EP0732154A1 - Nettoyage avec des gaz liquides - Google Patents

Nettoyage avec des gaz liquides Download PDF

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Publication number
EP0732154A1
EP0732154A1 EP96103894A EP96103894A EP0732154A1 EP 0732154 A1 EP0732154 A1 EP 0732154A1 EP 96103894 A EP96103894 A EP 96103894A EP 96103894 A EP96103894 A EP 96103894A EP 0732154 A1 EP0732154 A1 EP 0732154A1
Authority
EP
European Patent Office
Prior art keywords
pressure
cleaning
gas
liquefied
pressure vessel
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.)
Granted
Application number
EP96103894A
Other languages
German (de)
English (en)
Other versions
EP0732154B1 (fr
Inventor
Stephan Dipl.-Ing. Rief
Robert Dipl.-Ing. Adler
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.)
Linde Gas AG
Original Assignee
Linde 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
Application filed by Linde GmbH filed Critical Linde GmbH
Publication of EP0732154A1 publication Critical patent/EP0732154A1/fr
Application granted granted Critical
Publication of EP0732154B1 publication Critical patent/EP0732154B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/0021Cleaning by methods not provided for in a single other subclass or a single group in this subclass by liquid gases or supercritical fluids
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/50Solvents
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06LDRY-CLEANING, WASHING OR BLEACHING FIBRES, FILAMENTS, THREADS, YARNS, FABRICS, FEATHERS OR MADE-UP FIBROUS GOODS; BLEACHING LEATHER OR FURS
    • D06L1/00Dry-cleaning or washing fibres, filaments, threads, yarns, fabrics, feathers or made-up fibrous goods
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D2111/00Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
    • C11D2111/10Objects to be cleaned
    • C11D2111/14Hard surfaces
    • C11D2111/20Industrial or commercial equipment, e.g. reactors, tubes or engines

