EP1743740A1 - Process and device for floor coverings - Google Patents
Process and device for floor coverings Download PDFInfo
- Publication number
- EP1743740A1 EP1743740A1 EP05015275A EP05015275A EP1743740A1 EP 1743740 A1 EP1743740 A1 EP 1743740A1 EP 05015275 A EP05015275 A EP 05015275A EP 05015275 A EP05015275 A EP 05015275A EP 1743740 A1 EP1743740 A1 EP 1743740A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- carrier medium
- granules
- covering
- spray
- spray head
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000007921 spray Substances 0.000 claims abstract description 76
- 239000008187 granular material Substances 0.000 claims abstract description 43
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 239000011248 coating agent Substances 0.000 claims description 18
- 238000000576 coating method Methods 0.000 claims description 18
- 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
- 239000007788 liquid Substances 0.000 claims description 3
- 239000006004 Quartz sand Substances 0.000 claims description 2
- 239000011324 bead Substances 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 2
- 239000002223 garnet 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
- 238000003754 machining Methods 0.000 claims description 2
- 239000010450 olivine Substances 0.000 claims description 2
- 229910052609 olivine Inorganic materials 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 3
- 238000005507 spraying Methods 0.000 abstract 4
- 239000002609 medium Substances 0.000 description 22
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000006163 transport media Substances 0.000 description 3
- 238000005422 blasting 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
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000000446 fuel 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
- 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 characterized in that the carrier medium is introduced at about 2 to 3 times the speed of sound and under a pressure of 1000 to 7000 bar, preferably of about 3000 bar, into a mixing chamber of a spray head, that in the mixing chamber, the granules are supplied to the carrier medium and the mixture formed from these is subsequently accelerated in a focusing unit in the form of a spray about to a flow rate of 1 to 2 times the speed of sound, that the spray formed from the carrier medium and the granules after fanned out from the focussing unit and that the distance between the spray head and the coating to be processed and / or the delivery pressure of the carrier medium are adjusted such that the carrier medium before impinging on the coating by the present in the jet and surrounding air of the granules separated and is at least partially volatilized, so that the granules diffuse acts on the surface and in the surface of a variety of invisible to the human eye at a viewing distance of about 150 cm micro crater are adjusted such that the carrier
- the distance between the spray head and the covering to be processed at approximately 70 to 130 cm, the diffusion distance in which the carrier medium is volatilized by the air enclosed in the spray jet and the air surrounding it, with approximately 70 to 80 % and the distance in which the granules are separated from the carrier medium with about 20 to 30% of the distance between the spray head and the coating 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 is characterized in that at a distance of about 70 to 130 cm above the surface to be treated, a spray head provided with a mixing chamber is arranged, by means of which the granules in the Carrier medium can be introduced and focused into a spray, and that the distance between the spray head and the coating to be processed is set such that the carrier medium separated from the granules and at least before the impact with the pad by the air in the spray and surrounding it is partially volatilized, so that the granules diffuse acts on the surface and in the surface of a variety of invisible to the human eye at a viewing distance of about 150 cm microcraters are incorporated.
- 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 processed in a simple and economical manner and designed to be non-slip, 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)
- 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)
- Floor Finish (AREA)
Abstract
Description
Die Erfindung bezieht sich auf ein Verfahren und eine Vorrichtung zur Bearbeitung von Belägen, insbesondere von Fußboden- und Treppenbelägen, aus mineralischen Werkstoffen mit polierten Oberflächen durch ein abrasives Material in Form eines Granulats, das dem Belag mit Hilfe eines Trägermediums unter hohem Druck zugeführt wird.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.
Die häufigsten Personenunfälle werden verursacht durch Ausrutschen auf glatten Fuß-, Boden- oder Treppenbelägen. Insbesondere durch gleitfördernde Mittel, die auf glatte Flächen aufgetragen werden, wird die Unfallgefahr noch erheblich erhöht. In den Bereichen des öffentlichen Lebens, aber auch im Privatbereich, werden zu repräsentativen Zwecken oftmals glänzend polierte Fußboden- oder Treppenbeläge verwendet. Diese werden auch in Trocken- und Nassbereichen sowie in den stark gefährdeten Übergangsbereichen eingesetzt.The most common personal accidents are caused by slipping on smooth foot, floor or stair coverings. In particular, by slip-promoting agents that are applied to smooth surfaces, the risk of accidents is significantly increased. In the areas of public life, but also in the private sector, glossy polished floor or stair coverings are often used for representative purposes. These are also used in dry and wet areas as well as in the high risk transition areas.
Zur Erhöhung der Rutschfestigkeit bzw. zur Erzielung von rutschhemmenden Eigenschaften sind bereits verschiedene Verfahren bekannt. Diese Verfahren werden oftmals in Abhängigkeit von den Einsatzbereichen der Fußboden- und Treppenbeläge angewandt.To increase the slip resistance or to achieve anti-slip properties, various methods are already known. These methods are often applied depending on the application areas of floor and stair coverings.
