EP3969494A1 - Procédé pour la dissolution d'adhésifs - Google Patents

Procédé pour la dissolution d'adhésifs

Info

Publication number
EP3969494A1
EP3969494A1 EP20724112.6A EP20724112A EP3969494A1 EP 3969494 A1 EP3969494 A1 EP 3969494A1 EP 20724112 A EP20724112 A EP 20724112A EP 3969494 A1 EP3969494 A1 EP 3969494A1
Authority
EP
European Patent Office
Prior art keywords
bond
supercritical
bridges
fluid
supercritical fluid
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.)
Pending
Application number
EP20724112.6A
Other languages
German (de)
English (en)
Inventor
Nicolai KOLB
Peter ALTENBUCHNER
Gabriele Brenner
Bernhard Schleimer
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.)
Evonik Operations GmbH
Original Assignee
Evonik Operations 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 Evonik Operations GmbH filed Critical Evonik Operations GmbH
Publication of EP3969494A1 publication Critical patent/EP3969494A1/fr
Pending legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J175/00—Adhesives based on polyureas or polyurethanes; Adhesives based on derivatives of such polymers
    • C09J175/04—Polyurethanes
    • C09J175/06—Polyurethanes from polyesters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00—Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/0021—Cleaning by methods not provided for in a single other subclass or a single group in this subclass by liquid gases or supercritical fluids
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/2805—Compounds having only one group containing active hydrogen
    • C08G18/288—Compounds containing at least one heteroatom other than oxygen or nitrogen
    • C08G18/289—Compounds containing at least one heteroatom other than oxygen or nitrogen containing silicon
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/48—Polyethers
    • C08G18/4825—Polyethers containing two hydroxy groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • C08G18/7671—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B2220/00—Type of materials or objects being removed
    • B08B2220/01—Adhesive materials
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2170/00—Compositions for adhesives
    • C08G2170/20—Compositions for hot melt adhesives
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J2301/00—Additional features of adhesives in the form of films or foils
    • C09J2301/50—Additional features of adhesives in the form of films or foils characterized by process specific features
    • C09J2301/502—Additional features of adhesives in the form of films or foils characterized by process specific features process for debonding adherents
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Definitions

