Classifications

• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L5/00—Structural features of suction cleaners
  • A47L5/12—Structural features of suction cleaners with power-driven air-pumps or air-compressors, e.g. driven by motor vehicle engine vacuum
  • A47L5/22—Structural features of suction cleaners with power-driven air-pumps or air-compressors, e.g. driven by motor vehicle engine vacuum with rotary fans
  • A47L5/24—Hand-supported suction cleaners
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L1/00—Cleaning windows
  • A47L1/06—Hand implements
  • A47L1/08—Hand implements with provision for supplying liquids, e.g. cleaning agents
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L7/00—Suction cleaners adapted for additional purposes; Tables with suction openings for cleaning purposes; Containers for cleaning articles by suction; Suction cleaners adapted to cleaning of brushes; Suction cleaners adapted to taking-up liquids
  • A47L7/0004—Suction cleaners adapted to take up liquids, e.g. wet or dry vacuum cleaners
  • A47L7/0019—Details of the casing
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L7/00—Suction cleaners adapted for additional purposes; Tables with suction openings for cleaning purposes; Containers for cleaning articles by suction; Suction cleaners adapted to cleaning of brushes; Suction cleaners adapted to taking-up liquids
  • A47L7/0004—Suction cleaners adapted to take up liquids, e.g. wet or dry vacuum cleaners
  • A47L7/0023—Recovery tanks
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L7/00—Suction cleaners adapted for additional purposes; Tables with suction openings for cleaning purposes; Containers for cleaning articles by suction; Suction cleaners adapted to cleaning of brushes; Suction cleaners adapted to taking-up liquids
  • A47L7/0004—Suction cleaners adapted to take up liquids, e.g. wet or dry vacuum cleaners
  • A47L7/0042—Gaskets; Sealing means
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L9/00—Details 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
  • A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
  • A47L9/18—Liquid filters
  • A47L9/182—Separating by passing the air over a liquid bath
• • A—HUMAN NECESSITIES
  • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
  • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
  • A47L9/00—Details 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
  • A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
  • A47L9/18—Liquid filters
  • A47L9/185—Means for the mechanical control of flow of air, e.g. deflectors, baffles or labyrinths

Definitions

• the invention relates to a vacuum cleaner in which circulates, in a casing, a suction flow of air charged with particles and / or liquid, between an inlet nozzle and a communication orifice with a suction chamber.
• the invention also relates to a heater designed to be incorporated in a household appliance or cleaning or in such an aspirator.
• the invention relates to the suction of mixed streams composed of air, water, and particles in suspension. It particularly relates to the field of household appliances and / or cleaning, especially steam cleaners or window cleaning devices, or the like.
• the water filtration aspirators comprise a suction device which causes a flow of air, charged with particles as well as liquid, through a liquid contained in a tank, where the filtration of the particles is effected by bubbling.
• the air is discharged to the outside after the passage, in some cases, in a water-air separator system. In these devices, filtration is carried out at the bottom, these devices are designed only for use in vertical tank position, which makes their use impossible for portable devices.
• WO 0154798 discloses a water filtration aspirator with conventional filters, such as plastic membranes or foam polymers, resistant to water. These devices are unsatisfactory because pore clogging by dirty water or unfiltered fine particles always occurs. quickly. As a result, there is a loss of power and work must be interrupted to clean or replace the filter. Indeed, no static filter system is able to permanently stop the passage of water, because of the permeability necessary for the passage of air.
• the suction device must then be, generally, either over-motorized or bi-motorized, thus expensive and bulky, or consolidated by a stronger axis, or by an oversized assembly. Otherwise, the device is quickly deteriorated due to vibrations, or lack of power of depression.
• GB 2 382 042 discloses a water-air separator with a rotating brush which blocks the flow of air charged with particles and through which the flow of air is forced through.
• the elements suspended in the air are fixed by capillarity, in particular water, guided along the brush bristles under the effect of the centrifugal force, and ejected towards a peripheral wall, at a distance from the brush, then towards collection and evacuation areas.
• Large pressure losses of the air flow in baffles require over-charging of the suction device, and therefore result in a rise in the noise level.
• the efficiency is imperfect, due to an outlet of the air flow which is either radial or annular axial and very far from the axis of rotation.
• a suction cone constituted by a suction cone, comprising a chamber in which is mounted rotatably about an axis a filtration means, permeable to air, and designed capable of conveying the collected water to its periphery by centrifugation, where the chamber comprises a bearing flange perpendicular to the axis of rotation of the filtering means, which forms closure means in cooperation with the support flange.
• the invention proposes to further improve the power-to-power ratio, the lightness, the cost and the simplicity of manufacture of the means for generating steam.
• it is important to provide solutions compatible with a low mass, from 1.5 kg to 4 kg for manual use, and small footprint.
• the device For a given size and airflow, the device must provide high air velocity performance in the separator as well as in the tank.
• the object of the invention is to solve these main difficulties by proposing a vacuum cleaner with water filtration, in which the trajectory of the suction flow is optimized to improve the separation of the particles upstream of the suction.
• the invention comprises an improved water-air separator, adaptable to any type of water filtration vacuum cleaner and suction apparatus suitable for sucking liquid.
• the invention incorporates a steam generator to overcome the earth safety conductor, which allows the use of a cable winder even for a device of very small volume and mass, in particular of mass less than 2 kg.
