EP2914643A1 - Polymers of [4-(methylether)-1,3-dioxolane-2-one of polyether polyol] - Google Patents

Polymers of [4-(methylether)-1,3-dioxolane-2-one of polyether polyol]

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Publication number
EP2914643A1
EP2914643A1 EP13801629.0A EP13801629A EP2914643A1 EP 2914643 A1 EP2914643 A1 EP 2914643A1 EP 13801629 A EP13801629 A EP 13801629A EP 2914643 A1 EP2914643 A1 EP 2914643A1
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European Patent Office
Prior art keywords
polymer
formula
radical
och
chosen
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.)
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Application number
EP13801629.0A
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German (de)
French (fr)
Inventor
Guillaume Michaud
Frédéric Simon
Stéphane Fouquay
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Bostik SA
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Bostik SA
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Publication of EP2914643A1 publication Critical patent/EP2914643A1/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G64/00Macromolecular compounds obtained by reactions forming a carbonic ester link in the main chain of the macromolecule
    • C08G64/20General preparatory processes
    • C08G64/30General preparatory processes using carbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/321Polymers modified by chemical after-treatment with inorganic compounds
    • C08G65/324Polymers modified by chemical after-treatment with inorganic compounds containing oxygen
    • C08G65/3245Carbondioxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G71/00Macromolecular compounds obtained by reactions forming a ureide or urethane link, otherwise, than from isocyanate radicals in the main chain of the macromolecule
    • C08G71/04Polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G81/00Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
    • C08G81/02Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers at least one of the polymers being obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C08G81/024Block or graft polymers containing sequences of polymers of C08C or C08F and of polymers of C08G
    • C08G81/025Block or graft polymers containing sequences of polymers of C08C or C08F and of polymers of C08G containing polyether sequences

Definitions

  • the subject of the present invention is polymers comprising at each of their ends a 1,3-dioxolan-2-one (or cyclocarbonate) end group linked to a polymeric chain by an alpha (a) substituted methylether (CH 2 -O) function.
  • These polyurethanes once formulated, are intended for use in coatings, mastics or adhesives, as additives and / or as resins.
  • diisocyanates are toxic compounds as such, and are generally obtained from phosgene, itself very toxic by inhalation or contact.
  • the manufacturing process used in industry generally involves the reaction of an amine with an excess of phosgene to form an isocyanate.
  • Patent Application EP1088021 discloses oligomeric compounds of 1,3-dioxolan-2-one, including oligomeric compounds of 4-methylether-1,3-dioxolan-2-one polypropylene glycol.
  • the oligomeric compounds are synthesized by carbonation in a high pressure reactor, from the corresponding compounds comprising terminal groups with oxirane (or epoxide) terminations: by carbonation, the oxirane groups are converted into 1,3-dioxolan-2-one groups.
  • the oligomeric compounds of 1,3-dioxolan-2-one are then mixed with amine oligomers so as to synthesize, by crosslinking, polyurethanes.
  • the oligomeric 4-methylether-1,3-dioxolan-2-one polypropylene glycol compounds described herein have a low molecular weight, typically 350 to 3200 g / mol, and a star-shaped structure comprising from 2 to 8 branches, each branch comprising a 4-methylether-1,3-dioxolan-2-one polypropylene glycol and all the branches being interconnected by a hydrocarbon group.
  • the 4-methylether-1,3-dioxolan-2-one group terminates the terminal group of each branch, the hydrocarbon group being at the other end of the branch.
  • No example of synthesis of a polypropylene glycol 4-methyl ether-1,3-dioxolane oligomeric compound is described. However, the carbonation reaction is not complete, since the oligomers comprise from 4 to 12% by weight of the starting oligomers, which is problematic during the formation of the polyurethanes.
  • the patent application WO 03/028644 of Eurotech Ltd describes oligomeric compounds of 4-methylether-1,3-dioxolan-2-one which are almost pure, and in particular oligomeric compounds of 4-methylether-1,3-dioxolane.
  • Polypropylene glycol 2-one low molecular weight, typically from 600 to 1600 g / mol.
  • the structure of these oligomers is star-shaped comprising from 3 to 6 branches, each branch comprising a 4-methylether-1,3-dioxolan-2-one of polypropylene glycol, and all the branches being connected together by a group hydrocarbon.
  • the 4-methylether-1,3-dioxolan-2-one group terminates the terminal group of each branch, the hydrocarbon group being at the other end of the branch.
  • No example of synthesis of an oligomeric compound of polypropylene glycol 4-methylether-1,3-dioxolane is described.
  • the present invention aims to provide new intermediates for the synthesis of polyurethanes without using isocyanate.
  • the present invention relates to a polymer of formula (I) comprising at least one terminal group 4-methylether-1,3-dioxolan-2-one:
  • R is a hydrogen or an alkyl which comprises from 1 to 4 carbon atoms, preferably R is hydrogen and / or a methyl radical;
  • n is a number from 1 to 6, preferably m is chosen from 2 and 3, even more preferably m is equal to 2;
  • B is a monovalent, divalent, trivalent, tetravalent, pentavalent or hexavalent radical, said radical generally comprising from 1 to 44 carbon atoms per molecule;
  • n is such that the number-average molar mass Mn of the polymer of formula (I) is in the range of 4000 to 18000 g / mol, and such that the polydispersity (Pd) of the polymer of formula (I) is included in a range of 1.0 to 1.4.
  • the polydispersity Pd is defined as the ratio Mw / Mn, that is to say the ratio of the molar mass by weight to the molar mass by number of the polymer.
  • the two molar masses Mn and Mw are measured according to the invention by Size Exclusion Chromatography (SEC), usually with PEG (PolyEthyleneGlycol) or PS (Polystyrene) calibration.
  • SEC Size Exclusion Chromatography
  • terminal group means a group located at the end of the chain (or end) of the polymer.
  • the radical B may be linear or branched, may comprise at least one saturated and / or unsaturated bond, and may comprise at least one cyclic and / or alicyclic group.
  • the radical B is preferably chosen from the group formed by the radicals formed from methanol, ethylene glycol, propylene glycol, neopentyl glycol, dimeric fatty alcohol, trimethylolpropane, pentaerythritol, glycerol, arabinol and sorbitol compounds, starting from at least a hydroxyl group.
  • the polymeric divalent radical - (- OCH 2 -CH (R) -) n - generally has a number-average molecular weight in the range of about 667 to 18000 g / mol.
  • the polymeric divalent radical - (- OCH 2 --CH (R) -) n - may be formed from a block or random copolymer of at least two divalent radicals of polymers of formulas - (- OCH 2 - CH (R1) -) n i- and - (- OCH 2 -CH (R2) -) n2 -, where n1 and n2 are such that the molar mass by number Mn of the polymer of formula (I) is within a range from 4000 to 18000 g / mol, and such that the polydispersity (Pd) of the polymer of formula (I) is in the range of 1.0 to 1.4.
