EP0582191A1 - Dispositif et procédé pour le traitement de surfaces sensibles, notamment de sculptures - Google Patents

Dispositif et procédé pour le traitement de surfaces sensibles, notamment de sculptures Download PDF

Info

Publication number
EP0582191A1
EP0582191A1 EP93112046A EP93112046A EP0582191A1 EP 0582191 A1 EP0582191 A1 EP 0582191A1 EP 93112046 A EP93112046 A EP 93112046A EP 93112046 A EP93112046 A EP 93112046A EP 0582191 A1 EP0582191 A1 EP 0582191A1
Authority
EP
European Patent Office
Prior art keywords
jet
treatment
section
mixing chamber
mixing
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
Application number
EP93112046A
Other languages
German (de)
English (en)
Other versions
EP0582191B1 (fr
Inventor
Johann Szücs
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of EP0582191A1 publication Critical patent/EP0582191A1/fr
Application granted granted Critical
Publication of EP0582191B1 publication Critical patent/EP0582191B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • 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
    • B24C7/0084—Equipment for feeding abrasive material; Controlling the flowability, constitution, or other physical characteristics of abrasive blasts the abrasive material being fed in a mixture of liquid and gas

Definitions

  • the invention relates to a device for the treatment, for example cleaning, of sensitive surfaces, in particular of strongly contoured surfaces such as that of sculptures made of wood, plaster, bronze and the like, according to the preamble of claim 1 and a method for the treatment of sensitive, strong contoured surfaces according to the preamble of claim 11.
  • blasting processes with abrasive particles are known which are thrown in a straight line under high pressure onto the surface to be cleaned.
  • EP 0 171 448 B1 discloses a method and a device for the same application, namely the cleaning of essentially planar, but in contrast to the previous, sensitive surfaces, according to which or in which cleaning by means of a cleaning jet rotating about its central axis he follows.
  • the cleaning jet contains atomized water, air and a cleaning agent consisting of solid particles.
  • the known device is essentially formed by a mixing head, into the mixing chamber of which a mixture of water and air is introduced under pressure on the one hand via an atomizing nozzle and on the other hand a mixture of air and solid particles via a further feed.
  • a first of the two mixture flows is introduced into the mixing chamber via a simple cylindrical bore.
  • the second mixture stream strikes the mixing chamber at an angle and an eccentricity to the first mixture stream.
  • the two mixture flows mix and leave the mixing head as a rotating cleaning jet.
  • the two mixture streams are introduced at an angle and eccentrically to one another into the mixing chamber of the known mixing head, at least one of the two pressurized streams is thrown against the mixing chamber wall opposite its inlet mouth and can produce an undesirable material removal in the impact area with increasing use of the mixing head.
  • This undesirable effect is particularly important because of the mutual eccentricity of the two mixture flows introduced into the mixing chamber, since the mixture flow directed onto the mixing chamber wall still has a large part of its kinetic energy on impact.
  • the invention has set itself the task of avoiding the disadvantages associated with the methods and devices known from the prior art.
  • a gentle and thorough treatment of sensitive and strongly contoured surfaces should be made possible.
  • a device for generating a rotating and therefore gentle treatment jet particularly good mixing and angular momentum transmission in the mixing chamber of a mixing head with simultaneous reduction in wear of the mixing chamber wall are to be achieved.
  • the jet particles By using a blasting process, namely a blasting process in which the blasting content is in its When the central axis pointing in the direction of the jet progresses, the jet particles, namely atomized liquid treatment agent and / or solid polishing or grinding particles, act in the form of a gentle wiping movement on the surface to be treated.
  • a blasting method according to the invention for the treatment of sensitive, highly contoured surfaces, for example of sculptures, the restoration of such objects can be considerably simplified and because of the time saved compared to the purely manual methods commonly used, for example the scraping out of dirt with appropriate hand tools or wiping with a rag. The risk of destroying a valuable object is reduced.
  • a mixture jet which can contain a single or also a mixture of different liquid treatment agents, is introduced via a first feed through a slot-shaped inlet opening into the mixing chamber, as a result of which a jet, which is to be referred to as a wide jet and is extended transversely to the direction of jet progress arises.
  • slit-shaped means that the inlet opening running transversely or approximately transversely to the central longitudinal axis of the broad jet has a longer and a shorter main axis. It is preferably simply rectangular, possibly with semicircular short sides.
  • this broad jet covers the path of the second jet, which is introduced into the mixing chamber at an angle of inclination and eccentrically to the central longitudinal axis of the wide jet, to a greater extent or even completely or almost completely.