• the present invention relates to a vacuum cleaner in which circulates, in a casing, a suction flow of air charged with particles and / or liquid, between an inlet nozzle and a communication port with a suction chamber, characterized by the it comprises at least one water-air separator designed adapted to be motorized and interposed between an upstream pipe and suction means and designed adapted to guide on the one hand the gas phase in said suction chamber, and d on the other hand the liquid phase and the particles in at least one reservoir in which said liquid phase is retained.
• said vacuum cleaner comprises, for the water filtration of said flow, a sparging tank in which said suction flow circulates, between said inlet nozzle and said communication orifice at an upstream pipe, upstream of suction means comprising a turbine, which splash reservoir comprises at least one peripheral vein of substantially annular shape designed to perform a centrifugation of said flow.
• said peripheral vein guides said flow to an area where partitions spaced apart from each other create a venturi effect.
• the invention also relates to a heater designed adapted to be incorporated in a household appliance or cleaning, or in such an aspirator, characterized in that it comprises at least one metal filament embedded in one or more elements consisting exclusively of ceramic-based materials, and that it comprises at least one vaporization chamber, which is constituted by a helicoidal space or the like between two bodies or housings nested one inside the other, at least one of these bodies or embedded housings being a ceramic body incorporating, embedded, such a metallic filament.
• the invention also relates to an iron with at least one heater 201 for steam generation and / or heating of the sole.
• FIG. 1 is a schematic view, partial and in longitudinal section of a basic version of the bubble tank that includes a water filtration vacuum cleaner according to the invention
• - Figure 2 is a schematic partial view in longitudinal section of a preferred version of this reservoir
• - Figure 3 is a schematic view, partial and in longitudinal section of the tank in the up position of the vacuum cleaner;
• - Figure 4 is a schematic view, partial and in longitudinal section of the tank in the stitched position of the vacuum cleaner;
• - Figure 5 is a schematic partial view in section of a water-air separator, equipping a vacuum cleaner according to the invention, in a preferred embodiment;
• FIG. 6 is a partial detail view of FIG. 5;
• FIG. 7 is a schematic partial view in perspective of a pre-separator that can be used with the separator of FIG. 5;
• FIG. 8 is a schematic and perspective view of a water filtration vacuum cleaner according to the invention.
• FIG. 9 is a schematic partial view, in longitudinal section, of an apparatus according to FIG. 8, without a sparging tank, and comprising a water-air separator according to FIG. 5;
• FIG. 10 is a diagrammatic view, in perspective and partially decarmbie, of a version of the aspirator with separator air-water and without tank of sparging;
• FIG. 11 is a diagrammatic view, in perspective and partially decarmbie, of a preferred version of the vacuum cleaner with air-water separator and with a splash tank in the basic version of FIG. 1;
• FIG. 12 is a view similar to FIG. 9, illustrating the cooling air path in the vacuum cleaner, in one embodiment with evacuation of the air sucked from the front of a ventilation turbine, and laterally on each side of it;
• - Figure 13 is a schematic perspective view of the air-water separator of Figure 6 with side air outlets;
• FIG. 14 is a schematic, partial and sectional view of steam generating means equipping an electrical household appliance, particularly a water filtration vacuum cleaner according to the invention.
• FIG. 15 is a schematic and perspective view of a water filtration vacuum cleaner with a lower cable winder
• FIG. 16 is a schematic view, and from above of a water filtration vacuum cleaner with cable winder incorporated between the central body and a side tank;
• FIG 17 is a schematic partial view in longitudinal section of a variant of bubbler tank with float
• FIG. 18 is a schematic view illustrating the cooling air path in the vacuum cleaner in a so-called rear bypass variant with evacuation of the air sucked from the upper part of the apparatus and peripherally from the rear of the apparatus; the ventilation turbine, using a hull enclosing the engine and separating the two air flows;
• Figure 19 is a view similar to Figure 14 showing a flat resistance;
• Figure 20 is a schematic view, partially open, and in perspective of a peripheral rear pass version of a vacuum cleaner according to the invention;
• FIG 21 is a detail in a longitudinal section of an ogival separator according to Figure 5 or 6;
• Figure 22 is a schematic view, in longitudinal section, similar to Figure 14, another heater according to the invention;
• Figure 23 is a schematic view, in longitudinal section, similar to Figure 22, yet another heater according to the invention.
• the invention relates to the separation of fluids contained in gases, in particular in the field of household appliances, in particular liquid, water filtration and steam cleaning aspirators known as steam vacuums, and the like.
• the invention is applicable to any gas and any liquid. In the following description is made in particular reference to a particular application where the gas is air, and the liquid is water.
• the invention relates to a vacuum cleaner 100 in which circulates, in a housing, a suction flow of air charged with particles and / or liquid, between an inlet nozzle 3 and a communication port with a suction chamber 60.
• a vacuum cleaner 100 in which circulates, in a housing, a suction flow of air charged with particles and / or liquid, between an inlet nozzle 3 and a communication port with a suction chamber 60.
• it comprises at least one water-air separator 1, designed capable of being motorized and interposed between the upstream pipe 2 and the suction means, and designed adapted to guide on the one hand the gas phase in the suction chamber 60, and on the other hand the liquid phase and the particles in at least one reservoir in which this liquid phase is preserved .
• this vacuum cleaner 100 is water filtration, and comprises a sparging tank 22 in which circulates a suction flow of air charged with particles and / or liquid, between an inlet nozzle 3 and a port 119 for communication with a suction chamber 60, at an upstream pipe 2, upstream of the suction means, in particular in the form of a turbine 10.
