EP1651093B1 - Procede permettant de faire fonctionner un lave-vaisselle et comportant au moins une etape sechage de programme - Google Patents

Procede permettant de faire fonctionner un lave-vaisselle et comportant au moins une etape sechage de programme Download PDF

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Publication number
EP1651093B1
EP1651093B1 EP04763100.7A EP04763100A EP1651093B1 EP 1651093 B1 EP1651093 B1 EP 1651093B1 EP 04763100 A EP04763100 A EP 04763100A EP 1651093 B1 EP1651093 B1 EP 1651093B1
Authority
EP
European Patent Office
Prior art keywords
air
heated
program step
drying
sorption column
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP04763100.7A
Other languages
German (de)
English (en)
Other versions
EP1651093A1 (fr
Inventor
Helmut Jerg
Kai Paintner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BSH Hausgeraete GmbH
Original Assignee
BSH Hausgeraete GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from DE10353775A external-priority patent/DE10353775A1/de
Application filed by BSH Hausgeraete GmbH filed Critical BSH Hausgeraete GmbH
Priority to EP16169510.1A priority Critical patent/EP3085292A1/fr
Publication of EP1651093A1 publication Critical patent/EP1651093A1/fr
Application granted granted Critical
Publication of EP1651093B1 publication Critical patent/EP1651093B1/fr
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Classifications

    • A—HUMAN NECESSITIES
    • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L15/00—Washing or rinsing machines for crockery or tableware
    • A47L15/42—Details
    • A47L15/48—Drying arrangements
    • A47L15/481—Drying arrangements by using water absorbent materials, e.g. Zeolith
    • A—HUMAN NECESSITIES
    • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L15/00—Washing or rinsing machines for crockery or tableware
    • A47L15/0018—Controlling processes, i.e. processes to control the operation of the machine characterised by the purpose or target of the control
    • A47L15/0021—Regulation of operational steps within the washing processes, e.g. optimisation or improvement of operational steps depending from the detergent nature or from the condition of the crockery
    • A47L15/0042—Desorption phases of reversibly dehydrogenated drying material, e.g. zeolite in a sorption drying system
    • 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
    • A47L15/0018—Controlling processes, i.e. processes to control the operation of the machine characterised by the purpose or target of the control
    • A47L15/0047—Energy or water consumption, e.g. by saving energy or water
    • 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
    • A47L2501/00—Output in controlling method of washing or rinsing machines for crockery or tableware, i.e. quantities or components controlled, or actions performed by the controlling device executing the controlling method
    • A47L2501/10—Air circulation, e.g. air intake or venting arrangements
    • 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
    • A47L2501/00—Output in controlling method of washing or rinsing machines for crockery or tableware, i.e. quantities or components controlled, or actions performed by the controlling device executing the controlling method
    • A47L2501/34—Change machine operation from normal operational mode into special mode, e.g. service mode, resin regeneration mode, sterilizing mode, steam mode, odour eliminating mode or special cleaning mode to clean the hydraulic circuit