  • the longitudinal axis of the inlet opening has a transverse component to the plane which is spanned by the parallel projections of the blasting center axes of the two jets introduced into the mixing chamber.
  • the longitudinal axis of this opening is preferably approximately at right angles on this plane.
  • the inlet with the slit-shaped opening can be designed, for example, as a slit diaphragm or, in a particularly advantageous embodiment, as the narrowest passage opening of a nozzle which tapers towards this narrowest opening and then reopens.
  • the second jet which can contain a mixture of compressed gas and solid particles, is introduced into the mixing chamber via a second feed, the passage cross section of which according to the invention widens in its course towards the inlet into the mixing chamber.
  • the kinetic energy of this second beam can be reduced with an otherwise identical mass throughput.
  • This effect is particularly advantageously brought about by the inventive design of a sudden widening.
  • This is the only way to ensure that the second jet in its core area, which is eccentric to the central axis of the first jet and could shoot past the first jet, no longer has a pronounced speed peak, but instead has an overall turbulent, comparatively blunt speed profile.
  • the second beam or its components therefore point when they meet the first beam in the direction of the beam advance at a lower speed than would be the case if the course of the second feed was even or gradually widened.
  • the jet content has cross-speed components, which in turn contribute to the good mixing and thus also to the improvement of the angular momentum imprinting or generation.
  • the widening takes place from a first to a second circular-cylindrical passage cross section, the diameter ratio of which is in the range between 2: 3 and 4: 5, particularly preferably around 3: 4.
  • This ratio is preferably between 4: 3 and 6: 5, in particular 5: 4, so that in the preferred embodiment of the invention, the ratio chain of approximately 3: 4: from the diameter of the first section of the second feeder via its second section to the mixing chamber diameter. 5 results.
  • a protrusion is advantageously formed behind the area of the mixing chamber wall which is at the level of the intersection of the two mixing jets, in particular behind the area which lies in the extension of the central axis of the second jet.
  • This projection is advantageously made as sharp as possible. This prevents or at least reduces the beam components hitting the chamber wall at an angle to the chamber wall and at the same time promotes the early formation of rotation.
  • the mixture jet formed in this way and already rotating is preferably guided through a section of the mixing head which is tapered gradually, in particular continuously, and adjoins the mixing chamber and is constricted in the process.
  • the geometry of this The section is dimensioned according to the invention such that the stretch formed as the quotient of the length and - in the case of a preferred circular-cylindrical cross-sectional shape - the inlet diameter of the section is between 4: 1 and 8: 1 and is particularly preferably 5: 1.
  • the taper as the quotient of the inlet and outlet diameter should be at most 4: 1 and preferably only about 2.3: 1.
  • Said projection is preferably formed in that the tapered section has a smaller diameter than the mixing chamber at its mixing chamber end and an annular projection or a circumferential shoulder is formed.
  • the tapered section preferably abuts a sintered ring at this transition point.
  • the diameter of the mixing chamber should be reduced by a ratio of about 5: 4, but at least the protrusion should protrude half a millimeter into the opening cross-section.
  • the tapered section like the inner walls of the mixing head that preferably come into contact with the jet components, is formed by a material that has a surface that is wear-resistant but at the same time has sufficient roughness to allow the jet components to slide along easily to prevent.
  • the desired properties can be achieved by using different ceramic materials, so that in particular the tapered section has at least one ceramic surface, but the projection itself is particularly wear-resistant as a sintered ring.
  • the mixture jet is stabilized and stabilized in the rotation, as a result of which, in particular, a treatment jet which is particularly suitable for the main use and cone-shaped with a small opening angle can be generated.
  • the ratio of the lengths of these two sections lying one behind the other is also important.
  • the length of the outlet-side section is advantageously at least a sixth, in particular a fifth to a quarter, of the length of the tapered section.
  • the liquid treatment agent is in most cases water. Depending on the type of treatment, the water can also be replaced by a special washing liquid or a protective liquid, for example against rust. If necessary, a corresponding mixture of different treatment agents can also be used.
  • solid particles are additionally fed to the mixing head as polishing or grinding particles.
  • ice particles can also form these solid particles, with ice particles that have already crystallized being fed to the mixing head, or these ice particles are only generated in the already atomized mixture jet following the mixing chamber.
