EP1921968B1 - Method for treating dust and devices for carrying out this method - Google Patents

Method for treating dust and devices for carrying out this method Download PDF

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Publication number
EP1921968B1
EP1921968B1 EP06777015A EP06777015A EP1921968B1 EP 1921968 B1 EP1921968 B1 EP 1921968B1 EP 06777015 A EP06777015 A EP 06777015A EP 06777015 A EP06777015 A EP 06777015A EP 1921968 B1 EP1921968 B1 EP 1921968B1
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EP
European Patent Office
Prior art keywords
dust
treating
binding agent
added
particles
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.)
Not-in-force
Application number
EP06777015A
Other languages
German (de)
French (fr)
Other versions
EP1921968A2 (en
Inventor
Andre Bertram
Günther ENNEN
Jörg KINNIUS
Stefan Tiekötter
Dirk Wegener
Cornelius Wolf
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.)
Miele und Cie KG
Original Assignee
Miele und Cie KG
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 DE200510041170 external-priority patent/DE102005041170B3/en
Priority claimed from DE200510047812 external-priority patent/DE102005047812A1/en
Application filed by Miele und Cie KG filed Critical Miele und Cie KG
Priority to PL06777015T priority Critical patent/PL1921968T3/en
Publication of EP1921968A2 publication Critical patent/EP1921968A2/en
Application granted granted Critical
Publication of EP1921968B1 publication Critical patent/EP1921968B1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

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Classifications

    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/106Dust removal
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/102Dust separators
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/14Bags or the like; Rigid filtering receptacles; Attachment of, or closures for, bags or receptacles
    • A47L9/1409Rigid filtering receptacles
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/16Arrangement or disposition of cyclones or other devices with centrifugal action
    • A47L9/1683Dust collecting chambers; Dust collecting receptacles
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/18Liquid filters
    • A47L9/182Separating by passing the air over a liquid bath
    • AHUMAN NECESSITIES
    • A47FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47LDOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10Filters; Dust separators; Dust removal; Automatic exchange of filters
    • A47L9/18Liquid filters
    • A47L9/183Spray cleaning