  • the present invention relates to a method in which a bond is brought into contact with a supercritical fluid, characterized in that the bond is based on one or more adhesives which have crosslinked polymers, the crosslinked polymers having at least one oxygen atom in the polymer chain, and the crosslinked polymers are crosslinked via urethane bridges or - 0-CH 2 -CH (0H) -CH 2 -0 bridges or molecular chains having corresponding bridges, and that after the bond has been brought into contact with the supercritical fluid in which the bond is involved the supercritical fluid is loaded, at least one of the parameters pressure, volume, amount of substance or temperature is changed in such a way that the fluid changes from the supercritical state to another state, as well as the use of this method as at least one sub-step in a method for releasing adhesions from Components.
  • Chemically reactive adhesives e.g. Polyurethane adhesives - both moisture-curing 1-component and 2-component adhesives - are used in many industrial processes where particularly high demands are placed on the bond.
  • polyurethane adhesives have excellent properties.
  • DBD Detachable On command
  • a common approach for de-bonding on demand is the input of temperature, whereby the adhesion and / or the cohesion are influenced.
  • This approach is disadvantageous, however, since the non-reactive incorporated polymers usually lead to a lower cohesion of the adhesive, even at lower temperatures.
  • Supercritical fluids sometimes also called supercritical fluids
  • supercritical CO2 are well known in the literature and combine the properties of liquid and gas. More precisely, they are space-filling liquids with the viscosity of gases, which have good diffusion properties.
  • the use of supercritical CO2 has been described for numerous applications. For example, the cleaning of metallic substrates, which are contaminated on the surface with paints or adhesions, by means of extraction with supercritical CO2 is described (WO 2006095371 A1). A similar extraction or cleaning process is also described for paper (EP 480476 A1).
  • thermoplastic plastics such as thermoplastic polyurethane (TPU) can be foamed by treatment with supercritical CO2 (US 20170259473 A1).
  • thermoplastic bonds are, however, mechanically less stable compared to the above-mentioned, strongly crosslinked reactive adhesives and correspondingly negative in terms of cohesion and longevity, which clearly limits their industrial use.
  • the present invention therefore relates to a method in which a bond is brought into contact with a supercritical fluid, characterized in that the bond is based on one or more adhesives which have crosslinked polymers, the crosslinked polymers having at least one oxygen atom in the polymer chain and the crosslinked polymers via urethane bridges or -0-CH 2 -CH (0H) -CH 2 -0 bridges or corresponding bridges Molecular chains are cross-linked, and that after the bond has been brought into contact with the supercritical fluid, in which the bond is loaded with the supercritical fluid, at least one of the parameters pressure, volume, amount of substance or temperature is changed so that the fluid changes from the supercritical state goes into another state as claimed in the claims.
  • the present invention also relates to the use of this method according to the invention as at least one sub-step in a method for detaching adhesive bonds between components.
  • the method according to the invention has the advantage that the transition of the supercritical fluid into the gaseous or liquid state causes the bond or the adhesive to be foamed so much that the bond strength decreases sufficiently to enable the components to be separated from one another, preferably non-destructively.
  • the tensile shear forces that have to be applied in order to loosen a bond can be reduced preferably by at least 50%.
  • Another advantage of the method according to the invention is that customary adhesive compositions can be used so that the industrial requirements with regard to mechanical strength and durability of the bonds are not influenced.
  • the indices given can represent both absolute numbers and mean values. In the case of polymeric compounds, the indices preferably represent mean values.
  • the method according to the invention in which an adhesive bond is brought into contact with a supercritical fluid, is characterized in that the adhesive bond is based on one or more adhesives based, which have crosslinked polymers, wherein the crosslinked polymers have at least one oxygen atom in the polymer chain and the crosslinked polymers are crosslinked via urethane bridges or -0-CH 2 -CH (0H) - CH 2 -0 bridges or corresponding bridges having molecular chains, and that after bringing the bond into contact with the supercritical fluid, in which the bond is loaded with the supercritical fluid, at least one of the parameters pressure, volume, amount of substance or temperature is changed so that the fluid is changed from the supercritical state to another state transforms.
  • the supercritical fluid preferably changes from the supercritical state to the gaseous state.
  • the transition of the fluid from the supercritical state to another state takes place in the method according to the invention preferably while the adhesive bond is (still) loaded with the supercritical fluid.
  • bonds are understood to be those which bond at least two components to one another.
  • the bonds can be flat or abutted.
  • adhesives that have crosslinked polymers are understood to be those adhesives which, after the physical application of the adhesive, via a subsequent chemical reaction, either with the environment (for example air humidity in the case of reactive adhesives) or with themselves (for example 2-component polyurethane or epoxy adhesive) enter into a chemical reaction.
  • the adhesives can e.g. B. moisture or radiation curable or thermally crosslinking adhesives, preferably polyurethane adhesives.
  • cross-linked adhesives are no longer soluble or meltable after complete curing / reaction and have a significantly higher cohesion than non-reactive adhesives.
  • the supercritical fluid is preferably supercritical carbon dioxide.
  • the crosslinked polymers are preferably based on polyester and / or polyether polyols, preferably polyester polyols.
  • the polyether polyols can be all known polyether polyols; they are preferably polyethylene glycol, polypropylene glycol or copolymers of ethylene glycol and propylene glycol, the monomers being distributed both randomly and in blocks.
  • the polyester polyols can be all known polyester polyols. Preferred bonds are based at least in part on amorphous polymers, preferably amorphous polyester-polyols. Amorphous polymers are characterized by the fact that no melting peak can be detected in DSC for these polymers. DSC stands for dynamic differential calorimetry, which is carried out based on the DSC method DIN 53765 using a heating rate of 10 K / min. Amorphous polymers accordingly have no melting temperature, but only a glass transition temperature. In Depending on the glass transition temperature, the amorphous polymers are either in liquid or solid, vitreous form at room temperature.
  • the crosslinked polymers are based on polyester polyols, in particular amorphous polyester polyols, which have an OH number, determined according to DIN 53240-2, of less than 30 mg KOH / g, preferably from 1 to 25 mg KOH / g have, especially because these crosslinked polymers can be foamed more strongly.
  • the polyester polyols used are preferably those with a functionality of at least 1, preferably 1 to 100, preferably 1.5 to 20 and particularly preferably 2.0 to 10, preferably at least one di- or polyol and at least one di- or polycarboxylic acid contain.
  • the polyols and polycarboxylic acids there are basically no restrictions and all mixing ratios can basically occur. The selection depends on the desired physical properties of the polyester. These can be solid and amorphous, liquid and amorphous and / or (partially) crystalline at room temperature.
  • Polycarboxylic acids are to be understood as meaning compounds which carry more than one and preferably two or more carboxyl groups.
  • carboxy functionalities are also understood to mean their derivatives, for example esters or anhydrides.
  • the polycarboxylic acids can preferably be aromatic or saturated or unsaturated aliphatic or saturated or unsaturated cycloaliphatic di- or polycarboxylic acids.
  • Dicarboxylic acids are preferably used.
  • suitable aromatic di- or polycarboxylic acids and their derivatives are compounds such as dimethyl terephthalate, terephthalic acid, isophthalic acid, naphthalenedicarboxylic acid and phthalic anhydride.