  • a rotating treatment jet which has an opening angle of less than 30 °, in particular even less than 20 °, in order to reach behind the protruding surfaces and possibly even partially hidden surfaces with the wiping movement To let the beam content act as specifically as possible only in such an area.
  • mixing head 1 a first jet of a mixture of a liquid treatment agent and a pressurized gas is fed via a first feed 10 and a second jet is fed via a second feed 20, which is a pressurized gas, an example of which is given below always called compressed air, and contains solid particles.
  • the central axis 22 of the second feed 20 is inclined at an angle ⁇ to the central axis 11 of the first jet introduced through the first feed 10 via an inlet 12 into the mixing chamber 30.
  • the central axes 11 and 22 of the two beams run eccentrically past one another, so that the mixture jet formed from the two beams is set in rotation about its beam advancement direction, which coincides with the axis 11 of the first beam.
  • the central axis 11 of the first jet introduced into the mixing chamber 30 via the inlet 12 points to the outlet of the mixing chamber 30.
  • the central steel axis 11 even coincides with the axis of symmetry of the rotationally symmetrical mixing chamber 30.
  • other arrangements for the jet introduction into the mixing chamber are also conceivable while maintaining an inclination angle ⁇ and an eccentricity.
  • Outlet section 44 is a section with an approximately constant cross-sectional profile educated.
  • the treatment jet 50 emerging from the outlet 44 opens conically at an opening angle ⁇ of approximately 20 °, so that the treatment jet opens at the usual working distance to a cone surface which is at most five marks in size.
  • the first jet supplied via the first feed 10 is in the form of an extended one in a direction transverse to its center axis 11 and therefore as a wide jet referred to the beam introduced into the mixing chamber 30. It is thereby achieved that the cross-sectional area of the second beam, which strikes the wide beam with an eccentricity, is largely covered by the wide beam and its kinetic energy is thus absorbed in the best possible way.
  • the broad jet protects the area 34 of the mixing chamber wall which lies in a straight extension of the central axis 22 of the second feed 20.
  • the second jet shooting past would strike the chamber wall in area 34, as could be the case, for example, with a mixing head designed according to EP 0 171 448 B1.
  • the smaller the dimensions of a mixing head the better.
  • the shielding described by the first beam designed as a wide beam without the shielding described by the first beam designed as a wide beam, a not insignificant material removal from the wall region 34 would be feared.
  • the nozzle 12 is shown at its narrowest point in cross section AA.
  • This narrowest point is formed by a slot-shaped nozzle opening 14, which is rectangular in the exemplary embodiment, the longitudinal axis 16 of which is approximately perpendicular to the plane defined by the central longitudinal axis 11 of the nozzle 12 or of the first jet and the parallel projection 22 'of the central axis 22 of the second feed , so the direction of the second jet introduced into the mixing chamber 30.
  • the longitudinal axis 16 of the nozzle opening 14 could, however, also extend to a predetermined extent at a different, suitable angle of inclination to this plane.
  • the second feed 20 is widened toward the inlet to the mixing chamber 30.
  • the widening is designed as a sudden widening 27, so that a first section 26 of the second feed 20 with a constant passage cross section suddenly widens to a subsequent further section 28 with a likewise constant but larger passage cross section.
  • Turbulence occurs at the widening 27, which opens at an angle of approximately 60 ° for production reasons, but is ideally designed to be seamless, as a result of which the pulse component of the second beam pointing in the direction of the central axis 22 is reduced.
  • An opening angle of 60 ° is the lower limit.
  • the second jet therefore strikes the flat side of the wide jet with a pronounced turbulent flow profile.
  • the second feed 20 is formed by a circular cylindrical pipe socket 24 with the first section 26 at the connection end, which can be inserted into a feed 21 for treatment agents and has an outer diameter A which is at least 1.5 times, to form a sudden cross-sectional constriction 23. in particular approximately twice the diameter of the first section 26.
  • the described design of the mixing head 1 particularly benefits its use for treating strongly contoured surfaces such as sculptures or figures made of wood, plaster, bronze and the like, which often have strongly jagged and strongly disrupted surfaces, so that the tool used, i.e. the mixing head 1 must be designed in the correspondingly small dimensions, which can certainly be described as miniature. If the two beams hitting each other in the mixing chamber were bundled comparatively strongly, the eccentricity of their respective central axes would scarcely be preventable because of the fact that they missed each other.
  • the opening angle ⁇ of the emerging treatment beam 50 is dimensioned such that the beam impinging on the surface to be treated covers an area of less than five mark piece size, ie less than about 7 cm 2, at the typical working distance.
