EP1667569B1 - Dishwasher - Google Patents
Dishwasher Download PDFInfo
- Publication number
- EP1667569B1 EP1667569B1 EP04740668.1A EP04740668A EP1667569B1 EP 1667569 B1 EP1667569 B1 EP 1667569B1 EP 04740668 A EP04740668 A EP 04740668A EP 1667569 B1 EP1667569 B1 EP 1667569B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- sorption column
- air
- washing
- line
- washing container
- 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.)
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- 239000003570 air Substances 0.000 claims description 63
- 238000005406 washing Methods 0.000 claims description 59
- 238000001179 sorption measurement Methods 0.000 claims description 54
- 238000001035 drying Methods 0.000 claims description 38
- 238000010438 heat treatment Methods 0.000 claims description 32
- 239000000463 material Substances 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 18
- 238000003795 desorption Methods 0.000 claims description 13
- 238000004140 cleaning Methods 0.000 claims description 10
- 239000012080 ambient air Substances 0.000 claims description 8
- 238000005338 heat storage Methods 0.000 claims 1
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 239000007921 spray Substances 0.000 description 6
- 229910021536 Zeolite Inorganic materials 0.000 description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 5
- 239000010457 zeolite Substances 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 238000004851 dishwashing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000012487 rinsing solution Substances 0.000 description 1
- 239000000243 solution Substances 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
Definitions
- the invention relates to a dishwasher with a washing container and devices for washing dishes.
- a dishwasher has a washing method whose program sequence generally consists of at least one sub-program step “pre-wash”, a sub-program step “cleaning”, at least one sub-program step “intermediate washing”, a sub-program step “rinsing” and a sub-program step “drying”.
- the rinsing liquid is heated before or during a partial program step.
- the rinsing liquid is usually heated by means of electrical heaters.
- Different drying systems are known for drying items to be washed in a dishwasher.
- the items to be washed can be dried by self-heat drying if the washing liquid is heated in the “final rinse” sub-program step and thus the hot-rinsed items dries automatically due to the inherent heat generated by the items during the “drying” sub-program step.
- the rinsing liquid in the partial program step "final rinsing" e.g. in a heat exchanger, heated to a certain temperature and applied to the items to be washed via spray devices available in the dishwasher.
- the relatively high temperature of the washing liquid in the "final rinse" subprogram step of usually 65 ° C to 75 ° C ensures that a sufficiently large amount of heat is transferred to the items to be washed so that the water adhering to the items to be washed evaporates due to the heat stored in the items.
- a separate heat source for example a hot air blower, is used in the washing compartment to heat the moist air mixture during the drying process so that the air in the washing compartment can absorb a larger amount of moisture.
- Dishwashers are known in which the moist air is vented to the outside. This is disadvantageous because the surrounding kitchen furniture is damaged.
- a dishwasher of the type mentioned is known in which the air from the washing compartment is passed through a closable opening in the wall of the washing compartment onto reversibly dehydratable material and from there to the outside via an opening.
- the desorption of the reversibly dehydratable material takes place during the standstill phase of the device, whereby the water vapor that is produced in the process is directed to the outside again via the opening.
- this is disadvantageous because the surrounding kitchen furniture is damaged.
- a disadvantage of the heating systems described above according to the prior art described above is that the heating of the rinsing liquid is associated with a high energy requirement and the required thermal energy must be generated anew for each heating phase by means of the electrical heating elements.
- the known heating systems also have the disadvantage that the heating of the rinsing liquid in the sub-program step "rinsing" and the processes in the sub-program step “drying" themselves are associated with a high energy requirement and the required thermal energy is lost after the drying process.
- a rinsing liquor is heated by a water heater arranged outside its rinsing container and pressed into a distribution and spray system by a pump.
- a largely closed drying system is used for a drying process, in which air circulates from the washing compartment via a drying device which can be regenerated by heating and from this circulates back into the washing compartment.
- the drying device consists of a drying container which is in thermal contact with the heater and which is filled with a drying agent that adsorbs moisture, such as a zeolite.
- the air flow of the drying system is with provided a closure that interrupts the air circulation during the washing of the dishwasher.
- the US 6,434,857 B1 relates only to a washer-dryer whose tumbler is separated from the circuit of a drying system by a valve during a washing cycle.
- the object of the present invention is therefore to provide a dishwasher with which it is possible, from an economic point of view, to efficiently clean and dry the items to be washed in the washing compartment and to keep the associated energy consumption as low as possible.
- This object is achieved by the dishwasher according to the invention having the features according to claim 1.
- Advantageous further developments of the present invention are characterized in the subclaims.
- the dishwasher according to the invention with a washing container and devices for washing dishes using washing liquor has a sorption column that is connected to the washing container in an air-conducting manner and contains reversibly dehydratable material, the sorption column on the one hand for drying the dishes and on the other hand for desorption of the sorption column to heat the heat energy used in the Rinsing container located washing liquor and the dishes is at least partially usable.
- reversibly dehydratable material with hygroscopic properties, e.g. B. zeolite
- heating of the items to be treated is preferably not necessary in the part program step "rinsing".
- a heating of the items to be treated in the partial program step which precedes the partial program step “drying”, in particular the partial program step “final rinsing”, is possible, but not useful. Nevertheless, a slight warming during "rinsing", z. B. to 30 ° C, be appropriate. This means a substantial energy saving.
- the generally always occurring warming of the air due to the released heat of condensation in the sorption column in the part program step "drying" increases its moisture absorption capacity each time it is passed through the sorption column, which improves the drying result and shortens the drying time Drying time leads.
- An additional heating of the air with a heater in the partial program step "drying" and thus also of the dishes is normally not necessary because the sorption column due to the heat of condensation of the steam to high temperatures, z. B. 150 ° C, heated, and thereby the air sufficiently high temperatures, z. B. 60 ° -70 ° C reached.
- the reversibly dehydratable material is heated to very high temperatures for desorption, for which purpose thermal energy is necessary.
- the stored liquid emerges as hot water vapor.
- the water vapor is preferably passed into the treatment room of the device with an air stream and the air in the treatment room is thus heated and thereby the washing liquor and / or the dishes are also heated.
- the air that is passed through cools down, causing the water vapor to partially condense at the top. This is preferably done as a closed air circuit.
- the introduction of the hot water vapor and the heated air into the treatment room during a partial program step with the treatment liquid to be heated or, under certain circumstances, with the treatment liquid that has already been heated is largely sufficient to heat the treatment liquid sufficiently. This means that further heating can largely be dispensed with and the thermal energy used for desorption can be used almost entirely to heat the treatment liquid, rinsing solution and / or dishes, apart from the low energy required to overcome the binding forces between water and reversibly dehydratable material . In addition to saving energy, efficient cleaning of the items to be treated is also guaranteed.