Aus der
Aus der
Des Weiteren ist aus der
Diese Verfahren eignen sich nicht für hochglänzend polierte Oberflächen, da durch diese Verfahren der Glanz der Oberfläche entfernt und damit ein anderes ästhetisches Erscheinungsbild erzielt wird.These methods are not suitable for high-gloss polished surfaces, as these processes remove the gloss of the surface and thus achieve a different aesthetic appearance.
Ferner ist aus der
Aufgabe der Erfindung ist es daher, ein Verfahren sowie eine Vorrichtung zur schaffen, die in kostengünstiger Weise die Herstellung einer rutschfesten Oberfläche auf Fußboden- und Treppenbelägen, insbesondere aus mineralischen Werkstoffen, ermöglicht, ohne dass eine nachteilige Beeinträchtigung der repräsentativen, insbesondere hochglänzenden, Oberfläche gegeben ist und die zukünftigen höheren Ansprüche der DIN 51130 nach R9 bis R13 erfüllt. Des Weiteren soll erreicht werden, dass eine gleichbleibende Qualität des bearbeiteten Belages gegeben ist und dass eine Reproduzierbarkeit eines Bearbeitungsergebnisses ohne Schwierigkeiten ermöglicht wird.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.
Gemäß der Erfindung ist das Verfahren zur Bearbeitung von Belägen dadurch gekennzeichnet, dass das Trägermedium mit etwa 2- bis 3-facher Schallgeschwindigkeit und unter einem Druck von 1000 bis 7000 bar, vorzugsweise von ca. 3000 bar, in eine Mischkammer eines Sprühkopfes eingebracht wird, dass in der Mischkammer das Granulat dem Trägermedium zugeführt wird und das aus diesen gebildete Gemisch nachfolgend in einer Fokussiereinheit in Form eines Sprühstrahls etwa auf eine Strömungsgeschwindigkeit von 1- bis 2-facher Schallgeschwindigkeit beschleunigt wird, dass der aus dem Trägermedium und dem Granulat gebildete Sprühstrahl nach dem Austritt aus der Fokussiereinheit aufgefächert wird und dass der Abstand zwischen dem Sprühkopf und dem zu bearbeitenden Belag und/oder der Förderdruck des Trägermediums derart eingestellt werden, dass das Trägermedium vor dem Auftreffen auf den Belag durch die in dem Strahl befindliche und diesen umgebende Luft von dem Granulat getrennt und zumindest teilweise verflüchtigt wird, so dass das Granulat diffus auf den Belag einwirkt und in dessen Oberfläche eine Vielzahl von für das menschliche Auge bei einem Betrachtungsabstand von ca. 150 cm unsichtbare Mikrokrater eingearbeitet werden.According to the invention, the method for processing coverings is characterized in that the carrier medium is introduced at about 2 to 3 times the speed of sound and under a pressure of 1000 to 7000 bar, preferably of about 3000 bar, into a mixing chamber of a spray head, that in the mixing chamber, the granules are supplied to the carrier medium and the mixture formed from these is subsequently accelerated in a focusing unit in the form of a spray about to a flow rate of 1 to 2 times the speed of sound, that the spray formed from the carrier medium and the granules after fanned out from the focussing unit and that the distance between the spray head and the coating to be processed and / or the delivery pressure of the carrier medium are adjusted such that the carrier medium before impinging on the coating by the present in the jet and surrounding air of the granules separated and is at least partially volatilized, so that the granules diffuse acts on the surface and in the surface of a variety of invisible to the human eye at a viewing distance of about 150 cm micro crater are incorporated.
Zweckmäßig ist es hierbei, den Abstand zwischen dem Sprühkopf und dem zu bearbeitenden Belag mit etwa 70 bis 130 cm zu wählen, die Diffusionsstrecke, in der das Trägermedium durch die in dem Sprühstrahl eingeschlossene und die diesen umgebende Luft verflüchtigt wird, mit etwa 70 bis 80% und die Strecke, in der das Granulat von dem Trägermedium getrennt ist, mit etwa 20 bis 30% des Abstandes zwischen dem Sprühkopf und dem zu bearbeitenden Belag zu bemessen.It is expedient in this case to choose the distance between the spray head and the covering to be processed at approximately 70 to 130 cm, the diffusion distance in which the carrier medium is volatilized by the air enclosed in the spray jet and the air surrounding it, with approximately 70 to 80 % and the distance in which the granules are separated from the carrier medium with about 20 to 30% of the distance between the spray head and the coating to be processed.
Angebracht ist es auch, das Granulat in dem Mischkopf von dem Trägermedium über eine oder mehrere vorzugsweise in Strömungsrichtung des Trägermediums geneigt in den Mischkopf einmündende Kanäle anzusaugen.It is also appropriate to suck the granules in the mixing head of the carrier medium via one or more preferably in the flow direction of the carrier medium inclined into the mixing head opening channels.