Definitions

  • the present invention relates to a method of treating dust in a vacuum cleaner. Moreover, the invention relates to various devices for carrying out such a method.
  • dust retention systems are used, which are usually arranged between the air inlet of a dust collection chamber and the suction side of a fan and hold back the absorbed dust before entering the fan.
  • the best known variant is a bag shaped filter which is internally pressurized, d. h., the dust settles inside the bag.
  • the bag is usually still downstream of a fine dust filter, which receives dust particles in the order of less than 2 microns, which pass through the bag. The removal of this dust content from the room air wins with the increasing number of people with allergies in importance, as these particles are respirable because of their small size and therefore lead to a health burden.
  • the bag When reaching the maximum capacity, which is about 400 grams, the bag must be replaced, this can be hygienic especially with closable bags, as the dust remains in the bag and is disposed of with this. Such replacement is required several times a year, depending on usage, and incurs costs. Also, the fine dust filter must be replaced after a certain period of use, but here are the intervals because of the small amount of fine dust larger, from the manufacturers, a replacement after about a year is recommended. Because of the small particle sizes, a small proportion by mass of fine dust is produced, which is why commercially available fine dust filters have a capacity of about 10 grams.
  • the dust is separated into at least two fractions, which differ by the size or mass of the dust particles, and a dust binder is added to a fraction, so that the dust is not only loosely deposited in a dust collection room, but experiences some bonding and cross-linking and during the emptying of the dust collecting space no turbulence takes place.
  • the burden of particulate matter, pathogenic particles or other pollutants is thereby reduced and the handling of the dust collection chamber, which must be emptied at regular intervals, becomes significantly more hygienic and the contents of the dust collection chamber can be used as a mixture, e.g. as lumps, to be disposed of at once.
  • the fraction whose dust particles are mostly smaller than the fraction to which a dust binder is added is then taken up by a fine dust filter. This avoids that particles of this fraction are returned to the room air and swirled there.
  • the dust is separated into three fractions, which differ by the size and / or mass of the dust particles, and a dust binder is added to the fraction with dust particles, which have a majority of medium size or mass.
  • the first fraction containing only coarse particles, can be emptied without any dusting even without binder. Therefore, a dust binder is needed only for the middle fraction. The amount required for binding can be significantly reduced compared to methods that collect the first two fractions in a container.
  • the facilities with which the dust is separated should be dimensioned so that the first fraction contains a majority of dust particles with a size of more than 200 microns, that the second fraction contains a majority of dust particles with a size between 200 microns and 30 microns and that a third fraction contains a majority of dust particles with a size of less than 30 microns.
  • Particles of the third fraction are still very large at 30 ⁇ m, which in turn causes a particulate matter filter with a very large absorption capacity. In this way, however, it is achieved that in the second fraction, even with a blurred separation, only very few respirable particulate matter particles are present. This ensures that users are not or only slightly at risk when emptying the container for the second fraction, even if they have decided against the use of a dust binder or forgot its addition.
  • a suitable fine dust filter should have at least a storage capacity of 200 grams. Since due to the separation limit of 30 microns relatively large and massive particles enter the fine dust filter, a commercial filter with a capacity of 10 grams would quickly exhausted. This would contradict the idea of a vacuum cleaner, which should require little or no consumables. For this reason, a filter capacity is selected which guarantees a service life of more than one year under normal usage conditions. In addition to the increased service life, the advantage of a low flow loss of only about 20% (at the end of the service life, based on the initial state) is achieved.
  • the use of such a filter is preferably carried out in a vacuum cleaner in which a dust binder for the next larger fraction is used. However, a use of such a filter is also possible without a dust binder, especially when the separation limits of the dust collecting container are so sharp that the next largest fraction contains no respirable particles.
  • the FIG. 1 shows purely schematically a vacuum cleaner 1 in longitudinal section.
  • the vacuum cleaner 1 has in a known manner a housing 2 which is divided into a fan chamber 3 and a dust collecting space 4.
  • the dust collecting space 4 is closed by a pivotable cover 5 and has a first opening 6 into which the coupling 7 of a suction hose 8 opens.
  • a suction tube not shown
  • SaugvorA also not shown
  • a second opening 9 is in the partition 10 between Dust collecting space 4 and 3 blower chamber arranged. Behind this opening 9 is a fine dust filter 11.
  • a motor fan 12 is arranged in the fan chamber 3, which is directed with its suction side to the fine dust filter 11 and the opening 9 and with its outlet side via further openings 18 - possibly with upstream filter (not shown) - connected to the ambient air 13.
  • a receiving space 14 for a device control and operating and display elements (see FIG. 3 ) arranged.
  • this is a centrifugal separator 20, the aforementioned variants Massenträgheitsabscheider or dust cassette are also conceivable.
  • the separator used is dimensioned such that a fraction is collected within the dust collection container, the majority of which are greater than 30 microns.
  • FIG. 2 shows the centrifugal separator 20 as a detail. It comprises a cyclone cone 21, which is provided with an air feed 22 and an air discharge 23.
  • the air supply 22 is in fluid communication with the opening 6, the air discharge 23 via the line 15 with the opening 9 (s. FIG. 1 ).
  • the cyclone cone 21 is inserted into a cylindrical container 24, which, as shown in the figure, can be divided into a tubular holder 25 and a dust collecting container 26 arranged underneath.
  • the sucked dust-laden air is set in the cyclone cone 21 in a rotational movement, so that according to the principle of centrifugal force of the coarse dust 17 is pressed against the outer wall and falls down into the dust collector 26. In the further airway then the fine dust is separated by the fine dust filter 11.
  • the container 26 is filled, which can be determined via fill level, pressure or dust quantity sensors or simply by measuring the switch-on times of the blower (not shown), this is indicated to the user via a display device 35 (see FIG. FIG. 3
  • FIG. 3 shows the top view of an inventively designed vacuum cleaner 1.
  • a control panel 30 next to the known control and display elements such as on / off switch 31, change indicator 32 for the fine dust filter 11, cable rewind button 33 and power controller 34 more elements provided, the function explained later is.
  • this may be the above-described display 35 for emptying the dust collector 26.
  • FIGS. 4 and 5 is activated to activate the change indicator from the EP 0 759 157 B1 known piezosensor used, which to the device control - symbolically indicated in the figure by the dashed box 36 - is a signal that correlates with the absorbed amount of dust.
  • the user can then do the Separate dust collector 26 from the rest of the centrifugal separator 20 and empty the coarse dust 17. This is where the invention begins:
  • a dust binder is added to this.
  • a dust-binding agent in the context of the invention is a one- or multi-component additive which is present in solid and / or liquid and / or gaseous phase, the phase being possibly variable in order to penetrate the sucked-up dust present in loose, unbound form mix and at least partially make a binding of the dust.
  • the dust binder is also intended to bind the fine dust, germs, bacteria, pollen and other pollutants present in the dust collector in order to avoid turbulence and the resulting burden on the user when disposed of.
  • the filled dust collection chamber can be emptied in a hygienic manner, without resulting in dusting.
  • Suitable dust-dispersing agents which can be used are suitably dispersible liquids, powders, foams, granules or solid, in particular tablet-shaped, pressed substances.
  • the dust binder fragrances, cleansing or germ-inhibiting substances may be added.
  • the addition of the dust binder in the dust collection container by means of a suitable device which is integrated either within the vacuum cleaner or in a suction attachment or is designed as an external apparatus with a receptacle for the dust collector.
  • Embodiments of dust collection containers are shown in which a dust binder is added and mixed with the dust.
  • a dust binder a liquid, powder, foam or granules can be used, mixed forms are conceivable. In particular, when using granules should this be added to a substance which improves the adhesion of the dust.
  • the dust-binding agent may be enriched with agents which have a cleaning action, for example by adding surfactants or similar cleaning-promoting substances. Bactericidal, bacteriostatic, and / or fungicidal agents may also be added to prevent microbial contamination within the dust collector. These properties are achieved, for example, by doping the material with silver ions.
  • fragrances can be used to make the handling of the dust collection room more pleasant.
  • agents for mixing dust and dust binder in particular when adding the agent at the beginning or at the end of the suction process or when added in an external apparatus.
  • mechanical or motor means can be used, which set the container in motion, rotation or vibration.
  • a dust amount sensor 41 is arranged in the air supply 22, which detects the amount of dust flowing through. Further, in the air supply 22, a metering device 42 for powder and / or granules as dust binder 43 is provided. The quantity detected by the dust quantity sensor 41 is passed on to the device control 36, and this causes, in the presence of an amount which requires emptying of the collecting container 26, that the dust binder is discharged via a metering flap 44 into the air supply 22 and swirled there with the still dust-laden air becomes. Due to the subsequent cyclone-like turbulence of the air with the dust 17 and the dust binder 43 optimal mixing is achieved.
  • the dust binder 43 is collected together with the dust 17 in the container 26 and can then be disposed of at regular intervals.
  • the metering of the dust binder 43 can take place via flaps, pistons, screws and / or nozzles.
  • the addition of the dust binder can be done either directly in the dust collection chamber 26 or in the region of the air supply 22, for example, the addition can already be done on the suction attachment of the vacuum cleaner 1 (not shown).
  • FIG. 5 another embodiment of a dust collection container 26 is shown, in which the coarse dust 17 is bound.
  • at least one spraying device 50 is provided on the container 26, by means of which a fluid 52 can be discharged into the dust collecting chamber 26.
  • the spray device 50 comprises a reservoir 53, in which the fluid 52 is arranged as a dust binder.
  • 36 activatable dosing pumps 54 are provided by the device control to promote by means of hoses 55, the liquid dust binder 52 in the dust collector 26.
  • one or more nozzles 51 are provided, from which the discharged from the hoses 55 fluid 52 is discharged into the dust collecting space 26 and atomized.
  • the dispersed, dust-binding fluid 52 is shown schematically by the spray 56.
  • the dust-binding agent 52 may be a glycol-containing or glycerin-containing liquid which reduces the surface tension to values of less than 40 mN / m and, if appropriate, is supplemented with fungicidal, bacteriostatic and / or bactericidal ingredients. Also conceivable is the use of a highly diluted adhesive, such as wallpaper paste.
  • the liquid dust binder 52 should preferably be dispersible. Instead of a fluid can be sprayed with appropriate design of metering pumps and nozzles also powdered, foam or granular media. For metering, other pressure-generating elements may be used instead of the pumps 54.
  • the dust binder 52 can also be supplied via controllable valves and dispersed with ultrasound.
  • the control of the supply of the liquid dust binder 52 can also be done here depending on the data of a dust quantity sensor 41, but alternatively also according to one of the other previously enumerated variants.
  • the walls of the dust collection chamber 26 may be made of plastic for cost-effective production. It is of course also possible to provide an anti-stick coating to facilitate cleaning.
  • FIG. 6 an embodiment of a dust collection chamber 26 is shown, in which the dust 17 is bound by a substance which is first melted and can be cooled after receiving the dust 17 and then removed from the dust collecting space 26.
  • Paraffin 60 for example, is used for this purpose, which is added to the container as tablet 61 or granules.
  • a heat source 62 is provided, which is supplied via a power supply 63 with electrical energy.
  • a receptacle 64 for the paraffin tablet 61 is located at the bottom of the container 26, a receptacle 64 for the paraffin tablet 61. Furthermore, the dust 17 is shown schematically, which lies on the paraffin tablet 61. At regular intervals, the container 26 can be removed from the vacuum cleaner 1 and cleaned.
  • the heat source is supplied in the form of a heating plate 62 via the power supply 63 with electrical energy, whereby the paraffin 60 is transferred from the solid to the liquid phase. It can also be the waste heat of the fan 12 are used.
  • the density of the paraffin 60 is on the order of ⁇ 1 g / cm 3 , for example in the range between 0.5 and 0.7 cm 3 .
  • all bodies will sink into the paraffin 60, which has a density> about 0.8 g / cm 3 .
  • These conditions meet house dust particles 17 whose density is in the range> 1g / cm 3 . Due to the size ratios of the density of the individual substances and the relatively easy-to-reach phase change of the paraffin tablet 61, it is possible to easily bind the dust 17 in the container 26 and sink it into the paraffin 60. If the container 26 is sufficiently filled, the cooled lump of paraffin 60 and bound dust 17 can be disposed of without dusting.
  • the non-polar, molecular structure of the paraffin 60 and its low surface tension ensures that, in contrast to water, particles can basically sink in easily in the liquid phase of the paraffin 60.
  • the melting point of the paraffin 60 can be set in a wide range.
  • the paraffin tablet 61 is in the region of the receptacle 64 which is made of a repulsive (anti-sticking) material or material having a repulsive surface, preferably silicone. Due to the better thermal conductivity, the receptacle can also consist of Teflon-coated aluminum.
  • the receptacle 64 may be detachably received in the container 26 to be taken out and replaced by a new paraffin tablet 61 possibly with a new receptacle 64.
  • substances whose phase is variable by supplying heat energy substances whose viscosity can be changed by kinetic energy - so-called tixotropic substances - can be used as a dust binder.
  • tixotropic substances substances whose viscosity can be changed by kinetic energy - so-called tixotropic substances - can be used as a dust binder.
  • cellulose suspensions may be mentioned here
  • FIG. 10 shows a dust collector 26, which is equipped with such a pressing device 100.
  • a compression ram 101 is arranged in the removable dust collecting container 26, which is manually or automatically, ie electromotively or aerodynamically driven, and thereby pressed onto the coarse dust 17 and the binder.
  • the dust is in the liquid binder - preferably paraffin 60 - pressed and thus produced by compacting a "dust-binder press cake".
  • the pressing process can be carried out every time the vacuum cleaner is switched off or when the collecting container is completely filled.
  • Dust collecting container 26 shown an agitator 110, which is manually but also automatically driven by a rotatable shaft 111.
  • the coarse dust 17 partially or completely covers the blades 112 of the agitator 110.
  • a metering device 113 with the dust binder 114.
  • the binder 114 is continuously (eg during operation) or discontinuous (e.g. after each switch-on or when the dust collector is completely filled), it is metered onto the coarse dust 17.
  • the binder 114 is homogeneously mixed with the dust 17, whereby the binder use can be minimized.
  • the Figures 12a and 12b show the basic schematic structure of another way of dust binding.
  • pads 120 are placed in the dust collection container, which completely cover the floor.
  • the pads 120 consist of at least two components, a first storage medium 121 with dust binder 122 and a second storage medium 123 for the coarse dust 17.
  • the pads 120 are designed as consumables.
  • the material of the first storage medium is porous to coarse-pored, sponge-like and liquid-storing, preferably foam is used. It is impregnated with a liquid dust binder 121.
  • the dust binder 121 is ideally as a liquid with low vapor pressure - such. As glycerol or glycol - before.
  • the second storage medium 123 for the dust must be fluid conducting and storing, coarsely porous, fibrous.
  • Cellulose fibers are preferably used at this point, the fibers being injected into the foam to ensure good contact with the dust binder 121.
  • Cellulose fibers are characterized by a high capillarity, whereby the dust binder 121 is transported from the foam to the surface of the second storage medium 123 in order to wet or bind the dust 17 there, thus avoiding dusting.
  • a "dust cake” forms on the surface of the storage medium 123, see FIG. 4b .
  • the pad 120 is preferably disposed of through the bottom closure 124 of the dust collection container 26 together with the bonded dust 17 without dusting.
  • FIG. 13 3 schematically shows a three-fraction dust separator 160 with a coarse dust container 161 with coarse dust (first fraction 162), a container 163 for the second, middle dust fraction 164, and a particulate matter filter 165 with particulate matter (third fraction 166).
  • the structural design of the entire separator is explained elsewhere.
  • the dust entering the dust collector 160 is separated as follows:
  • the grit 162 mainly comprises particles in the grain size range of more than about 200 ⁇ m, which are collected in the coarse dust container 161. Particles in which the grain size is in the majority in the range of about 30 microns to about 200 microns are collected in the dust collector 163; Particles that are smaller than 30 ⁇ m, are mostly in the fine dust filter 165. In these considerations, it should be noted that the separation limits are blurred. Therefore, the second fraction 164 also includes particulate matter 166, which is known to be dusty during emptying. For the second dust fraction 164, therefore, a dust collecting container 163 is used, with the aid of which and the application of water 170, a hygienic dust removal is possible.
  • FIG. 14 shows the construction of a suitable dust collection container 163 with the dust 164, a dust supply 171 with valve flap 172, a water filling valve 173, a vent valve 174, a chute 175, an outflow opening 176 and a Scblinnzu arrangement 177.
  • Water 170 is ideal for binding dust.
  • the dust 164 in the dust collecting container 163 may be mixed with the dust 164 by shaking the container 163.
  • the chute 175 with the outflow opening 176 is in the in the FIG. 14 closed position shown and the vent valve 174 is not actuated, ie closed.
  • FIG. 15 shows the accumulation bin 163 during the draining process.
  • a water-dust mixture is formed, which can be emptied by pivoting the chute 175 via the outflow opening 176 and the funnel-shaped chute feed 177.
  • the added amount of water should be such that a good flowable mixture is formed.
  • the vent valve 174 must be opened.
  • the inner walls of the dust collector 163 and all other items are treated or coated with a non-stick layer (lotus flower effect). To be able to empty the containers 161 and 163 separately, they are formed separable. To avoid confusion optical differences, especially versions in different colors are advisable.
  • the use of water 170 as a dust binder has the advantage that the dust 164 without the use of a special material binder hygienic, ie can be disposed of without dusting, so no costly consumable material is necessary.
  • particulate matter filter 400 is connected downstream of the above Staubabscheide systems. Regardless of the embodiment as a centrifugal separator / cyclone separator ( FIGS. 1 to 15 ) or Separator according to the mass inertia principle / annular gap separator, the fine dust filter 400 has the task of binding the pre-separator passing particles so that they do not return to the ambient air. According to the Staubabscheide system is constructed such that it has a greater separation limit over conventional systems and thus collects only dust to about 30 microns. The dust, which is smaller than 30 microns, hereinafter referred to as fine dust, passes in majority in the fine dust filter 400.
  • FIGS. 16 and 17 explain the basic structure of the proposed filter system, which preferably has the shape of a cuboid cassette.
  • a frame-shaped or rectangular wide-open and two-sided open holder 401 contains the front and rear side filter media 402 and 403. Further, the air supply 404 is arranged for the exhaust air from the Staubabscheide system in the top of the holder 401.
  • the holder 401 is preferably designed as a rectangular folding frame.
  • As a further alternative solution is proposed to perform the holder 401 as circumferentially closed, air-permeable, porous or also filtering hollow body, in which the filter medium 402 and 403 is used, wherein the filter properties of filtering holder 401 and inside filter medium 402 and 403 can distinguish.
  • the holder 401 may preferably consist of sintered plastic or a comparable material.
  • the cartridge-shaped filter geometry are adapted to the given space requirements of a commercially available vacuum cleaner and should be in the range of a standard packaging for vacuum cleaner filter bags, about 170 mm x 230 mm x 85 mm H x W x D.
  • FIG. 18 and FIG. 19 show in detail an embodiment of the first alternative solution
  • Figure 29 shows a further embodiment of this alternative.
  • FIG. 18 shows the fine dust filter 400 in plan view with the filter medium 402 and 403 and the air supply 404.
  • the filter medium 402, 403 consists of a highly storable mat-shaped, preferably an electrostatically charged synthetically produced or natural filter fleece, wherein the mat thickness about 10 to 20 mm. The electrostatic charge takes place during the production process of the filter fleece.
  • the air feed 404 is preferably designed as a slot in order to ensure optimum flow of the filter medium 402, 403.
  • FIG. 19 again shows the between the filter medium 402, 403 and the air supply 404 located filter material-free cavity 405. Furthermore, the exhaust air flow from the Staubabscheide system symbolized by the arrows 406.
  • the filter arrangement can be further improved if there is cotton wool or a cotton-like material in the cavity 405 between the two filter media 402, 403. Experiments have shown that especially smaller particles ⁇ 15 microns can be well bound or stored in cotton wool.
  • FIG. 20 describes a further variant in plan view.
  • the filter medium 402, 403 here consists of a highly storable thin, preferably electrostatically charged, synthetically produced or natural filter fleece, wherein the thickness of the nonwoven layer is now about 4 to 7 mm.
  • the filter fleece 402, 403 In order to achieve a comparable dust absorption capacity with low flow losses, the filter fleece 402, 403 must be folded or pleated in this embodiment.
  • the "pleating angle" ⁇ is about 30 °. The pleating creates a large filter surface.
  • the capacity is essentially achieved by a high depth storage.

Abstract

A method for treating dust including: separating, in a vacuum cleaner, the dust into at least two fractions which differ in at least one of a size and a mass of particles of the dust; and adding a dust-binding agent to at least a first of the fraction.

Description

Die vorliegende Erfindung betrifft ein Verfahren zur Behandlung von Staub in einem Staubsauger. Darüber hinaus betrifft die Erfindung verschiedene Vorrichtungen zur Durchführung eines solchen Verfahrens.The present invention relates to a method of treating dust in a vacuum cleaner. Moreover, the invention relates to various devices for carrying out such a method.

