Dishwasher with system of sorption drying

FIELD: personal use articles.

SUBSTANCE: drying device of a dishwasher (GS) comprises at least one sorption chamber (SB) with a reversibly dehydrogenated sorption drying material (ZEO). This chamber is connected to the washing chamber (SPB) of the dishwasher with at least one air duct (LK). The sorption material (ZEO) is located in the sorption chamber (SB) in the form of a sorption element (SE) in such a way that through substantially every point of the surface (SDF) of passing of the sorption element (SE) substantially the same amount of air may pass.

EFFECT: improvement of the device.

33 cl, 17 dwg

The technical field

The present invention relates to a dishwasher, in particular a domestic dishwasher, which contains at least one of the washing chamber and at least one system of the sorption drying for drying is subjected to washing items, the system of the sorption drying contains at least one adsorption chamber with means daydreamy, i.e., dewatering, sorption material, which is connected to the wash chamber, at least one duct to create air flow.

The level of technology

For example, from patent applications DE 10353774 A1, DE 10353775 A1 or DE 102005004096 A1 known dishwashers with a so-called sorption column, designed for drying dishes. At step "drying" of the corresponding program of the dishwasher, which is designed for drying dishes, moist air from the washing chamber of the dishwasher is run using an air blower through the sorption column contained which means daydreamy desiccant material takes away moisture from the passing air through condensation. For regeneration, i.e. desorption of the sorption column, means daydreamy desiccant material contained therein, is heated to very high temperature. As a result, water accumulated in m is the material, is released in the form of hot water vapor and is directed into the washing chamber with the air flow created by the blower device. This makes it possible to heat the wash solution and/or the dishes in the washing chamber, and the air in the washing chamber. Such sorption column turned out to be a very beneficial device for economical and quiet drying dishes. To prevent local overheating of the drying material during the desorption is provided a heating device located in the direction of the air flow before it enters the air sorption columns (for example, DE A). Despite this "air heating" during desorption, usually it is difficult to constantly maintain a sufficient quality of drainage reversal negidrirovannogo dewatering of the material.

Disclosure of inventions

The task of the invention to provide a dishwasher, in particular a domestic dishwasher, which will improve the sorption and/or desorption means negidrirovannogo, i.e., dewatering, dewatering of the material contained in the sorption element of the sorption drying device.

This problem is solved dishwasher, in particular a domestic dishwasher of the type specified above due to the fact that the sorption material is located in the sorption chamber in the form with blondage element so so, essentially, through every point of the surface passing through the sorption element could be, essentially, the same volume of air.

Thus, to the extent possible, it is guaranteed that the cleaned items in the washing chamber can be dried efficiently, economically and reliably. In addition, it is possible to compactly arrange the drying device in the dishwasher.

In particular, to the extent possible, it is guaranteed that the humid air, which at the time corresponding to the selected drying process flows through the duct from the washing chamber into the sorption chamber and passes through its sorption element with a sorption drying material can be dried efficiently, economically and reliably. After this drying process, for example, during at least one of the washing process or subsequent purification running washing, the sorption material in preparation for the next drying process can be efficiently, economically and gently regenerated, that is prepared by the method of desorption.

Other variants of the invention are disclosed in the dependent claims.

Brief description of drawings

The invention and variants of its execution, as well as their advantages are described in detail below based on the drawings on which the image is but:

Fig.1: schematic view of a dishwasher with a washing chamber and system of the sorption drying, the components of which are constructed according to the invention.

Fig.2: a schematic perspective view of the open washing chamber of the dishwasher (see Fig.1) with the system components of the sorption drying, which is shown partially open, i.e. without coverage.

Fig.3: schematic side view of the system of the sorption drying Assembly (see Fig.1 and 2), the components of which are partially outside on the side wall of the washing chamber, and partly in bottom constructive node under the washing chamber.

Fig.4: a schematic perspective explosive view of the various nodes (individually) sorption camera system sorption drying according to Fig.1-3.

Fig.5: schematic horizontal projection of the sorption chamber (see Fig.4).

Fig.6: schematic horizontal projection (bottom) node sorption chamber (see Fig.5), which is a metal sheet with slits for air-conditioning air flow passing through the sorption material in the sorption chamber.

Fig.7: schematic horizontal projection (bottom) another unit of the sorption chamber (see Fig.4), a tubular heater, designed to heat the sorption material in the sorption chamber with a view to its desorption.

Fig.8: schematic horizontal the social projection (top) tubular heater (see Fig.7) located above the metal sheet with slits (see Fig.6).

Fig.9: a schematic cross-section (side view) sorption chamber according to Fig.4, 5.

Fig.10: is a schematic perspective view of the internal structure of the sorption chamber according to Fig.4, 5, 9, partly in section.

Fig.11: schematic horizontal projection (top) set of system components of the sorption drying according to Fig.1-10.

Fig.12-14: various schematic views of the exhaust system component of the sorption drying (see Fig.1-3), are shown separately.

Fig.15: a schematic cross-section (side) of the intake system element sorption drying (see Fig.1-3), are shown separately.

Fig.16: schematic horizontal projection (top) bottom construction unit of the dishwasher (see Fig.1 and 2).

Fig.17: schematic view of thermoelectric safety device against overheating sorption chamber (see Fig.4-10) system sorption drying (see Fig.1-3, 11).

The implementation of the invention

Elements having the same functionality and principle, have the same designations in Fig.1-17.

In Fig.1 schematically illustrates the dishwasher GS, the main components of which is washing Luggage SPB located underneath the bottom constructive node BG and the TS of the sorption drying, constructed according to the invention. Preferably, the system TS drying is external, that is, it is located outside the washing chamber SPB, partly on the side wall SW, partly in bottom constructive node BG. The main components of this system: at least one duct LK, at least one fixed the fan unit or blower device LT and at least one sorption Luggage SB. Preferably, the washing chamber SPB is one or more lattice baskets GK designed for stacking and washing to be washed items, such as tableware. For the supply of liquid to clean the items inside the washing chamber SPB provided by one or more spray devices, such as one or more rotating consoles SA with jets. In this embodiment, in the washing chamber SPB set the bottom rotary console with nozzles and upper rotating console with jets.

For treatment to be washing items dishwashers perform the washing programme, which contain several stages. In particular, the appropriate washing programme can contain the following separate phases of time for each other: pre-washing (to remove coarse contaminants; treatment stage (with the addition of detergent in the liquid, in particular water); stage intermediate rinsing; final rinse (with an Addendum is receiving the fluid, for example in water, mouthwash, in particular air conditioner); and the final stage of drying (running drying of treated subjects). However, depending on the stage of cleaning or washing the washing on the relevant cleared items is served clean water and/or water and detergent, for example, for the treatment process, process intermediate rinsing and/or final rinse process.

In this embodiment, the fan unit LT and sorption Luggage SB are located in the bottom constructive node BG under the floor DURING the wash chamber SPB. Duct LK starts from the outlet opening ALA, which is located above the bottom DURING the wash chamber SPB in its side wall SW. Next, the inlet area RA1 pipe duct passes from the outside of this side wall SW down to the fan unit LT in bottom constructive node BG. Through the connecting area VA of the duct LK release of the fan unit LT is connected with the inlet opening EO of the sorption camera SB in the area, which is located near the bottom. The outlet opening ALA of the washing chamber SPB is located above the bottom DURING the wash chamber, preferably in the Central region of the side wall SW, and is designed to suction air from the inner space of the washing chamber SPB. Alternatively, of course, can be the positioning of the outlet opening ALA of the rear wall RW (see Fig.2) washing chamber SPB. Essentially, in particular, an advantageous variant, in which the outlet is located, preferably, at least above the level of the foam (i.e. level, which can rise foam generated in the cleaning process), preferably in the upper half of the washing chamber SPB on one of its side walls SW and/or on the back wall. Can also be a suitable option, in which at least one side wall, the lid and/or the rear wall of the washing chamber SPB made several outlet openings, which are connected to at least one duct with one or more inlet openings, which are placed in the housing of the sorption camera SB on the site prior to the sorption material of this camera.