Nach einer Weiterbildung sollten auf einer oder beiden Seiten in Verstellrichtung des Sprühstrahls umlaufende Luftwirbel gebildet werden.According to a development circulating air vortex should be formed on one or both sides in the adjustment direction of the spray.
Der aus dem Sprühkopf austretende aus dem Trägermedium und dem Granulat gebildete Sprühstrahl sollte derart aufgefächert werden, dass das Granulat auf dem zu bearbeitenden Belag in einer Breite von etwa 10 bis 20 cm, vorzugsweise mit einem Sprühstrahldurchmesser von 16 cm, diffus aufschlägt.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.
Bei einem kontinuierlich in einer Transportrichtung bewegten zu bearbeitenden Belag und einem quer zu dieser verstellbaren Sprühkopf sollten die Verstellgeschwindigkeiten des Belages und des Sprühkopfes derart aufeinander abgestimmt sein, dass der Sprühstrahl achssenkrecht zur Transportrichtung des Belages auf diesen einwirkt.In a continuously moving in a transport direction to be processed coating and a transverse to this adjustable spray head, 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.
Die Vorrichtung zur Bearbeitung von Belägen, mittels der dieses Verfahren vorteilhaft anwendbar ist, ist dadurch gekennzeichnet, dass mit einem Abstand von ca. 70 bis 130 cm über dem zu bearbeitenden Belag ein mit einer Mischkammer versehener Sprühkopf angeordnet ist, mittels dem das Granulat in das Trägermedium einbringbar und zu einem Sprühstrahl fokussierbar ist, und dass der Abstand zwischen dem Sprühkopf und dem zu bearbeitenden Belag derart eingestellt ist, dass das Trägermedium vor dem Auftreffen auf den Belag durch die in dem Sprühstrahl befindliche und diesen umgebende Luft von dem Granulat getrennt und zumindest teilweise verflüchtigt wird, so dass das Granulat diffus auf den Belag einwirkt und in dessen Oberfläche eine Vielzahl von für das menschliche Auge bei einem Betrachtungsabstand von ca. 150 cm unsichtbare Mikrokratern eingearbeitet werden.The device for processing coverings, by means of which this method is advantageously applicable, is characterized in that at a distance of about 70 to 130 cm above the surface to be treated, a spray head provided with a mixing chamber is arranged, by means of which the granules in the Carrier medium can be introduced and focused into a spray, and that the distance between the spray head and the coating to be processed is set such that the carrier medium separated from the granules and at least before the impact with the pad by the air in the spray and surrounding it is partially volatilized, so that the granules diffuse acts on the surface and in the surface of a variety of invisible to the human eye at a viewing distance of about 150 cm microcraters are incorporated.
Zweckmäßig ist es hierbei, ein- oder beidseits des Sprühstrahls in dessen Verstellrichtung verlaufend jeweils einen Luftkanal vorzusehen, die durch Leitwände, vorzugsweise in Form eines den Sprühstrahl umgebenden Mantels, gebildet sind, die in der Höhe mit Abstand zu dem Belag und zu dem Sprühkopf aufgehängt sind, wobei die Leitwände etwa parallel zu dem sich auffächernden Sprühstrahl des Gemisches angeordnet sein sollten.It is expedient in this case, in each case on one or both sides of the spray jet in the adjustment direction, to provide an air channel which is guided by guide walls, preferably in the form of a spray surrounding the jacket, which are suspended in height at a distance from the lining and to the spray head, wherein the guide walls should be arranged approximately parallel to the fanning spray of the mixture.
Angezeigt ist es ferner, den Sprühkopf und/oder den Belag derart gegeneinander zu verstellen, dass bei dessen Bearbeitung eine zweifache Überdeckung der bearbeitenden Oberfläche des Belages durch den Sprühstrahl gegeben ist.It is also shown, 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.
Das Granulat sollte mit einer Körnung von 0,02 bis 2,00 mm Korngröße dem Trägermedium beigemischt werden, auch sollte das Granulat eine Dichte von mindestens 1 bis 4 Gramm pro cm3 aufweisen.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 .
Als dem Trägermedium beizumischendes Granulat können Quarzsand, Olivin, Granat, Sick, Glaskugeln, Glassplitter oder vergleichbare harte Bauteile, als Trägermedium kann Wasser, Glykol, Öl oder flüssige Gase, wie z.B. Kohlensäure, vorgesehen werden.As granules to be admixed with the carrier medium, 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.