  • linear aliphatic di- or polycarboxylic acids examples include oxalic acid, dimethyl oxalate, malonic acid, dimethyl malonate, succinic acid, dimethyl succinate, glutaric acid, dimethyl glutarate, 3,3-dimethyl glutaric acid, adipic acid, adipic acid, dimethyl ester, pimelic acid, dimethyl ethylactic acid, dimethyl ethylazic acid, dimethyl ethylazic acid.
  • unsaturated linear di- and / or polycarboxylic acids include itaconic acid, fumaric acid, maleic acid or maleic anhydride.
  • saturated cycloaliphatic di- and / or polycarboxylic acids include derivatives of 1,4-cyclohexanedicarboxylic acids, 1,3-cyclohexanedicarboxylic acids and 1,2-cyclohexanedicarboxylic acids.
  • polyols used for the production of the polyester is arbitrary per se.
  • Polyols are to be understood as meaning compounds which carry more than one and preferably two or more hydroxyl groups.
  • linear or branched aliphatic and / or cycloaliphatic and / or aromatic polyols can be included.
  • Suitable diols or polyols are ethylene glycol, propanediol-1,2, propanediol-1,3, butanediol-1,4, butanediol-1,3, butanediol-1,2, butanediol-2,3, pentanediol-1,5 , Hexanediol-1, 6, octanediol-1, 8, nonanediol-1, 9, dodecanediol-1, 12, neopentyl glycol, butylethylpropanediol-1,3, methylpropanediol-1,3, methylpentanediol, cyclohexanedimethanol, tricylclo- [2.2.1] -decanedimethanol, isomers of
  • Limonene dimethanol isosorbitol, trimethylolpropane, glycerine, 1,2,6-hexanetriol, pentaerythrol, polyethylene glycol, polypropylene glycol and mixtures thereof.
  • Aromatic diols or polyols are reaction products of aromatic polyhydroxy compounds such as. B. hydroquinone, bisphenol A, bisphenol F, dihydroxynaphthalene, etc. with epoxides such. B. ethylene oxide or propylene oxide.
  • ether diols As diols or polyols, ether diols, d. H. Oligomers or polymers, e.g. B. based on ethylene glycol, propylene glycol or butanediol-1,4 may be included.
  • Polyols or polycarboxylic acids with more than two functional groups such as trimellitic anhydride, trimethylolpropane, pentaerythrol or glycerol, can also be used.
  • lactones and hydroxycarboxylic acids can be used as components of the polyester.
  • Bifunctional diols and dicarboxylic acids are preferably used.
  • the preferred polyester polyols can preferably be synthesized via a melt condensation.
  • the aforementioned di- or polycarboxylic acids and di- or polyols in an equivalent ratio of hydroxyl to carboxyl groups of 0.5 to 1.5, preferably 1.0 to 1.3 are initially introduced and melted.
  • the polycondensation is preferably carried out in the melt at temperatures between 150 and 280 ° C. within 3 to 30 hours.
  • a large part of the amount of water released is preferably first distilled off at normal pressure.
  • the remaining water of reaction and volatile diols are preferably split off until the desired molecular weight is reached.
  • the reaction can additionally be accelerated by adding an entrainer and / or a catalyst before or during the reaction.
  • Suitable entrainers are, for example, toluene and xylenes.
  • Suitable catalysts are e.g. Organotitanium or tin compounds such as tetrabutyl titanate or dibutyl tin oxide. Catalysts based on other metals such as. B. zinc or antimony, and metal-free esterification catalysts. Further additives and driving aids such as antioxidants or color stabilizers are also possible.
  • the adhesives can consist of just one or several different polyols; the adhesive is preferably formulated using several polyether and / or polyester polyols.
  • the adhesives can contain other auxiliaries customary for adhesive formulations, such as, for example, non-OH-functionalized polymers, e.g. B. thermoplastic polyurethanes (TPU) and / or polyacrylates and / or ethylene-vinyl acetate copolymers (EVA); Pigments or fillers, e.g. B. talc, silicon dioxide, titanium dioxide, barium sulfate, calcium carbonate, carbon black or colored pigments; Tackifier like.
  • B. colophony resins hydrocarbon resins, phenolic resins and anti-aging agents and auxiliaries.
  • the proportion of auxiliaries in the adhesives can be up to 50% by weight, preferably from 0.1 to 25% by weight, based on the total adhesive formulation.
  • the crosslinked polymers are preferably crosslinked via urethane bridges or bonds or molecular chains having corresponding bridges and not via molecular chains having -0-CH 2 -CH (OH) -CH 2 -0 bridges or corresponding bridges.
  • the crosslinked polymers are particularly preferably based on polyether and / or polyester polyols, preferably at least in part on amorphous polyester polyols, and are crosslinked via urethane bridges or bonds or molecular chains having corresponding bridges.
  • the crosslinking through bridges containing the unit -0-CH 2 -CH (0H) -CH 2 -0- or molecular chains containing corresponding bridges can take place, for example, by using compounds containing glycidyl ether groups. Such compounds can be obtained, for example, by reacting an OH group with epichlorohydrin.
  • the urethane bridges or bonds or corresponding bridges or bonds having molecular chains can e.g. can be obtained by using isocyanate compounds.
  • Suitable isocyanate compounds are preferably 4,4'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate, toluene diisocyanate isomers, isophorone diisocyanate,
  • Bringing the bond into contact with the supercritical fluid takes place preferably for a period of 1 minute to 48 hours, preferably 10 minutes to 24 hours and particularly preferably 2 to 22 hours.
  • the reduction of the tensile shear forces can be increased through a longer period of contact with the supercritical fluid.
  • one of the parameters pressure, volume, amount of substance or temperature is changed so that the fluid changes from the supercritical state to another state, preferably within a period of less than 15 seconds, preferably less than or equal to 10 seconds.
  • the method according to the invention can be used to reduce the tensile shear forces of the bond by preferably at least 50%, preferably at least 80%. It can be advantageous if, using the method according to the invention, the bond of at least one of the bonded components is completely detached. It can also be advantageous if the bond becomes so unstable that the components can be detached without the action of forces. In this case, the bond can completely detach from at least one of the bonded components or the bond itself can fall apart.
  • the method according to the invention is therefore preferably used as at least one sub-step in a method for releasing adhesive bonds between components.
  • the surfaces of the bonded components or the bonded components themselves can have the same materials or consist of these.
  • the surfaces of the bonded components or the bonded components themselves can, however, also have or consist of different materials.
  • the materials are preferably selected from metal, plastic or wood.
  • at least one bonded component or the surface thereof has or consists of a metal.
  • the thermal properties of the polymers used in the context of the present invention are determined by dynamic differential calorimetry (DSC) based on the DSC method DIN 53765. The values of the second heating interval are given, the heating rate was 10 K / min. 2.
  • the adhesive properties of the adhesives / adhesive formulations used in the context of the present invention were determined on the basis of the tensile shear strength according to DIN EN 1465 in N / mm 2 . 3. OHZ
  • the polymers used often have hydroxyl groups as end groups.
  • the concentration of the OH groups is determined titrimetrically in accordance with DIN 53240-2 in mgKOH / g polymer.
  • the NCO number was determined titrimetrically in percent by weight based on DIN EN 1242. 5.
  • the number-average and weight-average molecular weights (Mn and Mw) of the polymers used in the context of the present invention are determined according to DIN 55672-1 by means of gel permeation chromatography in tetrahydrofuran as the eluent and polystyrene for calibration.
  • the 2-component epoxy adhesives were produced according to the manufacturer's instructions for use.
  • bonds / test specimens to be investigated were treated (loaded) in a 1 L steel reactor with 100 bar CO2 at a temperature of 50 ° C. and the conditions were maintained for 20 hours. The reactor was then released to normal pressure within 10 seconds and the test specimens removed for further analysis.
  • films of cured adhesives with the dimensions 3 x 3 cm were cut and the expansion was evaluated per dimension.
  • the layer thickness of the films before expansion was 1.2 mm.
  • Reactive adhesives that are not polyurethane adhesives had no significant effect in the investigations; this applies to both the silane-functionalized polyolefin OK1, the silane-terminated polyol STP1 and the 2-component epoxy adhesives EK1 and EK2.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

