EP2323537B1 - Dishwasher machine comprising a sorption drying device - Google Patents
Dishwasher machine comprising a sorption drying device Download PDFInfo
- Publication number
- EP2323537B1 EP2323537B1 EP09781148.3A EP09781148A EP2323537B1 EP 2323537 B1 EP2323537 B1 EP 2323537B1 EP 09781148 A EP09781148 A EP 09781148A EP 2323537 B1 EP2323537 B1 EP 2323537B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- sorption
- machine according
- dishwasher machine
- air
- pot
- 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.)
- Active
Links
- 238000001179 sorption measurement Methods 0.000 title claims description 239
- 238000001035 drying Methods 0.000 title claims description 52
- 238000005406 washing Methods 0.000 claims description 72
- 239000000463 material Substances 0.000 claims description 57
- 238000010438 heat treatment Methods 0.000 claims description 33
- 230000005484 gravity Effects 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 238000005304 joining Methods 0.000 claims description 3
- 230000000295 complement effect Effects 0.000 claims description 2
- 239000003779 heat-resistant material Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 229910001256 stainless steel alloy Inorganic materials 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 239000002594 sorbent Substances 0.000 description 58
- 238000000034 method Methods 0.000 description 28
- 230000008569 process Effects 0.000 description 28
- 239000007788 liquid Substances 0.000 description 26
- 238000003795 desorption Methods 0.000 description 23
- 239000007921 spray Substances 0.000 description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 238000004140 cleaning Methods 0.000 description 19
- 230000000630 rising effect Effects 0.000 description 15
- 238000013021 overheating Methods 0.000 description 11
- 238000005507 spraying Methods 0.000 description 9
- 230000003750 conditioning effect Effects 0.000 description 7
- 239000003599 detergent Substances 0.000 description 7
- 238000007789 sealing Methods 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 6
- 239000006260 foam Substances 0.000 description 6
- 230000001174 ascending effect Effects 0.000 description 5
- 239000008187 granular material Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000011010 flushing procedure Methods 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- 238000010926 purge Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- 210000002414 leg Anatomy 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 101100235013 Arabidopsis thaliana LCY1 gene Proteins 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 239000000443 aerosol Substances 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000012459 cleaning agent Substances 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 230000009849 deactivation Effects 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 101150058348 SWE1 gene Proteins 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000007791 dehumidification Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000011796 hollow space material Substances 0.000 description 1
- 238000007373 indentation Methods 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 210000003127 knee Anatomy 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Images
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
- A47L15/00—Washing or rinsing machines for crockery or tableware
- A47L15/42—Details
- A47L15/48—Drying arrangements
- A47L15/481—Drying arrangements by using water absorbent materials, e.g. Zeolith
-
- 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
- A47L15/00—Washing or rinsing machines for crockery or tableware
- A47L15/42—Details
- A47L15/4251—Details of the casing
Definitions
- the present invention relates to a dishwasher, in particular a domestic dishwasher, with at least one rinsing container and at least one sorption drying system for drying items to be washed, wherein the sorption drying system has at least one sorption container with reversibly dehydratable sorption material, which is connected via at least one air duct with the rinsing container for generating an air flow.
- Dishwashers are known with a so-called sorption column for drying dishes.
- a so-called sorption column for drying dishes.
- humid air from the washing compartment of the dishwasher is passed through the sorption column by means of a blower and moisture is removed from the air through which it is reversibly dehydratable by condensing moisture.
- For regeneration ie desorption of the sorption column whose reversibly dehydratable dry material is heated to very high temperatures.
- DE 10 2005 004 095 A1 is a dishwasher with a Sorptionstrockenvorraum known. Neither DE 10 2005 004 006 A1 yet DE 10 2005 004 095 A1 give an indication of the mechanical structure of the housing of the sorption column.
- the object of the invention is to provide a dishwasher, in particular a domestic dishwasher, with further improved sorption and / or desorption results for the reversibly dehydratable dry material of the sorption unit of its sorption drying apparatus.
- the sorption container has a pot-shaped housing part which is closed by a cover part.
- a peripheral outer edge of the cover part is connected to the upper edge of the cup-shaped housing part only by a mechanical connection, in particular by a forming, joining, latching, clamping, in particular by a beaded connection, or clinch connection.
- FIGS. 1 17 each provided with the same reference numerals.
- FIG. 1 shows a schematic representation of a dishwasher GS, which has as main components a washing container SPB, arranged underneath a bottom assembly BG and a sorption drying system TS according to the inventive design principle.
- the sorption drying system TS is preferably provided externally, ie outside the washing container SPB, partly on a side wall SW and partly in the bottom assembly BG. It comprises as main components at least one air duct LK, at least one fan unit inserted in it or a fan LT and at least one sorption tank SB.
- In the washing container SB are preferably one or more grid baskets GK for receiving and rinsing items such. B. pieces of dishes housed.
- one or more spraying devices such as one or more rotating spray arms SA, are provided in the interior of the washing container SPB.
- a lower spray arm and an upper spray arm are suspended in the washing container SPB in a rotating manner.
- Dishwashers undergo washing programs that have a plurality of program steps for cleaning items to be washed.
- the respective rinsing program can comprise in particular the following individual program steps which proceed one after the other: a pre-rinsing step for removing soiling, a cleaning step with detergent addition to liquid or water, an intermediate rinsing step, a rinsing step with application of liquid or water added with expansion agents or rinse aid , and a final drying step, in which the cleaned items is dried.
- fresh water and / or service water mixed with detergent is added to this, for example. for a cleaning process, for an intermediate rinsing, and / or applied for a rinse on the respective items to be washed.
- the fan unit LT and the sorption SB are here in the embodiment in the bottom assembly BG below the bottom BO of the washing container SPB housed.
- the air duct LK extends from an outlet opening ALA, which is provided above the bottom BO of the washing container SBP in the side wall SW, outside of this side wall SW with an inlet-side pipe section RA1 down to the fan unit LT in the bottom assembly BG.
- the outlet of the fan unit LT Via a connecting section VA of the air duct LK, the outlet of the fan unit LT is connected to an inlet opening EO of the sorbent container SB in its area near the ground.
- the outlet opening ALA of the washing container SPB is preferably provided above its bottom BO in the middle region or in the central region of the side wall SW for drawing in air from the interior of the washing container SPB.
- the outlet opening ALA in the rear wall RW (see FIG. 2 ) of the washing container SPB is particularly advantageous that the outlet opening is preferably at least above a Foam level up to which foam can form in a cleaning process, preferably in the upper half of the washing container SPB in one of its side walls SW and / or provide back wall.
- the fan unit LT is preferably designed as an axial fan. It serves for the forced flow of a sorption unit SE in the sorption container SB with moist-hot air LU from the rinsing container SPB.
- the sorption unit SE contains reversibly dehydratable sorption material ZEO, which can absorb and store moisture from the air LU passed through it.
- the sorption SB has in the near-ceiling region of its housing on the upper side of an outflow opening AO (see FIGS. 4 . 5 ), which via an outlet element AUS through an insertion opening DG (see FIG. 13 ) in the bottom BO of the washing container SPB is connected to the interior thereof.
- this sorption drying system TS a closed air circulation system is provided by this sorption drying system TS.
- the spatial arrangement of the various components of this sorption drying system TS is shown in the schematic perspective view of FIG. 2 and the schematic side view of the FIG. 3 out.
- the course of the bottom BO is additionally shown in dash-dotted lines, whereby the spatial-geometric relationships of the structure of the sorption drying system TS are better illustrated.
- the outlet opening ALA is preferably arranged at a location above the bottom BO, which allows the collection or suction of as much moist hot air LU from the upper half of the washing container SPB in the air duct LK. After a cleaning process, in particular rinsing with heated liquid, moist hot air preferably collects above the bottom BO, in particular in the upper half of the washing container SPB.
- the outlet opening ALA is preferably at an altitude above the level of foam, which may occur during regular flushing operation or in the event of a fault. In particular, foam can be caused by detergent in the water during the cleaning process.
- the position of the exit point or outlet opening ALA is selected such that a rising distance on the side wall SW is still freely available for the inlet-side pipe section RA1 of the air duct LK.
- the outlet opening or outlet opening in the middle region, ceiling region, and / or upper region of the side wall SW and / or rear wall RW of the washing container SPB also largely prevents water from the sump in the bottom of the washing container or from its liquid spraying system through the outlet opening ALA of the washing container Rinsing container SPB injected directly into the air duct LK and then can get into the sorbent SB, what else there sorption ZEO inadmissible damp, partially damage or unusable, or even completely destroyed.
- the sorption SB is viewed in the flow direction before the sorption SE at least one heater HZ for desorption and thus regeneration of the sorbent ZEO arranged.
- the heating device HZ is used to heat air LU, which is driven through the fan unit LT by the air duct LK in the sorption.
- This positively heated air absorbs the stored moisture, in particular water, from the sorption material ZEO as it flows through the sorption material ZEO.
- This expelled from the sorbent ZEO water is transported by the heated air through the outlet element AUS of the sorbent SB into the interior of the washing.
- This desorption process preferably takes place when liquid is carried out for a cleaning process or other rinsing process of a subsequent dishwashing program. It can be used for the desorption process heated by the heating device HZ be used simultaneously to heat the liquid in the washing container SPB, which is energy efficient.
- FIG. 2 shows with the door open TR of the dishwasher GS of FIG. 1 Main components of the sorption drying system TS in the side wall SW and the bottom assembly BG partially in the exposed state in perspective view.
- the FIG. 3 shows suitably to the totality of the components of the sorption drying system TS viewed from the side.
- the inlet-side pipe section RA1 of the air duct LK has, starting from the height position of its inlet opening EI at the location of the outlet opening ALA of the washing compartment SPB a pipe section AU rising upward with respect to the direction of gravity and then a pipe section AB sloping downwards with respect to the direction of gravity SKR.
- the upwardly rising pipe section AU extends slightly upward with respect to the vertical direction of gravity SKR and merges into a curved section KRA, which is bent convexly and for the inflowing air flow LS1 a directional reversal of about 180 ° downwards into the adjoining, substantially vertically downwards sloping pipe section AB forces. This ends in the fan unit LT.
- the first, upwardly rising pipe section AU, the curvature section KRA, and the downstream, second, downwardly sloping pipe section AB form a flat channel with a substantially flat rectangular cross-sectional geometry shape.
- one or more flow guide ribs or drainage ribs AR are provided, which follow its curvature profile.
- a plurality of arcuate drainage ribs AR are substantially nested concentrically in one another and arranged at a transverse distance from one another in the interior of the curved section KRA. They extend here in the embodiment in the rising pipe section AU and in the sloping pipe section AB on a partial length.
- These drainage ribs AR are disposed at height positions above the outlet ALA of the purge tank SPB and the inlet EI of the inlet side pipe section RA1 of the air duct LK, respectively.
- These drainage ribs AR serve to receive liquid droplets and / or condensate from the air flow LS1 drawn in from the washing container SPB.
- the flow guide ribs AR drip off collected liquid droplets in the direction of the outlet ALA.
- the liquid droplets can drip off the flow guide ribs AR in the direction of a return rib RR.
- the return rib RR is provided at a point in the interior of the sloping pipe section AB, which is higher than the outlet opening ALA of the washing container SPB or higher than the inlet opening EI of the air duct LK.
- the return rib RR in the interior of the sloping pipe section AB forms a drainage slope and is aligned with a cross-connection line RF in the direction of the outlet ALA of the washing compartment SPB.
- the cross-connection line RF bridges the gap between the leg of the upwardly rising pipe section AU and the leg of the downwardly sloping pipe section AB.
- the cross-connection line RF connects the interior of the upwardly rising pipe section AU and the interior of the downwardly sloping pipe section AB with each other.
- the slope of the return rib RR and the adjoining, aligned cross-connection line RF is selected such that a condensate return of condensate or other liquid droplets that drip down from the gutters AR in the region of the sloping pipe section AB, in the outlet opening ALA of the washing container SPB is ensured.
- the drainage ribs AR are preferably mounted on the inner wall of the air duct LK facing away from the Spül organizationsenwand SW, since this outer side inner wall of the air duct is cooler than the flushing tank SPB facing inner wall of the air duct. At this cooler inner wall condensate precipitates stronger than on the side wall SW facing inner wall of the air duct LK down. It may therefore be sufficient if the drainage ribs AR are designed as web elements which protrude from the outer inner wall of the air duct LK only over a partial width of the total cross-sectional width of the formed as a flat channel air duct in the direction of the inner side wall SW facing inner wall of the air duct, so that a lateral cross-section gap remains for air flow.
- the return rib RR is preferably mounted on the inside of the outer inner wall of the air duct LK as a web element, which protrudes in the direction of its inner inner wall on a partial width or partial width of the entire width of the flat formed air duct LK. This ensures that a sufficient passage cross-section remains free in the region of the return rib RR for the passage of the air flow LS1.
- the drainage ribs AR and the return rib RR serve in particular also to separate water droplets, detergent droplets, rinse aid droplets, and / or other aerosols which are located in the inflowing air LS1 and return them into the rinsing container SPB through the outlet opening ALA.
- This is particularly advantageous in a desorption process when a cleaning step takes place at the same time.
- a relatively large amount of steam or mist may be present in the washing container SPB, in particular due to the spraying of liquid by means of the spraying arms SA.
- Such a vapor or mist may contain finely divided water as well as detergent or rinse aid and other cleaning agents.
- the drainage ribs AR For these finely dispersed liquid particles entrained in the air flow LS1, the drainage ribs AR, a deposition device, form.
- other deposition means in particular structures with a plurality of edges, such as e.g. Wire mesh, be provided.
- the tube section AU ascending obliquely upwards or substantially vertically ensures that liquid droplets or even spray jets which are sprayed out by a spraying device SA, for example a spray arm during the cleaning process or other rinsing process, are largely prevented from passing directly over the suctioned Air flow LS1 to enter the sorbent of the sorption.
- a spraying device SA for example a spray arm during the cleaning process or other rinsing process
- the Sorption material ZEO for a sorption process during the drying step are made inadmissibly humid and unusable. In particular, it could lead to premature saturation by introduced liquid droplets such as mist droplets or vapor droplets.
- the dishwasher GS here has a drying device for drying items to be washed by sorption by means of reversibly dehydratable sorption material ZEO, which is stored in a sorption container SE.
- This is connected via at least one air duct LK to the washing container SPB for generating an air flow LS1.
- the air duct has along its inlet-side pipe section RA1 a substantially flat rectangular cross-sectional geometry shape. Viewed in the direction of flow, the air-guiding channel, according to its inlet-side pipe section RA1, merges into a substantially cylindrical pipe section VA. It is preferably made of at least one plastic material.
- the air duct LK has at least one upwardly rising pipe section AU. It extends from the outlet opening ALA of the washing container SPB upwards. He further has, viewed in the flow direction after the rising pipe section AU at least one downwardly sloping pipe section AB. Between the rising pipe section AU and the sloping pipe section AB at least one curvature section KRA is provided.
- the curvature section KRA in particular has a larger cross-sectional area than the rising tube section AU and / or the sloping pipe section AB.
- one or more flow guide ribs AR are provided for equalizing the air flow LS1. If necessary, at least one of the flow guide ribs AR extends beyond the curved section KRA into the rising pipe section AU and / or sloping pipe section AB.
- the one or more flow guide ribs AR are provided at positions above the height position of the outlet ALA of the purge tank SPB.
- the respective flow guide rib AR extends from the Spül actuallyergeophuse- facing channel wall to the opposite, Spül relieergephase- remote channel wall of the air duct LK, preferably substantially continuously.
- At least one return rib RR is provided in the interior of the sloping pipe section AB on the Spippo constituergetude- facing channel wall and / or Spül successiveergephaseuse- remote channel wall of the air duct LK at a point which is higher than the inlet opening EI of the air duct LK.
- the return rib RR is connected via a cross-connection line RF in the space between the descending pipe section AU and the sloping pipe section AB for condensate return to the inlet opening EI of the air duct LK. It has a slope towards the inlet opening EI out.
- the return rib extends from the Spül thereergeophusebehgewand channel wall to the opposite, Spül relieergephase- remote channel wall of the air duct LK preferably only on a partial cross-sectional width.
- the falling branch AB of the air duct LK is introduced substantially perpendicularly into the fan unit LT.
- the sucked-in air flow LS1 is blown from the fan unit LT on the output side via a tubular connection section VA into an inlet connection ES of the sorption container SB coupled to it in the area near the bottom thereof.
- the air flow LS1 flows into the lower region of the sorption container SB with an inflow direction ESR and changes into a different flow direction DSR with which it flows through the interior of the sorption container SB.
- This through-flow direction DSR runs from bottom to top through the sorption SB.
- the inlet nozzle ES directs the incoming air flow LS1 into the sorption container SB such that it is deflected from its inflow direction ESR, in particular by approximately 90 degrees, into the throughflow direction DSR of the sorption container SB.
- the sorption SB below the bottom BO in a bottom assembly BG of the washing compartment SPB largely free-hanging arranged so that it has a predetermined minimum gap distance LS against adjacent components and / or parts of the floor assembly BG for heat protection LS (see also Figure 10 ) having.
- At least one transport securing element TRS is provided at a predetermined free space distance FRA for the free-hanging sorbent container SB below the bottom BO of the floor assembly BG, so that the sorption container SB is supported from below if the sorption container SB moves downwards during its transport from its freely suspended position ,
- the sorption container SB has at least one outer housing AG in addition to its inner housing IG in such a way that its entire housing is double-walled there. Between the inner housing IG and the outer housing AG thus an air gap clearance LS is present as a thermal insulation layer.
- a further overheating protection measure is additionally or independently provided for the freely suspended storage or accommodation of the sorbent container SB in order to present any adjacent components and components of the floor assembly BG Inadequate levels of overheating or burns should be adequately protected.
- the housing of the sorption container SB has such a geometry that there is a sufficient gap distance as heat protection around the remaining parts or components of the base assembly BG.
- the sorption container SB for this purpose on its the rear wall RW of the bottom assembly BG facing housing wall SW2 to a curved formation AF, which corresponds with its facing geometry of the rear wall RW.
- the sorption SB is at the bottom of the bottom BO, in particular in the region of a passage opening DG (see FIG. 3 . 13 ) of the bottom BO, the washing container SB. This is particularly the case in the schematic side view of FIG. 3 illustrated.
- the bottom BO of the washing container SPB starting from its outer edges ARA on a liquid collecting FSB tapered slope on.
- the sorption container SB is mounted on the bottom BO of the washing container SPB in such a way that its lid part DEL extends substantially parallel to the underside of the bottom BO and with a predetermined gap distance LSP to the latter.
- a coupling connection between at least one bottom side member, in particular a base SO, the sorbent SB and a top floor component, in particular the outlet element OFF, the sorbent SB in the region of a passage opening DG in the bottom BO of the purge SB provided.
- a coupling connection in particular a clamping connection is provided.
- the clamping connection can by a detachable connection, in particular screw, with or without bayonet lock BJ (see FIG. 13 ), be formed between the bottom-bottomed component of the sorbent SB and the upper floor component of the sorbent SB.
- An edge zone RZ see FIG.
- the bottom-side outlet component and / or the bottom-top splash guard component AUS projects with its end-side end portion through the passage opening DG of the bottom BO.
- the bottom-side outlet part has a base SO around the outlet opening AO of the cover part DEL of the sorbent container SB.
- the floor-top splash protection component AUS has a discharge connection AKT and a splash protection cover SH. At least one sealing element DI1 is provided between the floor-top-side component AUS and the bottom-floor-side component SO.
- the sorption SB is therefore arranged below the bottom BO of the washing container SPB largely free-hanging so that it has a predetermined minimum gap distance LSP with respect to adjacent components and parts of the bottom assembly BG for heat protection.