Bei Anwendung des erfindungsgemäßen Verfahrens ist die Gewähr gegeben, dass das Granulat mit hoher Geschwindigkeit auf den Belag aufschlägt, ohne dass dieses dabei z. Bsp. durch eine Wasserschicht gebremst wird, so dass eine intensive Bearbeitung des Belages erfolgt. Durch die Wahl der einzelnen aufeinander abgestimmten Parameter und Verfahrensschritte wird nämlich das Trägermedium zwischen dem Sprühkopf und dem Belag nahezu vollständig verflüchtigt, das Granulat kann somit intensiv auf den Belag einwirken und Mikrokrater, durch die eine Rutschhemmung hervorgerufen wird, erzeugen.When using the method according to the invention, the guarantee is given that the granules strike the pavement at high speed, without this z. For example, is braked by a layer of water, so that an intensive processing of the coating takes place. By choosing 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.
Der Einsatz von insbesondere flüssigen Träger-Medien weist ferner den Vorteil auf, dass ein flexibles, anwendungsspezifisches und umweltfreundliches Verfahren zur Herstellung von bedarfsgerechter rutschfester Ausrüstung von glatten, vor allem polierten Oberflächen, gegeben ist. Dadurch lässt sich dieses Verfahren auch an unterschiedlichen Einsatzorten anwenden. Somit ist nicht nur eine stationäre Bearbeitung von Belägen an einem Herstellungsort möglich, sondern dieses Verfahren kann auch mobil eingesetzt werden.The use of in particular 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.
Bei der Durchführung des Verfahrens ist des Weiteren in vorteilhafter Weise vorgesehen, dass ein gemischter Strahl aus dem Sprühkopf diffus ausgestossen wird. Der gemischte Strahl wird kegelförmig ausgegeben, so dass bei einem nichtbewegten Sprühkopf eine Oberfläche mit einem Durchmesser behandelt oder bearbeitet wird, der um ein Vielfaches größer als der Austrittsdurchmesser des Sprühkopfes der Fokussiereinrichtung ist. Dies wird durch einen kurzen Strömungskanal als Fokussiereinheit ermöglicht, der sich an die Mischkammer anschließt, in der das Gemisch des Strahles erzeugt wird. Turbulenzen in dem in der Mischkammer gebildeten Gemisch bleiben weitgehend in dem Sprühstrahl erhalten, so dass ein diffuser Strahlaustritt gegeben wird.In carrying out the method, it is further advantageously provided that 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.
Mit Hilfe des erfindungsgemäßen Verfahrens bzw. der vorschlagsgemäßen Vorrichtung können somit auf einfache und wirtschaftliche Weise polierte Flächen bearbeitet und rutschhemmend gestaltet werden, ohne dass die Mikrokrater, die dieses bewirken, sichtbar sind. Der dazu erforderliche Bauaufwand ist gering, dennoch ist ein überdurchschnittliches Arbeitsergebnis zu erzielen.With the aid of the method according to the invention or the proposed device, polished surfaces can thus be processed in a simple and economical manner and designed to be non-slip, 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.
In der Zeichnung ist ein Ausführungsbeispiel der gemäß der Erfindung,ausgebildeten Vorrichtung zur Bearbeitung von Belägen dargestellt, das nachfolgend im Einzelnen erläutert ist. Hierbei zeigt:
- Figur 1
- die Vorrichtung bei der Bearbeitung eines Belages, in einem Axialschnitt,
Figur 2- die Oberfläche eines mittels der Vorrichtung nach Figur 1 bearbeiteten mit Mikrokratern versehenen Belages, in vergrößerter Wiedergabe,
Figur 3- den Verstellweg des Sprühkopfes bei der Vorrichtung nach Figur 1 während der Bestrahlung des Belages, in schematischer Darstellung, und
Figur 4- die Verstellbewegung des Sprühkopfes bei kontinuierlicher Verstellbewegung des Belages, ebenfalls in schematischer Darstellung.
- FIG. 1
- the device during the machining of a covering, in an axial section,
- FIG. 2
- the surface of a microcratered coating treated by means of the device according to FIG. 1, in enlarged reproduction,
- FIG. 3
- the adjustment of the spray head in the apparatus of Figure 1 during the irradiation of the coating, in a schematic representation, and
- FIG. 4
- the adjustment of the spray head with continuous adjustment of the coating, also in a schematic representation.