  • the polymeric divalent radical - (- OCH 2 -CH (R) -) n - comprises a plurality of oxyalkylene repeating units, preferably oxyethylenes, oxypropylenes, oxybutylenes and / or oxyhexylenes.
  • the polymeric divalent radical - (- OCH 2 -CH (R) -) n - is chosen from the group formed by the polyoxyethylene, polyoxypropylene, polyoxybutylene and polyoxyhexylene radicals, and their copolymers.
  • the copolymers are generally sequenced or statistical.
  • the divalent radical - (- OCH 2 -CH (R) -) n - is formed from a polyether polyol selected from the group consisting of copolymers formed from ethylene oxide and oxide of propylene.
  • the copolymers are generally sequenced or statistical.
  • these polyether polyols can be prepared by cyclic ring-opening polymerization. comprising oxygen such as a compound selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, often in the presence of an initiator such as a monomeric diol.
  • the invention also relates to a process for the preparation of at least one polymer of formula (I) according to the invention, comprising a step of carbonation of at least one polymer of formula (III) below in which B, R, m and n have the same meanings as those of formula (I):
  • the carbonation step is generally carried out as is known to those skilled in the art, at the pressure and temperature indicated above.
  • the carbonation step is generally carried out in the presence of CO2 in any form, for example in the liquid, gaseous or supercritical state (depending on the reaction pressure), and a reagent generally chosen from tetrabutylammonium bromide, tetrabutylammonium hydroxide, the mixtures comprising tin tetrachloride (SnCl 4 : 5H 2 O).
  • the carbonation step is preferably carried out in the presence of supercritical CO2 and tetrabutylammonium bromide.
  • the carbonation step is for example carried out according to the procedure described in the patent application WO 03/028644 or in the patent application FR 2952933.
  • the polymer of formula (III) is obtained by reaction of at least one polymer of formula (II), in which B, R, m and n have the same meanings as those of formula (I). ):
  • This reaction which makes it possible to substitute the terminal hydroxyl groups with oxirane (or epoxidic) groups, can be carried out for example according to the procedure described in US Pat. No. 2,888,426, or else according to the procedure described in patent application JP 2007009158. It can be done in one or more stages.
  • the invention finally relates to a process for preparing polyurethanes comprising reacting at least one polymer of formula (I) according to the invention with at least one compound comprising at least one, preferably at least two, amino groups, for example chosen from amines, diamines, triamines and polyamines, as well as polyurethanes obtainable by this preparation process.
  • the amines are preferably such that at least one amino group, preferably all the amino groups, are primary amino groups.
  • polyurethanes once formulated (i.e. formulated with other optional additives), are intended for use in coatings, putties or adhesives, as fillers and / or as resins. It is also possible to independently formulate the polymer of formula (I) and the compound comprising at least one amino group, before mixing.
  • the starting material PPG polypropylene glycol
  • the starting material PPG was either the commercial product Acclaim ® Polyol 4200 (molar mass Mn of 4000 g / mol) or the commercial product Acclaim ® Polyol 18200 (having a molecular weight Mn of 18000 g / mol), both products being marketed by Bayer Material Science.
  • Each PPG was of formula:
  • n being a function of the molar mass of the PPG.
  • the starting compound is a Acclaim ® Polyol 4200 or Acclaim ® Polyol 18200:
  • the total yield of all the two steps a) and b) in each case was about 93% calculated on the initial polypropylene glycol, whether the Acclaim ® 4200 or 18200 Acclaim ®.
  • the starting compound is a Acclaim ® Polyol 4200 or Acclaim ® Polyol 18200:
  • This carbonation step was carried out in the presence of supercritical CO2 and tetrabutylammonium bromide at a temperature of about 120 ° C, and the carbon dioxide was introduced at a pressure of about 20 MPa.
  • a mixture of one of the propylene glycol di [4- (methyl ether) -1,3-dioxolan-2-one] from the example was separately reacted at 80 ° C and in a stoichiometric ratio. 2 and primary diamine type polyether diamine (JEFFAMINE EDR 176, Huntsman) and this, until complete disappearance of the infrared band characteristic of groups 1, 3-dioxolan-2-one (at 1800 cm "1 ) and appearance of bands characteristic of the carbamate bond (band at 1700 cm -1 ).
  • the reaction time was about 72 hours.
  • the product thus synthesized resulted in the formation of a polyhydroxyurethane, which suitably formulated two-component blend provided the desired adhesive properties.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Polyethers (AREA)
  • Polyurethanes Or Polyureas (AREA)

Abstract

The invention relates to a polymer having formula (I), wherein: R is a hydrogen or an alkyl having between 1 and 4 carbon atoms; m is a number between 1 and 6; B is a monovalent, divalent, trivalent, tetravalent, pentavalent or hexavalent radical comprising between 1 and 44 carbon atoms per molecule; and n is such that the number-average molar mass Mn of the polymer of formula (I) is between 4000 and 18000 g/mol, and the polymolecularity (Pd) thereof is in a range of 1.0 to 1.4. The invention relates to a method for the production of the polymer having formula (I). The invention also relates to a method for the production of polyurethanes, comprising the reaction of a polymer having formula (I) with a compound containing an amino group, as well as polyurethanes that can be obtained in this manner.

Description

Polymères de r4-(méthyléther)-1 ,3-dioxolane-2-one de polyéther polyoll  Polymers of polyether polyol r4- (methylether) -1, 3-dioxolan-2-one
La présente invention a pour objet des polymères comprenant en chacune de leurs extrémités un groupement terminal 1 ,3-dioxolane-2-one (ou cyclocarbonate) lié à une chaîne polymérique par une fonction méthyléther (CH2-O) substituée en alpha (a) de la 1 ,3-dioxolane-2-one, et leur utilisation pour la préparation de polyuréthanes par réaction avec un composé comprenant au moins un groupement aminé. Ces polyuréthanes, une fois formulés, sont destinés à être utilisés dans des revêtements, mastics ou adhésifs, en tant qu'additifs et/ou en tant que résines. The subject of the present invention is polymers comprising at each of their ends a 1,3-dioxolan-2-one (or cyclocarbonate) end group linked to a polymeric chain by an alpha (a) substituted methylether (CH 2 -O) function. 1,3-dioxolan-2-one, and their use for the preparation of polyurethanes by reaction with a compound comprising at least one amino group. These polyurethanes, once formulated, are intended for use in coatings, mastics or adhesives, as additives and / or as resins.