Preferably, the fan unit LT is made in the form of an axial fan. It serves to force feed the humid and hot air LU from the washing chamber SPB on the sorption element SE in the sorption chamber SB. Sorption element SE contains means daydreamy sorption material ZEO, which can absorb and retain moisture from passing through the air LU. Near cover sorption camera SB, on the upper side, is located the outlet AO (see Fig.4, 5), which is connected an outlet element AUS through the through hole at back is their DG (see Fig.13) IN the bottom of the washing chamber SPB with the internal space of the camera. Thus, during the drying programme (washing up), running the drying of treated subjects, humid and hot air LU using the included fan unit LT can be absorbed from the interior of the washing chamber of the steam through the outlet opening ALA of the intake area RA1 pipe duct LK. Then the air can be transmitted through the connecting section VA inward sorption camera SB for the forced ventilation means negidrirovannogo sorption material ZEO in sorption element SE. The sorption material ZEO sorption element SE pulls water from passing humid air, which means that after passing through the adsorption element SE of the dried air may be blown inside the washing chamber of the steam through the exhaust or blowing element AUS. This provides a closed air circulation system through this system TS sorption drying. The spatial location of the various components of this system TS sorption drying is shown in schematic perspective view (Fig.2), as well as schematic side view (Fig.3). In Fig.3 additionally shows a dotted outline of the bottom of the BO of the washing chamber SPB, which contributes to a better understanding of the spatial-geometric structure of the system is s TS sorption drying.

Preferably, the outlet opening ALA is located above the bottom of the BO in a position which allows you to pick up or absorb the maximum amount of damp and hot air LU of the upper half of the washing chamber SPB in the duct LK. After the cleaning process, in particular the process of final heated rinse liquid, wet, and hot air is collected, preferably, above the bottom, particularly in the upper half of the washing chamber SPB. Preferably, the outlet opening ALA is located vertically above the level of foam that can be generated during normal cleaning or in the event of a malfunction. In particular, the formation of foam can be called detergent added to water during treatment process. In addition, the location of the release or outlet ALA best way is chosen so that the inlet area RA1 pipe duct LK on the side wall SW was available as a rising area. In addition, the exhaust hole located in the area of the cover, the Central region and/or the upper region of the side wall SW and/or the rear wall RW of the washing chamber SPB, enables you to securely prevent a situation in which water could be directly injected into the duct LK from the sump (at the bottom of the washing chamber or from the injection of liquid through the outlet opening ALA of the washing Kam the market SPB, then she could get into the sorption chamber SB. In the sorption material ZEO in this chamber could be unacceptable hydrated, partially damaged and become unusable or even completely destroyed.

In the sorption chamber SB located in front of her sorption element SE (in flow direction) is at least one heating device HZ, designed for desorption and thus regeneration of the sorption material ZEO. The heating device HZ serves to heat the air LU, who with the help of the fan unit LT can stretch out on the duct LK in the sorption chamber. This forced heated air picks up the accumulated liquid, in particular water, from the sorption material ZEO when passing through the sorption material ZEO. Water taken from the sorption material ZEO is transferred heated air through the outlet element AUS sorption camera SB inside the washing chamber. Preferably, the desorption process occurs when desirable or is being heated fluid cleaning process or other process subsequent washing programmes washing. When this air is heated to the desorption process heating device HZ and passing through the sorption material in the sorption chamber, can simultaneously use is for heating the liquid in the wash chamber SPB as the sole means of heating or as a Supplement to the conventional water heater.

In Fig.2 presents a perspective view of the main components of the TS sorption drying, located on the side wall SW and bottom constructive node BG (partially open), when the door is open TR dishwasher GS with Fig.1. In Fig.3 presents the corresponding set of system components TS sorption drying (side view). The inlet area RA1 pipe duct LK contains, starting from its inlet EI (located in the area of the outlet opening ALA of the washing chamber SPB), plot AU pipes rising up relative to the gravity vector, and then the section AB of the pipe, falling down relative to the vector SKR gravity. Rising land AU pipe runs up with a small inclination relative to the vertical vector SKR gravity and enters the curved section of the KRA, which has a convex shape and forces the flow LS1 incoming air to change its direction by approximately 180° down in the adjacent area AB of the pipe, passing essentially vertically downwards. This section ends in the fan unit LT. In this embodiment, first, the rising parcel AU pipes, curved section of the KRA and the subsequent dropping down the section AB of the pipe form a planar channel, which in cross section has essentially the form of a flat rectangle.

Inside ZOLOTOGO plot KRA provided by one or more guides or drain ribs AR, the shape of which corresponds to the curvature of the plot. In this embodiment, several arcuate drain ribs AR nested within each other, essentially concentrically located within the curved section of the KRA at a transverse distance from each other with a slight gap between them). In this embodiment, these edges are partially come into the rising land AU pipes and lowering the section AB of the pipe. These drain ribs AR located at a height on the release of the ALA of the washing chamber SPB or inlet EI inlet area RA1 pipe duct LK. These drain ribs AR are used to make liquid droplets and/or condensate from a stream LS1 of intake air from the washing chamber SPB. In the area rising area AU pipes droplets of fluid that has accumulated on the guide ribs AR, can flow in the direction of release of ALA. In the area of the descending pipe section AB droplets of fluid can drain from the alignment ribs AR in the direction of the return rib RR. While the return rib RR is inside the descending section AB of the pipe in the place, which is located above the outlet opening ALA of the washing chamber SPB or higher inlet EI duct LK. While the return rib RR falling within section AB of the pipe forms a drain bevel, and its axis coincides with the axis of the transverse soedinitelnoj the pipeline RF in the direction of release of the ALA of the washing chamber SPB. When this transverse connecting pipe RF covers the intermediate space between the shoulder of the rising area AU of the pipe and the shoulder of the descending section AB of the pipe. When this transverse connecting pipe RF connects with each other the inner space of the rising parcel AU pipe and the inner space of the descending section AB of the pipe. The slope of the return rib RR and the adjacent, aligned transverse connecting pipe RF is selected so that was guaranteed return of condensate or other liquid droplets flowing down from the drain ribs AR in the area of the descending section AB of the pipe, the outlet opening ALA of the washing chamber SPB.

Preferably, drain ribs AR located on the inner wall of the duct LK, remote from the side wall SW of the washing chamber, as the temperature of the inner wall of the duct, located on the outer side, below the temperature of the inner wall of the duct facing the washing chamber SPB. This cooler inner wall of the condensate settles better than on the inner wall of the duct LK facing the side wall SW. It may also be sufficient if the drain ribs AR will be made in the form of jumpers that will act on the inner wall of the duct LK, located on the external side is s, only part of the total width of the duct (in the form of flat channel) in the direction of the inner wall of the duct, located on the inner side and facing the side wall SW. Thanks to this side of the channel cross section will remain free for the passage of air. If necessary, it may be desirable option, in which the drain ribs AR will pass through the channel from the inner wall of the duct, located on the outer side to the inner wall of the duct LK, located on the inner side. Because of this, in particular, curved stretch KRA can be implemented directional movement, and the deviation of the air. Thus, the maximum prevents turbulence of the air, forming interference. Thus, through the duct LK, made in the form of a flat channel, you can transfer the desired volume of air.

Preferably, the return rib RR is located on the inner side of the inner wall of the duct LK outside, and made in the form of jumpers, which acts in the direction of the inner wall of the duct LK, located on the inner side, and is part of the total width of the flat duct LK. Thereby it is guaranteed that in the region of the return rib RR sufficient portion of the channel cross section will remain free for the passage of leakage flow LS1 air. Of course, it may be appropriate alternative, in which the return rib RR will pass through the channel from the inner wall of the duct, located on the outer side to the inner wall of the duct LK, located on the inner side, leaving for the passage of air, in particular, located in the middle of the through hole.

In particular, drain ribs AR and return rib RR will also be used for deposition of drops of water, drops of detergent, drops of conditioning and/or other aerosols contained in the incoming air LS1, and for their removal through the outlet opening ALA of the washing chamber SPB. This is advantageous, in particular, for the desorption process, if at the same time running the cleanup phase. During this stage of cleaning in the washing chamber SPB can be relatively large amount of steam or mist, caused in particular by spraying the liquid through the console SA with jets. This vapor or mist may contain fine mist of water, detergent, conditioner, and other cleaning substances. For such liquid particles carried by a stream LS1 air in the form of fine powder, drain ribs AR form a deposition device. In an alternative embodiment, instead of the drain ribs AR best way can be provided by other means of deposition, in particular design the AI with many edges, for example wire mesh.