Die in Figur 1 dargestellte und mit 1 bezeichnete Vorrichtung dient zur Bearbeitung eines Belages 2, insbesondere eines Fußboden- oder Treppenbelages aus mineralischen Werkstoffen, dessen Oberfläche 3 poliert ist, um in diese, wie dies in Figur 2 gezeigt ist, nahezu unsichtbare Mikrokrater 4 einzuarbeiten, damit der Belag 2 trotz der polierten Oberfläche 3 rutschhemmend ist. Dies wird im Wesentlichen durch Beschuss des Belages 2 durch ein Granulat 6 bewerkstelligt, das mit Hilfe eines Transportmediums 5, beispielsweise Wasser, das zusammen mit dem Granulat 6 mit hoher Geschwindigkeit aus einem Sprühkopf 11 ausgestoßen wird, dem Belag 2 zugeführt wird.The device shown in Figure 1 and designated 1 is used to process a
Der Sprühkopf 11 ist hierbei in einem definierten Abstand a von ca. 70 bis 130 cm vertikal über dem Belag 2 angeordnet und besteht aus einem auf das Ende eines zur Zuführung des Transportmediums 5 vorgesehenen Rohres 13 aufgeschraubten Halter 14, in den ein mit einer Düse 17 ausgerüstetes Einsatzstück 15 eingesetzt ist. Das Einsatzstück 15 weist eine Mischkammer 16 auf, in die in Strömungsrichtung des Transportmediums geneigt Kanäle 18 zur Zuführung des Granulates 6 in die Mischkammer 16 münden. Des Weiteren ist der Mischkammer 16 eine durch ein Rohrstück gebildete Fokussiereinheit 19 nachgeschaltet, die durch eine auf den Halter 14 aufgeschraubte Überwurfmutter 20 gehalten ist. Aus dem Sprühkopf 11 tritt somit ein zunächst gebündelter Sprühstrahl 12 aus, der sich nach dem Austritt aus der Fokussiereinheit 19 auffächert.The
Dem Sprühkopf 12 ist eine Ummantelung 21 zugeordnet, die durch ein geschlossenes, mit Abstand zu dem Belag 2 sowie dem Sprühstrahl 12 und parallel zu diesem angeordnetes Luftleitblech 22 gebildet ist. Auf diese Weise ist zwischen der Ummantelung 21 und dem Sprühstrahl 12 ein diesen umgebender Luftkanal 23 geschaffen, in dem Luftwirbel 24 entstehen.The
Das Trägermedium strömt etwa mit 2- bis 3-facher Schallgeschwindigkeit und unter einem Druck von 1000 bis 7000 bar, vorzugsweise unter 3000 bar, in die Mischkammer 16 des Sprühkopfes 11 ein. Aufgrund der Injektorwirkung wird in der Mischkammer 16 das Granulat 6 in diese eingesaugt und das aus diesem und dem Trägermedium 5 gebildete Gemisch wird in der Fokussiereinheit 19 zu einem Sprühstrahl 12 gebündelt, der mit etwa 1- bis 2-facher Schallgeschwindigkeit aus der Fokussiereinheit 19 austritt. Bei Austritt aus dem Sprühkopf 11 wird der Sprühstrahl 12 aufgefächert. Durch die in dem Sprühstrahl 12 eingeschlossene und die diesen umgebende Luft wird sodann auf einer Diffusionsstrecke, die etwa 70 bis 80 % des Abstandes a entspricht, das Trägermedium verflüchtigt, so dass auf einer Wegstrecke von etwa 20 bis 30 % des Abstandes a das Granulat 6 von dem Trägermedium 5 getrennt ist. Das Aufschlagen des Granulates 6 auf den Belag 2 wird somit nicht durch das Trägermedium 5 beeinträchtigt, das Granulat 6 kann vielmehr, wie dies in Figur 2 gezeigt ist, in der Oberfläche 3 des Belages 2 eine Unzahl von Mikrokratern 4 ausbilden.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
Der Sprühkopf 11 bzw. der Sprühstrahl 12 kann gemäß Figur 3 bei ruhendem Belag 2 linear über diesem verfahren werden. Die Umkehrung der Bewegungsrichtung des Sprühkopfes 11 sollte hierbei seitlich neben dem Belag 2 erfolgen, auch sollte bei der Bearbeitung des Belages eine Überdeckung des Sprühstrahls 12 gegeben sein.The
Bei einem in einer Transportrichtung T kontinuierlich bewegton, z.B. auf einer Palette 10 gelagerten Belag 2 z. Bsp. in Form von einzelnen Fliesen ist es angezeigt, den Sprühkopf 11 quer zu der Transportrichtung T zu verstellen oder pendeln zu lassen. Die Verstellbewegung des Sprühkopfes 11 sollte hierbei in Abhängigkeit von der Transportgeschwindigkeit der Palette 10 derart verlaufen und auf diese abgestellt sein, dass sich auf dem Belag 2 eine linienförmige achssenkrecht zu der Transportbewegung T verlaufende Bearbeitungsfläche ergibt. Die Bearbeitungsfläche ist in Figur 4 durch die mit F gekennzeichneten Pfeile, die Verstellbewegungen des Sprühkopfes 11 sind durch die mit St gekennzeichneten Pfeile schematisch dargestellt.In a continuously moving in a transport direction T, for example, mounted on a
Claims (15)
dadurch gekennzeichnet,
dass das Trägermedium (5) mit etwa 2- bis 3-facher Schallgeschwindigkeit und unter einem Druck von 1000 bis 7000 bar, vorzugsweise von ca. 3000 bar, in eine Mischkammer eines Sprühkopfes (11) eingebracht wird,
