EP2576886B1 - Cooling device and method therefore for co2 washing machines - Google Patents
Cooling device and method therefore for co2 washing machines Download PDFInfo
- Publication number
- EP2576886B1 EP2576886B1 EP11723039.1A EP11723039A EP2576886B1 EP 2576886 B1 EP2576886 B1 EP 2576886B1 EP 11723039 A EP11723039 A EP 11723039A EP 2576886 B1 EP2576886 B1 EP 2576886B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- fluid
- cooling
- pressure
- regulator
- unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000001816 cooling Methods 0.000 title claims description 45
- 238000000034 method Methods 0.000 title claims description 21
- 238000005406 washing Methods 0.000 title description 4
- 239000012530 fluid Substances 0.000 claims description 55
- 238000004140 cleaning Methods 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000003860 storage Methods 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 14
- 239000002826 coolant Substances 0.000 claims description 10
- 238000005108 dry cleaning Methods 0.000 claims description 8
- 230000007423 decrease Effects 0.000 claims description 5
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 239000012809 cooling fluid Substances 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 16
- 229910002092 carbon dioxide Inorganic materials 0.000 description 8
- 239000001569 carbon dioxide Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 230000007613 environmental effect Effects 0.000 description 5
- 239000003507 refrigerant Substances 0.000 description 5
- 239000000356 contaminant Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000001419 dependent effect Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D31/00—Other cooling or freezing apparatus
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
- D06F43/081—Reclaiming or recovering the solvent from a mixture of solvent and contaminants, e.g. by distilling
- D06F43/083—Condensing arrangements
Definitions
- the present invention relates to dry cleaning systems namely washing machines using dry solvents such as carbon dioxide.
- the present invention relates to a cooling device and method for cooling solvents being used in such systems.
- EP0405941A2 discloses a system and a method for the additional recovering of solvents from a solvent cleaning process in which extraction means are connected to a chamber in which the cleaning process is performed to extract solvent from the chamber after the drying stage of the cleaning process, and means are provided for condensing the solvent from extracted flow and for returning the condensed solvent for re-use in a subsequent cleaning process.
- a drawback with the prior art systems is that they use cooling arrangements such as plate heat-exchanger for cooling the fluids in the system.
- This type of cooling device uses refrigerants, for example R404 refrigerant, which is not environmental friendly.
- refrigerants for example R404 refrigerant
- the use of this type or similar refrigerant is surrounded by governmental rules which therefore make it cumbersome to use.
- Due to the low working temperatures of prior art system a further drawback is that the refrigerant needs to be cooled in order to have a cooling effect on the fluids in these systems.
- an apparatus for cleaning articles comprising, a compressor unit for processing fluid, a regulator associated with the compressor unit, for increasing pressure of the fluid between the compressor unit and the regulator, characterised by a cooling unit arranged between the compressor unit and the regulator for cooling of the fluid.
- the cooling unit for cooling the fluid can comprise a simpler solution compared to prior art. This is due to the increased pressure where the cooling unit is arranged.
- the cooling unit comprises water as coolant.
- the temperature of the water may be around room temperature such as around 20°C or above.
- the water supply for the water used in the cooling unit as coolant can be taken directly from a duct, thereby water can be supplied on a need to have basis into the cooling unit.
- the apparatus according to the invention may use a compressor unit comprising one, two or more compressor stages.
- a compressor unit comprising one, two or more compressor stages.
- the pressure after the compressor unit is about 70 bar or more.
- the regulator may be any kind of device suitable to increase the pressure in the apparatus according to the invention.
- it may comprise a back pressure valve or an expansion valve. It may also comprise a valve for a fixed pressure increase such as a fixed counter pressure valve.
- Other solutions known to the person skilled in the art may also be used in order to increase the pressure in the arrangement according to the invention.
- a method for cooling fluid being used as a solvent in a dry cleaning system comprising the steps of: compressing the fluid, regulating pressure of the fluid, characterised in that the method further comprising the step of cooling the compressed fluid.
- the cooling step preferably comprises cooling the fluid with water as coolant.
- water may be room tempered and directly supplied from a duct on a need to have basis.