  • the opening angle ⁇ of the treatment beam 50 is approximately 20 °. In any case, it is less than 30 °.
  • the ideally continuously tapering section 42 is formed with an extension of approximately 5: 1 following the mixing chamber 30.
  • the term stretch is understood to mean the ratio of the length to the diameter of this circular-cylindrical section 42. Good results are achieved with extensions between 4: 1 and 8: 1.
  • the tapered section 42 merges into a further circular-cylindrical section 44 with a constant passage cross section.
  • this last section 44 as it emerged in the course of the development work, the mixing is evened out again and the movements of the jet content which do not take place in the direction of rotation are calmed down.
  • the two sections 42 and 44 are inserted as a one-piece sleeve 40 made of a ceramic material in a receptacle 36 of the mixing chamber housing 32.
  • the tapered section 42 lies on the chamber side Formation of a shoulder 39 on a sintered ring 38 with a sharp edge.
  • the extension of the central axis 22 of the second feed 20 points into or shortly before the area 34 lying between the sintered ring 38 and the mixing chamber wall.
  • the shoulder 39 formed behind the impact area 34 by the sintered ring 38 prevents the impinging jet components from sliding along the chamber wall, thereby the formation of rotation and further - would otherwise be undesirably delayed.
  • a connecting piece 24 forming the second feed 20 with the two sections 26 and 28 has an outer diameter, preferably of half an inch, with a suitable connection area 25 for connection to the common compressed gas sources and hoses.
  • the end face 27 at the free end of the nozzle 24 should be as flat as possible. It therefore extends flat up to the inner diameter of a pushed-on hose 21 and is only chamfered minimally on the outer edge to protect it from damage.
  • the end face 27 also extends as close as possible to the edge of the first section 26, which is designed as a simple bore, in order to ideally result in a sudden narrowing 23 from the cross section of the hose 23 to that of the first section 26.
  • a rounding and even an excessive chamfering of the end face 27 surprisingly exert a not negligible, undesirable influence on the flow profile of the second jet when it is introduced into the mixing chamber 30.
  • the diameter of the first section 26 of the second feed 20 is approximately 6 mm, while the second, widened section 28 has a diameter of approximately 8 mm.
  • the length ratio of these two sections 26 and 28 is approximately 3: 2, the length of the chamber-side section 28 being assumed to be the length of its central axis up to the cut with the mixing chamber wall and the first section 26 having a length of 20 to 40 mm, in particular of about 30 mm.
  • the diameter of the circular-cylindrical mixing chamber 30 in the exemplary embodiment is approximately 10 mm.
  • the substantially rectangular nozzle opening 14 has a length 1 of approximately 1.2 mm and a width d of approximately 0.4 mm.
  • the first jet also fulfills its function with a length 1 of the nozzle opening 14 of 0.8 to 1.8 mm and a width b of 0.2 to 1.2 mm.
  • the nozzle opening 14 is at least 1.5 to at most 4 times as long as it is wide. It is preferably two to three times as long as it is wide.
  • the length 1 of the nozzle opening 14 should not be much less than 1 tenth of the diameter of the mixing chamber 30 as a dimensioning rule, which is to be regarded as the lower limit of the ratio of the mixing chamber diameter and the opening length.
  • the tapering section 42 At its inlet on the mixing chamber side, the tapering section 42 has a diameter of approximately 8 mm, which narrows to approximately 3.5 mm towards the outlet section 44. The diameter decreases at most to a quarter of its value at the inlet on the mixing chamber side.
  • the outlet section 44 itself then has a constant diameter of approximately 3.5 mm. Its outer outlet edge is sharp. If necessary, it is additionally designed to be particularly wear-resistant. All diameters refer to circular cylindrical cross-sectional areas.
  • mixing head described here is used in conjunction with a fine-grained cleaning medium, even sensitive aluminum surfaces can be cleaned mechanically without the use of chemical cleaning agents.
  • the material comes into question, as described in European patent application 0 374 291, namely a mineral blasting material with a hardness (Mohs hardness) of maximum 4 and with a diameter of 0.01 to 1 mm.
  • a particularly suitable material is dolomite.
  • pumice stone flour or a mixture of dolomite with pumice stone flour can also be used.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Nozzles (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Cleaning In General (AREA)
  • Mechanical Treatment Of Semiconductor (AREA)
  • Coating Apparatus (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Detergent Compositions (AREA)
  • Feeding Of Articles By Means Other Than Belts Or Rollers (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
EP93112046A 1992-08-03 1993-07-28 Dispositif et procédé pour le traitement de surfaces sensibles, notamment de sculptures Expired - Lifetime EP0582191B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4225590 1992-08-03
DE4225590A DE4225590C2 (de) 1992-08-03 1992-08-03 Vorrichtung für die Behandlung von empfindlichen Oberflächen, insbesondere von Skulpturen