Definitions

  • the invention relates to a method for operating a dishwasher with at least one partial program step "drying".
  • drying for example, items to be washed in a dishwasher
  • different methods are known.
  • the items to be washed can be dried by self-heat drying if the rinsing liquid is heated in a rinse-out subprogram step and the hot, rinsed items are automatically dried by the self-heat of the item to be washed during the drying process.
  • the rinsing liquid is heated in the subprogram step "rinse", for example, in a heat exchanger to a certain temperature and applied to the items to be washed via spraying.
  • rinsing usually from 65 ° C to 75 ° C is achieved that a sufficiently large amount of heat is transferred to the items to be washed, so that the water adhering to the items by the heat stored in the items to be washed evaporated.
  • a separate heat source e.g. a hot air blower, used to heat the humid air mixture during the drying process, so that the air in the rinse tank can absorb a larger amount of water.
  • 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 heat energy for each heating phase must be recreated by means of the electrical heating elements.
  • the known heating systems have the disadvantage that the heating of the rinsing liquid in the partial program step “rinse" and the operations in the sub-program step “drying" are themselves associated with a high energy demand and the required heat energy is lost after the drying process.
  • the laundry treatment and flushing device of DE 36 26 887 A1 has an air guidance system with air guidance control means, in which a container filled with adsorptive desiccant container is alternately connected to a process air to be dehumidified and a regeneration air flow.
  • a regeneration phase relatively dry ambient air is conducted from outside via an air guide channel by means of a blower into the container filled with desiccant.
  • heat is supplied to the desiccant for regeneration by a heater in the air duct over which the ambient air is sucked by means of the blower.
  • After flowing through the adsorptive drying agent from this moisture absorbing and thus moist regeneration air is discharged through an exhaust duct to the outside.
  • a hollow cylinder is arranged as a drying container, which is filled with a moisture adsorbing desiccant and is in thermal contact with the water heater.
  • the input-side connection of the drying container is connected via an air duct with a cover-side outlet of the washing.
  • a blower is inserted.
  • About its output-side connection of the drying container is connected to a mouth opening in the purge outlet.
  • the air duct is provided with a closure that interrupts the air circulation during rinsing.
  • the highly moisture-containing air is pressed during a drying process from the washing container by means of the now switched on fan in the drying vessel.
  • the desiccant stored in the drying vessel absorbs the moisture from the air flowing through the drying vessel, and the thus dried air is blown into the purge vessel via the outlet side port of the drying vessel and the exhaust port.
  • the object of the present invention is to provide a method with which it is possible to operate a dishwasher as economically as possible, to dry it efficiently in its material to be dried and to keep the associated energy expenditure as low as possible.
  • the air is heated by heat of condensation during the passage of the sorption column and, if necessary, additionally heated by a heater.
  • air is passed from the treatment space through the sorption column and into the treatment space and heated during the passage.
  • the reversibly dehydratable material for desorption is heated to very high temperatures, for which heat energy is necessary.
  • the stored occurs Liquid as hot steam.
  • the water vapor is preferably passed with an air flow in the treatment room of the device and thus the air in the treatment room is heated and thereby the treatment liquid, for. B. the rinsing liquor and / or the good to be cleaned, z. B. heated the dishes with.
  • the air passed through cools down, as a result of which the water vapor contained in it completely or partially condenses. This is preferably done as a closed air circuit.
  • the introduction of the hot water vapor and the heated air into the treatment chamber during a partial program step with the treatment liquid to be heated or possibly already heated is largely sufficient to sufficiently heat the treatment liquid.
  • the passage of the air is carried out during a program step with the treatment liquid to be heated.
  • air is passed through the sorbent column and heated and the air is passed through a heat storage for cooling and subsequently air for heating through the heat storage and into the treatment chamber, to temporarily store the heat used for desorption in the heat storage ,
  • the sorption column or the air in a line to the sorption column is heated by a heater for desorption.
  • the treatment liquid and / or the material to be treated is heated by the heated air passed through and the desorbed moisture is at least partially released from the sorption column in the treatment space.
  • the inventive method for operating a device with at least one partial program step "drying” is performed in the illustrated embodiment in a dishwasher.
  • a dishwasher is known to have a rinsing process whose program sequence generally consists of at least one partial program step "pre-rinsing", one sub-program step “cleaning”, at least one sub-program step “intermediate rinsing", one sub-program step "rinsing” and one sub-program step “drying”.
  • air is passed from a treatment space through a sorption column and then preferably back into the treatment space.
  • the treatment space of the dishwasher for this purpose-the washing container- is equipped with an outlet in the upper region of the washing container. From this outlet, an air line leads to a fan and from the fan to the sorption column.
  • This sorption column contains reversibly dehydratable material which extracts moisture from the air during the passage and is known to be heated and thus also heats the air which has passed through it. In addition to this warming effect, it is also possible to heat the air additionally with a heater.
  • a further air line leads from the sorption column to an inlet located in the lower region of the washing container.
  • the heated air introduced into the purge bin is completely dry and has high moisture absorption capacity. It rises in the washing up and takes up the residual moisture on the material to be treated - the items to be washed. It is now, as already described above, fed back to the sorption column.
  • reversibly dehydratable material preferably does not require heating of the material to be treated, e.g. for dishwashers in the partial program step "rinsing". This means a significant energy saving.
  • heating the air By heating the air, its moisture absorption capacity is increased with each passing through the sorption column, which leads to the improvement of the drying result and to the shortening of the drying time.
  • an exchange of polluted air from the environment is completely excluded, whereby a scrubanschmutzung the treated material is prevented.
  • the reversibly dehydratable material is known to have a limited fluid holding capacity. To make it reusable, a desorption is necessary in which the reversibly dehydratable material is heated to a high temperature and the liquid then emerges as vapor.
  • the desorption of the reversibly dehydratable material is preferably carried out during a partial program step with treatment liquid to be heated.
  • the desorption of the reversibly dehydratable material is carried out during a partial program step "cleaning" and / or "pre-rinsing", in which the items to be washed are treated with heated treatment liquid - rinsing liquor - in a dishwasher by means of spraying devices.
  • a z. B. operated in the sorption column heating, which heats the reversibly dehydratable material to a high temperature.
  • air is sucked out of the washing container during a partial program step "cleaning" by means of the above-mentioned fan and forced through the sorption column.
  • the hot steam emerging from the sorption column and the now heated air enter the rinsing tank through the inlet already mentioned above and there they encounter the circulated rinsing liquor and / or crockery which is thereby heated.
  • the introduction of the hot water vapor and the heated air into the treatment chamber during a partial program step with the treatment liquid to be heated or possibly already heated is largely sufficient to adequately heat the treatment liquid and / or the dishes. This can largely account for a further heating and the energy used for desorption can be almost completely used for heating the treatment liquid (rinsing liquor) and / or the dishes except for the low energy required to overcome the binding forces between water and reversibly dehydratable material , Furthermore, an efficient cleaning of the material to be treated is guaranteed in addition to the energy savings.
  • the desorption of the reversibly dehydratable material is not carried out during a partial program step with treatment liquid to be heated, but at any other time by the energy released during the desorption energy in a heat storage, eg. B. with a liquefied at high heat of fusion medium or a latent storage, is cached, and will give as needed to be heated to a treatment liquid and / or the dishes.
  • a heat storage eg. B. with a liquefied at high heat of fusion medium or a latent storage
  • the sorption column is - as already described - preferably during a partial program step with the treatment liquid to be heated with a heater a very high temperature, z. B. 300 ° C, heated, so that the sorbent gives off the absorbed water.
  • the Sorptonskolonne heated to high temperatures eg. B. 150 ° -200 ° C, by the heat of condensation of water vapor or moisture.
  • the introduced into the washing dry air or the air with steam can reach temperatures that cause damage to the dishes, eg. B. plastic parts, can lead.
  • the air inlet temperature in the washing compartment must therefore be lowered so far in a further embodiment with a cooling that no damage occurs.
  • this residual water is passed on or around the inlet opening and thereby cooled the air flow.
  • the dry and warm air absorbs part of the water, which leads due to the evaporative cooling to cool the air flow.
  • a heat exchange takes place through the spray water and the air flow with water vapor at the inlet opening.
  • the inlet opening is applied to the effect that the air flow does not hit directly on the dishes and a sufficient cooling of the air flow through the spray water takes place.
  • the heating for heating the sorption column for desorption - hereinafter called Heilheizug - has a dishwasher according to the invention in an embodiment not shown via a water heater for the rinsing liquor, if not omitted on the basis of the present invention thereto.
  • a heating is necessary, this can be achieved either with the known from the prior art water heater or with the air heater with the fan on.
  • the advantage of heating with the air heating is that in the subsequent part program step "drying" the heat energy stored in the sorption column can be used for drying.
  • the fan are turned on - with switched off air heating.
  • a method is provided with which it is possible to operate devices of the type mentioned as economically as possible, to efficiently dry the material to be dried and to keep the associated energy consumption as low as possible.