• the vacuum cleaner 100 according to the invention can be used manually, or on a mobile support type broom or portable. In a preferred application as illustrated in the figures, it is a portable handheld device.
• the sparging tank 22 comprises at least one peripheral stream 103, at least partially, of substantially annular shape designed capable of performing a centrifugation of said stream before entering baffles.
• This vein 103 may develop at any opening angle, even greater than one turn.
• the sparging reservoir 22 is delimited by at least one radially external partition 101, with constant or progressive curvature, without any obstacle or sudden change in concavity, which defines, with a first internal partition 106 which is a jet deflector, a vein 103 for circulating the inflow of air loaded with liquid or / and particles.
• this reservoir 22 is of substantially flat shape, and may in particular comprise, between the external partition 101 and the first internal partition 106, one or more lateral cheeks sealingly connected by gluing, welding, molding or the like.
• the reservoir 22 may in particular be framed by a first substantially flat lateral cheek, and a second lateral cheek spherical cap or the like.
• the shape of the side cheeks is dictated by the capacity of the tanks and / or accessories they contain, by the ergonomic requirements of the device. In the case of a very compact device, a spherical or polyhedral shape with substantially equal facets, cubic or other, offers the optimum interior volume for the smallest space, therefore also the lowest weight.
• the vein 103 preferably develops in a substantially circular plane, or the like, so as to create the conditions, under the effect of the suction transmitted by the orifice 119, of a vortex rejecting the flow, by centrifugation which has for the effect of grouping together such liquid or solid elements, in the vicinity of the outer wall 101.
• the flows comprising liquid or dry particles are represented by arrows solid line, purified air flows are represented in dashed arrows.
• the flow circulates, inside the splash tank 22, along the external partition 101.
• a baffle with a return at the level of an internal partition 113 flap the liquid phase and tends to fall in a lower peripheral zone 22A of the tank 22, variable according to the inclination of the device, forming a liquid receptacle.
• the air is in turn sucked by the orifice 119, which it reaches after having bypassed a baffle partition 116 after passing through a chamber 108.
• This simplified version does not make it possible to filter dry dust in all positions. in space, the liquid filter element to be near an outlet 150. It is nevertheless a very economical version well suited for a glass cleaner.
• the vein 103 performs a centrifugation of the flow before its entry in baffles at which partitions 106 and 107, spaced apart from each other, create a venturi effect.
• the end 105 of the first internal partition 106 farthest from the inlet nozzle 3 is spaced from the outer partition 101 by a small distance dl, so as to accelerate the speed of the flow.
• the path of the flow downstream of the vein 103 continues in a chamber 111, limited on the outside by a partition 113, preferably extended by a partition 114, along which the liquid phase of the flow flows, after have streamed along the outer wall 101.
• a second internal partition 107 further from the outer partition 101 than the first internal partition 106, and disposed substantially parallel to the latter on the side of an end 105 that comprises the latter, defines a first receptacle 115 for the collected liquid.
• the first 106 and second 107 internal partitions are substantially parallel to the outer partition 101, at least in the vicinity of the end 105.
• the shape of the second internal partition 107 is such that the possible excess of liquid s' flows on the inner wall 106A of the first inner partition 106, which inner wall 106A defines a second receptacle 109 for the collected liquid.
• first partition 106 and the second partition 107 are curved, and their centers of curvature are situated on the same side of the second partition 107, towards the inside of the sparging reservoir 22, that is to say in the away from the outer partition 101.
• the average radius of curvature of the first partition 106 is greater than that of the second partition 107.
• This second internal partition 107 has an end 108 located further downstream of the flow than the end 105 of the first internal partition 106, and which is located at a distance d2 from the outer wall 101 which is greater than the distance d1.
• the conditions are thus met to create a venturi effect, and to force the call of liquid in a turbulence zone 110 in the form of a jet sprayed against or towards the partition 113, in the direction from upstream to downstream of the flow, which is useful especially when the vacuum cleaner 100 is in an extreme angular position such that the water is no longer in direct contact with the particle stream and can momentarily no longer ensure its role of filter.
• This venturi solution is applicable in a variant visible in FIG.
• suction-type or broom-type vacuum cleaners and in particular having perpendicular flat tank partitions. or horizontal. It can use all known venturi effect systems: vortex, diaphragm, nozzle, convergent inlet or divergent outlet, or propulsive.
• the substantially circular shape of the reservoir 22 and of the vein 103 allow the apparatus 100 to be operated in different positions, in particular if the user rotates it about an axis substantially perpendicular to the different flow streams in the different veins and baffles that includes the reservoir 100, including normal to the plane of the figure in the example of Figure 2. Therefore, the particular arrangement of the second internal partition 107 and the inner wall 106A of the first internal partition 106 is particularly advantageous because any overflow of the liquid collected in the first receptacle 115 contributes either to feed the second receptacle 109 or to drive the excess liquid in the turbulence zone 110 which allows to bring this liquid back, after run-off on the partitions 113 and 114 in the first receptacle 115.
• the second receptacle 109 tends, for its part, to be permanently emptied by the venturi effect between the ends 105 and 108, and to feed the turbulence zone 110, and therefore, consequently, to fill the first receptacle 115.
• a drain plug 43 is disposed at this first receptacle 115.
• the partition 114 Downstream in the direction of circulation of the flow, the partition 114 is extended by a partition 116 which baffles and prevents the passage of liquid, while the flow of air runs along this partition 116 in a chamber 117, then, in the opposite direction, along another partition or the other face 116A of the partition 116, in a chamber 118, before being discharged through the orifice 119.