Publications (2)

Publication Number Publication Date
EP0582191A1 true EP0582191A1 (fr) 1994-02-09
EP0582191B1 EP0582191B1 (fr) 1996-06-19

Family

ID=6464721

Family Applications (1)

Application Number Title Priority Date Filing Date
EP93112046A Expired - Lifetime EP0582191B1 (fr) 1992-08-03 1993-07-28 Dispositif et procédé pour le traitement de surfaces sensibles, notamment de sculptures

Country Status (16)

Country Link
US (1) US5462605A (fr)
EP (1) EP0582191B1 (fr)
JP (1) JPH0655452A (fr)
CN (1) CN1082464A (fr)
AT (1) ATE139472T1 (fr)
AU (1) AU663607B2 (fr)
CA (1) CA2100500A1 (fr)
CZ (1) CZ155893A3 (fr)
DE (2) DE4225590C2 (fr)
HU (1) HU218517B (fr)
IL (1) IL106556A (fr)
NO (1) NO178917C (fr)
NZ (1) NZ248319A (fr)
PL (1) PL299914A1 (fr)
SK (1) SK80393A3 (fr)
ZA (1) ZA932206B (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999043470A1 (fr) * 1998-02-25 1999-09-02 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede et un dispositif de production de jets de particules gazeuses en deux phases contenant en particulier des particules de glace seche de co¿2?
DE10145062B4 (de) * 2001-04-20 2004-10-28 Heinrich Schlick Gmbh Strahlkopf
WO2015101519A1 (fr) * 2014-01-03 2015-07-09 Roland Heinz Fuchs Procédé de traitement de surface d'objets, en particulier en vue de les peindre par la suite
WO2018184798A1 (fr) * 2017-04-04 2018-10-11 Robert Bosch Gmbh Dispositif et procédé de découpage au jet de fluide haute pression