- the present invention provides a dishwasher with which it is possible, from an economic point of view, to efficiently clean and dry the items to be washed and to keep the associated energy consumption as low as possible.
- the rinsing container has an outlet with a line to the sorption column, the line preferably having a shut-off valve and then, in the flow direction, preferably an inlet valve to the ambient air, and the rinsing container also has an inlet with a line from the sorption column, wherein in a fan is arranged in the line to the sorption column which at least temporarily introduces at least part of the air in the washing container or from the ambient air of the sorption column.
- a fan is arranged in the line to the sorption column which at least temporarily introduces at least part of the air in the washing container or from the ambient air of the sorption column.
- the fan can be easily controlled so that the use of the sorption column can be precisely controlled.
- the fan increases the effect of the sorption column, since the air to be passed through is conveyed more quickly.
- the sorption column has a container for the reversibly dehydratable material, which allows the exchange of moisture and / or heat between the reversibly dehydratable material and the air surrounding it.
- a heating element preferably an electrical heating element, is arranged for desorption of the reversibly dehydratable material.
- the heating element is arranged in the line to the sorption column for desorption of the reversibly dehydratable material (11).
- the air that can be introduced into the washing container via the inlet can be cooled so that the dishes are not damaged by high temperatures.
- a droplet separator is arranged at the outlet or the line at the outlet is led up a partial area so that no spray water reaches the sorption column via the line.
- the thermal energy used for desorption is prior to use for heating the washing liquor and / or the dishes in a heat store, e.g. B. latent storage, storable.
- a heat store e.g. B. latent storage, storable.
- the single FIGURE shows, in a schematic representation, a dishwasher 1 according to the invention with a washing container 2, in which crockery baskets 3, 4 are arranged for the arrangement of items to be washed (not shown).
- the dishwasher 1 has a sorption column 10 containing reversibly dehydratable material 11 connected to the washing container 2 in a liquid-conducting manner, the sorption column 10, as will be explained in more detail below, being used on the one hand for drying and on the other hand for heating air that is passed through.
- the rinsing container 2 has an outlet 5 with a line 6 to the sorption column 10, arranged in its upper region in the exemplary embodiment described, and an inlet 8 with a line 7 from the sorption column 10, arranged in its lower region in the exemplary embodiment described.
- a fan 9 is arranged which supplies the sorption column 10 with air from the washing container 2.
- an electrical heating element 12 in the embodiment shown is arranged in the sorption column 10 in the embodiment described. This arrangement of the heating element 12 in the sorption column 10 is not part of the invention.
- a dishwasher has a washing method whose program sequence generally consists of at least one sub-program step “pre-wash”, a sub-program step “cleaning”, at least one sub-program step “intermediate washing”, a sub-program step “rinsing” and a sub-program step “drying”.
- air is passed from the washing container 2, on the one hand, through the sorption column 10 and back into the washing container 2 during the “drying” part of the program.
- the fan 9 is switched on.
- the airway is indicated by the arrows A, B and C.
- the air introduced into the sorption column 10 by the fan 9 via the line 6 is withdrawn from the reversibly dehydratable material 11 of all moisture.
- the air is heated by the heat of condensation of moisture or water vapor released in the sorption column, which advantageously increases the air's moisture absorption capacity.
- the now warmed, z. B. up to 40 ° -70 ° C, and very dry air now passes through line 8 back into the rinsing container.
- the heated air introduced into the washing compartment 2 is completely dry and, due to the higher temperatures, has a high absorption capacity for moisture. It rises in the washing compartment 2 and absorbs the residual moisture on the items to be washed. As already described above, it is now fed back to the sorption column 10.
- air from the washing container 2 is passed through during a partial program step with washing liquid to be heated or possibly already heated, preferably during the partial program step "cleaning" and / or "pre-rinse", in the described embodiment during the partial program step "cleaning” the sorption column 10 and passed back into the washing tank 2.
- the fan 9 is switched on.
- the airway is indicated by arrows A, B and C indicated.
- the heater 12 is also switched on in order to carry out the desorption of the reversibly dehydratable material 11.
- reversibly dehydratable material 11 is heated to very high temperatures for desorption.
- the stored liquid emerges as hot water vapor.
- the fan 9 By directing air by means of the fan 9 through the lines 6, 8 in accordance with the air path of the arrows A, B, C, the water vapor is passed into the washing compartment 2 and the air in the washing compartment is also heated.
- the introduction of the hot steam and the heated air into the washing compartment 2 during the “cleaning” part of the program in the treatment room is largely sufficient to sufficiently heat the washing solution and / or the dishes. This means that further heating is largely unnecessary and the energy used for desorption can be used almost entirely to heat the washing liquor and / or the dishes, apart from the low energy required to overcome the binding forces between water and reversibly dehydratable material. In addition to saving energy, efficient cleaning of the items to be washed is also guaranteed.
- a shut-off valve is in the line 6 and then in the flow direction of the airway according to arrow A an inlet valve, for. B. arranged via another line to the ambient air.
- the shut-off valve is open and the inlet valve is closed, so that only air from the washing compartment 2 is sucked in by the fan 9.
- the rinsing container needs an outlet (not shown) in order to be able to release this air from the environment back into the environment.
- the outlet 5 is designed in such a way that, due to an increase in the average from the outlet 5 to the line 6, the flow velocity in the line 6 is lower than in the outlet 5, so that there are no water droplets in the air (mist) in the line 6 occur.
- the line 6 can be led upwards after the outlet 5 or a droplet separator (not shown) can be arranged at the outlet 5.
- the electrical heating element is not located in the sorption column 10, but in the line 6 between the fan 9 and the sorption column 10, in order to ensure uniform heating of the dehydratable material 11, e.g. B. zeolite to achieve. Excessive temperatures of the dehydratable material can thus advantageously be avoided in order to exclude damage to the dehydratable material 11 resulting therefrom.
- the sorption column is - as already described - preferably during a partial program step with the treatment liquid to be heated with a heater to a very high temperature, e.g. B. 300 ° C, so that the sorption column releases the absorbed water.
- a very high temperature e.g. B. 300 ° C
- the sorption column is heated to high temperatures, e.g. B. 150 ° -200 ° C, due to the heat of condensation of the water vapor or the moisture.
- This means that the dry air or the air with steam that is placed in the washing compartment can reach temperatures, e.g. B. 80 ° C, which can damage the dishes, z. B. plastic parts, can lead.