- the regulating step according to the invention preferably comprises the step of increasing the pressure. So that a higher pressure is build up in a certain part in the apparatus. In particular the pressure is increased where the cooling step takes place in the system, before the fluid is transferred to the storage device.
- the method may further comprise a second cooling step comprising a pressure decrease.
- a second cooling step comprising a pressure decrease.
- Figure 1 shows a dry cleaning apparatus according to the present invention comprising a storage device 1, a compressor 2, a cooling unit 3, a cleaning chamber 4 for cleaning fabrics, a distiller 5, a refill tube 6 and a regulator 7.
- the dry cleaning apparatus preferably uses carbon dioxide as solvent fluid which is stored in the storage device 1.
- the fluid When a cleaning program is started the fluid is transferred via pipes to the cleaning chamber 4 in order to clean the articles that are present in the cleaning chamber 4.
- the compressor unit 2 In order to have the fluid in the right phase where the cleaning effect is as effective as possible the compressor unit 2 builds up a pressure in the apparatus.
- the compressor unit 2 does not necessarily directly influence what phase the fluid is in, within the cleaning chamber 4, during e.g. a cleaning process. This is dependent on the temperature and/or pressure in accordance with the ideal gas law or related laws. For example the temperature can be decided by the pressure or the other way around. Thus in some parts of the system the fluid may be in a liquid state or in a gas state or in both liquid and gas state, depending on the pressure and temperature.
- the fluid Before the fluid is transferred to the storage device 1 after cleaning, the fluid is first distilled in the distiller 5 in order to remove contaminants from the fluid.
- the fluid is heated so that it gasifies and thereby can be removed from the distiller 5 without the contaminants.
- the fluid Before the fluid is transferred into the storage device 1 it has to be cooled in the cooling unit 3.
- the pressure on the fluid has to be at a certain level so that the water provides a cooling effect on the fluid.
- the pressure of the fluid passing the cooling unit is increased by a regulator 7 so that the temperature and pressure of the fluid is 35°C or more and 70 bar or higher.
- Room tempered water is about 20°C or above, however it can also be cooler such as between 15°C - 20°C. As long as the water is cooler than the fluid it is supposed to cool, a cooling effect can be achieved. Thus this makes it possible to use water as coolant directly supplied from a duct. Thereby as long as the apparatus is connected to a water supply duct, coolant will always be present. Coolant can also be requested on a need to have basis automatically by the apparatus according to the invention.
- the regulator 7 can either be of a variable active type that regulates the pressure independently of the pressure after the regulator 7.
- the pressure before the regulator 7 is set to a fixed level (e.g. 70 bar) independently of the pressure after the regulator 7.
- the delta( ⁇ ) value of the pressure before and after the regulator 7 is variable.
- the regulator 7 may also be of a fixed type that ensures a fixed pressure difference, delta( ⁇ ) pressure, before and after the regulator 7, such as +5, +10 or +15 bar, based on the pressure after the regulator 7.
- Figure 2 illustrates an embodiment according to the invention during evacuation of fluid from the cleaning chamber 4.
- the compressor 2 evacuates the fluid, in gas phase, from the cleaning chamber 4 by building up the pressure after the compressor 2.
- This is achieved by the regulator 7, thereby the fluid can be cooled by water in the cooling unit 3.
- the regulator 7 regulates the pressure so that the pressure of the fluid is 70 bar or higher before the regulator and about 55-60 bar after the regulator 7.
- Figure 3 illustrates the apparatus according to the invention during distillation activity.
- gas is transferred from the distiller 5 via the compressor 2.
- the compressor 2 increases the pressure of the fluid and thus also the temperature of the fluid.
- the fluid is transferred via pipes through the distiller 5 in order to use the heat in the pressurised fluid to evaporate the fluid in the distiller 5.
- the fluid is transferred to the cooling unit 3 for cooling and then transferred to the storage device 1 via the regulator 7. Since the pressure decreases after the regulator 7, a further temperature decrease is achieved when the fluid enters the storage device 1.
- Figure 4 depict an apparatus according to the invention comprising a compressor unit 2 comprising two compressor stages.