In particular, the rising angle or essentially vertically upwards plot AU pipe is used to the maximum extent possible to prevent direct ingress of liquid droplets or even spray jets produced by the spray device SA, for example, a console with nozzles during the cleaning or another cleaning process, together with the intake flow LS1 air on the sorption material in the sorption chamber. In the absence of such withholding or deposition of droplets of a liquid, in particular droplet of mist or vapor sorption material ZEO would be unacceptably wet and unusable. In particular, could occur premature saturation of the admitted liquid drops, for example drops of mist or vapor. Thanks to the intake of the rising branch of the AU bandwidth, and one or more precipitating or catching elements in the upper bend or curved top section of the KRA, which is located between the rising branch of the AU and the descending branch AB bandwidth, to the extent possible, prevents the passage of drops of detergent, conditioner and/or other aerosols through this barrier in a downward direction and hit the fan LT, and into the sorption chamber SB. Of course, instead of what the combination of rising land AU pipes and the descending section AB of the pipe, and instead of one or more precipitating elements can be a barrier to other design performs the same function.

In summary, dishwasher GS in this embodiment, contains a drying device for drying is subjected to washing items by adsorption using reversal negidrirovannogo sorption material ZEO, which is placed in the sorption chamber SE. This chamber is connected to the washing chamber SPB, at least one duct LK, designed to create a flow LS1 air. The inlet area RA1 pipe duct in cross section has essentially the form of a flat rectangle. After its intake area RA1 duct passes (in flow direction) cylindrical, essentially, VA area of the pipe. Preferably, this area is made of at least one polymeric material. This site is located, in particular, between the side wall SW and/or rear wall RW of the washing chamber and the outer wall of the housing of the dishwasher. When this duct LK contains at least one rising area AU of the pipe. This section goes upward from the outlet opening ALA of the washing chamber SPB. In addition, rising land AU pipes (in flow direction) it contains, best way, at least one descending section AB Tr the least. Between the rising parcel AU pipes and the descending section AB of the pipe is provided, at least one curved section of the KRA. In particular, the cross-sectional area of the curved section KRA exceeds the cross-sectional area rising area AU of the pipe and/or a lowering of the section AB of the pipe. Inside the curved section KRA includes one or more guide ribs AR designed to smooth the flow LS1 air. At least one of the guide ribs AR optionally extends from the curved section of the KRA in the rising parcel AU pipes and/or lowering the pipe section AB. One or more guide ribs AR are, in particular, on the release of the ALA of the washing chamber SPB. The corresponding guide rib AR goes from the wall of the duct facing the housing of the washing chamber to the opposite wall of the duct remote from the housing of the washing chamber, preferably, is essentially the entire width of the duct. At least one return rib RR is located inside the descending section AB of the pipe on the wall of the duct facing the housing of the washing chamber and/or on the duct wall, remote from the housing of the washing chamber above the inlet EI duct LK. The return rib RR is connected to condensate drain) with inlet EI duct LK transverse connecting trubor what Bodom RF, which lies in the intermediate space between the rising parcel AU pipes and the descending section AB of the pipe. It is inclined to the intake hole EI. Return the edge goes from the wall of the duct facing the housing of the washing chamber in the direction of the wall of the duct LK, remote from the housing of the washing chamber, and is, preferably, only part of the width of the cross section of the duct.

In Fig.3 descending branch AB of the duct LK enters the fan unit LT, essentially vertically. The intake air flow LS1 air is blown from the issue of the fan unit LT through the tubular connecting section VA in connected with him inlet ES sorption camera SB, which is located near the bottom of the camera. The stream LS1 air enters the lower part of the sorption camera SB in the direction of the ESR occurrences (in this case, in particular, essentially horizontal) and is deflected in a different direction DSR of the passage (flow) of the stream where it passes through the interior of the sorption camera SB. Such a direction DSR of the passage passes through the sorption chamber SB from the bottom up. In particular, the inlet pipe ES rejects the incoming flow LS1 air in the sorption chamber SB so that he deviated from his direction ESR occurrences, in particular, approximately 90° in the direction of the DSR is responsive is of sorption camera SB.

According Fig.3, the sorption Luggage SB most freely suspended under the bottom of the BO in the bottom constructive node BG washing chamber SPB so that between it and the adjacent components and/or parts of the bottom structural node BG remained the specified minimum clearance LS (see also Fig.10) that is designed to protect from overheating. For sorption camera SB, freely suspended under the floor DURING the wash chamber, that is, in this case, under the cover bottom constructive node BG, given the destruction of FRA is provided, at least one transport protective element TRS. This item is installed so that he was propped up from below the sorption chamber SB, if when moving down from its freely suspended position. At least in the area of the sorption element SE sorption camera SB, in addition to the internal casing IG this camera provides at least one external enclosure AG. This external enclosure is mounted so that the overall body GT camera has got a double. That is, between the inner casing IG and the external shell AG has air gap LS, performs the function of insulating the layer. Due to the fact that the wall sorption camera SB, at least around sorption element SE this camera, partially or fully, is, at m is re, double, in addition to the freely suspended position sorption camera SB or independently of it provides additional protection against overheating. This additional protection from overheating adequately protects possibly available neighboring nodes and components of bottom constructive node BG from impermissible overheating or burnout.

Essentially, the housing of the sorption camera SB has such a geometric shape that provides sufficient clearance along its perimeter to the rest of the parts, or components bottom constructive node BG, serves as a protection against overheating. For example, to this end, the wall SW2 corps sorption camera SB, facing the rear wall RW of the bottom structural node BG, has a concavity AF, the form of which follows the shape turned towards her rear wall RW.

Sorption Luggage SB is located on the bottom side of the bottom of the BO of the washing chamber SPB, in particular, in the area of the through-hole DG (see Fig.3, 13) of the bottom of the BO. This shows, in particular, in schematic side view (Fig.3). In this figure the bottom of the BO of the washing chamber SPB has slope from their outer edges ARA to the field FSB fluid collection. Sorption Luggage SB is mounted on the bottom of the BO of the washing chamber SPB so that its cover DEL runs essentially parallel to the bottom side of the bottom of the BO and to remove the specified LSP from it. Free hanging with blonay camera SB provides the connection between, at least one connecting node with the lower side of the bottom sorption camera SB, in particular the basement SO, and the node with the upper side of the bottom (in particular, the discharge element AUS) sorption camera SB in the area of the through-hole DG in the bottom DURING the wash chamber SPB. The connection is, in particular, a clamping connection. Clamping connection can be implemented detachable, in particular a screw connection, bayonet locking BJ (see Fig.13) or without it, which connects the node with the lower side of the bottom sorption camera SB and the node with the upper side of the bottom sorption camera SB. Edge region RZ (see Fig.13) around the through hole DG-bottom BO is clamped between the discharge node with the lower side of the bottom, such as a basement SO the sorption camera SB, and located above the bottom of the BO outlet element or element AUS protection from spray. In Fig.13, in order to simplify the figure, the bottom of the BO of the washing chamber SPB and the lower node with the lower side of the bottom shown by the dotted line. The end extremity of the discharge of the node with the lower side of the bottom and/or splash guard AUS with the upper side of the bottom passes through the through hole DG-bottom BO. The final node from the bottom part contains the socle SO, surrounding the outlet AO cap DEL sorption camera SB. The splash guard off on the upper side of the bottom contains the discharge port ACT and the splash cover SH. Between node AUS from the top side of the bottom of the site SO from the bottom of the bottom is provided, at least one sealing element DI1.

Summarizing the above, sorption Luggage SB as freely as possible is suspended under the bottom of the BO of the washing chamber of the steam so that it is defended by a specified minimum distance LSP from neighboring components and parts of the bottom structural node BG to protect from overheating. Under sorption camera SB also provides installation protective element TRS, attached to the bottom of the bottom structural node on the specified removal FRA. This installation protective element TRS is in order if necessary to prop up the bottom of freely suspended under the bottom of the BO of the washing chamber SPB sorption camera SB, when she, for example, when the transport moves down together with the bottom BO due to concussion. This installation protective element TRS can be formed, in particular, curved down U-shaped metal bracket that is fixed on the bottom of the bottom structural node. In the upper part of the sorption camera SB, on the cover of the DEL has a vent AO. Around the outer edges of this outlet AO is acting up the basement SO. In the hole of the base SO having approximately circular shape, is inserted a cylindrical pipe STE cap (see Fig.4, 5, 9, 13), who stands up and serves as a mating component for cremamagazine it the outlet (inlet) pipe ACT. Preferably, it has an external thread with a built-in bayonet locking BJ, which accordingly cooperates with the internal thread of the exhaust inlet pipe AKT. On the upper side of the cap SO include the selection edge, which concentrically surrounds the nozzle STE cap and on which is located a sealing ring DI1. It is shown in Fig.3, 4, 9, 13. This sorption Luggage SB pressed tightly against this sealing ring DI1 to the bottom side of the bottom of the BO. Sorption Luggage hold for the removal of the LSP from the lower side of the bottom BO due to the height of the plinth SO. From the top side of the bottom BO exhaust inlet pipe ACT passes down through the through hole DG-bottom BO and screwed to the paired nozzle STE cap, and also recorded from opening the bayonet locking BJ. When this exhaust inlet pipe ACT is located on the perimeter of the outer edge of the area RZ of the bottom of the BO around the through hole DG and tight annular outer edge of the APR to this area. This effect is achieved due to the fact that the outer edge region RZ of the bottom of the BO around the through hole DG tightly clamped between an annular lower bearing edge of the APR exhaust inlet pipe ACT and upper supporting edge of the cap SO located there through the sealing ring DI1. Since the sealing ring DI1 pressed with igna side to the bottom of the BO, it is protected from damage and ageing under the action of the detergent contained in the wash liquid. Thus, it provides a tight end-to-end connection between the exhaust inlet spigot ACT and base are SO. Best way, such a connection at the same time works as a device for hanging sorption camera SB.