dass in der Mischkammer (16) das Granulat (6) dem Trägermedium (5) zugeführt wird und das aus diesen gebildete Gemisch nachfolgend in einer Fokussiereinheit (19) in Form eines Sprühstrahls (12) etwa auf eine Strömungsgeschwindigkeit von 1-bis 2-facher Schallgeschwindigkeit beschleunigt wird,
dass der aus dem Trägermedium (5) und dem Granulat (6) gebildete Sprühstrahl (12) nach dem Austritt aus der Fokussiereinheit (19) aufgefächert wird und
dass der Abstand (a) zwischen dem Sprühkopf (11) und dem zu bearbeitenden Belag (2) und/oder der Förderdruck des Trägermediums (5) derart eingestellt werden, dass das Trägermedium (5) vor dem Auftreffen auf den Belag (2) durch die in dem Sprühstrahl (12) befindliche und diesen umgebende Luft von dem Granulat (6) getrennt und zumindest teilweise verflüchtigt wird, so dass das Granulat (6) diffus auf den Belag (2) einwirkt und in dessen Oberfläche (3) eine Vielzahl von für das menschliche Auge bei einem Betrachtungsabstand von ca. 150 cm unsichtbare Mikrokrater (4) eingearbeitet werden.Method for processing coverings (2), in particular of floor and stair coverings, of mineral materials with polished surfaces (3) by means of an abrasive material in the form of a granulate (6) which is applied to the covering (2) by means of a carrier medium (5) is supplied under high pressure,
characterized,
that the carrier medium (5) is introduced with about 2 to 3 times the speed of sound and under a pressure of 1000 to 7000 bar, preferably of about 3000 bar, into a mixing chamber of a spray head (11),
that in the mixing chamber (16) the granules (6) is supplied to the carrier medium (5) and the mixture formed from these in a focusing unit (19) in the form of a spray jet (12) approximately to a flow rate of 1 to 2 times Speed of sound is accelerated,
that the spray jet (12) formed from the carrier medium (5) and the granules (6) is fanned out after emerging from the focusing unit (19) and
that the distance (a) between the spray head (11) and the covering (2) to be processed and / or the delivery pressure of the carrier medium (5) are adjusted such that the carrier medium (5) before striking the covering (2) the air in the spray jet (12) and surrounding it from the granules (6) separated and at least partially volatilized, so that the granules (6) acts diffusely on the covering (2) and in the surface (3) a plurality of invisible to the human eye at a viewing distance of about 150 cm micro crater ( 4) are incorporated.
dadurch gekennzeichnet,
dass der Abstand (a) zwischen dem Sprühkopf (11) und dem zu bearbeitenden Belag (2) mit etwa 70 bis 130 cm gewählt wird.Method according to claim 1,
characterized,
that the distance (a) between the spray head (11) and the covering (2) to be processed is selected to be approximately 70 to 130 cm.
dadurch gekennzeichnet,
dass die Diffusionsstrecke, in der das Trägermedium (5) durch die in dem Sprühstrahl (12) eingeschlossene und die diesen umgebende Luft verflüchtigt wird, etwa 70 bis 80%, und die Strecke, in der das Granulat (6) von dem Trägermedium (5) getrennt ist, etwa 20 bis 30% des Abstandes (a) zwischen dem Sprühkopf (11) und dem zu bearbeitenden Belag (2) betragen.Method according to claim 1 or 2
characterized,
that the diffusion distance in which the carrier medium (5) is volatilized by the air enclosed in the spray jet (12) and the surrounding air is about 70 to 80%, and the distance in which the granules (6) from the carrier medium (5 ), about 20 to 30% of the distance (a) between the spray head (11) and the covering to be processed (2) amount.
der Ansprüche 1 bis 3,
dadurch gekennzeichnet,
dass das Granulat (6) in dem Mischkopf (16) von dem Trägermedium (5) über einen oder mehrere vorzugsweise in Strömungsrichtung des Trägermediums (5) geneigt in den Mischkopf (16) einmündende Kanäle (18) angesaugt wird.Method according to one or more
of claims 1 to 3,
characterized,
in that the granulate (6) in the mixing head (16) is sucked in by the carrier medium (5) via one or more channels (18), which preferably lead in the direction of flow of the carrier medium (5) into the mixing head (16).
der Ansprüche 1 bis 4,
dadurch gekennzeichnet,
dass auf einer oder beiden Seiten in Verstellrichtung des Sprühstrahls (12) umlaufende Luftwirbel (24) gebildet werden.Method according to one or more
of claims 1 to 4,
characterized,
that circulating air vortexes (24) are formed on one or both sides in the adjustment direction of the spray jet (12).