- the air inlet temperature in the washing area must therefore be reduced in a further embodiment with cooling to such an extent that no damage occurs.
- a variant of a dishwasher according to the invention has a flow heater for the washing liquor, if based on the present Invention is not performed on this. If, in a further embodiment of the invention, heating is necessary in the part program step “final rinsing”, this can be achieved either with the flow heater or with the air heater with the fan switched on.
- the advantage of heating with air heating is that the thermal energy stored in the sorption column can be used for drying in the subsequent partial program step "drying".
- the fan can be switched on during the heating phase of the “final rinse” part of the program, with the air heating switched off.
- moist air is passed through the sorption column, which absorbs the moisture, and the sorption column and thus also the air that is passed through is heated by the condensation energy released.
- the sorption column e.g. B. with zeolite, is in this embodiment with a corresponding large amount of z. B. to design zeolite that a good drying result can also be achieved in the part program step "drying".
- the present invention provides a dishwasher with which it is possible, from an economic point of view, to efficiently clean and dry the items to be washed in the washing compartment 2 and to keep the associated energy consumption as low as possible.
Description
Die Erfindung betrifft eine Geschirrspülmaschine mit einem Spülbehälter und Vorrichtungen zum Spülen von Geschirr.The invention relates to a dishwasher with a washing container and devices for washing dishes.
Eine Geschirrspülmaschine weist bekanntlich ein Spülverfahren auf, dessen Programmablauf im Allgemeinen aus wenigstens einem Teilprogrammschritt "Vorspülen", einem Teilprogrammschritt "Reinigen", wenigstens einem Teilprogrammschritt "Zwischenspülen", einem Teilprogrammschritt "Klarspülen" und einem Teilprogrammschritt "Trocknen" besteht. Zur Erhöhung des Reinigungseffekts wird dabei die Spülflüssigkeit vor oder während eines Teilprogrammschrittes erwärmt. Die Erwärmung der Spülflüssigkeit erfolgt üblicherweise mittels elektrischer Heizungen. Zur Trocknung von Spülgut in einer Geschirrspülmaschine sind unterschiedliche Trocknungssysteme bekannt.As is known, a dishwasher has a washing method whose program sequence generally consists of at least one sub-program step “pre-wash”, a sub-program step “cleaning”, at least one sub-program step “intermediate washing”, a sub-program step “rinsing” and a sub-program step “drying”. To increase the cleaning effect, the rinsing liquid is heated before or during a partial program step. The rinsing liquid is usually heated by means of electrical heaters. Different drying systems are known for drying items to be washed in a dishwasher.
Beispielsweise kann das Spülgut durch Eigenwärmetrocknung getrocknet werden, wenn die Spülflüssigkeit im Teilprogrammschritt "Klarspülen" erwärmt wird und somit das heiß klargespülte Spülgut durch die so aufgebaute Eigenwärme des Spülguts während des Teilprogrammschritts "Trocknen" von selbst trocknet. Um diese Eigenwärmetrocknung zu erreichen, wird die Spülflüssigkeit im Teilprogrammschritt "Klarspülen", z.B. in einem Wärmetauscher, auf eine bestimmte Temperatur erwärmt und über in der Geschirrspülmaschine vorhandene Sprüheinrichtungen auf das Spülgut aufgebracht. Durch die relativ hohe Temperatur der Spülflüssigkeit im Teilprogrammschritt "Klarspülen" von üblicherweise 65°C bis 75°C wird erreicht, dass eine hinreichend große Wärmemenge auf das Spülgut übertragen wird, so dass das am Spülgut anhaftende Wasser durch die im Spülgut gespeicherte Wärme verdampft.For example, the items to be washed can be dried by self-heat drying if the washing liquid is heated in the “final rinse” sub-program step and thus the hot-rinsed items dries automatically due to the inherent heat generated by the items during the “drying” sub-program step. In order to achieve this self-heating drying, the rinsing liquid in the partial program step "final rinsing", e.g. in a heat exchanger, heated to a certain temperature and applied to the items to be washed via spray devices available in the dishwasher. The relatively high temperature of the washing liquid in the "final rinse" subprogram step of usually 65 ° C to 75 ° C ensures that a sufficiently large amount of heat is transferred to the items to be washed so that the water adhering to the items to be washed evaporates due to the heat stored in the items.
Bei einer weiteren bekannten Trocknungseinrichtung wird eine separate Heizquelle, z.B. ein Heißluftgebläse, im Spülbehälter dazu verwendet, das feuchte Luftgemisch beim Trocknungsvorgang zu erwärmen, damit die Luft im Spülbehälter eine größere Menge an Feuchtigkeit aufnehmen kann.In another known drying device, a separate heat source, for example a hot air blower, is used in the washing compartment to heat the moist air mixture during the drying process so that the air in the washing compartment can absorb a larger amount of moisture.
Es sind Geschirrspülmaschinen bekannt, bei denen die Feuchtluft nach außen abgelassen wird. Dies ist nachteilig, da die umgebenden Küchenmöbel geschädigt werden.Dishwashers are known in which the moist air is vented to the outside. This is disadvantageous because the surrounding kitchen furniture is damaged.
Daher sind weitere Geschirrspülmaschinen bekannt, bei denen die Feuchtluft vor dem Ausleiten über Kondensationsflächen geleitet wird, an denen die Feuchtigkeit kondensiert. Dieses Kondenswasser wird entweder in den Spülbehälter oder in spezielle Auffangbehälter geleitet.Therefore, further dishwashers are known in which the moist air is passed over condensation surfaces on which the moisture condenses before being discharged. This condensed water is either directed into the rinsing container or into special collecting containers.
Aus der
Ein Nachteil bei den oben beschriebenen Heizungssystemen nach dem weiter oben beschriebenen Stand der Technik besteht darin, dass die Erwärmung der Spülflüssigkeit mit einem hohen Energiebedarf verbunden ist und die benötigte Wärmeenergie für jede Erwärmungsphase mittels der elektrischen Heizelemente neu erzeugt werden muss. Ebenso haben die bekannten Heizungssysteme den Nachteil, dass die Erwärmung der Spülflüssigkeit im Teilprogrammschritt "Klarspülen" sowie die Vorgänge im Teilprogrammschritt "Trocknen" selbst mit einem hohen Energiebedarf verbunden sind und die benötigte Wärmeenergie nach dem Trocknungsvorgang verloren geht.A disadvantage of the heating systems described above according to the prior art described above is that the heating of the rinsing liquid is associated with a high energy requirement and the required thermal energy must be generated anew for each heating phase by means of the electrical heating elements. The known heating systems also have the disadvantage that the heating of the rinsing liquid in the sub-program step "rinsing" and the processes in the sub-program step "drying" themselves are associated with a high energy requirement and the required thermal energy is lost after the drying process.