La synthèse de polyuréthanes se fait traditionnellement par réaction entre un diol et un diisocyanate. Les diisocyanates sont des composés toxiques en tant que tels, et sont généralement obtenus à partir de phosgène, lui-même très toxique par inhalation ou par contact. Le procédé de fabrication utilisé dans l'industrie met généralement en œuvre la réaction d'une aminé avec un excès de phosgène pour former un isocyanate.  The synthesis of polyurethanes is usually done by reaction between a diol and a diisocyanate. Diisocyanates are toxic compounds as such, and are generally obtained from phosgene, itself very toxic by inhalation or contact. The manufacturing process used in industry generally involves the reaction of an amine with an excess of phosgene to form an isocyanate.
La recherche d'alternatives à la synthèse de polyuréthanes sans utiliser d'isocyanate (ou NIPU pour « Non Isocyanate Polyuréthane s en anglais), représente donc un enjeu majeur.  The search for alternatives to the synthesis of polyurethanes without using isocyanate (or NIPU for "Non Isocyanate Polyurethane s" in English), therefore represents a major challenge.
Cette recherche a fait l'objet de nombreuses études de recherche et de développement. Les pistes les plus étudiées concernent l'utilisation de polymères dont chacun des groupements terminaux comprend un groupement 1 ,3-dioxolane-2-one en terminaison. Ces polymères réagissent avec des aminés ou oligomères d'amines pour former des polyuréthanes.  This research has been the subject of numerous research and development studies. The most studied tracks concern the use of polymers, each of whose end groups comprises a 1, 3-dioxolan-2-one group on termination. These polymers react with amines or oligomers of amines to form polyurethanes.
Cependant, aucune des solutions proposées n'est satisfaisante.  However, none of the proposed solutions is satisfactory.
La demande de brevet EP1088021 , de Eurotech Ltd., décrit des composés oligomères de 1 ,3-dioxolane-2-one, parmi lesquels des composés oligomères de 4-méthyléther-1 ,3-dioxolane-2-one de polypropylène glycol. Les composés oligomères sont synthétisés par carbonatation dans un réacteur haute pression, à partir des composés correspondants comprenant des groupements terminaux à terminaisons oxyranes (ou époxydes) : par carbonatation, les groupements oxyranes se transforment en groupements 1 ,3-dioxolane-2-ones. Les composés oligomères de 1 ,3-dioxolane-2-one sont ensuite mélangés à des oligomères d'amines de façon à synthétiser, par réticulation, des polyuréthanes. Patent Application EP1088021, Eurotech Ltd., discloses oligomeric compounds of 1,3-dioxolan-2-one, including oligomeric compounds of 4-methylether-1,3-dioxolan-2-one polypropylene glycol. The oligomeric compounds are synthesized by carbonation in a high pressure reactor, from the corresponding compounds comprising terminal groups with oxirane (or epoxide) terminations: by carbonation, the oxirane groups are converted into 1,3-dioxolan-2-one groups. The oligomeric compounds of 1,3-dioxolan-2-one are then mixed with amine oligomers so as to synthesize, by crosslinking, polyurethanes.
Les composés oligomères de 4-méthyléther-1 ,3-dioxolane-2-one de polypropylène glycol décrits dans ce document ont une faible masse molaire, typiquement 350 à 3200 g/mol, et une structure en forme d'étoile comprenant de 2 à 8 branches, chaque branche comprenant un 4-méthyléther-1 ,3- dioxolane-2-one de polypropylène glycol et toutes les branches étant reliées entre elles par un groupement hydrocarboné. Le groupement 4-méthyléther- 1 ,3-dioxolane-2-one est en terminaison du groupement terminal de chaque branche, le groupement hydrocarboné se trouvant à l'autre extrémité de la branche. Aucun exemple de synthèse d'un composé oligomère de 4- méthyléther-1 ,3-dioxolane de polypropylène glycol n'est décrit. Cependant, la réaction de carbonatation n'est pas complète, puisque les oligomères comprennent de 4 à 12% en poids des oligomères de départ, ce qui est problématique lors de la formation des polyuréthanes.  The oligomeric 4-methylether-1,3-dioxolan-2-one polypropylene glycol compounds described herein have a low molecular weight, typically 350 to 3200 g / mol, and a star-shaped structure comprising from 2 to 8 branches, each branch comprising a 4-methylether-1,3-dioxolan-2-one polypropylene glycol and all the branches being interconnected by a hydrocarbon group. The 4-methylether-1,3-dioxolan-2-one group terminates the terminal group of each branch, the hydrocarbon group being at the other end of the branch. No example of synthesis of a polypropylene glycol 4-methyl ether-1,3-dioxolane oligomeric compound is described. However, the carbonation reaction is not complete, since the oligomers comprise from 4 to 12% by weight of the starting oligomers, which is problematic during the formation of the polyurethanes.
La demande de brevet WO 03/028644, de Eurotech Ltd décrit des composés oligomères de 4-méthyléther-1 ,3-dioxolane-2-one quasiment purs, et en particulier des composés oligomères de 4-méthyléther-1 ,3-dioxolane-2-one de polypropylène glycol de faible masse molaire, typiquement de 600 à 1600 g/mol. La structure de ces oligomères est en forme d'étoile comprenant de 3 à 6 branches, chaque branche comprenant un 4-méthyléther-1 ,3-dioxolane-2- one de polypropylène glycol, et toutes les branches étant reliées entre elles par un groupement hydrocarboné. Le groupement 4-méthyléther-1 ,3-dioxolane-2- one est en terminaison du groupement terminal de chaque branche, le groupement hydrocarboné se trouvant à l'autre extrémité de la branche. Aucun exemple de synthèse d'un composé oligomère de 4-méthyléther-1 ,3-dioxolane de polypropylène glycol n'est décrit.  The patent application WO 03/028644 of Eurotech Ltd describes oligomeric compounds of 4-methylether-1,3-dioxolan-2-one which are almost pure, and in particular oligomeric compounds of 4-methylether-1,3-dioxolane. Polypropylene glycol 2-one low molecular weight, typically from 600 to 1600 g / mol. The structure of these oligomers is star-shaped comprising from 3 to 6 branches, each branch comprising a 4-methylether-1,3-dioxolan-2-one of polypropylene glycol, and all the branches being connected together by a group hydrocarbon. The 4-methylether-1,3-dioxolan-2-one group terminates the terminal group of each branch, the hydrocarbon group being at the other end of the branch. No example of synthesis of an oligomeric compound of polypropylene glycol 4-methylether-1,3-dioxolane is described.