Because the base is SO up to a height of LSP cap from the rest of the surface cover DEL, guaranteed the existence of a gap between the cover DEL and the bottom side of the bottom of the BO. In this embodiment (Fig.3) the bottom of the BO of the washing chamber SPB has a slope from its edge region on the perimeter of the side wall SW and the posterior wall RW in the direction of the field FSB collecting liquid, which is preferably at the center. Underneath can be a sump PSU circulation pump UWP (see Fig.16). In Fig.3 the bottom of the BO, tilted from the outside inward to the deeper team field FSB, shown by the dotted line. The location of the sump PSU with the installed circulating pump UWP under deeper team area FSB is shown on the horizontal projection of the bottom structural node BG (see Fig.16). Preferably, the sorption camera SB set at the bottom of the BO of the washing chamber SPB so that its cover DEL runs essentially parallel to the bottom side of the bottom of the BO and to remove the specified LSP is t her. To this end, the cap SO located on the nozzle STE cap is set at right angles to the surface normal of the cover DEL.

In accordance with Fig.4 and 10, sorption Luggage SB contains a Cup-shaped part of the GT housing, which is closed by a cover DEL. In the Cup-shaped part of the GT chassis is at least one sorption element SE reversal daydreamy sorption material ZEO. Sorption element SE is located in a bowl-part of the GT chassis so that its sorption material ZEO could be blown by a stream LS2 air, essentially in the direction of the gravity vector or in the opposite direction. This thread LS2 is formed by deflection of the flow LS1 air passing through the duct LK. Sorption element SE contains at least one lower sieve or grate US and at least one of the upper sieve or grid OS, which are located at specified distance H in height from each other (see in particular Fig.9). The space between the two screens or grilles US, OS, most filled with the sorption material ZEO. In the Cup-shaped part of the GT housing is located at least one heating device HZ. The heating device HZ is (in the direction DSR of the passage flow sorption camera SB), in particular, before the sorption element SE containing means is everyway sorption material ZEO. The heating device HZ is provided in the lower cavity UH Cup-shaped part of the GT body, which is going to air LS1 coming from the duct LK. In the Cup-shaped part of the GT chassis is the inlet opening EO duct LK. Cover DEL is the outlet of the AO for the prom element AUS. Cover DEL and Cup-shaped part of the GT chassis is used, preferably, a heat-resistant material, in particular sheet metal, preferably stainless steel or stainless alloy. Cover DEL as tight closes the Cup-shaped part of the GT body. The outer edge of the perimeter of the lid DEL connects with the upper edge of the Cup-shaped part of the GT body only mechanically, in particular by using deformation, joint, clamps, clamps, in particular flange or rivets. This method is technologically simple and provides a stable, heat-resistant and airtight connection. Cup-shaped part of the GT case has one or more side walls SW1, SW2 (see Fig.5), which is oriented essentially vertically. The external contours of this part, essentially correspond to the internal circuits intended for her mounting space EBR provided, in particular, in the bottom constructive node BG (see Fig.16). Both adjacent to each other, the side walls SW1, SW2 have outer surfaces, is the quiet focus, essentially at right angles to each other. At least one lateral wall, SW2 for example, contains at least one recess, such as AF (see Fig. 3), the shape of which essentially corresponds to the shape of the rear wall and/or side wall of the bottom structural node BG, located under the bottom of the BO of the washing chamber SPB. Sorption Luggage SB is in the back corner EBR between the rear wall RW and the adjacent side wall SW of the dishwasher GS, in particular its bottom constructive node BG.

Cup-shaped part of the GT housing has at least one through hole DUF intended, at least one electrical contact AF1, AF2 (see Fig.4). In the overlap region above the through hole DUF provides protection from drops leaf TSB length which at least corresponds to the area occupied by these holes. Leaf TSB that protects against drops, is sloped to drain.

In Fig.4 shows a schematic and perspective explosive view of the various components of the sorption camera SB in an exploded state. Components of the sorption camera SB are located vertically above each other on several levels. This design sorption camera SB in the form of layers (vertically upwards) illustrates, in particular, the cut (Fig.9) and in perspective view in cross-section (Fig.10). Sorption to the measure SB contains the lower cavity UH, which is located near the bottom and is designed to collect air received through approximately horizontal inlet ES. Above this lower cavity UH is the sheet SK with slots that is used for conditioning the flow of air coming in above him tubular heater HZ. When this sheet SK with slots planted on the base edge envelope of the inner space of the sorption camera SB on the perimeter. This reference edge is separated by a given distance in height from the inner side of the bottom sorption camera SB to form a lower cavity UH. Preferably, the sheet SK with slots contains one or more clamps to secure it on the side of the side surface, at least on the inner wall of the sorption camera SB. This can be implemented in a reliable fixation of the sheet SK with slots. In accordance with the form of a sheet with slits from the bottom (see Fig. 6), this sheet contains the slits SL, which essentially correspond to the trajectory turns tubular heater located above the sheet SK with slots. While the slots or oblong holes SL sheet SK with slots are located in those places where the flow LS1 air coming into the sorption chamber SB, essentially horizontally, has a lower rate (essentially vertical) direction DSR is ragozzine flow sorption camera SB and spreads more that is a wider area than in places where the flow LS1 air has a higher speed in the direction DSR of the passage flow sorption camera SB. Due to this maximum is aligned to the local profile of the flow LS2 air that passes through the adsorption chamber SB upwards in the direction of the DSR flow. In the context of the invention under the alignment of the local profile of the air flow is understood, in particular, the situation in which, essentially, through any point of the joining surface of the passage is, essentially, the same volume of air approximately the same flow velocity.

Tubular heater HZ is (in the direction of the DSR flow) at a given height above the sheet SK with slots. For this, he can keep using several sheet parts W, made in the form of ridges, at a certain height above the slits SL. Such sheet-metal part W (see Fig.6), preferably, alternately back tubular heater top and bottom throughout its duration. As a result, firstly, provides reliable fixation of the tubular heater HZ above the sheet SK with slots, and secondly, to the extent possible, prevents the deformation of the sheet SK with slots that could occur under the action of heat from truncator the heater HZ. In the direction of the DSR flow for tube heater HZ is free intermediate space ZR (see Fig.9), after which the flow LS2 air rising, essentially, from the bottom up, is fed to the inlet surface of the SDF of the sorption element SE. At the entrance of this sorption element SE is lower sieve or grate US. At some distance H in height from the sieve or grid US, at the output of the element is the top sieve or grid OS. For both of US sit, OS on the internal walls of the sorption chamber is provided intermittent or continuous supporting edge, allowing you to set and hold the sieves US, OS in the respective height position. Preferably, both sieves US, OS are parallel to each other on a given distance H in height from each other. The space between the bottom sieve US and the top sieve OS filled with the sorption material ZEO, so that was very fully occupied volume between the two sieves US, OS. When sorption camera mounted SB, input US sieve and output sieve OS are essentially in a horizontal plane (relative to the vertical Central axis of the sorption camera SB and relative to the direction DSR of passing flow) one above the other and at a given distance H in height from each other. In other words, in this embodiment executed what I sorption element SE is formed sorption material ZEO, fills the volume between the bottom sieve US and the top sieve OS. In the direction of the DSR flow over the sorption element SE is provided by the upper chamber HE used to collect the outgoing air. This exhaust air LS2 is directed through the release of AO pipe STE cap into the exhaust inlet pipe of the ACT, where it is blown into the interior of the washing chamber SPB.