Families Citing this family (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997014760A1 (fr) * 1995-10-17 1997-04-24 Chesapeake Specialty Products Procede de traitement de materiaux contenant du fer et produits ainsi obtenus
US5846338A (en) * 1996-01-11 1998-12-08 Asyst Technologies, Inc. Method for dry cleaning clean room containers
US5693369A (en) * 1996-01-16 1997-12-02 Russell; Rosemarie M. Process for finishing a bronze sculpture
JP3315611B2 (ja) * 1996-12-02 2002-08-19 三菱電機株式会社 洗浄用２流体ジェットノズル及び洗浄装置ならびに半導体装置
US6454871B1 (en) * 1997-06-23 2002-09-24 Princeton Trade & Technology, Inc. Method of cleaning passageways using a mixed phase flow of gas and a liquid
US6027572A (en) * 1997-06-23 2000-02-22 Princeton Trade And Technologt, Inc Cleaning method for removing biofilm and debris from lines and tubing
US6105880A (en) * 1998-01-16 2000-08-22 The Sherwin-Williams Company Mixing block for mixing multi-component reactive material coating systems and an apparatus using same
DE19804233A1 (de) * 1998-02-04 1999-08-12 Kaercher Gmbh & Co Alfred Strahlmittel-Injektorpistole
US6147149A (en) * 1999-03-03 2000-11-14 Glouster Co., Inc. Adhesive caulking material which can mimic the appearance of a multicolored stone surface
US6280302B1 (en) * 1999-03-24 2001-08-28 Flow International Corporation Method and apparatus for fluid jet formation
JP3410385B2 (ja) * 1999-04-19 2003-05-26 株式会社ディスコ 洗浄装置及び切削装置
KR100419299B1 (ko) * 2001-02-28 2004-02-19 (주)케이.씨.텍 표면 세정을 위한 승화성 고체 입자 분사용 노즐
CN1871408B (zh) * 2003-10-21 2010-11-24 国际壳牌研究有限公司 喷嘴单元以及用于在目标物中挖孔的方法
US7371342B2 (en) * 2004-05-06 2008-05-13 Corporation Nacional Del Cobre De Chile Method for unlocking nozzles of reactors
CN100393431C (zh) * 2005-01-31 2008-06-11 田永茂 除尘器
US20080230100A1 (en) * 2007-02-22 2008-09-25 Patterson Daniel R Nozzle assembly
CN101817165A (zh) * 2010-04-06 2010-09-01 北京航空航天大学 基于微细冰水混合介质的低温冷风射流绿色切削方法
JP5746901B2 (ja) * 2011-04-14 2015-07-08 株式会社不二製作所 研磨方法及びブラスト加工装置のノズル構造
CN104190583A (zh) * 2014-08-25 2014-12-10 青海盐湖工业股份有限公司 用于废硫酸处理的雾化器
CN104759359A (zh) * 2015-04-02 2015-07-08 周玉红 一种脉冲袋式集尘机内腔吹洗喷嘴
DE112017001606T5 (de) * 2016-03-31 2018-12-13 Denso Corporation Reinigungsvorrichtung für einen bordseitigen optischen Sensor
CN106425889A (zh) * 2016-12-15 2017-02-22 贾跃民 新型的高压含沙水射流喷嘴总成
CN109015390B (zh) * 2017-06-12 2021-02-26 孙洪孟 冰射流清洗设备
CN113318254B (zh) * 2021-06-15 2023-08-22 苏州艾贝欧生物科技有限公司 过氧化氢冲击汽化消毒器
CN117597198A (zh) * 2021-07-06 2024-02-23 Dlh鲍尔斯公司 脉冲式喷射清洁喷嘴组件和方法

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2605596A (en) * 1949-11-10 1952-08-05 William C Uhri Method of cleaning surfaces
EP0090691A1 (fr) * 1982-03-15 1983-10-05 Commissariat A L'energie Atomique Buse de sablage à jet plat et contenant des particules solides abrasives
EP0110529A2 (fr) * 1982-10-22 1984-06-13 Flow Industries Inc. Jet abrasif liquide à haute vitesse
GB2159069A (en) * 1984-05-17 1985-11-27 John Link Blasting nozzle
EP0171448A1 (fr) * 1984-08-14 1986-02-19 Johann Szücs Dispositif et procédé pour le nettoyage de surfaces métalliques et en pierre
DE3622292A1 (de) * 1985-07-17 1987-01-29 Diesel Rudolf Ing Schule Sandstrahlduese
EP0437168A2 (fr) * 1990-01-10 1991-07-17 Possis Corporation Tête de coupe pour machine de découpe au jet d'eau
DE4002787A1 (de) * 1990-01-31 1991-08-01 Eichbauer Fritz Vorrichtung zum reinigen von oberflaechen