La présente invention a pour but de fournir de nouveaux intermédiaires permettant la synthèse de polyuréthanes sans utiliser d'isocyanate. Ainsi, la présente invention concerne un polymère de formule (I) comprenant au moins un groupement terminal 4-méthyléther-1 ,3-dioxolane-2-one : The present invention aims to provide new intermediates for the synthesis of polyurethanes without using isocyanate. Thus, the present invention relates to a polymer of formula (I) comprising at least one terminal group 4-methylether-1,3-dioxolan-2-one:
dans laquelle : in which :
- R est un hydrogène ou un alkyl qui comprend de 1 à 4 atomes de carbone, de préférence R est l'hydrogène et/ou un radical méthyle;  - R is a hydrogen or an alkyl which comprises from 1 to 4 carbon atoms, preferably R is hydrogen and / or a methyl radical;
- m est un nombre de 1 à 6, de préférence m est choisi parmi 2 et 3, de façon encore plus préférée m est égal à 2 ;  m is a number from 1 to 6, preferably m is chosen from 2 and 3, even more preferably m is equal to 2;
- B est un radical monovalent, divalent, trivalent, tétravalent, pentavalent ou hexavalent, ledit radical comprenant généralement de 1 à 44 atomes de carbone par molécule ;  B is a monovalent, divalent, trivalent, tetravalent, pentavalent or hexavalent radical, said radical generally comprising from 1 to 44 carbon atoms per molecule;
- et n est tel que la masse molaire en nombre Mn du polymère de formule (I) est comprise dans une fourchette de 4000 à 18000 g/mol, et tel que la polymolécularité (Pd) du polymère de formule (I) est comprise dans une fourchette de 1 ,0 à 1 ,4.  and n is such that the number-average molar mass Mn of the polymer of formula (I) is in the range of 4000 to 18000 g / mol, and such that the polydispersity (Pd) of the polymer of formula (I) is included in a range of 1.0 to 1.4.
La polymolécularité Pd est définie comme le rapport Mw / Mn, c'est-à-dire le rapport de la masse molaire en poids à la masse molaire en nombre du polymère.  The polydispersity Pd is defined as the ratio Mw / Mn, that is to say the ratio of the molar mass by weight to the molar mass by number of the polymer.
Les deux masses molaires Mn et Mw sont mesurées selon l'invention par chromatographie d'exclusion stérique (ou SEC, acronyme de « Size Exclusion Chromatography » en anglais), usuellement avec étalonnage PEG (PolyEthylèneGlycol) ou PS (Polystyrène).  The two molar masses Mn and Mw are measured according to the invention by Size Exclusion Chromatography (SEC), usually with PEG (PolyEthyleneGlycol) or PS (Polystyrene) calibration.
Par groupement terminal, on entend un groupement situé en bout de chaîne (ou extrémité) du polymère. Le radical B peut être linéaire ou ramifié, peut comprendre au moins une liaison saturée et/ou insaturée, et peut comprendre au moins un groupement cyclique et/ou alicyclique. By terminal group means a group located at the end of the chain (or end) of the polymer. The radical B may be linear or branched, may comprise at least one saturated and / or unsaturated bond, and may comprise at least one cyclic and / or alicyclic group.
Le radical B est de préférence choisi dans le groupe formé par les radicaux formés à partir des composés méthanol, éthylène glycol, propylène glycol, néopentyl glycol, alcool gras dimère, triméthylolpropane, pentaérythritol, glycérol, arabinol et sorbitol, par départ d'au moins un groupement hydroxyle.  The radical B is preferably chosen from the group formed by the radicals formed from methanol, ethylene glycol, propylene glycol, neopentyl glycol, dimeric fatty alcohol, trimethylolpropane, pentaerythritol, glycerol, arabinol and sorbitol compounds, starting from at least a hydroxyl group.
Le radical divalent polymérique -(-OCH2-CH(R)-)n- a généralement une masse molaire en nombre comprise dans une fourchette d'environ 667 à 18000 g/mol. The polymeric divalent radical - (- OCH 2 -CH (R) -) n - generally has a number-average molecular weight in the range of about 667 to 18000 g / mol.
Le radical divalent polymérique -(-OCH2-CH(R)-)n- peut être formé à partir d'un copolymère, séquencé ou statistique, d'au moins deux radicaux divalents de polymères, de formules -(-OCH2-CH(R1 )-)ni- et -(-OCH2-CH(R2)-)n2-, où n1 et n2 sont tels que la masse molaire en nombre Mn du polymère de formule (I) est comprise dans une fourchette de 4000 à 18000 g/mol, et tel que la polymolécularité (Pd) du polymère de formule (I) est comprise dans une fourchette de 1 ,0 à 1 ,4. The polymeric divalent radical - (- OCH 2 --CH (R) -) n - may be formed from a block or random copolymer of at least two divalent radicals of polymers of formulas - (- OCH 2 - CH (R1) -) n i- and - (- OCH 2 -CH (R2) -) n2 -, where n1 and n2 are such that the molar mass by number Mn of the polymer of formula (I) is within a range from 4000 to 18000 g / mol, and such that the polydispersity (Pd) of the polymer of formula (I) is in the range of 1.0 to 1.4.
Selon un mode de réalisation préféré de l'invention, le radical divalent polymérique -(-OCH2-CH(R)-)n- comprend une pluralité d'unités répétitives oxyalkylènes, de préférence oxyéthylènes, oxypropylènes, oxybutylènes et/ou oxyhéxylènes. According to a preferred embodiment of the invention, the polymeric divalent radical - (- OCH 2 -CH (R) -) n - comprises a plurality of oxyalkylene repeating units, preferably oxyethylenes, oxypropylenes, oxybutylenes and / or oxyhexylenes.
Selon un mode de réalisation préféré de l'invention, le radical divalent polymérique -(-OCH2-CH(R)-)n- est choisi dans le groupe formé par les radicaux polyoxyéthylènes, polyoxypropylènes, polyoxybutylènes, polyoxyhéxylènes, et leurs copolymères. Les copolymères sont généralement séquencés ou statistiques. According to a preferred embodiment of the invention, the polymeric divalent radical - (- OCH 2 -CH (R) -) n - is chosen from the group formed by the polyoxyethylene, polyoxypropylene, polyoxybutylene and polyoxyhexylene radicals, and their copolymers. The copolymers are generally sequenced or statistical.
De préférence, le radical divalent -(-OCH2-CH(R)-)n- est formé à partir d'un polyéther polyol choisi dans le groupe formé par les copolymères formés à partir d'oxyde d'éthylène et d'oxyde de propylène. Les copolymères sont généralement séquencés ou statistiques. Preferably, the divalent radical - (- OCH 2 -CH (R) -) n - is formed from a polyether polyol selected from the group consisting of copolymers formed from ethylene oxide and oxide of propylene. The copolymers are generally sequenced or statistical.
Comme il est connu de l'homme du métier, ces polyéthers polyols peuvent être préparés par polymérisation à ouverture de cycle de composé cyclique comprenant de l'oxygène tel qu'un composé choisi dans le groupe formé par l'oxyde d'éthylène, l'oxyde de propylène, l'oxyde de butylène, souvent en présence d'un initiateur tel qu'un diol monomérique. As is known to those skilled in the art, these polyether polyols can be prepared by cyclic ring-opening polymerization. comprising oxygen such as a compound selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide, often in the presence of an initiator such as a monomeric diol.