- Figure 5 shows a method according to the invention comprising a pressure increase step 8, a regulation step 9 wherein the pressure is regulated by the regulator 7 so that an increase of the pressure is achieved, and a cooling step 10 wherein the pressurized fluid is cooled by the cooling unit 3.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Cleaning By Liquid Or Steam (AREA)
- Detergent Compositions (AREA)
Description
- The present invention relates to dry cleaning systems namely washing machines using dry solvents such as carbon dioxide. In particular the present invention relates to a cooling device and method for cooling solvents being used in such systems.
- Washing systems using dry solvents such as carbon dioxide have been known for several years. In recent years this technology has become more popular mainly due to the environmental advantages compared to other washing systems using different solvents. Known dry cleaning systems usually contain a cleaning chamber wherein e.g. fabrics are cleaned, a distiller for separating the carbon dioxide from contaminants so that the carbon dioxide can be reused, a storage tank for storing the carbon dioxide when not in use for cleaning, a cooling unit, and a compressor for moving solvents in the system and for building up a pressure in the system. One example of such a system is disclosed in
EP 1842602 , which discloses a multiple bath CO2 system wherein the system and method is designed for processing parts in more than one bath of dense phase carbon dioxide. The system disclosed inEP1842602 is designed to work within a temperature interval between 10-20°C which corresponds to pressure up to 58 bar. Currently the trend in this technology goes towards increasing the pressure in these systems in order to achieve advantages in the cleaning properties of the solvent being used. - A further example is disclosed in
EP0405941A2 , which discloses a system and a method for the additional recovering of solvents from a solvent cleaning process in which extraction means are connected to a chamber in which the cleaning process is performed to extract solvent from the chamber after the drying stage of the cleaning process, and means are provided for condensing the solvent from extracted flow and for returning the condensed solvent for re-use in a subsequent cleaning process. - A drawback with the prior art systems is that they use cooling arrangements such as plate heat-exchanger for cooling the fluids in the system. This type of cooling device uses refrigerants, for example R404 refrigerant, which is not environmental friendly. The use of this type or similar refrigerant is surrounded by governmental rules which therefore make it cumbersome to use. Furthermore it also increases the production cost since more complex solutions needs to be used in order to comply with the rules. Due to the low working temperatures of prior art system a further drawback is that the refrigerant needs to be cooled in order to have a cooling effect on the fluids in these systems.
- Thus it is an object of the present invention to provide an improved dry cleaning apparatus.
- It is another object of the present invention to provide an improved cooling arrangement.
- It is yet another object of the present invention to provide a technical solution that is simple.
- It is even a further object of the present invention to provide a more environmental friendly solution.
- The above objects and others are achieved by providing an apparatus and method having the characteristics defined in the independent claims. Embodiment of the invention are defined by the dependent claims.
- According to a first aspect of the invention the above object and others are achieved by providing an apparatus for cleaning articles comprising, a compressor unit for processing fluid, a regulator associated with the compressor unit, for increasing pressure of the fluid between the compressor unit and the regulator, characterised by a cooling unit arranged between the compressor unit and the regulator for cooling of the fluid.
- By having such an arrangement an improved dry cleaning apparatus can be achieved since the cooling unit for cooling the fluid can comprise a simpler solution compared to prior art. This is due to the increased pressure where the cooling unit is arranged. Preferably the cooling unit comprises water as coolant. The temperature of the water may be around room temperature such as around 20°C or above. The water supply for the water used in the cooling unit as coolant can be taken directly from a duct, thereby water can be supplied on a need to have basis into the cooling unit.
- The apparatus according to the invention may use a compressor unit comprising one, two or more compressor stages. Preferably the pressure after the compressor unit is about 70 bar or more.
- The regulator may be any kind of device suitable to increase the pressure in the apparatus according to the invention. For example it may comprise a back pressure valve or an expansion valve. It may also comprise a valve for a fixed pressure increase such as a fixed counter pressure valve. Other solutions known to the person skilled in the art may also be used in order to increase the pressure in the arrangement according to the invention.
- According to a second aspect of the invention the above objects and others are achieved by a method for cooling fluid being used as a solvent in a dry cleaning system, the method comprising the steps of: compressing the fluid, regulating pressure of the fluid, characterised in that the method further comprising the step of cooling the compressed fluid. By compressing the fluid and then cooling the fluid between the compressor and regulator a number of advantages can be achieved. For example a simpler and cheaper cooling solution can be used.