Bei Staubsaugern, insbesondere bei Bodenstaubsaugem, kommen Staubrückhaltesysteme zum Einsatz, die in der Regel zwischen dem Lufteinlass eines Staubsammelraums und der Saugseite eines Gebläses angeordnet sind und den aufgenommenen Staub vor dem Eintritt in das Gebläse zurückhalten. Die bekannteste Variante ist ein als Beutel geformter Filter, welches innenbeaufschlagt ist, d. h., der Staub lagert sich im Inneren des Beutels ab. Dem Beutel ist in der Regel noch ein Feinstaubfilter nachgeschaltet, welcher Staubpartikel in der Größenordnung von weniger als 2 µm aufnimmt, die den Beutel passieren. Die Entfernung dieses Staubanteils aus der Raumluft gewinnt mit der ansteigenden Zahl von Allergikern an Bedeutung, da diese Partikel wegen ihrer geringen Größe lungengängig sind und deshalb zu einer gesundheitlichen Belastung führen. Bei Erreichen der maximalen Aufnahmekapazität, die bei ca. 400 Gramm liegt, muss der Beutel ausgetauscht werden, dies kann insbesondere bei verschließbaren Beuteln hygienisch erfolgen, da der Staub im Beutel bleibt und mit diesem entsorgt wird. Ein solcher Austausch ist je nach Gebrauchsgewohnheit mehrmals im Jahr erforderlich und verursacht Kosten. Auch der Feinstaubfilter muss nach einer gewissen Nutzungszeit ausgetauscht werden, hier sind jedoch die Intervalle wegen der geringen Menge des Feinstaubs größer, von den Herstellern wird ein Austausch nach ca. einem Jahr empfohlen. Wegen der geringen Partikelgrößen entsteht ein kleiner Masseanteil an Feinstaub, deshalb besitzen handelsübliche Feinstaubfilter ein Fassungsvermögen von etwa 10 Gramm.In vacuum cleaners, in particular vacuum cleaner, dust retention systems are used, which are usually arranged between the air inlet of a dust collection chamber and the suction side of a fan and hold back the absorbed dust before entering the fan. The best known variant is a bag shaped filter which is internally pressurized, d. h., the dust settles inside the bag. The bag is usually still downstream of a fine dust filter, which receives dust particles in the order of less than 2 microns, which pass through the bag. The removal of this dust content from the room air wins with the increasing number of people with allergies in importance, as these particles are respirable because of their small size and therefore lead to a health burden. When reaching the maximum capacity, which is about 400 grams, the bag must be replaced, this can be hygienic especially with closable bags, as the dust remains in the bag and is disposed of with this. Such replacement is required several times a year, depending on usage, and incurs costs. Also, the fine dust filter must be replaced after a certain period of use, but here are the intervals because of the small amount of fine dust larger, from the manufacturers, a replacement after about a year is recommended. Because of the small particle sizes, a small proportion by mass of fine dust is produced, which is why commercially available fine dust filters have a capacity of about 10 grams.

In manchen Kleinstsaugern, Mehrzwecksaugern oder Gewerbegeräten gibt es außenbeaufschlagte Filter, die das Gebläse umgeben. Der Vorteil ist die größere Aufnahmekapazität, der Nachteil besteht darin, dass die Filter dieser Staubsauger nur für Grobstaub ausgelegt sind, der Feinstaub, welcher allergieauslösende Pollen und Mikroorganismen beinhaltet, passiert den Filter und wird vom Gebläse in den Raum zurückgeblasen und dabei sogar aufgewirbelt.In some micro-cleaners, multi-purpose vacuum cleaners or commercial appliances, there are external filters surrounding the blower. The advantage is the greater absorption capacity, the disadvantage is that the filters of this vacuum cleaner are designed only for coarse dust, the particulate matter, which allergenic pollen and microorganisms includes, passes through the filter and is blown back into the room by the fan and even stirred up.

Es besteht der Wunsch nach einem wiederverwendbaren Filtersystem für Grobstaub, welches folgende Eigenschaften besitzt:

  • kompakter Aufbau;
  • eine dem Staubbeutel vergleichbare Filterleistung;
  • hygienische Entnahmemöglichkeit des gesammelten Staubs;
  • geringe Saugleistungsverluste.
There is a desire for a reusable filter system for coarse dust which has the following properties:
  • compact construction;
  • a filter bag performance comparable to the dust bag;
  • hygienic removal of the collected dust;
  • low suction power losses.

Hier sind im Wesentlichen folgende Systeme bekannt:

  1. 1. auswaschbare und wiederverwendbare Textilfilterbeutel ( DE 199 11 331 C1 );
    hier bestehen in erster Linie Bedenken hinsichtlich der Hygiene, da die stark verunreinigten Beutel zunächst manuell geleert und anschließend in der Waschmaschine gewaschen werden müssen;
  2. 2. Staubkassetten aus porösem Sintermaterial ( EP 1 179 312 A2 );
  3. 3. Fliehkraftabscheider, sogenannte Zyklone ( EP 0 647 114 B1 );
Essentially the following systems are known here:
  1. 1. Washable and reusable textile filter bags ( DE 199 11 331 C1 );
    Here, there are primarily hygiene concerns, since the heavily contaminated bags must first be manually emptied and then washed in the washing machine;
  2. 2. Dust cassettes made of porous sintered material ( EP 1 179 312 A2 );
  3. 3. Centrifugal separator, so-called cyclones ( EP 0 647 114 B1 );

Die beiden letztgenannten Systeme bieten die Möglichkeit, den Staubsammelbehälter einfach zu entnehmen, zu entleeren und bei Verschmutzung zu reinigen. Bei handelsüblichen Systemen, insbesondere bei den Fliehkraftabscheidern, wird bisher versucht, die von den Staubbeuteln bekannte Staubabscheidung nachzubilden. Aus diesem Grund ist die Trenngrenze der Abscheider sehr klein, aufgrund der unscharfen Trennung befinden sich deshalb große Mengen von lungengängigem Feinstaub in den Staubsammelbehältern. Das Entleeren dieser Behälter führt dann dazu, dass die leichteren Bestandteile des ausgeschütteten Staubs auffliegen und sich in der Luft verteilen. Hierdurch werden insbesondere Allergiker belastet. Ein Verfahrem gemäß dem Oberbegriff des Unabhängigen Anspruchs ist aus DE-U-202004003494 bekannt.The latter two systems offer the possibility to easily remove the dust collector, empty and clean when dirty. In commercially available systems, in particular in the centrifugal separators, attempts have been made to emulate the dust separation known from the anthers. For this reason, the separation limit of the separator is very small, because of the fuzzy separation are therefore large amounts of respirable particulate matter in the dust collection containers. The emptying of these containers then causes the lighter components of the dumped dust to fly up and spread in the air. As a result, in particular allergy sufferers are charged. A method according to the preamble of the independent claim is out DE-U-202004003494 known.

Es ist daher Aufgabe der vorliegenden Erfindung ein Verfahren zur Behandlung von Staub zu schaffen, bei dem die Entsorgung unter Hygienegesichtspunkten verbessert ist.It is therefore an object of the present invention to provide a method for the treatment of dust, in which the disposal is improved from a hygiene point of view.

Diese Aufgabe wird durch ein Verfahren mit den Merkmalen des Anspruches 1 gelöst.This object is achieved by a method having the features of claim 1.

Erfindungsgemäß wird der Staub in mindestens zwei Fraktionen getrennt, welche sich durch die Größe oder Masse der Staubpartikel unterscheiden, und einer Fraktion wird ein Staubbindemittel zugegeben, so dass der Staub nicht nur lose in einem Staubsammelraum abgelegt wird, sondern eine gewisse Bindung und Vernetzung erfährt und bei der Entleerung des Staubsammelraumes keine Verwirbelung stattfindet. Die Belastung durch Feinstaub, pathogene Partikel oder andere Schadstoffe ist dadurch reduziert und der Umgang mit dem Staubsammelraum, der in regelmäßigen Intervallen geleert werden muss, wird deutlich hygienischer und der Inhalt des Staubsammelraumes kann als Gemisch, z.B. als Klumpen, auf einmal entsorgt werden.According to the invention, the dust is separated into at least two fractions, which differ by the size or mass of the dust particles, and a dust binder is added to a fraction, so that the dust is not only loosely deposited in a dust collection room, but experiences some bonding and cross-linking and during the emptying of the dust collecting space no turbulence takes place. The burden of particulate matter, pathogenic particles or other pollutants is thereby reduced and the handling of the dust collection chamber, which must be emptied at regular intervals, becomes significantly more hygienic and the contents of the dust collection chamber can be used as a mixture, e.g. as lumps, to be disposed of at once.

Die Fraktion, deren Staubpartikel mehrheitlich kleiner sind als die Fraktion, der ein Staubbindemittel zugegeben wird, wird dann von einem Feinstaubfilter aufgenommen. Hierdurch wird vermieden, dass Partikel dieser Fraktion wieder an die Raumluft zurückgegeben und dort verwirbelt werden.The fraction whose dust particles are mostly smaller than the fraction to which a dust binder is added is then taken up by a fine dust filter. This avoids that particles of this fraction are returned to the room air and swirled there.

Bei einer besonders vorteilhaften Ausführungsform wird der Staub in drei Fraktionen getrennt, welche sich durch die Größe und/oder Masse der Staubpartikel unterscheiden, und der Fraktion mit Staubpartikeln, welche mehrheitlich mittlere Größe oder Masse besitzen, wird ein Staubbindemittel zugegeben. Die erste Fraktion, die nur grobe Teile enthält, kann ohne jegliches Aufstauben auch ohne Bindemittel entleert werden. Daher wird nur für die mittlere Fraktion ein Staubbindemittel benötigt. Die zur Bindung benötigte Menge kann dabei gegenüber Verfahren, die die ersten beiden Fraktionen in einem Behälter sammeln, erheblich reduziert werden.In a particularly advantageous embodiment, the dust is separated into three fractions, which differ by the size and / or mass of the dust particles, and a dust binder is added to the fraction with dust particles, which have a majority of medium size or mass. The first fraction, containing only coarse particles, can be emptied without any dusting even without binder. Therefore, a dust binder is needed only for the middle fraction. The amount required for binding can be significantly reduced compared to methods that collect the first two fractions in a container.

Dabei sollten die Einrichtungen, mit denen der Staub getrennt wird, derart dimensioniert werden, dass die erste Fraktion mehrheitlich Staubpartikel mit einer Größe von mehr als 200 µm enthält, dass die zweite Fraktion mehrheitlich Staubpartikel mit einer Größe zwischen 200 µm und 30 µm enthält und dass eine dritte Fraktion mehrheitlich Staubpartikel mit einer Größe von weniger als 30 µm enthält. Die Partikel der dritten Fraktion sind mit 30 µm teilweise noch sehr groß, was wiederum einen Feinstaubfilter mit sehr großer Aufnahmekapazität bedingt. Hierdurch wird aber erreicht, dass in der zweiten Fraktion auch bei einer unscharfen Trennung nur sehr wenig lungengängige Feinstaubpartikel vorhanden sind. Dies stellt sicher, dass Benutzer beim Entleeren des Behälters für die zweite Fraktion auch dann nicht oder nur gering gefährdet sind, wenn sie sich gegen die Benutzung eines Staubbindemittels entscheiden oder dessen Zugabe vergessen haben.Here, the facilities with which the dust is separated, should be dimensioned so that the first fraction contains a majority of dust particles with a size of more than 200 microns, that the second fraction contains a majority of dust particles with a size between 200 microns and 30 microns and that a third fraction contains a majority of dust particles with a size of less than 30 microns. Particles of the third fraction are still very large at 30 μm, which in turn causes a particulate matter filter with a very large absorption capacity. In this way, however, it is achieved that in the second fraction, even with a blurred separation, only very few respirable particulate matter particles are present. This ensures that users are not or only slightly at risk when emptying the container for the second fraction, even if they have decided against the use of a dust binder or forgot its addition.