L'invention concerne encore un procédé de préparation d'au moins un polymère de formule (I) selon l'invention, comprenant une étape de carbonatation d'au moins un polymère de formule (III) ci-après dans laquelle B, R, m et n ont les mêmes significations que celles de la formule (I) :  The invention also relates to a process for the preparation of at least one polymer of formula (I) according to the invention, comprising a step of carbonation of at least one polymer of formula (III) below in which B, R, m and n have the same meanings as those of formula (I):
(III) en présence de CO2, généralement à une pression comprise entre 5.104 et 2.107 Pa (i.e. entre 0,5 et 200 bar) et à une température comprise entre 30 et 180°C, cette étape étant de préférence réalisée dans des conditions supercritiques à une pression comprise entre 107 et 2.107 Pa (i.e. entre 100 et 200 bar) et à une température comprise entre 80 et 150°C. Lorsque la température est inférieure à 80°C, la cinétique est généralement beaucoup trop lente et l'énergie d'activation est généralement insuffisante, et lorsque la température est supérieure à 180°C, on observe généralement une dégradation du catalyseur. (III) in the presence of CO2, generally at a pressure between 5.10 4 and 2.10 7 Pa (ie between 0.5 and 200 bar) and at a temperature between 30 and 180 ° C, this step preferably being carried out in supercritical conditions at a pressure between 10 7 and 2.10 7 Pa (ie between 100 and 200 bar) and at a temperature between 80 and 150 ° C. When the temperature is below 80 ° C, the kinetics is generally much too slow and the activation energy is generally insufficient, and when the temperature is above 180 ° C, there is generally a degradation of the catalyst.
L'étape de carbonatation s'effectue généralement ainsi qu'il est connu de l'homme du métier, à la pression et à la température indiquées ci-dessus. Ainsi l'étape de carbonatation s'effectue généralement en présence de CO2 sous toute forme, par exemple à l'état liquide, gazeux ou supercritique (selon la pression de réaction), et d'un réactif généralement choisi parmi le bromure de tétrabutylammonium, l'hydroxyde de tétrabutylammonium, les mélanges comprenant du tétrachlorure d'étain (SnCI4 :5H2O). L'étape de carbonatation s'effectue de préférence en présence de CO2 à l'état supercritique et de bromure de tétrabutylammonium. The carbonation step is generally carried out as is known to those skilled in the art, at the pressure and temperature indicated above. Thus the carbonation step is generally carried out in the presence of CO2 in any form, for example in the liquid, gaseous or supercritical state (depending on the reaction pressure), and a reagent generally chosen from tetrabutylammonium bromide, tetrabutylammonium hydroxide, the mixtures comprising tin tetrachloride (SnCl 4 : 5H 2 O). The carbonation step is preferably carried out in the presence of supercritical CO2 and tetrabutylammonium bromide.
L'étape de carbonatation est par exemple effectuée selon le mode opératoire décrit dans la demande de brevet WO 03/028644 ou dans la demande de brevet FR 2952933. Dans un mode de réalisation préféré, le polymère de formule (III) est obtenu par réaction d'au moins un polymère de formule (II), dans laquelle B, R, m et n ont les mêmes significations que celles de la formule (I) : The carbonation step is for example carried out according to the procedure described in the patent application WO 03/028644 or in the patent application FR 2952933. In a preferred embodiment, the polymer of formula (III) is obtained by reaction of at least one polymer of formula (II), in which B, R, m and n have the same meanings as those of formula (I). ):
B-[-(OCH2-CH(R))n-OH]m (II), B - [- (OCH 2 -CH (R)) n -OH] m (II),
avec l'épichlorhydrine. with epichlorohydrin.
Cette réaction, qui permet de substituer les groupements hydroxyles terminaux par des groupements oxiranes (ou époxides), peut être effectuée par exemple selon le mode opératoire décrit dans le brevet US 2888426, ou bien selon le mode opératoire décrit dans la demande de brevet JP 2007009158. Elle peut s'effectuer en une ou plusieurs étapes.  This reaction, which makes it possible to substitute the terminal hydroxyl groups with oxirane (or epoxidic) groups, can be carried out for example according to the procedure described in US Pat. No. 2,888,426, or else according to the procedure described in patent application JP 2007009158. It can be done in one or more stages.
L'invention concerne enfin un procédé de préparation de polyuréthanes comprenant la réaction d'au moins un polymère de formule (I) selon l'invention avec au moins un composé comprenant au moins un, de préférence au moins deux, groupements aminés, par exemple choisi parmi les aminés, les diamines, les triamines et les polyamines, ainsi que les polyuréthanes susceptibles d'être obtenus par ce procédé de préparation.  The invention finally relates to a process for preparing polyurethanes comprising reacting at least one polymer of formula (I) according to the invention with at least one compound comprising at least one, preferably at least two, amino groups, for example chosen from amines, diamines, triamines and polyamines, as well as polyurethanes obtainable by this preparation process.
Les aminés sont de préférence telles qu'au moins un groupement aminé, de préférence tous les groupements aminés, sont des groupements aminés primaires.  The amines are preferably such that at least one amino group, preferably all the amino groups, are primary amino groups.
Les polyuréthanes ainsi obtenus, qui sont nouveaux, sont avantageusement sans isocyanate.  The polyurethanes thus obtained, which are new, are advantageously without isocyanate.
Ces polyuréthanes, une fois formulés (i.e. mis en formule avec d'autres additifs éventuels), sont destinés à être utilisés dans des revêtements, mastics ou adhésifs, en tant que charges et/ou en tant que résines. Il est aussi possible de formuler indépendamment le polymère de formule (I) et le composé comprenant au moins un groupement aminé, avant leur mélange.  These polyurethanes, once formulated (i.e. formulated with other optional additives), are intended for use in coatings, putties or adhesives, as fillers and / or as resins. It is also possible to independently formulate the polymer of formula (I) and the compound comprising at least one amino group, before mixing.
L'invention sera mieux comprise à la vue des exemples qui suivent.  The invention will be better understood from the following examples.
EXEMPLES EXAMPLES
Les exemples qui suivent illustrent l'invention sans pour autant en limiter la portée. Les réactions de synthèse des exemples ont été menées selon le schéma ci-après : The examples which follow illustrate the invention without limiting its scope. The synthetic reactions of the examples were carried out according to the diagram below:
(III) (III)
2)  2)
(I)  (I)
Le composé (I) synthétisé était tel que m = 2, R = méthyl, et B était un radical divalent propylène ( -CH2-CH(CH3)- ).  The compound (I) synthesized was such that m = 2, R = methyl, and B was a divalent propylene radical (-CH 2 -CH (CH 3) -).