Sheet SK with slots provides air flow or affects the air flow LS2, rising upwards in the direction of the DSR flow, so that through the tubular heater, essentially, at any point of its longitudinal length, essentially, took place the same volume of air. The combination of the sheet with slits and located over him tubular heater HZ to the extent possible, ensures that the flow LS2 air can be evenly heated during desorption process in front of the entrance surface of the lower sieve US sorption element SE. When this sheet with slots provides the most uniform local distribution of the flow of heated air on the entrance surface of the STF sorption element SE.

In addition to the sheet SK with slots or independently, if necessary, it may be appropriate heating device located outside Sorbs the Onna camera SB in the connecting section between the fan unit LT-inlet sorption camera SB. Since the cross-sectional area of this tubular connecting section VA is less than the sectional area of the sorption camera SB for flow air flow LS1 air can be evenly heated to the desorption process before he gets into the sorption chamber SB. In this case, if necessary, you can completely abandon sheet SK with slits.

In particular, if air heating is a heating device in the sorption chamber SB, if necessary, it may be desirable option, where as before the heating device HZ, and after it (in the direction of the DSR flow passage sorption camera SB) is at least one element of the conditioning air flow. This item is located so that through the volume of the sorption material ZEO for the input surface SDF bottom sieves US at any point could be about the same volume of air. Because of this, in particular, even during the sorption process, when the heating device HZ deactivated, i.e. disabled, to the maximum extent possible the effect of the fullest possible participation of all the sorption drying material in the selection of moisture from the passing air LS1. Similarly, during the desorption process, in which the passing air LS2 heating is by a heating device HZ, the accumulated water is again removed from all of the sorption material, located in the intermediate space between the two sieves US, OS. In the sorption material ZEO at each point within this space can be reclaimed, essentially, completely and thereby regenerated for subsequent drying process.

The surface area of the SDF passing the sorption element SE inside sorption camera SB in this embodiment, more of the cross-section area of the end of an inlet pipe ES duct LK or tubular connecting section VA. Preferably, the surface area of the SDF passing through the sorption material in the 2-40 times, in particular in 4-30 times, preferably 5-25 times the flow area of the intake pipe ES duct LK, which is measured in the input area of the nozzle in the inlet opening EO of the sorption camera SB.

In summary, the sorption material ZEO bulk fills the volume between the bottom sieve US and the top sieve OS so that the surface of the SDF reference stream and the surface of the SAF exit flow is oriented essentially perpendicular to the vertical direction DSR flow. The lower sieve US, the top sieve OS and located between the sorption material ZEO form similar to each other surface of the passage through which the air LS2. Due to the fact to the extent possible, allows flow of approximately the same volume through any point of the sorption material in the sorption volume element SE. As a result, when desorption to the extent possible, excluded local overheating and thus possible damage to the sorption material ZEO. Thus, when sorption is possible uniform sampling of the moisture from the drying air and, thus, optimal use of the sorption material ZEO available in sorption element SE.

Summarizing the above, in particular, it may be desirable option, in which the sorption chamber SB and/or in the inlet section VA, ES pipe (which is converted from the entrance to the sorption chamber SB) duct LK, in particular after at least one fan unit LT is installed in the duct LK, there is one or more elements of SK-conditioning flow. Such elements have one or more slits SL for air in such a way as to ensure the alignment of the local profile of the flow LS2 air that passes through the adsorption chamber SB upwards in the direction of the DSR flow. In the direction DSR of the passage flow sorption camera SB in the lower cavity UH this camera is provided, at least one element SK air conditioning, located along the axis of the height in front of the heating device HZ. In this embodiment, as an element of SK air conditioning is used the East with slots or holes. The slits SL in the sheet SK correspond, essentially, one tubular heater HZ, which is located at some distance above the slits SL of the sheet with slits and serves as a heating device. Sheet with slits is located essentially parallel to and at some distance from the surface of the SDF air inlet of the sorption element SE sorption camera SB. Air hole, in particular the slits SL are located in those areas of the element SK air-conditioning, in which the flow LS1 air coming into the sorption chamber SB, has a smaller velocity in the direction of the DSR passing sorption camera SB, preferably, extends over larger areas than in places where the flow LS1 air coming into the sorption chamber SB has a higher speed in the direction DSR of the passage flow sorption camera SB.

In summary, the system of the sorption drying has the following specific conditions of flow in the region of the sorption chamber. Duct LK connected with sorption camera SB so that the incoming flow LS1 air enters the sorption chamber SB in the direction of the ESR occurrence and is deflected in a different direction DSR flow, where it passes through the interior of the sorption camera SB. The direction of the production coming out of sorption camera SB flow LS2 in which Suha match essentially, the direction DSR flow. The inlet area RA1 pipe duct LK is in the sorption chamber SB so that the direction of the ESR his entry goes in the direction DSR of the passage flow sorption camera SB at an angle, in particular from 45° to 135°, preferably about 90°. Before sorption camera SB (flow direction) in the intake area RA1 duct LK has at least one fan unit LT, designed to create a forced flow LS1 air in the direction of the at least one inlet SW sorption camera SB. The fan unit LT is installed in the bottom constructive node under the washing chamber SPB. The surface area of the SDF passing through the sorption material ZEO inside sorption camera SB this option provides more surface area for the passage of the inlet pipe ES duct LK included in the inlet opening EO of the sorption camera SB. Preferably, the surface area of the SDF passing sorption camera SB 2-40 times, in particular in 4-30 times, preferably 5-25 times more surface area for the passage of the end of an inlet pipe ES duct LK included in the inlet opening EO of the sorption camera SB. At least one sorption element SE of the sorption material ZEO is located in the sorption chamber SB still the way to flow LS1 air coming into the sorption chamber SB from the washing chamber SPB on the duct LK, could pass through the sorption material ZEO, essentially, in a direction that corresponds to the gravity vector or the opposite of him. Sorption element SE sorption camera SB contains at least one lower sieve or grate US and at least one of the upper sieve or grid OS, which are located at specified distance H in height from each other, and the space between the two screens or grilles US, OS, most filled with the sorption material ZEO. In particular, the surface of the SDF entry and the surface of the SAF exit sorption element SE sorption camera SB have essentially the same area. In addition, the surface of the SDF entry and the surface of the SAF exit sorption element SE sorption camera SB suitable are essentially similar to each other. Sorption camera (in the direction of the DSR flow) contains at least one layered structure consisting of the lower cavity UH and located above it (in the direction of the DSR flow) sorption element SE. At the bottom of the cavity UH camera is at least one heating device HZ. In the sorption chamber SB on sorption element SE is at least one upper cavity HE designed the traveler to collect the outgoing air LS2. The sorption material ZEO fills the bulk volume of the sorption element SE sorption camera SB so as to form a surface SDF reference stream, which is essentially perpendicular to the direction DSR flow, and the surface of the SAP output stream, which is most parallel to the first surface. In the top cover DEL sorption chamber has at least one outlet JSC, which is connected through a through hole DG in the bottom DURING the wash chamber SPB with the inner space of the washing chamber through at least one outlet node of the ACT.

Best way, the sorption material ZEO is located in the sorption chamber SB in the form of the sorption element SE so that, essentially, through any point of occurrence of the surface of the SDF passing the sorption element SE could be, essentially, the same volume of air. Preferably, as the sorption material ZEO is used containing aluminum oxide and/or silicon reversal daydreamy material, silica and/or zeolite, in particular zeolite types A, X, Y, individually or in any combinations. Expediently, the sorption material is poured into the sorption chamber SB in the form of granular solids or granules with lots of grains, essentially, from 1 to 6 mm, in particular from 2.4 to 4 mm The height H of the layer of filled grains, at least 5 times the grain size. The sorption material ZEO is present in the form of granular solids or granules, it is advisable filled in the adsorption chamber in the direction of the gravity vector layer, the height of which, essentially, 5-40 times, in particular, 10-15 times higher than the grain size of the granular solids or granules. Preferably, the height H poured layer of the sorption material ZEO is, essentially, from 1.5 to 25 cm, in particular from 2 to 8 cm, preferably from 4 to 6 cm, Preferably granular solid or granules may consist of a number of essentially spherical particles. Best way, the sorption material ZEO, made in the form of granular solids or granules, it has an average density of backfill at least 500 kg/m³in particular, in essence, from 500 to 800 kg/m³in particular from 600 to 700 kg/m³in particular from 630 to 650 kg/m³in particular, preferably approximately 640 kg/m³.

Expediently, the weight amount of reversal negidrirovannogo sorption material ZEO in the sorption chamber SB, designed to absorb moisture, which has a flow LS2 air is selected so that the amount of liquid absorbed sorption material ZEO was the smaller amount of liquid, served on the cleaned items, in particular, at the stage of final rinse.