Bei der Geschirrspülmaschine der
Die
Diese Aufgabe wird durch die erfindungsgemäße Geschirrspülmaschine mit den Merkmalen gemäß Anspruch 1 gelöst. Vorteilhafte Weiterbildungen der vorliegenden Erfindung sind in den Unteransprüchen gekennzeichnet.In the dishwasher of the
The
This object is achieved by the dishwasher according to the invention having the features according to claim 1. Advantageous further developments of the present invention are characterized in the subclaims.
Die erfindungsgemäße Geschirrspülmaschine mit einem Spülbehälter und Vorrichtungen zum Spülen von Geschirr mittels Spülflotte, weist eine mit dem Spülbehälter luftleitend verbundene, reversibel dehydrierbares Material enthaltende Sorptionskolonne auf, wobei die Sorptionskolonne einerseits zur Trocknung des Geschirrs und andererseits zur Desorption der Sorptionkolonne eingesetzte Wärmeenergie zur Erwärmung der im Spülbehälter befindlichen Spülflotte und des Geschirrs wenigstens teilweise verwendbar ist.
Durch den Einsatz von reversibel dehydrierbarem Material mit hygroskopischen Eigenschaften, z. B. Zeolith, ist eine Erwärmung des zu behandelnden Gutes im Teilprogrammschritt "Klarspülen" vorzugsweise nicht notwendig. Eine Erwärmung des zu behandelnden Gutes im Teilprogrammschritt der dem Teilprogrammschritt "Trocknen" vorhergeht, insbesondere der Teilprogrammschritt "Klarspülen", ist zwar möglich, jedoch nicht sinnvoll. Trotzdem kann eine geringe Erwärmung beim "Klarspülen", z. B. auf 30°C, angemessen sein. Dies bedeutet eine wesentliche Energieeinsparung. Durch die im Allgemeinen immer auftretende Erwärmung der Luft aufgrund der frei werdenden Kondensationswärme in der Sorptionskolonne im Teilprogrammschritt "Trocknen" wird deren Feuchtigkeitsaufnahmekapazität bei jedem Durchleiten durch die Sorptionskolonne erhöht, was zur Verbesserung des Trocknungsergebnisses und zur Verkürzung der Trocknungszeit führt. Eine zusätzliche Erwärmung der Luft mit einer Heizung im Teilprogrammschritt "Trocknen" und damit auch des Geschirrs ist normalerweise nicht erforderlich, weil sich die Sorptionskolonne aufgrund der Kondensationswärme des Wasserdampfes auf hohe Temperaturen, z. B. 150°C, erwärmt, und dadurch auch die Luft ausreichend hohe Temperaturen, z. B. 60°-70°C, erreicht.
Wie bekannt, wird das reversibel dehydrierbare Material zur Desorption auf sehr hohe Temperaturen erhitzt, wozu Wärmeenergie notwendig ist. Dabei tritt die gespeicherte Flüssigkeit als heißer Wasserdampf aus. Erfindungsgemäß wird der Wasserdampf vorzugsweise mit einem Luftstrom in den Behandlungsraum des Geräts geleitet und die Luft im Behandlungsraum somit erwärmt und dadurch auch die Spülflotte und/oder das Geschirr mit erwärmt. Die durchgeleitete Luft kühlt ab, wodurch der Wasserdampf ganz oben teilweise kondensiert. Vorzugsweise erfolgt dies als geschlossener Luftkreislauf. Die Einleitung des heißen Wasserdampfs und der erwärmten Luft in den Behandlungsraum während eines Teilprogrammschrittes mit zu erwärmender oder unter Umständen mit bereits erwärmter Behandlungsflüssigkeit reicht weitgehendst aus, um die Behandlungsflüssigkeit ausreichend zu erwärmen. Damit kann eine weitere Heizung weitgehendst entfallen und die zur Desorption eingesetzte Wärmeenergie kann bis auf die geringe Energie, die zur Überwindung der Bindungskräfte zwischen Wasser und reversibel dehydrierbarem Material benötigt wird, nahezu vollständig zur Erwärmung der Behandlungsflüssigkeit, Spülflotte, und/oder des Geschirrs verwendet werden. Weiterhin ist neben der Energieeinsparung auch eine effiziente Reinigung des zu behandelnden Guts gewährleistet.
Mit der vorliegenden Erfindung ist eine Geschirrspülmaschine bereitgestellt, mit der es möglich ist, unter wirtschaftlichen Gesichtspunkten das im Spülbehälter befindliche Spülgut effizient zu reinigen und zu trocknen sowie den damit verbundenen Energieaufwand so gering wie möglich zu halten.
Nach einem bevorzugten Merkmal der Erfindung wird Luft aus dem Spülbehälter und/oder aus der Umgebungsluft einerseits während des Teilprogrammschritts "Trocknen" und andererseits vorzugsweise während eines Teilprogrammschritts mit zu erwärmender Spülflüssigkeit, bevorzugt während des Teilprogrammschritts "Reinigen" und/oder "Vorspülen", durch die Sorptionskolonne und in den Spülbehälter geleitet, womit die oben erwähnten Vorteile in der erfindungsgemäßen Geschirrspülmaschine bestimmungsgemäß eingesetzt werden.The dishwasher according to the invention with a washing container and devices for washing dishes using washing liquor has a sorption column that is connected to the washing container in an air-conducting manner and contains reversibly dehydratable material, the sorption column on the one hand for drying the dishes and on the other hand for desorption of the sorption column to heat the heat energy used in the Rinsing container located washing liquor and the dishes is at least partially usable.
By using reversibly dehydratable material with hygroscopic properties, e.g. B. zeolite, heating of the items to be treated is preferably not necessary in the part program step "rinsing". A heating of the items to be treated in the partial program step which precedes the partial program step “drying”, in particular the partial program step “final rinsing”, is possible, but not useful. Nevertheless, a slight warming during "rinsing", z. B. to 30 ° C, be appropriate. This means a substantial energy saving. The generally always occurring warming of the air due to the released heat of condensation in the sorption column in the part program step "drying" increases its moisture absorption capacity each time it is passed through the sorption column, which improves the drying result and shortens the drying time Drying time leads. An additional heating of the air with a heater in the partial program step "drying" and thus also of the dishes is normally not necessary because the sorption column due to the heat of condensation of the steam to high temperatures, z. B. 150 ° C, heated, and thereby the air sufficiently high temperatures, z. B. 60 ° -70 ° C reached.