- a transport securing element TRS is additionally fixed in a predetermined free space distance FRA at the bottom of the floor assembly. This transport securing element TRS is used to support the sorbent container SB, which is suspended below the bottom BO of the washing container SPB, if necessary from below, if this is to be supported, for example during transport together with the Bottom BO vibrates down due to shocks.
- This transport securing element TRS can be formed, in particular, by a downwardly U-shaped metal clamp, which is fixedly mounted on the bottom of the floor assembly.
- the sorption SB has at the top of its cover part DEL on the outflow opening AO.
- a cylindrical base nozzle element STE is attached (see FIGS. 4 . 5 . 9 . 13 ) which projects upwards and serves as a counterpart to the outflow connection piece or outlet connection piece AKT to be fastened thereto.
- It preferably has an external thread with integrated bayonet lock BJ, which interacts with the internal thread of the Ausblaskaminstutzens AKT accordingly.
- the base SO has the sealing ring DI1 on its upper side, concentric around the base neck STE receiving edge. This is in the Figures 3 . 4 . 9 . 13 illustrated.
- the sorption container SB is firmly pressed against this with the sealing ring DI1 on the underside of the bottom BO. It is held by the height of the base SO on clearance LSP from the bottom of the bottom BO. From the top of the bottom BO ago is through the through-hole DG of the bottom BO of the exhaust stack AKT down pushed through and bolted to the counter-piece base socket STE and the opening secured by the bayonet lock BJ.
- the exhaust gas nozzle AKT surrounds an outer edge zone RZ of the bottom BO around the passage opening DG with an annular outer edge APR.
- the bottom BO of the washing container SPB runs here in the embodiment of FIG. 3 starting from its peripheral edge zone with the side walls SW and the rear wall RW toward a preferably central liquid collecting area FSB inclined with inclination to. Below this, the pump sump PSU of a circulation pump UWP can be located (see FIG. 16 ). In the FIG. 3 this is drawn dash-dotted from outside to inside obliquely to the lower collection area FSB tapered bottom BO.
- the arrangement of the pump sump PSU with the recirculation pump UWP seated therein below the lower collecting area FSB is shown in the plan view of the floor assembly BG of FIG. 16 seen.
- the sorption container SB is preferably mounted on the bottom BO of the washing container SPB such that its lid part DEL extends substantially parallel to the underside of the bottom BO and with a predetermined gap distance LSP thereto.
- the base SO is placed obliquely on the seated base stub STE with respect to the surface normal of the cover part DEL with a corresponding inclination angle.
- the sorbent SB a cup-shaped housing part GT, which is closed with a cover part DEL.
- At least the sorption unit SE with reversibly dehydratable sorption material ZEO is provided in the cup-shaped housing part GT.
- the sorption unit SE is accommodated in the cup-shaped housing part GT in such a way that its sorption material ZEO can be flowed through in or against the direction of gravity with an air flow LS2 generated by deflecting the air flow LS1 brought about via the air duct LK.
- the sorption unit SE has at least one lower sieve element or grating element US and at least one upper sieve element or grating element OS at a predefinable height distance H from one another (see in particular FIG Figure 9 ).
- cup-shaped housing part GT At least one heating device HZ is provided.
- the heating device HZ In the cup-shaped housing part GT viewed in the direction of flow DSR of the sorbent SB, the heating device HZ is provided in particular in front of the sorption SE with the reversibly dehydratable sorbent ZEO.
- the heating device HZ is provided in a lower cavity UH of the cup-shaped housing part GT for collecting inflowing air LS1 from the air duct LK.
- cup-shaped Housing part GT is the inlet opening EO provided for the air duct LK.
- the outlet opening AO In the cover part DEL the outlet opening AO is provided for the outlet element OFF.
- a heat-resistant material in particular metal sheet, preferably stainless steel or a stainless steel alloy is used.
- the cover part DEL closes the pot-shaped housing part GT largely hermetically.
- the peripheral outer edge of the cover part DEL is connected to the upper edge of the cup-shaped housing part GT only by a mechanical connection, in particular by a forming, joining, latching, clamping, in particular by a beaded connection, or clinch connection.
- the cup-shaped housing part GT has one or more side walls SW1, SW2 (see FIG. 5 ), which are substantially vertical. It has an outer contour shape that substantially corresponds to the inner contour shape of a mounting area EBR provided for it, in particular in a floor assembly BG (see FIG FIG.
- the two adjoining side walls SW1, SW2 have outer surfaces that are substantially perpendicular to each other.
- At least one side wall, such as SW2 has at least one formation, such as AF, which is substantially complementary to a formation on the rear wall and / or side wall of the bottom assembly BG provided below the bottom BO of the purge bin SPB.
- the sorption container SB is provided in a rear corner region EBR between the rear wall RW and an adjacent side wall SW of the dishwasher GS, in particular its bottom assembly BG.
- the cup-shaped housing part GT has at least one passage opening DUF for at least one electrical contact element AP1, AP2 (see FIG. 4 ).
- a drip protection plate TSB is attached at least over the extent thereof.
- the drip protection plate TSB has a drainage slope.
- FIG. 4 shows a schematic and perspective exploded view of the various components of the sorbent SB in the disassembled state.
- the components of the sorption container SB are arranged one above the other in several situation levels. This stacked from bottom to top construction of the sorbent SB is particularly in the sectional view of FIG. 9 as well as in the cutaway perspective view of FIG. 10 illustrated.
- the sorption SB has the bottom, lower cavity UH, for collecting inflowing air from the inlet port ES on. Above this lower cavity UH sits a slotted sheet SK, which serves as a flow conditioning agent for a pipe coil heater HZ arranged above it.
- the slotted sheet SK sits on an all around in the interior of the sorbent SB circumferential support edge.
- This support edge has over the inner bottom of the sorbent SB a predetermined height distance to form the lower cavity UH.
- the slotted sheet SK preferably has one or more clamping parts in order to jam it laterally or laterally with a partial surface, at least one inner wall of the sorption container SB. As a result, a reliable storage protection for the slotted sheet SK can be provided.
- According to the bottom view of the slotted sheet of FIG. 6 has these slots SL, which follow substantially the course of the Windungsverlauf arranged over the slot plate coil heater.
- the slots or passages SL of the slotted plate SK are formed at those locations at which the air flow LS1 entering the sorption container SB in the throughflow direction DSR of the sorbent container SB has a lower velocity is greater, in particular wider or wider, than at those locations in which the air flow LS1 entering the sorption container has a greater velocity in the throughflow direction DSR of the sorption container SB.
- a substantial homogenization of the local flow cross-sectional profile of the air flow LS2 is achieved, which flows through the sorption container SB from bottom to top in the throughflow direction DSR.
- homogenizing the local flow cross-sectional profile of the air flow means in particular that essentially the same volume of air passes through the same flow rate at each entry point of a flow area.
- the coil heater RZ is arranged with a predetermined height clearance in the direction of flow DSR behind the slotted sheet SK. For this purpose, it can be held at a height distance above the passages SL by means of a plurality of sheet metal parts BT, which are web-like. These sheet metal parts BT (see FIG. 6 ) support preferably alternately once from below and once from above the coil heater in their course. As a result, on the one hand a reliable Lankfundfeld the pipe coil heater HZ on the slotted sheet SK allows. On the other hand are distortions of the slot plate SK, which under the Heat development of the coil heater HZ could occur, largely avoided.
- the coil heater HZ When viewed in the direction of flow DSR, the coil heater HZ follows a free space ZR (see FIG Fig. 9 ), until the air flow LS2 ascending substantially from the bottom upwards enters the inlet cross-sectional area SDF of the sorption unit SE.
- This sorption unit SE has on the input side a lower screen element or grid element US.
- an output-side, upper screen element or grid element OS is provided at a height distance H from this screen element or grid element US.
- an output-side, upper screen element or grid element OS is provided at a height distance H from this screen element or grid element US.
- an output-side, upper screen element or grid element OS is provided for the two sieve elements US, OS, are provided on the inner walls of the sorption container sections or all around support edges to position the screen elements US, OS in their associated altitude and hold.
- the two screen elements US, OS are preferably arranged parallel to each other in this predetermined height distance H.
- the sorption material ZEO is filled in such a way that the volume between the two sieve elements US, OS is largely completely filled.
- the input-side screen element US and the output side screen element OS relative to the vertical center axis of the sorbent SB or based on the flow direction DSR in substantially horizontal planes of position above one another with the predetermined height distance H from each other.
- the sorption unit SE is formed by a filling volume of sorption material ZEO between a lower sieve element US and an upper sieve element OS.
- the upper cavity OH for collecting outflowing air is provided above the sorption unit SE. This outflowing air LS2 is led through the outlet AO of the base nozzle STE into the blow-off nozzle ATK, from where it is blown out into the interior of the washing container SPB.
- slotted sheet SK flow conditioning or flow influencing of the flow LS2 ascending from bottom to top in the direction of flow DSR is performed such that the coil heater is substantially surrounded by substantially the same volume of air flow at each point of its longitudinal course.
- slotted plate and arranged above pipe coil heater HZ is largely ensured that the air flow LS2 in front of the entrance surface of the lower screen US Sorption unit SE can be heated largely uniformly during the desorption process.
- the slotted sheet ensures a largely uniform local distribution of the heated air volume flow over the inlet cross-sectional area STF of the sorption unit SE.
- the slotted sheet SK it may also be expedient to provide a heating device outside of the sorption container BE in the connection section between the fan unit LT and the inlet opening of the sorption container SB. Since the average cross-sectional area of this tubular connecting portion VA is smaller than the average cross-sectional area of the sorbing tank SB for an air flow, the air flow LS1 before it enters the sorption SB can be heated in advance largely uniformly for the desorption process. Then, if necessary, the slotted sheet SK completely eliminated.
- the heating of the air takes place by means of a heating device in the sorption container SB
- the sorption process in particular, during which the heating device HZ is deactivated, ie switched off, is largely achieved in that all sorption material is largely completely involved in the dehumidification of the air flowing through LS1.
- the flow cross-sectional area SDF of the sorption unit SE in the interior of the sorption container SB is here larger in the embodiment than the average cross-sectional area of the end-side inlet nozzle ES of the air duct LK or of the tubular connection portion VA.
- the flow cross-sectional area SDF of the sorption material is preferably between 2 and 40 times, in particular between 4 and 30 times, preferably between 5 and 25 times, larger than the average cross-sectional area of the inlet nozzle ES of the air duct LK, with this opens into the inlet opening EO of the sorbent SB.
- the sorbent material ZEO fills a bulk volume between the lower sieve element US and the upper sieve element OS such that the flow inlet cross-sectional area SDF and a flow exit cross-sectional area SAF are substantially perpendicular to the flow direction DSR which extends in the vertical direction.
- the lower sieve element US, the upper sieve element OS and the sorption material ZEO interposed therebetween each have mutually congruent penetration surfaces for the air LS2 flowing through. This largely ensures that at any point in the volume of sorption unit SE whose sorption material can be acted upon by about the same volume flow. As a result, during the desorption overheating points and thus any damage to the sorbent ZEO are largely avoided.
- sorption a uniform absorption of moisture from the air to be dried and thus optimum utilization of the sorption material ZEO provided in the sorption unit SE are made possible.
- one or more flow conditioning elements SK in the sorption tank SB and / or in an input pipe section VA, ES of the air duct LK, in particular after at least one fan unit LT inserted into the air duct LK, with one or more air passages SL, that a homogenization of the local flow cross-sectional profile of the air flow LS2 is effected when flowing through the sorption container SB in its bottom-upward flow direction DSR.
- at least one of its lower cavity UH is at least one Flow conditioning SK provided with height distance in front of the heater HZ.
- a slotted sheet or perforated plate is provided here in the embodiment.
- the slots SL in the slotted sheet SK essentially follow the winding course of a coil heater HZ, which is positioned with free space above the slits SL in the slotted sheet as a heating device.
- the slotted plate is arranged substantially parallel to and at a free space distance from the air inlet cross-sectional area SDF of the sorption unit SE of the sorption container SE.
- Air passages, in particular slits SL, in the flow conditioning element SK are formed at those locations at which the airflow LS1 entering the sorption container SB in the flow direction DSR of the sorbent container SB has a lower velocity than at those locations at which the sorbent container SB enters Air flow LS1 in the flow direction DSR of the sorbent SB has a greater speed.
- the sorting drying system TS has the following specific flow conditions in the region of the sorption container SB.
- the air duct LK is coupled to the sorbent vessel SB such that the incoming air flow LS1 enters the sorbent vessel SB with an inflow direction ESR and merges into a different flow direction DSR with which it flows through the interior of the sorbent vessel SB.
- the outlet flow direction of the air flow LS2 emerging from the sorption container SB essentially corresponds to the throughflow direction DSR.
- the inlet-side pipe section RA1 of the air duct LK opens into the sorption SB so that its inflow ESR in the flow direction DSR of the sorbent SB, in particular between 45 ° and 135 °, preferably by about 90 °, is deflected.
- the fan unit LT In the flow direction, in front of the sorption container SB, at least the fan unit LT is inserted into the inlet-side tube section RA1 of the air-guiding channel LK for generating a forced air flow LS1 in the direction of at least one inlet opening EO of the sorbent container SB.
- the fan unit LT is arranged in the floor assembly BG below the washing container SPB.
- the flow cross-sectional area SDF for the sorption material ZEO inside the sorption container SB is formed larger than the passage cross-sectional area of the inlet nozzle ES of the air duct LK, with which this in the Inlet EO of the sorbent SB opens.
- the flow cross-sectional area SDF of the sorption container SB is preferably between 2 and 40 times, in particular between 4 and 30 times, preferably between 5 and 25 times, larger than the passage cross-sectional area of the end-side inlet nozzle ES of the air guide channel LK. with which this opens into the inlet opening EO of the sorbent SB.
- At least one sorption unit SE with sorption material ZEO is accommodated in the sorption container such that the sorption material ZEO can be flowed through air LS1 essentially in or counter to the direction of gravity, which is led out of the rinsing container SPB into the sorption container SB via the air guidance channel LK.
- the sorption unit SE of the sorption container SB has at least one lower sieve element or grating element US and at least one upper sieve element or grating element OS at a predefinable height distance H from one another, wherein the volume of space between the two sieve elements or grating elements US, OS is largely completely filled with the sorption material ZEO ,
- the inlet cross-sectional area SDF and the outlet cross-sectional area SAF of the sorption unit SE of the sorption container SB are in particular selected to be substantially the same size.
- the inlet cross-sectional area SDF and the outlet cross-sectional area SAF of the sorption unit SE of the sorption container SB are expediently also arranged substantially congruent to one another.
- the sorption container has, viewed in its throughflow direction DSR, at least one stratification of a lower cavity UH and a sorption unit SE arranged above it and arranged downstream in the flow direction DSR. He has in his lower cavity UH at least one heater HZ.
- the sorption container SE has, via its sorption unit SE, at least one upper hollow space OH for collecting outflowing air LS2.
- the sorption material ZEO fills a bulk volume in such a way that a flow inlet cross-sectional area SDF arranged essentially perpendicular to the throughflow direction DSR and a flow exit cross-sectional area SAF arranged largely parallel thereto are formed.
- the sorption container has in its upper cover part DEL at least one outflow opening AO, which is connected via a passage opening DG in the bottom BO of the washing container SPB with its interior by means of at least one Ausströmbauteils AKT.
- the sorption material ZEO is stored in the sorption container SB in an advantageous manner in the form of the sorption unit SE, such that essentially every entry point of the passage cross-sectional area SDF of the sorption unit SE can be acted upon by a substantially identical air volume flow value.
- the sorbent material ZEO is preferably an aluminum and / or silicon oxide-containing, reversibly dehydratable material, silica gel, and / or zeolite, in particular zeolite of type A, X, Y, alone or in any desired combination.
- the sorption material is expediently provided in the sorption container SB in the form of a granular solid or granules having a multiplicity of particle bodies with a particle size substantially between 1 and 6 mm, in particular between 2.4 and 4.8 mm, the bed height H the particle body at least 5 times their grain size corresponds.
- the sorption material ZEO present as a granular solid or granulate expediently exists in the direction of gravity in the sorption container with a bulk height which corresponds essentially to 5 to 40 times, in particular 10 to 15 times, the particle size of the granular solid or granules.
- the bed height H of the sorbent material ZEO is preferably selected substantially between 1.5 and 25 cm, in particular between 2 and 8 cm, preferably between 4 and 6 cm.
- the granular solid or granules may preferably be formed from a plurality of substantially spherical particle bodies.
- the sorption material ZEO which is in the form of a granular solid or granulate, advantageously has an average bulk density of at least 500 kg / m 3 , in particular substantially between 500 and 800 kg / m 3 , in particular between 600 and 700 kg / m 3 , in particular between 630 to 650 kg / m 3 , particularly preferably from about 640 kg / m 3 , on.
- the reversibly dehydratable sorbent material ZEO for absorbing a moisture amount transported in the air flow LS2 is expediently provided with such a weight amount that the amount of moisture absorbed by the sorption material ZEO is less than an amount of liquid applied to the items to be washed, in particular an amount of liquid applied in the final rinse step. is.
- the reversibly dehydratable sorption material with such a weight amount is provided in the sorption container SB, that this is sufficient to absorb a moisture amount, which corresponds substantially to a wetting amount, with which the items to be washed is wetted after the end of a rinse step.
- the amount of absorbed water preferably corresponds to between 4 and 25%, in particular between 5 and 15%, of the amount of liquid applied to the items to be washed.
- sorbent SB a weight amount substantially between 0.2 and 5 kg, in particular between 0.3 and 3 kg, preferably between 0.5 and 2.5 kg, housed in sorbent ZEO.
- the sorption material ZEO in particular has pores preferably with a size substantially between 1 and 12 angstroms, in particular between 2 and 10, preferably between 3 and 8 angstroms.
- a sorption material is provided which is desorbable at a temperature substantially in the range between 80 ° and 450 ° C, in particular between 220 ° and 250 ° C.
- the air duct, the sorption, and / or one or more additional flow influencing elements are suitably designed such that by the sorbent material for its sorption and / or desorption an air flow with a flow rate substantially between 2 and 15 l / sec, in particular between 4 and 7 l / sec is effected.
- the sorption material ZEO is assigned at least one heating device HZ with which an equivalent heating power between 250 and 2500 W, in particular between 1000 and 1800 W, preferably between 1200 and 1500 W, can be provided for heating the sorption material for its desorption is.
- the ratio of heating power of at least one heating device, which is assigned to the sorption material for its desorption, and air volume flow of the air flow flowing through the sorbent material between 100 and 1250 W sec / l, in particular between 100 and 450 W sec / l, preferably between 200 and 230 W sec / l, selected.
- the bed height H of the sorption material ZEO is essentially constant over the inlet cross-sectional area SDF of the sorbent container SB.
- the sorption material for absorbing an amount of water essentially between 150 and 400 ml, in particular between 200 and 300 ml, in the sorption container SB.
- At least one component of the sorption drying system TS at least one thermal overheating protection device TSI (see FIGS. 4 . 6, 8, 9 ) intended.
- a component may preferably be formed by a component of the sorbent container SB.
- At least one thermal overheating protection device TSI can be assigned to this component.
- This thermal overheat protection device TSI is mounted on the outside of the sorption SB.
- thermal overheating protection device at least one electrical temperature protection unit is provided. It is assigned here in the embodiment of the heating device HZ, which is housed in the sorption SB.
- the electrical temperature protection unit is in the embodiment of FIGS. 4 . 6, 8 and 9 provided in an outside indentation EBU on the inner housing IG of the sorbent container SB in the high-level region of the heating device HZ. It comprises at least one electric thermal switch TSA and / or at least one safety fuse SSI (see FIG. 17 ).
- the electrical thermal switch TSA and / or the fuse SSI of the electrical temperature protection unit TSI are respectively, preferably in series, in at least one power supply line UB1, UB2 the heater HZ inserted (see FIG. 8 ).
- At least one control device HE, ZE (see FIG. 16 ), which interrupts the energy supply to the heating device HZ in particular in the event of a fault.