Claims (4)

  1. Procédé d'exploitation d'un lave-vaisselle avec au moins une étape de programme partielle « séchage », de l'air étant dirigé au départ d'un espace de traitement à travers une colonne de sorption avant de revenir dans l'espace de traitement dans l'au moins une étape de programme partielle « séchage », dans lequel la colonne de sorption contient un matériau à déshydrogénation réversible et qui prélève l'humidité de l'air durant le passage, la colonne de sorption ou l'air situé dans un conduit menant à la colonne de sorption étant chauffé(e) par un chauffage pour la désorption du matériau à déshydrogénation réversible, caractérisé en ce que pour la désorption du matériau à déshydrogénation réversible de l'air est dirigé au départ de l'espace de traitement à travers la colonne de sorption avant de revenir dans l'espace de traitement et est chauffé durant le passage, et en ce que le passage de l'air durant une étape de programme s'opère avec du fluide de traitement à chauffer.
  2. Procédé selon la revendication 1, caractérisé en ce que l'air chauffé dirigé chauffe le fluide de traitement et/ou la vaisselle à traiter et l'humidité désorbé de la colonne de sorption est au moins partiellement versée dans l'espace de traitement.
  3. Procédé selon l'une des revendications 1 ou 2, caractérisé en ce que dans une étape de programme partielle avec du fluide de traitement à chauffer, p. ex. « rinçage », de l'air est dirigé au départ de l'espace de traitement à travers la colonne de sorption avant de revenir dans l'espace de traitement chauffage éteint, l'air se chauffant par la chaleur de condensation dans la colonne de sorption.
  4. Procédé selon l'une des revendications 1 à 3, caractérisé en ce que la désorption du matériau à déshydrogénation réversible s'opère durant une étape de programme partielle « lavage » et/ou « prélavage ».
EP04763100.7A 2003-07-30 2004-07-05 Procede permettant de faire fonctionner un lave-vaisselle et comportant au moins une etape sechage de programme Active EP1651093B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP16169510.1A EP3085292A1 (fr) 2003-07-30 2004-07-05 Procédé de fonctionnement d'un lave-vaisselle ayant au moins une étape de programme partiel

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10334791 2003-07-30
DE10353775A DE10353775A1 (de) 2003-07-30 2003-11-18 Verfahren zur Betreiben eines Gerätes mit wenigstens einem Teilprogrammschritt "Trocknen"
PCT/EP2004/007338 WO2005018410A1 (fr) 2003-07-30 2004-07-05 Procede permettant de faire fonctionner un appareil et comportant au moins une etape «sechage » de programme

Related Child Applications (2)

Application Number Title Priority Date Filing Date
EP16169510.1A Division-Into EP3085292A1 (fr) 2003-07-30 2004-07-05 Procédé de fonctionnement d'un lave-vaisselle ayant au moins une étape de programme partiel
EP16169510.1A Division EP3085292A1 (fr) 2003-07-30 2004-07-05 Procédé de fonctionnement d'un lave-vaisselle ayant au moins une étape de programme partiel