As is known, the reversibly dehydratable material is heated to very high temperatures for desorption, for which purpose thermal energy is necessary. The stored liquid emerges as hot water vapor. According to the invention, the water vapor is preferably passed into the treatment room of the device with an air stream and the air in the treatment room is thus heated and thereby the washing liquor and / or the dishes are also heated. The air that is passed through cools down, causing the water vapor to partially condense at the top. This is preferably done as a closed air circuit. The introduction of the hot water vapor and the heated air into the treatment room during a partial program step with the treatment liquid to be heated or, under certain circumstances, with the treatment liquid that has already been heated is largely sufficient to heat the treatment liquid sufficiently. This means that further heating can largely be dispensed with and the thermal energy used for desorption can be used almost entirely to heat the treatment liquid, rinsing solution and / or dishes, apart from the low energy required to overcome the binding forces between water and reversibly dehydratable material . In addition to saving energy, efficient cleaning of the items to be treated is also guaranteed.
The present invention provides a dishwasher with which it is possible, from an economic point of view, to efficiently clean and dry the items to be washed and to keep the associated energy consumption as low as possible.
According to a preferred feature of the invention, air from the washing container and / or from the ambient air on the one hand during the partial program step "drying" and on the other hand preferably during a partial program step with rinsing liquid to be heated, preferably during the partial program step "cleaning" and / or "pre-rinsing" the sorption column and passed into the rinsing tank, bringing the above mentioned advantages are used as intended in the dishwasher according to the invention.
Erfindungsgemäß weist der Spülbehälter einen Auslass mit einer Leitung zur Sorptionskolonne auf, wobei die Leitung vorzugsweise über ein Absperrventil und in Strömungsrichtung anschließend vorzugsweise über ein Einlassventil zur Umgebungsluft verfügt, und des Weiteren weist der Spülbehälter einen Einlass mit einer Leitung von der Sorptionskolonne auf, wobei in der Leitung zur Sorptionskolonne ein Gebläse angeordnet ist, das wenigstens einen Teil der Luft im Spülbehälter oder aus der Umgebungsluft der Sorptionskolonne wenigstens zeitweise einführt. Bei einem vorzugsweise geschlossenen Luftsystem ist ein Austausch von verschmutzter Luft aus der Umgebung vollständig ausgeschlossen, womit eine Rückanschmutzung des behandelten Gutes verhindert wird. Das Gebläse lässt sich leicht ansteuern, so dass der Einsatz der Sorptionskolonne genau gesteuert werden kann. Außerdem verstärkt das Gebläse die Wirkung der Sorptionskolonne, da die durchzuleitende Luft schneller gefördert wird.According to the invention, the rinsing container has an outlet with a line to the sorption column, the line preferably having a shut-off valve and then, in the flow direction, preferably an inlet valve to the ambient air, and the rinsing container also has an inlet with a line from the sorption column, wherein in a fan is arranged in the line to the sorption column which at least temporarily introduces at least part of the air in the washing container or from the ambient air of the sorption column. In the case of a preferably closed air system, an exchange of contaminated air from the environment is completely excluded, which prevents back contamination of the treated goods. The fan can be easily controlled so that the use of the sorption column can be precisely controlled. In addition, the fan increases the effect of the sorption column, since the air to be passed through is conveyed more quickly.
In einer weiteren Ausführungsform weist die Sorptionskolonne einen Behälter für das reversible dehydierbare Material auf, der den Austausch von Feuchtigkeit und/oder Wärme zwischen dem reversibel dehydrierbaren Material und der ihn umgebender Luft ermöglicht.In a further embodiment, the sorption column has a container for the reversibly dehydratable material, which allows the exchange of moisture and / or heat between the reversibly dehydratable material and the air surrounding it.
Erfindungsgemäß ist zur Desorption des reversibel dehydrierbaren Materials ein Heizelement, vorzugsweiseelektrisches Heizelement, angeordnet.According to the invention, a heating element, preferably an electrical heating element, is arranged for desorption of the reversibly dehydratable material.
Erfindungsgemäß ist zur Desorption des reversibel dehydrierbaren Materials (11) das Heizelement in der Leitung zur Sorptionskolonne angeordnet.
In einer anderen, vorteilhaften Ausführungsform ist die über den Einlass in den Spülbehälter einleitbare Luft kühlbar, damit das Geschirr nicht durch hohe Temperatur geschädigt wird.According to the invention, the heating element is arranged in the line to the sorption column for desorption of the reversibly dehydratable material (11).
In another, advantageous embodiment, the air that can be introduced into the washing container via the inlet can be cooled so that the dishes are not damaged by high temperatures.
Nach einer zusätzlichen Variante ist am Auslass ein Tropfenabscheider angeordnet oder die Leitung am Auslass einen Teilbereich nach oben geführt, damit über die Leitung kein Spritzwasser zur Sorptionskolonne gelangt.According to an additional variant, a droplet separator is arranged at the outlet or the line at the outlet is led up a partial area so that no spray water reaches the sorption column via the line.
Nach einer anderen Ausführungsform ist die zur Desorption eingesetzte Wärmeenergie vor der Verwendung zur Erwärmung der Spülflotte und/oder des Geschirrs in einem Wärmespeicher, z. B. Latentspeicher, speicherbar.According to another embodiment, the thermal energy used for desorption is prior to use for heating the washing liquor and / or the dishes in a heat store, e.g. B. latent storage, storable.
Die Erfindung wird nachstehend anhand dem in der Zeichnung dargestellten Ausführungsbeispiel einer erfindungsgemäßen Geschirrspülmaschine erläutert.The invention is explained below with reference to the exemplary embodiment of a dishwasher according to the invention shown in the drawing.
Die einzige Figur zeigt in schematischer Darstellungsweise eine erfindungsgemäße Geschirrspülmaschine 1 mit einem Spülbehälter 2, in dem Geschirrkörbe 3, 4 zur Einordnung von nicht dargestelltem Spülgut angeordnet sind.The single FIGURE shows, in a schematic representation, a dishwasher 1 according to the invention with a
Erfindungsgemäß weist die Geschirrspülmaschine 1 eine mit dem Spülbehälter 2 flüssigkeitsleitend verbundene, reversibel dehydrierbares Material 11 enthaltende Sorptionskolonne 10 auf, wobei die Sorptionskolonne 10, wie weiter unten näher erläutert wird, einerseits zur Trocknung als auch andererseits zur Erwärmung durchgeleiteter Luft verwendet wird.According to the invention, the dishwasher 1 has a
Der Spülbehälter 2 weist einen, im beschriebenen Ausführungsbeispiel in seinem oberen Bereich angeordneten, Auslass 5 mit einer Leitung 6 zur Sorptionskolonne 10 und einen im beschriebenen Ausführungsbeispiel in seinem unteren Bereich angeordneten, Einlass 8 mit einer Leitung 7 von der Sorptionskolonne 10 auf. In der Leitung 6 zur Sorptionskolonne 10 ist ein Gebläse 9 angeordnet, das der Sorptionskolonne 10 Luft aus dem Spülbehälter 2 zuführt.The
Bei dem geschlossenen Luftsystem ist ein Austausch von verschmutzter Luft aus der Umgebung vollständig ausgeschlossen, womit eine Rückanschmutzung des behandelten Gutes verhindert wird.With the closed air system, an exchange of contaminated air from the environment is completely excluded, which prevents back contamination of the treated goods.