- An error case is formed for example by exceeding an upper temperature limit.
- the largely freely suspended suspension of the sorption container in particular below the bottom BO of the washing container SPB, can also be used.
- the thermal overheating protection device may further comprise a mounting of the sorption container SB such that the sorption container SB has a predetermined minimum gap distance LSP with respect to adjacent components and / or parts of a base assembly BG.
- At least one outer housing AG may be provided in addition to the inner housing IG of the sorption container SB, in addition to or independently of the above measures, at least in the region of the sorption unit SE of the sorption container SB. Between the inner housing IG and the outer housing AG while an air gap clearance LS is present as a thermal insulation layer.
- the coil heater HZ the FIGS. 4 . 7, 8, 9 has two terminal poles AP1, AP2, which are guided through corresponding passage openings in the housing of the washing compartment SB to the outside.
- Each terminal pin AP1, AP2 is preferably connected in series with an overheat protection element.
- the overheat protection elements are combined in the temperature fuse unit TSI, which is arranged on the outside of the housing of the sorption container SB in the vicinity of the two pole pins AP1, AP2.
- FIG. 17 shows the overheating protection circuit for the coil heater HZ of FIG. 8 ,
- the first bridging line UB1 is attached to the first, rigid pole pin AP1 by means of a welded joint SWE1.
- the second, rigid Polw AP2 by means of a welded joint SWE2 the second bridging line UB2 attached.
- the bridging line UP2 is electrically contacted with the thermal switch TSA.
- the bridging line UB1 is electrically connected to the thermoelectric fuse SSI via a plug contact SV3.
- a first power supply line SZL1 is connected via a plug-in connection SV1 to a connection lug AF1 of the fuse element SSI guided to the outside.
- a second power supply line SZL2 is connected via a plug connection SV2 to the outwardly guided connection lug AF2 of the thermal switch element TSA.
- the second power supply line SZL2 forms a neutral, while the first power supply line SZL1 can be a "live phase".
- the thermal switch TSA opens as soon as a first upper limit for the temperature of the coil heater HZ is exceeded. As soon as this falls below again, it closes again, so that the coil heater HZ is heated again. However, if a critical upper temperature limit, which is above the first upper limit, reached for the coil heater HZ, the fuse SSI melts through and the circuit for the coil heater HZ is permanently interrupted.
- the two temperature fuse elements of the temperature protection device TSI are in largely intimate, heat-conducting contact with the inner housing IG of the sorption. They can be triggered separately from each other when certain specific upper temperature limits are exceeded.
- the splash guard SH is in the FIG. 12 shown schematically from above.
- the transition zones GF, URA it has convexly curved flattenings GF between its largely plane-surface top side and its side walls projecting substantially vertically downwards (viewed from the inside outwards) (see FIG FIG. 13 ) on. If a spray jet from the spray arm SA meets these edge zones flattened or arched transition zones GF, URA, then this film pours largely over the entire area over the splash guard SH and cools it during the desorption process.
- a lower edge zone UR of the semicircular cylinder-section-like side wall of the splash guard SH is curved toward the inside in the direction of the outflow AKT or arched. This is good FIG. 13 seen.
- a circumferential, radially outwardly projecting spray water deflector element or shielding element PB, in particular baffle plate is provided in the area of the upper edge of the outflow connecting piece AKT. This is radially outward into the gap or gap between the circular cylindrical outflow AKT and the inner wall of the splash guard SH from.
- the deflection path is in FIG. 13 denoted by ALS.
- the outwardly projecting shielding element PB is in the embodiment of FIG. 13 supported at individual circumferential points of its outer edge by means of web elements SET with respect to the inner wall of the circumferential in the form of a ring segment portion side wall of the splash guard SH.
- the splash guard SH is arranged with respect to the outlet connection AKT with a free height distance to form a free space or cavity.
- FIG. 14 shows the splash guard SH viewed from below together with the outflow AKT.
- the shielding element PB shields the outlet opening of the Outflow nozzle AKT as laterally or laterally projecting edge or web substantially all around.
- the shielding element PB closes off the underside of the splash guard SH in the region of the rectilinear side wall facing the spray arm SA. Only in the semicircular curved portion of the splash guard SH between the shielding PB and the radially offset, outside concentrically arranged side wall of the splash guard SH a gap clearance LAO is released, through which the air from the outflow AKT can flow into the interior of the sump SPB.
- the gap clearance LAO is substantially sickle-shaped.
- the air flow LS2 is thereby forced to a deflection ALS, which deflects it from its vertical upward flow direction downwards, where it can emerge only through the crescent-shaped, partial circle portion-shaped gap clearance LAO in the lower part of the splash guard SH.
- the outflow AKT is expediently with such a height HO from the bottom BO from that its upper edge is higher than the level of intended for a rinsing process target total amount of rinsing or - foam amount.
- the outflow element AUS which is mounted on the output side of the sorption container SB and projects into the interior of the rinse container SPB, is thus expediently designed such that the air flow LS2 emerging from it is directed away from the spray arm SA.
- the outflowing airflow LS2 is directed into a rearward corner area between the rear wall RW and the adjacent side wall SW of the washing compartment.
- spray water or foam during cleaning or other flushing through the opening of the Ausströmstutzens can get into the interior of the sorption. This could impair or even nullify the desorption process.
- sorbent material could be permanently damaged by flushing liquid. Extensive tests have shown that the functionality of the sorption material in the sorption container can largely be preserved or preserved over the life of the dishwasher, if it is reliably prevented that no water, cleaning agent or rinse aid in the rinse water can enter the sorption material.
- At least one outflow device AUS which is connected to at least one outflow opening AO of the sorbent container SB, arranged in the interior of the washing container SPB, the air blown out of her LS2 of at least one housed in the washing container SPB sprayer SA is largely directed away.
- the outflow device AUS is arranged outside the working range of the spray device SA.
- the spraying device may, for example, be a rotating spray arm SA.
- the outflow device AUS is preferably provided in a rear corner region EBR between the rear wall RW and an adjacent side wall SW of the washing container SPB.
- the outflow device AUS has a blow-out opening ABO with a height clearance HO above the bottom BO of the rinse container SPB, which is higher than the level of a set rinse bath total amount provided for a rinse operation.
- the outflow device AUS comprises a discharge connection AKT and a splash protection cover SH.
- the splash guard SH has a geometry which has the blow-out opening ABO of the outflow nozzle AKT.
- the splash guard SH is slipped over the outflow AKT so that a downwardly flowing forced flow path ALS can be impressed by the outflow port AKT from the sorbent SB with an ascending flow direction high after air emerging from the exhaust port ABO of the outflow.
- the above the bottom BO of the washing container SPB upwardly projecting outflow AKT is coupled to the connection piece STE on the cover part DEL of the arranged under the bottom BO sorption SB.
- the splash guard SH is designed to be closed on its upper side and underside in its housing area GF facing the spraying device SA.
- the splash guard SH covers the blow-off opening ABO of the outlet connection AKT with an upper free space.
- the outflow branch AKT has an upper, outwardly curved edge or circumferential collar KR.
- the splash guard SH envelopes an upper end portion of the outflow AKT such that between its inner wall and the outer wall of the outflow AKT a clearance SPF is formed.
- the gap SPF between the splash guard SH and the outflow AKT is formed such that an Luftausströmweg ALS is provided from the outflow AKT, which is directed away from the spray SA in the washing container SB.
- a projecting into the gap SPF SPITZ Spritzwasserabweiselement is provided at the outflow AKT .
- a lower edge zone UR of the splash guard SH is curved inwards.
- the splash guard SH has such a rounded outer surface, that it can pour an incident spray of the spray SA to film over its surface.
- FIG. 15 shows a schematic longitudinal sectional view of the fixation of the inlet side, front end portion ET of the air duct LK in the region of the outlet opening ALA in the side wall SW of the washing compartment SPB of FIG. 2 ,
- the front end section ET of the air duct LK protrudes into the interior of the washing compartment SPB in such a way that a collar edge projecting vertically against the side wall SW is formed.
- This has an internal thread SG.
- an annular inlet element IM is screwed with an external thread. It thus acts as a fixing element for holding the end portion ET.
- This annular fixing element has a toroidal, round receiving chamber for a sealing element DI2.
- This sealing element DI2 seals an annular gap between the outer edge of the inlet-side, end-side end section ET of the air duct LK and the fixing element.
- the fixing element is formed here in the exemplary embodiment in particular by a union nut-like screw ring, which is bolted to the inlet side, front end portion ET of the air duct LK.
- the annular fixing element IM a central passage MD, can be sucked through the air LU from the interior of the washing container SPB.
- At least one rib-shaped engagement protection in / or in front of the inlet opening MD of the inlet-side tube section ET of the air-guiding channel LK, which has freely continuous gaps between its engagement ribs RIP for the inflow of air from the rinsing container.
- These ribs RIP are indicated by dash-dotted lines.
- FIG. 16 shows in a schematic plan view of the bottom assembly BG. It comprises, in addition to the fan unit LT, the sorption tank SB, the circulation pump UWP, etc., a main control unit HE for controlling and checking it.
- the heating device HZ of the sorption container SB is also regulated for its desorption process by means of at least one control device. This is formed here in the embodiment by an additional control device ZE. It serves to the Disconnect the power supply line SZL to the heating device HZ as required or connect it through.
- the additional control device ZE is controlled by the main control unit HE via a bus line BUL. From the main controller HE, a power supply line SVL is guided to the additional control device ZE. It also controls the fan unit LT via a control line SLL. In particular, the power supply line of the fan unit LT can also be integrated in the control line SLL.
- the temperature sensor TSE is between stiffening ribs VR (see FIG. 3 ) suspended in the space between the two legs of the inlet side pipe section RA1 of the air duct LK. In this case, it is brought into contact with the side wall SW of the washing container SPB.
- the main control device HE simultaneously activates the additional control device ZE via the bus line BUL in such a way that an electrical voltage is applied to the pole pins AP1, AP2 of the heating device HZ via the current connection line SZL.
- the main control unit HE can determine via the measuring signals of the temperature sensor, it can instruct the additional control unit ZE via the bus line BUL to remove the voltage at the power supply line SZL and thereby the heating device HZ completely switch off.
- the desorption process for the sorbent material in the sorption tank to be terminated.
- FIG. 16 This is schematically illustrated by the fact that a program key or a program menu item PG1 is located, which via a control line SL1 means Control signals SS1 of the control logic HE corresponding activation or deactivation signals to turn on and off the Sorptionstrockensystems TE.
- a first selection key for selecting a program variant "energy” or "sorption operation” can be provided in the control panel of the dishwasher.
- This program focuses on saving energy. This is achieved in that the rinse process is not heated at all by means of a continuous flow heater and the drying of the items to be washed, in particular of the dishes, is effected solely by means of the sorption drying system TS.
- the sorption drying system that is now being used can be used to save electrical heating energy by sorption of air humidity. Thus, it can be achieved both by so-called “self-heat drying” and by sorption drying, i. By combining or supplementing both types of drying, an improved drying of wet or moist ware can be achieved.
- Another button “Drying capacity” may be provided in the control panel of the dishwasher, which increases the fan run time of the fan unit. As a result, an improved drying of all crockery parts can be achieved.
- another "program runtime" key may be provided. If the sorption drying system is switched on, the program runtime can be reduced compared to conventional drying systems (without sorption drying). Possibly. By further heating in the cleaning phase and optionally by increasing the spraying pressure by increasing the motor speed of the circulation pump, the running time during cleaning can be further shortened. Furthermore, by increasing the rinse temperature, the drying time can be further reduced.
- an operating button with the function "influencing the cleaning performance” may be provided.
- the cleaning performance can be increased while the running time remains constant, without the energy consumption being increased compared to a dishwasher without a sorption drying system. Because by the fact that at the same time the sorption process is started during the cleaning process and thereby hot air, which is loaded with a leaked from the sorbent amount of water, enters the washing, heating energy can be saved for heating a desired Spülbad total amount of liquid.
Landscapes
- Washing And Drying Of Tableware (AREA)
Description
Die vorliegende Erfindung betrifft eine Geschirrspülmaschine, insbesondere Haushaltsgeschirrspülmaschine, mit mindestens einem Spülbehälter und mindestens einem Sorptionstrocknungssystem zum Trocknen von Spülgut, wobei das Sorptionstrocknungssystem mindestens einen Sorptionsbehälter mit reversibel dehydrierbarem Sorptionsmaterial aufweist, der über mindestens einen Luftführungskanal mit dem Spülbehälter zur Erzeugung einer Luftströmung verbunden ist.The present invention relates to a dishwasher, in particular a domestic dishwasher, with at least one rinsing container and at least one sorption drying system for drying items to be washed, wherein the sorption drying system has at least one sorption container with reversibly dehydratable sorption material, which is connected via at least one air duct with the rinsing container for generating an air flow.
Z.B. aus der
Aus
Der Erfindung liegt die Aufgabe zugrunde, eine Geschirrspülmaschine, insbesondere Haushaltsgeschirrspülmaschine, mit weiter verbessertem Sorptions- und/oder Desorptionsergebnis für das reversibel dehydrierbare Trockenmaterial der Sorptionseinheit ihrer Sorptionstrocknungsvorrichtung bereitzustellen.The object of the invention is to provide a dishwasher, in particular a domestic dishwasher, with further improved sorption and / or desorption results for the reversibly dehydratable dry material of the sorption unit of its sorption drying apparatus.
Diese Aufgabe wird bei einer Geschirrspülmaschine der eingangs genannten Art dadurch gelöst, dass der Sorptionsbehälter ein topfförmiges Gehäuseteil aufweist, das mit einem Deckelteil verschlossen ist.This object is achieved in a dishwasher of the type mentioned above in that the sorption container has a pot-shaped housing part which is closed by a cover part.
Ein umlaufender Außenrand des Deckelteils ist mit dem oberen Rand des topfförmigen Gehäuseteils lediglich durch eine mechanische Verbindung, insbesondere durch eine Umform-, Füge-, Rast-, Klemm-, insbesondere durch eine Umbördelverbindung, oder Clinchverbindung, verbunden.A peripheral outer edge of the cover part is connected to the upper edge of the cup-shaped housing part only by a mechanical connection, in particular by a forming, joining, latching, clamping, in particular by a beaded connection, or clinch connection.
Dadurch ist weitgehend sichergestellt, dass Spülgut im Spülbehälter einwandfrei, energieeffizient und zuverlässig getrocknet werden kann. Darüber hinaus ist eine kompakte Unterbringung der Trocknungseinrichtung in der Geschirrspülmaschine ermöglicht.This largely ensures that items to be washed in the washing can be properly, energy-efficiently and reliably dried. In addition, a compact housing of the drying device in the dishwasher is possible.
Insbesondere ist weitgehend sichergestellt, dass feuchte Luft, die beim jeweilig gewünschten Trocknungsvorgang über den Luftführungskanal aus dem Spülbehälter in den Sorptionsbehälter geführt ist und dessen Sorptionseinheit mit dem Sorptionstrocknungsmaterial durchströmt, durch Sorption mittels des Sorptionstrocknungsmaterial einwandfrei, zuverlässig und energieeffizient getrocknet werden kann. Später nach diesem Trocknungsvorgang, z.B. bei mindestens einem Spül- oder Reinigungsvorgang eines späteren, neu gestarteten Geschirrspülprogramms, kann das Sorptionsmaterial zur Aufbereitung für einen nachfolgenden Trocknungsvorgang einwandfrei, energieeffizient und materialschonend wieder durch Desorption regeneriert, d.h. aufbereitet werden.In particular, it is largely ensured that moist air, which is passed through the air duct during the respective desired drying process from the washing into the sorption and sorption unit flows through the Sorptionstrocknungsmaterial can be dried properly by sorption by means of Sorptionstrocknungsmaterial, reliable and energy efficient. Later after this drying process, e.g. in at least one rinsing or cleaning process of a later, newly started dishwashing program, the sorbent can be regenerated properly for desorption for a subsequent drying process, energy-efficient and gentle on the material by desorption, i. be prepared.
Sonstige Weiterbildungen der Erfindung sind in den Unteransprüchen wiedergegeben.Other developments of the invention are given in the dependent claims.
Die Erfindung und ihre Weiterbildungen werden nachfolgend anhand von Zeichnungen näher erläutert.The invention and its developments are explained in more detail with reference to drawings.
Es zeigen:
- Fig. 1
- schematisch eine Geschirrspülmaschine mit einem Spülbehälter und einem Sorptionstrocknungssystem, dessen Komponenten nach dem erfindungsgemäßen Konstruktionsprinzip ausgebildet sind,
- Fig. 2
- schematisch in perspektivischer Darstellung den geöffneten Spülbehälter der Geschirrspülmaschine von
Figur 1 mit Komponenten des Sorptionstrocknungssystems, die teilweise freigelegt, d.h. ohne Abdeckung eingezeichnet sind, - Fig. 3
- in schematischer Seitenansicht die Gesamtheit des Sorptionstrocknungssystems von
Figur 1 ,2 , deren Komponenten teilweise außen an einer Seitenwand des Spülbehälters sowie teilweise in einer Bodenbaugruppe unterhalb des Spülbehälters untergebracht sind, - Fig. 4
- als Einzelheit schematisch in perspektivischer Explosionsdarstellung verschiedene Bauteile des Sorptionsbehälters der Sorptionstrocknungsvorrichtung der
Figuren 1 mit 3, - Fig. 5
- schematisch in Draufsicht den Sorptionsbehälter von
Figur 4 , - Fig. 6
- in schematischer Draufsicht von unten betrachtet als Bauteil des Sorptionsbehälters von
Figur 5 ein Schlitzblech zur Strömungskonditionierung von Luft, die Sorptionsmaterial im Sorptionsbehälter durchströmt, - Fig. 7
- in schematischer Draufsicht von unten betrachtet als weitere Einzelheit des Sorptionsbehälters von
Figur 4 eine Rohrschlangenheizung zum Aufheizen von Sorptionsmaterial im Sorptionsbehälter zu dessen Desorption, - Fig. 8
- in schematischer Draufsichtsdarstellung von oben betrachtet die Rohrschlangenheizung von
Figur 7 , die oberhalb dem Schlitzblech vonFigur 6 angeordnet ist, - Fig. 9
- in schematischer Schnittdarstellung von der Seite her betrachtet den Sorptionsbehälter der
Figuren 4 ,5 , - Fig. 10
- in schematischer Perspektivdarstellung den Innenaufbau des Sorptionsbehälters der
Figuren 4 ,5, 9 im teilweise aufgeschnittenen Zustand, - Fig. 11
- in schematischer Draufsichtsdarstellung von oben betrachtet die Gesamtheit der Komponenten des Sorptionstrocknungssystems der
Figuren 1 bis 10 , - Fig. 12 mit 14
- schematisch in verschiedenen Ansichten das Auslasselement des Sorptionstrocknungssystems der
Figuren 1 mit 3 als Einzelheit, - Fig. 15
- in schematischer Schnittdarstellung von der Seite her betrachtet das Einlasselement des Sorptionstrocknungssystems der
Figuren 1 mit 3 als Einzelheit, - Fig. 16
- in schematischer Draufsichtsdarstellung von oben betrachtet die Bodenbaugruppe der Geschirrspülmaschine von
Figur 1 sowieFigur 2 , und - Fig. 17
- in schematischer Darstellung die thermoelektrische Hitzeabsicherung des Sorptionsbehälters der
Figuren 4 mit 10 des Sorptionstrockungssystems derFiguren 1 mit 3, 11.