In particular, it may be desirable option, in which the sorption chamber SB is the weight amount of the reversal negidrirovannogo sorption material, which is sufficient to absorb moisture, corresponding essentially to the volume of liquid that remains to be washing the items upon completion of the final rinse. The amount of absorbed water is preferably from 4 to 25%, in particular from 5 to 15% of the volume of fluid filed on the cleaned items.

It is advisable, in the sorption chamber SB placed the weight amount of the sorption material ZEO, comprising, essentially, from 0.2 to 5 kg, in particular from 0.3 to 3 kg, preferably from 0.5 to 2.5 kg

In particular, the sorption material ZEO contains pores, preferably having a size essentially of from 1 to 12 angstroms, in particular from 2 to 10 angstroms, preferably from 3 to 8 angstroms.

Expediently, the absorptivity of the material is essentially of 15 to 40, preferably from 20 to 30 weight percent of its dry mass.

In particular, the desorption of the sorption material is possible at a temperature essentially of from 80° to 450°C., in particular from 220° to 250°C.

Duct, sorption Luggage and/or Odie is or more elements, directing the flow, it is designed in such a way that through the sorption material to sorption and/or desorption could be the air flow speed, essentially, from 2 to 15 l/sec, in particular from 4 to 7 l/sec.

In particular, it may be expedient variant, in which the sorption material ZEO is attached, at least one heating device HZ, which can provide equivalent heating capacity from 250 to 2500 W, in particular from 1000 to 1800 watts, preferably from 1200 to 1500 watts to heat the sorption material in order desorption.

Preferably, the ratio of the heating power of at least one of a heating device attached to the sorption material for desorption, and the flow rate of air passing through the sorption material is selected in the range from 100 to 1250 W·s/l, in particular from 100 to 450 W·s/l, preferably from 200 to 230 W·s/l

Preferably, the sorption chamber for the sorption material is provided by the surface of the passage, the area of which amounts to, essentially, from 80 to 800 cm²in particular from 150 to 500 cm².

Appropriate height H poured layer of the sorption material ZEO above the surface of the SDF occurrence of sorption camera SB is essentially constant.

In particular, suitable VA is int, in which the sorption material in the sorption chamber SB is able to absorb water volume, essentially, from 150 to 400 ml, in particular from 200 to 300 ml.

In addition, at least one system component TS of the sorption drying is provided by at least one thermal device TSI protection from overheating (see Fig.4, 6, 8, 9). Preferably, this component may be a node sorption camera SB. This node can be attached, at least one thermal device TSI protection from overheating. In this case thermal device TSI protection against overheating is located outside on the sorption chamber SB. As thermal devices TSI overheating protection is used, at least one electrical protection unit from overheating. In this embodiment, it is attached to the heating device HZ, which is in the sorption chamber SB.

In the embodiment according to Fig.4, 6, 8, and electrical protection unit from overheating placed in an external recess EBU on the inner casing IG sorption camera SB at the height of the heating device HZ. It contains at least one electrical switch TSA and/or at least one fuse SSI (see Fig.17). Electric switch TSA and/or fuse SSI electric unit TSI protect it from overheating, install the Lena, preferably, sequentially, at least one electrical circuit UB1, UB2 heating device HZ (see Fig.8).

In addition, it may be appropriate, at least one control device is NOT, ZE (see Fig.16), which, in particular, in case of an error interrupts the power supply to the heating device HZ. The error is, for example, exceeding the upper limit temperature.

In addition, as thermal protection device against overheating can be used as free suspension sorption chamber, in particular, at the base BO of the washing chamber SPB.

In addition, thermal protection device against overheating may include a support sorption camera SB so that between sorption camera SB and adjacent components and/or parts of the bottom structural node BG had a specified minimum distance LSP.

As a thermal protection device from overheating, in addition to the above measures or independently, may be used, at least one external enclosure AG, supplementing the internal casing IG sorption camera SB, at least in the area of the sorption element SE sorption camera SB. Thus between the inner casing IG and the external shell AG provided a heat-insulating layer in the form of an air gap LS.

Heat is a recreational device HZ, it is shown in Fig.4, 7, 8, 9) has two poles AP1, OR connections that are brought out through the corresponding through holes in the housing of the sorption camera SB. Preferably, each connecting pole or contact AP1, AR connected in series with the element overheating protection. Elements overheat protection combined in a unit TSI protect it from overheating, which is located outside of the housing of the sorption camera SB near both contacts AP1, AR. In Fig.17 shows a diagram of the overheat protection for the tube heater HZ with Fig.8. On the first hard contact AP1 using welded connections SWE1 installed first cable jumper UB1. Accordingly, the second hard contact OR using welded connections SWE2 fixed second cable jumper UB2. By means of plug connections SV4 cable jumper UP2 electrically connected with the switch TSA. Cable jumper UB1 through the plug contact SV3 electrically connected to thermoelectric fuse SSI. On the input side by means of plug connections SV1 first supply line SZL1 connected to the ungrounded output terminal AF1 fuse SSI. Accordingly, the second supply line SZL2 connected to the ungrounded output terminal AF2 th TSA through connectors SV2. In particular, vtorayatisya wire SZL2 may be a neutral wire, while the first supply line SZL1 can be a "phase". Switch TSA opens when exceeds the first upper limit temperature of the tubular heater HZ. As soon as the temperature falls below this value, the switch again closes, resulting in renewed heating tube heater HZ. If, however, you will reach the critical temperature limit tube heater HZ, greater than the first limit, it will melt fuse SSI, and the electrical circuit of tube heater HZ will be open for a long time. Both element overheat protection device TSI overheating protection are in close heat conducting contact with the inner casing IG sorption chamber. They can operate independently from each other, when will be exceeded certain assigned to them outside temperature.

In accordance with Fig.10, 13, 14 discharge port ACT, coupled with the outlet of the JSC in the basement SO the sorption camera SB passes through the through hole DG-bottom BO, preferably, in the corner area EBR washing chamber SPB, which is located outside the surface of the rotation, cover with a console SA with jets. This is shown in Fig.2. Essentially, an outlet ACT out of the bottom of the BO in the place of the inner space of the washing ka is a career SPB, which lies outside the surface of rotation generated by the lower console SA with jets. The upper end of the exhaust inlet pipe or outlet pipe of the ACT is covered by a splash-proof casing SH. The splash cover SH covers the discharge port ACT like a cap or fungus. This casing (when viewed from above; see Fig.12) from the top side is completely closed, in particular, it is completely closed even with the bottom side in the area facing the SA console with jets. In this embodiment, the spray hood SH is, in first approximation, the shape of a semicircular cylinder. In Fig.12 presents a schematic top view of the spray casing SH. On the upper side of the casing in the transition regions GF, URA between maximally flat upper side of the casing and descending essentially vertically down side (if looking from the inside out) are convex flattening GF (see Fig.13). When a jet, for example, from the console SA nozzles hits such flattened or convex surface edge of the transition region GF, URA, it is most fully wraps around in the form of a film splashproof casing SH and cools it during the desorption process.

In order to prevent fluid when spraying through the bottom of the console SA to the nozzle through the outlet vent ACT of sorbtion the th camera SB, the lower edge region UR side spray SH casing having the form of a fragment of a circular cylinder, creased or bent inward in the direction of the vent ACT. This is well illustrated in Fig.13. In addition, in the area of the upper edge around the perimeter of the vent ACT provided radially protruding outward deflecting the spray item or screen item PB, in particular reflector. This element is radially outward in the intermediate space or gap between the outlet of the ACT in the form of a circular cylinder and the inner wall of the spray casing SH. Thus between the outer edge of this shielding element PB and the inner wall of the spray casing SH remains free through hole for air flow coming out from the exhaust pipe ACT in the direction of the splash cover shell SH and is deflected by it down to the bottom edge of UR spray casing SH, in particular, by approximately 180°. The path deviation is indicated in Fig.13 as ALS. In the embodiment according to Fig.13 shielding element PB, speaker output, built in certain points of the perimeter of the outside edge of the jumpers SET, which rely on the internal side of the side wall of the spray casing SH, having the form of a segment of a circle. The splash cover SH location is n at some height above the outlet of the ACT, forming a free space or cavity.