Zur Desorption des reversibel dehydrierbaren Materials 11 ist ein im gezeigten Ausführungsbeispiel elektrisches Heizelement 12 im beschriebenen Ausführungsbeispiel in der Sorptionskolonne 10 angeordnet. Diese Anordnung des Heizelements 12 in der Sorptionskolonne 10 gehört nicht zur Erfindung.For desorption of the reversibly dehydratable material 11, an
Eine Geschirrspülmaschine weist bekanntlich ein Spülverfahren auf dessen Programmablauf im Allgemeinen aus wenigstens einem Teilprogrammschritt "Vorspülen", einem Teilprogrammschritt "Reinigen", wenigstens einem Teilprogrammschritt "Zwischenspülen", einem Teilprogrammschritt "Klarspülen" und einem Teilprogrammschritt "Trocknen" besteht. Erfindungsgemäß und bei dem erläuterten Ausführungsbeispiel wird Luft aus dem Spülbehälter 2 einerseits während des Teilprogrammschritts "Trocknen" durch die Sorptionskolonne 10 und wieder in den Spülbehälter 2 zurück geleitet. Hierzu wird das Gebläse 9 eingeschaltet. Der Luftweg ist mit den Pfeilen A, B und C angedeutet. Der von dem Gebläse 9 über die Leitung 6 in die Sorptionskolonne 10 eingeleitete Luft wird von dem reversibel dehydrierbaren Material 11 sämtliche Feuchtigkeit entzogen. Dabei wird die Luft von der in der Sorptionskolonne frei werdenden Kondensationswärme der Feuchtigkeit oder des Wasserdampfes erwärmt, wodurch vorteilhafterweise das Feuchtigkeitsaufnahmevermögen der Luft ansteigt. Die nun erwärmte, z. B. auf bis zu 40°-70°C, und sehr trockene Luft gelangt nun über die Leitung 8 wieder in den Spülbehälter. Die in den Spülbehälter 2 eingeleitete, erwärmte Luft ist vollständig trocken und weist aufgrund der höheren Temperaturen ein hohes Aufnahmevermögen für Feuchtigkeit auf. Sie steigt im Spülbehälter 2 nach oben und nimmt die Restfeuchtigkeit an dem Spülgut auf. Sie wird nun, wie oben schon beschrieben, wieder der Sorptionskolonne 10 zugeleitet.As is known, a dishwasher has a washing method whose program sequence generally consists of at least one sub-program step “pre-wash”, a sub-program step “cleaning”, at least one sub-program step “intermediate washing”, a sub-program step “rinsing” and a sub-program step “drying”. According to the invention and in the exemplary embodiment explained, air is passed from the
Durch den Einsatz von reversibel dehydrierbarem Material 11 im Teilprogrammschritt "Trocknen" ist eine Erwärmung des zu behandelnden Gutes im Teilprogrammschritt "Klarspülen" normalerweise nicht notwendig. Dies bedeutet eine wesentliche Energieeinsparung. Durch die Erwärmung der Luft wird bei jedem Durchleiten durch die Sorptionskolonne 10 die Feuchtigkeitsaufnahmekapazität der Luft erhöht, was zur Verbesserung des Trocknungsergebnisses und zur Verkürzung der Trocknungszeit führt. Erfindungsgemäß und bei dem erläuterten Ausführungsbeispiel wird Luft aus dem Spülbehälter 2 andererseits während eines Teilprogrammschritts mit zu erwärmender oder unter Umständen bereits erwärmter Spülflüssigkeit, bevorzugt während des Teilprogrammschritts "Reinigen" und/oder "Vorspülen", im beschriebenen Ausführungsbeispiel während des Teilprogrammschritts "Reinigen" durch die Sorptionskolonne 10 und wieder in den Spülbehälter 2 zurück geleitet. Hierzu wird, wie schon oben erläutert, das Gebläse 9 eingeschaltet. Der Luftweg ist mit den Pfeilen A, B und C angedeutet. Weiterhin wird die Heizung 12 eingeschaltet, um die Desorption des reversibel dehydrierbaren Materials 11 vorzunehmen.As a result of the use of reversibly dehydratable material 11 in the “drying” sub-program step, it is normally not necessary to heat the items to be treated in the “rinsing” sub-program step. This means a substantial energy saving. The heating of the air increases the moisture absorption capacity of the air each time it is passed through the
Wie bekannt, wird reversibel dehydrierbares Material 11 zur Desorption auf sehr hohe Temperaturen erhitzt. Dabei tritt die gespeicherte Flüssigkeit als heißer Wasserdampf aus. Durch die Leitung von Luft mittels des Gebläses 9 durch die Leitungen 6, 8 entsprechend dem Luftweg der Pfeile A,B, C wird der Wasserdampf in den Spülbehälter 2 geleitet und auch die Luft im Spülbehälter erwärmt. Die Einleitung des heißen Wasserdampfs und der erwärmten Luft in den Spülbehälter 2 während des Teilprogrammschritts "Reinigen" in den Behandlungsraum reicht weitgehendst aus, um die Spülflotte und/oder das Geschirr ausreichend zu erwärmen. Damit kann eine weitere Heizung weitgehendst entfallen und die zur Desorption eingesetzte Energie kann bis auf die geringe Energie, die zur Überwindung der Bindungskräfte zwischen Wasser und reversibel dehydrierbarem Material benötigt wird, nahezu vollständig zur Erwärmung der Spülflotte und/oder das Geschirr verwendet werden. Weiterhin ist neben der Energieeinsparung auch eine effiziente Reinigung des Spülguts gewährleistet.As is known, reversibly dehydratable material 11 is heated to very high temperatures for desorption. The stored liquid emerges as hot water vapor. By directing air by means of the
In einer weiteren nicht dargestellten Ausführungsform ist in der Leitung 6 ein Absperrventil und daran anschließend in Strömungsrichtung des Luftweges gemäß Pfeil A ein Einlassventil, z. B. auch über eine weitere Leitung, zur Umgebunsluft angeordnet. Im oben beschriebenen Beispiel ist das Absperrventil geöffnet und das Einlassventil geschlossen, so dass nur Luft aus dem Spülbehälter 2 vom Gebläse 9 angesaugt wird. Durch das ganz oder teilweise Schließen des Auslassventils und das ganz oder teilweise Öffnen des Einlassventils wird ganz oder teilweise vom Gebläse 9 Umgebungsluft angesaugt und in den Spülbehälter über die Leitung 8 und den Einlass 7 eingeführt. Hierzu benötigt der Spülbehälter einen Auslass (nicht dargestellt), um diese Luft aus der Umgebung wieder an die Umgebung abgeben zu können.In a further embodiment not shown, a shut-off valve is in the
