EP1890823A1 - Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation - Google Patents

Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation

Info

Publication number
EP1890823A1
EP1890823A1 EP06753495A EP06753495A EP1890823A1 EP 1890823 A1 EP1890823 A1 EP 1890823A1 EP 06753495 A EP06753495 A EP 06753495A EP 06753495 A EP06753495 A EP 06753495A EP 1890823 A1 EP1890823 A1 EP 1890823A1
Authority
EP
European Patent Office
Prior art keywords
cleaning
liquid
fluid
compressed gas
mixing chamber
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
EP06753495A
Other languages
German (de)
English (en)
Other versions
EP1890823B1 (fr
Inventor
Dieter Wurz
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
Priority claimed from DE102005021650A external-priority patent/DE102005021650A1/de
Priority claimed from DE200510037991 external-priority patent/DE102005037991A1/de
Application filed by Individual filed Critical Individual
Priority to SI200631692T priority Critical patent/SI1890823T1/sl
Priority to PL06753495T priority patent/PL1890823T3/pl
Publication of EP1890823A1 publication Critical patent/EP1890823A1/fr
Application granted granted Critical
Publication of EP1890823B1 publication Critical patent/EP1890823B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02—Spray pistols; Apparatus for discharge
    • B05B7/04—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
    • B05B7/0416—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid
    • B05B7/0441—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid with one inner conduit of liquid surrounded by an external conduit of gas upstream the mixing chamber
    • B05B7/0458—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid with one inner conduit of liquid surrounded by an external conduit of gas upstream the mixing chamber the gas and liquid flows being perpendicular just upstream the mixing chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/02—Spray pistols; Apparatus for discharge
    • B05B7/04—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge
    • B05B7/0416—Spray pistols; Apparatus for discharge with arrangements for mixing liquids or other fluent materials before discharge with arrangements for mixing one gas and one liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/24—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device
    • B05B7/2489—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device an atomising fluid, e.g. a gas, being supplied to the discharge device
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
    • B05B7/24—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device
    • B05B7/2489—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device an atomising fluid, e.g. a gas, being supplied to the discharge device
    • B05B7/2491—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas with means, e.g. a container, for supplying liquid or other fluent material to a discharge device an atomising fluid, e.g. a gas, being supplied to the discharge device characterised by the means for producing or supplying the atomising fluid, e.g. air hoses, air pumps, gas containers, compressors, fans, ventilators, their drives