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2083851A (en) * 1935-10-08 1937-06-15 Frank E Marcy Spraying nozzle
US3881656A (en) * 1974-02-15 1975-05-06 Universal Oil Prod Co Mixing apparatus
AU514743B2 (en) * 1977-03-18 1981-02-26 Charles R. Gardner Valve assembly and spraying apparatus therefor
US4328107A (en) * 1980-11-28 1982-05-04 Synergo, Inc. Process and apparatus for forming dispersions
US4562366A (en) * 1981-12-31 1985-12-31 Andrew Zaderej In-line solid state time delay device
DE3204861A1 (de) * 1982-02-11 1983-08-25 Johan 8000 München Szücs Verfahren und vorrichtung zum reinigen von fassaden oder dgl.
DE3419348A1 (de) * 1984-05-24 1985-11-28 Inter-Unitek GmbH, 8032 Gräfelfing Vorrichtung zur befestigung einer kieferregulierungsapparatur
DE8606183U1 (de) * 1986-03-06 1986-06-12 Bauer, Josef, 21224 Rosengarten Naßstrahlvorrichtung
US4815241A (en) * 1986-11-24 1989-03-28 Whitemetal Inc. Wet jet blast nozzle

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2605596A (en) * 1949-11-10 1952-08-05 William C Uhri Method of cleaning surfaces
EP0090691A1 (fr) * 1982-03-15 1983-10-05 Commissariat A L'energie Atomique Buse de sablage à jet plat et contenant des particules solides abrasives
EP0110529A2 (fr) * 1982-10-22 1984-06-13 Flow Industries Inc. Jet abrasif liquide à haute vitesse
GB2159069A (en) * 1984-05-17 1985-11-27 John Link Blasting nozzle
EP0171448A1 (fr) * 1984-08-14 1986-02-19 Johann Szücs Dispositif et procédé pour le nettoyage de surfaces métalliques et en pierre
DE3622292A1 (de) * 1985-07-17 1987-01-29 Diesel Rudolf Ing Schule Sandstrahlduese
EP0437168A2 (fr) * 1990-01-10 1991-07-17 Possis Corporation Tête de coupe pour machine de découpe au jet d'eau
DE4002787A1 (de) * 1990-01-31 1991-08-01 Eichbauer Fritz Vorrichtung zum reinigen von oberflaechen

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999043470A1 (fr) * 1998-02-25 1999-09-02 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procede et un dispositif de production de jets de particules gazeuses en deux phases contenant en particulier des particules de glace seche de co¿2?
US6695686B1 (en) 1998-02-25 2004-02-24 L'air Liquide Societe Anonyme A Directoire Et Conseil De Surveillance Pour L'etude Et L'exploitation Des Procedes Georges Claude Method and device for generating a two-phase gas-particle jet, in particular containing CO2 dry ice particles
DE10145062B4 (de) * 2001-04-20 2004-10-28 Heinrich Schlick Gmbh Strahlkopf
WO2015101519A1 (fr) * 2014-01-03 2015-07-09 Roland Heinz Fuchs Procédé de traitement de surface d'objets, en particulier en vue de les peindre par la suite
WO2018184798A1 (fr) * 2017-04-04 2018-10-11 Robert Bosch Gmbh Dispositif et procédé de découpage au jet de fluide haute pression

Also Published As

Publication number Publication date
CN1082464A (zh) 1994-02-23
NZ248319A (en) 1996-02-27
DE59302994D1 (de) 1996-07-25
AU663607B2 (en) 1995-10-12
HUT75614A (en) 1997-05-28
NO932726D0 (no) 1993-07-29
PL299914A1 (en) 1994-02-07
IL106556A (en) 1995-06-29
HU9301993D0 (en) 1993-09-28
ZA932206B (en) 1993-10-13
US5462605A (en) 1995-10-31
CA2100500A1 (fr) 1994-02-04
IL106556A0 (en) 1993-12-08
JPH0655452A (ja) 1994-03-01
EP0582191B1 (fr) 1996-06-19
ATE139472T1 (de) 1996-07-15
DE4225590C2 (de) 1995-04-27
AU4440893A (en) 1994-02-10
NO178917C (no) 1996-07-03
DE4225590A1 (de) 1994-02-17
CZ155893A3 (en) 1994-04-13
HU218517B (hu) 2000-09-28
NO932726L (no) 1994-02-04
SK80393A3 (en) 1994-03-09
NO178917B (no) 1996-03-25