La présente invention concerne un procédé dans lequel une liaison adhésive est mise en contact avec un fluide supercritique, caractérisé en ce que la liaison adhésive est à base d'un ou de plusieurs adhésifs qui présentent des polymères réticulés, les polymères réticulés présentant au moins un atome d'oxygène dans la chaîne de polymère et étant réticulés par l'intermédiaire de ponts de type uréthane ou par des ponts -O-CH2-CH(OH)-CH2-O- ou par des chaînes moléculaires présentant des ponts correspondants, et en ce qu'après la mise en contact de la liaison adhésive avec le fluide supercritique, dans laquelle la liaison adhésive est chargée avec le fluide supercritique, au moins l'un des paramètres de pression, de volume, de quantité de matière ou de température est modifé de telle façon que le fluide passe de l'état supercritique à un autre état, ainsi que l'utilisation de ce procédé en tant qu'au moins une étape partielle dans un procédé pour la dissolution de liaisons adhésives de composants.
EP20724112.6A 2019-05-17 2020-05-07 Procédé pour la dissolution d'adhésifs Pending EP3969494A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP19175091.8A EP3738991A1 (fr) 2019-05-17 2019-05-17 Procédé de dissolution des adhésifs
PCT/EP2020/062739 WO2020234002A1 (fr) 2019-05-17 2020-05-07 Procédé pour la dissolution d'adhésifs