• This air flow discharged in whole or part of its impurities according to the configuration of the apparatus, and represented in dashed arrows in FIG. 2, is then sucked up to the suction chamber, and in a preferred version, through a separator 1 for get rid of residual liquids and / or particles.
• FIG. 17 illustrates another variant, which has a downward direction of inverted air coming out of an orifice 151, and provided with a float 152 acting as an overflow.
• a partition 153 extends the partition 106 and prohibits any passage of purified air, which must pass through the chamber 108 and then overlap a curved partition 154. This has the advantage of retaining soiled water, in case of reversal of the device horizontally. This complementarity thus offers the faculty of being able to work in all positions in space.
• Such a spiral - shaped baffle which can rotate several times, and constituting a real spiral from the periphery of the tank, guarantees a constant and effective separation whatever the air flow, in all the positions in the space.
• the separation is independent of the gaseous volume flow rate, which varies according to the accessories used, the positioning and the surface to be cleaned.
• These turns are wound either horizontally or vertically more suitable for the usual straight tanks on vacuum cleaners sleds.
• FIG. 3 illustrates a working position in which the aspirator 100 is pitched, with the inlet nozzle 3 facing upwards. In this configuration, all the liquid is returned to the receptacle 115, and the vein 103 carrying particles in the air could not be filtered by liquid, if there was the venturi effect at the end 105 which, by the jet 110, allows the mixing of the dry particles and the liquid for their filtration.
• Figure 4 illustrates a working position in which the vacuum cleaner 100 is in a dive, with the inlet nozzle 3 facing downwards.
• the liquid is returned to the receptacles 115 and 109, as well as to the end 104 of the vein 103, and is therefore always in contact with the aspirated dry particles.
• the partitions internal to the tank 22 take on shapes and sizes that vary according to the type of apparatus 100, depending on the positions of the filling, emptying, communication and filling positions as well as on the inclinations permissible for the device, be it a broom, a manual or a laptop.
• the partition 154 does not join the two walls of the tank, and thus allows use the device lying on the side
• the orifice 119 communicates directly with a suction chamber 60, and the sucked air is rejected externally at a downstream pipe 4, without passing through the 22.
• the air is removed from its water by a separator 20.
• the water flows through the passage 119 to go into the tank 22.
• the passage 119 allows the return of air to the separator 20, and the flow of residual water retained by it to go to the reservoir 22, in which the majority is retained.
• the vacuum cleaner 100 comprises a liquid-gas separator 1 arranged in a particular manner.
• This separator 1 comprises means for channeling the flow of gas between an upstream pipe 2 and a downstream pipe 4 intended for the evacuation of purified gas freed from any liquid and any impurity.
• suction or pressurization means At the level of the upstream pipe 2 arrives, under the effect of suction or pressurization means, either a flow of liquid-laden gas directly from the inlet nozzle 3, or a particle-laden gas flow and or liquid already cleared of a large portion of its particles and its liquid phase during its journey in the sparger tank 22.
• These upstream pipes 2 and downstream 4 are connected by a communication port 13.
• the separator 1 comprises , rotatably mounted about an axis of rotation 8 to 1 inside the upstream pipe 2, at least one filtration means 19, permeable to gas, and designed adapted to convey at its periphery, by centrifugation, the captured liquid .
• the separation between the water and the air is carried out during the meeting between the gas flow and a filtration means 19, which is interposed on the passage of the flow, inside the chamber or the channel formed by means channel, and which closes the communication port 13, and which is mounted fixed or preferably rotatable inside one or the other upstream pipe 2 or downstream 4, preferably the upstream pipe 2.
• the filtration means 19 is driven by a rotational movement about an axis of rotation 8, which is preferably that of a turbine 10 generating the depression and which is driven by motorization means 7, particular electric. It can also be driven by independent drive means, or by a turbine driven by the flow passing through the separator 1.
• the separator 1 comprises means for adjusting its rotation speed as a function of the difference in pressure between the upstream and downstream pipes 2 and 4, and / or the flow rate of the gas flow in the separator 1.
• the filtration means 19 consists of an ogival separator 20, provided with fins or / and radial brushes, fixed on a turbine 10 movable in rotation downstream of the communication orifice 13, and with which it communicated by the latter.
• a turbine 10 movable in rotation downstream of the communication orifice 13, and with which it communicated by the latter.
• the air flow is loaded into water droplets. This flow is driven, under the effect of the depression created by at least one turbine 10, to the ogival separator 20 which eliminates these droplets and any humidified particles, which would be entrained in the mist formed upstream during the bubbling in the tank bubbling 22.
• the liquid is captured by a barrier effect obtained by the rotation of the filtering means 19, which is permeable to gas, about its axis of rotation 8, in combination with the capillarity along this filtering means, which makes it possible to radially guide, by centrifugation, towards its periphery, drops of liquid or / and particles present in the flow sucked.
• a high speed of rotation of the filtration means 19 prevents the direct passage of the flow of liquid through the filter means by its intervals.
• the speed of rotation of the separator, the number of fins and their shape, the width of the intervals between fins, are adaptable depending on the configuration of the device and desired performance.
• a portable apparatus as shown in FIG. 9 advantageously comprises, in a chamber at the level of the upstream pipe 2, a water collection zone 21 delimited by a housing deflector 11, and communicating via the orifice 119 with the sparging tank 22.
