WO2013059479A2 - Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom - Google Patents

Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom Download PDF

Info

Publication number
WO2013059479A2
WO2013059479A2 PCT/US2012/060840 US2012060840W WO2013059479A2 WO 2013059479 A2 WO2013059479 A2 WO 2013059479A2 US 2012060840 W US2012060840 W US 2012060840W WO 2013059479 A2 WO2013059479 A2 WO 2013059479A2
Authority
WO
WIPO (PCT)
Prior art keywords
alkyl
halo
heterocyclyl
cycloalkyl
aryl
Prior art date
Application number
PCT/US2012/060840
Other languages
French (fr)
Other versions
WO2013059479A3 (en
Inventor
Bernard Miles Malofsky
Adam Gregg Malofsky
Tanmoy Dey
Jeffrey M. Sullivan
Original Assignee
Bioformix Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to EP12842121.1A priority Critical patent/EP2768897B1/en
Priority to EP18152189.9A priority patent/EP3339301A3/en
Priority to JP2014537250A priority patent/JP2014532625A/en
Priority to CA2853073A priority patent/CA2853073A1/en
Priority to US14/352,369 priority patent/US9221739B2/en
Priority to MX2014004782A priority patent/MX360462B/en
Application filed by Bioformix Inc. filed Critical Bioformix Inc.
Publication of WO2013059479A2 publication Critical patent/WO2013059479A2/en
Publication of WO2013059479A3 publication Critical patent/WO2013059479A3/en
Priority to US14/868,795 priority patent/US9828324B2/en
Priority to US15/661,893 priority patent/US10414839B2/en
Priority to US15/678,533 priority patent/US20170342011A1/en
Priority to US16/455,040 priority patent/US20190315892A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F222/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides, or nitriles thereof
    • C08F222/10Esters
    • C08F222/12Esters of phenols or saturated alcohols
    • C08F222/14Esters having no free carboxylic acid groups, e.g. dialkyl maleates or fumarates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/67Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton
    • C07C45/68Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
    • C07C45/72Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms by reaction of compounds containing >C = O groups with the same or other compounds containing >C = O groups
    • C07C45/75Reactions with formaldehyde
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/76Ketones containing a keto group bound to a six-membered aromatic ring
    • C07C49/794Ketones containing a keto group bound to a six-membered aromatic ring having unsaturation outside an aromatic ring
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/76Ketones containing a keto group bound to a six-membered aromatic ring
    • C07C49/794Ketones containing a keto group bound to a six-membered aromatic ring having unsaturation outside an aromatic ring
    • C07C49/796Ketones containing a keto group bound to a six-membered aromatic ring having unsaturation outside an aromatic ring polycyclic
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/76Ketones containing a keto group bound to a six-membered aromatic ring
    • C07C49/794Ketones containing a keto group bound to a six-membered aromatic ring having unsaturation outside an aromatic ring
    • C07C49/798Ketones containing a keto group bound to a six-membered aromatic ring having unsaturation outside an aromatic ring containing rings other than six-membered aromatic rings
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/76Ketones containing a keto group bound to a six-membered aromatic ring
    • C07C49/80Ketones containing a keto group bound to a six-membered aromatic ring containing halogen
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/03Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/30Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/52Esters of acyclic unsaturated carboxylic acids having the esterified carboxyl group bound to an acyclic carbon atom
    • C07C69/604Polycarboxylic acid esters, the acid moiety containing more than two carboxyl groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/66Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety
    • C07C69/73Esters of carboxylic acids having esterified carboxylic groups bound to acyclic carbon atoms and having any of the groups OH, O—metal, —CHO, keto, ether, acyloxy, groups, groups, or in the acid moiety of unsaturated acids
    • C07C69/738Esters of keto-carboxylic acids or aldehydo-carboxylic acids
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D307/00Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D307/40Radicals substituted by oxygen atoms
    • C07D307/46Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D307/00Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/38Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
    • C07D307/54Radicals substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D333/00Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom
    • C07D333/02Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings
    • C07D333/04Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom
    • C07D333/06Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to the ring carbon atoms
    • C07D333/22Radicals substituted by doubly bound hetero atoms, or by two hetero atoms other than halogen singly bound to the same carbon atom
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D333/00Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom
    • C07D333/02Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings
    • C07D333/04Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom
    • C07D333/06Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom with only hydrogen atoms, hydrocarbon or substituted hydrocarbon radicals, directly attached to the ring carbon atoms
    • C07D333/24Radicals substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F116/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
    • C08F116/36Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by a ketonic radical
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F128/00Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur
    • C08F128/06Homopolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur by a heterocyclic ring containing sulfur
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/10Esters
    • C08F20/12Esters of monohydric alcohols or phenols
    • C08F20/14Methyl esters, e.g. methyl (meth)acrylate
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/10Esters
    • C08F20/26Esters containing oxygen in addition to the carboxy oxygen