Definitions

  • the invention relates to a spray nozzle with an outlet or mixing chamber and at least two through holes opening into the outlet or mixing chamber, wherein the through holes are each connected to a fluid line.
  • the invention also relates to a spray arrangement with a spray nozzle according to the invention and to a method for operating a spray nozzle according to the invention and a spray arrangement according to the invention.
  • spray nozzles with an outlet or mixing chamber and at least two through holes opening into the outlet or mixing chamber, which are each connected to a fluid line, are used, in particular so-called two-substance nozzles.
  • a disadvantage of these two-component nozzles is the tendency to solid deposits, in particular in the Zu Kunststoffbohrungen.
  • the safe operation of two-fluid nozzles requires in many cases a frequent expansion of the nozzle lances on which the spray nozzles are arranged. Only in this way are nozzles according to the prior art accessible for cleaning work.
  • nozzles which allow a very fine atomization of the liquid.
  • two-fluid nozzles are also increasingly being used.
  • the liquid is finely atomized at moderate pressures with the aid of a compressed gas, for example compressed air or steam.
  • a compressed gas for example compressed air or steam.
  • two-fluid nozzles occur relatively frequently malfunctions due to deposits in the through holes to the outlet or mixing chamber. Affected are bottlenecks of a liquid supply to the mixing chamber, but in particular also the most radially arranged holes for the compressed air introduction into the mixing chamber. This forces frequent removal of the nozzle lances and cleaning of the nozzles.
  • a spray nozzle is provided with an outlet or mixing chamber and at least two opening into the outlet or mixing through holes, the through holes are each connected to a fluid line, wherein at least one of the through holes is self-cleaning and / or devices for cleaning at least one of the passage holes are provided.
  • the formation of deposits on the through-holes is prevented by the fact that they are either self-cleaning or additional devices are provided for cleaning at least one of the through-holes.
  • the self-cleaning takes place during a spraying operation and the devices for cleaning remove any depositing ments in the through-holes during the spraying operation or a cleaning operation.
  • At least one of the through-bores has a rounded, tapering cross-section on its side facing away from the outlet or mixing chamber such that a fluid flow passes through the through-bore to the mouth into the mixing chamber without flow separation.
  • the through hole is rounded jet-shaped on its side facing away from the mixing chamber.
  • At least one of the fluid lines is formed as a liquid feed line to the mixing chamber and in the region of at least one through hole formed as a liquid inlet bore, a movable plunger for cleaning the liquid inlet bore is provided.
  • Such a plunger can reliably ensure that any deposits are loosened and removed again.
  • the plunger can be moved, for example magnetostrictive or by hydraulic means. - A -
  • the plunger is arranged upstream of the liquid inlet bore and formed at its, the liquid inlet bore facing the end of a conical or frusto-conical shape.
  • the plunger in the supply line to the liquid inlet bore is arranged with its longitudinal direction parallel to the flow direction and is tapered at both ends.
  • the plunger can be made streamlined and the flow resistance caused by the plunger in the liquid supply line can be kept low.
  • the conical or frusto-conical end of the plunger is adapted to an inlet region of the liquid inlet bore that tapers in the flow direction.
  • one of the fluid lines is designed as a liquid supply line and means are provided to impart pressure surges to the liquid present in the liquid supply line.
  • pressure surges can be used to clean the through holes. It is advantageous that no mechanical devices must be introduced into the through hole and that the pressure surges can also be impressed during the spraying operation.
  • pressure surges are impressed with frequencies in the ultrasonic range. In this way, any deposits can be smashed and discharged through the mixing chamber of the nozzle. In a sense, the resulting To compare cleaning effect with the ultrasonic destruction of kidney stones.
  • one of the fluid lines is designed as a compressed gas supply line to a mixing chamber and upstream of the pressure gas inlet bore formed at least one through hole means for introducing abrasive dusts are provided in the compressed gas supply line.
  • Deposits can be removed erosively by means of abrasive dusts.
  • the hardness of the abrasive fine dust should be much lower than the hardness of the nozzle material.
  • one of the fluid lines is designed as a compressed gas supply line to a mixing chamber and upstream of the pressure gas inlet bore designed as at least one through-hole means for introducing cleaning liquid are provided in the compressed gas supply line.
  • Such a cleaning liquid may, for example, be demineralized water and the compressed gas is subjected to a mist of mist of the cleaning liquid. It may be helpful to apply chemicals to the cleaning fluid to assist the solution process with the deposits in the through-holes. It is not necessary to dope the atomizing air continuously with cleaning liquid, but in many cases, an intermittent loading may be sufficient. If appropriate, a separate atomization chamber can be provided in order to separate the cleaning liquid into small droplets before it is introduced into the compressed gas feed line.
  • one of the fluid lines is designed as a compressed gas supply line to a mixing chamber and upstream of the Compressed gas inlet bore formed at least one through hole means for introducing sponge or foam-like particles are provided in the compressed gas supply line, which can be pressed under the pressure of the supplied compressed gas through the at least one pressure gas inlet bore.
  • one of the fluid lines is designed as a compressed gas supply line to a mixing chamber and upstream of the pressure gas inlet bore designed as at least one through hole means for introducing steam into the compressed gas supply line are provided.
  • one of the fluid lines is designed as a fluid supply line and the through bore formed as a fluid inlet bore has a constriction, wherein a ratio of length to diameter of the constriction is greater than 1, in particular greater than 1.5.
  • Deposits in the liquid inlet bore may cause a liquid jet entering the mixing chamber to be deflected laterally. Due to the corresponding dimensioning of the constriction, the liquid jet is introduced into the mixing chamber largely centrically symmetrically even if deposits in the form of covering tiles have accumulated in front of the constriction.
  • one of the fluid lines is designed as a liquid feed line to a mixing chamber and one of the fluid lines as a compressed gas feed line to the mixing chamber, wherein the pressure gas inlet surrounds the mixing chamber at least in sections annularly and a plurality of through-holes formed as compressed gas inlet bores with respect to a central axis of the spray nozzle radially Mixing chamber are arranged.
  • the problem underlying the invention is also solved by a method for operating a spray nozzle according to the invention, in which the step of introducing a cleaning fluid or cleaning particles is provided in a formed as compressed gas inlet fluid line upstream of at least one formed as a pressure gas inlet bore through hole in the mixing chamber.
  • any deposits formed in the through holes of the spray nozzle can be reliably removed and discharged, for example, together with the spray.
  • water vapor, chemically acting cleaning fluid or abrasive fine dust can be introduced upstream of the at least one compressed gas inlet bore.
  • the introduction of spongy or foam-like cleaning particles upstream of the at least one compressed gas inlet bore is possible, which are then pressed under the pressure of the compressed gas through the pressure gas inlet holes into the mixing chamber.
  • it is provided to impart pressure surges to the liquid to be atomized in the fluid line formed as a liquid feed upstream of the at least one through-bore formed as a liquid inlet bore into the mixing chamber.
  • pressure surges impurities or deposits in the through holes can also be reliably solved.
  • pressure surges with frequencies in the ultrasonic range can be impressed in order to smash deposits in the through holes or other parts of the nozzle.
  • a spray arrangement with a spray nozzle according to the invention are provided in the means to effect in a cleaning operation in at least one of the fluid lines and the associated through-hole fluid flow from the mixing or discharge chamber into the fluid line.
  • the fluid to be sprayed can be, for example, a liquid or a liquid solid suspension.
  • the spray assembly according to the invention can be used with two-fluid nozzles or so-called single-fluid return nozzles, in which a part of the fluid flowing into the outlet chamber does not exit from the nozzle but is returned to a return line. In extreme cases, the amount of return is equal to the feed amount in single-material return nozzles, so that no fluid is injected into a gas space. This effect can be used for a cleaning operation.
  • a flow direction which is opposite to the spraying operation is set in the cleaning mode between the mixing chamber and the liquid feed line or an optionally upstream filter.
  • the fluid lines have a compressed gas supply line to the mixing chamber and a liquid supply to the mixing chamber and the means for reversing the flow direction cause in the cleaning operation, a fluid flow from the mixing chamber through the liquid inlet bore and into the liquid keitszutechnisch into it.
  • the liquid inlet bore can be reliably cleaned in a cleaning operation.
  • a fluid line formed as a fluid supply line has at least one shut-off valve and at least one cleaning valve located downstream of the shut-off valve in the liquid supply direction.
  • the fluid flow flowing in the opposite direction relative to the spraying operation can be discharged through the cleaning valve, so that any soiling or deposits can be discharged from the spraying arrangement.
  • a vacuum source is provided, which is connectable by means of the cleaning valve to the liquid supply line.
  • the backflow in the liquid supply line can be increased, but it can also be prevented by applying a correspondingly high negative pressure, for example, that in the cleaning Liquid or compressed gas escapes from the outlet of the nozzle into the process environment.
  • a Abschlämm disposer is provided, which is connectable by means of the cleaning valve to the liquid supply line.
  • a filter device which is serially connected in the liquid supply line and which is provided upstream and downstream of a filter insert, each with a filter chamber, wherein both Filterkammem are connected by means of a respective cleaning valve with a Abschlämm effet.
  • a filter device can be cleaned in the cleaning operation in reverse flow direction.
  • the dissolved deposits will collect in the downstream in the spraying operation filter chamber.