In einer anderen nicht dargestellten Ausführungsform ist der Auslass 5 dahingehend ausgebildet, dass durch eine Durchschnittsvergrößerung vom Auslass 5 zur Leitung 6 die Strömungsgeschwindigkeit in der Leitung 6 kleiner ist als im Auslass 5, so dass keine Wassertropfen in der Luft (Nebel) in der Leitung 6 auftreten. Um das Eindringen von Spritzwasser in die Leitung 6 und damit in die Sorptionskolonne 10 zu verhindern, kann entweder die Leitung 6 nach dem Auslass 5 nach oben geführt werden oder am Auslass 5 ein Tropfenabscheider (nicht dargestellt) angeordnet werden.In another embodiment, not shown, the
In einer weiteren nicht dargestellten erfindungsgemäßen Ausführungsform befindet sich das elektrische Heizelement nicht in der Sorptionskolonne 10, sondern in der Leitung 6 zwischen Gebläse 9 und Sorptionskolonne 10, um eine gleichmäßige Erwärmung des dehydrierbaren Materials 11, z. B. Zeolith, zu erreichen. Überhöhte Temperaturen des dehydrierbaren Materials können damit vorteilhafterweise vermieden werden, um daraus resultierende Schäden am dehydrierbaren Material 11 auszuschließen.In a further embodiment of the invention, not shown, the electrical heating element is not located in the
Die Sorptionskolonne wird - wie bereits beschrieben - vorzugsweise während eines Teilprogrammschrittes mit zu erwärmender Behandlungsflüssigkeit mit einer Heizung auf eine sehr hohe Temperatur, z. B. 300° C, aufheizt, damit die Sorptionskolonne das aufgenommene Wasser abgibt. Auch beim Teilprogrammschritt "Trocknen" erhitzt sich die Sorptionskolonne auf hohe Temperaturen, z. B. 150°-200°C, durch die Kondensationswärme des Wasserdampfes oder der Feuchitgkeit.
Damit kann die in den Spülbehälter eingelegte trockene Luft oder die Luft mit Wasserdampf Temperaturen erreichen, z. B. 80°C, welche zu einem Schaden beim Geschirr, z. B. Kunststoffteile, führen können. Die Lufteintrittstemperatur in dem Spülraum muss deshalb in einer weiteren Ausführung mit einer Kühlung soweit abgesenkt werden, dass keine Schäden auftreten.The sorption column is - as already described - preferably during a partial program step with the treatment liquid to be heated with a heater to a very high temperature, e.g. B. 300 ° C, so that the sorption column releases the absorbed water. Also in the part program step "drying" the sorption column is heated to high temperatures, e.g. B. 150 ° -200 ° C, due to the heat of condensation of the water vapor or the moisture.
This means that the dry air or the air with steam that is placed in the washing compartment can reach temperatures, e.g. B. 80 ° C, which can damage the dishes, z. B. plastic parts, can lead. The air inlet temperature in the washing area must therefore be reduced in a further embodiment with cooling to such an extent that no damage occurs.
Im Teilprogrammschritt "Trocknen" wird hierzu Restwasser auf und um die Eintrittsöffnung geleitet und dadurch der Luftstrom gekühlt. Außerdem nimmt die trockene und warme Luft einen Teil des Wassers auf, was aufgrund der Verdunstungskälte zum Abkühlen des Luftstroms führt. In einem Teilprogrammschritt mit zu erwärmender Behandlungsflüssigkeit findet durch das Spritzwasser und den Luftstrom mit Wasserdampf an die Eintrittsöffnung ein Wärmetausch statt. Vorteilhafterweise wird die Eintrittsöffnung dahingehend ausgelegt, dass der Luftstrom nicht unmittelbar auf das Geschirr trifft und eine ausreichende Abkühlung des Luftstroms durch das Spritzwasser statt findet.
Neben der Heizung zum Erhitzen der Sorptionskolonne zur Desorption - nachfolgend Luftheizung genannt - verfügt eine erfindungsgemäße Geschirrspülmaschine in einer Variante über einen Durchlauferhitzer für die Spülflotte, falls aufgrund der vorliegenden Erfindung hierauf nicht verrichtet wird. Falls beim Teilprogrammschritt "Klarspülen" in einer weiteren Ausführung der Erfindung ein Aufheizen notwendig ist, kann dies entweder mit dem Durchlauferhitzer oder mit der Luftheizung bei eingeschaltetem Gebläse erreicht werden. Der Vorteil beim Heizen mit der Luftheizung liegt darin, dass im darauffolgenden Teilprogrammschritt "Trocknen" die in der Sorptionskolonne gespeicherte Wärmeenergie zur Trocknung genutzt werden kann.In the partial program step "Drying", residual water is directed to and around the inlet opening, thereby cooling the air flow. In addition, the dry and warm air absorbs part of the water, which leads to the cooling of the air flow due to the evaporation cold. In a partial program step with the treatment liquid to be heated, a heat exchange takes place through the spray water and the air flow with water vapor at the inlet opening. The inlet opening is advantageously designed in such a way that the air flow does not hit the dishes directly and the air flow is adequately cooled by the spray water.
In addition to the heater for heating the sorption column for desorption - hereinafter referred to as air heating - a variant of a dishwasher according to the invention has a flow heater for the washing liquor, if based on the present Invention is not performed on this. If, in a further embodiment of the invention, heating is necessary in the part program step “final rinsing”, this can be achieved either with the flow heater or with the air heater with the fan switched on. The advantage of heating with air heating is that the thermal energy stored in the sorption column can be used for drying in the subsequent partial program step "drying".