    • C08F20/28Esters containing oxygen in addition to the carboxy oxygen containing no aromatic rings in the alcohol moiety
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/10Esters
    • C08F20/26Esters containing oxygen in addition to the carboxy oxygen
    • C08F20/30Esters containing oxygen in addition to the carboxy oxygen containing aromatic rings in the alcohol moiety
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/10Esters
    • C08F20/38Esters containing sulfur
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/62Monocarboxylic acids having ten or more carbon atoms; Derivatives thereof
    • C08F20/68Esters
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F22/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical and containing at least one other carboxyl radical in the molecule; Salts, anhydrides, esters, amides, imides or nitriles thereof
    • C08F22/10Esters
    • C08F22/12Esters of phenols or saturated alcohols
    • C08F22/20Esters containing oxygen in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F24/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a heterocyclic ring containing oxygen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F28/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur
    • C08F28/06Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur by a heterocyclic ring containing sulfur
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/01Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/013Fillers, pigments or reinforcing additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L21/00Compositions of unspecified rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L33/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
    • C08L33/04Homopolymers or copolymers of esters
    • C08L33/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur, or oxygen atoms in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L33/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
    • C08L33/04Homopolymers or copolymers of esters
    • C08L33/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur, or oxygen atoms in addition to the carboxy oxygen
    • C08L33/16Homopolymers or copolymers of esters containing halogen atoms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L35/00Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
    • C08L35/02Homopolymers or copolymers of esters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D129/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Coating compositions based on hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Coating compositions based on derivatives of such polymers
    • C09D129/12Homopolymers or copolymers of unsaturated ketones
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D133/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
    • C09D133/04Homopolymers or copolymers of esters
    • C09D133/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D133/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Coating compositions based on derivatives of such polymers
    • C09D133/04Homopolymers or copolymers of esters
    • C09D133/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
    • C09D133/16Homopolymers or copolymers of esters containing halogen atoms
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D135/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least another carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Coating compositions based on derivatives of such polymers
    • C09D135/02Homopolymers or copolymers of esters
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D141/00Coating compositions based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a bond to sulfur or by a heterocyclic ring containing sulfur; Coating compositions based on derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D4/00Coating compositions, e.g. paints, varnishes or lacquers, based on organic non-macromolecular compounds having at least one polymerisable carbon-to-carbon unsaturated bond ; Coating compositions, based on monomers of macromolecular compounds of groups C09D183/00 - C09D183/16
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/06Homopolymers or copolymers of esters of esters containing only carbon, hydrogen and oxygen, the oxygen atom being present only as part of the carboxyl radical
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J133/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J133/04Homopolymers or copolymers of esters
    • C09J133/14Homopolymers or copolymers of esters of esters containing halogen, nitrogen, sulfur or oxygen atoms in addition to the carboxy oxygen
    • C09J133/16Homopolymers or copolymers of esters containing halogen atoms
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09JADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
    • C09J135/00Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least another carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Adhesives based on derivatives of such polymers
    • C09J135/02Homopolymers or copolymers of esters
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Definitions

  • the invention relates to a new class of methylene beta-diketone monomers, to methods of producing or synthesizing such monomers, and to the use and application of such monomers as commercial products and compositions, including, for example, monomer-based products (e.g., inks, adhesives, coatings, sealants or reactive molding) and polymer-based products (e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants).
  • monomer-based products e.g., inks, adhesives, coatings, sealants or reactive molding
  • polymer-based products e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants.
  • the new monomers relate to a platform of methylene beta-diketone monomers having the general structural formula:
  • Products produced with such monomers include, for example, polymerizable compositions and polymers formed therefrom, e.g., inks, adhesives, coatings, sealants, reactive moldings, fibers, films, sheets, medical polymers, composite polymers and surfactants.
  • Methylene malonate monomers have been disclosed for example in U.S.
  • Patent Nos. U.S. Patent Nos. 2,313,501 ; 2,330,033; 3,221,745; 3,523,097; 3,557, 185; 3,758,550; 3,975,422; 4,049,698; 4,056,543; 4,160,864; 4,931,584; 5,142,098;
  • methylene malonates have the potential to form the basis of a large-scale platform of raw materials useful in a wide variety of chemical products.