  • contaminants from the supplied liquid to be sprayed will accumulate in the upstream filter chamber.
  • both filter chambers can then be emptied and connected via the drain line, for example, to a blowdown container.
  • one of the fluid lines is designed as a pressurized gas supply line and there are provided means for introducing a cleaning liquid into the compressed gas supply line.
  • a collecting container for cleaning liquid and means for conveying the cleaning liquid from the collecting container are provided in the compressed gas supply line.
  • the cleaning liquid can be circulated in the spray arrangement according to the invention, for example, until its cleaning effect is exhausted. In this way, a very economical operation of the spray arrangement according to the invention is possible.
  • means are provided for admixing the cleaning liquid from the collecting container during the spraying operation into the liquid supply line.
  • an effluent-free operation of the spray arrangement according to the invention can be achieved, since cleaning liquid used for the cleaning operation is first collected in the collecting container and then added again during the spraying operation in the liquid to be sprayed.
  • the admixing can take place in such a way that the cleaning liquid is discharged from the spray nozzle in the spray mode until it is ineffective.
  • an already existing Abschlämm constituer can be used as a collecting container.
  • the problem underlying the invention is also solved by a method for operating a spray arrangement according to the invention, in which the step of reversing a direction of fluid flow in a cleaning operation with respect to a spraying operation is provided at least in a region of the mouth of one of the fluid lines in the mixing or outlet chamber.
  • a fluid line of the spray nozzle is in the form of a fluid supply line which opens into the mixing chamber and another fluid line.
  • the cleaning fluid flow traverses the mixing chamber in the opposite direction to the spraying operation, so that blockages or soiling of through-bores can be removed.
  • the cleaning fluid may be compressed gas used during the spraying operation.
  • a negative pressure can be applied to the cleaning valve during the cleaning operation.
  • the flow reversal can be assisted during the cleaning operation, and it can also be prevented during the cleaning operation, cleaning fluid exiting the spray nozzle.
  • the cleaning fluid is a mixture of compressed gas and cleaning fluid.
  • the cleaning fluid may consist solely of cleaning fluid.
  • ambient gas can be sucked through a nozzle outlet opening, so that the cleaning fluid contains ambient gas.
  • flue gas can be sucked in, if it is to be assumed that the properties of the flue gas from the process environment do not impair the dissolution of deposits.
  • it is provided to circulate the cleaning fluid from the cleaning valve to the compressed gas line through the mixing chamber and the liquid feed line again to the cleaning valve.
  • the cleaning fluid can be used several times.
  • the cleaning fluid can then be collected during the cleaning operation in a collecting container and, in order to achieve an effluent-free operation, be admixed again during the spraying operation from the collecting container into the liquid feed line.
  • FIG. 1 is a sectional view of a two-fluid nozzle according to the prior
  • Fig. 2 is a partial enlargement of the sectional view of
  • FIG. 3 is a further enlarged detail of the sectional view of FIG. 1,
  • FIG. 4 shows a two-fluid nozzle according to the invention according to a first embodiment of the invention
  • FIG. 5 is a sectional view of a two-fluid nozzle according to the invention measured GE a second embodiment
  • Fig. 6 is a partial enlargement of the sectional view of Fig. 5 and Fig. 7 is a schematic view of a spray arrangement according to the invention.
  • Fig. 1 shows a schematic sectional view of the structure of a known two-fluid nozzle according to the prior art.
  • a liquid to be atomized 1 is supplied via a tube 2 of the largely centrally symmetrical two-fluid nozzle 3, while compressed gas 17 is blown through bores 5 from an outer annular space 6 in a mixing chamber 7.
  • the supply pipe 2 is guided for the liquid inside the tube 4 for the supply of the compressed gas.
  • this is by no means mandatory.
  • Via a nozzle orifice 8 Via a nozzle orifice 8, a two-substance mixture 9 of atomizing gas and drops leaves the mixing chamber 7 at a relatively high speed.
  • the sputtering gas in most cases consists of compressed air, air is used for simplification.
  • the through holes 5 are designed for compressed gas at the transition from an annular chamber 6 to the mixing chamber 7 sharp.
  • the air flow at an entry edge 12 of the through-bores 5 forms detachment regions 13, which can extend as far as the mixing chamber 7.
  • this annular Ablinate (1) 13 the liquid to be atomized back flow against the flow direction of the air, as indicated by arrows 14, and here forms drying deposits 11, which are already shown in Fig. 2. These deposits 11 reduce the air flow and force regular cleaning of the nozzles.
  • a constriction 10 which is shown in Figs. 1 and 2.
  • Deposits 15 can also occur here, in particular of platelets which have detached from wall deposits in the liquid supply lines. These platelets 15 preferably collect at a constriction, for example frustoconical constriction, at the transition from the inner diameter of the liquid feed line to the constriction 10.
  • FIG. 4 shows a first embodiment of a two-substance nozzle 60 according to the invention.
  • the through bores 5 are compressed gas or compressed air on the side of the compressed gas supply line, which here forms an annular chamber surrounding the mixing chamber 7 in sections a rounding 16 provided.
  • the leading edge 12 is thus not sharp-edged but rounded off, so that the cross-section of the through-holes 5 for the compressed gas feed line into the mixing chamber 7 starts from the mixing chamber 7.
  • This rounding 16 causes the air flow does not detach from the bore wall. Instead, a wall shear stress generated by the air flow acts continuously on the bore wall in the direction of the mixing chamber 7 in the through-holes 5, which are now formed like a nozzle. This wall shear stress hinders a backflow of liquid from the mixing chamber 7 into the through-holes 5, so that the formation of deposits is largely prevented by the drying residue of the evaporation of the liquid.
  • the two-substance nozzle 60 is designed to be axisymmetric with respect to a central axis 61.
  • a liquid feed line 62 is guided centrally through a nozzle body and leads to a frusto-conical taper 63 and the cylindrical constriction 10 in the mixing chamber 7.
  • To be sprayed liquid from the liquid feed line 62 thus shoots centrally into the mixing chamber 7 a.
  • a tapered constriction 64 adjoins the mixing chamber 7, which then merges again into an outlet funnel 65 that widen in the manner of a truncated cone.
  • the pressure gas supply line 4 is formed as an annular channel and surrounds the liquid supply line 62 and in its further course then in sections the mixing chamber 7.
  • a plurality of through holes 5 are arranged radially through which, as already stated, compressed gas from the Compressed gas supply line 4 passes into the mixing chamber.
  • the incoming liquid jet is intimately mixed with the likewise entering compressed gas, so that emerges from the outlet funnel 65, a spray with a fine droplet spectrum.
  • Bellows may also form in the radial through-holes 5 during transient atomization processes due to temporary backflow into the through-holes 5 for supplying air.
  • FIGS. 1 to 3 and having the sharp entry edges 12 deposits are even detected in the annular chamber 6, which should actually only be traversed by air.
  • the cleaning liquid 21 is introduced via a nozzle 66 shown in Fig. 4 in the compressed gas supply line 4 upstream of the through holes 5.
  • the cleaning liquid 21 can be introduced into the compressed gas feed line 4 near the mixing chamber 7.
  • the pressurization of the compressed gas, for example air, with a droplet mist of cleaning fluid 21 can also be made at a greater distance from the mixing chamber 7.
  • the cleaning liquid 21 is pressed by the atomizing air in the compressed gas supply line 4 at high speed through the usually, but by no means compelling, radially arranged through bores 5, which are thus kept clear of coverings.
  • the steam nozzle 68 may also be arranged in the annular compressed gas supply line 4.
  • the steam nozzle 68 may also be arranged in the annular compressed gas supply line 4.
  • a further possibility is indicated of removing coating leaflets in the region in front of the constriction 10 of the liquid inlet bore into the mixing chamber 7.
  • a flutter valve 69 in the liquid supply line 62 is schematically indicated in the illustration of FIG. 4, which can be switched on.
  • the flutter valve 69 it is possible to impart pressure surges to the liquid to be atomized in the liquid feed line 62, which causes a disintegration of the linings or lining plates, in particular in the region of the taper 63 and the constriction 10 of the liquid inlet bore into the mixing chamber 7. In certain This is similar to the ultrasonic fragmentation of kidney stones.
  • flutter valve 69 it is also possible, for example, to use an ultrasound transmitter with a suitable ultrasound transducer which imparts pressure surges in the ultrasound range and thereby ensures a cleaning of the fluid supply line 62 and in particular the taper 63 and the constriction 10.
  • a further embodiment of a two-substance nozzle 70 according to the invention is shown in the schematic sectional view of FIG. 5.
  • the two-fluid nozzle 70 has in many parts an identical structure to the two-fluid nozzle 60 of FIG. 4, so that only the two-fluid nozzle 60 of FIG. 4 different elements are explained in detail.
  • the atomizing air in the compressed gas supply line 4 can be charged with small foam beads 72, as shown schematically in FIG. These are introduced into the compressed gas supply line 4 and then pressed alternately by stochastic laws through the various through holes 5. As a result, the radial through bores 5 can be kept free from deposits.
  • a comparable method has hitherto been used exclusively for the cleaning of long condenser tubes.
  • the introduction of the foam beads 72 can be used with or without additional doping with a cleaning liquid 21.
  • the atomizing air can be acted upon with abrasive fine dust 74, which then also leads in the through-holes 5 to an erosive detachment of the pads.
  • abrasive fine dust 74 is shown schematically in the illustration of FIG.
  • the hardness of the abrasive fine dust 74 should be much lower than the hardness of the nozzle material, so that in fact only the pads and not the bore walls are removed.
  • a cleaning mechanism is also provided for the fluid inlet bore 76.
  • a plunger 20 which is shown schematically in Fig. 5 and which can be moved, for example, magnetostrictive or by hydraulic means along the direction indicated in Fig. 5 double arrow.
  • the plunger 20 has a nikzylindri- see basic body and tapers conically at its two ends.
  • the plunger 20 is arranged with its longitudinal axis parallel to the flow direction and concentric with the central axis 71 of the nozzle 70.