• the casing deflector 11 forms a partition between the upstream pipe 2 and the downstream pipe 4, and has an axial opening of diameter less than the largest diameter of the separator and ogival and is preferably unique so as to avoid any flow of parasitic gas.
• the collection zone 21 is substantially annular, around the periphery of the filtration means 19, is large enough to prevent the formation of a vortex, and allows the free flow of water drops along the wall, without accumulation local which would be detrimental to the proper functioning of the separator 1.
• the casing deflector 11 allows the device to be held in multiple positions, while guaranteeing its operation, even if the unit is turned over, which is particularly advantageous for a portable device.
• its profile is bell-shaped, substantially parallel to that of a turbine deflector 12 mounted on the front face of a turbine 10 and which comprises the axial communication port 13 between the upstream pipe 2 and the pipe downstream 4, and the clearance between them is a few millimeters, especially 1 to 3 mm.
• an ogival separator 20 it is preferably fixed on such a turbine deflector 12, on the largest possible diameter, by gluing, welding, or the like, at junction points 2OB .
• the arch separator 20 can also be mounted directly thereon. Fixing the separator ogival 20 directly on the upstream face of the turbine 10, and on the largest possible diameter, allows to benefit from a large diameter passage which causes a lower axial speed of the air and therefore a more efficient separation, and a center of gravity of the separator closer to its drive source.
• the ogival separator 20 has its largest diameter near the orifice 13, which it overflows widely, and it narrows away from the orifice 13, especially until joining the axis in a version preferred as shown in FIGS. 5 and 9.
• This equilateral separator 20 may be of relatively small length relative to its diameter, in particular less than or equal to once the latter, so as to eliminate any unbalance problem.
• the ogival separator 20 may be of conical or truncated conical shape, in a preferred version, the choice of a domed ogival shape has the advantage of not offering a flat front to the incoming air flow. , which avoids any turbulence harmful to the free flow of air.
• the equilateral separator 20 comprises, extending substantially parallel to its axis of rotation 8, a return 20A to cap the casing deflector 11 to form a baffle, and which may consist of an overflow of the fins or bristles of the separator 20 downstream, partially covering the casing deflector 11.
• the ogival separator 20 is preferably monobloc, and comprises, towards the front of the device, a cap 170 full.
• the separator 20 is composed of alternating fins: inner fins 171 extending the cap and separated by spaces in which are interspersed peripheral fins 173 which form the bulk of the ogival body.
• the inner fins 171 are each extended by a portion 172 in overflow, which causes extraction of water, and prevents water from seeping at the junction between inner fins 171 and peripherals 173.
• the axis of rotation 8 of the filtering means 19 is parallel to the flow in the area of the filtering means 19, their relative orientation may be different without departing from the invention.
• the turbine 10, preferably molded of plastic is fixed on a consolidation plate 14, preferably metal, which has a single attachment point 15 on the shaft 9 of a motor constituting the means of motorization 7, and which allows a better resistance at the axis, and resistance to deformation of the plastic related to the strong centrifugal force exerted on the vanes of the turbine.
• the body of the separator 1 is molded, and the upstream pipe 2, the downstream pipe 4, the pipe means and the casing deflector 11 constitute a one-piece member which defines the orifice 13.
• the turbine 10 is rotatable in a convergence chamber 160 of the air sucked downstream of the filtration means 19, which chamber is preferably part of the same molded monobloc member.
• the chamber preferably comprises gas deflection channels, towards a peripheral or bypass end 5 radially connected to the downstream pipe 4, or by radially upstream return by reversal of the air thus rejected. Lateral outlets of the downstream pipe 4 and the convergence chamber C can also be reversed and in the same way allow the evacuation of the air downstream of the apparatus.
• the downstream pipe 4 communicates, preferably, with air outlets 301 of large area, and / or large section, for example hollow bodies 300 interposed between a central body of the vacuum cleaner 100 and side cheeks that includes the latter, so as to reduce as much as possible the sound emission, which is further reduced by sound-absorbing elements or coatings in these hollow bodies 300.
• the molded design of the channeling means which constitute the body of the separator 1 has an economic advantage of the makes simplification of assembly, and a gain in weight and volume.
• the surfaces and the interior elements, the turbine or turbines, the walls of the various channels and chambers, are covered with a coating or soundproofing treatment.
• the rotation speed of the filtration means 19 is typically more than 20000 revolutions per minute and preferably close to 25000 revolutions per minute.
• a complementary separation device 40 comprises a screen or filter, in particular a pleated filter.
• This additional separation device can be fixedly mounted as shown in Figure 5, or mobile in rotation about the axis of the ogival separator 20.
• This device 40 is preferably of generally frustoconical shape.
• This shape facilitates, when the axis of the separator is vertical with the upstream pipe 2 in the lower position, the self-cleaning of the sieve by runoff of the liquid: thus and under the action of the rotation at high speed, the sieve constituting the device 40 is little or not clogged, and opposes a very low pressure drop to the flow.
• the separator 1 advantageously incorporates at least one pre-separator 41, in the form of a closed casing on the upstream side with the exception of an opening 42, communicating with at least one turn that imparts vortex or cyclonic movement downstream to the flow of liquid and particle-laden gas prior to suction.
• the pre-separator 41 is upstream of the crossing of the complementary separating device 40 and of the passage in the separator 20. This pre-separator 41 thus performs a first peripheral drive of the liquid and particles it contains. In a preferred version, this pre-separator 41 cyclonic effect directs them in a tank 22 of bubbling or dirty water. It is usable whatever the type of device.