  • methylene beta-diketone monomers and their associated monomeric and polymeric -based products would be useful in industrial, consumer, and medical applications.
  • methylene beta-diketone monomers would provide a benefit over other monomers in that the incorporation of a ketone group adjacent to the active methylene group reduces the susceptibility of degradation of the monomer upon utilization or further functionalization.
  • methylene beta-diketone monomers and their products can be produced via sustainable routes as well as be designed to be environmentally benign, biologically benign and as such many of the products can be generally regarded as "green.”
  • the invention provides a methylene beta-diketone monomer has a structure: wherein Ri and R 2 are independently C1-Q5 alkyl, C2-C15 alkenyl, halo-(Ci- Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -Cg cycloalkyl), heterocyclyl, heterocyclyl-(Ci- Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Cis alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C 1 -C15 alkyl, halo-(d- Ci5 alkyl
  • heterocyclyl heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
  • the invention provides a method of making a methylene beta-diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula: under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; and b) isolating a methylene beta-diketone monomer from the reaction complex, wherein the methylene beta-diketone monomer has the structural formula:
  • Ri and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci 5 alkyl), C 3 -C 6 cycloalkyl, halo-(C 3 -C 6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl,
  • heterocyclyl heterocyclyl, heterocyclyl-(Ci-Ci 5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci 5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
  • the methods of the invention herein include the step of isolating the methylene beta-diketone by: i. contacting the reaction complex, or a portion thereof, with an energy transfer means to produce a vapor phase including the methylene beta- diketone monomer; and
  • the methods of the invention herein include isolating the methylene beta-diketone by: i. heating the reaction complex, or a portion thereof, to a temperature between about 130°C and about 300°C to produce a vapor phase including the methylene beta-diketone monomer; and
  • the methods of the invention are performed under reaction conditions of: a) an initiating temperature of between about 60 °C and about 130 °C; b) atmospheric pressure.
  • the invention provides a method of preparing a methylene beta- diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula:
  • reaction complex under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; b) contacting the reaction complex, or a portion thereof, with an energy transfer means at a temperature between about 150°C and about 300°C to provide the reaction complex, or portion thereof, as a vapor phase; and c) isolating a methylene beta-diketone monomer from the reaction complex or portion thereof, wherein the methylene beta-diketone monomer has the structural formula: wherein each instance of Ri and R 2 are independently C 1 -C 15 alkyl, C2-C 15 alkenyl, halo-(Ci-Ci 5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci 5 alkyl), aryl
  • the invention provides a polymerizable composition comprising a methylene beta-diketone monomer of the invention.
  • the polymerizable composition is capable of bonding glass to a substrate in a time period of less than about 90 seconds, less than about 60 seconds, less than about 30 seconds, or less than about 15 seconds.
  • the polymerizable composition comprising a methylene beta-diketone monomer further comprises at least one additive selected from the group consisting of an acidic stabilizer, a free radical stabilizer, a sequestering agent, a cure accelerator, a rheology modifier, a plasticizing agent, a thixotropic agents, a natural rubber, a synthetic rubbers, a filler agent and a reinforcing agent.
  • at least one additive selected from the group consisting of an acidic stabilizer, a free radical stabilizer, a sequestering agent, a cure accelerator, a rheology modifier, a plasticizing agent, a thixotropic agents, a natural rubber, a synthetic rubbers, a filler agent and a reinforcing agent.
  • the invention provides an adhesive product comprising a methylene beta-diketone monomer of the invention.
  • the adhesive products have a shelf life of at least one year.
  • the invention provides a polymer formed by polymerization of one or more methylene beta-diketone monomers or a polymerizable composition thereof.
  • the polymers of the invention are useful as a sealant, a coating, a textile fiber, a water-treatment polymer, an ink carrier, a paint carrier, a packaging film, a molding, a medical polymer, a polymer film, a polymer fiber, or a polymer sheet.
  • the polymers of the invention have repeat units of the formula: wherein R and R' are independently Q-C15 alkyl, C 2 -C 15 alkenyl, halo-(Ci-Ci 5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -Ce cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci 5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C 1 -C 15 alkyl, halo-(Ci-Ci 5 alkyl), C3-C6 cycloalkyl, halo-(C 3 -C 6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl, ary
  • the invention provides an oligomeric complex prepared by reacting a beta-diketone with a source of formaldehyde; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of an acidic or non-acidic solvent.