Ein geeigneter Feinstaubfilter sollte mindestens eine Speicherkapazität von 200 Gramm besitzen. Da aufgrund der Trenngrenze von 30 µm relativ große und massereiche Partikel in den Feinstaubfilter gelangen, wäre ein handelsüblicher Filter mit einer Aufnahmekapazität von 10 Gramm schnell erschöpft. Dies widerspräche dem Gedanken eines Staubsaugers, welcher kein oder nur wenig Verbrauchsmaterial benötigen soll. Aus diesem Grund wird eine Filterkapazität gewählt, welche bei normalen Nutzungsgewohnheiten eine Standzeit von mehr als einem Jahr gewährleistet. Neben der erhöhten Standzeit wird noch der Vorteil eines geringen Strömungsverlustes von nur ca. 20% (am Ende der Standzeit, bezogen auf den Ausgangszustand) erzielt. Der Einsatz eines solchen Filters erfolgt vorzugsweise bei einem Staubsauger, bei dem ein Staubbindemittel für die nächstgrößere Fraktion verwendet wird. Ein Einsatz eines solchen Filters ist aber auch ohne Staubbindemittel möglich, insbesondere dann, wenn die Trenngrenzen des Staubabscheide-Behälters so scharf sind, dass die nächstgrößere Fraktion keine lungengängigen Partikel enthält.A suitable fine dust filter should have at least a storage capacity of 200 grams. Since due to the separation limit of 30 microns relatively large and massive particles enter the fine dust filter, a commercial filter with a capacity of 10 grams would quickly exhausted. This would contradict the idea of a vacuum cleaner, which should require little or no consumables. For this reason, a filter capacity is selected which guarantees a service life of more than one year under normal usage conditions. In addition to the increased service life, the advantage of a low flow loss of only about 20% (at the end of the service life, based on the initial state) is achieved. The use of such a filter is preferably carried out in a vacuum cleaner in which a dust binder for the next larger fraction is used. However, a use of such a filter is also possible without a dust binder, especially when the separation limits of the dust collecting container are so sharp that the next largest fraction contains no respirable particles.

Es ist auch vorteilhaft, wenn die Zugabe des Staubbindemittels in einem in den Staubsauger einsetzbaren und von dort entnehmbaren Staubsammelbehälter erfolgt. Hierdurch ist einerseits eine einfache Entleerung des Konglomerats aus Staub und Staubbindemittel ohne zusätzliche Behälter möglich, andererseits wird eine einfache Reinigung des Staubsammelbehälters ermöglicht.It is also advantageous if the addition of the dust binder is carried out in a usable in the vacuum cleaner and removable from there dust collector. This is on the one hand a simple emptying of the conglomerate of dust and dust binder without additional containers possible, on the other hand, a simple cleaning of the dust collector is possible.

Bezüglich anderer zweckmäßiger oder sogar vorteilhafter Gestaltungsformen des erfindungsgemäßen Verfahrens wird auf die weiteren abhängigen Ansprüche 6 bis 18 verwiesen.With regard to other expedient or even advantageous embodiments of the method according to the invention, reference is made to the further dependent claims 6 to 18.

Die Erfindung wird nachfolgend anhand von mehreren Ausführungsbeispielen mit Bezug auf die beigefügten Zeichnungen näher erläutert. Es zeigen:

Figur 1
eine schematische Ansicht eines Ausführungsbeispiels eines erfindungsge- mäßen Staubsaugers;
Figur 2
eine perspektivische Ansicht des Staubsammelraumes des Staubsaugers der Figur 1 in Explosionsdarstellung;
Figur 3
eine Draufsicht auf den Staubsauger der Figur 1;
Figur 4
eine geschnittene Seitenansicht eines Staubsammelraumes mit Dosierein- richtung;
Figur 5
eine teilweise geschnittene Ansicht eines weiteren Ausführungsbeispiels eines Staubsammelraumes mit Dosiereinrichtung;
Figur 6
eine teilweise geschnittene Ansicht eines weiteren Ausführungsbeispiels eines Staubsammelraumes mit Heizeinrichtung;
Figur 10
einen Staubsammelbehälter mit Pressvorrichtung;
Figur 11
einen Staubsammelbehälter mit Rührwerk;
Figuren 12a, b
eine weitere Alternative der Staubbindung;
Figur 13
die Schemaskizze eines Drei-Fraktionen-Staubabscheiders;
Figur 14
einen Staubsammelbehälter mit Wasserzuführung;
Figur 15
den Staubsammelbehälter gemäß Figur 17 beim Entleerungsvorgang;
Figuren 16, 17
den prinzipiellen Aufbau eines Feinstaubfilters;
Figuren 18, 19
detailliert eine erste Ausführungsform des Feinstaubfilters in Draufsicht und Seitenansicht
Figur 20
eine zweite Ausführungsform des Feinstaubfilters in Draufsicht.
The invention will be explained in more detail below with reference to several embodiments with reference to the accompanying drawings. Show it:
FIG. 1
a schematic view of an embodiment of an inventive vacuum cleaner;
FIG. 2
a perspective view of the dust collection chamber of the vacuum cleaner FIG. 1 in exploded view;
FIG. 3
a plan view of the vacuum cleaner FIG. 1 ;
FIG. 4
a sectional side view of a dust collection room with dosing;
FIG. 5
a partially sectioned view of another embodiment of a dust collecting space with metering device;
FIG. 6
a partially sectioned view of another embodiment of a dust collection chamber with heater;
FIG. 10
a dust collecting container with pressing device;
FIG. 11
a dust collector with stirrer;
FIGS. 12a, b
another alternative of dust binding;
FIG. 13
the schematic of a three-fraction dust collector;
FIG. 14
a dust collector with water supply;
FIG. 15
the dust collector according to FIG. 17 during the emptying process;
FIGS. 16, 17
the basic structure of a fine dust filter;
FIGS. 18, 19
detailed a first embodiment of the particulate filter in plan view and side view
FIG. 20
a second embodiment of the particulate filter in plan view.

Die Figur 1 zeigt rein schematisch einen Staubsauger 1 im Längsschnitt. Der Staubsauger 1 besitzt in bekannter Weise ein Gehäuse 2, welches in einen Gebläseraum 3 und einen Staubsammelraum 4 unterteilt ist. Der Staubsammelraum 4 wird durch einen schwenkbaren Deckel 5 verschlossen und besitzt eine erste Öffnung 6, in die die Kupplung 7 eines Saugschlauchs 8 mündet. An den Saugschlauch 8 können unter eventueller Zwischenschaltung eines Saugrohrs (nicht dargestellt) verschiedene Saugvorsätze (ebenfalls nicht dargestellt) angeschlossen werden. Eine zweite Öffnung 9 ist in der Trennwand 10 zwischen Staubsammelraum 4 und Gebläseraum 3 angeordnet. Hinter dieser Öffnung 9 befindet sich ein Feinstaubfilter 11. Dahinter ist in dem Gebläseraum 3 ein Motorgebläse 12 angeordnet, welches mit seiner Saugseite zum Feinstaubfilter 11 bzw. zur Öffnung 9 gerichtet ist und mit seiner Ausblasseite über weitere Öffnungen 18 - evtl. mit vorgeschaltetem Filter (nicht dargestellt) - mit der Umgebungsluft 13 verbunden. Über dem Gebläseraum ist ein Aufnahmeraum 14 für eine Gerätesteuerung und Bedien- und Anzeigeelemente (siehe Figur 3) angeordnet. Beim Einschalten des Gebläses 12 wird in bekannter Weise die staubbeladene Luft, in der Figur durch den Pfeil 16 symbolisiert, über den Saugschlauch 8 durch den Staubsammelraum 9 geleitet. Um dort den Grobstaub 17 zu separieren, ist dort in ebenfalls bekannter Weise ein staubbeutelloses Staubsammelsystem eingesetzt. Im dargestellten Ausführungsbeispiel ist dies ein Fliehkraftabscheider 20, die eingangs genannten Varianten Massenträgheitsabscheider oder Staubkassette sind ebenfalls denkbar. Der verwendete Abscheider ist derart dimensioniert, dass innerhalb des Staubsammelbehälters eine Fraktion gesammelt wird, deren Bestandteile mehrheitlich größer als 30 µm sind.The FIG. 1 shows purely schematically a vacuum cleaner 1 in longitudinal section. The vacuum cleaner 1 has in a known manner a housing 2 which is divided into a fan chamber 3 and a dust collecting space 4. The dust collecting space 4 is closed by a pivotable cover 5 and has a first opening 6 into which the coupling 7 of a suction hose 8 opens. With the possible interposition of a suction tube (not shown) to the suction hose 8 different Saugvorsätze (also not shown) can be connected. A second opening 9 is in the partition 10 between Dust collecting space 4 and 3 blower chamber arranged. Behind this opening 9 is a fine dust filter 11. Behind it, a motor fan 12 is arranged in the fan chamber 3, which is directed with its suction side to the fine dust filter 11 and the opening 9 and with its outlet side via further openings 18 - possibly with upstream filter ( not shown) - connected to the ambient air 13. Above the fan room is a receiving space 14 for a device control and operating and display elements (see FIG. 3 ) arranged. When you turn on the fan 12, the dust-laden air, symbolized in the figure by the arrow 16, passed through the suction hose 8 through the dust collection chamber 9 in a known manner. In order to separate there the coarse dust 17, there is also used in a known manner, a dust bagless dust collection system. In the illustrated embodiment, this is a centrifugal separator 20, the aforementioned variants Massenträgheitsabscheider or dust cassette are also conceivable. The separator used is dimensioned such that a fraction is collected within the dust collection container, the majority of which are greater than 30 microns.

Figur 2 zeigt den Fliehkraftabscheider 20 als Einzelheit. Er umfasst einen Zyklonkegel 21, der mit einer Luftzuführung 22 und einer Luftabführung 23 versehen ist. Die Luftzuführung 22 steht strömungsmäßig mit der Öffnung 6 in Verbindung, die Luftabführung 23 über die Leitung 15 mit der Öffnung 9 (s. Figur 1). Der Zyklonkegel 21 wird in einen zylindrischen Behälter 24 eingesetzt, der, wie in der Figur gezeigt, in eine rohrförmige Halterung 25 und einen darunter angeordneten Staubsammelbehälter 26 unterteilt sein kann. Die angesaugte staubbeladene Luft wird im Zyklonkegel 21 in eine Drehbewegung versetzt, so dass nach dem Fliehkraftprinzip der Grobstaub 17 an die Außenwand gedrückt wird und nach unten in den Staubsammelbehälter 26 fällt. Im weiteren Luftweg wird dann noch der Feinstaub durch den Feinstaubfilter 11 abgeschieden. Ist der Behälter 26 gefüllt, was über Füllstands-, Druck oder Staubmengensensoren oder einfach durch Messung der Einschaltzeiten des Gebläses ermittelt werden kann (nicht dargestellt), wird dies dem Benutzer über eine Anzeigevorrichtung 35 (s. Figur 3) mitgeteilt. FIG. 2 shows the centrifugal separator 20 as a detail. It comprises a cyclone cone 21, which is provided with an air feed 22 and an air discharge 23. The air supply 22 is in fluid communication with the opening 6, the air discharge 23 via the line 15 with the opening 9 (s. FIG. 1 ). The cyclone cone 21 is inserted into a cylindrical container 24, which, as shown in the figure, can be divided into a tubular holder 25 and a dust collecting container 26 arranged underneath. The sucked dust-laden air is set in the cyclone cone 21 in a rotational movement, so that according to the principle of centrifugal force of the coarse dust 17 is pressed against the outer wall and falls down into the dust collector 26. In the further airway then the fine dust is separated by the fine dust filter 11. If the container 26 is filled, which can be determined via fill level, pressure or dust quantity sensors or simply by measuring the switch-on times of the blower (not shown), this is indicated to the user via a display device 35 (see FIG. FIG. 3 ).