Publications (2)

Publication Number Publication Date
EP1651093A1 EP1651093A1 (fr) 2006-05-03
EP1651093B1 true EP1651093B1 (fr) 2016-09-07

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EP04763100.7A Active EP1651093B1 (fr) 2003-07-30 2004-07-05 Procede permettant de faire fonctionner un lave-vaisselle et comportant au moins une etape sechage de programme

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US (1) US8601716B2 (fr)
EP (1) EP1651093B1 (fr)
JP (1) JP2007533940A (fr)
WO (1) WO2005018410A1 (fr)

Families Citing this family (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8601716B2 (en) * 2003-07-30 2013-12-10 Bsh Bosch Und Siemens Hausgeraete Gmbh Method for operating a device with at least one partial programme step of drying
DE102005004095A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine
DE102005004096A1 (de) 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung
DE102005004092A1 (de) 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung und Verfahren zum Betreiben derselben
DE102005004089A1 (de) 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung und Verfahren zum Betreiben derselben
ES2279675B1 (es) * 2005-03-23 2008-08-01 Ibai, S. Coop. Armario de desarrugado y secado de ropa.
US7958651B2 (en) * 2006-05-19 2011-06-14 Maniha Allan M Clothes dryer rake
US8186075B2 (en) * 2006-05-31 2012-05-29 Joel Beckett Forced air flow electric shoe dryer
EP2323531B1 (fr) * 2008-07-28 2014-11-26 BSH Bosch und Siemens Hausgeräte GmbH Lave-vaisselle à système de séchage par sorption
RU2506881C2 (ru) * 2008-07-28 2014-02-20 Бсх Бош Унд Сименс Хаусгерете Гмбх Способ эксплуатации посудомоечной машины
DE102008040770A1 (de) * 2008-07-28 2010-02-04 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zum Betreiben eines wasserführenden Haushaltsgerät
DE102008039896A1 (de) * 2008-08-27 2010-03-04 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit Sorptionstrockenvorrichtung
US9610003B2 (en) * 2008-08-27 2017-04-04 BSH Hausgeräte GmbH Domestic dishwasher with a sorption drying device and corresponding method
DE102008039894A1 (de) 2008-08-27 2010-03-04 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit Sorptionstrockenvorrichtung
DE102008039895A1 (de) * 2008-08-27 2010-03-04 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit Sorptionstrockenvorrichtung
DE102008039889A1 (de) * 2008-08-27 2010-03-04 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit Sorptionstrockenvorrichtung
DE102010023327A1 (de) * 2010-06-10 2011-12-15 Süd-Chemie AG Trocknungsvorrichtung enthaltend ein Alumo-Phosphat
DE102010041215A1 (de) * 2010-09-22 2012-03-22 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine, insbesondere Haushaltsgeschirrspülmaschine
KR102034096B1 (ko) * 2013-09-02 2019-10-18 삼성전자주식회사 식기세척기
KR102188109B1 (ko) * 2014-05-30 2020-12-07 삼성전자주식회사 식기세척기
EP3086068A1 (fr) * 2015-04-20 2016-10-26 Rhino Research Europe B.V. Système de séchage d'air utilisant des zéolites
US9810480B2 (en) * 2015-06-12 2017-11-07 Targeted Microwave Solutions Inc. Methods and apparatus for electromagnetic processing of phyllosilicate minerals
US9907451B2 (en) * 2016-05-09 2018-03-06 Samsung Electronics Co., Ltd. Dishwasher drying system with thermal storage heat exchanger
KR102350079B1 (ko) * 2017-08-09 2022-01-11 엘지전자 주식회사 의류처리장치