  • the cone-shaped taper of the plunger 20 facing the mixing chamber 7 in the flow direction is adapted to the taper 73 of the liquid inlet bore 76. In this way, the plunger 20 comes in the region of the taper 73 flat to the plant and can thereby smash any existing plaque there.
  • the tapered at both ends of the embodiment of the plunger 20 and its arrangement with its longitudinal axis parallel to the flow direction leads to a low flow resistance and thus to a low pressure drop in the liquid supply line 2.
  • the plunger 20 is movably disposed within a plunger chamber 75, which compared to the liquid supply 2 has an expanded cross-section and in FIG Seen flow direction to the mixing chamber through the taper 73 and the throat 10 of the liquid inlet bore 76 is limited.
  • FIG. 5 shows a section of the two-substance nozzle 70 according to the invention.
  • platelike deposits 15 can be seen, which have settled in the region of the taper 73 in front of the constriction 10.
  • These deposits are typically not formed on the liquid inlet bore 76, unlike the deposits formed on the air passage bore 5 itself, but represent a mostly overwhelming percentage of scaling of debris present in the extensive fluid supply piping system as well as in the prior art the nozzle lance itself have arisen.
  • Such deposits in the form of leaves can detach from the walls. They are then entrained by the liquid flow and lead with appropriate dimensions of the liquid inlet bore 76 and in particular at the bottleneck 10 for laying the cross section through the leaflets 15.
  • FIG. 7 shows a spray arrangement 80 according to the invention in accordance with a preferred embodiment.
  • two-fluid nozzles were often used to evaporate the suspension, which is produced in wet flue gas cleaning systems.
  • the flue gas cleaning is increasingly carried out even in such, equipped with two-fluid nozzles apparatus.
  • the liquid 1 to be sprayed must be enriched with a sorbent, for example with lime milk, in order to effect the incorporation of the acid formers, such as sulfur dioxide and hydrogen chloride.
  • a lime milk concentration of, for example, 10%, which is advantageous for the flue gas purification process, the risk of contamination for the pipelines and for the nozzle lances and nozzles is considerably increased, so that deposits can occur.
  • cross-section linings occur through platelet-shaped shutters from the supply line to the nozzle lance and from the nozzle lance itself.
  • the formwork from the supply lines to the nozzle lances can be eliminated in a known manner with the aid of a coarse filter.
  • the mesh size of this filter must be smaller than the narrowest cross-section at the liquid inlet into the mixing chamber.
  • the areas of the nozzle lance and the nozzle which are subject to coating can be intermittently cleaned without the nozzle lance having to be removed for this purpose.
  • This is inventively achieved by reversing the flow direction in the liquid supply to the nozzle, connected to the backwashing of loose deposits to a arranged in the supply line to the nozzle lance particle.
  • This cleaning process can still be improved by chemically effective cleaning fluids.
  • connection flanges 118 for the liquid to be atomized and with connection flanges 119 for compressed gas, which effects the atomization.
  • a double-acting, coarse mesh filter 120 is installed in the liquid supply line 125 .
  • the liquid supply to the nozzle lance 117 can be regulated or interrupted.
  • the cleaning valves 122, 123 and a drain valve 124 can be opened to the blowdown container 126.
  • the Abschlämm constituteer can be brought to negative pressure.
  • Abschlämm hereer 126 solids or thick sludge 134 and Abschlämmfactkeit 132 are collected.
  • the thick sludge 134 can be discharged via a discharge valve 135, it is possible to recirculate the blow-off liquid 132 with the cleaning additives contained, ie the cleaning liquid used, via a line 133.
  • the AbschlämmAvemkeit 132 which contains a large proportion of used cleaning liquid, conveyed into a storage tank and thus be used again for cleaning purposes.
  • the blowdown container 126 can be used as the central unit for receiving the slurry and the cleaning liquid become. This is indicated by the supply lines with the reference numerals 129, 130 and 131.
  • the compressed gas 115 for the atomization of the liquid is supplied from the compressor 136 and via the pressure gas main valve 137 in the
  • Compressed gas feed 138 fed.
  • the feed of the cleaning liquids 140 and 141 which are stored in the containers 142 and 143.
  • Cleaning fluids in the compressed gas the pressure in the feeders 142 and 143 must be slightly higher than that of the compressed gas. Therefore, a pressurized gas supply 148 of the container via the valves 144 and 145 is provided. Cleaning fluid can optionally on the
  • Valves 146 and 147 are fed into the compressed gas line 138.
  • blow-off liquid 132 can be recirculated and is then pumped by the pump 154 into one of the containers 142, 143, for example.
  • liquid 1 to be sprayed is thus conveyed through the liquid supply line 125 to the nozzle lance 117 when the main liquid valve 121 is open. At the same time passes through the compressor 136 ambient air 115 through the valve 137 in the line 138 and the compressed gas supply line 4 of the nozzle lance 117. In the spraying operation, no cleaning liquid is supplied via the feed station 139 in the rule.
  • the compressed gas passes into the annular chamber 6, which at least partially surrounds the mixing chamber 7 and through the through-holes 5 in the mixing chamber 7.
  • the liquid to be sprayed shoots through the constriction 10 of the liquid inlet bore centrally symmetrically in the mixing chamber 7 a. Another constriction 114 closes the mixing chamber 7 from the nozzle outlet 8 back. After Bottleneck 114 is adjoined by an outlet funnel, so that a spray jet exits through the nozzle outlet 8 into the process environment 116.
  • the main liquid valve 121 is switched off and the cleaning valves 122, 123, 124 are opened.
  • the compressed gas supply is further maintained and cleaning liquid is fed from the containers 142, 143 via the feed point 139, so that a mixture of cleaning liquid and compressed gas, in particular ambient air 115, is located in the compressed gas feed line 4.
  • cleaning valves 122, 123, 124 at least a portion of the compressed gas is conveyed through the mixing chamber 7 through the lance tube 2 and the feed line 125 to the filter 120 and discharged from here into the Abschlämm constituer 126.
  • the compressed gas flowing into the mixing chamber 7 can exit the mixing chamber 7 via two openings during the cleaning operation, once via the slightly larger constriction 114 of the mixing chamber. mer 7 to the gas space 116 or over the bottleneck 10 in the liquid supply line, namely the lance tube 2 and then to the filter 120 and the Abschlämm constitutioner 26 out.
  • Investigations by the inventor have shown that the dynamic pressure of the atomizing air flowing toward the filter 20 for the removal of platelet-shaped scrapings in the region of the constriction 10, together with the liquid 1 still present in the liquid feed line, the lance tube 2, back to the filter 120 usually quite enough. You can reinforce this cleaning air flow by applying a negative pressure to the Abschlämm constituer 126, which, as already described, by opening the valve 127 and activating the pump 28 takes place.
  • the cleaning effect can be enhanced by applying pressure surges to the cleaning fluid.
  • one of the valves between see mixing chamber 7 and Abschlämm constituer 126 may be designed as a flutter valve.
  • cleaning liquid can also emerge from the nozzle mouth 8. This is usually desirable to replace deposits in the mouth region of the nozzle.
  • This cleaning liquid which enters the gas space 116 via the nozzle mouth 8, becomes even in the cleaning operation so finely sprayed that it is not dangerous for downstream components, since the drops are evaporated in time.
  • the partial flow of the cleaning fluid leaving via the nozzle mouth 8 can be lowered as much as desired by applying a sufficiently low negative pressure to the blowdown container 126. If necessary, one can also reduce the pressure of the atomizing air accordingly.
  • gas can be sucked in through the nozzle mouth 8 through the liquid feed line, the lance tube 2, and the feed line 125 to the nozzle lance 117 by a sufficiently strong reduction of the negative pressure in the blowdown container 126, if this is the case Composition of the gas in the gas space 116, for example, a suitable flue gas composition, does not appear detrimental.
  • two-substance nozzle lances are frequently charged not only with the liquid and compressed gas to be atomized, but also with sheath air, which is guided in a tube which concentrically encloses the two-substance nozzle lance. During operation, this envelope air then encloses the nozzle orifice 8.
  • the sucking back of gas during the cleaning operation it is therefore not necessary for any flue gas to be sucked back over the nozzle lance in this case. Rather, the sucked back gas may consist of neutral enveloping air.
  • sucking back cladding air it is thus possible to clean nozzles and nozzle lances without the cleaning liquid having to enter the flue gas. And there does not always have to be flue gas in the gas space 16.
  • flue gas in the gas space 16.
  • the cleaning liquid which makes up the largest percentage of the blowdown liquid 132 in the blowdown tank 126, can recirculate via the pipe 133 and the pump 154. until their absorption capacity is exhausted, taking account of economic aspects. Therefore, cleaning liquid should only be blown into the gas space 116 via the nozzle orifice 8, as is beneficial for the process or necessary for the cleaning of the nozzle orifice 8.
  • a cleaning fluid then consists exclusively of cleaning fluid and it is possible to rinse the spray assembly 80 with cleaning fluid.
  • the cleaning liquid is then not fed into the compressed gas, but the compressed gas is completely switched off, so that the compressed gas side is supplied exclusively with cleaning liquid.
  • the cleaning liquid would also be conveyed back through the supply air holes 5 and the mixing chamber 7 through the lance tube 2 for the liquid supply to the filter 120. In this case, gas could also be sucked back from the gas space 116 via the nozzle mouth 8 to a certain extent.
  • the blow-down liquid 132 which consists to a large extent of cleaning liquid, would have to be evaporated. This can be done by Zumi see the Abschlämmmatikeit 132 in the main liquid stream 1 during the spraying operation.
  • the dosing liquid 132 into the main liquid stream 1 is expediently added in such a way that the blowdown liquid 132 exits from the nozzle mouth 8 in diluted form for ineffectiveness.
  • Abschlämmitzkeit can be removed via the line 133 and mixed by means of the pump 154 and the dashed lines shown feed line 81 of the liquid to be sprayed 1. With extreme dirt and deposits can also be so by means of the supply line 81 a lot of cleaning liquid are fed, that virtually exclusively cleaning liquid is conveyed to the mixing chamber 7 and thereby causes a thorough cleaning.
  • cleaning fluid eg lye