In Fig.14 illustrates a bottom view of the spray casing SH and the discharge port ACT. This shielding element PB screens outlet vent ACT essentially in a circle in the form of protruding side edges or jumpers. In particular, the shielding element PB closes the lower side of the spray casing SH in the area of rectilinear side wall facing the SA console with jets. Only in the zone of the spray casing SH (which is curved in a semicircle between the shielding element PB and radially offset from him, outer concentric side wall of the spray casing SH left the gap LAO, through which the air from the exhaust pipe of the ACT may enter into the interior of the washing chamber SPB. In this embodiment (see Fig.14) gap LAO has essentially the shape of a sickle. Thanks to this thread LS2 air force is directed along the path ALS deviations. That is, the air vertically upwards in the direction of release, is deflected down, where he can only go through the Crescent-shaped gap LAO (having the form of a segment of a circle) in the lower part of the spray casing SH. Expediently, an outlet ACT is above the bottom of the BO at such a height HO, which enables its upper edge to be you who e filling level of the washing chamber, provided for the washing process, or above the level of the resulting foam.

The final element AUS, located at the outlet of the sorption camera SB and protruding into the interior of the washing chamber SPB, expediently designed in such a way that coming out of the flow LS2 air was directed away from the console SA with jets. In particular, the output stream LS2 air is deflected in the back or located at the rear of the corner region between the rear wall RW and the adjacent side wall SW of the washing chamber. Thus, to the extent possible, prevents water spray or foam during the process of cleaning or another cleaning process through the hole in the exhaust pipe to the inside of the sorption chamber. This hit could break or even negate the desorption process. In addition, the washing liquid could seriously damage the sorption material. Numerous tests have shown that the functionality of the sorption material in the sorption chamber can be maximally preserved during the lifetime of the dishwasher, if it is reliably exclude the ingress of water, detergents and/or air conditioner in the washing liquid on the sorption material.

Summarizing the above, at least one outlet AUS, which is connected, at least about what it bleed hole AO sorption camera SB, located within the wash chamber SPB thus to exhaust the air out of it LS2 was sent to the maximum in the direction of at least one spray device SA, located in the washing chamber SPB. When this outlet AUS is located outside the working area of the spraying device SA. The spray device may represent, for example, rotating the SA console with jets. Preferably, the discharge device AUS is located in the rear corner region EBR between the rear wall RW and the adjacent side wall SW of the washing chamber SPB. In particular, the discharge device includes AUS outlet AVO located above the bottom of the BO of the washing chamber SPB on the height BUT greater than the level of the washing chamber, provided for the washing process. The exhaust device includes AUS discharge port ACT and the splash cover SH. Spray hood SH is designed to cover the outlet of the air cooler vent ACT. The splash cover SH covers the discharge port ACT so that the air rising through the discharge port ACT of sorption camera SB in an upward direction after exiting the outlet of the air cooler vent ACT could force it to deviate downwards, passing ALS. The discharge port ACT, the speaker up nadem BO of the washing chamber SPB, connected with the connecting pipe STE on the cover DEL sorption camera SB, located under the bottom of the BO. Spray hood SH is closed with the upper and lower sides in the field GF of his corps, addressed to the spray device SA. The splash cover SH covers the outlet of the air cooler vent ACT with the formation of free space at the top. While the discharge port ACT has an upper, convex outward edge or annular flange KR. The splash cover SH covers the upper extremity of the exhaust pipe ACT so that between its inner surface and the outer surface of the exhaust pipe, the ACT remained clearance SPF. The gap between SPF spray casing SH and the outlet of the ACT is thus to ensure the path ALS air outlet of the exhaust pipe ACT directed away from the spray device SA in the washing chamber SPB. On the exhaust pipe of the ACT provides an element PB, deflecting the spray and projecting into the gap SPF. The lower edge region UR spray casing SH curves inward. The outer surface of the spray casing SH rounded so that falling on her jet from the spray device SA could be spread as a film on the surface.

In Fig.15 shows a schematic longitudinal section of the disorder commit end end EM duct LK on inlet side in the region of the outlet opening ALA in the side wall SW of the washing chamber SPB (see Fig.2).

End end EM duct LK is inside the washing chamber of the steam so formed annular flange, protruding at right angles from the side wall SW. This collar has an internal thread SG. In this internal thread SG is screwed an annular inlet element IM with external thread. He also serves as a fixation element for holding the extremity of EM. This annular retainer element contains a toroidal, annular receiving chamber for the sealing element DI2. Such a sealing element DI2 seals the annular gap between the outer edge of the end tip of the ET of the duct LK on inlet side and the locking element. In this embodiment, the locking element is, in particular, the threaded ring in the form of a cap nut, which is screwed to the end tip of the ET of the duct LK on inlet side. In this embodiment, the annular retainer element IM is the average lumen MD, through which the inner space of the washing chamber SPB can be absorbed air LU.

If necessary, it may be desirable option, in which the input hole MD inlet section of the ET tube duct LK or before they are provided, at least one protective element in the form of ribs, between the plates RIP there with the vozny passages for the escape of air from the washing chamber. In Fig.15 these plates RIP shown by the dotted line.

In Fig.16 presents a schematic horizontal projection of the bottom structural node BG. In addition to the fan unit LT, sorption camera SB, circulation pump UWP, etc. it includes the main controller is NOT intended for control of these elements and their control. In addition, the heating device HZ sorption camera SB during the desorption process is controlled using at least one controller. In this embodiment, this function performs additional controller ZE. He is used to having rasmijoti or close the supply line SZL heating device HZ. Additional controller ZE is controlled by the main controller HE bus BUL. Supply line SVL leads from the primary controller to the secondary controller ZE. This controller also controls the fan unit LT through the control wire SLL. In the control wire SLL can, in particular, to build and supply wire of the fan unit LT.

To the main controller through the signal wires are connected, at least one temperature sensor TSE (see Fig.2), which delivers corresponding signals to measure the temperature in the inner space of the washing chamber to the main controller. The temperature sensor is to TSE hung between the ribs VR stiffness (see Fig.3) in the intermediate space between the two arms of the intake area RA1 pipe duct LK. He is in contact with the side wall SW of the washing chamber SPB.

If now will start the cleaning process, the main controller does NOT simultaneously include bus BUL additional controller ZE so that voltage was supplied by a power supply wire SZL to terminals AP1, AR heating device HZ. Once in the inner space of the washing chamber SPB reaches some specified critical upper limit on the temperature that can be determined by the base controller is NOT on the measurement signals of the temperature sensor, it can provide additional controller ZE bus BUL instructed to remove the voltage from the power wiring SZL, thereby completely disable the heating device HZ. Thus, it can be reliably completed, for example, the process of desorption of the sorption material in the sorption chamber.

If necessary, it may be desirable option in which the user of the dishwasher will be able to enable or disable system TS sorption drying by enabling or disabling specially designed software button or corresponding menu item is selected in the software menu. In Fig.16 this function is schematically shown in the de program buttons or PG1 software menu transmitting the control wire SL1 to the control logic device does NOT control the control signals SS1 corresponding to the signals enable and disable system TS sorption drying.

In particular, on the control panel of the dishwasher can be provided by the first selection button "power" or "Sorption" mode. This program is set to save energy. This effect is achieved due to the fact that when performing the process of final rinse heat flow heater is not performed, and drying is subjected to washing items, in particular dishes, is performed exclusively by means of the TS sorption drying.

In particular, if necessary, it may be desirable option, in which in addition to clean sorption drying the inner space of the washing chamber is heated during the final rinse through the heated washing liquid. While beneficial, may not be sufficient if the heat transfer on susidies items due process final rinse will occur with less energy compared to the variant without the sorption drying. The reason is that now used the system sorption drying saves electrical energy, spent the and heat due to the absorption of moisture from the air. Thus, it is possible to provide so-called "drying your own warm and sorption drying, that is, to improve drying wet or damp subjected to washing items by combining or additions of both types of drying.

In addition to the button "power" or independently of it on the control panel of the dishwasher can be provided for an additional button "Power drying, which increases the time an air blower fan unit. This makes it possible to improve the drying of all elements of the dish.

In addition to the above special buttons or independently of them may be provided an additional button "program". If enabled, the system of the sorption drying time may be reduced compared to conventional drying systems (without sorption drying). If necessary, you can further reduce the number of cleaning due to the additional heat during the cleanup phase and, optionally, by increasing the injection pressure by increasing the engine speed of the circulation pump. In addition, it is possible to further reduce the drying time by increasing the temperature of the final rinse.

In addition to the previous special buttons or independent who may be provided a button with the function "Change performance cleaning". When pressing this button, you can increase the performance of cleaning, preserving the duration of phase without increasing the power consumption compared with a dishwasher without a sorption drying. Due to the fact that simultaneously with the cleaning process starts the desorption process, and the fact that hot air that contains derived from the sorption material water enters the washing chamber, it is possible to save energy expended on heating the required amount of liquid into the wash chamber.