Figur 3 zeigt die Draufsicht auf einen erfindungsgemäß ausgebildeten Staubsauger 1. Hier sind in einem Bedienfeld 30 neben den bekannten Bedien- und Anzeigeelementen wie Ein-/Ausschalter 31, Wechselanzeige 32 für den Feinstaubfilter 11, Kabelaufrolltaste 33 und Leistungssteller 34 weitere Elemente vorgesehen, deren Funktion später erklärt ist. Unter anderem kann dies die vorbeschriebene Anzeige 35 zum Entleeren des Staubsammelbehälters 26 sein. In den folgenden Ausführungsbeispielen (Figuren 4 und 5) wird zur Aktivierung der Wechselanzeige ein aus der EP 0 759 157 B1 bekannter Piezosensor verwendet, welcher an die Gerätesteuerung - in der Figur durch den gestrichelten Kasten 36 symbolisch angedeutet - ein Signal gibt, das mit der aufgesaugten Staubmenge korreliert. Der Benutzer kann dann den Staubsammelbehälter 26 vom Rest des Fliehkraftabscheiders 20 trennen und den Grobstaub 17 entleeren. Hier setzt die Erfindung ein: FIG. 3 shows the top view of an inventively designed vacuum cleaner 1. Here are in a control panel 30 next to the known control and display elements such as on / off switch 31, change indicator 32 for the fine dust filter 11, cable rewind button 33 and power controller 34 more elements provided, the function explained later is. Among other things, this may be the above-described display 35 for emptying the dust collector 26. In the following embodiments ( FIGS. 4 and 5 ) is activated to activate the change indicator from the EP 0 759 157 B1 known piezosensor used, which to the device control - symbolically indicated in the figure by the dashed box 36 - is a signal that correlates with the absorbed amount of dust. The user can then do the Separate dust collector 26 from the rest of the centrifugal separator 20 and empty the coarse dust 17. This is where the invention begins:

Um ein Aufstauben des Grobstaubs beim Entleeren des Staubsammelbehälters zu vermeiden, wird diesem ein Staubbindemittel zugegeben. Ein Staubbindemittel im Sinne der Erfindung stellt ein ein- oder mehrkomponentiges Additiv dar, welches in fester und/oder flüssiger und/oder gasförmiger Phase vorliegt, wobei die Phase ggf. veränderbar ist, um den in loser ungebundener Form vorliegenden aufgesaugten Staub zu durchdringen, zu vermischen und zumindest teilweise eine Bindung des Staubes vorzunehmen. Das Staubbindemittel soll neben dem Grobstaub insbesondere auch den im Staubsammelbehälter vorhandenen Feinstaub, Keime, Bakterien, Pollen und andere Schadstoffe binden, um bei der Entsorgung eine Verwirbelung und die daraus resultierende Belastung für den Benutzer zu vermeiden. Dadurch kann der gefüllte Staubsammelraum auf hygienische Weise entleert werden, ohne dass es zu einem Aufstauben kommt. Als Staubbindemittel können entsprechend geeignete dispergierbare Flüssigkeiten, Pulver, Schaum, Granulat oder feste, insbesondere tablettenförmig gepresste Stoffe verwendet werden. Außerdem können dem Staubbindemittel Duftstoffe, reinigende oder keimhemmende Substanzen zugesetzt sein. Die Zugabe des Staubbindemittels in den Staubsammelbehälter erfolgt durch eine dafür geeignete Vorrichtung, die entweder innerhalb des Staubsaugers oder in einem Saugvorsatz integriert ist oder als externe Apparatur mit einer Aufnahme für den Staubsammelbehälter ausgebildet ist.In order to avoid dusting of the coarse dust when emptying the dust collector, a dust binder is added to this. A dust-binding agent in the context of the invention is a one- or multi-component additive which is present in solid and / or liquid and / or gaseous phase, the phase being possibly variable in order to penetrate the sucked-up dust present in loose, unbound form mix and at least partially make a binding of the dust. In addition to the coarse dust, the dust binder is also intended to bind the fine dust, germs, bacteria, pollen and other pollutants present in the dust collector in order to avoid turbulence and the resulting burden on the user when disposed of. As a result, the filled dust collection chamber can be emptied in a hygienic manner, without resulting in dusting. Suitable dust-dispersing agents which can be used are suitably dispersible liquids, powders, foams, granules or solid, in particular tablet-shaped, pressed substances. In addition, the dust binder fragrances, cleansing or germ-inhibiting substances may be added. The addition of the dust binder in the dust collection container by means of a suitable device which is integrated either within the vacuum cleaner or in a suction attachment or is designed as an external apparatus with a receptacle for the dust collector.

In den Figuren 4 und 5 sind Ausführungsbeispiele von Staubsammelbehältern gezeigt, in denen ein Staubbindemittel zugegeben und mit dem Staub vermengt wird. Als Staubbindemittel kann eine Flüssigkeit, Pulver, Schaum oder Granulat verwendet werden, auch Mischformen sind denkbar. Insbesondere bei der Verwendung von Granulat sollte diesem ein Stoff zugesetzt werden, welcher die Anhaftung des Staubs verbessert. Ferner kann das Staubbindemittel mit Mitteln angereichert sein, die eine reinigende Wirkung besitzen, beispielsweise durch Beigabe von Tensiden oder ähnlichen die Reinigung fördernde Substanzen. Auch bakterizide, bakteriostatische, und/oder fungizide Mittel können beigegeben werden, um eine Verkeimung innerhalb des Staubsammelbehälters zu vermeiden. Diese Eigenschaften werden beispielsweise durch die Dotierung des Materials mit Silberionen erreicht. Ferner können Duftstoffe eingesetzt werden, um den Umgang mit dem Staubsammelraum angenehmer zu machen.In the FIGS. 4 and 5 Embodiments of dust collection containers are shown in which a dust binder is added and mixed with the dust. As a dust binder, a liquid, powder, foam or granules can be used, mixed forms are conceivable. In particular, when using granules should this be added to a substance which improves the adhesion of the dust. Furthermore, the dust-binding agent may be enriched with agents which have a cleaning action, for example by adding surfactants or similar cleaning-promoting substances. Bactericidal, bacteriostatic, and / or fungicidal agents may also be added to prevent microbial contamination within the dust collector. These properties are achieved, for example, by doping the material with silver ions. Furthermore, fragrances can be used to make the handling of the dust collection room more pleasant.

Das Staubbindemittel muss zur Erfüllung seiner Funktion im Sinne der Erfindung mit dem Staub in Kontakt treten, wobei folgende mögliche Varianten zur Dosierung bestehen:

  • • Das Staubbindemittel wird vom Benutzer direkt in den Staubsammelbehälter dosiert. Diese Möglichkeit ist äußerst kostengünstig realisierbar, da keine zusätzlichen aktiven Wirkelemente in den Staubsauger eingebaut werden müssen, wobei nachteilig ist, dass der Verbraucher mit dem eingesaugten Staub in Kontakt kommen kann, bevor dieser gebunden ist. Um diesen Nachteil zu beseitigen, kann das Staubbindemittel durch Einschalten des Gebläses in den Staubsammelbehälter eingesaugt werden.
  • • Das Staubbindemittel wird über eine Dosiervorrichtung in den Staubsammelbehälter gegeben, wobei die Aktivierung über am Staubsauger, am Saugvorsatz oder an der externen Apparatur angeordnete Betätigungsmittel erfolgt.
  • • Das Staubbindemittel wird automatisch vom Staubsauger oder vom Saugvorsatz dosiert. Dies kann bei eingeschaltetem Gebläse durch entsprechende Dosiereinrichtungen im Bereich der Luftzuführung erfolgen, oder direkt in den Staubsammelbehälter.
  • • Das Staubbindemittel wird am Anfang eines Saugprozesses dosiert, wobei entweder die für den Staubsammelbehälter notwendige Menge nach Entleerung einmalig zugegeben wird oder über mehrere Teilschnitte eine Dosierung erfolgt. Ferner kann die Zugabe des Staubbindemittels auch nach dem Saugvorgang erfolgen. Die Aktivierung der hierzu notwendigen Dosiervorrichtung bezüglich der Menge, des Zugabezeitpunkts und/oder der Zugabefrequenz kann zeit-, füllstands- oder staubmengengesteuert sein. Hierzu können die gleichen Vorrichtungen benutzt werden wie zur eingangs beschriebenen Wechselanzeige.
  • • Das Staubbindemittel wird automatisch beim Einsetzen des Staubsammelbehälter zugegeben.
The dust-binding agent must come into contact with the dust in order to fulfill its function within the meaning of the invention, the following possible variants for metering consisting:
  • • The dust binder is metered by the user directly into the dust collector. This possibility is extremely inexpensive to implement, since no additional active active elements must be installed in the vacuum cleaner, which is disadvantageous that the consumer can come in contact with the dust sucked in before it is bound. To eliminate this disadvantage, the dust binder can be sucked by switching on the blower in the dust collector.
  • • The dust binder is added to the dust collector via a dosing device, whereby the activation takes place via an actuating device arranged on the vacuum cleaner, on the suction attachment or on the external apparatus.
  • • The dust binder is automatically dosed by the vacuum cleaner or the suction attachment. This can be done with the fan on by appropriate metering in the air supply, or directly into the dust collector.
  • • The dust binder is dosed at the beginning of a suction process, whereby either the amount required for the dust collecting container is added once after emptying or dosing takes place over several partial cuts. Furthermore, the addition of the dust binder can also take place after the suction process. The activation of the dosing device required for this purpose with respect to the amount, the time of addition and / or the addition frequency can be controlled in terms of time, level or amount of dust. For this purpose, the same devices can be used as for the change indicator described above.
  • • The dust binder is added automatically when the dust collector is inserted.

Vorteilhaft ist die Verwendung von Mitteln zum Durchmischen von Staub und Staubbindemittel, insbesondere bei der Zugabe des Mittels am Anfang oder am Ende des Saugvorgangs oder bei Zugabe in einer externen Apparatur. Hierzu können mechanische oder motorische Mittel verwendet werden, die den Behälter in Bewegung, Drehung oder Schwingung versetzen.Advantageous is the use of agents for mixing dust and dust binder, in particular when adding the agent at the beginning or at the end of the suction process or when added in an external apparatus. For this purpose, mechanical or motor means can be used, which set the container in motion, rotation or vibration.

In dem in Figur 4 gezeigten Ausführungsbeispiel ist in der Luftzuführung 22 ein Staubmengensensor 41 angeordnet, der die Menge des durchströmenden Staubes erfasst. Ferner ist in der Luftzuführung 22 eine Dosiervorrichtung 42 für Pulver und/oder Granulat als Staubbindemittel 43 vorgesehen. Die vom Staubmengensensor 41 erfasste Menge wird an die Gerätesteuerung 36 weitergegeben, und diese veranlasst bei Vorliegen einer Menge, welche eine Entleerung des Sammelbehälters 26 erforderlich macht, dass das Staubbindemittel über eine Dosierklappe 44 in die Luftzuführung 22 abgegeben und dort mit der noch staubbeladenen Luft verwirbelt wird. Aufgrund der nachfolgenden zyklonartigen Verwirbelung der Luft mit dem Staub 17 und dem Staubbindemittel 43 wird eine optimale Vermischung erreicht. Das Staubbindemittel 43 wird zusammen mit dem Staub 17 in dem Behälter 26 gesammelt und kann dann in regelmäßigen Abständen entsorgt werden. Die Dosierung des Staubbindemittels 43 kann über Klappen, Kolben, Schnecken und/oder Düsen erfolgen. Dabei kann die Zugabe des Staubbindemittels entweder unmittelbar in dem Staubsammelraum 26 oder im Bereich der Luftzuführung 22 erfolgen, z.B. kann die Zugabe bereits an dem Saugvorsatz des Staubsaugers 1 erfolgen (nicht dargestellt).In the in FIG. 4 shown embodiment, a dust amount sensor 41 is arranged in the air supply 22, which detects the amount of dust flowing through. Further, in the air supply 22, a metering device 42 for powder and / or granules as dust binder 43 is provided. The quantity detected by the dust quantity sensor 41 is passed on to the device control 36, and this causes, in the presence of an amount which requires emptying of the collecting container 26, that the dust binder is discharged via a metering flap 44 into the air supply 22 and swirled there with the still dust-laden air becomes. Due to the subsequent cyclone-like turbulence of the air with the dust 17 and the dust binder 43 optimal mixing is achieved. The dust binder 43 is collected together with the dust 17 in the container 26 and can then be disposed of at regular intervals. The metering of the dust binder 43 can take place via flaps, pistons, screws and / or nozzles. The addition of the dust binder can be done either directly in the dust collection chamber 26 or in the region of the air supply 22, for example, the addition can already be done on the suction attachment of the vacuum cleaner 1 (not shown).