  • the oligomeric complex has between 2 and 12 repeat units having the structural formula:
  • R and R' are independently Q-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-Q
  • the invention provides a methylene beta-diketone monomer prepared according to the methods of the invention.
  • Figures 1 and 2 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of 5,5-dimethylhexane-2,4-dione and formaldehyde.
  • Figure 3 depicts an NMR spectrum demonstrating evidence of a methylene diketone reaction product formed by the reaction of heptane-3,5-dione with formaldehyde.
  • Figure 4 depicts an NMR spectrum demonstrating evidence of a methylene beta-diketone reaction product formed by the reaction of 5-methylhexane-2,4-dione with formaldehyde.
  • Figures 5 and 6 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of l-phenylbutane-l,3-dione with formaldehyde.
  • Figure depicts is an NMR spectrum demonstrating evidence of a methylene diketone reaction product formed by the reaction of l,3-diphenylpropane-l,3-dione with formaldehyde.
  • Figures 8 and 9 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of nonane-4,6-dione with formaldehyde.
  • the present invention provides new and nonobvious improvements and modifications in the use and application of the Knoevenagel reaction in order to produce methylene beta-diketone monomers:
  • reaction scheme shows a direct condensation reaction
  • an intermediary species oligomeric complex
  • the oligomeric complex may then be cracked to yield the monomer product.
  • the reaction scheme may also yield side reactions and undesired products, and unreacted starting material from which the methylene beta-diketone monomers are subsequently isolated.
  • beta-diketone refers to a compound having the core formula— -C(0)-CH 2 -C(0) .
  • reaction complex refers to the materials which result after reacting a beta-diketone starting material with a source of formaldehyde.
  • reaction complexes may comprise, without limitation, methylene beta-diketone monomers, oligomeric complexes, irreversible complex impurities, starting materials, or latent acid-forming impurities.
  • reaction vessel refers to any container in which the reactants, solvents, catalysts or other materials may be combined for reaction.
  • Such reaction vessels can be made of any material known to one of skill in the art such as metal, ceramic or glass.
  • vapor phase refers to a gaseous phase which may comprise, without limitation, vaporized methylene beta-diketone monomer, vaporized starting materials; vaporized solvents, or vaporized impurities.
  • the term “recovering” or “obtaining” or “isolating” refers to the removal of the monomer from the reaction mixture, vapor phase, or condensed vapor phase by one of the methods described herein, although the desired product may not be in a purified form.
  • the term “crack” is also used to indicate depolymerization of an oligomeric complex.
  • the desired methylene beta-diketone monomer may be obtained by “cracking" an oligomeric complex found in the reaction complex.
  • sterically hindered refers to a compound in which the size of groups within the molecule prevents chemical reactions that are observed in related smaller molecules.
  • volatile and “non-volatile” refers to a compound which is capable of evaporating readily at normal temperatures and pressures, in the case of volatile; or which is not capable of evaporating readily at normal temperatures and pressures, in the case of non-volatile.
  • energy transfer means refers to a means which is capable of volatizing a reaction complex, usually by, but not limited to, rapidly heating the reaction complex to temperatures from about 150°C to about 300°C.
  • energy transfer means include, but are not limited to, heat transfer agents, heat transfer surfaces, lasers, and sources of radiation.
  • heat transfer agent refers to a material which is capable of achieving a high temperature and transferring that temperature to a reaction mixture.
  • heat transfer agents are typically able to reach temperatures from about 150°C to about 300°C and include, but are note limited to silica, silicone oil, mineral oil, a petroleum based heat transfer oil or a synthetic chemical based heat transfer oil.
  • the heat transfer agent can be pre-formed reaction complex.
  • pre-formed reaction complex refers to a reaction complex as defined herein which is prepared by reacting step (a) as described herein in advance of the vaporization step (b).
  • Such pre-formed reaction complexes can be formed up to a year, up to six months, up to 3 months, up to 1 month, up to 2 weeks, up to 1 week, up to 3 days, or up to 1 day in advance of the vaporization step (b).
  • the vaporization step (b) is performed on a newly prepared reaction complex.
  • the pre-formed reaction complex can refer to an oligomeric complex as defined herein.