1. Dishwasher (GS), in particular a household dishwasher, containing at least one of the washing chamber (SPB) and at least one system (TS) sorption drying for drying is subjected to washing items, the system (TS) sorption drying contains at least one adsorption chamber (SB) with reversal daydreamy sorption material ZEO), which is connected to the washing chamber (SPB), at least one duct (LK) for thread creation (LS1) of air, characterized in that that sorption material ZEO) is located in the sorption chamber (SB) in the form of the sorption element (SE) so that, essentially, through every point of the surface (SDF) passing the sorption element (SE) were essentially the same volume of air, and one or more items (SK) conditioning flow is established in blonay camera (SB) and/or in the intake area (VA, ES) pipe duct (LK) to ensure alignment of local profile flow (LS2) of air that passes through the adsorption chamber (SB) in the direction (DSR) of its passing a stream of air.

2. Dishwasher under item 1, characterized in that the sorption drying material ZEO) is provided containing aluminum oxide and/or silicon reversal daydreamy material, silica and/or zeolite, in particular zeolite types A, X, Y, individually or in any combination.

3. Dishwasher under item 1, characterized in that the sorption material ZEO) is provided in the sorption chamber (SB) in the form of dumping in the form of granular solids or granules with lots of grains, essentially, from 1 to 6 mm, in particular from 2.4 to 4.8 mm, and the height (H) of the layer of filled grains, at least 5 times the grain size.

4. Dishwasher under item 1, characterized in that the sorption material ZEO), present in the form of granular solids or granules, is provided in the sorption chamber (SB) in the form of a layer, the height (H) which, in the direction of the gravity vector, essentially, 5-40 times, especially in 10-15 times the size of the grains of the granular solids or granules.

5. Dishwasher under item 3 or 4, characterized in that the height (H) covered sorption layer m is material (ZEO) is essentially, from 1.5 cm to 25 cm, in particular from 2 cm to 8 cm, preferably from 4 cm to 6 cm

6. Dishwasher under item 3, wherein the granular solid material or granulate consists of a set of essentially spherical particles.

7. Dishwasher under item 3 or 4, characterized in that the sorption material ZEO), made in the form of granular solids or granules, is the average density of the backfill at least 500 kg/m³in particular, in essence, from 500 to 800 kg/m³in particular from 600 to 700 kg/m³especially from 630 to 650 kg/m³especially preferably approximately 640 kg/m³.

8. Dishwasher under item 1, wherein the weight amount of the reversal negidrirovannogo sorption material ZEO) in the sorption chamber (SB), designed to absorb moisture, which has a thread (LS1) of air is selected so that the amount of liquid absorbed sorption material ZEO) was less than the amount submitted on the cleaned items, in particular, at the stage of final rinse.

9. Dishwasher under item 1, characterized in that the sorption chamber (SB) is the weight amount of the reversal negidrirovannogo sorption material, which is sufficient to absorb moisture, corresponding essentially about what he liquid, which remains to be washing the items upon completion of the final rinse.

10. Dishwasher under item 8 or 9, characterized in that the amount of absorbed water is preferably from 4 to 25%, particularly from 5 to 15% of the volume of fluid filed on the cleaned items.

11. Dishwasher under item 8 or 9, characterized in that the sorption chamber (SB) placed the weight amount of the sorption material ZEO) comprising, essentially, from 0.2 to 5 kg, in particular from 0.3 to 3 kg, preferably from 0.5 to 2.5 kg

12. Dishwasher under item 1, characterized in that the sorption material ZEO) contains pores having a size essentially of from 1 to 12 angstroms, in particular from 2 to 10 angstroms, preferably from 3 to 8 angstroms.

13. Dishwasher according to one of paragraphs.1-4, 8, 9, characterized in that the water absorbing capacity of the sorption material ZEO) is, essentially, from 15 to 40, preferably from 20 to 30 weight percent of its dry mass.

14. Dishwasher according to one of paragraphs.1-4, 8, 9, characterized in that the desorption of the sorption material ZEO) is possible at a temperature essentially of from 80° to 450°C., in particular from 220° to 250°C.

15. Dishwasher under item 1, characterized in that the duct (LK), sorption camera (SB) and/or one or more additional elements (LT, SK), towards the shining stream, designed in such a way that through the sorption material ZEO) for the sorption and/or desorption could pass flow (LS2) air speeds, essentially, from 2 to 15 l/s, in particular from 4 to 7 l/C.

16. Dishwasher under item 1, wherein the sorption material (ZEO) is attached, at least one heating device (HZ), which can provide equivalent heating capacity from 250 to 2500 W, in particular from 1000 to 1800 watts, preferably from 1200 to 1500 watts to heat the sorption material ZEO) in order desorption.

17. Dishwasher under item 16, characterized in that the ratio of the heating power of the at least one heating device (HZ) attached to the sorption material (ZEO) for desorption and flow rate (LS2) of the air passing through the sorption material is selected in the range from 100 to 1250 W·s/l, in particular from 100 to 450 W·s/l, preferably from 200 to 230 W·s/l

18. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, characterized in that the sorption chamber (SB for the sorption material ZEO) is provided by the surface of the passage, the area of which amounts to, essentially, from 80 to 800 cm²in particular from 150 to 500 cm².

19. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, characterized in that the height (H) covered sorption layer is of material (ZEO) above the surface (SDF) occurrence of the adsorption element (SE) sorption chambers (SB) is essentially constant.

20. Dishwasher under item 1, characterized in that the sorption chamber (SB) is located in the bottom constructive node (BG) under the bottom (BO) of the washing chamber (SPB).

21. Dishwasher under item 1, characterized in that the duct (LK) is largely located outside the washing chamber (SPB).

22. Dishwasher under item 1, characterized in that before the sorption chamber (SB) (in flow direction) in the intake area (RA1) pipe duct (LK) has at least one fan unit (LT), designed to create a forced flow (LS1) of air in the direction of the at least one inlet (SW) sorption chambers (SB).

23. Dishwasher under item 22, wherein the fan unit (LT) is located in the bottom constructive node (BG) under the washing chamber (SPB).

24. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the duct (LK) is connected to the sorption chamber (SB) so that the thread (LS1) of the air included in a region (near the bottom) sorption chambers (SB) in the direction (ESR) occurrence and deflected in a different direction (DSR) flow in which it passes through the inner space of the sorption chambers (SB).

25. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the inlet area (RA1) of the pipe in which duhovogo (LK) is included in the sorption chamber (SB) to the direction (ESR) of its occurrences passed in the direction (DSR) passing a stream of sorption chambers (SB) at an angle, in particular, about 90°.

26. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the surface area (SDF) passing through the sorption material ZEO) inside sorption chambers (SB) is greater than the surface area of the passage inlet pipe (ES) of the duct (LK), which enters the inlet (SW) sorption chambers (SB).

27. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the surface (SDF) passing the sorption chambers (SB) 2-40 times, especially in 4-30 times, preferably 5-25 times more surface passing the end of an inlet pipe (ES) of the duct (LK), which enters the inlet (SW) sorption chambers (SB).

28. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that at least one adsorption element (SE) with sorption material ZEO) is located in the sorption chamber (SB) so that the sorption material ZEO) was flushed in the direction that substantially coincides with the gravity vector, or oppositely, air (LS1, LS2), which is served by the duct (LK) from the washing chamber (SPB) in the sorption chamber (SB).

29. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that Sorbs the organizational element (SE) contains, at least one lower sieve or grid (US) and at least one upper strainer or grating (OS), located at specified distance (M) height from each other, and that the spatial volume between the two sieves or grids (US, OS) are largely filled with the sorption material ZEO).

30. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the sorption chamber (SB) in the direction opposite to the gravity vector, contains at least one layered structure consisting of a heating device (HZ), followed by an intermediate space (ZR) followed by a sorption element (SE).

31. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, characterized in that the sorption chamber (SB) located in front of her sorption element (SE) in the direction (DSR) flow is at least one heating device (HZ).

32. Dishwasher under item 1, characterized in that at the bottom, near the bottom of the cavity (UH) sorption chambers (SB) is at least one heating device (HZ).

33. Dishwasher according to one of paragraphs.1-4, 8, 9, 12, 15, 21, 22, wherein the sorption material in the sorption compartment (SB) is able to absorb water volume, essentially, from 150 to 400 ml, in particular from 200 to 300 ml.