Family Cites Families (147)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2340345A (en) * 1941-05-23 1944-02-01 Sanford E Richeson Coffee roasting machine
US2411039A (en) * 1943-10-12 1946-11-12 Ralph V Heuser Drying apparatus with air desiccating means and automatic regenerating means therefor
US2519873A (en) * 1945-09-24 1950-08-22 Union Oil Co Adsorption process and apparatus
US2549104A (en) * 1946-06-29 1951-04-17 Socony Vacuum Oil Co Inc Method for revivification of desiccants
US2633928A (en) * 1946-09-28 1953-04-07 Chester A Chamberlain Dehumidifying apparatus
US2674338A (en) * 1949-12-02 1954-04-06 Fmc Corp Method and apparatus for the recovery of nitrogen oxides from gaseous mixtures
US2858279A (en) * 1952-09-30 1958-10-28 Exxon Research Engineering Co Method of drying a fluid hydroforming catalyst
US3034221A (en) * 1957-10-11 1962-05-15 Gen Motors Corp Clothes drier having absorbent bed
NL101577C (fr) * 1957-12-31 1900-01-01
US3031381A (en) * 1960-01-29 1962-04-24 Robert L Langerhans Method of drying bacteria
DE1191299B (de) * 1960-07-23 1965-04-15 Glanzstoff Ag Verfahren zur kontinuierlichen Trocknung von Schnitzelgut aus organischen Hochpolymeren
NL279568A (fr) * 1961-06-13
US3342629A (en) * 1963-10-24 1967-09-19 Callery Chemical Co Wood treating process and product thereof
US3304623A (en) * 1964-07-13 1967-02-21 Realistic Company Hair dryer
CH457283A (de) * 1965-09-13 1968-05-31 Progress Ag Verfahren zur Herstellung von schnellstlöslichen Trockenprodukten
US3387385A (en) * 1965-10-22 1968-06-11 Whirlpool Co Nozzle for liquid extraction apparatus
US3374052A (en) * 1965-12-20 1968-03-19 Dept Of Chemical Engineering System for solid particles-fluid contact operations
US3417481A (en) * 1966-06-16 1968-12-24 Joseph F. Rumsey Jr. Attachment for dryers or the like
US3666621A (en) * 1968-02-16 1972-05-30 Industrial Nucleonics Corp Process and apparatus for moisture and fiber content control in a papermaking machine
US3507051A (en) * 1968-02-26 1970-04-21 Willard R Calvert Regeneration process
US3458941A (en) * 1968-03-13 1969-08-05 Pillsbury Co Freeze drying apparatus and process
DE2016831A1 (de) 1970-04-09 1971-10-21 Bosch Hausgeraete Gmbh Geschirrspülmaschine
US3729835A (en) * 1971-06-01 1973-05-01 F Massett Specimen drying apparatus
CH544918A (de) * 1971-11-10 1973-11-30 Ciba Geigy Ag Trocknungsverfahren
DE2251423A1 (de) * 1972-10-20 1974-05-02 Kernforschungsanlage Juelich Verfahren und sorptionskolonne zum wiederaufarbeiten von in einer sauren loesung enthaltenen brenn- und/oder brutstoffen mit thorium als brutstoff
US4124528A (en) * 1974-10-04 1978-11-07 Arthur D. Little, Inc. Process for regenerating adsorbents with supercritical fluids
DE2509937C3 (de) * 1975-03-07 1981-04-16 Hoechst Ag, 6000 Frankfurt Vorrichtung zur Nachbehandlung von Homo- und Copolymerisaten des Vinylchlorids
US4023940A (en) * 1975-07-02 1977-05-17 Whitlock, Inc. Regeneration cycle control for industrial air dryer
US4112590A (en) * 1975-07-02 1978-09-12 August Lepper, Maschinen- Und Apparatebau Gmbh Combined drum washer and drying arrangement
NL7711292A (nl) * 1976-10-18 1978-04-20 Baltes Hans Werkwijze voor het drogen van wasgoed en droog- kast voor toepassing van deze werkwijze.
US4125946A (en) * 1977-06-14 1978-11-21 Melvin Prager Apparatus for drying clothes using solar energy
DE2806873C3 (de) * 1978-02-17 1981-03-26 Bauknecht Hausgeräte GmbH, 70565 Stuttgart Trommelwasch- und Trockenmaschine
JPS5524543A (en) * 1978-08-11 1980-02-21 Kuri Kagaku Sochi Kk Manufacture of concentrated and dried powder from solution or dispersion
US4248706A (en) * 1978-09-29 1981-02-03 Westvaco Corporation Two stage fluid bed regeneration of spent carbon
US4283204A (en) * 1979-09-07 1981-08-11 Exxon Research & Engineering Co. Process for the separation of contaminants from feed streams using magnetic beds
US4389422A (en) * 1980-04-10 1983-06-21 General Foods Corporation Method for producing aromatized microporous substrates
DE3031446A1 (de) * 1980-08-20 1982-07-22 Mittex AG, 9490 Vaduz Verfahren zum schonenden trocknen waermeempfindlichen gutes, vorrichtung zur durchfuehrung des verfahrens und anlage mit solchen vorrichtungen
US4497121A (en) * 1981-05-04 1985-02-05 Polaroid Corporation Process simulator
US4480393A (en) * 1981-06-15 1984-11-06 Minnesota Mining And Manufacturing Company Vapor recovery method and apparatus