- The cooling step preferably comprises cooling the fluid with water as coolant. Thereby a more environmental friendly solution can be achieved. As mentioned above the water may be room tempered and directly supplied from a duct on a need to have basis.
- The regulating step according to the invention preferably comprises the step of increasing the pressure. So that a higher pressure is build up in a certain part in the apparatus. In particular the pressure is increased where the cooling step takes place in the system, before the fluid is transferred to the storage device.
- The method may further comprise a second cooling step comprising a pressure decrease. When the fluid passes the regulator into the storage device a decrease of the pressure of the fluid may take place. This further cools down the fluid that is to be stored in the storage device.
- These and other aspects of the invention will be apparent from and elucidated with reference to the embodiments described hereinafter.
-
-
Figure 1 illustrates an embodiment of the apparatus according to the present invention comprising an arrangement of a regulator and cooling unit -
Figure 2 illustrates the apparatus according to the present invention during fluid evacuation, where the fluid is in gas phase. -
Figure 3 illustrates the apparatus according to the present invention during distillation. -
Figure 4 illustrates an embodiment of the present invention in an apparatus having a two stage compressor solution. -
Figure 5 illustrates method steps according to the present invention. - Figures are preferably schematically drafted in order to facilitate understanding. Therefore other designs that could be drafted in the same schematic way are implicitly also disclosed in this document.
-
Figure 1 shows a dry cleaning apparatus according to the present invention comprising astorage device 1, acompressor 2, acooling unit 3, acleaning chamber 4 for cleaning fabrics, adistiller 5, arefill tube 6 and aregulator 7. The dry cleaning apparatus preferably uses carbon dioxide as solvent fluid which is stored in thestorage device 1. - When a cleaning program is started the fluid is transferred via pipes to the
cleaning chamber 4 in order to clean the articles that are present in thecleaning chamber 4. In order to have the fluid in the right phase where the cleaning effect is as effective as possible thecompressor unit 2 builds up a pressure in the apparatus. - However the
compressor unit 2 does not necessarily directly influence what phase the fluid is in, within thecleaning chamber 4, during e.g. a cleaning process. This is dependent on the temperature and/or pressure in accordance with the ideal gas law or related laws. For example the temperature can be decided by the pressure or the other way around. Thus in some parts of the system the fluid may be in a liquid state or in a gas state or in both liquid and gas state, depending on the pressure and temperature. - Before the fluid is transferred to the
storage device 1 after cleaning, the fluid is first distilled in thedistiller 5 in order to remove contaminants from the fluid. - Thus in the
distiller 5 the fluid is heated so that it gasifies and thereby can be removed from thedistiller 5 without the contaminants. Before the fluid is transferred into thestorage device 1 it has to be cooled in thecooling unit 3. - In order to be able to use room tempered water as coolant, the pressure on the fluid has to be at a certain level so that the water provides a cooling effect on the fluid. For this purpose the pressure of the fluid passing the cooling unit is increased by a
regulator 7 so that the temperature and pressure of the fluid is 35°C or more and 70 bar or higher. By increasing the pressure and hence also the temperature to these levels it is possible to use room tempered water as coolant. Thereby it is no longer necessary to use refrigerants such as R404 and other cooling means to achieve the same. - Room tempered water is about 20°C or above, however it can also be cooler such as between 15°C - 20°C. As long as the water is cooler than the fluid it is supposed to cool, a cooling effect can be achieved. Thus this makes it possible to use water as coolant directly supplied from a duct. Thereby as long as the apparatus is connected to a water supply duct, coolant will always be present. Coolant can also be requested on a need to have basis automatically by the apparatus according to the invention.
- Furthermore other fluids which are liquid at room temperature and which are environmental friendly may also be used for cooling.