In Figur 5 ist eine weitere Ausführungsform eines Staubsammelbehälters 26 dargestellt, bei dem der Grobstaub 17 gebunden wird. Hierfür ist an dem Behälter 26 mindestens eine Sprüheinrichtung 50 vorgesehen, mittels der ein Fluid 52 in den Staubsammelraum 26 abgegeben werden kann. Die Sprüheinrichtung 50 umfasst einen Vorratsbehälter 53, in dem das Fluid 52 als Staubbindemittel angeordnet ist. Ferner sind von der Gerätesteuerung 36 aktivierbare Dosierpumpen 54 vorgesehen, um mittels Schläuchen 55 das flüssige Staubbindemittel 52 in den Staubsammelbehälter 26 zu fördern. Hierfür sind ein oder mehrere Düsen 51 vorgesehen, aus denen das aus den Schläuchen 55 geförderte Fluid 52 in den Staubsammelraum 26 abgegeben und zerstäubt wird. Das dispergierte, staubbindende Fluid 52 ist schematisch durch den Sprühnebel 56 dargestellt. Das Staubbindemittel 52 kann eine glykolhaltige oder glyzerinhaltige Flüssigkeit sein, die die Oberflächenspannung auf Werte von weniger als 40 mN/m reduziert und ggfs. mit fungiziden, bakteriostatischen und/oder bakteriziden Inhaltsstoffen ergänzt ist. Ebenso denkbar ist die Verwendung eines hochverdünnten Klebers, beispielsweise Tapetenkleister. Das flüssige Staubbindemittel 52 sollte vorzugsweise jedoch dispergierbar sein. Anstelle eines Fluids können bei entsprechender Ausbildung der Dosierpumpen und Düsen ebenfalls pulver-, schaum- oder granulatförmige Medien versprüht werden. Zur Dosierung können anstelle der Pumpen 54 auch andere Druck erzeugende Elemente eingesetzt werden. Ferner kann das Staubbindemittel 52 auch über steuerbare Ventile zugeführt und mit Ultraschall dispergiert werden. Die Steuerung der Zuführung des flüssigen Staubbindemittels 52 kann auch hier abhängig von den Daten eines Staubmengensensors 41 erfolgen, alternativ aber auch nach einer der anderen zuvor aufgezählten Varianten. Die Wände des Staubsammelraumes 26 können für eine kostengünstige Herstellung aus Kunststoff gefertigt sein. Es ist natürlich auch möglich, eine antihaftende Beschichtung vorzusehen, um die Reinigung zu erleichtern.In FIG. 5 another embodiment of a dust collection container 26 is shown, in which the coarse dust 17 is bound. For this purpose, at least one spraying device 50 is provided on the container 26, by means of which a fluid 52 can be discharged into the dust collecting chamber 26. The spray device 50 comprises a reservoir 53, in which the fluid 52 is arranged as a dust binder. Furthermore, 36 activatable dosing pumps 54 are provided by the device control to promote by means of hoses 55, the liquid dust binder 52 in the dust collector 26. For this purpose, one or more nozzles 51 are provided, from which the discharged from the hoses 55 fluid 52 is discharged into the dust collecting space 26 and atomized. The dispersed, dust-binding fluid 52 is shown schematically by the spray 56. The dust-binding agent 52 may be a glycol-containing or glycerin-containing liquid which reduces the surface tension to values of less than 40 mN / m and, if appropriate, is supplemented with fungicidal, bacteriostatic and / or bactericidal ingredients. Also conceivable is the use of a highly diluted adhesive, such as wallpaper paste. However, the liquid dust binder 52 should preferably be dispersible. Instead of a fluid can be sprayed with appropriate design of metering pumps and nozzles also powdered, foam or granular media. For metering, other pressure-generating elements may be used instead of the pumps 54. Furthermore, the dust binder 52 can also be supplied via controllable valves and dispersed with ultrasound. The control of the supply of the liquid dust binder 52 can also be done here depending on the data of a dust quantity sensor 41, but alternatively also according to one of the other previously enumerated variants. The walls of the dust collection chamber 26 may be made of plastic for cost-effective production. It is of course also possible to provide an anti-stick coating to facilitate cleaning.

In Figur 6 ist ein Ausführungsbeispiel eines Staubsammelraumes 26 gezeigt, bei dem der Staub 17 durch einen Stoff gebunden wird, der zunächst geschmolzen wird und nach der Aufnahme des Staubs 17 erkaltet und dann aus dem Staubsammelraum 26 entfernt werden kann. Hierzu wird beispielsweise Paraffin 60 verwendet, was dem Behälter als Tablette 61 oder Granulat zugegeben wird. An dem Behälter 26 ist eine Wärmequelle 62 vorgesehen, die über eine Spannungsversorgung 63 mit elektrischer Energie versorgt wird.In FIG. 6 an embodiment of a dust collection chamber 26 is shown, in which the dust 17 is bound by a substance which is first melted and can be cooled after receiving the dust 17 and then removed from the dust collecting space 26. Paraffin 60, for example, is used for this purpose, which is added to the container as tablet 61 or granules. On the container 26, a heat source 62 is provided, which is supplied via a power supply 63 with electrical energy.

Wie in Figur 6 weiter zu sehen ist, befindet sich am Boden des Behälters 26 eine Aufnahme 64 für die Paraffintablette 61. Ferner ist schematisch der Staub 17 dargestellt, der auf der Paraffintablette 61 liegt. In regelmäßigen Abständen kann der Behälter 26 aus dem Staubsauger 1 entnommen und gereinigt werden.As in FIG. 6 can be seen further, is located at the bottom of the container 26, a receptacle 64 for the paraffin tablet 61. Furthermore, the dust 17 is shown schematically, which lies on the paraffin tablet 61. At regular intervals, the container 26 can be removed from the vacuum cleaner 1 and cleaned.

Beim Saugen wird der Hausstaub zunächst mit Hilfe des Fliehkraftabscheiders 20 fraktioniert, wobei Partikel mit einem Durchmesser < 30 µm den Fliehkraftabscheider 20 passieren und in dem Feinstaubfilter 11 gebunden werden. Alle weiteren Staubbestandteile 17 fallen infolge der Gravitation auf das Paraffin 60. Bei einem bestimmten Füllgrad wird die Wärmequelle in Form einer Heizplatte 62 über die Spannungsversorgung 63 mit elektrischer Energie versorgt, wodurch das Paraffin 60 von der festen in die flüssige Phase überführt wird. Es kann auch die Abwärme des Gebläses 12 verwendet werden.When sucking the house dust is first fractionated using the centrifugal separator 20, wherein particles with a diameter <30 microns pass through the centrifugal separator 20 and in the fine dust filter 11 are bound. All other dust components 17 fall due to gravity on the paraffin 60. At a certain degree of filling, the heat source is supplied in the form of a heating plate 62 via the power supply 63 with electrical energy, whereby the paraffin 60 is transferred from the solid to the liquid phase. It can also be the waste heat of the fan 12 are used.

Die Dichte des Paraffins 60 liegt in einer Größenordnung von < 1 g/cm3, etwa im Bereich zwischen 0,5 und 0,7 cm3. Nach dem archimedischen Prinzip werden alle Körper in dem Paraffin 60 versinken, die eine Dichte > ca. 0,8 g/cm3 aufweisen. Diese Bedingungen erfüllen Hausstaubpartikel 17, deren Dichte im Bereich > 1g/cm3 liegt. Aufgrund der Größenverhältnisse der Dichte der einzelnen Stoffe und des relativ einfach zu erreichenden Phasenwechsels der Paraffintablette 61 gelingt es so, den in dem Behälter 26 befindlichen Staub 17 einfach zu binden und in dem Paraffin 60 zu versenken. Wenn der Behälter 26 ausreichend gefüllt ist, kann der abgekühlte Klumpen aus Paraffin 60 und gebundenem Staub 17 ohne Aufstauben entsorgt werden. Insbesondere die unpolare, molekulare Struktur des Paraffins 60 und dessen niedrige Oberflächenspannung sorgt dafür, dass im Gegensatz zu Wasser, Partikel grundsätzlich in der flüssigen Phase des Paraffins 60 leicht einsinken können. Ferner kann der Schmelzpunkt des Paraffins 60 in einem weiten Bereich eingestellt werden.The density of the paraffin 60 is on the order of <1 g / cm 3 , for example in the range between 0.5 and 0.7 cm 3 . According to the Archimedean principle, all bodies will sink into the paraffin 60, which has a density> about 0.8 g / cm 3 . These conditions meet house dust particles 17 whose density is in the range> 1g / cm 3 . Due to the size ratios of the density of the individual substances and the relatively easy-to-reach phase change of the paraffin tablet 61, it is possible to easily bind the dust 17 in the container 26 and sink it into the paraffin 60. If the container 26 is sufficiently filled, the cooled lump of paraffin 60 and bound dust 17 can be disposed of without dusting. In particular, the non-polar, molecular structure of the paraffin 60 and its low surface tension ensures that, in contrast to water, particles can basically sink in easily in the liquid phase of the paraffin 60. Further, the melting point of the paraffin 60 can be set in a wide range.

Damit das ausgehärtete Paraffin 60 leicht aus dem Staubsammelbehälter 26 entfernt werden kann, befindet sich die Paraffintablette 61 in dem Bereich der Aufnahme 64, die aus einem repulsiven (antihaftenden) Material oder einem Material mit einer repulsiven Oberfläche besteht, vorzugsweise Silikon. Aufgrund der besseren Wärmeleitfähigkeit kann die Aufnahme auch aus mit Teflon beschichtetem Aluminium bestehen. Die Aufnahme 64 kann dabei lösbar in dem Behälter 26 aufgenommen sein, um herausgenommen zu werden und durch eine neue Paraffintablette 61 ggf. mit einer neuen Aufnahme 64 ersetzt zu werden.In order for the cured paraffin 60 to be easily removed from the dust collector 26, the paraffin tablet 61 is in the region of the receptacle 64 which is made of a repulsive (anti-sticking) material or material having a repulsive surface, preferably silicone. Due to the better thermal conductivity, the receptacle can also consist of Teflon-coated aluminum. The receptacle 64 may be detachably received in the container 26 to be taken out and replaced by a new paraffin tablet 61 possibly with a new receptacle 64.

Neben Stoffen, deren Phase durch Zuführung von Wärmeenergie veränderbar ist, können auch Substanzen, deren Viskosität durch Bewegungsenergie verändert werden kann - sogenannte tixotrope Stoffe - als Staubbindemittel Verwendung finden. Als Beispiel seien hier Cellulose-Suspensionen genanntIn addition to substances whose phase is variable by supplying heat energy, substances whose viscosity can be changed by kinetic energy - so-called tixotropic substances - can be used as a dust binder. As an example, cellulose suspensions may be mentioned here

Neben den beschriebenen Verfahren zur Applikation des Staubbindemittels - vorzugsweise Paraffin - besteht des weiteren die Möglichkeit, den Staub in das flüssige Paraffin zu pressen, um den Bindemitteleinsatz zu minimieren. Figur 10 zeigt einen Staubsammelbehälter 26, der mit einer solchen Pressvorrichtung 100 ausgerüstet ist. Hierzu wird in dem entnehmbaren Staubsammelbehälter 26 ein Kompressionsstempel 101 angeordnet, der manuell oder auch automatisch, d. h. elektromotorisch oder auch aerodynamisch, angetrieben wird und dadurch auf den Grobstaub 17 bzw. das Bindemittel gepresst. Nach dem Einschalten der Heizplatte 62 wird der Staub in das flüssige Bindemittel - vorzugsweise Paraffin 60 - gepresst und somit durch Verdichten ein "Staub-Bindemittel-Presskuchen" erzeugt. Der Pressvorgang kann nach jedem Ausschalten des Staubsaugers oder bei vollständig gefülltem Sammelbehälter durchgeführt werden.In addition to the described methods of applying the dust binder - preferably paraffin - there is also the possibility of pressing the dust into the liquid paraffin in order to minimize the use of binders. FIG. 10 shows a dust collector 26, which is equipped with such a pressing device 100. For this purpose, a compression ram 101 is arranged in the removable dust collecting container 26, which is manually or automatically, ie electromotively or aerodynamically driven, and thereby pressed onto the coarse dust 17 and the binder. After switching on the heating plate 62, the dust is in the liquid binder - preferably paraffin 60 - pressed and thus produced by compacting a "dust-binder press cake". The pressing process can be carried out every time the vacuum cleaner is switched off or when the collecting container is completely filled.