- Fig. 1
- 1 is a schematic illustration of a dishwasher with a rinsing container and a sorption drying system whose components are designed according to the design principle according to the invention,
- Fig. 2
- schematically in perspective view of the open washing container of the dishwasher
FIG. 1 with components of the sorption drying system, which are partially exposed, ie drawn without cover, - Fig. 3
- in a schematic side view of the entirety of the Sorptionstrocknungssystems of
FIG. 1 .2 the components of which are accommodated partly on the outside of a side wall of the washing container and partly in a base assembly below the washing container, - Fig. 4
- As a detail schematically in perspective exploded view of various components of the sorption of the sorption drying device of
FIGS. 1 with 3, - Fig. 5
- schematically in plan view the sorption of
FIG. 4 . - Fig. 6
- seen in a schematic plan view from below as a component of the sorption of
FIG. 5 a slotted sheet for conditioning the flow of air through sorption material in the sorption tank, - Fig. 7
- seen in a schematic plan view from below as another detail of the sorption of
FIG. 4 a coil heater for heating sorption material in the sorption container for its desorption, - Fig. 8
- in a schematic plan view from above the coil heater of
FIG. 7 above the slotted sheet ofFIG. 6 is arranged - Fig. 9
- in a schematic sectional view of the side viewed from the sorption of the
FIGS. 4 .5 . - Fig. 10
- in a schematic perspective view of the internal structure of the sorption of the
FIGS. 4 .5, 9 in the partially cut state, - Fig. 11
- in a schematic plan view from above, the entirety of the components of the Sorptionstrocknungssystems the
FIGS. 1 to 10 . - Fig. 12 with 14th
- schematically in different views the outlet of the Sorptionstrocknungssystems the
FIGS. 1 with 3 as a detail, - Fig. 15
- viewed in a schematic sectional view from the side, the inlet member of the Sorptionstrocknungssystems the
FIGS. 1 with 3 as a detail, - Fig. 16
- in a schematic plan view from above the bottom assembly of the dishwasher of
FIG. 1 such asFIG. 2 , and - Fig. 17
- in a schematic representation of the thermoelectric heat protection of the sorption of the
FIGS. 4 with 10 of sorption drying system ofFIGS. 1 with 3, 11.
Elemente mit gleicher Funktion und Wirkungsweise sind in den
Zur Reinigung von Spülgut durchlaufen Geschirrspülmaschinen Spülprogramme, die eine Mehrzahl von Programmschritten aufweisen. Das jeweilige Spülprogramm kann insbesondere folgende, zeitlich nacheinander ablaufende Einzel-Programmschritte umfassen: einen Vorspülschritt zur Entfernung grober Anschmutzungen, einen Reinigungsschritt mit Reinigungsmittelzugabe zu Flüssigkeit bzw. Wasser, einen Zwischenspülschritt, einen Klarspülschritt mit Aufbringen von mit Entspannungsmitteln bzw. Klarspüler versetzter Flüssigkeit bzw. Wasser, sowie einen abschließenden Trocknungsschritt, bei dem das gereinigte Spülgut getrocknet wird. Je nach Reinigungsschritt bzw. Spülvorgang eines gewählten Geschirrspülprogramms wird dabei mit Reiniger versetztes Frischwasser und/oder Brauchwasser z.B. für einen Reinigungsvorgang, für einen Zwischenspülgang, und/oder für einen Klarspülvorgang auf das jeweilig zu spülende Spülgut aufgebracht.Dishwashers undergo washing programs that have a plurality of program steps for cleaning items to be washed. The respective rinsing program can comprise in particular the following individual program steps which proceed one after the other: a pre-rinsing step for removing soiling, a cleaning step with detergent addition to liquid or water, an intermediate rinsing step, a rinsing step with application of liquid or water added with expansion agents or rinse aid , and a final drying step, in which the cleaned items is dried. Depending on the cleaning step or rinsing process of a selected dishwashing program, fresh water and / or service water mixed with detergent is added to this, for example. for a cleaning process, for an intermediate rinsing, and / or applied for a rinse on the respective items to be washed.
Die Lüftereinheit LT sowie der Sorptionsbehälter SB sind hier im Ausführungsbeispiel in der Bodenbaugruppe BG unterhalb des Bodens BO des Spülbehälters SPB untergebracht. Der Luftführungskanal LK verläuft von einer Auslassöffnung ALA, die oberhalb des Bodens BO des Spülbehälters SBP in dessen Seitenwand SW vorgesehen ist, außen an dieser Seitenwand SW mit einem einlassseitigen Rohrabschnitt RA1 nach unten zur Lüftereinheit LT in der Bodenbaugruppe BG. Über einen Verbindungsabschnitt VA des Luftführungskanals LK ist der Ausgang der Lüftereinheit LT mit einer Eintrittsöffnung EO des Sorptionsbehälters SB in dessen bodennahem Bereich verbunden. Die Auslassöffnung ALA des Spülbehälters SPB ist oberhalb dessen Bodens BO vorzugsweise im Mittenbereich bzw. im Zentralbereich der Seitenwand SW zum Ansaugen von Luft aus dem Inneren des Spülbehälters SPB vorgesehen. Alternativ dazu ist es selbstverständlich auch möglich, die Auslassöffnung ALA in der Rückwand RW (siehe
Die Lüftereinheit LT ist vorzugsweise als Axiallüfter ausgebildet. Sie dient der Zwangsbeströmung einer Sorptionseinheit SE im Sorptionsbehälter SB mit feucht-heißer Luft LU aus dem Spülbehälter SPB. Die Sorptionseinheit SE enthält reversibel dehydrierbares Sorptionsmaterial ZEO, das Feuchtigkeit aus der durch sie hindurchgeleiteten Luft LU aufnehmen und speichern kann. Der Sorptionsbehälter SB weist im deckennahen Bereich seines Gehäuses auf der Oberseite eine Ausströmöffnung AO (siehe
Die Auslassöffnung ALA ist vorzugsweise an einer Stelle oberhalb des Bodens BO angeordnet, die das Einsammeln bzw. Ansaugen von möglichst viel feucht-heißer Luft LU aus der oberen Teilhälfte des Spülbehälters SPB in den Luftführungskanal LK ermöglicht. Denn nach einem Reinigungsvorgang, insbesondere Klarspülvorgang mit aufgeheizter Flüssigkeit, sammelt sich feuchtheiße Luft vorzugsweise oberhalb des Bodens BO, insbesondere in der oberen Hälfte des Spülbehälters SPB. Die Auslassöffnung ALA liegt vorzugsweise in einer Höhenlage oberhalb des Pegels von Schaum, der beim regulären Spülbetrieb oder im Störfall auftreten kann. Insbesondere kann Schaum durch Reinigungsmittel im Wasser beim Reinigungsvorgang hervorgerufen werden. Zum anderen ist die Position der Austrittstelle bzw. Auslassöffnung ALA derart gewählt, dass für den einlassseitigen Rohrabschnitt RA1 des Luftführungskanals LK noch eine ansteigende Wegstrecke an der Seitenwand SW frei zur Verfügung steht. Durch die Austrittsöffnung bzw. Auslassöffnung im Mittenbereich, Deckenbereich, und/oder oberen Bereich der Seitenwand SW und/oder Rückwand RW des Spülbehälters SPB ist zudem weitgehend vermieden, dass Wasser aus dem Sumpf im Boden des Spülbehälters oder aus dessen Flüssigkeitsprühsystem durch die Auslassöffnung ALA des Spülbehälters SPB direkt in den Luftführungskanal LK eingespritzt und anschließend in den Sorptionsbehälter SB hineingelangen kann, was dort ansonsten dessen Sorptionsmaterial ZEO unzulässig feucht, teilweise beschädigen oder unbrauchbar machen, oder gar ganz zerstören könnte.The outlet opening ALA is preferably arranged at a location above the bottom BO, which allows the collection or suction of as much moist hot air LU from the upper half of the washing container SPB in the air duct LK. After a cleaning process, in particular rinsing with heated liquid, moist hot air preferably collects above the bottom BO, in particular in the upper half of the washing container SPB. The outlet opening ALA is preferably at an altitude above the level of foam, which may occur during regular flushing operation or in the event of a fault. In particular, foam can be caused by detergent in the water during the cleaning process. On the other hand, the position of the exit point or outlet opening ALA is selected such that a rising distance on the side wall SW is still freely available for the inlet-side pipe section RA1 of the air duct LK. The outlet opening or outlet opening in the middle region, ceiling region, and / or upper region of the side wall SW and / or rear wall RW of the washing container SPB also largely prevents water from the sump in the bottom of the washing container or from its liquid spraying system through the outlet opening ALA of the washing container Rinsing container SPB injected directly into the air duct LK and then can get into the sorbent SB, what else there sorption ZEO inadmissible damp, partially damage or unusable, or even completely destroyed.
Im Sorptionsbehälter SB ist in Strömungsrichtung betrachtet vor dessen Sorptionseinheit SE mindestens eine Heizungseinrichtung HZ zur Desorption und damit Regenerierung des Sorptionsmaterials ZEO angeordnet. Die Heizungseinrichtung HZ dient zur Aufheizung von Luft LU, die mittels der Lüftereinheit LT durch den Luftführungskanal LK in den Sorptionsbehälter hindurchgetrieben wird. Diese zwangsaufgeheizter Luft nimmt die gespeicherte Feuchtigkeit, insbesondere Wasser, aus dem Sorptionsmaterial ZEO beim Durchströmen durch das Sorptionsmaterial ZEO auf. Dieses aus dem Sorptionsmaterial ZEO ausgetriebene Wasser wird durch die aufgeheizte Luft über das Auslasselement AUS des Sorptionsbehälters SB in das Innere des Spülbehälters transportiert. Dieser Desorptionsvorgang findet vorzugsweise dann statt, wenn Flüssigkeit für einen Reinigungsvorgang oder sonstigen Spülvorgang eines nachfolgenden Geschirrspülprogramms durchgeführt wird. Dabei kann die für den Desorptionsvorgang durch die Heizungseinrichtung HZ erhitzte Luft gleichzeitig zur Erhitzung der Flüssigkeit im Spülbehälter SPB herangezogen werden, was energiesparend ist.In the sorption SB is viewed in the flow direction before the sorption SE at least one heater HZ for desorption and thus regeneration of the sorbent ZEO arranged. The heating device HZ is used to heat air LU, which is driven through the fan unit LT by the air duct LK in the sorption. This positively heated air absorbs the stored moisture, in particular water, from the sorption material ZEO as it flows through the sorption material ZEO. This expelled from the sorbent ZEO water is transported by the heated air through the outlet element AUS of the sorbent SB into the interior of the washing. This desorption process preferably takes place when liquid is carried out for a cleaning process or other rinsing process of a subsequent dishwashing program. It can be used for the desorption process heated by the heating device HZ be used simultaneously to heat the liquid in the washing container SPB, which is energy efficient.
Im Inneren des Krümmungsabschnitts KRA sind ein oder mehrere Strömungsleitrippen bzw. Ablaufrippen AR vorgesehen, die dessen Krümmungsverlauf nachfolgen. Im Ausführungsbeispiel sind mehrere bogenförmige Ablaufrippen AR im Wesentlichen konzentrisch ineinander geschachtelt sowie mit Querabstand zueinander im Inneren des Krümmungsabschnitts KRA angeordnet. Sie erstrecken sich hier im Ausführungsbeispiel auch in den ansteigenden Rohrabschnitt AU sowie in den abfallenden Rohrabschnitt AB auf einer Teillänge hinein. Diese Ablaufrippen AR sind in Höhenpositionen oberhalb des Auslasses ALA des Spülbehälters SPB bzw. des Einlasses EI des einlassseitigen Rohrabschnitts RA1 des Luftführungskanals LK angeordnet. Diese Ablaufrippen AR dienen dazu, Flüssigkeitströpfchen und/oder Kondensat aus der aus dem Spülbehälter SPB angesaugten Luftströmung LS1 aufzunehmen. Im Abschnittsbereich des nach oben ansteigenden Rohrabschnitts AU können die an den Strömungsleitrippen AR gesammelten Flüssigkeitströpfchen in Richtung des Auslasses ALA abtropfen. Im Bereich des nach unten abfallenden Rohrabschnitts AB können die Flüssigkeitströpfchen von den Strömungsleitrippen AR in Richtung auf eine Rücklaufrippe RR abtropfen. Die Rücklaufrippe RR ist dabei an einer Stelle im Inneren des abfallenden Rohrabschnitts AB vorgesehen, die höher als die Auslassöffnung ALA des Spülbehälters SPB bzw. die höher als die Einlassöffnung EI des Luftführungskanals LK liegt. Die Rücklaufrippe RR im Inneren des abfallenden Rohrabschnitts AB bildet dabei eine Ablaufschräge und fluchtet mit einer Querverbindungsleitung RF in Richtung auf den Auslass ALA des Spülbehälters SPB zu. Die Querverbindungsleitung RF überbrückt dabei den Zwischenraum zwischen dem Schenkel des nach oben ansteigenden Rohrabschnitts AU und dem Schenkel des nach unten abfallenden Rohrabschnitts AB. Die Querverbindungsleitung RF verbindet dabei das Innere des nach oben ansteigenden Rohrabschnitts AU sowie das Innere des nach unten abfallenden Rohrabschnitts AB miteinander. Das Gefälle der Rücklaufrippe RR sowie der sich daran anschließenden, fluchtenden Querverbindungsleitung RF ist derart gewählt, dass eine Kondensatrückführung von Kondenswasser- oder sonstigen Flüssigkeitströpfchen, die von den Ablaufrippen AR im Bereich des abfallenden Rohrabschnitts AB nach unten abtropfen, in die Auslassöffnung ALA des Spülbehälters SPB sichergestellt ist.In the interior of the curvature section KRA, one or more flow guide ribs or drainage ribs AR are provided, which follow its curvature profile. In the exemplary embodiment, a plurality of arcuate drainage ribs AR are substantially nested concentrically in one another and arranged at a transverse distance from one another in the interior of the curved section KRA. They extend here in the embodiment in the rising pipe section AU and in the sloping pipe section AB on a partial length. These drainage ribs AR are disposed at height positions above the outlet ALA of the purge tank SPB and the inlet EI of the inlet side pipe section RA1 of the air duct LK, respectively. These drainage ribs AR serve to receive liquid droplets and / or condensate from the air flow LS1 drawn in from the washing container SPB. In the section region of the upwardly rising pipe section AU, the flow guide ribs AR drip off collected liquid droplets in the direction of the outlet ALA. In the region of the downwardly sloping tube section AB, the liquid droplets can drip off the flow guide ribs AR in the direction of a return rib RR. The return rib RR is provided at a point in the interior of the sloping pipe section AB, which is higher than the outlet opening ALA of the washing container SPB or higher than the inlet opening EI of the air duct LK. The return rib RR in the interior of the sloping pipe section AB forms a drainage slope and is aligned with a cross-connection line RF in the direction of the outlet ALA of the washing compartment SPB. The cross-connection line RF bridges the gap between the leg of the upwardly rising pipe section AU and the leg of the downwardly sloping pipe section AB. The cross-connection line RF connects the interior of the upwardly rising pipe section AU and the interior of the downwardly sloping pipe section AB with each other. The slope of the return rib RR and the adjoining, aligned cross-connection line RF is selected such that a condensate return of condensate or other liquid droplets that drip down from the gutters AR in the region of the sloping pipe section AB, in the outlet opening ALA of the washing container SPB is ensured.
Die Ablaufrippen AR sind vorzugsweise auf der der Spülbehälterseitenwand SW abgewandten Innenwand des Luftführungskanals LK angebracht, da diese außenseitige Innenwand des Luftführungskanals kühler als die dem Spülbehälter SPB zugewandte Innenwand des Luftführungskanals ist. An dieser kühleren Innenwand schlägt sich Kondenswasser stärker als an der der Seitenwand SW zugewandten Innenwand des Luftführungskanals LK nieder. Es kann also genügen, wenn die Ablaufrippen AR als Stegelemente ausgebildet sind, die von der außen liegenden Innenwand des Luftführungskanals LK nur über eine Teilbreite der Gesamtquerschnittsbreite des als Flachkanal ausgebildeten Luftführungskanals in Richtung auf die innenliegende, der Seitewand SW zugewandten Innenwand des Luftführungskanals abstehen, so dass eine laterale Querschnittslücke zur Luftdurchströmung verbleibt. Gegebenenfalls kann es aber auch zweckmäßig sein, die Ablaufrippen AR zwischen der außen liegenden Innenwand und der innen liegenden Innenwand des Luftführungskanals LK durchgängig auszubilden. Dadurch wird insbesondere im Krümmungsabschnitt KRA eine gezieltere Luftführung erreicht. Störende Luftverwirbelung sind weitgehend vermieden. Auf diese Weise kann durch des als Flachkanal ausgebildeten Lüftführungskanals LK eine gewünschtes Luftvolumen gefördert werden.The drainage ribs AR are preferably mounted on the inner wall of the air duct LK facing away from the Spülbehälterseitenwand SW, since this outer side inner wall of the air duct is cooler than the flushing tank SPB facing inner wall of the air duct. At this cooler inner wall condensate precipitates stronger than on the side wall SW facing inner wall of the air duct LK down. It may therefore be sufficient if the drainage ribs AR are designed as web elements which protrude from the outer inner wall of the air duct LK only over a partial width of the total cross-sectional width of the formed as a flat channel air duct in the direction of the inner side wall SW facing inner wall of the air duct, so that a lateral cross-section gap remains for air flow. Optionally, however, it may also be expedient to design the drainage ribs AR continuously between the outer inner wall and the inner inner wall of the air duct LK. As a result, a more targeted air guidance is achieved, in particular in the curved section KRA. Disturbing air turbulence is largely avoided. This way you can be conveyed by the designed as a flat channel Lüftführungskanals LK a desired volume of air.
Die Rücklaufrippe RR ist vorzugsweise innenseitig an der außenliegenden Innenwand des Luftführungskanals LK als Stegelement angebracht, das auf einer Teilbreite bzw. Teilweite der Gesamtweite des flach ausgebildeten Luftführungskanals LK in Richtung auf dessen innenliegende Innenwand hin absteht. Dadurch ist sichergestellt, dass ein ausreichender Durchtrittsquerschnitt im Bereich der Rücklaufrippe RR zum Durchströmen des Luftstroms LS1 frei bleibt. Alternativ kann es selbstverständlich auch zweckmäßig sein, die Rücklaufrippe RR als durchgängiges Element zwischen der außenseitigen Innenwand und der innen liegenden Innenwand des Luftführungskanals LK vorzusehen und für den Luftdurchtritt insbesondere mittig liegende Durchtrittsöffnungen vorzusehen.The return rib RR is preferably mounted on the inside of the outer inner wall of the air duct LK as a web element, which protrudes in the direction of its inner inner wall on a partial width or partial width of the entire width of the flat formed air duct LK. This ensures that a sufficient passage cross-section remains free in the region of the return rib RR for the passage of the air flow LS1. Alternatively, it may of course also be expedient to provide the return rib RR as a continuous element between the outside inner wall and the inner inner wall of the air duct LK and provide for the passage of air in particular centrally located passages.
Die Ablaufrippen AR sowie die Rücklaufrippe RR dienen insbesondere auch dazu, Wassertröpfchen, Reinigungsmitteltröpfchen, Klarspülmitteltröpfchen, und/oder sonstige Aerosole, die sich in der einströmenden Luft LS1 befinden, abzuscheiden und durch die Auslassöffnung ALA in den Spülbehälter SPB zurückzuführen. Dies ist insbesondere vorteilhaft bei einem Desorptionsvorgang, wenn zeitgleich ein Reinigungsschritt stattfindet. Während dieses Reinigungsschritts kann sich relativ viel Dampf bzw. Nebel im Spülbehälter SPB, insbesondere auf Grund des Versprühens von Flüssigkeit mittels der Sprüharme SA, befinden. Ein derartiger Dampf bzw. Nebel kann sowohl Wasser als auch Reinigungsmittel oder Klarspüler sowie sonstige Reinigungstoffe fein verteilt enthalten. Für diese im Luftstrom LS1 mitgeführten fein dispergierten Flüssigkeitsteilchen bilden die Ablaufrippen AR, eine Abscheidungsvorrichtung. Anstelle von Ablaufrippen AR können alternativ in vorteilhafter Weise auch sonstige Abscheidungsmittel, insbesondere Gebilde mit einer Vielzahl von Kanten wie z.B. Drahtgeflechte, vorgesehen sein.The drainage ribs AR and the return rib RR serve in particular also to separate water droplets, detergent droplets, rinse aid droplets, and / or other aerosols which are located in the inflowing air LS1 and return them into the rinsing container SPB through the outlet opening ALA. This is particularly advantageous in a desorption process when a cleaning step takes place at the same time. During this cleaning step, a relatively large amount of steam or mist may be present in the washing container SPB, in particular due to the spraying of liquid by means of the spraying arms SA. Such a vapor or mist may contain finely divided water as well as detergent or rinse aid and other cleaning agents. For these finely dispersed liquid particles entrained in the air flow LS1, the drainage ribs AR, a deposition device, form. Alternatively, instead of drainage ribs AR, other deposition means, in particular structures with a plurality of edges, such as e.g. Wire mesh, be provided.