Le produit de départ PPG (PolyPropylèneGlycol) était soit le produit commercial Acclaim® Polyol 4200 (de masse molaire en nombre Mn de 4000 g/mol), soit le produit commercial Acclaim® Polyol 18200 (de masse molaire en nombre Mn de 18000 g/mol), ces deux produits étant commercialisés par la société Bayer Material Science. Chaque PPG était de formule : The starting material PPG (polypropylene glycol) was either the commercial product Acclaim ® Polyol 4200 (molar mass Mn of 4000 g / mol) or the commercial product Acclaim ® Polyol 18200 (having a molecular weight Mn of 18000 g / mol), both products being marketed by Bayer Material Science. Each PPG was of formula:
HO-(-CH(CH3)- CH2-O-)n/2-B-(-O-CH2-CH(CH3)-)n/2-OH, HO - (- CH (CH 3) -CH 2 -O-) n / 2-B - (-O-CH 2 -CH (CH 3) -) n / 2-OH,
n étant fonction de la masse molaire du PPG. 1 ) Synthèses des diqlycidyl éthers de polypropylène qlvcol de formule mi n being a function of the molar mass of the PPG. 1) Syntheses of polypropylene diqlycidyl ethers qvcol of formula mi
Chacune de ces deux synthèses a été effectuée en deux étapes successives a) et b), conformément au protocole décrit dans le brevet US 2888426.  Each of these two syntheses was carried out in two successive steps a) and b), according to the protocol described in US Pat. No. 2,888,426.
Etape a) : Addition de l'épichlorhydrine sur les groupements hydroxyles terminaux des polypropylène glycols  Step a): Addition of epichlorohydrin to the terminal hydroxyl groups of polypropylene glycols
i. Première addition i. First addition
2,5 moles de Acclaim® Polyol 4200 (Mn = 4000) ayant un IOH de 28,0 mg KOH/g (10,0 g), ont été mélangées avec 30 cm3 d'une solution à 10% de trifluorure de Bore (BF3) dans l'éther (soit environ 2 à 3 g de BF3). Le mélange a été chauffé jusqu'à environ 80 ± 3°C. Environ 7,5 moles d'épichlorohydrine (699 g) ont été introduites sur une période de 4 à 5 heures. Après 8 à 10 heures, la réaction était complète et l'excès d'épichlorhydrine a été éliminé sous vide.2.5 moles of Acclaim ® Polyol 4200 (Mn = 4000) having an OH value of 28.0 mg KOH / g (10.0g), were mixed with 30 cm 3 of a 10% solution of boron trifluoride (BF 3 ) in ether (ie about 2 to 3 g of BF 3 ). The mixture was heated to about 80 ± 3 ° C. About 7.5 moles of epichlorohydrin (699 g) were introduced over a period of 4 to 5 hours. After 8 to 10 hours the reaction was complete and the excess epichlorohydrin was removed in vacuo.
i. Seconde addition i. Second addition
2,5 moles de Acclaim® Polyol 18200 (Mn = 18000) ayant un IOH de 6,2 mg KOH/g (45,0 g), ont été mélangées avec 30 cm3 d'une solution à 10% de trifluorure de Bore (BF3) dans l'éther (soit environ 2 à 3 g de BF3). Le mélange a été chauffé jusqu'à environ 80 ± 3°C. Environ 7,5 moles d'épichlorohydrine (699 g) ont été introduites sur une période de 4 à 5 heures. Après 16 à 18 heures, la réaction était complète et l'excès d'épichlorhydrine a été éliminé sous vide. 2.5 moles of Acclaim® Polyol 18200 (Mn = 18000) having an IOH of 6.2 mg KOH / g (45.0 g) were mixed with 30 cm 3 of a 10% solution of boron trifluoride. (BF 3 ) in ether (ie about 2 to 3 g of BF 3 ). The mixture was heated to about 80 ± 3 ° C. About 7.5 moles of epichlorohydrin (699 g) were introduced over a period of 4 to 5 hours. After 16-18 hours the reaction was complete and the excess epichlorohydrin was removed in vacuo.
Les produits obtenus étaient de structure suivante, que le composé de départ soit un Acclaim® Polyol 4200 ou un Acclaim® Polyol 18200 : The products obtained were the following structure, the starting compound is a Acclaim ® Polyol 4200 or Acclaim ® Polyol 18200:
Etapes b) : Etapes de déshydrochloration des produits de l'étape a) Steps b): Dehydrochlorination steps of the products of step a)
1626 g d'aluminate de sodium technique ont été ajoutés à chacun des deux milieux réactionnels issus de l'étape a), avec 340 g d'eau et 5521 g de dioxane. A chaque fois, le milieu réactionnel a été mis sous agitation à température ambiante pendant 30 minutes puis chauffé et maintenu au reflux du condenseur pendant 10 heures (environ 95°C). Au terme des 10 heures, le milieu réactionnel a été filtré et le résidu de filtration a été lavé avec du dioxane. Le filtrat a été porté à une température de 150°C sous pression réduite (30 mm Hg) afin d'éliminer le mélange eau/dioxane. Le résidu a montré entre 1 ,87 et 2,00 radicaux glycidyl éthers par mole de polypropylène glycol.  1626 g of technical sodium aluminate were added to each of the two reaction media from step a), with 340 g of water and 5521 g of dioxane. Each time, the reaction mixture was stirred at room temperature for 30 minutes and then heated and maintained at reflux of the condenser for 10 hours (about 95 ° C). After 10 hours, the reaction medium was filtered and the filter residue was washed with dioxane. The filtrate was brought to a temperature of 150 ° C under reduced pressure (30 mm Hg) to remove the water / dioxane mixture. The residue showed between 1.87 and 2.00 glycidyl ether radicals per mole of polypropylene glycol.
Le rendement total de l'ensemble des deux étapes a) et b) était pour chacun des cas d'environ 93%, calculé sur le polypropylène glycol initial, que ce soit l'Acclaim® 4200 ou l'Acclaim® 18200. The total yield of all the two steps a) and b) in each case was about 93% calculated on the initial polypropylene glycol, whether the Acclaim ® 4200 or 18200 Acclaim ®.
Les produits finaux ont été filtrés séparément sur argile. Il aurait aussi été possible de les filtrer sur un composé de type charbon actif ou équivalent.  The final products were filtered separately on clay. It would also have been possible to filter them on a compound of the active carbon type or equivalent.