Es besteht des weiteren die Möglichkeit, den Staub mit Hilfe eines Rührwerks mit dem Staubbindemittel zu vermengen. Hierzu wird in dem in Figur 11 dargestellten Staubsammelbehälter 26 ein Rührwerk 110 angeordnet, das manuell aber auch automatisch über eine drehbare Achse 111 angetrieben wird. Der Grobstaub 17 bedeckt teilweise oder ganz die Schaufeln 112 des Rührwerks 110. Innerhalb bzw. oberhalb des Staubsammelbehälters befindet sich eine Dosiervorrichtung 113 mit dem Staubbindemittel 114. Das Bindemittel 114 wird kontinuierlich (z. B. während des Betriebs) oder diskontinuierlich (z. B. nach jedem Einschalten oder bei vollständig gefülltem Staubsammelbehälter) auf den Grobstaub 17 dosiert. Mit Hilfe des Rührwerks 110 wird das Bindemittel 114 homogen mit dem Staub 17 durchmischt, wodurch der Bindemitteleinsatz minimiert werden kann.There is also the possibility to mix the dust with the aid of an agitator with the dust binder. For this purpose, in the in FIG. 11 Dust collecting container 26 shown an agitator 110, which is manually but also automatically driven by a rotatable shaft 111. The coarse dust 17 partially or completely covers the blades 112 of the agitator 110. Within or above the dust collection container is a metering device 113 with the dust binder 114. The binder 114 is continuously (eg during operation) or discontinuous (e.g. after each switch-on or when the dust collector is completely filled), it is metered onto the coarse dust 17. With the aid of the agitator 110, the binder 114 is homogeneously mixed with the dust 17, whereby the binder use can be minimized.

Die Figuren 12a und 12b zeigen den prinzipiellen schematischen Aufbau einer weiteren Möglichkeit der Staubbindung. Hier werden in den Staubsammelbehälter Pads 120 eingelegt, die den Boden vollständig bedecken. Die Pads 120 bestehen aus mindestens zwei Komponenten, einem ersten Speichermedium 121 mit Staubbindemittel 122 sowie einem zweiten Speichermedium 123 für den Grobstaub 17. Vorzugsweise sind die Pads 120 als Verbrauchsmaterial ausgeführt. Das Material des ersten Speichermediums ist porös bis grobporig, schwammartig und flüssigkeitsspeichernd, vorzugsweise kommt Schaumstoff zum Einsatz. Es ist mit einem flüssigen Staubbindemittel 121 getränkt. Das Staubbindemittel 121 liegt im Idealfall als Flüssigkeit mit niedrigem Dampfdruck - wie z. B. Glycerin oder Glykol - vor. Das zweite Speichermedium 123 für den Staub muss flüssigkeitsleitend und -speichernd sein, grobporig, faserartig. Vorzugsweise werden an dieser Stelle Cellulosefasern verwendet, wobei die Fasern in den Schaumstoff eingespritzt werden, um einen guten Kontakt zum Staubbindemittel 121 zu gewährleisten. Cellulosefasern zeichnen sich durch eine hohe Kapillarität aus, wodurch das Staubbindemittel 121 aus dem Schaumstoff an die Oberfläche des zweiten Speichermediums 123 transportiert wird, um dort den Staub 17 zu benetzen bzw. zu binden und so ein Aufstauben zu vermeiden. An der Oberfläche des Speichermediums 123 bildet sich somit im Verlauf der Zeit ein "Staubkuchen", siehe Figur 4b. Bei erschöpfter Kapazität des ersten Speichermediums 122 wird der Pad 120 vorzugsweise durch den Bodenverschluss 124 des Staubsammelbehälters 26 zusammen mit dem gebundenen Staub 17 ohne Aufstauben entsorgt.The Figures 12a and 12b show the basic schematic structure of another way of dust binding. Here, pads 120 are placed in the dust collection container, which completely cover the floor. The pads 120 consist of at least two components, a first storage medium 121 with dust binder 122 and a second storage medium 123 for the coarse dust 17. Preferably, the pads 120 are designed as consumables. The material of the first storage medium is porous to coarse-pored, sponge-like and liquid-storing, preferably foam is used. It is impregnated with a liquid dust binder 121. The dust binder 121 is ideally as a liquid with low vapor pressure - such. As glycerol or glycol - before. The second storage medium 123 for the dust must be fluid conducting and storing, coarsely porous, fibrous. Cellulose fibers are preferably used at this point, the fibers being injected into the foam to ensure good contact with the dust binder 121. Cellulose fibers are characterized by a high capillarity, whereby the dust binder 121 is transported from the foam to the surface of the second storage medium 123 in order to wet or bind the dust 17 there, thus avoiding dusting. Thus, over time, a "dust cake" forms on the surface of the storage medium 123, see FIG. 4b , When the capacity of the first storage medium 122 is exhausted, the pad 120 is preferably disposed of through the bottom closure 124 of the dust collection container 26 together with the bonded dust 17 without dusting.

In einer weiteren Variante wird Wasser als Staubbindemittel verwendet. Die Figur 13 zeigt schematisch einen Drei-Fraktionen-Staubabscheider 160 mit einem Grobstaubbehälter 161 mit Grobstaub (erste Fraktion 162), einem Behälter 163 für die zweite, mittlere Staubfraktion 164, sowie einem Feinstaubfilter 165 mit Feinstaub (dritte Fraktion 166). Der konstruktive Aufbau des gesamten Abscheiders ist an anderer Stelle erläutert.In another variant, water is used as a dust binder. The FIG. 13 3 schematically shows a three-fraction dust separator 160 with a coarse dust container 161 with coarse dust (first fraction 162), a container 163 for the second, middle dust fraction 164, and a particulate matter filter 165 with particulate matter (third fraction 166). The structural design of the entire separator is explained elsewhere.

Der in den Staubabscheider 160 gelangte Staub wird folgendermaßen getrennt:
Der Grobstaub 162 umfasst mehrheitlich Partikel im Korngrößenbereich von mehr als ca. 200 µm, die im Grobstaubbehälter 161 gesammelt werden. Partikel, bei denen die Korngröße mehrheitlich im Bereich von ca. 30 µm bis ca. 200 µm liegen, werden im Staubsammelbehälter 163 gesammelt; Partikel, die kleiner als 30 µm sind, gelangen mehrheitlich in den Feinstaubfilter 165. Bei diesen Betrachtungen ist zu beachten, dass die Trenngrenzen unscharf sind. Deshalb beinhaltet die zweite Fraktion 164 auch Feinstaub 166, welcher bekanntlich beim Entleeren zum Aufstauben neigt. Für die zweite Staubfraktion 164 wird deshalb ein Staubsammelbehälter 163 verwendet, mit dessen Hilfe und der Applikation von Wasser 170 eine hygienische Staubentnahme möglich ist.
The dust entering the dust collector 160 is separated as follows:
The grit 162 mainly comprises particles in the grain size range of more than about 200 μm, which are collected in the coarse dust container 161. Particles in which the grain size is in the majority in the range of about 30 microns to about 200 microns are collected in the dust collector 163; Particles that are smaller than 30 μm, are mostly in the fine dust filter 165. In these considerations, it should be noted that the separation limits are blurred. Therefore, the second fraction 164 also includes particulate matter 166, which is known to be dusty during emptying. For the second dust fraction 164, therefore, a dust collecting container 163 is used, with the aid of which and the application of water 170, a hygienic dust removal is possible.

Die Figur 14 zeigt den Aufbau eines geeigneten Staubsammelbehälters 163 mit dem Staub 164, einer Staubzuführung 171 mit Ventilklappe 172, einem Wassereinfüllventil 173, einem Entlüftungsventil 174, einer Schütte 175, einer Ausflussöffnung 176 sowie einer Schüttenzuführung 177. Wasser 170 eignet sich hervorragend zur Bindung von Staub. Mit Hilfe des über das Wassereinfüllventil 173 eingefüllten Wassers 170 wird der Staub 164 im Staubsammelbehälter 163 ggfs. durch Schütteln des Behälters 163 mit dem Staub 164 vermischt. Die Schütte 175 mit der Ausflussöffnung 176 ist in der in der Figur 14 gezeigten Lage verschlossen und das Entlüftungsventil 174 nicht betätigt, d. h. geschlossen.The FIG. 14 shows the construction of a suitable dust collection container 163 with the dust 164, a dust supply 171 with valve flap 172, a water filling valve 173, a vent valve 174, a chute 175, an outflow opening 176 and a Schüttenzuführung 177. Water 170 is ideal for binding dust. By means of the water 170 filled via the water filling valve 173, the dust 164 in the dust collecting container 163 may be mixed with the dust 164 by shaking the container 163. The chute 175 with the outflow opening 176 is in the in the FIG. 14 closed position shown and the vent valve 174 is not actuated, ie closed.

Die Figur 15 zeigt dann den Stausammelbehälter 163 während des Entleerungsvorgangs. Nach guter Durchmischung von Wasser 170 und Staub 164 entsteht ein Wasser-Staub-Gemisch, das durch Schwenken der Schütte 175 über die Ausflussöffnung 176 und die trichterförmige Schüttenzuführung 177 entleert werden kann. Die zugegebene Wassermenge ist so zu bemessen, dass ein gut fließfähiges Gemisch entsteht. Zur Entleerung muss das Entlüftungsventil 174 geöffnet werden. Vorteilhafterweise sind die Innenwände des Staubsammelbehälters 163 sowie alle anderen Einzelteile mit einer Antihaftschicht (Lotusblüteneffekt) behandelt bzw. überzogen. Um die Behälter 161 und 163 separat entleeren zu können, sind sie trennbar ausgebildet. Zur Vermeidung von Verwechslungen sind optische Unterschiede, insbesondere Ausführungen in unterschiedlichen Farben ratsam. Die Verwendung von Wasser 170 als Staubbindemittel weist den Vorteil auf, dass der Staub 164 ohne Verwendung eines speziellen materiellen Bindemittels hygienisch, d. h. ohne Aufstauben entsorgt werden kann, somit ist kein kostenintensives Verbrauchmaterial notwendig.The FIG. 15 then shows the accumulation bin 163 during the draining process. After thorough mixing of water 170 and dust 164, a water-dust mixture is formed, which can be emptied by pivoting the chute 175 via the outflow opening 176 and the funnel-shaped chute feed 177. The added amount of water should be such that a good flowable mixture is formed. For emptying the vent valve 174 must be opened. Advantageously, the inner walls of the dust collector 163 and all other items are treated or coated with a non-stick layer (lotus flower effect). To be able to empty the containers 161 and 163 separately, they are formed separable. To avoid confusion optical differences, especially versions in different colors are advisable. The use of water 170 as a dust binder has the advantage that the dust 164 without the use of a special material binder hygienic, ie can be disposed of without dusting, so no costly consumable material is necessary.

Der in verschiedenen Ausführungsformen in den Figuren 16 bis 20 dargestellte Feinstaub-Filter 400 ist den vorbeschriebenen Staubabscheide-Systemen nachgeschaltet. Unabhängig von der Ausführungsform als Fliehkraftabscheider / Zyklonabscheider (Figuren 1 bis 15) oder Abscheider nach dem Massenträgheitsprinzip / Ringspaltabscheider hat der Feinstaubfilter 400 die Aufgabe, die den Vorabscheider passierenden Partikel zu binden, damit diese nicht wieder in die Umgebungsluft gelangen. Erfindungsgemäß ist das Staubabscheide-System derart aufgebaut, dass es gegenüber herkömmlichen Systemen eine größere Trenngrenze hat und somit nur Staub bis ca. 30 µm sammelt. Der Staub, der kleiner als 30 µm ist, im Folgenden als Feinstaub bezeichnet, gelangt mehrheitlich in den Feinstaubfilter 400.The in various embodiments in the FIGS. 16 to 20 shown particulate matter filter 400 is connected downstream of the above Staubabscheide systems. Regardless of the embodiment as a centrifugal separator / cyclone separator ( FIGS. 1 to 15 ) or Separator according to the mass inertia principle / annular gap separator, the fine dust filter 400 has the task of binding the pre-separator passing particles so that they do not return to the ambient air. According to the Staubabscheide system is constructed such that it has a greater separation limit over conventional systems and thus collects only dust to about 30 microns. The dust, which is smaller than 30 microns, hereinafter referred to as fine dust, passes in majority in the fine dust filter 400.