Publications (1)

Publication Number Publication Date
EP3969494A1 true EP3969494A1 (fr) 2022-03-23

Family

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Family Applications (2)

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EP19175091.8A Withdrawn EP3738991A1 (fr) 2019-05-17 2019-05-17 Procédé de dissolution des adhésifs
EP20724112.6A Pending EP3969494A1 (fr) 2019-05-17 2020-05-07 Procédé pour la dissolution d'adhésifs

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Application Number Title Priority Date Filing Date
EP19175091.8A Withdrawn EP3738991A1 (fr) 2019-05-17 2019-05-17 Procédé de dissolution des adhésifs

Country Status (3)

Country Link
US (1) US20220306917A1 (fr)
EP (2) EP3738991A1 (fr)
WO (1) WO2020234002A1 (fr)

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5074958A (en) 1990-10-12 1991-12-24 Kimberly-Clark Corporation Method for removing polychlorinated dibenzodioxins and polychlorinated dibenzofurans and stickies from secondary fibers using supercritical propane solvent extraction
US5607518A (en) * 1995-02-22 1997-03-04 Ciba Geigy Corporation Methods of deblocking, extracting and cleaning polymeric articles with supercritical fluids
US5860467A (en) 1996-12-03 1999-01-19 The University Of North Carolina At Chapel Hill Use of CO2 -soluble materials in making molds
JP4093658B2 (ja) 1998-12-08 2008-06-04 日東電工株式会社 微細発泡粘着テープ又はシートと、その製造方法
ITSA20050007A1 (it) * 2005-03-10 2006-09-11 Uni Di Salerno Processo per la pulizia di cilindri da stampa e/o da accoppiamento, utilizzati nell'industria grafica e nella produzione di imballaggi flessibili.
JP4985881B1 (ja) * 2011-02-04 2012-07-25 ダイキン工業株式会社 ボンデッドシールからの金属部材の分離回収方法、およびボンデッドシールの製造方法
US9375866B2 (en) 2013-03-15 2016-06-28 Nike, Inc. Process for foaming thermoplastic elastomers
KR102245051B1 (ko) 2014-07-02 2021-04-26 헨켈 아게 운트 코. 카게아아 제거가능 폴리우레탄 핫 멜트 접착제 및 용도

Also Published As

Publication number Publication date
EP3738991A1 (fr) 2020-11-18
WO2020234002A1 (fr) 2020-11-26
US20220306917A1 (en) 2022-09-29

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