- As mentioned earlier the
regulator 7 can either be of a variable active type that regulates the pressure independently of the pressure after theregulator 7. Thus, the pressure before theregulator 7 is set to a fixed level (e.g. 70 bar) independently of the pressure after theregulator 7. Hence the delta(Δ) value of the pressure before and after theregulator 7 is variable. Theregulator 7 may also be of a fixed type that ensures a fixed pressure difference, delta(Δ) pressure, before and after theregulator 7, such as +5, +10 or +15 bar, based on the pressure after theregulator 7. -
Figure 2 illustrates an embodiment according to the invention during evacuation of fluid from thecleaning chamber 4. Thecompressor 2 evacuates the fluid, in gas phase, from thecleaning chamber 4 by building up the pressure after thecompressor 2. This is achieved by theregulator 7, thereby the fluid can be cooled by water in thecooling unit 3. Preferably theregulator 7 regulates the pressure so that the pressure of the fluid is 70 bar or higher before the regulator and about 55-60 bar after theregulator 7. -
Figure 3 illustrates the apparatus according to the invention during distillation activity. During distillation, gas is transferred from thedistiller 5 via thecompressor 2. Thecompressor 2 increases the pressure of the fluid and thus also the temperature of the fluid. The fluid is transferred via pipes through thedistiller 5 in order to use the heat in the pressurised fluid to evaporate the fluid in thedistiller 5. Thereafter the fluid is transferred to thecooling unit 3 for cooling and then transferred to thestorage device 1 via theregulator 7. Since the pressure decreases after theregulator 7, a further temperature decrease is achieved when the fluid enters thestorage device 1. -
Figure 4 depict an apparatus according to the invention comprising acompressor unit 2 comprising two compressor stages. -
Figure 5 shows a method according to the invention comprising apressure increase step 8, aregulation step 9 wherein the pressure is regulated by theregulator 7 so that an increase of the pressure is achieved, and a coolingstep 10 wherein the pressurized fluid is cooled by thecooling unit 3. - In the above description the term "comprising" does not exclude other elements or steps and "a" or "an" does not exclude a plurality.
- Furthermore the terms "include" and "contain" does not exclude other elements or steps.
Claims (10)
- A dry cleaning apparatus for cleaning articles using fluids comprising,- a compressor unit (2) for processing fluid,- a storage unit (1) for storage of the fluid,- a cooling unit (3) arranged between the compressor unit (2) and the storage unit (1) for cooling of the fluid,characterised by a regulator (7) associated with the compressor unit (2), the regulator (7) is arranged before the storage unit (1) for increasing pressure of the fluid where the cooling unit(3) is arranged, between the compressor unit (2) and the regulator (7).
- An apparatus according to claim 1, wherein the cooling unit (3) comprises water as coolant.
- An apparatus according to claim 2 wherein the temperature of the water is above 20°C.
- An apparatus according to any of the previous claims, wherein the compressor unit (2) comprises two or more compressor stages.
- An apparatus according to any of the previous claims, wherein the regulator (7) comprises a back pressure valve.
- An apparatus according to claim 1-4, wherein the regulator (7) comprises an expansion valve.
- An apparatus according to claim 1-4, wherein the regulator (7) comprises a fixed counter pressure valve.
- A method for cooling fluid being used as a solvent in an apparatus for cleaning articles according to any one of the claims 1-7, the method comprising the steps of:- compressing the fluid,- Characterised by regulating pressure of the fluid,by increasing the pressure where a cooling step takes place before the fluid is transferred to a storage device.
- A method according to claim 8, wherein the cooling step comprises cooling the fluid with water as coolant.