Insbesondere sorgt der schräg nach oben oder im Wesentlichen vertikal ansteigende Rohrabschnitt AU dafür, dass Flüssigkeitströpfchen oder gar Sprühstrahlen, die von einer Sprüheinrichtung SA, wie zum Beispiel einem Sprüharm beim Reinigungsvorgang oder sonstigem Spülvorgang, ausgesprüht werden, weitgehend davon abgehalten werden, direkt über die angesaugte Luftströmung LS1 in das Sorptionsmaterial des Sorptionsbehälters zu gelangen. Ohne diesen Rückhalt bzw. diese Abscheidung von Flüssigkeitströpfchen, insbesondere Nebeltröpfchen bzw. Dampftröpfchen, könnte das Sorptionsmaterial ZEO für einen Sorptionsvorgang beim Trockenschritt unzulässig feucht und unbrauchbar gemacht werden. Insbesondere könnte es zu einer vorzeitigen Sättigung durch eingeschleuste Flüssigkeitströpfchen wie z.B. Nebeltröpfchen bzw. Dampftröpfchen kommen. Durch den einlassseitigen, aufsteigenden Ast AU des Durchführungskanals sowie den ein oder mehreren Abscheidungs- bzw. Abfangelementen im oberen Kniebereich bzw. Scheitelbereich des Krümmungsabschnitts KRA zwischen dem aufsteigenden Ast AU und dem abfallenden Ast AB des Durchführungskanals ist es zudem auch weitgehend vermieden, dass Reinigungsmitteltröpfchen, Klarspülertröpfchen, und/oder sonstige Aerosoltröpfchen über diese Barriere hinaus weiter nach unten zum Lüfter LT und von dort aus in den Sorptionsbehälter SB gelangen können. Selbstverständlich ist es auch möglich, anstelle der Kombination aus ansteigendem Rohrabschnitt AU und abfallendem Rohrabschnitt AB sowie anstelle der ein oder mehreren Abscheidungselemente eine anders ausgebildete Barriereeinrichtung mit derselben Funktion vorzusehen.In particular, the tube section AU ascending obliquely upwards or substantially vertically ensures that liquid droplets or even spray jets which are sprayed out by a spraying device SA, for example a spray arm during the cleaning process or other rinsing process, are largely prevented from passing directly over the suctioned Air flow LS1 to enter the sorbent of the sorption. Without this support or this separation of liquid droplets, in particular mist droplets or vapor droplets, the Sorption material ZEO for a sorption process during the drying step are made inadmissibly humid and unusable. In particular, it could lead to premature saturation by introduced liquid droplets such as mist droplets or vapor droplets. By the inlet side, ascending branch AU of the feedthrough channel and the one or more Abscheidungs- or interception elements in the upper knee area or crest region of the curvature KRA between the rising branch AU and the falling branch AB of the feedthrough channel, it is also largely avoided that detergent droplets, Rinse droplets, and / or other aerosol droplets beyond this barrier further down to the fan LT and can get from there into the sorption SB. Of course, it is also possible, instead of the combination of rising pipe section AU and sloping pipe section AB and instead of the one or more deposition elements to provide a differently designed barrier device with the same function.
Zusammenfassend betrachtet weist die Geschirrspülmaschine GS hier im Ausführungsbeispiel eine Trocknungseinrichtung zum Trocknen von Spülgut durch Sorption mittels reversibel dehydrierbarem Sorptionsmaterial ZEO auf, das in einem Sorptionsbehälter SE gelagert ist. Dieser ist über mindestens einen Luftführungskanal LK mit dem Spülbehälter SPB zur Erzeugung einer Luftströmung LS1 verbunden. Der Luftführungskanal weist entlang seinem einlassseitigen Rohrabschnitt RA1 eine im Wesentlichen flach rechteckförmige Querschnittsgeometrieform auf. Der Luftführungskanal geht in Strömungsrichtung betrachtet nach seinem einlassseitigen Rohrabschnitt RA1 in einen im Wesentlichen zylinderförmigen Rohrabschnitt VA über. Er ist vorzugsweise aus mindestens einem Kunststoffmaterial hergestellt. Er ist insbesondere zwischen einer Seitenwand SW und/oder Rückwand RW des Spülbehälters und einer äußeren Gehäusewand der Geschirrspülmaschine angeordnet. Der Luftführungskanal LK weist dabei mindestens einen nach oben ansteigenden Rohrabschnitt AU auf. Er erstreckt sich ausgehend von der Austrittsöffnung ALA des Spülbehälters SPB nach oben. Er weist ferner in Strömungsrichtung betrachtet nach dem ansteigenden Rohrabschnitt AU mindestens einen nach unten abfallenden Rohrabschnitt AB auf. Zwischen dem ansteigenden Rohrabschnitt AU und dem abfallenden Rohrabschnitt AB ist mindestens ein Krümmungsabschnitt KRA vorgesehen. Der Krümmungsabschnitt KRA hat insbesondere eine größere Querschnittsfläche als der ansteigende Rohrabschnitt AU und/oder der abfallende Rohrabschnitt AB. Im Inneren des Krümmungsabschnitts KRA sind ein oder mehrere Strömungsleitrippen AR zur Vergleichmäßigen der Luftströmung LS1 vorgesehen. Mindestens eine der Strömungsleitrippen AR erstreckt sich ggf. über den Krümmungsabschnitt KRA in den ansteigenden Rohrabschnitt AU und/oder abfallenden Rohrabschnitt AB hinaus. Die ein oder mehreren Strömungsleitrippen AR sind in Positionen oberhalb der Höhenposition des Auslasses ALA des Spülbehälters SPB vorgesehen. Die jeweilige Strömungsleitrippe AR erstreckt sich von der Spülbehältergehäuse- zugewandten Kanalwand zur gegenüberliegenden, Spülbehältergehäuse- abgewandten Kanalwand des Luftführungskanals LK, vorzugsweise im Wesentlichen durchgängig. Mindestens eine Rücklaufrippe RR ist im Inneren des abfallenden Rohrabschnitts AB an der Spülbehältergehäuse- zugewandten Kanalwand und/oder Spülbehältergehäuse- abgewandten Kanalwand des Luftführungskanals LK an einer Stelle vorgesehen ist, die höher als die Einlassöffnung EI des Luftführungskanals LK liegt. Die Rücklaufrippe RR ist über eine Querverbindungsleitung RF im Zwischenraum zwischen dem absteigenden Rohrabschnitt AU und dem abfallenden Rohrabschnitt AB zur Kondensatrückführung mit der Einlassöffnung EI des Luftführungskanals LK verbunden. Sie weist ein Gefälle zur Einlassöffnung EI hin auf. Die Rücklaufrippe erstreckt sich von der Spülbehältergehäusezugewandten Kanalwand zur gegenüberliegenden, Spülbehältergehäuse- abgewandten Kanalwand des Luftführungskanals LK vorzugsweise lediglich auf einer Teilquerschnittsbreite.In summary, in the exemplary embodiment, the dishwasher GS here has a drying device for drying items to be washed by sorption by means of reversibly dehydratable sorption material ZEO, which is stored in a sorption container SE. This is connected via at least one air duct LK to the washing container SPB for generating an air flow LS1. The air duct has along its inlet-side pipe section RA1 a substantially flat rectangular cross-sectional geometry shape. Viewed in the direction of flow, the air-guiding channel, according to its inlet-side pipe section RA1, merges into a substantially cylindrical pipe section VA. It is preferably made of at least one plastic material. It is in particular arranged between a side wall SW and / or rear wall RW of the washing container and an outer housing wall of the dishwasher. The air duct LK has at least one upwardly rising pipe section AU. It extends from the outlet opening ALA of the washing container SPB upwards. He further has, viewed in the flow direction after the rising pipe section AU at least one downwardly sloping pipe section AB. Between the rising pipe section AU and the sloping pipe section AB at least one curvature section KRA is provided. The curvature section KRA in particular has a larger cross-sectional area than the rising tube section AU and / or the sloping pipe section AB. In the interior of the curvature section KRA, one or more flow guide ribs AR are provided for equalizing the air flow LS1. If necessary, at least one of the flow guide ribs AR extends beyond the curved section KRA into the rising pipe section AU and / or sloping pipe section AB. The one or more flow guide ribs AR are provided at positions above the height position of the outlet ALA of the purge tank SPB. The respective flow guide rib AR extends from the Spülbehältergehäuse- facing channel wall to the opposite, Spülbehältergehäuse- remote channel wall of the air duct LK, preferably substantially continuously. At least one return rib RR is provided in the interior of the sloping pipe section AB on the Spülbehältergehäuse- facing channel wall and / or Spülbehältergehäuse- remote channel wall of the air duct LK at a point which is higher than the inlet opening EI of the air duct LK. The return rib RR is connected via a cross-connection line RF in the space between the descending pipe section AU and the sloping pipe section AB for condensate return to the inlet opening EI of the air duct LK. It has a slope towards the inlet opening EI out. The return rib extends from the Spülbehältergehäusebehgewand channel wall to the opposite, Spülbehältergehäuse- remote channel wall of the air duct LK preferably only on a partial cross-sectional width.
In der
Gemäß der
Verallgemeinert ausgedrückt weist das Gehäuse des Sorptionsbehälters SB eine derartige Geometrieform auf, dass umlaufend zu den übrigen Teilen bzw. Komponenten der Bodenbaugruppe BG ein ausreichender Spaltabstand als Hitzeschutz vorhanden ist. Beispielsweise weist der Sorptionsbehälter SB zu diesem Zweck an seiner der Rückwand RW der Bodenbaugruppe BG zugewandten Gehäusewand SW2 eine gewölbte Ausformung AF an, die mit der ihr zugewandten Geometrieform der Rückwand RW korrespondiert.Expressed in general terms, the housing of the sorption container SB has such a geometry that there is a sufficient gap distance as heat protection around the remaining parts or components of the base assembly BG. For example, the sorption container SB for this purpose on its the rear wall RW of the bottom assembly BG facing housing wall SW2 to a curved formation AF, which corresponds with its facing geometry of the rear wall RW.
Der Sorptionsbehälter SB ist an der Unterseite des Bodens BO, insbesondere im Bereich einer Durchgangsöffnung DG (siehe
Zusammenfassend betrachtet ist der Sorptionsbehälter SB also unterhalb des Bodens BO des Spülbehälters SPB weitgehend freihängend derart angeordnet, dass er gegenüber benachbarten Komponenten und Teilen der Bodenbaugruppe BG zum Hitzeschutz einen vorgegebenen Mindestspaltabstand LSP aufweist. Unterhalb des Sorptionsbehälters SB ist zusätzlich ein Transportsicherungselement TRS in einem vorgegebenen Freiraumabstand FRA feststehend am Boden der Bodenbaugruppe angebracht. Dieses Transportsicherungselement TRS dient dazu, den unterhalb des Bodens BO des Spülbehälters SPB freihängend angebrachten Sorptionsbehälters SB gegebenenfalls von unten her abzustützen, wenn dieser zum Beispiel beim Transport zusammen mit dem Boden BO aufgrund von Erschütterungen nach unten durchschwingt. Dieses Transportsicherungselement TRS kann insbesondere durch eine nach unten U-förmig gebogene Metallklammer gebildet sein, die am Boden der Bodenbaugruppe feststehend montiert ist. Der Sorptionsbehälter SB weist oben an seinem Deckelteil DEL die Ausströmöffnung AO auf. Rings um den Außenrand dieser Ausströmöffnung AO ist ein nach oben abstehender Sockel SO angebracht. In der etwa kreisrunden Öffnung dieses Sockels SO ist ein zylinderförmiges Sockelstutzenelement STE angebracht (siehe
Dadurch, dass der Sockel SO um eine Sockelhöhe LSP von der übrigen Oberfläche des Deckelteils DEL nach oben absteht, ist sichergestellt, dass ein Spaltfreiraum zwischen dem Deckelteil DEL und der Unterseite des Bodens BO vorhanden ist. Der Boden BO des Spülbehälters SPB läuft hier im Ausführungsbeispiel von
Entsprechend den
Das topfförmige Gehäuseteil GT weist mindestens eine Durchgangsöffnung DUF für mindestens ein elektrisches Kontaktelement AP1, AP2 auf (siehe
Die Rohrschlangenheizung RZ ist mit einem vorgegebenen Höhenfreiraum in Durchströmungsrichtung DSR betrachtet hinter dem Schlitzblech SK angeordnet. Dazu kann es mittels einer Vielzahl von Blechteilen BT, die stegartig ausgebildet sind, auf Höhenabstand über den Durchlässen SL gehalten werden. Diese Blechteile BT (siehe
Durch das Schlitzblech SK wird eine Strömungskonditionierung bzw. Strömungsbeeinflussung der von unten nach oben in Durchströmungsrichtung DSR aufsteigenden Strömung LS2 derart vorgenommen, dass die Rohrschlangenheizung im Wesentlichen an jeder Stelle ihres Längsverlaufs im Wesentlichen mit demselben Luftvolumenstrom umströmt wird. Durch die Kombination von Schlitzblech und darüber angeordneter Rohrschlangenheizung HZ wird weitgehend sichergestellt, dass die Luftströmung LS2 vor der Eintrittsfläche des unteren Siebelements US der Sorptionseinheit SE weitgehend gleichmäßig beim Desorptionsvorgang aufgeheizt werden kann. Dabei sorgt das Schlitzblech für eine weitgehend gleichmäßige örtliche Verteilung des aufgeheizten Luftvolumenstroms über die Eintrittsquerschnittsfläche STF der Sorptionseinheit SE betrachtet.Through the slotted sheet SK, flow conditioning or flow influencing of the flow LS2 ascending from bottom to top in the direction of flow DSR is performed such that the coil heater is substantially surrounded by substantially the same volume of air flow at each point of its longitudinal course. Through the combination of slotted plate and arranged above pipe coil heater HZ is largely ensured that the air flow LS2 in front of the entrance surface of the lower screen US Sorption unit SE can be heated largely uniformly during the desorption process. In this case, the slotted sheet ensures a largely uniform local distribution of the heated air volume flow over the inlet cross-sectional area STF of the sorption unit SE.
Zusätzlich oder unabhängig zum Schlitzblech SK kann es gegebenenfalls auch zweckmäßig sein, eine Heizungseinrichtung außerhalb des Sorptionsbehälters BE in dem Verbindungsabschnitt zwischen der Lüftereinheit LT und der Einlassöffnung des Sorptionsbehälters SB vorzusehen. Da die Durchschnittsquerschnittsfläche dieses rohrförmigen Verbindungsabschnitts VA kleiner als die Durchschnittsquerschnittsfläche des Sorptionsbehälters SB für eine Luftströmung ist, kann die Luftströmung LS1, bevor sie in den Sorptionsbehälter SB gelangt, bereits vorab weitgehend gleichmäßig für den Desorptionsvorgang aufgeheizt werden. Dann kann gegebenenfalls das Schlitzblech SK vollständig entfallen.In addition or independently of the slotted sheet SK, it may also be expedient to provide a heating device outside of the sorption container BE in the connection section between the fan unit LT and the inlet opening of the sorption container SB. Since the average cross-sectional area of this tubular connecting portion VA is smaller than the average cross-sectional area of the sorbing tank SB for an air flow, the air flow LS1 before it enters the sorption SB can be heated in advance largely uniformly for the desorption process. Then, if necessary, the slotted sheet SK completely eliminated.
Insbesondere wenn die Aufheizung der Luft mittels einer Heizungseinrichtung im Sorptionsbehälter SB erfolgt, kann es gegebenenfalls auch zweckmäßig sein, in Durchströmungsrichtung DSR des Sorptionsbehälters SB betrachtet sowohl vor als auch nach der Heizungseinrichtung HZ jeweils mindestens ein Strömungskonditionierungselement derart vorzusehen, dass die Volumenmenge an Sorptionsmaterial ZEO hinter der Eintrittsquerschnittsfläche SDF des unteren Siebelements US an jeder Stelle etwa mit dem selben Luftvolumenstrom durchströmbar ist. Dadurch wird insbesondere auch beim Sorptionsvorgang, während dem die Heizungsvorrichtung HZ deaktiviert ist, das heißt ausgeschaltet ist, weitgehend erreicht, dass sämtliches Sorptionsmaterial weitgehend vollständig bei der Entfeuchtung der durchströmenden Luft LS1 beteiligt ist. In analoger Weise wird beim Desorptionsvorgang, bei dem die durchströmende Luft LS2 durch die Heizungseinrichtung HZ aufgeheizt ist, aus sämtlichen Sorptionsmaterial im Zwischenraum zwischen den beiden Siebelementen US, OS gespeichertes Wasser wieder zum Austreten gebracht, so dass an allen Stellen innerhalb dieses Raumvolumens das Sorptionsmaterial ZEO im Wesentlichen vollständig getrocknet und damit regeneriert für einen nachfolgenden Trocknungsvorgang zur Verfügung gestellt werden kann.If, in particular, the heating of the air takes place by means of a heating device in the sorption container SB, it may also be expedient to provide at least one flow conditioning element in the throughflow direction DSR of the sorption container SB before and after the heating device HZ in such a way that the volume amount of sorption material ZEO is behind the inlet cross-sectional area SDF of the lower screen element US at each point about the same air flow rate can be flowed through. As a result, the sorption process, in particular, during which the heating device HZ is deactivated, ie switched off, is largely achieved in that all sorption material is largely completely involved in the dehumidification of the air flowing through LS1. In an analogous manner, in the desorption process in which the air flowing through LS2 is heated by the heating device HZ, water stored from all sorption material in the intermediate space between the two sieve elements US, OS is released again, so that the sorption material ZEO is at all points within this volume essentially completely dried and thus regenerated for a subsequent drying process can be provided.
Die Durchströmungsquerschnittsfläche SDF der Sorptionseinheit SE im Inneren des Sorptionsbehälters SB ist hier im Ausführungsbeispiel größer als die Durchschnittsquerschnittsfläche des endseitigen Einlassstutzens ES des Luftführungskanals LK bzw. des rohrförmigen Verbindungsabschnitts VA ausgebildet. Die Durchströmungsquerschnittsfläche SDF des Sorptionsmaterials ist vorzugsweise zwischen den 2- und 40-fachen, insbesondere zwischen dem 4- und 30-fachen, bevorzugt zwischen dem 5- und 25-fachen, größer als die Durchschnittsquerschnittsfläche des Einlassstutzens ES des Luftführungskanals LK ausgebildet, mit der dieser in die Eintrittsöffnung EO des Sorptionsbehälters SB einmündet.The flow cross-sectional area SDF of the sorption unit SE in the interior of the sorption container SB is here larger in the embodiment than the average cross-sectional area of the end-side inlet nozzle ES of the air duct LK or of the tubular connection portion VA. The flow cross-sectional area SDF of the sorption material is preferably between 2 and 40 times, in particular between 4 and 30 times, preferably between 5 and 25 times, larger than the average cross-sectional area of the inlet nozzle ES of the air duct LK, with this opens into the inlet opening EO of the sorbent SB.