Landscapes

  • Nozzles (AREA)
  • Details Or Accessories Of Spraying Plant Or Apparatus (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

L'invention concerne une buse de pulvérisation, un dispositif de pulvérisation, ainsi qu'un procédé permettant de faire fonctionner une buse de pulvérisation et un dispositif de pulvérisation. L'invention concerne une buse de pulvérisation comprenant une chambre de sortie ou de mélange (7), et au moins deux alésages traversants (5) débouchant dans la chambre de sortie ou de mélange, lesdits alésages étant reliés respectivement à un conduit de fluide. L'invention est caractérisée en ce qu'au moins l'un des alésages traversants est réalisé autonettoyant et/ou en ce qu'il est prévu des dispositifs de nettoyage d'au moins l'un des alésages traversants (74). Application, par exemple pour l'emploi de buses à deux composants pour l'épuration des gaz de fumée.
EP06753495.8A 2005-05-06 2006-05-05 Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation Not-in-force EP1890823B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
SI200631692T SI1890823T1 (sl) 2005-05-06 2006-05-05 Pršilna šoba, pršilni sestav in postopek za obratovanje pršilne šobe in pršilnega sestava
PL06753495T PL1890823T3 (pl) 2005-05-06 2006-05-05 Dysza rozpylająca, układ rozpylający i sposób eksploatacji dyszy rozpylającej i układu rozpylającego

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102005021650A DE102005021650A1 (de) 2005-05-06 2005-05-06 Verfahren und Vorrichtung zur Optimierung von Zweistoff-Düsen
DE200510037991 DE102005037991A1 (de) 2005-08-09 2005-08-09 Verfahren und Vorrichtung zur on-line-Abreinigung von Düsen sowie der zugehörigen Düsenlanzen
PCT/EP2006/004220 WO2006119923A1 (fr) 2005-05-06 2006-05-05 Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation

Publications (2)

Publication Number Publication Date
EP1890823A1 true EP1890823A1 (fr) 2008-02-27
EP1890823B1 EP1890823B1 (fr) 2013-08-14

Family

ID=36658668

Family Applications (1)

Application Number Title Priority Date Filing Date
EP06753495.8A Not-in-force EP1890823B1 (fr) 2005-05-06 2006-05-05 Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation

Country Status (10)

Country Link
US (2) US8453945B2 (fr)
EP (1) EP1890823B1 (fr)
JP (1) JP5376937B2 (fr)
KR (1) KR101298564B1 (fr)
CA (2) CA2606868C (fr)
DK (1) DK1890823T3 (fr)
PL (1) PL1890823T3 (fr)
RU (2) RU2438796C2 (fr)
SI (1) SI1890823T1 (fr)
WO (1) WO2006119923A1 (fr)