• the use of several pre-separators 41 makes it possible to generate a continuous or repetitive spiral effect, vertical or horizontal.
• This description illustrates the case of a vacuum cleaner 100 with water filtration, where the flow sucked to the inlet nozzle 3 is directed towards the sparging tank 22 for its water filtration.
• This separator 1, comprising a separator 20, can be used for other variants of household appliances, as shown in Figure 9, where the inlet nozzle 3 directly guides the flow sucked to the separator 20 ogival , if necessary preceded by a pre-separator 41 and / or a complementary separating device 40.
• the reservoir 22 is a reservoir of water. dirty water which collects the liquid and particles from the collection zone 21 between the casing deflector 11, the separator 1, and the casing 6 by a channel 119.
• the liquid-gas separator according to the invention has many advantages. It does not get clogged, unlike separators formed with porous filters impermeable to water. Its pressure drop is constant over time, which means that the suction power of an appliance that incorporates such a separator 1 remains constant over time. Indeed, it allows the maintenance of a flow rate of gas, especially air, constant because the separator according to the invention is self-cleaning and can not clog or foul. As a result, the user has no unpleasant maintenance to perform.
• the liquid-gas separation efficiency is very good, which reduces the release of particles into the environment, and also prevents excessive humidification of the surrounding atmosphere. This separator makes it possible to design a simplified gas circuit, and its morphology makes it possible to improve the compactness and the reduction of the cost of the apparatus in which it is mounted.
• the separator 1 according to the invention has the advantage of allowing the constitution of a removable filter body adaptable between the body and the tubes of a classic vacuum cleaner particles, while allowing the removal of the paper bag, suction of liquids or maintaining a constant air flow.
• the use of the principle of water filtration coupled with the use of a separator 1 according to the invention adapts advantageously to any type of household appliance or cleaning, including steam.
• the vacuum cleaner 100 comprises means for generating an air flow, in particular in the form of motorization means 7 driving a turbine 10, and comprises, in a casing 6, between an upstream pipe 2 and a downstream pipe 4, at least one such separator 1.
• This vacuum cleaner 100 is very compact, and comprises a reservoir of clean liquid 30 supplied by a filling orifice 34 preferably provided with a cartridge filter 33, for example anti-scale resin.
• This tank 30 is connected by a pump 31 to steam generating means 32, constituted by at least one heating element 201 comprising at least one metallic filament embedded in one or more elements consisting exclusively of ceramic-based materials and comprising minus one spray chamber.
• the latter is preferably constituted by a helical space or the like between two bodies nested one inside the other, at least one of these nested bodies being a ceramic body incorporating, embedded, such a metal filament.
• the heating body 201 preferably comprises at least one electrical resistor 200, the characteristics of which can be read in the applications FR 06 10563 and PCT / FR2007 / 05 2423 of the same applicant and to which the present application refers. Notably, in the latter document is described heating means 419. This is universally applicable, whether on irons, household appliances, cleaning, or other, just as the heating body 201 describes right here.
• Heating means 419 tubular in shape, preferably comprises, going from the inside to the outside: first a central tube 421 metal, optionally stainless according to the electrical insulation used, in which circulates the water to be vaporized , directly, either through a device designed to maximize its path and therefore the contact surface, such as a coil, a spiral partition 442, or the like, plated on the wall of the tube 421.
• a device designed to maximize its path and therefore the contact surface such as a coil, a spiral partition 442, or the like, plated on the wall of the tube 421.
• Such spiral guidance avoids too direct output steam flow.
• alloys with a high expansion index such as aluminum alloys.
• the means 419 then comprises an electrical insulation chosen to be also the best possible thermal conductor 422 or 425, and is designed to allow the removal of the earth in this type of heating body. Such an insulator may also be applied inside the tube 421.
• the means 419 then comprises a heating resistor 423, in particular economically composed of an electrical coil, placed on the periphery of the insulation covering the tube 421. and connected to an electrical circuit by means of two plugs.
• the thickness of the flange may be supplemented with a thermally conductive ceramic to improve the inertia of the assembly if necessary.
• this resistor 423 is not sheathed, in the light of the smallest possible volume.
• the heating resistor 423 may have different configurations, for example wound in turns on the periphery of the thermal conductive electrical insulator, or back and forth on the periphery of the tube 421. If the resistor 423 is coated with an electrical insulator, the turns can be joined.
• the tube 421 may comprise at least one groove, in particular a helical groove, for housing the turns.
• the resistor 423 in turns, for the same length of tube 421 can, with respect to a straight resistance, have a much greater cross section, it can also be better applied to the tube, hence a increased reliability.
• the means 419 finally comprises an external thermal insulator 424, advantageously also electrically insulating, protecting all of the heating means 419.
• the material used is preferably based on non-fibrous ceramics with a high coefficient of thermal insulation.
• the thermal conductive electrical insulator 422 or 425 is in the form of a one-piece material which may be, for example, a ceramic 422, or a porcelain of food type or the like, or in the form of a thin layer 425 deposited on the surface of the central tube 421, for example a layer of aluminum oxide obtained by plasma spraying.
• This deposit can also be obtained by ceramizing low temperature (500 0 C) after soaking in a mixture of aluminum oxide and silicon dioxide among others, this economical solution also provides a perfect protection against oxidation metal tube 421, which can be made of non-stainless material, and with, in addition, double electrical insulation.