- A method according to any of claims 8-9, wherein the method further comprising a second cooling step comprising a pressure decrease.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SE1000577 | 2010-05-28 | ||
PCT/EP2011/058708 WO2011147956A2 (en) | 2010-05-28 | 2011-05-27 | Cooling device and method therefore for co2 washing machines |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2576886A2 EP2576886A2 (en) | 2013-04-10 |
EP2576886B1 true EP2576886B1 (en) | 2017-03-15 |
Family
ID=44626667
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11723039.1A Active EP2576886B1 (en) | 2010-05-28 | 2011-05-27 | Cooling device and method therefore for co2 washing machines |
Country Status (3)
Country | Link |
---|---|
US (1) | US20130167558A1 (en) |
EP (1) | EP2576886B1 (en) |
WO (1) | WO2011147956A2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10352591B2 (en) * | 2010-05-28 | 2019-07-16 | Electrolux Laundry Systems Sweden Ab | Cooling device and method therefore for CO2 washing machine |
KR102460179B1 (en) | 2020-11-17 | 2022-10-28 | 엘지전자 주식회사 | Laundry Treatment Apparatus And Control Method Thereof |
KR102536873B1 (en) * | 2021-01-25 | 2023-05-26 | 엘지전자 주식회사 | Washing machine |
KR102552904B1 (en) * | 2021-01-25 | 2023-07-07 | 엘지전자 주식회사 | Washing machine |
KR102472995B1 (en) * | 2021-01-25 | 2022-12-01 | 엘지전자 주식회사 | Washing machine |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB887677A (en) * | 1958-07-10 | 1962-01-24 | Pica Soc Nouv | Apparatus for solvent recovery |
US3002287A (en) * | 1960-02-18 | 1961-10-03 | Detrex Chem Ind | Control means for solvent recovery machine |
DE2426741C3 (en) * | 1974-06-01 | 1982-02-25 | Hoechst Ag, 6000 Frankfurt | Device for cleaning textiles, leather and furs with organic solvents and for distilling the solvent |
DE3038789A1 (en) * | 1980-10-14 | 1982-04-29 | Lohmann Gmbh & Co Kg, 5450 Neuwied | Fractionated condensation of solvent vapour mixt. - by compressed carrier gas through multistage turbine and condensate fraction after each stage |
US4984318A (en) * | 1989-06-28 | 1991-01-15 | Coindreau Palau Damaso | Method and system for the recovering of solvents in dry cleaning machines |
US6004403A (en) * | 1991-11-05 | 1999-12-21 | Gebhard Gray Associates | Solvent cleaning system |
US5702535A (en) * | 1991-11-05 | 1997-12-30 | Gebhard-Gray Associates | Dry cleaning and degreasing system |
US5267455A (en) * | 1992-07-13 | 1993-12-07 | The Clorox Company | Liquid/supercritical carbon dioxide dry cleaning system |
US6397421B1 (en) * | 1999-09-24 | 2002-06-04 | Micell Technologies | Methods and apparatus for conserving vapor and collecting liquid carbon dioxide for carbon dioxide dry cleaning |
US7513132B2 (en) * | 2003-10-31 | 2009-04-07 | Whirlpool Corporation | Non-aqueous washing machine with modular construction |
KR20030046506A (en) * | 2000-10-13 | 2003-06-12 | 미셀 테크놀로지즈, 인코포레이티드 | Device and process for dry-cleaning process using carbon dioxide and a divided pressure vessel |
JP4175811B2 (en) * | 2002-01-30 | 2008-11-05 | 日本サーモスタット株式会社 | Thermo element |
JP4121822B2 (en) * | 2002-10-04 | 2008-07-23 | 三洋電機株式会社 | Dry cleaning device |
CN1670295A (en) * | 2004-03-15 | 2005-09-21 | 三洋电机株式会社 | Dry cleaner and corresponding drying machine |
US7966684B2 (en) * | 2005-05-23 | 2011-06-28 | Whirlpool Corporation | Methods and apparatus to accelerate the drying of aqueous working fluids |
EP1747822A1 (en) * | 2005-07-28 | 2007-01-31 | Linde Aktiengesellschaft | Cooling / heating system for CO2 cleaning machine |
DE602007001206D1 (en) | 2006-04-06 | 2009-07-16 | Linde Ag | Mehrbad CO2 cleaning |
-
2011
- 2011-05-27 US US13/700,240 patent/US20130167558A1/en not_active Abandoned
- 2011-05-27 WO PCT/EP2011/058708 patent/WO2011147956A2/en active Application Filing
- 2011-05-27 EP EP11723039.1A patent/EP2576886B1/en active Active
Also Published As
Publication number | Publication date |
---|---|
US20130167558A1 (en) | 2013-07-04 |
EP2576886A2 (en) | 2013-04-10 |
WO2011147956A3 (en) | 2012-01-19 |
WO2011147956A2 (en) | 2011-12-01 |
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