Families Citing this family (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8453945B2 (en) 2005-05-06 2013-06-04 Dieter Wurz Spray nozzle, spray device and method for operating a spray nozzle and a spray device
WO2009030674A2 (fr) * 2007-09-04 2009-03-12 Shell Internationale Research Maatschappij B.V. Cuve de trempe
GB0810155D0 (en) * 2008-06-04 2008-07-09 Pursuit Dynamics Plc An improved mist generating apparatus and method
EP2263780B1 (fr) * 2009-06-18 2017-12-06 ENVIROSERV GmbH Installation de nettoyage de gaz de fumées dotée d'une variation de buses
EP2263779B1 (fr) * 2009-06-18 2015-03-11 ENVIROSERV GmbH Installation de nettoyage de gaz de fumée dotée d'une unité de sortie
US9873096B2 (en) * 2009-12-29 2018-01-23 Indian Oil Corporation Limited Feed nozzle assembly
WO2011150368A1 (fr) * 2010-05-28 2011-12-01 Arizona Board Of Regents Acting For And On Behalf Of Arziona State University Appareil et procédés pour une buse virtuelle à dynamique des gaz
US8834074B2 (en) * 2010-10-29 2014-09-16 General Electric Company Back mixing device for pneumatic conveying systems
DE102011078076A1 (de) * 2011-06-24 2012-12-27 Dürr Ecoclean GmbH Düsenmodul und Reinigungsvorrichtung mit Düsenmodul
CN102997620B (zh) * 2011-09-15 2015-10-21 江苏申久化纤有限公司 一种带喷淋装置的干燥机
EP2808087B1 (fr) * 2013-05-28 2019-02-27 Valmet Technologies, Inc. Dispositif pour traiter un voile de fibres
CN103301967B (zh) * 2013-06-17 2015-11-25 深圳市华星光电技术有限公司 一种配向膜料液喷头
WO2015059941A1 (fr) * 2013-10-21 2015-04-30 株式会社不二製作所 Méthode d'usinage par sablage et dispositif d'usinage par sablage
KR101438722B1 (ko) * 2014-02-03 2014-09-05 김현태 미세세정을 위한 트위스터 분사 시스템
DE102014003877A1 (de) 2014-03-19 2015-09-24 Dieter Wurz Verfahren und Vorrichtung zur on-line-Reinigung von Zweistoffdüsen
FR3020578B1 (fr) * 2014-05-05 2021-05-14 Total Raffinage Chimie Dispositif d'injection, notamment pour injecter une charge d'hydrocarbures dans une unite de raffinage.
DE102015206548A1 (de) 2015-04-13 2016-10-13 Lechler Gmbh Sprühanordnung und Verfahren zum Betreiben einer Sprühanordnung
US10413920B2 (en) * 2015-06-29 2019-09-17 Arizona Board Of Regents On Behalf Of Arizona State University Nozzle apparatus and two-photon laser lithography for fabrication of XFEL sample injectors
US10634397B2 (en) * 2015-09-17 2020-04-28 Purdue Research Foundation Devices, systems, and methods for the rapid transient cooling of pulsed heat sources
CN105478257A (zh) * 2015-12-24 2016-04-13 镇江常青园林工程有限公司 一种喷头元件
CN105618290B (zh) * 2016-03-16 2018-06-26 湖北荷普药业股份有限公司 一种雾化喷头
DE102017101370A1 (de) 2017-01-25 2018-07-26 Eisenmann Se Vorrichtung zum Vernebeln einer Spülflüssigkeit
DE102017001025B4 (de) * 2017-02-03 2020-10-08 Rs Rittel Gmbh Verbrennungsanlage und Verfahren zur Abgasbehandlung
FI20175158L (fi) * 2017-02-21 2018-08-22 Metabar Tech Oy Suutin, suutinjärjestely ja nesteenjakojärjestelmä
WO2018204655A1 (fr) * 2017-05-03 2018-11-08 Coil Solutions, Inc. Outil de portée étendue
CN107413747A (zh) * 2017-09-22 2017-12-01 武汉华星光电技术有限公司 一种清洁装置及清洁方法
US11028727B2 (en) * 2017-10-06 2021-06-08 General Electric Company Foaming nozzle of a cleaning system for turbine engines
CN109399747B (zh) * 2018-11-23 2024-01-12 国网新疆电力有限公司电力科学研究院 喷枪及适用于脱硫废水烟道蒸发装置
CN110270464B (zh) * 2019-05-22 2024-02-09 杭州沃凌的机电有限公司 一种磁致伸缩超声阀
KR102388407B1 (ko) 2019-07-02 2022-04-21 세메스 주식회사 노즐 장치, 기판 처리 장치 및 방법
KR102511585B1 (ko) * 2020-11-08 2023-03-16 부산대학교 산학협력단 경흉강 섬유아교도포법 시술용 카테터 탈크 분사 모듈
CN112517262B (zh) * 2020-11-19 2021-09-07 湖南尚亿智能制造有限公司 一种机械零件喷漆加工设备
RU205299U1 (ru) * 2021-03-19 2021-07-07 Общество с ограниченной ответственностью Научно-производственное предприятие «Томская электронная компания» Устройство очистки гидравлических выходов от солевых отложений
DE102022200850A1 (de) * 2022-01-26 2023-07-27 Firedos Gmbh Verschlussteil für ein Ventil