Definitions

  • the invention relates to a method for cleaning objects in a pressure vessel with liquefied gases.
  • DE-42 30 485 discloses a cleaning device for smaller workpieces using liquefied gases, a drum being rotatably and / or pivotably arranged in a pressure-resistant container and being connected to a drive device. By rotating the drum, both the cleaning fluid in the pressure-resistant container and the objects in the drum are set in turbulent motion, which increases the cleaning effect. Chemical solvents, mechanical abrasives and inflowing inert gases can also increase cleaning success.
  • at least one lock is provided on the pressure-resistant container for loading and unloading the objects. These locks make a complete ventilation of the pressure-resistant container for the removal of the objects or for loading unnecessary.
  • Liquid carbon dioxide at temperatures between 20 and approximately 30 ° C. with pressures corresponding to the vapor pressure values is used for the processes of the two steps mentioned.
  • WO 94/01613 a method for cleaning textiles using liquefied or supercritical carbon dioxide is known, which is introduced at temperatures between 20 and 100 ° C. and corresponding pressures between 60 and 350 bar into a pressure vessel loaded with the textiles. After the textiles have been washed, there is a displacement flushing with a second fluid, again a compressed gas, such as air or nitrogen.
  • a compressed gas such as air or nitrogen.
  • WO 90/06189 a method for removing impurities from a substrate is known in that the substrate is brought into contact by means of a compressed gas with liquid-like density at critical or supercritical pressure, the phase of the gas between liquid state and supercritical state being varied the temperature of the gas is shifted in a number of stages between supercritical and subcritical temperatures.
  • This multi-stage temperature variation is based on a change in the cohesive energy content of the gas dense phase.
  • the aim is to make the solubility of the compressed gas effective with regard to contamination. Mechanical interactions between the compressed gas and the contaminants are not taken into account.
  • the object of the present invention is therefore to develop a cleaning process with liquefied gases in which the same cleaning results can be achieved with less effort.
  • This object is achieved in that the gas liquefied under pressure is introduced into the pressure vessel which contains the objects to be cleaned, that subsequently or previously the temperature of the liquefied gas is lowered below the critical temperature of the gas and that the cleaning at least is carried out essentially below the critical temperature and below the critical pressure of the gas.
  • the increased mechanical interaction is due to a higher mass transport of fluid to the surface to be cleaned due to the increased density and the greater shear forces between the fluid and the substrate surface due to the increased viscosity of the fluid.
  • the viscosity increases exponentially with the reciprocal of the temperature.
  • noble gases such as helium or argon
  • hydrocarbons such as methane, ethane, propane, ethene or propene, as well as trifluoromethane, carbon dioxide, nitrous oxide and sulfur hexafluoride are suitable as fluids.
  • the liquefied gas is poured into the pressure vessel until it fills part of the same.
  • the liquefied gas is then in equilibrium with its gaseous phase.
  • the pressure vessel can be filled with liquefied gas until it is only in the liquid phase. Then the density and viscosity of the liquid can be increased even further if the pressure in the pressure vessel is increased while the temperature is kept constant.
  • carbon dioxide is particularly preferable, being liquid and gaseous at pressures of below 60 bar Phase with temperatures between -20 and + 20 ° C is used for the cleaning process according to the invention.
  • the pressure vessel can be completely filled with liquid carbon dioxide, the temperature then being kept constant at a value between -20 and + 20 ° C. and the pressure being increased to a value above the corresponding value on the vapor pressure curve .
  • the mechanical interactions can be increased if the liquefied gas and / or the objects to be cleaned are circulated in the pressure vessel. This is done in a known manner by means of an impeller or a rotatable drum in the pressure vessel.
  • the pressure vessel is only partially filled with liquefied gas, there is an additional frictional effect on the surface of the soiled objects when the objects to be cleaned are circulated by constant immersion and immersion out of or into the liquid phase.
  • the mechanical interaction can be increased if it is operated intermittently and / or with an alternating direction of rotation.
  • the method according to the invention has proven to be effective in many tests, in particular for cleaning textiles. It is also suitable to clean metal surfaces or electronic assemblies such as circuit boards from contaminants, which mostly contain organic residues.
  • contaminated test tissues soiled with various fats are cleaned in a pressure vessel into which liquefied carbon dioxide is introduced.
  • the pressure vessel contains a drum that rotates in the pressure vessel, whereby the textiles and the liquefied gas are moved relative to one another.
  • the gas is removed from a storage container in which carbon dioxide liquefied under pressure is present at ambient temperature, and the pressure container is partially filled.
  • the temperature in the pressure vessel is then reduced to approx. 10 ° C while the drum is rotated.
  • the pressure container can be completely filled after a certain cleaning time, the temperature of the liquid carbon dioxide then being kept constant at about 10 ° C. while the pressure is increased to over 45 bar.
  • the pressure can be increased, for example, up to 70 bar (below critical pressure).
  • the cleaning results are completely sufficient even at low pressure increases, so that operating and system costs can be significantly reduced compared to previous cleaning methods.
  • the procedure and a possible addition of surfactants will be selected. After cleaning, the contaminated carbon dioxide is removed and can be reused after relaxation, during which the contaminants fail. This contributes to environmental protection and further reduces costs.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Textile Engineering (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Cleaning In General (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
EP96103894A 1995-03-16 1996-03-12 Nettoyage avec des gaz liquides Expired - Lifetime EP0732154B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19509573A DE19509573C2 (de) 1995-03-16 1995-03-16 Reinigung mit flüssigem Kohlendioxid
DE19509573 1995-03-16

Publications (2)

Publication Number Publication Date
EP0732154A1 true EP0732154A1 (fr) 1996-09-18
EP0732154B1 EP0732154B1 (fr) 1999-06-16

Family

ID=7756865

Family Applications (1)

Application Number Title Priority Date Filing Date
EP96103894A Expired - Lifetime EP0732154B1 (fr) 1995-03-16 1996-03-12 Nettoyage avec des gaz liquides

Country Status (4)

Country Link
US (2) US5759209A (fr)
EP (1) EP0732154B1 (fr)
AT (1) ATE181261T1 (fr)
DE (2) DE19509573C2 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999010585A1 (fr) * 1997-08-27 1999-03-04 Micell Technologies, Inc. Procedes et compositions pour le nettoyage a sec
US6200352B1 (en) 1997-08-27 2001-03-13 Micell Technologies, Inc. Dry cleaning methods and compositions
US6218353B1 (en) 1997-08-27 2001-04-17 Micell Technologies, Inc. Solid particulate propellant systems and aerosol containers employing the same
US6248136B1 (en) 2000-02-03 2001-06-19 Micell Technologies, Inc. Methods for carbon dioxide dry cleaning with integrated distribution