• This technique which is similar to enamelling, can also be used to prevent limescale fixation, which causes electrical safety and efficiency to be disturbed.
• the covering of the tube 421 is still possible with a deposit based on aluminum oxide and resin. These materials are not limitative, other types of applications and products remain possible, when it comes to using materials with the property of electrical insulation and thermal conductivity or thermal and electrical insulation outdoors .
• An insulating layer 422 or 425 such as alumina or magnesia, with a thickness of approximately 0.10 mm gives good results.
• the insulator 425, applied to the tube 421 is a better thermal conductor than the insulator 422 used for the protection of the heating resistor 424. This difference in thermal conduction advantageously comes from a much higher level of alumina. high in the insulator 425 as in the insulator 422.
• the thickness of the tube 421 is calculated as a function of the desired steam flow rate, the electric power of the resistor, and the inertia necessary for a permanent flow.
• Other non-limiting materials such as magnesia, dense alumina, boron nitride, silicon, can be used according to the needs and means of non-limiting applications.
• the thermal conductive electrical insulation in the form of a thin layer 425 has the advantage of reducing the size of the heating means 419 and allows a faster thermal diffusion to the central tube 421 in contact with water. This application in thin layer can be done by plasma spraying or resin varnishing, or dipping in a bath, or enameling, or any other known system.
• the heating assembly is advantageously completed by two connectors 426 and 427, larger in output to avoid pressure, allowing the interlocking of the conductive pipes.
• the heating means 419 for its simplicity, is more economical and lighter than the usual shielded resistances embedded in aluminum blocks.
• This heating body 201 can be used alone in a wide variety of applications, especially for household appliances and cleaning, for use of the boiler in particular: coffee maker or electric kettle, or for a sole and / or a boiler iron.
• the heating body 201 is further improved as can be seen in FIGS. 14 and 22: it comprises at least one filament 130, connected to the sector by its ends 132 and 133.
• a core 131 serves as support to at least one filament 130, this core 131 is embedded or enclosed in a ceramic body 134, which has an inlet 138 of liquid, preferably water to generate steam.
• the filament or filaments 130 are contained in a container made of an insulating material, especially a ceramic material, in particular an inner body or tube 301. The latter is enclosed in an internal body 302, preferably made of metal, and so preferred aluminum alloy or stainless steel.
• the filament 130 is preferably made in the form of a shielded resistor, preferably consisting of a resistor embedded in a particularly ceramic insulating powder providing a first level insulation, this powder being contained in a tube generally metal.
• the body 134 is enclosed in a housing 137, and the liquid flows, preferably at the periphery of the body 134, in one or more channels 135 to one or more outlet ports 138A.
• the internal body 302 is enclosed in a sealed body 303, so as to provide between them one or more circulation channels 135 forming a vaporization chamber of the liquid.
• such a channel 135 is spiral, or comprises a succession of loops for example U, and preferably double U, so as to lengthen the path of the liquid, so as to obtain a fine vapor outlet, unlike the simple ordinary heating tube which also ejects water under the effect of the pressure of the steam already formed.
• the body 134 cooperates, at an outer surface 134A, with an inner surface 137A that comprises a housing 137.
• the latter is preferably a ceramic tube, which incorporates at least one resistance 140 , in particular spirally wound and embedded in the ceramic, and connected to the sector by its ends 141 and 142.
• the body 134 and the housing 137 are assembled by complementary surfaces, respectively 143 and 143A, in particular in the form of a thread and a a tapping.
• the housing 137 has a steam outlet orifice 139 generated by the heating of the liquid introduced into the inlet 138, under the effect of the filament (s) 130 and the resistance (s) 140.
• the filament 130 or / and the The resistor 140 can very advantageously take the form of a long developed length, for example in a spiral, or preferably because it is more economical, with a succession of single or multi-stage U-shaped loops constituting a coil.
• the inner body 302 cooperates with a sealed body 303, preferably the inner body 302 is contained in a cylinder, and the sealed body 303 is a tube fitted just on the cylinder.
• the sealed body 303 is preferably metal, and preferably aluminum alloy or stainless steel.
• the sealed body 303 is itself enclosed in an intermediate body 304 of insulating material and preferably ceramic.
• the intermediate body 304 is preferably made in the form of a tube.
• the intermediate body 304 is in turn enclosed in an outer housing 305 preferably metal, and preferably aluminum alloy or stainless steel.
• This outer casing 305 incorporates at least one resistor or filament 140. The latter may advantageously consist of at least one shielded resistor according to the principle explained above.
• the cooperation of the inner body 302 and the intermediate body 304 is made, but not limited to, by screwing, one of the two having a thread and the other a tapping, or vice versa.
• the assembly can also be done by gluing.
• the inner body 301 is a ceramic tube
• the inner body 302 is aluminum alloy
• the sealing body 303 is made of stainless steel, so as to sustainably resist corrosion very calcareous waters, and preferably in a symmetry of revolution
• the intermediate body 304 is ceramic and preferably tubular
• the outer housing 305 is aluminum alloy.
• seals not shown in FIG. 14, but visible in FIG. 22, in the preferred but nonlimiting form of O-rings, respectively 306 between the body 302 and the intermediate body 304 and the end of the body 303, and 307 between the body 302 and the intermediate body 304 at the end thereof. It is understood that this embodiment provides total protection in double insulation and double sealing of the heater 201. Thus, the reliability is complete, and it is no longer necessary to use grounding cable, which allows to gain weight, space, cost, and also to make available to the user a much longer cable length than that of a conventional device connected in three son.