Les produits obtenus étaient de structure suivante, que le composé de départ soit un Acclaim® Polyol 4200 ou un Acclaim® Polyol 18200 : The products obtained were the following structure, the starting compound is a Acclaim ® Polyol 4200 or Acclaim ® Polyol 18200:
B ·B ·
(III)  (III)
2) Synthèse des dii4-(méthyléther)-1 ,3-dioxolane-2-one de polypropylène qlycoll (composés de formule (D)  2) Synthesis of polypropylene qlycoll diis 4- (methyl ether) -1,3-dioxolan-2-one (compounds of formula (D)
Cette synthèse a été effectuée conformément au protocole décrit dans la demande de brevet WO 03/028644 ou dans la demande de brevet FR 2952933.  This synthesis was carried out in accordance with the protocol described in the patent application WO 03/028644 or in the patent application FR 2952933.
La carbonatation s'est déroulée séparément pour chacun des deux composés de formule (III) issus de l'étape 1 ), dans un réacteur haute pression en présence du diglycidyl éther de polypropylène glycol issu de l'étape 1 ), et de 4 à 6 % en poids de bromure de tétrabutylammonium (TBNBr). Le réacteur a été chauffé à une température de 120°C puis du dioxyde de carbone a été introduit jusqu'à atteindre une pression d'au moins 100 bar (1 bar = 105 Pa). La réaction a été arrêtée lorsque la conversion des fonctions époxydes était totale. The carbonation took place separately for each of the two compounds of formula (III) resulting from step 1), in a high pressure reactor in the presence of the polypropylene glycol diglycidyl ether from step 1), and from 4 to 6% by weight of tetrabutylammonium bromide (TBNBr). The reactor was heated to a temperature of 120 ° C and then carbon dioxide was introduced until reaching a pressure of at least 100 bar (1 bar = 10 5 Pa). The reaction was stopped when the conversion of the epoxide functions was complete.
Cette étape de carbonatation a été effectuée en présence de CO2 supercritique et de bromure de tétrabutylamonium, à une température d'environ 120°C, et le dioxyde de carbone a été introduit à une pression comprise d'environ 20 MPa.  This carbonation step was carried out in the presence of supercritical CO2 and tetrabutylammonium bromide at a temperature of about 120 ° C, and the carbon dioxide was introduced at a pressure of about 20 MPa.
Les produits ainsi obtenus, correspondants respectivement aux polyols Acclaim® 4200 et Acclaim® 18200, ont été chacun caractérisés par RMN : 1HNMR (CDCI3) ppm : 4,85 (bm, CH3CH-O), 4.4-4.0 (m, 4H, CH2-O 1 ,3- dioxolane-2-one), 3.65-3.25 (bm, CHO and CH2 polymère), 3.2 (m, 2H CHO 1 ,3-dioxolane-2-one), 2.8-2.6 (m, 4H CH2O 1 ,3-dioxolane-2-one), 1 .25 (bs, CH3 polymère). 13CNMR (CDCI3) ppm : 155.7, 130.1 , 129.2, 128.4, 125.4, 76.0-68.6, 68.2, 68.1 , 49.2, 44.7, 17.4, 16.8. The products thus obtained, corresponding respectively to Acclaim polyols ® 4200 and Acclaim ® 18200 were each characterized by NMR: 1 HNMR (CDCl 3) ppm: 4.85 (bm, CH 3 CH-O), 4.4-4.0 (m , 4H, CH 2 -O 1, 3-dioxolan-2-one), 3.65-3.25 (bm, CHO and CH 2 polymer), 3.2 (m, 2H CHO 1, 3-dioxolan-2-one), 2.8- 2.6 (m, 4H CH 2 O 1, 3-dioxolan-2-one), 1.25 (bs, CH 3 polymer). 13 CNMR (CDCI 3 ) ppm: 155.7, 130.1, 129.2, 128.4, 125.4, 76.0-68.6, 68.2, 68.1, 49.2, 44.7, 17.4, 16.8.
Ils étaient de structure suivante, que le composé de départ soit un Acclaim® Polyol 4200 ou un Acclaim® Polyol 18200 : They were of the following structure, whether the starting compound was an Acclaim ® Polyol 4200 or an Acclaim ® Polyol 18200:
3. Synthèse des polvhydroxyuréthanes à partir des di[4-(méthyléther)- 1 ,3-dioxolane-2-one de propylène qlycolsl de l'exemple 2 3. Synthesis of polyhydroxyurethanes from the di [4- (methylether) -1,3-dioxolan-2-one propylene glycolsl of Example 2
Il a été mis en réaction, séparément, à 80°C et dans un rapport stœchiométrique, un mélange d'un des di[4-(méthyléther)-1 ,3-dioxolane-2-one de propylène glycol] de l'exemple 2 et de diamine primaire de type polyéther diamine (JEFFAMINE EDR 176, Huntsman) et ce, jusqu'à disparition complète de la bande infrarouge caractéristique des groupements 1 ,3-dioxolane-2-one (à 1800 cm"1) et apparition des bandes caractéristiques de la liaison carbamate (bande à 1700 cm"1). La durée de la réaction était d'environ 72 heures. Dans chaque cas, le produit ainsi synthétisé a conduit à la formation d'un polyhydroxyuréthane, lequel mélange bicomposant formulé de façon adéquate a permis d'obtenir les propriétés adhésives souhaitées. A mixture of one of the propylene glycol di [4- (methyl ether) -1,3-dioxolan-2-one] from the example was separately reacted at 80 ° C and in a stoichiometric ratio. 2 and primary diamine type polyether diamine (JEFFAMINE EDR 176, Huntsman) and this, until complete disappearance of the infrared band characteristic of groups 1, 3-dioxolan-2-one (at 1800 cm "1 ) and appearance of bands characteristic of the carbamate bond (band at 1700 cm -1 ). The reaction time was about 72 hours. In each case, the product thus synthesized resulted in the formation of a polyhydroxyurethane, which suitably formulated two-component blend provided the desired adhesive properties.

Claims

REVENDICATIONS
1 . Polymère de formule (I) comprenant au moins un groupement terminal 4-méthyléther-1 ,3-dioxolane-2-one: 1. Polymer of formula (I) comprising at least one end group 4-methylether-1,3-dioxolan-2-one:
dans laquelle : in which :
- R est un hydrogène ou un alkyl qui comprend de 1 à 4 atomes de carbone, de préférence R est l'hydrogène et/ou un radical méthyle ;  - R is a hydrogen or an alkyl which comprises from 1 to 4 carbon atoms, preferably R is hydrogen and / or a methyl radical;
- m est un nombre de 1 à 6, de préférence m est choisi parmi 2 et 3, de façon encore plus préférée m est égal à 2 ;  m is a number from 1 to 6, preferably m is chosen from 2 and 3, even more preferably m is equal to 2;
- B est un radical monovalent, divalent, trivalent, tétravalent, pentavalent ou hexavalent, ledit radical comprenant généralement de 1 à 44 atomes de carbone par molécule ;  B is a monovalent, divalent, trivalent, tetravalent, pentavalent or hexavalent radical, said radical generally comprising from 1 to 44 carbon atoms per molecule;
- et n est tel que la masse molaire en nombre Mn du polymère de formule (I) est comprise dans une fourchette de 4000 à 18000 g/mol, et tel que la polymolécularité (Pd) du polymère de formule (I) est comprise dans une fourchette de 1 ,0 à 1 ,4.  and n is such that the number-average molar mass Mn of the polymer of formula (I) is in the range of 4000 to 18000 g / mol, and such that the polydispersity (Pd) of the polymer of formula (I) is included in a range of 1.0 to 1.4.