US4513590A (en) * 1983-03-08 1985-04-30 Dual Filtrex, Inc. Combination filter apparatus for use with a dry cleaning machine
US4652278A (en) * 1983-04-12 1987-03-24 Near Equilibrium Research Associates Solids drying
DE3471367D1 (en) * 1983-12-19 1988-06-23 Duphar Int Res Method of drying a solid and device therefor
SE448419B (sv) * 1984-04-19 1987-02-23 Haldex Ab Anordning vid ett torktorn for en trycktorkare
US4622757A (en) * 1984-12-24 1986-11-18 Energy International, Inc. Cogeneration microwave food dryer
DE3511320C1 (de) * 1985-03-28 1986-10-09 Max-Planck-Gesellschaft zur Förderung der Wissenschaften e.V., 3400 Göttingen Vorrichtung zur Reinigung der Gasatmosphaeren mehrerer Arbeitsraeume
DE3512593A1 (de) * 1985-04-06 1985-09-19 Manfred Dr. 2420 Eutin Ehrhardt Geraet zur extraktion loeslicher bestandteile aus festkoerpern mit hilfe von fluessigen loesungsmitteln
SU1573062A1 (ru) * 1986-02-27 1990-06-23 Центральный научно-исследовательский институт бытового обслуживания Способ рекуперации растворителей в машинах химической чистки
US4715965A (en) * 1986-05-19 1987-12-29 Sigerson Adam L Method for separating and recovering volatilizable contaminants from soil
DE3626887A1 (de) * 1986-08-08 1988-02-11 Miele & Cie Waeschebehandlungs- und spuelgeraet, herd o. dgl., mit einer entfeuchtungseinrichtung
US4761162A (en) * 1986-10-09 1988-08-02 Union Oil Company Of California Upgrading and storage of solid carbonaceous fuel
US4756726A (en) * 1986-11-20 1988-07-12 Terry Peace Regenerable dehumidifier
SU1744158A1 (ru) * 1986-12-16 1992-06-30 Центральный научно-исследовательский институт бытового обслуживания Машина дл химической чистки текстильных изделий
DE3710710A1 (de) * 1987-03-31 1988-10-13 Philips Patentverwaltung Kondensations-waeschetrockner
US4765162A (en) * 1987-08-10 1988-08-23 Raymond Ouellette Washer-dryer apparatus
US4805317A (en) * 1987-11-13 1989-02-21 Airflow Company Microwave regeneration of adsorbent materials for reuse as drying agents
DE3741652A1 (de) * 1987-12-09 1989-06-22 Bauknecht Hausgeraete Einrichtung zum trocknen von geschirr
DE3830664A1 (de) 1988-09-09 1990-03-22 Bauknecht Hausgeraete Einrichtung zum trocknen von geschirr in einer haushalt-geschirrspuelmaschine
FR2636607B1 (fr) * 1988-09-22 1991-07-05 Chicot Denis Installation pour le transport et/ou le stockage de produits sensibles aux variations de temperature et d'humidite
DE3837648A1 (de) * 1988-11-05 1990-05-10 Basf Ag Vorrichtung zur auswaschung von photopolymeren druckplatten mittels loesungsmitteln, trocknung der druckplatten und rueckgewinnung der loesungsmittel
US5058401A (en) * 1988-12-22 1991-10-22 Brother Kogyo Kabushiki Kaisha Washing, dehydrating and drying machine
DE3904111A1 (de) * 1989-02-11 1990-08-16 Battelle Institut E V Verfahren und vorrichtung zur umweltfreundlichen massenentsaeuerung von buechern und anderen papiererzeugnissen
US4887438A (en) * 1989-02-27 1989-12-19 Milton Meckler Desiccant assisted air conditioner
FR2648484A1 (fr) * 1989-06-16 1990-12-21 Ciapem Seche-linge a rejet differe de l'humidite
IT221382Z2 (it) * 1989-12-01 1994-03-16 Zanussi A Spa Industrie Dispositivo di condensazione del vapore per macchine asciugabiancheriao macchine combinate per il lavaggio e l'asciugatura della biancheria
US5003143A (en) * 1990-04-09 1991-03-26 Progressive Recovery, Inc. Microwave sludge drying apparatus and method
US5373704A (en) * 1990-04-17 1994-12-20 Arthur D. Little, Inc. Desiccant dehumidifier
JPH04184079A (ja) * 1990-11-14 1992-07-01 Matsushita Electric Ind Co Ltd 乾燥装置
DE4040389C2 (de) * 1990-12-17 1994-03-03 Air Prod Gmbh Verfahren zur Vermeidung oder Verringerung von störfallbedingten Zeitverzögerungen bei der Lösungsmittelrückgewinnung aus Fertigungsprozessen
DE4102969C1 (fr) * 1991-02-01 1992-10-08 Cs Halbleiter- Und Solartechnologie Gmbh, 8000 Muenchen, De
DE4124277A1 (de) * 1991-07-22 1993-01-28 Linde Ag Verfahren zur dekontamination von verunreinigten boeden
US5230167A (en) * 1991-10-30 1993-07-27 Westinghouse Electric Corp. Removal or organics and volatile metals from soils using thermal desorption
US5361514A (en) * 1991-10-30 1994-11-08 Westinghouse Electric Corporation Removal of volatile and semi-volatile contaminants from solids using thermal desorption and gas transport at the solids entrance