der Ansprüche 1 bis 5,
dadurch gekennzeichnet,
dass der aus dem Sprühkopf (11) austretende aus dem Trägermedium (5) und dem Granulat (6) gebildete Sprühstrahl (12) derart aufgefächert wird, dass das Granulat (6) auf dem zu bearbeitenden Belag (3) in einer Breite von etwa 10 bis 20 cm, vorzugsweise mit einem Sprühstrahldurchmesser von 16 cm, diffus aufschlägt.Method according to one or more
of claims 1 to 5,
characterized,
in that the spray jet (12) emerging from the spray head (11) from the carrier medium (5) and the granules (6) is fanned out in such a way that the granules (6) have a width of approximately 10 μm on the coating (3) to be processed to 20 cm, preferably with a spray jet diameter of 16 cm, diffuses.
der Ansprüche 1 bis 6,
dadurch gekennzeichnet,
dass bei einem kontinuierlich in einer Transportrichtung (T) bewegten zu bearbeitenden Belag (2) der Sprühkopf (11) quer zu dieser verstellt oder gependelt werden, dass die Verstellgeschwindigkeiten des Belages (2) und des Sprühkopfes (11) in der Weise aufeinander abgestimmt sind, dass der Sprühstrahl (12) achssenkrecht zur Transportrichtung (T) des Belages (2) auf diesen einwirkt.Method according to one or more
of claims 1 to 6,
characterized,
that in a continuously moving in a transport direction (T) to be processed covering (2) of the spray head (11) are transversely adjusted or pendulum to this, that the adjustment speeds of the pad (2) and the spray head (11) are matched to one another in such a way in that the spray jet (12) acts on the latter axially perpendicular to the transport direction (T) of the lining (2).
dadurch gekennzeichnet,
dass mit einem Abstand (a) von ca. 70 bis 130 cm über dem zu bearbeitenden Belag (2) ein mit einer Mischkammer (16) versehener Sprühkopf (11) angeordnet ist, mittels dem das Granulat (6) in das Trägermedium (5) einbringbar und zu einem Sprühstrahl (12) fokussierbar ist, und dass der Abstand (a) zwischen dem Sprühkopf (11) und dem zu bearbeitenden Belag (2) derart eingestellt ist, dass das Trägermedium (5) vor dem Auftreffen auf den Belag (2) durch die in dem Sprühstrahl (12) befindliche und diesen umgebende Luft von dem Granulat (6) getrennt und zumindest teilweise verflüchtigt wird, so dass das Granulat (6) diffus auf den Belag (2) einwirkt und in dessen Oberfläche (3) eine Vielzahl von für das menschliche Auge bei einem Betrachtungsabstand von ca. 150 cm unsichtbare Mikrokratern (4) eingearbeitet werden.Device (1) for processing coverings (2), in particular of floor and stair coverings, of mineral materials with polished surfaces (3) an abrasive material in the form of a granulate (6) which can be supplied to the lining (2) with the aid of a carrier medium (5) under high pressure,
characterized,
that at a distance (a) from about 70 to 130 cm over the machined coating (2) with a mixing chamber (16)-provided spray head (11) is arranged, by means of which the granulate (6) in the carrier medium (5) einbringbar and focusable to a spray jet (12), and that the distance (a) between the spray head (11) and the covering to be processed (2) is set such that the carrier medium (5) before striking the covering (2 ) is separated and at least partially volatilized by the air in and / or surrounding the spray jet (12) so that the granules (6) diffuse on the coating (2) and in the surface (3) thereof Variety of invisible to the human eye at a viewing distance of about 150 cm invisible micro-craters (4) are incorporated.
dadurch gekennzeichnet,
dass ein- oder beiderseits des Sprühstrahls (12) in dessen Verstellrichtung verlaufend jeweils ein Luftkanal (23) vorgesehen ist, die durch Leitwände (22), vorzugsweise in Form eines den Sprühstrahl (12) umgebenden Mantels (21), gebildet sind, die in der Höhe mit Abstand zu dem Belag (2) und zu dem Sprühkopf (11) aufgehängt sind.Device according to claim 8,
characterized,
that one or both sides of the spray jet (12) in its direction of adjustment extend in each case an air channel (23) is provided by baffles (22), preferably are, formed in the shape of the spray jet (12) surrounding the shell (21) in the height with distance to the pad (2) and to the spray head (11) are suspended.
dadurch gekennzeichnet,
dass die Leitwände (22) etwa parallel zu dem sich auffächernden Sprühstrahl (12) des Gemisches angeordnet sind.Device according to claim 9,
characterized,
that the baffles (22) approximately parallel to the fanning-out spray jet (12) are arranged in the mixture.