• FIG. 23 illustrates a simplified and very economical variant in which the liquid flows between an inlet 138 and an outlet 139 in a body 303 forming a vaporization chamber. 135, and preferably made of stainless steel, this body 303 being contained in, and cooperating with, an intermediate body 304 made of insulating material, in particular ceramic, the latter incorporated in an outer body 305, in particular aluminum alloy which encloses itself at least one armored resistor or filament 140.
• the cladding by metal bodies makes it possible to prevent thermal shocks, in particular with the use of aluminum alloys, and thus to preserve the parts made of ceramic. And even in case of breakage, the ceramic is maintained, and the double seal completely protects the user.
• the total power of the resistor (s) 140 is between 3 and 4 times that of the filament (s) 130, for example 1500W and 500W respectively, for an electrical resistance 200 with a length of 10 to 15 cm.
• the filament 130 may be spirally disposed on the core 131, with in this case a larger diameter. In both cases, a total power of 2000W can be obtained for a length of the order of 10 to 11 cm, and a diameter of about 5 cm.
• the housing 137 is, again, advantageously isolated on its outer surface by a fiber or ceramic insulation, or the like, retained by a holding housing, for example plastic. This design is not limited to the tubular shape, and such steam generating means 32 are usable, whatever the geometry of implantation, for any type of boiler, in particular shielded outside or inside to withstand the pressure .
• Figure 19 illustrates a variant on the same principle, between two ceramic bodies incorporating resistors 140, a labyrinth 155, preferably spiral, is used for heating or vaporization of water, in an extremely compact volume.
• the wide variety of forms achievable for the resistance 200 advantageously allows it to replace the heating bodies of electric kettles and coffee makers, and allows its coupling to a plastic or ceramic container to make a boiler. Such a boiler is particularly economical and efficient.
• this apparatus 100 comprises two cheeks, one consisting of a reservoir of clean liquid 30, the other of a sparging reservoir 22, one of which may contain a housing for the reel 53.
• This reservoir of clean liquid 30 advantageously incorporates an anti-scale cartridge, especially resin.
• the apparatus 100 is able to operate in all positions in space thanks to the casing baffles 21.
• the operator manipulates it in all these positions, without particular fatigue, since it maintains it at its center of gravity.
• the vacuum cleaner 100 according to the invention is traversed by a cooling air circuit.
• An outside air inlet 200 is provided, preferably close to the handle 50, and may include a baffle 201 optionally provided with an air filter.
• a pipe brings this fresh air into a chamber 202 located at one end of the motorization means 7 of the turbine 10.
• these means 7 are fixed on a partition separating this chamber 202 from another chamber 203 in which is located the Another end of the motorization means 7. These are traversed by the flow of fresh air from the chamber 202 to the chamber 203, the air exits through an orifice 204 in a pipe 205 which leads into a chamber 206 surrounding the steam generating means 32, that it thus contributes to cooling, before it leaves the apparatus through at least one outlet mouth 207.
• the latter communicates advantageously with the outlet channels of the air sucked downstream of the downstream chamber 4, made in the form of chambers located between the central body comprising the handle 50 and the lateral cheeks.
• the circulation of the sucked air extracts, by the venturi effect, at the level of an extraction channel, the air present in the zone surrounding the suction motor, and thus creates an air flow. cooling, without requiring of moving organ such as a propeller or the like, thereby making the manufacture less expensive.
• bypass three types of air outlets, called bypass, are preferentially usable: - lateral exit from the front of the device, that is to say on the side of the endpiece Entrance 3, with double cheek; lateral exit from the rear of the apparatus, that is to say the opposite side to the inlet nozzle 3, in the upper part or from the side, with possible removal of a tank part, with double play ; device output to the rear of the device and in the upper part with a motor sealing box.
• the cooling air is advantageously evacuated by the handle 50 of the apparatus.
• a particularly interesting embodiment of such an apparatus 100 is a steam window squeegee with a vacuum, a vacuum mass of about 1.5 kg, for a clean liquid reservoir 30 and a bubbling tank 22 each about 500 ml , and for which an installed power of 40OW, or even 20OW, is enough to carry out a cleaning of quality, without fatigue for the operator.
• a turbine 10 with a diameter of 76 mm, and a separator with a diameter of 52 mm for example, allow an air flow rate of 15 to 20 liters per second, compatible with a good efficiency of suction and separation.
• the inlet of the apparatus may be provided with a tube, for venturi routing a liquid from a tank of clean or slightly soiled liquid, so to moisten these dusts, and then separate by the different separation means described above.
• the invention also relates to an iron with at least one heater 201 for steam generation and / or heating of the sole.

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• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Filters For Electric Vacuum Cleaners (AREA)
• Filtering Of Dispersed Particles In Gases (AREA)
• Separating Particles In Gases By Inertia (AREA)

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• 2009
  • 2009-08-10 US US13/058,357 patent/US20110131756A1/en not_active Abandoned
  • 2009-08-10 EP EP09740454A patent/EP2323528A2/de not_active Withdrawn
  • 2009-08-10 CN CN200980140029.7A patent/CN102176853B/zh not_active Expired - Fee Related
  • 2009-08-10 JP JP2011522540A patent/JP2011530358A/ja active Pending
  • 2009-08-10 WO PCT/FR2009/051579 patent/WO2010018342A2/fr active Application Filing

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