Family Cites Families (55)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US733463A (en) * 1902-02-15 1903-07-14 Ezra D Dennison Petroleum-burner for furnaces.
US733579A (en) * 1903-04-01 1903-07-14 Joseph Fitton Hydrocarbon-burner.
GB492852A (en) * 1937-12-16 1938-09-28 Parks Cramer Co Improvements in and relating to liquid atomizing devices
US2893646A (en) 1958-10-07 1959-07-07 Charles C Batts Fluid spray nozzle
US3228611A (en) * 1963-01-17 1966-01-11 Bolton Emerson Apparatus for cleaning showers
US3272441A (en) * 1965-11-03 1966-09-13 Gulf Research Development Co Aspirating spray nozzle
JPS5372213A (en) 1976-12-08 1978-06-27 Takuo Mochizuki Device for preventing clogging of jet nozzle
IT1117662B (it) * 1977-01-14 1986-02-17 Italimpianti Bruciatore radiante per combustibile liquidi e gassosi
DE2747707C2 (de) 1977-10-25 1982-10-21 Daimler-Benz Ag, 7000 Stuttgart Anlage zum Farbspritzen von Serienteilen wechselnder Farbe
US4341347A (en) * 1980-05-05 1982-07-27 S. C. Johnson & Son, Inc. Electrostatic spraying of liquids
SU1028378A1 (ru) * 1980-05-16 1983-07-15 Предприятие П/Я Г-4780 Краскораспылительна установка
US4548359A (en) * 1983-06-02 1985-10-22 Capital Controls Company, Inc. Self-cleaning gas-liquid mixing apparatus
JPS6126868Y2 (fr) * 1984-09-01 1986-08-11
SU1260031A1 (ru) * 1985-01-28 1986-09-30 Научно-исследовательский и экспериментальный институт автомобильного электрооборудования и автоприборов Пневматический распылитель
JPS62201665A (ja) * 1986-03-01 1987-09-05 Kimitoshi Mato 二流体ノズル
US4881563A (en) * 1986-09-05 1989-11-21 General Motors Corporation Paint color change system
SU1507457A1 (ru) * 1987-04-07 1989-09-15 Киевский Институт Инженеров Гражданской Авиации Им.60-Летия Ссср Распылитель жидкости
SU1507454A1 (ru) 1987-07-13 1989-09-15 Белорусский Комплексный Проектно-Изыскательский И Научно-Исследовательский Институт Топливной Промышленности "Белниитоппроект" Циклон
JPH0725244Y2 (ja) * 1988-04-27 1995-06-07 株式会社エルエーシー 描画用インクスプレーガン装置
FR2640716B1 (fr) * 1988-12-20 1991-04-05 Fmc Europe Vanne raclable a trois voies et conduite raclable de distribution de liquides la comportant
FR2640717B1 (fr) * 1988-12-20 1991-04-05 Fmc Europe Vanne a deux voies destinee a etre montee en aval d'une conduite raclable de distribution de fluide
JPH0311457U (fr) * 1989-06-16 1991-02-05
FR2660215B1 (fr) * 1990-04-02 1995-07-21 Stein Industrie Lance de dispersion de pulpe.
CA2035702C (fr) * 1991-02-05 1996-10-01 Mohan Vijay Jet cavitant ou pulse genere par ultrasons
JPH0763606B2 (ja) * 1991-10-18 1995-07-12 フロイント産業株式会社 コーティング装置
JPH0563658U (ja) * 1992-02-05 1993-08-24 日立造船株式会社 二流体噴射ノズル
JPH0828684B2 (ja) 1992-02-19 1996-03-21 富士通株式会社 二重平衡偏波ダイバーシティ受信装置
JPH067717A (ja) 1992-06-26 1994-01-18 Nisshin Steel Co Ltd ノズルの閉塞防止方法
JPH0639330A (ja) * 1992-07-23 1994-02-15 Nec Corp 薬液塗布装置
JP2830683B2 (ja) * 1992-09-11 1998-12-02 トヨタ自動車株式会社 回転霧化静電塗装装置
DE4231119C1 (de) 1992-09-17 1994-04-21 Int Schuh Maschinen Co Gmbh Verfahren zum Auftragen von Klebstoffen und Beschichtungseinrichtung zur Durchführung des Verfahrens
JP3438175B2 (ja) * 1993-05-12 2003-08-18 日鉄化工機株式会社 噴霧ノズルとその使用方法
RU2102160C1 (ru) 1993-06-22 1998-01-20 Сухонин Сергей Данилович Распылитель
FR2710666B1 (fr) 1993-09-27 1996-03-01 Viafrance Sa Bloc de pulvérisation de produits routiers.
US5509849A (en) * 1994-04-18 1996-04-23 Church & Dwight Co., Inc. Blast nozzle for water injection and method of using same for blast cleaning solid surfaces
US5709749A (en) * 1994-10-03 1998-01-20 Behr Systems, Inc. Solvent supply for paint sprayer
KR100265890B1 (ko) * 1996-12-03 2000-09-15 라붸 린도베르 회전무화 헤드형 도장장치
US5938120A (en) * 1997-06-13 1999-08-17 Abbott Laboratories Fluid system and method
DE19728155A1 (de) * 1997-07-03 1999-01-07 Lactec Gmbh Verfahren und Vorrichtung zum Lackieren
AT407385B (de) * 1997-09-18 2001-02-26 Sez Semiconduct Equip Zubehoer Anordnung um das nachtropfen von flüssigkeiten aus leitungen zu verhindern
US5899387A (en) * 1997-09-19 1999-05-04 Spraying Systems Co. Air assisted spray system
US5964418A (en) * 1997-12-13 1999-10-12 Usbi Co. Spray nozzle for applying metal-filled solventless resin coating and method
US6062493A (en) 1998-02-26 2000-05-16 Abplanalp; Robert Henry Sprayer for liquids and nozzle insert
US6286929B1 (en) 1998-12-29 2001-09-11 Eastman Kodak Company Self-cleaning ink jet printer with oscillating septum and ultrasonics and method of assembling the printer
US6267301B1 (en) 1999-06-11 2001-07-31 Spraying Systems Co. Air atomizing nozzle assembly with improved air cap
US6161778A (en) * 1999-06-11 2000-12-19 Spraying Systems Co. Air atomizing nozzle assembly with improved air cap
JP2002079145A (ja) * 2000-06-30 2002-03-19 Shibuya Kogyo Co Ltd 洗浄ノズル及び洗浄装置
RU2184619C1 (ru) * 2001-03-22 2002-07-10 Душкин Андрей Леонидович Распылитель жидкости (варианты)
FI111054B (fi) * 2001-06-25 2003-05-30 Vesa Antero Koponen Suutin pintojen päällystämiseksi
DE10140216B4 (de) * 2001-08-17 2006-02-09 ITW Oberflächentechnik GmbH & Co. KG Verfahren und Vorrichtung an einer Lackiereinrichtung zum Reinigen einer Lack-Förderleitung
US6705539B1 (en) 2002-02-07 2004-03-16 Frank C. Bien Spray gun/applicator
AU2003223312A1 (en) * 2002-03-21 2003-10-08 Nordson Corporation Spray gun cleaning arrangements
US6666386B1 (en) * 2002-06-06 2003-12-23 Yu-Chiung Huang Atomizing nozzle structure
DE102005021650A1 (de) 2005-05-06 2006-11-09 Wurz, Dieter, Prof. Dr.-Ing. Verfahren und Vorrichtung zur Optimierung von Zweistoff-Düsen
US8453945B2 (en) * 2005-05-06 2013-06-04 Dieter Wurz Spray nozzle, spray device and method for operating a spray nozzle and a spray device

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2006119923A1 *

Also Published As

Publication number Publication date
JP5376937B2 (ja) 2013-12-25
US8453945B2 (en) 2013-06-04
SI1890823T1 (sl) 2013-12-31
CA2606868A1 (fr) 2006-11-16
RU2007144330A (ru) 2009-06-20
EP1890823B1 (fr) 2013-08-14
CA2606868C (fr) 2013-10-29
CA2815553A1 (fr) 2006-11-16
US8985478B2 (en) 2015-03-24
RU2438796C2 (ru) 2012-01-10
KR101298564B1 (ko) 2013-08-22
JP2008540079A (ja) 2008-11-20
RU2570868C2 (ru) 2015-12-10
WO2006119923A1 (fr) 2006-11-16
RU2011132606A (ru) 2013-02-10
DK1890823T3 (da) 2013-11-25
US20090121038A1 (en) 2009-05-14
KR20080012343A (ko) 2008-02-11
PL1890823T3 (pl) 2014-01-31
US20130161408A1 (en) 2013-06-27