Zusammenfassend betrachtet füllt das Sorptionsmaterial ZEO zwischen dem unteren Siebelement US und dem oberen Siebelement OS ein Schüttvolumen derart aus, dass die Strömungseintrittsquerschnittsfläche SDF sowie eine Strömungsaustrittsquerschnittsfläche SAF im Wesentlichen senkrecht zur Durchströmungsrichtung DSR, die in vertikaler Richtung verläuft, aufweist. Das untere Siebelement US, das obere Siebelement OS sowie das dazwischen eingelagerte Sorptionsmaterial ZEO weisen jeweils zueinander kongruente Durchdringungsflächen für die durchströmende Luft LS2 auf. Dadurch ist weitgehend sichergestellt, dass an jeder Stelle im Volumen der Sorptionseinheit SE deren Sorptionsmaterial etwa mit demselben Volumenstrom beaufschlagt werden kann. Dadurch sind bei der Desorption Überhitzungsstellen und damit etwaige Schädigungen des Sorptionsmaterials ZEO weitgehend vermieden. Bei der Sorption wird eine gleichmäßige Feuchtigkeitsaufnahme aus der zu trocknenden Luft und damit eine optimale Ausnutzung des in der Sorptionseinheit SE zur Verfügung gestellten Sorptionsmaterial ZEO ermöglicht.In summary, the sorbent material ZEO fills a bulk volume between the lower sieve element US and the upper sieve element OS such that the flow inlet cross-sectional area SDF and a flow exit cross-sectional area SAF are substantially perpendicular to the flow direction DSR which extends in the vertical direction. The lower sieve element US, the upper sieve element OS and the sorption material ZEO interposed therebetween each have mutually congruent penetration surfaces for the air LS2 flowing through. This largely ensures that at any point in the volume of sorption unit SE whose sorption material can be acted upon by about the same volume flow. As a result, during the desorption overheating points and thus any damage to the sorbent ZEO are largely avoided. During sorption, a uniform absorption of moisture from the air to be dried and thus optimum utilization of the sorption material ZEO provided in the sorption unit SE are made possible.
Verallgemeinernd zusammengefasst kann also zweckmäßig sein, ein oder mehrere Strömungskonditionierungselemente SK im Sorptionsbehälter SB und/oder in einem eingangsseitigen Rohrabschnitt VA, ES des Luftführungskanals LK, insbesondere nach mindestens einer in den Luftführungskanal LK eingefügten Lüftereinheit LT, derart mit ein oder mehreren Luftdurchlässen SL vorzusehen, dass eine Vergleichmäßigung des örtlichen Strömungsquerschnittsprofils der Luftströmung LS2 beim Durchströmen des Sorptionsbehälters SB in dessen von unten nach oben gerichteten Durchströmungsrichtung DSR bewirkt ist. In Durchströmungsrichtung DSR des Sorptionsbehälters SB betrachtet ist in dessen unterem Hohlraum UH mindestens ein Strömungskonditionierungselement SK mit Höhenabstand vor der Heizungseinrichtung HZ vorgesehen. Als Strömungskonditionierungselement SK ist hier im Ausführungsbeispiel ein Schlitzblech oder Lochblech vorgesehen. Die Schlitze SL im Schlitzblech SK folgen im Wesentlichen dem Windungsverlauf einer Rohrschlangenheizung HZ nach, die mit Freiraumabstand oberhalb der Schlitze SL im Schlitzblech als Heizungseinrichtung positioniert ist. Das Schlitzblech ist im Wesentlichen parallel sowie mit einem Freiraumabstand zur Lufteintrittsquerschnittsfläche SDF der Sorptioneinheit SE des Sorptionsbehälters SE angeordnet. Luftdurchlässe, insbesondere Schlitze SL, im Strömungskonditionierungselement SK sind an denjenigen Orten, an denen die in den Sorptionsbehälter SB eintretende Luftströmung LS1 in Durchströmungsrichtung DSR des Sorptionsbehälters SB eine geringere Geschwindigkeit aufweist, größer als an denjenigen Orten ausgebildet, an denen die in den Sorptionsbehälter SB eintretende Luftströmung LS1 in Durchströmungsrichtung DSR des Sorptionsbehälters SB eine größere Geschwindigkeit aufweist.To summarize in general terms, it can thus be expedient to provide one or more flow conditioning elements SK in the sorption tank SB and / or in an input pipe section VA, ES of the air duct LK, in particular after at least one fan unit LT inserted into the air duct LK, with one or more air passages SL, that a homogenization of the local flow cross-sectional profile of the air flow LS2 is effected when flowing through the sorption container SB in its bottom-upward flow direction DSR. Viewed in the throughflow direction DSR of the sorption container SB, at least one of its lower cavity UH is at least one Flow conditioning SK provided with height distance in front of the heater HZ. As Strömungskonditionierungselement SK a slotted sheet or perforated plate is provided here in the embodiment. The slots SL in the slotted sheet SK essentially follow the winding course of a coil heater HZ, which is positioned with free space above the slits SL in the slotted sheet as a heating device. The slotted plate is arranged substantially parallel to and at a free space distance from the air inlet cross-sectional area SDF of the sorption unit SE of the sorption container SE. Air passages, in particular slits SL, in the flow conditioning element SK are formed at those locations at which the airflow LS1 entering the sorption container SB in the flow direction DSR of the sorbent container SB has a lower velocity than at those locations at which the sorbent container SB enters Air flow LS1 in the flow direction DSR of the sorbent SB has a greater speed.
Zusammengefasst weist das Sortionstrocknungssystem TS im Bereich des Sorptionsbehälters SB folgende spezifische Strömungsverhältnisse auf. Der Luftführungskanal LK ist mit dem Sorptionsbehälter SB derart gekoppelt, dass die eintretende Luftströmung LS1 in den Sorptionsbehälter SB mit einer Einströmungsrichtung ESR einmündet und in eine davon verschiedene Durchströmungsrichtung DSR übergeht, mit der sie das Innere des Sorptionsbehälters SB durchströmt. Die Austrittsströmungsrichtung der aus dem Sorptionsbehälter SB austretenden Luftströmung LS2 entspricht im Wesentlichen der Durchströmungsrichtung DSR. Der einlassseitige Rohrabschnitt RA1 des Luftführungskanals LK mündet in den Sorptionsbehälter SB derart ein, dass seine Einströmungsrichtung ESR in die Durchströmungsrichtung DSR des Sorptionsbehälters SB, insbesondere zwischen 45° und 135°, bevorzugt um etwa 90°, umgelenkt ist. In Strömungsrichtung betrachtet ist vor dem Sorptionsbehälter SB ist mindestens die Lüftereinheit LT in den einlassseitigen Rohrabschnitt RA1 des Luftführungskanals LK zur Erzeugung einer Zwangsluftströmung LS1 in Richtung auf mindestens eine Eintrittsöffnung EO des Sorptionsbehälters SB eingefügt. Die Lüftereinheit LT ist in der Bodenbaugruppe BG unterhalb des Spülbehälters SPB angeordnet. Die Durchströmungsquerschnittsfläche SDF für das Sorptionsmaterial ZEO im Inneren des Sorptionsbehälters SB ist größer als die Durchtrittsquerschnittsfläche des Einlassstutzens ES des Luftführungskanals LK ausgebildet, mit der dieser in die Eintrittsöffnung EO des Sorptionsbehälters SB einmündet. Die Durchströmungsquerschnittsfläche SDF des Sorptionsbehälters SB ist vorzugsweise zwischen dem 2- und 40- fachen, insbesondere zwischen dem 4- und 30- fachen, bevorzugt zwischen dem 5- und 25- fachen, größer als die Durchtrittsquerschnittsfläche des endseitigen Einlassstutzens ES des Luftführungskanals LK ausgebildet, mit der dieser in die Eintrittsöffnung EO des Sorptionsbehälters SB einmündet. Im Sorptionsbehälter ist mindestens eine Sorptionseinheit SE mit Sorptionsmaterial ZEO derart untergebracht, dass das Sorptionmaterial ZEO im Wesentlichen in oder entgegen zur Schwerkraftrichtung mit Luft LS1 durchströmbar ist, die über den Luftführungskanal LK aus dem Spülbehälter SPB in den Sorptionsbehälter SB geführt ist. Die Sorptionseinheit SE des Sorptionsbehälters SB weist mindestens ein unteres Siebelement oder Gitterelement US und mindestens ein oberes Siebelement oder Gitterelement OS in einem vorgebbaren Höhenabstand H voneinander auf, wobei das Raumvolumen zwischen den beiden Siebelementen oder Gitterelementen US, OS mit dem Sorptionsmaterial ZEO weitgehend vollständig ausgefüllt ist. Die Eintrittsquerschnittsfläche SDF und die Austrittsquerschnittsfläche SAF der Sorptionseinheit SE des Sorptionsbehälters SB sind insbesondere im Wesentlichen gleich groß gewählt. Die Eintrittsquerschnittsfläche SDF und die Austrittsquerschnittsfläche SAF der Sorptionseinheit SE des Sorptionsbehälters SB sind ferner zweckmäßigerweise im Wesentlichen kongruent zueinander angeordnet. Der Sorptionsbehälter weist in seine Durchströmungsrichtung DSR betrachtet mindestens eine Schichtung aus einem unteren Hohlraum UH und einer darüber angeordneten, in Durchströmungsrichtung DSR nachgeordneten Sorptionseinheit SE auf. Er weist in seinem unteren Hohlraum UH mindestens eine Heizungseinrichtung HZ auf. Der Sorptionsbehälter SE weist über seiner Sorptionseinheit SE mindestens einen oberen Hohlraum OH zum Sammeln ausströmender Luft LS2 auf. Das Sorptionsmaterial ZEO füllt in der Sorptionseinheit SE des Sorptionsbehälters SB ein Schüttvolumen derart aus, das eine zur Durchströmungsrichtung DSR im Wesentlichen senkrecht angeordnete Strömungseintrittsquerschnittsfläche SDF und eine dazu weitgehend parallel angeordnete Strömungsaustrittsquerschnittsfläche SAF gebildet ist. Der Sorptionsbehälter hat in seinem oberen Deckenteil DEL mindestens eine Ausströmöffnung AO, die über eine Durchgangsöffnung DG im Boden BO des Spülbehälters SPB mit dessen Innerem mit Hilfe mindestens eines Ausströmbauteils AKT verbunden ist.In summary, the sorting drying system TS has the following specific flow conditions in the region of the sorption container SB. The air duct LK is coupled to the sorbent vessel SB such that the incoming air flow LS1 enters the sorbent vessel SB with an inflow direction ESR and merges into a different flow direction DSR with which it flows through the interior of the sorbent vessel SB. The outlet flow direction of the air flow LS2 emerging from the sorption container SB essentially corresponds to the throughflow direction DSR. The inlet-side pipe section RA1 of the air duct LK opens into the sorption SB so that its inflow ESR in the flow direction DSR of the sorbent SB, in particular between 45 ° and 135 °, preferably by about 90 °, is deflected. In the flow direction, in front of the sorption container SB, at least the fan unit LT is inserted into the inlet-side tube section RA1 of the air-guiding channel LK for generating a forced air flow LS1 in the direction of at least one inlet opening EO of the sorbent container SB. The fan unit LT is arranged in the floor assembly BG below the washing container SPB. The flow cross-sectional area SDF for the sorption material ZEO inside the sorption container SB is formed larger than the passage cross-sectional area of the inlet nozzle ES of the air duct LK, with which this in the Inlet EO of the sorbent SB opens. The flow cross-sectional area SDF of the sorption container SB is preferably between 2 and 40 times, in particular between 4 and 30 times, preferably between 5 and 25 times, larger than the passage cross-sectional area of the end-side inlet nozzle ES of the air guide channel LK. with which this opens into the inlet opening EO of the sorbent SB. At least one sorption unit SE with sorption material ZEO is accommodated in the sorption container such that the sorption material ZEO can be flowed through air LS1 essentially in or counter to the direction of gravity, which is led out of the rinsing container SPB into the sorption container SB via the air guidance channel LK. The sorption unit SE of the sorption container SB has at least one lower sieve element or grating element US and at least one upper sieve element or grating element OS at a predefinable height distance H from one another, wherein the volume of space between the two sieve elements or grating elements US, OS is largely completely filled with the sorption material ZEO , The inlet cross-sectional area SDF and the outlet cross-sectional area SAF of the sorption unit SE of the sorption container SB are in particular selected to be substantially the same size. The inlet cross-sectional area SDF and the outlet cross-sectional area SAF of the sorption unit SE of the sorption container SB are expediently also arranged substantially congruent to one another. The sorption container has, viewed in its throughflow direction DSR, at least one stratification of a lower cavity UH and a sorption unit SE arranged above it and arranged downstream in the flow direction DSR. He has in his lower cavity UH at least one heater HZ. The sorption container SE has, via its sorption unit SE, at least one upper hollow space OH for collecting outflowing air LS2. In the sorption unit SE of the sorption container SB, the sorption material ZEO fills a bulk volume in such a way that a flow inlet cross-sectional area SDF arranged essentially perpendicular to the throughflow direction DSR and a flow exit cross-sectional area SAF arranged largely parallel thereto are formed. The sorption container has in its upper cover part DEL at least one outflow opening AO, which is connected via a passage opening DG in the bottom BO of the washing container SPB with its interior by means of at least one Ausströmbauteils AKT.
Das Sorptionsmaterial ZEO ist im Sorptionsbehälter SB in vorteilhafter Weise derart in Form der Sorptionseinheit SE gelagert, dass im Wesentlichen jede Eintrittstelle der Durchtrittsquerschnittsfläche SDF der Sorptionseinheit SE mit einem im Wesentlichen gleichen Luftvolumenstromwert beaufschlagbar ist. Als Sorptionsmaterial ZEO ist vorzugsweise ein Aluminium- und/oder Siliziumoxid enthaltendes, reversibel dehydrierbares Material, Silicagel, und/oder Zeolith, insbesondere Zeolith vom Typ A, X, Y allein oder in beliebiger Kombination, vorgesehen. Das Sorptionsmaterial ist im Sorptionsbehälter SB zweckmäßiger Weise in Form eines körnigen Feststoffes oder Granulats mit einer Vielzahl von Partikelkörpern mit einer Kömungsgröße im Wesentlichen zwischen 1 und 6 mm, insbesondere zwischen 2,4 und 4,8 mm, als Schüttung vorgesehen, wobei die Schütthöhe H der Partikelkörper mindestens dem 5-fachen deren Körnungsgröße entspricht. Das als körniger Feststoff oder Granulat vorliegende Sorptionsmaterial ZEO liegt in Schwerkraftrichtung im Sorptionsbehälter zweckmäßigerweise mit einer Schütthöhe vor, die im Wesentlichen dem 5 - bis 40 - fachen, insbesondere dem 10 - bis 15 - fachen, der Partikelgröße des körnigen Feststoffs oder Granulats entspricht. Die Schütthöhe H des Sorptionsmaterials ZEO ist vorzugsweise im Wesentlichen zwischen 1,5 und 25 cm, insbesondere zwischen 2 und 8 cm, bevorzugt zwischen 4 und 6 cm, gewählt. Der körnige Feststoff oder das Granulat kann vorzugsweise aus einer Vielzahl von im Wesentlichen kugelförmigen Partikelkörpern gebildet sein. Das als körniger Feststoff oder Granulat ausgebildete Sorptionsmaterial ZEO weist in vorteilhafter Weise zweckmäßigerweise eine mittlere Schüttdichte von mindestens 500 kg/m3, insbesondere im Wesentlichen zwischen 500 und 800 kg/m3 , insbesondere zwischen 600 und 700 kg/m3, insbesondere zwischen 630 bis 650 kg/m3, insbesondere bevorzugt von etwa 640 kg/m3, auf.The sorption material ZEO is stored in the sorption container SB in an advantageous manner in the form of the sorption unit SE, such that essentially every entry point of the passage cross-sectional area SDF of the sorption unit SE can be acted upon by a substantially identical air volume flow value. The sorbent material ZEO is preferably an aluminum and / or silicon oxide-containing, reversibly dehydratable material, silica gel, and / or zeolite, in particular zeolite of type A, X, Y, alone or in any desired combination. The sorption material is expediently provided in the sorption container SB in the form of a granular solid or granules having a multiplicity of particle bodies with a particle size substantially between 1 and 6 mm, in particular between 2.4 and 4.8 mm, the bed height H the particle body at least 5 times their grain size corresponds. The sorption material ZEO present as a granular solid or granulate expediently exists in the direction of gravity in the sorption container with a bulk height which corresponds essentially to 5 to 40 times, in particular 10 to 15 times, the particle size of the granular solid or granules. The bed height H of the sorbent material ZEO is preferably selected substantially between 1.5 and 25 cm, in particular between 2 and 8 cm, preferably between 4 and 6 cm. The granular solid or granules may preferably be formed from a plurality of substantially spherical particle bodies. Advantageously, the sorption material ZEO, which is in the form of a granular solid or granulate, advantageously has an average bulk density of at least 500 kg / m 3 , in particular substantially between 500 and 800 kg / m 3 , in particular between 600 and 700 kg / m 3 , in particular between 630 to 650 kg / m 3 , particularly preferably from about 640 kg / m 3 , on.
Im Sorptionsbehälter SB ist das reversibel dehydrierbare Sorptionsmaterial ZEO zur Absorption einer in der Luftströmung LS2 transportierten Feuchtigkeitsmenge zweckmäßigerweise mit einer derartigen Gewichtsmenge vorgesehen ist, dass die durch das Sorptionsmaterial ZEO absorbierte Feuchtigkeitsmenge geringer als eine auf das Spülgut aufgebrachte Flüssigkeitsmenge, insbesondere eine im Klarspülschritt aufgebrachte Flüssigkeitsmenge, ist.In the sorption container SB, the reversibly dehydratable sorbent material ZEO for absorbing a moisture amount transported in the air flow LS2 is expediently provided with such a weight amount that the amount of moisture absorbed by the sorption material ZEO is less than an amount of liquid applied to the items to be washed, in particular an amount of liquid applied in the final rinse step. is.
Insbesondere kann es zweckmäßig sein, wenn im Sorptionsbehälter SB das reversibel dehydrierbare Sorptionsmaterial mit einer derartigen Gewichtsmenge vorgesehen ist, dass diese ausreicht, eine Feuchtigkeitsmenge zu absorbieren, die im Wesentlichen einer Benetzungsmenge entspricht, mit der das Spülgut nach dem Ende eines Klarspülschritts benetzt ist. Die absorbierte Wassermenge entspricht vorzugsweise zwischen 4 und 25 %, insbesondere zwischen 5 und 15 %, der auf das Spülgut aufgebrachten Flüssigkeitsmenge.In particular, it may be expedient if the reversibly dehydratable sorption material with such a weight amount is provided in the sorption container SB, that this is sufficient to absorb a moisture amount, which corresponds substantially to a wetting amount, with which the items to be washed is wetted after the end of a rinse step. The amount of absorbed water preferably corresponds to between 4 and 25%, in particular between 5 and 15%, of the amount of liquid applied to the items to be washed.
Zweckmäßigerweise ist im Sorptionsbehälter SB eine Gewichtsmenge im Wesentlichen zwischen 0,2 und 5 kg, insbesondere zwischen 0,3 und 3 kg, bevorzugt zwischen 0,5 und 2,5 kg, an Sorptionsmaterial ZEO untergebracht.Appropriately, in the sorbent SB a weight amount substantially between 0.2 and 5 kg, in particular between 0.3 and 3 kg, preferably between 0.5 and 2.5 kg, housed in sorbent ZEO.