2. Polymère selon la revendication 1 , ledit composé étant tel que le radical B est choisi dans le groupe formé par les radicaux formés à partir des composés méthanol, éthylène glycol, propylène glycol, néopentyl glycol, alcool gras dimère, triméthylolpropane, pentaérythritol, glycérol, arabinol et sorbitol, par départ d'au moins un groupement hydroxyle. 2. Polymer according to claim 1, said compound being such that the radical B is chosen from the group formed by the radicals formed from the compounds methanol, ethylene glycol, propylene glycol, neopentyl glycol, dimer fatty alcohol, trimethylolpropane, pentaerythritol, glycerol. arabinol and sorbitol, starting from at least one hydroxyl group.
3. Polymère selon l'une des revendications 1 et 2, tel que le radical divalent polymérique -(-OCH2-CH(R)-)n- comprend une pluralité d'unités répétitives oxyalkylènes, de préférence oxyéthylènes, oxypropylènes, oxybutylènes et/ou oxyhéxylènes. 3. Polymer according to one of claims 1 and 2, such that the polymeric divalent radical - (- OCH 2 -CH (R) -) n - comprises a plurality of oxyalkylene repeating units, preferably oxyethylenes, oxypropylenes, oxybutylenes and and / or oxyhexylenes.
4. Polymère selon l'une des revendications 1 à 3, tel que le radical divalent polymérique -(-OCH2-CH(R)-)n- est choisi dans le groupe formé par les radicaux polyoxyéthylènes, polyoxypropylènes, polyoxybutylènes, polyoxyhéxylènes, et leurs copolymères. 4. Polymer according to one of claims 1 to 3, such that the polymeric divalent radical - (- OCH 2 -CH (R) -) n - is chosen from the group formed by the polyoxyethylenes, polyoxypropylenes, polyoxybutylenes, polyoxyhexylenes, and their copolymers.
5. Polymère selon l'une des revendications 1 à 4, tel que le radical divalent polymérique -(-OCH2-CH(R)-)n- est formé à partir d'un polyéther polyol choisi dans le groupe formé par les copolymères réalisés à partir d'oxyde d'éthylène et d'oxyde de propylène. 5. Polymer according to one of claims 1 to 4, such that the polymeric divalent radical - (- OCH 2 -CH (R) -) n - is formed from a polyether polyol selected from the group formed by the copolymers made from ethylene oxide and propylene oxide.
6. Procédé de préparation d'au moins un polymère de formule (I) selon l'une quelconque des revendications 1 à 5, comprenant une étape de carbonatation d'au moins un polymère de formule (III) ci-après dans laquelle B, R, m et n ont les mêmes significations que celles de la formule (I) : 6. Process for the preparation of at least one polymer of formula (I) according to any one of claims 1 to 5, comprising a carbonation step of at least one polymer of formula (III) below wherein B, R, m and n have the same meanings as those of formula (I):
(III) en présence de CO2, généralement à une pression comprise entre 5.104 et 2.107 Pa et à une température comprise entre 30 et 180°C, cette étape étant de préférence réalisée dans des conditions supercritiques à une pression comprise entre 107 et 2.107 Pa et à une température comprise entre 80 et 150°C. (III) in the presence of CO2, generally at a pressure between 5.10 4 and 2.10 7 Pa and at a temperature between 30 and 180 ° C, this step being preferably carried out under supercritical conditions at a pressure of between 10 7 and 2.10 7 Pa and at a temperature between 80 and 150 ° C.
7. Procédé de préparation selon la revendication 6, tel que le polymère de formule (III) est obtenu par réaction d'au moins un polymère de formule (II), dans laquelle B, R, m et n ont les mêmes significations que celles de la formule (I) : B-[-(OCH2-CH(R))n-OH]m (II) 7. Preparation process according to claim 6, such that the polymer of formula (III) is obtained by reaction of at least one polymer of formula (II), in which B, R, m and n have the same meanings as those of formula (I): B - [- (OCH 2 -CH (R)) n -OH] m (II)
avec l'épichlorhydrine. with epichlorohydrin.
8. Procédé de préparation de polyuréthanes comprenant la réaction d'au moins un polymère de formule (I) selon l'une quelconque des revendications 1 à 5, avec au moins un composé comprenant au moins un, de préférence au moins deux, groupements aminés, par exemple choisi parmi les aminés, les diamines, les triamines et les polyamines. 8. A process for preparing polyurethanes comprising reacting at least one polymer of formula (I) according to any one of claims 1 to 5, with at least one compound comprising at least one, preferably at least two, amino groups. , for example chosen from amines, diamines, triamines and polyamines.
9. Polyuréthanes susceptibles d'être obtenus par le procédé de préparation selon la revendication 8. 9. Polyurethanes obtainable by the preparation process according to claim 8.
EP13801629.0A 2012-11-05 2013-10-30 Polymers of [4-(methylether)-1,3-dioxolane-2-one of polyether polyol] Withdrawn EP2914643A1 (en)

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FR1260484A FR2997700B1 (en) 2012-11-05 2012-11-05 POLYETHER POLYOL POLYETHER [4- (METHYLETHER) -1,3-DIOXOLANE-2-ONE POLYMERS]
PCT/FR2013/052596 WO2014068251A1 (en) 2012-11-05 2013-10-30 Polymers of [4-(methylether)-1,3-dioxolane-2-one of polyether polyol]

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US11472936B2 (en) 2018-02-21 2022-10-18 Cryovac, Llc Method and formulation for an isocyanate-free foam using isocyanate-free polyurethane chemistry

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US5567527A (en) * 1995-02-21 1996-10-22 Eastman Chemical Company Copolymers containing 1,3-dioxolane-2-one-4-yl groups and coatings made therefrom
US6120905A (en) * 1998-06-15 2000-09-19 Eurotech, Ltd. Hybrid nonisocyanate polyurethane network polymers and composites formed therefrom
EP1020457A1 (en) * 1999-01-14 2000-07-19 Polymate Ltd. The method of synthesis polyfunctional polyclocarbonate oligomers and polymers formed therefrom
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FR2997700A1 (en) 2014-05-09
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