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6148644A (en) 1995-03-06 2000-11-21 Lever Brothers Company, Division Of Conopco, Inc. Dry cleaning system using densified carbon dioxide and a surfactant adjunct
US6092538A (en) * 1996-09-25 2000-07-25 Shuzurifuresher Kaihatsukyodokumiai Method for using high density compressed liquefied gases in cleaning applications
US7338563B2 (en) * 1996-10-16 2008-03-04 Clark Steve L Process for cleaning hydrocarbons from soils
US7534304B2 (en) 1997-04-29 2009-05-19 Whirlpool Corporation Non-aqueous washing machine and methods
US6045588A (en) * 1997-04-29 2000-04-04 Whirlpool Corporation Non-aqueous washing apparatus and method
US6012307A (en) * 1997-12-24 2000-01-11 Ratheon Commercial Laundry Llc Dry-cleaning machine with controlled agitation
TW426775B (en) * 1998-03-16 2001-03-21 Ind Tech Res Inst Method of fibers scouring
US6098430A (en) * 1998-03-24 2000-08-08 Micell Technologies, Inc. Cleaning apparatus
US5977045A (en) * 1998-05-06 1999-11-02 Lever Brothers Company Dry cleaning system using densified carbon dioxide and a surfactant adjunct
CA2255413A1 (fr) 1998-12-11 2000-06-11 Fracmaster Ltd. Expansion d'azote dans du co2 liquide et utilisation de cette mousse comme fluide de fracturation
DE19859408A1 (de) * 1998-12-22 2000-07-06 Preussag Ag Minimax Verfahren zur Innenreinigung von Behältern
US6212916B1 (en) 1999-03-10 2001-04-10 Sail Star Limited Dry cleaning process and system using jet agitation
US6260390B1 (en) 1999-03-10 2001-07-17 Sail Star Limited Dry cleaning process using rotating basket agitation
US7044143B2 (en) * 1999-05-14 2006-05-16 Micell Technologies, Inc. Detergent injection systems and methods for carbon dioxide microelectronic substrate processing systems
AU5440200A (en) * 1999-06-11 2001-01-02 Raytheon Company Liquid carbon dioxide cleaning utilizing natural and modified natural solvents
US7097715B1 (en) * 2000-10-11 2006-08-29 R. R. Street Co. Inc. Cleaning system utilizing an organic cleaning solvent and a pressurized fluid solvent
US6755871B2 (en) * 1999-10-15 2004-06-29 R.R. Street & Co. Inc. Cleaning system utilizing an organic cleaning solvent and a pressurized fluid solvent
US6558432B2 (en) 1999-10-15 2003-05-06 R. R. Street & Co., Inc. Cleaning system utilizing an organic cleaning solvent and a pressurized fluid solvent
US6355072B1 (en) * 1999-10-15 2002-03-12 R.R. Street & Co. Inc. Cleaning system utilizing an organic cleaning solvent and a pressurized fluid solvent
US6776801B2 (en) 1999-12-16 2004-08-17 Sail Star Inc. Dry cleaning method and apparatus
US6475403B2 (en) * 2000-01-31 2002-11-05 Matsushita Electric Industrial Co., Ltd. Etching method and apparatus
WO2001060534A1 (fr) * 2000-02-18 2001-08-23 Eco2 Sa Dispositif et procede de nettoyage de precision de pieces
US7513132B2 (en) 2003-10-31 2009-04-07 Whirlpool Corporation Non-aqueous washing machine with modular construction
US6679067B1 (en) 2001-07-16 2004-01-20 C W Holdings Llc Cryogenic processes for treating pantyhose
RU2209166C1 (ru) 2002-06-07 2003-07-27 ООО "Марс" Упаковка со звуковоспроизведением
EP1442802A1 (fr) * 2003-01-28 2004-08-04 Linde Aktiengesellschaft Nettoyage avec du dioxyde de carbone liquide
US7300468B2 (en) 2003-10-31 2007-11-27 Whirlpool Patents Company Multifunctioning method utilizing a two phase non-aqueous extraction process
US7739891B2 (en) 2003-10-31 2010-06-22 Whirlpool Corporation Fabric laundering apparatus adapted for using a select rinse fluid
US7695524B2 (en) 2003-10-31 2010-04-13 Whirlpool Corporation Non-aqueous washing machine and methods
US7513004B2 (en) 2003-10-31 2009-04-07 Whirlpool Corporation Method for fluid recovery in a semi-aqueous wash process
WO2005106105A1 (fr) 2004-04-29 2005-11-10 Unilever N.V. Procede de nettoyage a sec
EP1618970A1 (fr) * 2004-07-22 2006-01-25 Linde Aktiengesellschaft Procédé de nettoyage au dioxyde de carbone
AU2005299107A1 (en) 2004-10-25 2006-05-04 Nanon A/S A method of producing a silicone rubber item and the product obtainable by the method
US7966684B2 (en) 2005-05-23 2011-06-28 Whirlpool Corporation Methods and apparatus to accelerate the drying of aqueous working fluids
US8668493B2 (en) * 2006-07-24 2014-03-11 Koninklijke Philips N.V. Liquid interdental cleaner
DE102007049286A1 (de) 2007-10-12 2009-04-23 Thomas Zundel Verfahren zur Reinigung von Leder und Ledertextilkombinationen
US9091017B2 (en) 2012-01-17 2015-07-28 Co2Nexus, Inc. Barrier densified fluid cleaning system
CA3153460A1 (fr) 2021-03-30 2022-09-30 Kyata Capital Inc. Systemes et methodes d'elimination de contaminants des surfaces de materiaux solides