Das Sorptionsmaterial ZEO weist insbesondere Poren vorzugsweise mit einer Größe im Wesentlichen zwischen 1 und 12 Angström, insbesondere zwischen 2 und 10, bevorzugt zwischen 3 und 8 Angström, auf.The sorption material ZEO in particular has pores preferably with a size substantially between 1 and 12 angstroms, in particular between 2 and 10, preferably between 3 and 8 angstroms.
Es hat zweckmäßigerweise eine Wasseraufnahmekapazität im Wesentlichen zwischen 15 und 40, bevorzugt zwischen 20 und 30 Gewichtsprozent seines Trockengewichts.It has expediently a water absorption capacity substantially between 15 and 40, preferably between 20 and 30 weight percent of its dry weight.
Insbesondere ist ein Sorptionsmaterial vorgesehen ist, das bei einer Temperatur im Wesentlichen im Bereich zwischen 80° und 450°C, insbesondere zwischen 220° und 250°C, desorbierbar ist.In particular, a sorption material is provided which is desorbable at a temperature substantially in the range between 80 ° and 450 ° C, in particular between 220 ° and 250 ° C.
Der Luftführungskanal, der Sorptionsbehälter, und/oder ein oder mehrere zusätzliche Strömungsbeeinflussungselemente sind zweckmäßigerweise derart ausgebildet, dass durch das Sorptionsmaterial zu dessen Sorption und/oder Desorption eine Luftströmung mit einem Volumenstrom im Wesentlichen zwischen 2 und 15 l/sec, insbesondere zwischen 4 und 7 l/sec bewirkbar ist.The air duct, the sorption, and / or one or more additional flow influencing elements are suitably designed such that by the sorbent material for its sorption and / or desorption an air flow with a flow rate substantially between 2 and 15 l / sec, in particular between 4 and 7 l / sec is effected.
Zweckmäßig kann es insbesondere sein, wenn dem Sorptionsmaterial ZEO mindestens eine Heizungseinrichtung HZ zugeordnet ist, mit der eine äquivalente Heizleistung zwischen 250 bis 2500 W, insbesondere zwischen 1000 und 1800 W, bevorzugt zwischen 1200 und 1500 W, zum Aufheizen des Sorptionsmaterials für dessen Desorption bereitstellbar ist.It can be expedient, in particular, if the sorption material ZEO is assigned at least one heating device HZ with which an equivalent heating power between 250 and 2500 W, in particular between 1000 and 1800 W, preferably between 1200 and 1500 W, can be provided for heating the sorption material for its desorption is.
Vorzugsweise ist das Verhältnis von Heizleistung mindestens einer Heizungseinrichtung, die dem Sorptionsmaterial zu dessen Desorption zugeordnet ist, und Luftvolumenstrom der Luftströmung, die das Sorptionsmaterial durchströmt, zwischen 100 und 1250 W sec/l, insbesondere zwischen 100 und 450 W sec/l, bevorzugt zwischen 200 und 230 W sec/l, gewählt.Preferably, the ratio of heating power of at least one heating device, which is assigned to the sorption material for its desorption, and air volume flow of the air flow flowing through the sorbent material, between 100 and 1250 W sec / l, in particular between 100 and 450 W sec / l, preferably between 200 and 230 W sec / l, selected.
Im Sorptionsbehälter ist für das Sorptionsmaterial vorzugsweise eine Durchtrittsquerschnittsfläche im Wesentlichen zwischen 80 und 800 cm2, insbesondere zwischen 150 und 500 cm2, vorgesehent.In the sorption container, a passage cross-sectional area of between 80 and 800 cm 2 , in particular between 150 and 500 cm 2 , is preferably provided for the sorption material.
Zweckmäßigerweise ist die Schütthöhe H des Sorptionsmaterials ZEO über die Eintrittsquerschnittsfläche SDF des Sorptionsbehälters SB im Wesentlichen konstant.Expediently, the bed height H of the sorption material ZEO is essentially constant over the inlet cross-sectional area SDF of the sorbent container SB.
Insbesondere ist es zweckmäßig, im Sorptionsbehälter SB das Sorptionsmaterial zur Absorption einer Wassermenge im Wesentlichen zwischen 150 und 400 ml, insbesondere zwischen 200 und 300 ml, auszubilden.In particular, it is expedient to form the sorption material for absorbing an amount of water essentially between 150 and 400 ml, in particular between 200 and 300 ml, in the sorption container SB.
Weiterhin ist für mindestens eine Komponente des Sorptionstrocknungssystems TS mindestens eine thermische Überhitzungschutzeinrichtung TSI (siehe
Die elektrische Temperaturschutzeinheit ist im Ausführungsbeispiel der
Weiterhin kann es zweckmäßig sein, mindestens eine Steuereinrichtung HE, ZE vorzusehen (siehe
Als thermische Überhitzungschutzeinrichtung kann ferner auch die weitgehend frei hängende Aufhängung des Sorptionsbehälters, insbesondere unterhalb des Bodens BO des Spülbehälters SPB, dienen.As a thermal overheating protection device, the largely freely suspended suspension of the sorption container, in particular below the bottom BO of the washing container SPB, can also be used.
Die thermische Überhitzungschutzeinrichtung kann weiterhin eine Lagerung des Sorptionsbehälters SB derart umfassen, dass der Sorptionsbehälter SB gegenüber benachbarten Komponenten und/oder Teilen einer Bodenbaugruppe BG einen vorgegebenen Mindestspaltabstand LSP aufweist.The thermal overheating protection device may further comprise a mounting of the sorption container SB such that the sorption container SB has a predetermined minimum gap distance LSP with respect to adjacent components and / or parts of a base assembly BG.
Als thermische Überhitzungschutzeinrichtung kann zusätzlich oder unabhängig zu oben angegebenen Maßnahmen zumindest im Bereich der Sorptionseinheit SE des Sorptionsbehälters SB mindestens ein Außengehäuse AG zusätzlich zum Innengehäuse IG des Sorptionsbehälters SB vorgesehen sein. Zwischen dem Innengehäuse IG und dem Außengehäuse AG ist dabei ein Luftspaltfreiraum LS als Wärmeisolationsschicht vorhanden.As a thermal overheating protection device, at least one outer housing AG may be provided in addition to the inner housing IG of the sorption container SB, in addition to or independently of the above measures, at least in the region of the sorption unit SE of the sorption container SB. Between the inner housing IG and the outer housing AG while an air gap clearance LS is present as a thermal insulation layer.
Die Rohrschlangenheizung HZ der
Entsprechend den
Um zu vermeiden, dass Flüssigkeit beim Sprühen mit dem unteren Sprüharm SA durch die Austrittsöffnung des Ausströmstutzen AKT in den Sorptionsbehälter SB gelangt, ist eine untere Randzone UR der halbkreiszylinder-abschnittsartigen Seitenwand der Spritzschutzhaube SH nach innen in Richtung auf den Ausströmstutzen AKT zu gekrümmt bzw. gewölbt. Dies ist gut aus
Das Ausströmelement AUS, das ausgangsseitig am Sorptionsbehälter SB angebracht ist, und in den Innenraum des Spülbehälters SPB ragt, ist also zweckmäßigerweise derart ausgebildet, dass die aus ihm austretende Luftströmung LS2 vom Sprüharm SA weggerichtet ist. Insbesondere wird die ausströmende Luftströmung LS2 in einen hinteren bzw. rückwärtigen Eckbereich zwischen der Rückwand RW und der angrenzenden Seitenwand SW des Spülbehälters gelenkt. Auf diese Weise wird weitgehend vermieden, dass Spritzwasser oder Schaum beim Reinigungsvorgang oder einem sonstigen Spülvorgang durch die Öffnung des Ausströmstutzens in das Innere des Sorptionsbehälters gelangen kann. Dadurch könnte der Desorptionsvorgang beeinträchtigt oder ganz zunichte gemacht werden. Darüber hinaus könnte durch Spülflüssigkeit Sorptionsmaterial dauerhaft geschädigt werden. Denn umfangreiche Tests gezeigt, dass die Funktionstüchtigkeit des Sorptionsmaterials im Sorptionsbehälter über die Lebensdauer der Geschirrspülmaschine weitgehend erhalten bzw. bewahrt werden kann, wenn zuverlässig verhindert ist, dass kein Wasser, Reinigungsmittel, oder Klarspüler im Spülwasser in das Sorptionsmaterial gelangen kann.The outflow element AUS, which is mounted on the output side of the sorption container SB and projects into the interior of the rinse container SPB, is thus expediently designed such that the air flow LS2 emerging from it is directed away from the spray arm SA. In particular, the outflowing airflow LS2 is directed into a rearward corner area between the rear wall RW and the adjacent side wall SW of the washing compartment. In this way it is largely avoided that spray water or foam during cleaning or other flushing through the opening of the Ausströmstutzens can get into the interior of the sorption. This could impair or even nullify the desorption process. In addition, sorbent material could be permanently damaged by flushing liquid. Extensive tests have shown that the functionality of the sorption material in the sorption container can largely be preserved or preserved over the life of the dishwasher, if it is reliably prevented that no water, cleaning agent or rinse aid in the rinse water can enter the sorption material.
Zusammenfassend betrachtet ist mindestens eine Ausströmvorrichtung AUS, die mit mindestens einer Ausströmöffnung AO des Sorptionsbehälters SB verbunden ist, derart im Inneren des Spülbehälters SPB angeordnet, das von ihr ausgeblasene Luft LS2 von mindestens einer im Spülbehälter SPB untergebrachten Sprüheinrichtung SA weitgehend weggerichtet ist. Die Ausströmvorrichtung AUS ist dabei außerhalb des Arbeitsbereichs der Sprüheinrichtung SA angeordnet. Die Sprüheinrichtung kann z.B. ein rotierender Sprüharm SA sein. Die Ausströmvorrichtung AUS ist vorzugsweise in einem hinteren Eckbereich EBR zwischen der Rückwand RW und einer angrenzenden Seitenwand SW des Spülbehälters SPB vorgesehen. Die Ausströmvorrichtung AUS weist insbesondere eine Ausblasöffnung ABO mit einem Höhenabstand HO über dem Boden BO des Spülbehälters SPB auf, der höher als der Pegel einer für einen Spülvorgang vorgesehenen Soll- Spülbadgesamtmenge liegt. Die Ausströmvorrichtung AUS umfasst einen Ausströmstutzen AKT und eine Spritzschutzhaube SH. Die Spritzschutzhaube SH weist eine die Ausblasöffnung ABO des Ausströmstutzens AKT überstülpende Geometrieform aufweist. Die Spritzschutzhaube SH ist über den Ausströmstutzen AKT derart übergestülpt, dass durch den Ausströmstutzen AKT aus dem Sorptionsbehälter SB mit einer aufsteigenden Strömungsrichtung hochströmende Luft nach ihrem Austritt aus der Ausblasöffnung ABO des Ausströmstutzens AKT eine abwärtsweisenden Zwangsströmungweg ALS aufprägbar ist. Der oberhalb des Bodens BO des Spülbehälters SPB nach oben abstehende Ausströmstutzen AKT ist mit dem Anschlussstutzen STE am Deckelteil DEL des unter dem Boden BO angeordneten Sorptionsbehälters SB gekoppelt. Die Spritzschutzhaube SH ist in ihrem der Sprüheinrichtung SA zugewandten Gehäusebereich GF oberseitig sowie unterseitig geschlossen ausgebildet. Die Spritzschutzhaube SH überdeckt die Ausblasöffnung ABO des Ausströmstutzens AKT mit einem oberen Freiraum. Der Ausströmstutzen AKT weist dabei einen oberen, nach außen gewölbten Rand bzw. ringsumlaufenden Kragen KR. Die Spritzschutzhaube SH umhüllt einen oberen Endabschnitt des Ausströmstutzens AKT derart, dass zwischen ihrer Innenwandung und der Außenwandung des Ausströmstutzens AKT ein Spaltfreiraum SPF gebildet ist. Der Spaltfreiraum SPF zwischen der Spritzschutzhaube SH und dem Ausströmstutzen AKT ist derart ausgebildet, dass ein Luftausströmweg ALS aus dem Ausströmstutzen AKT bereitgestellt ist, der von der Sprüheinrichtung SA im Spülbehälter SB weggerichtet ist. Am Ausströmstutzen AKT ist ein in den Spaltfreiraum SPF hineinragendes Spritzwasserabweiselement PB vorgesehen. Eine untere Randzone UR der Spritzschutzhaube SH ist nach innen gewölbt. Die Spritzschutzhaube SH weist eine derartig abgerundete Außenoberfläche auf, dass sie einen auftreffenden Sprühstrahl der Sprüheinrichtung SA sich filmartig über ihre Oberfläche ergießen lässt.In summary, at least one outflow device AUS, which is connected to at least one outflow opening AO of the sorbent container SB, arranged in the interior of the washing container SPB, the air blown out of her LS2 of at least one housed in the washing container SPB sprayer SA is largely directed away. The outflow device AUS is arranged outside the working range of the spray device SA. The spraying device may, for example, be a rotating spray arm SA. The outflow device AUS is preferably provided in a rear corner region EBR between the rear wall RW and an adjacent side wall SW of the washing container SPB. In particular, the outflow device AUS has a blow-out opening ABO with a height clearance HO above the bottom BO of the rinse container SPB, which is higher than the level of a set rinse bath total amount provided for a rinse operation. The outflow device AUS comprises a discharge connection AKT and a splash protection cover SH. The splash guard SH has a geometry which has the blow-out opening ABO of the outflow nozzle AKT. The splash guard SH is slipped over the outflow AKT so that a downwardly flowing forced flow path ALS can be impressed by the outflow port AKT from the sorbent SB with an ascending flow direction high after air emerging from the exhaust port ABO of the outflow. The above the bottom BO of the washing container SPB upwardly projecting outflow AKT is coupled to the connection piece STE on the cover part DEL of the arranged under the bottom BO sorption SB. The splash guard SH is designed to be closed on its upper side and underside in its housing area GF facing the spraying device SA. The splash guard SH covers the blow-off opening ABO of the outlet connection AKT with an upper free space. The outflow branch AKT has an upper, outwardly curved edge or circumferential collar KR. The splash guard SH envelopes an upper end portion of the outflow AKT such that between its inner wall and the outer wall of the outflow AKT a clearance SPF is formed. The gap SPF between the splash guard SH and the outflow AKT is formed such that an Luftausströmweg ALS is provided from the outflow AKT, which is directed away from the spray SA in the washing container SB. At the outflow AKT a projecting into the gap SPF SPITZ Spritzwasserabweiselement is provided. A lower edge zone UR of the splash guard SH is curved inwards. The splash guard SH has such a rounded outer surface, that it can pour an incident spray of the spray SA to film over its surface.
Gegebenenfalls kann es auch zweckmäßig sein, in/ oder vor der Eingangsöffnung MD des einlassseitigen Rohrabschnitts ET des Luftführungskanals LK mindestens einen rippenförmigen Eingriffsschutz vorzusehen, der zwischen seinen Eingriffsrippen RIP frei durchgängige Spalten zum Einströmen von Luft aus dem Spülbehälter aufweist. In der
An die Hauptsteuereinrichtung HE ist über eine Signalleitung auch mindestens ein Temperatursensor TSE (siehe
Sobald nun ein Reinigungsvorgang gestartet wird, schaltet gleichzeitig die Hauptsteuereinrichtung HE über die Busleitung BUL die Zusatzsteuereinrichtung ZE derart an, dass eine elektrische Spannung über die Stromverbindungsleitung SZL an die Polstifte AP1, AP2 der Heizungseinrichtung HZ angelegt ist. Sobald im Innenraum des Spülbehälters SPB eine bestimmte vorgegebene Temperaturobergrenze erreicht ist, was die Hauptsteuereinrichtung HE über die Messsignale des Temperatursensors feststellen kann, kann sie der Zusatzsteuereinrichtung ZE über die Busleitung BUL die Anweisung geben, die Spannung an der Stromzufuhrleitung SZL wegzunehmen und dadurch die Heizungseinrichtung HZ komplett auszuschalten. Damit kann z.B. der Desorptionsvorgang für das Sorptionsmaterial im Sorptionsbehälter beendet werden.As soon as a cleaning process is started, the main control device HE simultaneously activates the additional control device ZE via the bus line BUL in such a way that an electrical voltage is applied to the pole pins AP1, AP2 of the heating device HZ via the current connection line SZL. As soon as a certain predetermined upper temperature limit is reached in the interior of the washing container SPB, which the main control unit HE can determine via the measuring signals of the temperature sensor, it can instruct the additional control unit ZE via the bus line BUL to remove the voltage at the power supply line SZL and thereby the heating device HZ completely switch off. Thus, e.g. the desorption process for the sorbent material in the sorption tank to be terminated.
Gegebenenfalls kann es zweckmäßig sein, für eine Bedienperson der Geschirrspülmaschine die Option vorzusehen, über die Aktivierung bzw. Deaktivierung einer eigens vorgesehenen Programmtaste oder entsprechender Auswahl eines Programmmenüs das Sorptionstrockensystem TS zu aktivieren oder zu deaktivieren. In
Insbesondere kann im Bedienfeld der Geschirrspülmaschine eine erste Auswahltaste zur Auswahl einer Programmvariante "Energie" oder "Sorptionsbetrieb" vorgesehen sein. Bei diesem Programm liegt der Schwerpunkt auf Einsparung von Energie. Dies wird dadurch erreicht, dass beim Klarspülvorgang überhaupt nicht mittels eines Durchlauferhitzers geheizt wird und die Trocknung des Spülguts, insbesondere des Geschirrs, allein mit Hilfe des Sorptionstrocknungssystems TS bewirkt wird.In particular, a first selection key for selecting a program variant "energy" or "sorption operation" can be provided in the control panel of the dishwasher. This program focuses on saving energy. This is achieved in that the rinse process is not heated at all by means of a continuous flow heater and the drying of the items to be washed, in particular of the dishes, is effected solely by means of the sorption drying system TS.
Zweckmäßig kann es insbesondere sein, zusätzlich zur reinen Sorptionstrocknung den Innenraum des Spülbehälters durch aufgeheizte Klarspülflüssigkeit beim Klarspülvorgang aufzuheizen. Dabei kann es in vorteilhafter Weise ausreichend sei, wenn der durch den Klarspülvorgang bewirkte Wärmeübertrag auf das zu trocknende Spülgut mit einem geringeren Energieeinsatz als im Fall ohne Sorptionstrocknung erfolgt. Denn durch das nun verwendete Sorptionstrocknungssystem lässt sich durch Sorption von Luftfeuchtigkeit lässt sich elektrische Heizenergie einsparen. Es kann also sowohl durch sogenannte "Eigenwärmetrocknung" als auch durch Sorptiontrocknung, d.h. durch eine Kombination bzw. Ergänzung von beiden Trocknungsarten, eine verbesserte Trocknung von nassem oder feuchtem Spülgut erreicht werden.It may be expedient in particular to heat the interior of the rinsing container by heated rinsing liquid during rinsing in addition to the pure sorption drying. It may be advantageous in an advantageous manner, if effected by the rinsing heat transfer to the items to be dried with a lower energy input than in the case without Sorptionstrocknung. Because the sorption drying system that is now being used can be used to save electrical heating energy by sorption of air humidity. Thus, it can be achieved both by so-called "self-heat drying" and by sorption drying, i. By combining or supplementing both types of drying, an improved drying of wet or moist ware can be achieved.
Zusätzlich oder unabhängig von der Taste "Energie" kann eine weitere Taste "Trocknungsleistung" im Bedienfeld der Geschirrspülmaschine vorgesehen sein, die die Gebläselaufzeit der Lüftereinheit erhöht. Hierdurch kann eine verbesserte Trocknung aller Geschirrteile erreicht werden.In addition to or independent of the "Energy" button, another button "Drying capacity" may be provided in the control panel of the dishwasher, which increases the fan run time of the fan unit. As a result, an improved drying of all crockery parts can be achieved.