Similar Documents

Publication Publication Date Title
EP1890823B1 (fr) Buse de pulverisation, dispositif de pulverisation et procede permettant de faire fonctionner une buse de pulverisation et un dispositif de pulverisation
DE19740996B4 (de) Zweifluid-Reinigungsstrahldüse sowie Reinigungsvorrichtung und Anwendungsverfahren dafür
EP0634229B1 (fr) Procédé, assemblage et dispositif pour le nettoyage et revêtement interne d'une tuyauterie
DE102006053910B4 (de) Biowäscher
EP1997547B1 (fr) Procédé destiné au rétrolavage de filtres
DE202015104279U1 (de) Fluidisches Bauteil und Anwendungen des fluidischen Bauteils
DE102005021650A1 (de) Verfahren und Vorrichtung zur Optimierung von Zweistoff-Düsen
DE202006000969U1 (de) Reinigungsmolch
DE20280185U1 (de) Vorrichtung zur Abreinigung von Filtern für staubbelastete Abgabe
DE4103514C1 (fr)
DE102008024583B4 (de) Verfahren zum Betrieb einer Filtereinrichtung und Filtereinrichtung
EP3226996B1 (fr) Dispositif de filtration, système hydraulique et procédé de lavage à contre-courant
WO2000010681A1 (fr) Procede pour nettoyer des bougies d'un filtre a bougies
EP1512450A1 (fr) Dispositif de filtration
DE2417580A1 (de) Verfahren und vorrichtung zum richten eines feste abriebpartikel enhaltenden fluessigkeitsstrahls auf die oberflaeche eines werkstuecks
EP1161293B1 (fr) Dispositif de nettoyage
DE102018211096A1 (de) Luftdüse zur Reinigung einer Filtervorrichtung, Reinigungsvorrichtung für eine Filtervorrichtung mit selbiger Luftdüse, und Verfahren zur Reinigung einer Filtervorrichtung mit selbiger Reinigungsvorrichtung
DE19701010A1 (de) Verfahren zur Sanierung der Innenwände festverlegter Rohrleitungen
DE102005037991A1 (de) Verfahren und Vorrichtung zur on-line-Abreinigung von Düsen sowie der zugehörigen Düsenlanzen
DE19516740C2 (de) Vakuumtoilettensystem
WO1997017010A1 (fr) Procede et dispositif de rinçage
EP0527543B1 (fr) Procédé et dispositif pour le nettoyage des foiles filtrantes
DE102021213038B3 (de) Filtervorrichtung und Filteranordnung für ein flüssiges Medium sowie deren Verwendung
WO1993000148A1 (fr) Dispositif de nettoyage par voie humide, notamment pour separer des impuretes gazeuses, liquides et/ou solides contenues dans des courants gazeux
DE102007055584C5 (de) Reinigungseinrichtung und Verfahren zum Reinigen von Filtern

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

17P Request for examination filed

Effective date: 20071205

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

17Q First examination report despatched

Effective date: 20080424

DAX Request for extension of the european patent (deleted)
REG Reference to a national code

Ref country code: DE

Ref legal event code: R079

Ref document number: 502006013116

Country of ref document: DE

Free format text: PREVIOUS MAIN CLASS: B05B0007040000

Ipc: B05B0007240000

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

RIC1 Information provided on ipc code assigned before grant

Ipc: B05B 7/04 20060101ALI20130304BHEP

Ipc: B05B 7/24 20060101AFI20130304BHEP

INTG Intention to grant announced

Effective date: 20130328

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: AT

Ref legal event code: REF

Ref document number: 626477

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130815

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502006013116

Country of ref document: DE

Effective date: 20131010

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

Effective date: 20131118

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: WAGNER PATENT AG, CH

REG Reference to a national code

Ref country code: NL

Ref legal event code: T3

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

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

Ref country code: LT

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: 20130814

Ref country code: PT

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: 20131216

Ref country code: CY

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: 20130703

Ref country code: IS

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: 20131214

REG Reference to a national code

Ref country code: PL

Ref legal event code: T3

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

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: 20131115

Ref country code: LV

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: 20130814

REG Reference to a national code

Ref country code: SK

Ref legal event code: T3

Ref document number: E 15250

Country of ref document: SK

REG Reference to a national code

Ref country code: CH

Ref legal event code: PCAR

Free format text: NEW ADDRESS: BAECHERSTRASSE 9, 8832 WOLLERAU (CH)

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

Ref country code: CY

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: 20130814

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

Ref country code: RO

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: 20130814

Ref country code: EE

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: 20130814

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

Ref country code: ES

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: 20130814

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

26N No opposition filed

Effective date: 20140515

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502006013116

Country of ref document: DE

Effective date: 20140515

Ref country code: HU

Ref legal event code: AG4A

Ref document number: E020024

Country of ref document: HU

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20140505

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

Ref country code: SK

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

Effective date: 20140505

Ref country code: MC

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: 20130814

REG Reference to a national code

Ref country code: SK

Ref legal event code: MM4A

Ref document number: E 15250

Country of ref document: SK

Effective date: 20140505

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

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

Ref country code: SI

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

Effective date: 20140506

REG Reference to a national code

Ref country code: SI

Ref legal event code: KO00

Effective date: 20150106

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: 20140505

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 11

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

Ref country code: BG

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: 20130814

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

Ref country code: BE

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: 20140531

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 12

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 13

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

Ref country code: NL

Payment date: 20190521

Year of fee payment: 14

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

Ref country code: DK

Payment date: 20190523

Year of fee payment: 14

Ref country code: CZ

Payment date: 20190426

Year of fee payment: 14

Ref country code: IT

Payment date: 20190521

Year of fee payment: 14

Ref country code: PL

Payment date: 20190408

Year of fee payment: 14

Ref country code: FI

Payment date: 20190517

Year of fee payment: 14

Ref country code: DE

Payment date: 20190523

Year of fee payment: 14

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

Ref country code: FR

Payment date: 20190521

Year of fee payment: 14

Ref country code: HU

Payment date: 20190424

Year of fee payment: 14

Ref country code: TR

Payment date: 20190426

Year of fee payment: 14

Ref country code: SE

Payment date: 20190523

Year of fee payment: 14

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

Ref country code: CH

Payment date: 20190523

Year of fee payment: 14

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

Ref country code: AT

Payment date: 20190517

Year of fee payment: 14

Ref country code: GB

Payment date: 20190523

Year of fee payment: 14

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502006013116

Country of ref document: DE

REG Reference to a national code

Ref country code: FI

Ref legal event code: MAE

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

Effective date: 20200531

REG Reference to a national code

Ref country code: NL

Ref legal event code: MM

Effective date: 20200601

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 626477

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200505

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

Ref country code: AT

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

Effective date: 20200505

Ref country code: LI

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

Effective date: 20200531

Ref country code: HU

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

Effective date: 20200506

Ref country code: FI

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

Effective date: 20200505

Ref country code: SE

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

Effective date: 20200506

Ref country code: CH

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

Effective date: 20200531

Ref country code: CZ

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

Effective date: 20200505

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 NON-PAYMENT OF DUE FEES

Effective date: 20200601

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20200505

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

Ref country code: FR

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

Effective date: 20200531

Ref country code: GB

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

Effective date: 20200505

Ref country code: DK

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

Effective date: 20200531

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: 20201201

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

Ref country code: IT

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

Effective date: 20200505

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

Ref country code: TR

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

Effective date: 20200505

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

Ref country code: PL

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

Effective date: 20200505