Die Figuren 16 und 17 erläutern den prinzipiellen Aufbau des vorgeschlagenen Filtersystems, das vorzugsweise die Gestalt einer quaderförmigen Kassette besitzt. Eine rahmenförmige bzw. rechteckige breit- und beidseitig offene Halterung 401 enthält das vorder- und hinterseitige Filtermedium 402 bzw. 403. Ferner ist in der Oberseite der Halterung 401 die Luftzuführung 404 für die Abluft aus dem Staubabscheide-System angeordnet. Die Halterung 401 wird vorzugsweise als rechteckiger Faltrahmen ausgeführt. Als weitere Lösungsalternative wird vorgeschlagen, die Halterung 401 als umlaufend geschlossenen, luftdurchlässigen, porösen bzw. ebenfalls filtrierenden Hohlkörper auszuführen, in den das Filtermedium 402 bzw. 403 eingesetzt wird, wobei sich die Filtereigenschaften von filternder Halterung 401 und innen liegendem Filtermedium 402 bzw. 403 unterscheiden können. So kann die Halterung 401 vorzugsweise aus gesintertem Kunststoff oder einem vergleichbaren Material bestehen. Durch diese mehrstufige Filteranordnung lässt sich eine Feinstfilter-Qualität erreichen. Die Dimensionen der kassettenförmigen Filtergeometrie sind an die vorgegebenen Bauraumverhältnisse eines handelsüblichen Bodenstaubsaugers angepasst und sollten im Bereich einer Standardverpackung für Staubsauger-Filterbeutel, etwa 170 mm x 230 mm x 85 mm H x B x T liegen.The FIGS. 16 and 17 explain the basic structure of the proposed filter system, which preferably has the shape of a cuboid cassette. A frame-shaped or rectangular wide-open and two-sided open holder 401 contains the front and rear side filter media 402 and 403. Further, the air supply 404 is arranged for the exhaust air from the Staubabscheide system in the top of the holder 401. The holder 401 is preferably designed as a rectangular folding frame. As a further alternative solution is proposed to perform the holder 401 as circumferentially closed, air-permeable, porous or also filtering hollow body, in which the filter medium 402 and 403 is used, wherein the filter properties of filtering holder 401 and inside filter medium 402 and 403 can distinguish. Thus, the holder 401 may preferably consist of sintered plastic or a comparable material. Through this multi-stage filter arrangement can achieve a Feinstfilter quality. The dimensions of the cartridge-shaped filter geometry are adapted to the given space requirements of a commercially available vacuum cleaner and should be in the range of a standard packaging for vacuum cleaner filter bags, about 170 mm x 230 mm x 85 mm H x W x D.

Figur 18 und Figur 19 zeigen detailliert eine Ausführungsform der ersten Lösungsalternative, Figur 29 eine weitere Ausführungsform dieser Alternative. FIG. 18 and FIG. 19 show in detail an embodiment of the first alternative solution, Figure 29 shows a further embodiment of this alternative.

Figur 18 zeigt den Feinstaubfilter 400 in der Draufsicht mit dem Filtermedium 402 und 403 sowie der Luftzuführung 404. In dieser Ausführungsvariante besteht das Filtermedium 402, 403 aus einem hochspeicherfähigen mattenförmigen, vorzugsweise einem elektrostatisch geladenem synthetisch hergestelltem oder natürlichem Filtervlies, wobei die Mattendicke ca. 10 bis 20 mm beträgt. Die elektrostatische Aufladung erfolgt während des Herstellungsprozesses des Filtervlieses. Die Luftzuführung 404 wird vorzugsweise als Langloch ausgeführt, um eine optimale Anströmung des Filtermediums 402, 403 zu gewährleisten. Weiterhin zeigt die Figur 18 den zwischen dem Filtermedium 402, 403 und der Luftzuführung 404 angeordneten filtermaterialfreien Hohlraum 405, der ebenfalls eine optimale Anströmung des Filtermediums 402, 403 unterstützt. FIG. 18 shows the fine dust filter 400 in plan view with the filter medium 402 and 403 and the air supply 404. In this embodiment, the filter medium 402, 403 consists of a highly storable mat-shaped, preferably an electrostatically charged synthetically produced or natural filter fleece, wherein the mat thickness about 10 to 20 mm. The electrostatic charge takes place during the production process of the filter fleece. The air feed 404 is preferably designed as a slot in order to ensure optimum flow of the filter medium 402, 403. Furthermore, the shows FIG. 18 arranged between the filter medium 402, 403 and the air supply 404 filter material-free cavity 405, which also supports an optimal flow of the filter medium 402, 403.

Die Figur 19 zeigt nochmals den zwischen dem Filtermedium 402, 403 und der Luftzuführung 404 befindlichen filtermaterialfreien Hohlraum 405. Des weiteren ist der Abluftstrom aus dem Staubabscheide-System durch die Pfeile 406 symbolisiert. Die Filteranordnung kann noch verbessert werden, wenn sich in dem Hohlraum 405 zwischen den beiden Filtermedien 402, 403 Watte oder ein watteähnliches Material befindet. Versuche haben gezeigt, dass sich insbesondere kleinere Partikel < 15 µm in Watte gut binden bzw. speichern lassen.The FIG. 19 again shows the between the filter medium 402, 403 and the air supply 404 located filter material-free cavity 405. Furthermore, the exhaust air flow from the Staubabscheide system symbolized by the arrows 406. The filter arrangement can be further improved if there is cotton wool or a cotton-like material in the cavity 405 between the two filter media 402, 403. Experiments have shown that especially smaller particles <15 microns can be well bound or stored in cotton wool.

Figur 20 beschreibt eine weitere Variante in der Draufsicht. Das Filtermedium 402, 403 besteht hier aus einem hochspeicherfähigen dünnen, vorzugsweise elektrostatisch geladenem, synthetisch hergestelltem oder natürlichem Filtervlies, wobei die Dicke der Vlieslage jetzt ca. 4 bis 7 mm beträgt. Um eine vergleichbare Staubaufnahmekapazität bei niedrigen Strömungsverlusten zu erreichen, muss das Filtervlies 402, 403 in dieser Ausführung gefaltet bzw. plissiert werden. Der "Plissierwinkel" α beträgt ca. 30°. Durch die Plissierung wird eine große Filterfläche geschaffen. Bei Verwendung der oben beschriebenen Filtermatte wird die Kapazität im Wesentlichen durch eine hohe Tiefenspeicherung erreicht. FIG. 20 describes a further variant in plan view. The filter medium 402, 403 here consists of a highly storable thin, preferably electrostatically charged, synthetically produced or natural filter fleece, wherein the thickness of the nonwoven layer is now about 4 to 7 mm. In order to achieve a comparable dust absorption capacity with low flow losses, the filter fleece 402, 403 must be folded or pleated in this embodiment. The "pleating angle" α is about 30 °. The pleating creates a large filter surface. When using the filter mat described above, the capacity is essentially achieved by a high depth storage.

Claims (18)

  1. Method for treating dust in a vacuum cleaner, in which a dust-binding agent is added to the dust,
    characterised in that
    the dust is separated into at least two fractions which differ in terms of the size and/or mass of the dust particles, in that a dust-binding agent is added to one fraction and in that the fraction having particles which are mostly smaller than those of the fraction to which a dust-binding agent is added is received by a fine dust filter.
  2. Method for treating dust according to claim 1,
    characterised in that
    the dust is separated into three fractions which differ in terms of the size and/or the mass of the dust particles, and in that a dust-binding agent is added to the fraction having dust particles which are mostly of average size or mass.
  3. Method for treating dust according to claim 2,
    characterised in that
    a first fraction contains mostly dust particles having a size larger than 200 µm, in that a second fraction contains mostly dust particles having a size between 200 µm and 30 µm and in that a third fraction contains mostly dust particles having a size of less than 30 µm.
  4. Method for treating dust according to claim 3,
    characterised in that
    a fine dust filter having a storage capacity of at least 200 grams of fine dust is used.
  5. Method for treating dust according to any one of the preceding claims,
    characterised in that
    the dust-binding agent is added to a dust collection container which can be inserted into the vacuum cleaner and removed therefrom.
  6. Method for treating dust according to claim 5,
    characterised in that
    the quantity and/or the time of addition and/or the frequency of addition of the dust-binding agent is/are controlled in terms of time, filling level and dust quantity.
  7. Method for treating dust according to either claim 5 or claim 6,
    characterised in that
    the dust-binding agent is added to the suction air stream upstream of the dust collection container or directly to the dust collection container inserted into the vacuum cleaner.
  8. Method for treating dust according to claim 5,
    characterised in that
    the dust-binding agent is added to the dust collection container automatically after the dust collection container has been inserted into the dust collection chamber of the vacuum cleaner.
  9. Method for treating dust according to any one of the preceding claims,
    characterised in that
    a single or multi-component additive which is present in solid and/or liquid and/or gaseous phase is used as a dust-binding agent, it being possible to change the phase so as to bind and/or mix the dust which has been drawn in and is present in loose, unbound form, and thereby to bind the dust, at least in part.
  10. Method for treating dust according to claim 9,
    characterised in that
    the phase of the dust-binding agent can be changed by supplying or removing energy, in particular heat energy or kinetic energy.
  11. Method for treating dust according to either claim 9 or claim 10,
    characterised in that
    at least one of the following materials is used as a dust-binding agent:
    - a liquid, in particular a dispersible liquid;
    - a powder;
    - a foam;
    - a granular material;
    - a solid substance, in particular pressed into tablet form.
  12. Method for treating dust according to any one of the preceding claims,
    characterised in that
    a scent and/or an anti-germ substance is/are added to the dust-binding agent.
  13. Method for treating dust according to either claim 11 or claim 12,
    characterised in that
    an agent is added to the granular material which improves its adhesive properties for dust.
  14. Method for treating dust according to any one of claims 1 to 4,
    characterised in that
    a sponge-like object is used to bind the dust.
  15. Method for treating dust according to claim 14,
    characterised in that
    the sponge-like object is arranged on the base of the dust collection container.
  16. Method for treating dust according to claim 15,
    characterised in that
    the sponge-like object is impregnated with a liquid dust-binding agent having a low vapour pressure, for example glycerol or glycol.
  17. Method for treating dust according to claim 16,
    characterised in that
    the sponge-like object is provided, on the side thereof facing the dust inlet of the collection container, with a liquid-conducting coating having a high capillarity, for example cellulose fibres.
  18. Method for treating dust according to any one of claims 1 to 8,
    characterised in that
    water is used as a dust-binding agent.
EP06777015A 2005-08-26 2006-08-23 Method for treating dust and devices for carrying out this method Not-in-force EP1921968B1 (en)

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DE200510041170 DE102005041170B3 (en) 2005-08-26 2005-08-26 Dust separating container for e.g. floor vacuum cleaner, has air inlet, air outlet, and separating plate whose arrangement produces sudden deflection of airflow, where dust particles with minimum size are separated from airflow
DE200510047812 DE102005047812A1 (en) 2005-10-05 2005-10-05 Method for treatment of dust in which dust is separated in vacuum cleaner into at least two fractions which differ by size and/or mass of dust particles, and in which dust binding agent is fed to one fraction
DE102005061725 2005-12-21
DE102005061742 2005-12-21
DE102006006011 2006-02-08
PCT/EP2006/008252 WO2007022959A2 (en) 2005-08-26 2006-08-23 Method for treating dust and devices for carrying out this method

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EP1921968B1 true EP1921968B1 (en) 2011-07-27

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Also Published As

Publication number Publication date
ATE517571T1 (en) 2011-08-15
US20080230446A1 (en) 2008-09-25
EP1921968A2 (en) 2008-05-21
WO2007022959A3 (en) 2007-06-07
PL1921968T3 (en) 2011-11-30
DK1921968T3 (en) 2011-09-26
WO2007022959A2 (en) 2007-03-01

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