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990006189A1 (fr) 1988-12-07 1990-06-14 Hughes Aircraft Company Procede de nettoyage utilisant les variations de phases de gaz a phase dense
WO1992014558A1 (fr) 1991-02-19 1992-09-03 Union Industrie Comprimierter Gase Gmbh Nfg. Kg Nettoyage de pieces comportant des residus organiques
EP0530949A1 (fr) 1991-09-04 1993-03-10 The Clorox Company Nettoyage par perhydrolyse menée dans un médium fluide dense
WO1994001613A1 (fr) 1992-07-13 1994-01-20 The Clorox Company Systeme de nettoyage a sec a l'aide de dioxyde de carbone liquide/supercritique
EP0583653A1 (fr) 1992-08-10 1994-02-23 Hughes Aircraft Company Nettoyage par cavitation dans un gaz liquéfié
EP0587168A1 (fr) * 1992-09-11 1994-03-16 Linde Aktiengesellschaft Installation de nettoyage avec des gaz liquides ou supercritiques
EP0624405A1 (fr) 1993-04-12 1994-11-17 Hughes Aircraft Company Système de nettoyage pour mégasons utilisant des gaz comprimés et condensés

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5467492A (en) * 1994-04-29 1995-11-21 Hughes Aircraft Company Dry-cleaning of garments using liquid carbon dioxide under agitation as cleaning medium

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990006189A1 (fr) 1988-12-07 1990-06-14 Hughes Aircraft Company Procede de nettoyage utilisant les variations de phases de gaz a phase dense
WO1992014558A1 (fr) 1991-02-19 1992-09-03 Union Industrie Comprimierter Gase Gmbh Nfg. Kg Nettoyage de pieces comportant des residus organiques
EP0530949A1 (fr) 1991-09-04 1993-03-10 The Clorox Company Nettoyage par perhydrolyse menée dans un médium fluide dense
WO1994001613A1 (fr) 1992-07-13 1994-01-20 The Clorox Company Systeme de nettoyage a sec a l'aide de dioxyde de carbone liquide/supercritique
EP0583653A1 (fr) 1992-08-10 1994-02-23 Hughes Aircraft Company Nettoyage par cavitation dans un gaz liquéfié
EP0587168A1 (fr) * 1992-09-11 1994-03-16 Linde Aktiengesellschaft Installation de nettoyage avec des gaz liquides ou supercritiques
DE4230485A1 (de) 1992-09-11 1994-03-17 Linde Ag Anlage zur Reinigung mit verflüssigten oder überkritischen Gasen
EP0624405A1 (fr) 1993-04-12 1994-11-17 Hughes Aircraft Company Système de nettoyage pour mégasons utilisant des gaz comprimés et condensés

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999010585A1 (fr) * 1997-08-27 1999-03-04 Micell Technologies, Inc. Procedes et compositions pour le nettoyage a sec
US6200352B1 (en) 1997-08-27 2001-03-13 Micell Technologies, Inc. Dry cleaning methods and compositions
US6218353B1 (en) 1997-08-27 2001-04-17 Micell Technologies, Inc. Solid particulate propellant systems and aerosol containers employing the same
US6258766B1 (en) 1997-08-27 2001-07-10 Micell Technologies, Inc. Dry cleaning methods and compositions
US6248136B1 (en) 2000-02-03 2001-06-19 Micell Technologies, Inc. Methods for carbon dioxide dry cleaning with integrated distribution
US6332342B2 (en) 2000-02-03 2001-12-25 Mcclain James B. Methods for carbon dioxide dry cleaning with integrated distribution

Also Published As

Publication number Publication date
USRE38001E1 (en) 2003-02-25
EP0732154B1 (fr) 1999-06-16
ATE181261T1 (de) 1999-07-15
DE59602213D1 (de) 1999-07-22
DE19509573A1 (de) 1996-09-19
US5759209A (en) 1998-06-02
DE19509573C2 (de) 1998-07-16

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