Zusätzlich oder unabhängig von den obigen speziellen Tasten kann eine weitere Taste "Programmlaufzeit" vorgesehen sein. Wenn das Sorptionstrocknungssystem zugeschaltet wird, kann die Programmlaufzeit gegenüber herkömmlichen Trocknungssystemen (ohne Sorptionstrocknung) erniedrigt werden. Ggf. kann durch zusätzliches Aufheizen in der Reinigungsphase und optional durch Erhöhung des Sprühdrucks durch Erhöhung der Motordrehzahl der Umwälzpumpe die Laufzeit beim Reinigen weiter verkürzt werden. Des Weiteren kann auch durch eine Erhöhung der Klarspültemperatur die Trocknungszeit weiter verkürzt werden.In addition to or independent of the above special keys, another "program runtime" key may be provided. If the sorption drying system is switched on, the program runtime can be reduced compared to conventional drying systems (without sorption drying). Possibly. By further heating in the cleaning phase and optionally by increasing the spraying pressure by increasing the motor speed of the circulation pump, the running time during cleaning can be further shortened. Furthermore, by increasing the rinse temperature, the drying time can be further reduced.
Zusätzlich oder unabhängig von den vorherigen spezifischen Tasten kann eine Betätigungstaste mit der Funktion "Beeinflussung der Reinigungsleistung" vorgesehen sein. Bei Betätigung dieser Taste kann bei gleichbleibender Laufzeit die Reinigungsleistung erhöht werden, ohne dass sich der Energieverbrauch gegenüber einer Geschirrspülmaschine ohne Sorptionstrocknungssystem erhöht. Denn dadurch, dass beim Reinigungsvorgang zugleich der Sorptionsvorgang gestartet wird und dadurch heiße Luft, die mit einer aus dem Sorptionsmaterial ausgetretenen Wassermenge beladen ist, in den Spülbehälter gelangt, kann Heizenergie zum Aufheizen einer gewünschten Spülbad-Gesamtflüssigkeitsmenge eingespart werden.In addition to or independent of the previous specific keys, an operating button with the function "influencing the cleaning performance" may be provided. When this key is pressed, the cleaning performance can be increased while the running time remains constant, without the energy consumption being increased compared to a dishwasher without a sorption drying system. Because by the fact that at the same time the sorption process is started during the cleaning process and thereby hot air, which is loaded with a leaked from the sorbent amount of water, enters the washing, heating energy can be saved for heating a desired Spülbad total amount of liquid.
Claims (20)
- Dishwasher machine (GS), in particular a household dishwasher machine, comprising at least one washing compartment (SPB) and at least one sorption drying system (TS) for drying items to be washed, wherein the sorption drying system (TS) comprises at least one sorption compartment (SB) comprising reversibly dehydratable sorption material (ZEO), said compartment being connected to the washing compartment (SPB) by means of at least one air-guiding channel (LK) for the generation of an air flow (LS1), wherein
the sorption compartment (SB) comprises a pot-type housing part (GT) which is closed by a cover part (DEL), characterised in that ,
a circumferential outer edge of the cover part (DEL) is connected to an upper edge of the pot-type housing part (GT) only by a mechanical connection, in particular by a deforming connection, a joining connection, a latching connection, a clamping connection, in particular by a beaded connection or a clinched connection. - Dishwasher machine according to claim 1, characterised in that at least one sorption unit (SE) comprising reversibly dehydratable sorption material (ZEO) is provided in the pot-type housing part (GT).
- Dishwasher machine according to claim 2, characterised in that
the sorption unit (SE) is accommodated in the pot-type housing part (GT) in such a way that air (LS1) which is guided out of the washing compartment (SPB) into the sorption compartment (SB) by means of the air-guiding channel can flow through its sorption material (ZEO) substantially in or against the direction of gravity. - Dishwasher machine according to any one of claims 2 or 3, characterised in that
the sorption unit (SE) comprises at least one lower sieve element or grid element (US) and at least one upper sieve element or grid element (OS) at a predefined vertical distance (H) from one another, and in that the spatial volume between the two sieve elements or grid elements (US, OS) is filled largely completely with the sorption material (ZEO). - Dishwasher machine according to at least one of the preceding claims, characterised in that
at least one heating device (HZ) is provided in the pot-type cover part (GT). - Dishwasher machine according to at least one of the preceding claims,
characterised in that ,
viewed in the through-flow direction (DSR) of the sorption compartment (SB) in the pot-type cover part (GT), at least one heating device (HZ) is provided upstream of at least one sorption unit (SE) comprising reversibly dehydratable sorption material (ZEO). - Dishwasher machine according to any one of claims 5 or 6, characterised in that
the heating device (HZ) is provided in a lower cavity (UH) of the pot-type housing part (GT) for collecting inflowing air (LS1) from the air-guiding channel (LK). - Dishwasher machine according to at least one of the preceding claims, characterised in that
at least one intake opening (EO) for the air-guiding channel (LK) is provided in the pot-type housing part (GT). - Dishwasher machine according to at least one of the preceding claims, characterised in that
at least one discharge opening (AO) for at least one outlet element (AUS) is provided in the cover part (DEL). - Dishwasher machine according to at least one of the preceding claims, characterised in that
a heat-resistant material, in particular metal sheet, preferably stainless steel or a stainless steel alloy, is used for the cover part (DEL) and the pot-type cover part (GT).. - Dishwasher machine according to at least one of the preceding claims, characterised in that
the cover part (DEL) seals the pot-type housing part (GT) to a large extent hermetically. - Dishwasher machine according to at least one of the preceding claims, characterised in that
the pot-type housing part (GT) comprises one or more side walls (SW1, SW2) which run substantially vertically. - Dishwasher machine according to at least one of the preceding claims, characterised in that the pot-type housing part (GT) has an external contour which corresponds substantially to the internal contour of an installation area (EBR) provided for it, in particular in a base module (BG).
- Dishwasher machine according to at least one of the preceding claims, characterised in that
the pot-type housing part (GT) comprises at least two adjacent side walls (SW1, SW2) the external surfaces of which run substantially at right angles to one another. - Dishwasher machine according to at least one of the preceding claims, characterized in that the sorption compartment (SB) is arranged in a base module (BG) underneath the washing compartment (SPB).
- Dishwasher machine according to at least one of the preceding claims, characterised in that
at least one side wall (SW2) of the housing part (GT) exhibits at least one shape (AF) which is substantially complementary to a shape on the back wall and/or side wall of a base module (BG) which is provided under the base (BO) of the washing compartment (SPB). - Dishwasher machine according to at least one of the preceding claims, characterised in that
the sorption compartment (SB) is provided in a rear corner area (EBR) between the back wall (RW) and an adjacent side wall (SW) of the dishwasher machine (GS), in particular the base module (BG) thereof. - Dishwasher machine according to at least one of the preceding claims, characterised in that
the pot-type housing part (GT) comprises at least one through-opening (DUF) for at least one electrical contact element (AP1, AP2). - Dishwasher machine according to claim 18, characterised in that
a drip protection sheet (TSB) is mounted in a roofed area above the through-opening (DUF), at least over the extent thereof. - Dishwasher machine according to claim 19, characterised in that
the drip protection sheet (TSB) has a drainage incline.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL09781148T PL2323537T3 (en) | 2008-07-28 | 2009-07-28 | Dishwasher machine comprising a sorption drying device |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008040789A DE102008040789A1 (en) | 2008-07-28 | 2008-07-28 | Dishwasher with sorption drying device |
DE200810039897 DE102008039897A1 (en) | 2008-08-27 | 2008-08-27 | Dishwasher i.e. household dishwasher, for washing tableware, has sorption compartment comprising pot-type housing part closed by cover part, where sorption compartment is connected to washing compartment by air guiding channel |
PCT/EP2009/059694 WO2010012699A2 (en) | 2008-07-28 | 2009-07-28 | Dishwasher machine comprising a sorption drying device |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2323537A2 EP2323537A2 (en) | 2011-05-25 |
EP2323537B1 true EP2323537B1 (en) | 2014-12-03 |
Family
ID=41237980
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09781148.3A Active EP2323537B1 (en) | 2008-07-28 | 2009-07-28 | Dishwasher machine comprising a sorption drying device |
Country Status (10)
Country | Link |
---|---|
US (1) | US8709171B2 (en) |
EP (1) | EP2323537B1 (en) |
JP (1) | JP2011528970A (en) |
CN (1) | CN102112033B (en) |
AU (1) | AU2009275997B2 (en) |
ES (1) | ES2526437T3 (en) |
NZ (1) | NZ590109A (en) |
PL (1) | PL2323537T3 (en) |
RU (1) | RU2531268C2 (en) |
WO (1) | WO2010012699A2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4454536A1 (en) * | 2023-04-17 | 2024-10-30 | LG Electronics Inc. | Dishwasher having a moisture-absorbing and drying device |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU2009275987B2 (en) * | 2008-07-28 | 2014-06-12 | Bsh Hausgerate Gmbh | Dishwasher machine comprising a sorption drying device |
EP2323531B1 (en) * | 2008-07-28 | 2014-11-26 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher comprising a sorption drying system |
DE102012212636B4 (en) * | 2012-07-18 | 2015-04-02 | Premark Feg L.L.C. | Commercial dishwasher with drying system and method for operating such a dishwasher |
US9854957B2 (en) * | 2016-01-20 | 2018-01-02 | Haier Us Appliance Solutions, Inc. | Methods for operating dishwasher appliances having energy recovery features |
CN110974114B (en) * | 2019-12-10 | 2020-11-24 | 珠海格力电器股份有限公司 | Dish washing machine for removing residual water of tableware |
Family Cites Families (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE816989C (en) | 1949-02-25 | 1951-10-15 | Arno Andreas | Process for cleaning laundry, dishes, etc. a. |
US3378933A (en) | 1966-01-13 | 1968-04-23 | Gen Electric | Drying system for dishwasher |
US3862786A (en) | 1973-08-13 | 1975-01-28 | Gen Electric | Washer installation |
DE8026939U1 (en) | 1980-10-08 | 1982-02-04 | Bosch-Siemens Hausgeräte GmbH, 7000 Stuttgart | DISHWASHER |
DE3614345C1 (en) * | 1986-04-28 | 1987-09-24 | Bosch Siemens Hausgeraete | Dishwasher |
DE3830664A1 (en) | 1988-09-09 | 1990-03-22 | Bauknecht Hausgeraete | DEVICE FOR DRYING DISHES IN A HOUSEHOLD DISHWASHER |
DE4441264A1 (en) * | 1994-11-19 | 1996-05-23 | Behr Gmbh & Co | Air dehumidifier for vehicle passenger compartment |
DE29618572U1 (en) * | 1996-10-24 | 1998-02-26 | Schwarzbich, Jörg, 33615 Bielefeld | Home appliance |
DE19718047A1 (en) | 1997-04-29 | 1998-11-05 | Behr Gmbh & Co | Device to reduce humidity in cabin of electric car |
US5966959A (en) * | 1998-03-09 | 1999-10-19 | American Standard Inc. | Condensate drain pan arrangement with positive slope |
IT247109Y1 (en) | 1999-11-02 | 2002-05-02 | Candy Spa | STEAM CONDENSING CHAMBER FOR DISHWASHER MACHINES |
DE10353774A1 (en) | 2003-07-30 | 2005-02-24 | BSH Bosch und Siemens Hausgeräte GmbH | Drying items in domestic dish washing machines has a reversible hydroscopic material filled column through which recirculated air is driven by a fan |
US8293024B2 (en) | 2003-07-30 | 2012-10-23 | Bsh Bosch Und Siemens Hausgeraete Gmbh | Dishwasher |
DE10353775A1 (en) | 2003-07-30 | 2005-02-24 | BSH Bosch und Siemens Hausgeräte GmbH | Drying items in domestic process machines has reversible hydroscopic material filled column through which recirculated air is driven by fan |
DE10356787A1 (en) | 2003-12-04 | 2005-07-07 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
DE102005004093A1 (en) * | 2004-12-09 | 2006-06-22 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
DE102005004096A1 (en) * | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with a Sorptionstrockenvorrichtung |
CN201052131Y (en) * | 2004-12-09 | 2008-04-30 | Bsh博施及西门子家用器具有限公司 | Dishwasher |
CN200954096Y (en) * | 2004-12-09 | 2007-10-03 | Bsh博施及西门子家用器具有限公司 | Tableware washing machine |
DE102005004091A1 (en) * | 2004-12-09 | 2006-06-22 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with ozone storage |
DE102005004095A1 (en) | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
CN200951070Y (en) | 2004-12-09 | 2007-09-26 | Bsh博施及西门子家用器具有限公司 | Dish-washing machine |
DE102005004094A1 (en) | 2004-12-09 | 2006-06-22 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
DE102005004006B4 (en) | 2005-01-27 | 2007-02-01 | Carl Zeiss Ag | Holding device and transport device for handling lenses and methods for refining lenses |
RU55407U1 (en) * | 2005-06-07 | 2006-08-10 | Общество с ограниченной ответственностью "НАЙС" | WINDOW BLOCK |
TR200601887A1 (en) * | 2006-04-19 | 2009-02-23 | Bsh Ev Aletleri̇ Sanayi̇ Ve Ti̇caret Anoni̇m Şi̇rketi̇@ | A household appliance |
DE102006018252B4 (en) * | 2006-04-20 | 2009-02-05 | Cs Clean Systems Ag | sorption |
DE102007017284B3 (en) | 2007-04-12 | 2008-11-13 | BSH Bosch und Siemens Hausgeräte GmbH | Temperature detection with zeolite drying |
FR2924592B1 (en) * | 2007-12-10 | 2012-07-13 | Fagorbrandt Sas | WASHING AND DRYING MACHINE COMPRISING A CONDENSING DEVICE AND METHOD THEREOF |
AU2009275987B2 (en) | 2008-07-28 | 2014-06-12 | Bsh Hausgerate Gmbh | Dishwasher machine comprising a sorption drying device |
DE202008011159U1 (en) | 2008-08-21 | 2008-11-06 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher and Sorptionstrockenvorrichtung whose sorption material is adjusted by weight to the wetting amount in the washing compartment |
DE102008039885A1 (en) | 2008-08-27 | 2010-04-08 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with Sorptionstrockenvorrichtung |
-
2009
- 2009-07-28 WO PCT/EP2009/059694 patent/WO2010012699A2/en active Application Filing
- 2009-07-28 EP EP09781148.3A patent/EP2323537B1/en active Active
- 2009-07-28 AU AU2009275997A patent/AU2009275997B2/en not_active Ceased
- 2009-07-28 PL PL09781148T patent/PL2323537T3/en unknown
- 2009-07-28 CN CN200980129836.9A patent/CN102112033B/en active Active
- 2009-07-28 NZ NZ590109A patent/NZ590109A/en not_active IP Right Cessation
- 2009-07-28 RU RU2011104424/12A patent/RU2531268C2/en active
- 2009-07-28 JP JP2011520457A patent/JP2011528970A/en active Pending
- 2009-07-28 ES ES09781148.3T patent/ES2526437T3/en active Active
- 2009-07-28 US US13/054,084 patent/US8709171B2/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4454536A1 (en) * | 2023-04-17 | 2024-10-30 | LG Electronics Inc. | Dishwasher having a moisture-absorbing and drying device |
Also Published As
Publication number | Publication date |
---|---|
AU2009275997B2 (en) | 2014-09-18 |
US8709171B2 (en) | 2014-04-29 |
EP2323537A2 (en) | 2011-05-25 |
WO2010012699A2 (en) | 2010-02-04 |
AU2009275997A1 (en) | 2010-02-04 |
WO2010012699A3 (en) | 2010-07-01 |
CN102112033A (en) | 2011-06-29 |
NZ590109A (en) | 2012-12-21 |
ES2526437T3 (en) | 2015-01-12 |
JP2011528970A (en) | 2011-12-01 |
RU2011104424A (en) | 2012-09-10 |
RU2531268C2 (en) | 2014-10-20 |
US20110114136A1 (en) | 2011-05-19 |
PL2323537T3 (en) | 2015-05-29 |
CN102112033B (en) | 2014-04-02 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2328460B1 (en) | Dishwasher having a sorption drying device | |
EP2317904B1 (en) | Dishwasher comprising a sorption drying device | |
WO2010012689A1 (en) | Dishwasher machine comprising a sorption drying device | |
EP2326235B1 (en) | Dishwasher with sorption drying device | |
EP2328452B1 (en) | Dishwasher comprising a sorption drying machine | |
WO2010012703A2 (en) | Dishwasher machine comprising a sorption drying system | |
WO2010023087A2 (en) | Dishwasher comprising a sorption drying device | |
DE102008039888B4 (en) | Dishwasher with Sorptionstrockenvorrichtung | |
EP2323537B1 (en) | Dishwasher machine comprising a sorption drying device | |
EP2312988B1 (en) | Dishwasher machine comprising a sorption drying device | |
EP2317906B1 (en) | Dishwasher comprising a sorption drying unit | |
EP2328458B1 (en) | Dishwasher comprising a sorption drying device | |
WO2010023084A2 (en) | Dishwasher comprising a sorption drying device | |
DE102008039900A1 (en) | Dishwasher i.e. domestic dishwasher, has control device comprising washing program to control proper operation of dishwasher, and pushbuttons connected to control device for modifying washing program | |
DE102008039892A1 (en) | Dishwasher i.e. household dishwasher, for cleaning tableware, has sorption material provided in sorption unit such that identical air volume flow rate is subjected in each inlet point of cross-sectional passage surface of sorption unit | |
WO2010023085A1 (en) | Dishwasher comprising a sorption drying unit | |
DE102008039893A1 (en) | Dishwasher machine i.e. household dishwasher machine, has air guiding channel coupled to sorption compartment such that flow enters sorption compartment passes into throughflow direction along which flow flows via inner side of compartment | |
DE102008039897A1 (en) | Dishwasher i.e. household dishwasher, for washing tableware, has sorption compartment comprising pot-type housing part closed by cover part, where sorption compartment is connected to washing compartment by air guiding channel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20110228 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA RS |
|
DAX | Request for extension of the european patent (deleted) | ||
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
INTG | Intention to grant announced |
Effective date: 20140721 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 698857 Country of ref document: AT Kind code of ref document: T Effective date: 20141215 Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: LANGUAGE OF EP DOCUMENT: GERMAN |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2526437 Country of ref document: ES Kind code of ref document: T3 Effective date: 20150112 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 502009010310 Country of ref document: DE Effective date: 20150115 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PFA Owner name: BSH HAUSGERAETE GMBH, DE Free format text: FORMER OWNER: BSH BOSCH UND SIEMENS HAUSGERAETE GMBH, DE |
|
RAP2 | Party data changed (patent owner data changed or rights of a patent transferred) |
Owner name: BSH HAUSGERAETE GMBH |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: VDEP Effective date: 20141203 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20150303 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R081 Ref document number: 502009010310 Country of ref document: DE Owner name: BSH HAUSGERAETE GMBH, DE Free format text: FORMER OWNER: BSH BOSCH UND SIEMENS HAUSGERAETE GMBH, 81739 MUENCHEN, DE Effective date: 20150409 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20150304 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
REG | Reference to a national code |
Ref country code: PL Ref legal event code: T3 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: PC2A Owner name: BSH HAUSGERATE GMBH Effective date: 20150529 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20150403 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20150403 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 502009010310 Country of ref document: DE |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
26N | No opposition filed |
Effective date: 20150904 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: CD Owner name: BSH HAUSGERATE GMBH, DE Effective date: 20151022 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20150728 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20150728 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150731 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150728 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150731 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 8 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150728 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 698857 Country of ref document: AT Kind code of ref document: T Effective date: 20150728 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150728 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20090728 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 9 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20150731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20141203 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 10 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20210730 Year of fee payment: 13 Ref country code: FR Payment date: 20210722 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20210819 Year of fee payment: 13 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220731 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220728 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20230901 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220729 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: TR Payment date: 20230725 Year of fee payment: 15 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240731 Year of fee payment: 16 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PL Payment date: 20240715 Year of fee payment: 16 |