dadurch gekennzeichnet,
dass der Sprühkopf (11) und/oder der Belag (2) derart gegeneinander verstellbar sind, dass bei dessen Bearbeitung eine zweifache Überdeckung der bearbeiteten Oberfläche (3) des Belages (2) durch den Sprühstrahl (12) gegeben ist.Device according to claim 9 or 10,
characterized,
in that the spray head (11) and / or the covering (2) are adjustable relative to one another in such a way that, during its machining, a double covering of the machined surface (3) of the lining (2) by the spray jet (12) is provided.
der Ansprüche 8 bis 11,
dadurch gekennzeichnet,
dass das Granulat (6) mit einer Körnung von 0,02 bis 2,00 mm Korngröße dem Trägermedium (5) beigemischt ist.Device according to one or more
of claims 8 to 11,
characterized,
that the granules (6) with a grain size of 0.02 to 2.00 mm grain size is added to the carrier medium (5).
der Ansprüche 8 bis 12,
dadurch gekennzeichnet,
dass das Granulat (6) eine Dichte von mindestens 1 bis 4 Gramm pro cm3 aufweist.Device according to one or more
of claims 8 to 12,
characterized,
that the granulate (6) has a density of at least 1 to 4 grams per cm 3.
der Ansprüche 8 bis 13,
dadurch gekennzeichnet,
dass als dem Trägermedium (5) beizumischendes Granulat (6) Quarzsand, Olivin Granat, Sick Glaskugeln oder Glassplitter oder vergleichbare harte Bauteile vorgesehen sind.Device according to one or more
of claims 8 to 13,
characterized,
that as the carrier medium (5) to be mixed granules (6) quartz sand, olivine garnet, Sick glass beads or glass splinters or comparable hard components are provided.
der Ansprüche 8 bis 14,
dadurch gekennzeichnet,
dass als Trägermedium (5) Wasser, Glykol, ÖI oder flüssige Gase, wie z.B. Kohlensäure,vorgesehen sind.Device according to one or more
of claims 8 to 14,
characterized,
in that the carrier medium (5) is water, glycol, oil or liquid gases, such as, for example, carbonic acid.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES05015275T ES2292019T3 (en) | 2005-07-14 | 2005-07-14 | PROCEDURE AND DEVICE FOR COATING TREATMENT. |
EP05015275A EP1743740B1 (en) | 2005-07-14 | 2005-07-14 | Process and device for floor coverings |
DE502005001261T DE502005001261D1 (en) | 2005-07-14 | 2005-07-14 | Method and device for processing coverings |
AT05015275T ATE369940T1 (en) | 2005-07-14 | 2005-07-14 | METHOD AND DEVICE FOR PROCESSING COVERS |
PL05015275T PL1743740T3 (en) | 2005-07-14 | 2005-07-14 | Process and device for floor coverings |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05015275A EP1743740B1 (en) | 2005-07-14 | 2005-07-14 | Process and device for floor coverings |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1743740A1 true EP1743740A1 (en) | 2007-01-17 |
EP1743740B1 EP1743740B1 (en) | 2007-08-15 |
Family
ID=35395420
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP05015275A Active EP1743740B1 (en) | 2005-07-14 | 2005-07-14 | Process and device for floor coverings |
Country Status (5)
Country | Link |
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EP (1) | EP1743740B1 (en) |
AT (1) | ATE369940T1 (en) |
DE (1) | DE502005001261D1 (en) |
ES (1) | ES2292019T3 (en) |
PL (1) | PL1743740T3 (en) |
Cited By (2)
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CN103481204A (en) * | 2013-09-28 | 2014-01-01 | 宁波大隆机器制造有限公司 | Spray nozzle for high-pressure water-jet normal-temperature scale removal process |
WO2016071866A1 (en) * | 2014-11-05 | 2016-05-12 | Institute Of Geonics As Cr, V. V. I. | A high velocity abrasive fluid jet cutting device |
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- 2005-07-14 PL PL05015275T patent/PL1743740T3/en unknown
- 2005-07-14 DE DE502005001261T patent/DE502005001261D1/en active Active
- 2005-07-14 EP EP05015275A patent/EP1743740B1/en active Active
- 2005-07-14 ES ES05015275T patent/ES2292019T3/en active Active
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CN103481204A (en) * | 2013-09-28 | 2014-01-01 | 宁波大隆机器制造有限公司 | Spray nozzle for high-pressure water-jet normal-temperature scale removal process |
CN103481204B (en) * | 2013-09-28 | 2016-04-06 | 宁波大隆机器制造有限公司 | For the nozzle of high-pressure water jet normal temperature descaling process |
WO2016071866A1 (en) * | 2014-11-05 | 2016-05-12 | Institute Of Geonics As Cr, V. V. I. | A high velocity abrasive fluid jet cutting device |
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Publication number | Publication date |
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PL1743740T3 (en) | 2008-01-31 |
EP1743740B1 (en) | 2007-08-15 |
DE502005001261D1 (en) | 2007-09-27 |
ATE369940T1 (en) | 2007-09-15 |
ES2292019T3 (en) | 2008-03-01 |
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