In einer weiteren Variante kann während der Heizphase des Teilprogrammschrittes "Klarspülen" das Gebläse eingeschaltet werden, bei ausgeschalteter Luftheizung. Dadurch wird feuchte Luft durch die Sorptionskolonne geleitet, welche die Feuchtigkeit aufnimmt, und sich durch die frei werdende Kondensationsenergie die Sorptionskolonne und damit auch die durchgeleitete Luft erwärmt. Damit kann die Kondensationswärme zum Aufheizen der Spülflotte und/oder des Geschirrs verwendet werden. Die Sorptionskolonne, z. B. mit Zeolith, ist in dieser Ausführungsform mit einer entsprechenden großen Menge von z. B. Zeolith auszulegen, dass auch im Teilprogrammschritt "Trocknen" noch ein gutes Trochnungsergebnis erzielt werden kann.In a further variant, the fan can be switched on during the heating phase of the “final rinse” part of the program, with the air heating switched off. As a result, moist air is passed through the sorption column, which absorbs the moisture, and the sorption column and thus also the air that is passed through is heated by the condensation energy released. This means that the heat of condensation can be used to heat the washing liquor and / or the dishes. The sorption column, e.g. B. with zeolite, is in this embodiment with a corresponding large amount of z. B. to design zeolite that a good drying result can also be achieved in the part program step "drying".
Mit der vorliegenden Erfindung ist eine Geschirrspülmaschine bereitgestellt, mit der es möglich ist, unter wirtschaftlichen Gesichtspunkten das im Spülbehälter 2 befindliche Spülgut effizient zu reinigen und zu trocknen sowie den damit verbundenen Energieaufwand so gering wie möglich zu halten.The present invention provides a dishwasher with which it is possible, from an economic point of view, to efficiently clean and dry the items to be washed in the
Claims (8)
- Dishwasher (1) with a washing container (2) and devices for rinsing dishes using washing liquor, wherein the dishwasher (1) has a sorption column (10) containing reversibly dehydratable material (11) connected in an air-conducting manner to the washing container (2), wherein the sorption column (10) can be used at least partially on the one hand in order to dry the dishes and on the other hand for the thermal energy used to desorb the sorption column (10) in order to heat the washing liquor located in the washing container (2) and the dishes, wherein the washing container (2) has an outlet (5) with a line (6) to the sorption column (10), wherein the washing container (2) has an inlet (8) with a line (7) from the sorption column (10), wherein a fan (9) is arranged in the line (6) to the sorption column (10), said fan at least temporarily introducing at least one part of the air in the washing container (2) or from the ambient air of the sorption column (10), characterised in that in order to desorb the reversibly dehydratable material (11), a heating element (12) in the line (6) to the sorption column (10) is arranged between the fan (9) and the sorption column (10).
- Dishwasher according to claim 1,
characterised in that
air from the washing container (2) and/or from the ambient air is conducted on the one hand during the sub program step "drying" and on the other hand preferably during a sub program step with washing liquid to be heated, preferably during the sub program step "cleaning" and/or "pre-rinsing", through the sorption column (10) and into the washing container (2). - Dishwasher according to claim 1 or 2,
characterised in that
the line (6) to the sorption column (10) has a shut-off valve and then in the flow direction an inlet valve to the ambient air. - Dishwasher according to one of claims 1 to 3,
characterised in that
the sorption column (10) has a container for the reversibly dehydratable material (11), which enables the exchange of moisture and/or heat between the reversibly dehydratable material (11) and the air surrounding it. - Dishwasher according to one of claims 1 to 4,
characterised in that
an electrical heating element (11) is arranged in order to desorb the reversibly dehydratable material (11). - Dishwasher according to one of the preceding claims,
characterised in that
the air which can be introduced into the washing container (2) via the inlet (8) can be cooled. - Dishwasher according to one of the preceding claims, characterised in that a demister unit is arranged at the outlet (5) or the line (6) at the outlet (5) is guided one subregion upward so that no splash water reaches the sorption column (10) via the line (6).
- Dishwasher according to claim 1,
characterised in that
before being used to heat the wash liquor and/or the dishes the thermal energy used for desorption can be stored in a heat storage tank, e.g. a latent storage unit.
Priority Applications (1)
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PL04740668T PL1667569T3 (en) | 2003-07-30 | 2004-07-05 | Dishwasher |
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DE10334790 | 2003-07-30 | ||
DE10353774A DE10353774A1 (en) | 2003-07-30 | 2003-11-18 | Drying items in domestic dish washing machines has a reversible hydroscopic material filled column through which recirculated air is driven by a fan |
PCT/EP2004/007337 WO2005018409A1 (en) | 2003-07-30 | 2004-07-05 | Dishwasher |
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EP1667569B1 true EP1667569B1 (en) | 2020-09-09 |
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EP (1) | EP1667569B1 (en) |
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WO2005018410A1 (en) * | 2003-07-30 | 2005-03-03 | BSH Bosch und Siemens Hausgeräte GmbH | Method for operating a device with at least one partial programme step of drying |
DE102005004096A1 (en) | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with a Sorptionstrockenvorrichtung |
DE102005004092A1 (en) * | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with a Sorptionstrockenvorrichtung and method for operating the same |
DE102005004093A1 (en) | 2004-12-09 | 2006-06-22 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
DE102005004089A1 (en) | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | Dishwasher with a Sorptionstrockenvorrichtung and method for operating the same |
DE102005004094A1 (en) * | 2004-12-09 | 2006-06-22 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
DE102005004095A1 (en) * | 2004-12-09 | 2006-06-14 | BSH Bosch und Siemens Hausgeräte GmbH | dishwasher |
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DE3626887A1 (en) * | 1986-08-08 | 1988-02-11 | Miele & Cie | Laundry machine and dishwasher, oven or the like, with a dehumidifier |
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DE2016831A1 (en) | 1970-04-09 | 1971-10-21 | Bosch Hausgeraete Gmbh | dishwasher |
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2004
- 2004-07-05 US US10/564,230 patent/US8293024B2/en active Active
- 2004-07-05 WO PCT/EP2004/007337 patent/WO2005018409A1/en active Application Filing
- 2004-07-05 PL PL04740668T patent/PL1667569T3/en unknown
- 2004-07-05 EP EP04740668.1A patent/EP1667569B1/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
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DE3626887A1 (en) * | 1986-08-08 | 1988-02-11 | Miele & Cie | Laundry machine and dishwasher, oven or the like, with a dehumidifier |
Also Published As
Publication number | Publication date |
---|---|
PL1667569T3 (en) | 2021-03-08 |
EP1667569A1 (en) | 2006-06-14 |
US8293024B2 (en) | 2012-10-23 |
WO2005018409A1 (en) | 2005-03-03 |
US20060278257A1 (en) | 2006-12-14 |
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