US5343632A (en) * 1992-04-10 1994-09-06 Advanced Dryer Systems, Inc. Closed-loop drying process and system
KR0126736Y1 (ko) * 1992-07-09 1998-12-15 강진구 삶는 세탁기의 히터안전장치
JPH06137762A (ja) * 1992-10-26 1994-05-20 Matsushita Electric Works Ltd 乾燥装置
US5656178A (en) * 1993-04-29 1997-08-12 American Color And Chemical Corp. Method for treatment of contaminated materials with superheated steam thermal desorption and recycle
EP0695408B1 (fr) * 1993-05-12 2001-01-10 Valtion Teknillinen Tutkimuskeskus Prodede permettant d'ameliorer la resistance a la moissure et pourriture de produits cellulosiques
JPH10500053A (ja) * 1993-05-26 1998-01-06 エー・ピー・システムス（オーストラリア）プロプライアタリー・リミテッド 空気乾燥浄化システム
DE4340065A1 (de) 1993-11-24 1995-06-01 Bosch Siemens Hausgeraete Verfahren zum Regenerieren eines hygroskopischen Materials in einem Wäschetrockner
US5631685A (en) * 1993-11-30 1997-05-20 Xerox Corporation Apparatus and method for drying ink deposited by ink jet printing
JP3321945B2 (ja) * 1993-12-24 2002-09-09 松下電器産業株式会社 衣類乾燥機
US5526651A (en) * 1994-07-15 1996-06-18 Gas Research Institute Open cycle desiccant cooling systems
US5628122A (en) * 1994-10-05 1997-05-13 Peter And Theordore Spinardi Investments Lint remover for a clothes drying machine
US5479727A (en) * 1994-10-25 1996-01-02 Air Products And Chemicals, Inc. Moisture removal and passivation of surfaces
JP3558304B2 (ja) * 1995-02-22 2004-08-25 シャープ株式会社 食器洗浄機
US5713137A (en) * 1995-05-17 1998-02-03 Fujita; Sanai Apparatus for deodorizing, sterilizing and drying bedding and clothing
NL1000482C2 (nl) * 1995-06-01 1996-12-03 Tno Werkwijze en inrichting voor het verwarmen en koelen van voedingsproduk- ten.
DE69525350T2 (de) 1995-12-09 2002-08-14 Whirlpool Co Verfahren zur Energieeinsparung in Haushaltsgeräten und Gerät mit verbessertem Energiewirkungsgrad
FR2745896B1 (fr) * 1996-03-07 1998-04-24 Armines Procede et installation de sechage d'une masse de matiere fibreuse humide, notamment d'une masse de linge
US5882381A (en) * 1996-03-28 1999-03-16 Modern Equipment Company, Inc. Thermal desorption system
US6112675A (en) * 1996-04-08 2000-09-05 Foster Wheeler Environmental Corporation Process and apparatus for treating process streams from a system for separating constituents from contaminated material
US5832750A (en) * 1996-07-08 1998-11-10 Yamamoto; Keiko Combination washer-drier system
US5814224A (en) * 1996-08-12 1998-09-29 Institut Geokhimii I Analiticheskoi Khimii Im.V.I.Vernadskogo Ran (Geokhi Ran) Method for complex processing of sea-water
US5689893A (en) * 1996-09-13 1997-11-25 Westinghouse Air Brake Company Desiccant canister with positioning bore
US5735194A (en) * 1997-01-03 1998-04-07 Cochran; David M. Apparatus for separating chaff and roasting coffee and cocoa beans
DE19719398A1 (de) * 1997-05-07 1998-11-12 Amsco Finn Aqua Gmbh Verfahren zur Steuerung eines Gefriertrocknungsprozesses
US6228394B1 (en) * 1997-10-14 2001-05-08 Boehringer Ingelheim Pharmaceuticals, Inc. Supercritical fluid extraction of mould lubricant from hard shell capsules
JPH11178778A (ja) * 1997-12-17 1999-07-06 Zojirushi Corp 食器洗い乾燥機
US6358673B1 (en) * 1998-09-09 2002-03-19 Nippon Telegraph And Telephone Corporation Pattern formation method and apparatus
US6189236B1 (en) * 1998-11-05 2001-02-20 Union Carbide Chemicals & Plastics Technology Corporation Process for drying a reactor system employing a fixed bed adsorbent
US6094835A (en) * 1998-12-14 2000-08-01 University Of Central Florida Heat pump dryer with desciccant enhanced moisture removal
US6158144A (en) * 1999-07-14 2000-12-12 The Procter & Gamble Company Process for capillary dewatering of foam materials and foam materials produced thereby
US6418834B1 (en) * 1999-07-26 2002-07-16 Paul M. Perrine Apparatus for treating an item during travel of the item along a treating trough
CA2347784A1 (fr) * 1999-09-13 2001-03-22 Akihiro Morimoto Procede d'assechement dans les systemes d'alimentation en gaz
DE19952089C1 (de) * 1999-10-29 2001-04-05 Henkel Kgaa Verwendung von thermoplastischen Polymerzusammensetzungen als Trockenmittel
JP3767301B2 (ja) * 2000-02-16 2006-04-19 三菱電機株式会社 乾燥装置
US6434857B1 (en) * 2000-07-05 2002-08-20 Smartclean Jv Combination closed-circuit washer and drier
JP2002263050A (ja) * 2001-03-12 2002-09-17 Hoshizaki Electric Co Ltd 食器洗浄機
US7370436B2 (en) * 2001-07-09 2008-05-13 Ricardo Francisco Auer Dual apparatus and process for quick freezing and/or freeze drying produce