Similar Documents

Publication Publication Date Title
EP0582191B1 (fr) Dispositif et procédé pour le traitement de surfaces sensibles, notamment de sculptures
EP0171448B1 (fr) Dispositif et procédé pour le nettoyage de surfaces métalliques et en pierre
DE69908097T2 (de) Verfahren und vorrichtung zum erzeugen eines zweiphasigen gasteilchen-strahls, der im besonderen co2 trockeneisteilchen enthält
EP2877806B1 (fr) Procédé et dispositif destinés à nettoyer des surfaces d'un échangeur de chaleur à ailettes
DE2422597B2 (de) Spritzvorrichtung zum hydrostatischen Zerstäuben von Farbe und anderen flüssigen Stoffen
DE3527923C2 (fr)
EP0691183A1 (fr) Buse à jet utilisée dans des dispositifs pour le nettoyage notamment des surfaces de pierre et/ou métalliques
EP0375887B1 (fr) Méthode et dispositif pour le coupage et le nettoyage d'objets, ainsi que l'enlèvement de matériau par un mélange d'eau et de particules abrasives
DE3516103A1 (de) Mischkopf zum einbringen von abrasiven partikeln in einen hochdruckwasserstrahl
EP1765551B1 (fr) Dispositif pour generer un jet de particules de neige carbonique
EP2537484B1 (fr) Dispositif de mélange pour un pulvérisateur de poudre dentaire
DE4002787C2 (fr)
EP0509132A1 (fr) Méthode et dispositif pour le nettoyage de surfaces, en particulier de surfaces délicates
DE102004023246B3 (de) Strahlverfahren
DE3916446A1 (de) Verfahren und vorrichtung zur bearbeitung von festen stoffen mittels druckwasserstrahl
EP1842598B1 (fr) Buse d'éjection d'un agent de grenaillage
DE69902082T2 (de) Vorrichtung zur Reinigung von kontaminierten Oberflächen mit Hilfe eines Strahls, der aus Luft, feinkörnigem Strahlmittel und einer Flüssigkeit zusammengesetzt ist
DE3309742C2 (fr)
WO2003022525A2 (fr) Procede et dispositif de decapage
DE4312994C2 (de) Vorrichtung zur Verspritzung von Suspensionen, insbesondere Mörteln
DE69400060T2 (de) Flachstrahldüse, insbesondere für Hochdruckreiniger
DD220770A3 (de) Vorrichtung zum druckluftstrahlen
DE69011357T2 (de) Schneidverfahren und Vorrichtung.
DE69409542T2 (de) Düse zur oberflächenbehandlung sowie vorrichtung und verfahren zur oberflächenbehandlung mit einer solchen düse
DE20315998U1 (de) Vorrichtung zur Erzeugung eines rotierenden Fluidstrahls

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LI LU MC NL PT SE

17P Request for examination filed

Effective date: 19940321

17Q First examination report despatched

Effective date: 19950406

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LI LU MC NL PT SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19960619

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRE;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.SCRIBED TIME-LIMIT

Effective date: 19960619

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19960619

Ref country code: GB

Effective date: 19960619

Ref country code: FR

Effective date: 19960619

Ref country code: ES

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 19960619

Ref country code: DK

Effective date: 19960619

REF Corresponds to:

Ref document number: 139472

Country of ref document: AT

Date of ref document: 19960715

Kind code of ref document: T

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: 68797

REF Corresponds to:

Ref document number: 59302994

Country of ref document: DE

Date of ref document: 19960725

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19960731

Ref country code: BE

Effective date: 19960731

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19960919

Ref country code: PT

Effective date: 19960919

EN Fr: translation not filed
NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
GBV Gb: ep patent (uk) treated as always having been void in accordance with gb section 77(7)/1977 [no translation filed]

Effective date: 19960619

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Effective date: 19970131

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: DR. CONRAD A. RIEDERER PATENTANWALT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19970722

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IE

Payment date: 19970725

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19970730

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19970919

Year of fee payment: 5

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980728

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980728

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980731

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980731

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990501