direction du sens de réglage du jet, respectivement un canal d'air (23) formé(s) par les parois de guidage (22), de préférence sous la forme d'une enveloppe (21) entourant le jet de pulvérisation (12), et qui est disposé (sont disposés) à une certaine distance au-dessus du recouvrement (2) et du jet de pulvérisation (12). - Dispositif d'après la revendication 7,
caractérisé en ce que
les parois de guidage (22) sont disposées à peu près parallèle au jet de mélange (12) qui se disperse. - Dispositif d'après les revendications 7 ou 8,
caractérisé en ce que
la tête de pulvérisation (11) et/ou le recouvrement (2) se laissent régler entre eux de sorte que lors du traitement, le jet de pulvérisation (12) forme une double couche sur la surface traitée (3) du recouvrement (2). - Dispositif d'après une des revendications 7 à 9,
caractérisé en ce que
le granulé (6) mélangé au milieu support (5) a une granulation de 0,02 à 2,00 mm. - Dispositif d'après une des revendications 7 à 10,
caractérisé en ce que
la densité du granulé (6) s'élève à au moins 1 à 4 grammes par cm3. - Dispositif d'après une des revendications 7 à 11,
caractérisé en ce que,
en tant que granulé (6) à mélanger avec le milieu support (5), il est prévu du sable siliceux, de l'olivine, du grenat, du carbure de silicium, des billes de verre, des débris de verre ou des objet durs similaires. - Dispositif d'après une des revendications 7 à 12,
caractérisé en ce que,
en tant que milieu support (5), il est utilisé de l'eau, des glycols, de l'huile ou des gaz liquéfiés tel que du dioxyde de carbone.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES05015275T ES2292019T3 (es) | 2005-07-14 | 2005-07-14 | Procedimiento y dispositivo de tratamiento de revestimientos. |
EP05015275A EP1743740B1 (fr) | 2005-07-14 | 2005-07-14 | Procédé et dispositif pour le traitement de revêtements |
PL05015275T PL1743740T3 (pl) | 2005-07-14 | 2005-07-14 | Sposób i urządzenie do obróbki nawierzchni |
DE502005001261T DE502005001261D1 (de) | 2005-07-14 | 2005-07-14 | Verfahren und Vorrichtung zur Bearbeitung von Belägen |
AT05015275T ATE369940T1 (de) | 2005-07-14 | 2005-07-14 | Verfahren und vorrichtung zur bearbeitung von belägen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05015275A EP1743740B1 (fr) | 2005-07-14 | 2005-07-14 | Procédé et dispositif pour le traitement de revêtements |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1743740A1 EP1743740A1 (fr) | 2007-01-17 |
EP1743740B1 true EP1743740B1 (fr) | 2007-08-15 |
Family
ID=35395420
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP05015275A Active EP1743740B1 (fr) | 2005-07-14 | 2005-07-14 | Procédé et dispositif pour le traitement de revêtements |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP1743740B1 (fr) |
AT (1) | ATE369940T1 (fr) |
DE (1) | DE502005001261D1 (fr) |
ES (1) | ES2292019T3 (fr) |
PL (1) | PL1743740T3 (fr) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103481204B (zh) * | 2013-09-28 | 2016-04-06 | 宁波大隆机器制造有限公司 | 用于高压水射流常温除鳞工艺的喷嘴 |
CZ307832B6 (cs) * | 2014-11-05 | 2019-06-12 | Ăšstav geoniky AV ÄŚR, v. v. i. | Nástroj pro řezání vysokorychlostním abrazivním kapalinovým paprskem |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3139427A1 (de) | 1980-12-09 | 1982-09-23 | FAL AG, 6300 Zug | Verfahren zum aufrauhen ebener schnittflaechen von formkoerpern aus natursteinen und anlage zur durchfuehrung des verfahrens |
DE3545064A1 (de) | 1985-12-19 | 1987-06-25 | Linde Ag | Verfahren zum flammstrahlen von natuerlichen und/oder kuenstlichen steinarten |
JPH0673812B2 (ja) * | 1989-08-03 | 1994-09-21 | ダイキン工業株式会社 | 粉体加速方法及び粉体噴射装置並びに粉体輸送装置 |
DE3933843A1 (de) | 1989-10-10 | 1991-04-18 | Hofmann Hermann | Verfahren und vorrichtung zur bearbeitung von steinoberflaechen durch brennen oder stocken |
JPH05269733A (ja) * | 1992-03-26 | 1993-10-19 | Hideharu Osada | 建築用パネルの製造方法 |
JPH0825225A (ja) * | 1994-07-12 | 1996-01-30 | Chiyoda Tech & Ind Co Ltd | 石材の表面加工方法 |
DE19518270C1 (de) | 1995-05-18 | 1996-08-22 | Fraunhofer Ges Forschung | Rutschfester Fußbodenbelag und Verfahren zu seiner Herstellung |
GB0200372D0 (en) * | 2002-01-08 | 2002-02-20 | Aquablast Ltd | Removing surface coatings and contamination |
-
2005
- 2005-07-14 PL PL05015275T patent/PL1743740T3/pl unknown
- 2005-07-14 DE DE502005001261T patent/DE502005001261D1/de active Active
- 2005-07-14 ES ES05015275T patent/ES2292019T3/es active Active
- 2005-07-14 AT AT05015275T patent/ATE369940T1/de active
- 2005-07-14 EP EP05015275A patent/EP1743740B1/fr active Active
Also Published As
Publication number | Publication date |
---|---|
DE502005001261D1 (de) | 2007-09-27 |
PL1743740T3 (pl) | 2008-01-31 |
EP1743740A1 (fr) | 2007-01-17 |
ES2292019T3 (es) | 2008-03-01 |
ATE369940T1 (de) | 2007-09-15 |
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