KR100390515B1 (ko) * 2001-09-25 2003-07-04 엘지전자 주식회사 의류 세탁건조기 및 의류 건조기
US6658757B2 (en) * 2001-10-25 2003-12-09 M-I L.L.C. Method and apparatus for separating hydrocarbons from material
US20030147697A1 (en) * 2002-02-06 2003-08-07 Brady Patrick Richard Evaporative desorption soil treatment apparatus and process
US6883723B2 (en) * 2002-04-10 2005-04-26 Ecolab Inc. Product dispenser and carrier
EP1495178B1 (fr) * 2002-04-10 2007-04-04 Ecolab Inc. Support et distributeur de produit
JP4902103B2 (ja) * 2002-04-11 2012-03-21 メディミューン・エルエルシー 凍結乾燥フォームによる生物活性材料の保存
US20040045187A1 (en) * 2002-09-10 2004-03-11 Andrew Corporation Heatless and reduced-heat drying systems
AT412999B (de) * 2002-11-12 2005-09-26 Wiedl Alfred Anlage zum trocknen von gütern
NL1022548C2 (nl) * 2003-01-31 2004-08-03 Plato Internat Technology B V Werkwijze voor het veredelen van houtdelen.
KR100510680B1 (ko) * 2003-03-31 2005-08-31 엘지전자 주식회사 증기분사식 드럼세탁기
PL1667569T3 (pl) * 2003-07-30 2021-03-08 BSH Hausgeräte GmbH Zmywarka do naczyń
US8601716B2 (en) * 2003-07-30 2013-12-10 Bsh Bosch Und Siemens Hausgeraete Gmbh Method for operating a device with at least one partial programme step of drying
KR20050017481A (ko) * 2003-08-13 2005-02-22 엘지전자 주식회사 증기발생장치를 구비한 드럼세탁기
EP1664647B1 (fr) * 2003-09-25 2011-06-08 Panasonic Corporation Appareil de sechage de type pompe a chaleur, appareil de sechage et procede de sechage
US20050086830A1 (en) * 2003-10-24 2005-04-28 Zukor Kenneth S. Processing cap assembly for isolating contents of a container
US7326347B2 (en) * 2003-10-29 2008-02-05 Wrt International Llc Dynamic up-flow zeolite system and method
DE10356787A1 (de) * 2003-12-04 2005-07-07 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine
DE10356786A1 (de) * 2003-12-04 2005-07-07 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zum Trocknen in einem Haushaltgerät
US6892473B1 (en) * 2003-12-08 2005-05-17 Air Products And Chemicals, Inc. Process for removing water from ammonia
US20050139523A1 (en) * 2003-12-10 2005-06-30 Palmer Thomas L. Apparatus and method for air classification and drying of particulate matter
ES2644416T3 (es) * 2004-06-02 2017-11-28 Universal Stabilization Technologies, Inc. Conservación mediante vaporización
JP4494169B2 (ja) * 2004-11-11 2010-06-30 パナソニック株式会社 ドラム式洗濯乾燥機
DE102005004094A1 (de) * 2004-12-09 2006-06-22 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine
DE102005004092A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung und Verfahren zum Betreiben derselben
DE102005004097A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine und Verfahren zum Betreiben derselben
DE102005004093A1 (de) * 2004-12-09 2006-06-22 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine
DE102005004089A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung und Verfahren zum Betreiben derselben
DE102005004096A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine mit einer Sorptionstrockenvorrichtung
DE102005004095A1 (de) * 2004-12-09 2006-06-14 BSH Bosch und Siemens Hausgeräte GmbH Geschirrspülmaschine
US20070094887A1 (en) * 2005-10-03 2007-05-03 Philipp Peter R System and method for treating wooden materials with ozone
DE102006018252B4 (de) * 2006-04-20 2009-02-05 Cs Clean Systems Ag Sorptionskolonne
WO2007127286A2 (fr) * 2006-04-24 2007-11-08 Medical Instill Technologies, Inc. dispositif de lyophilisation perméable aux aiguilles et refermable de façon étanche par laser et procédé associé
US7627920B2 (en) * 2006-06-09 2009-12-08 Whirlpool Corporation Method of operating a washing machine using steam
US7591859B2 (en) * 2006-08-15 2009-09-22 Whirlpool Corporation Water supply control for a steam generator of a fabric treatment appliance using a weight sensor
DE102008023070A1 (de) * 2007-05-11 2008-11-13 Mecoswiss Mechanische Componenten Gmbh & Co.Kg Haushaltsmaschine mit einer Kühlvorrichtung
DE102007049054A1 (de) * 2007-05-11 2008-11-13 Mecoswiss Mechanische Componenten Gmbh & Co.Kg Haushaltsmaschine mit Kühlvorrichtung
DE102007049613B4 (de) * 2007-10-17 2010-08-12 Cs Clean Systems Ag Fahrwerk für Fässer, insbesondere zu Sorptionskolonnen
KR100847058B1 (ko) * 2007-12-10 2008-07-18 하상안 오염토양 정화시스템

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US20070101609A1 (en) 2007-05-10

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