  • the term "substantial absence” as in “substantial absence of acidic solvent” refers to a reaction mixture comprising less than 1% by weight of the particular component as compared to the total reaction mixture. In certain embodiments, a “substantial absence” refers to less than 0.7%, less than 0.5%, less than 0.4%m less than 0.3%, less than 0.2% or less than 0.1% by weight of the of the particular component as compared to the total reaction mixture. In certain other embodiments, a “substantial absence” refers to less than 1.0%, less than 0.7%, less than 0.5%, less than 0.4%m less than 0.3%, less than 0.2% or less than 0.1% by volume of the of the particular component as compared to the total reaction mixture.
  • the term "stabilized,” e.g., in the context of “stabilized” molecules of the invention or compositions comprising same, refers to the tendency of the molecules of the invention (or their compositions) to substantially not polymerize with time, to substantially not harden, form a gel, thicken, or otherwise increase in viscosity with time, and/or to substantially show minimal loss in cure speed (i.e., cure speed is maintained) with time.
  • shelf-life e.g., as in the context of the molecules of the invention having an improved “shelf-life,” refers to the molecules of the invention which are stabilized for a given period of time, e.g., 1 month, 6 months, or even 1 year or more.
  • Methylene beta-diketone monomers in accordance with the present invention may be made by a modified Knoevenagel condensation reaction of a beta-diketone with formaldehyde under suitable reaction conditions.
  • the general reaction scheme is provided below.
  • Methylene beta-diketone monomers in one aspect, provides a methylene beta-diketone monomer having the structural formula:
  • Ri and R 2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci 5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci 5 alkyl), C 3 -C 6 cycloalkyl, halo-(C 3 -C 6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci 5 alkyl), aryl, aryl -(C 1 -C15 alkyl), heteroaryl
  • the invention provides a methylene beta-diketone monomer having the structural formula:
  • Ri and R 2 are independently Q-C6 alkyl, halo-(Ci-C6 alkyl), C 3 -C6 cycloalkyl, aryl, or heteroaryl, each of which may be optionally substituted by halo or Ci-C 6 alkoxy.
  • the invention provides a methylene beta-diketone monomer having the structural formula: wherein each instance of Ri and R 2 are independently Ci-C 6 alkyl or aryl.
  • the reaction for making methylene beta-diketone monomers of the invention includes at least two basic reactants: a beta-diketone precursor and a source of formaldehyde.
  • the methylene beta-diketone precursors in accordance with exemplary embodiments disclosed herein include beta-diketones able to undergo a condensation reaction at the alpha carbon.
  • Beta-diketone precursors include, but are not limited to, molecules having the structural formula:
  • Ri and R 2 are independently C1-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci 5 alkyl), C 3 -C 6 cycloalkyl, halo-(C 3 -C 6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci 5 alkyl), aryl, aryl -(C 1 -C15 alkyl), heteroaryl
  • heterocyclyl heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci 5 alkoxy, C 1 -C 15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
  • the present invention contemplates the following specifically identified beta-diketone precursors: l,3-dimefhyl-propane-l,3- diones, l,3-diethyl-propane-l,3-diones, l-ethyl-3-methyl-propane-l,3-diones, 1,3- dipropyl-propane-l,3-diones, l,3-dibutyl-propane-l,3-diones, and 1,3-diphenyl- propane-l,3-diones, among others.
  • the beta-diketone precursor may be derived or obtained from any source, including any commercial source, derived from nature, other compounds, synthesized by other processes, etc.
  • the beta-diketone precursors are obtained from "green" sources.
  • the beta-diketone precursors can be derived from biological sources, such as via fermentation production systems whereby microorganisms generate the beta-diketone precursors is direct metabolic byproducts of fermentation— or whereby the microorganisms generate metabolic byproducts of fermentation that can be then converted inexpensively to the desired beta- diketone precursors.
  • fermentation production systems are well-known in the art and may utilize either— or both— microorganisms derived from nature or engineered microorganisms that are specifically designed to produce the desired beta- diketone precursors products, e.g., recombinant or engineered Escherichia coli.
  • the beta-diketone precursor is reacted with a source of formaldehyde.
  • the methods of the invention also contemplate any suitable source of formaldehyde.
  • the formaldehyde may be synthesized, derived from another chemical species (e.g., paraformaldehyde), or obtained from nature or from some other suitable source.
  • the formaldehyde is introduced in the form of a gas.
  • Commercial sources of formaldehyde and paraformaldehyde are readily available, which may include, for example, trioxane and formalin (e.g., aqueous formaldehyde).
  • the source of formaldehyde may be paraformaldehyde, formalin, trioxane or gaseous formaldehyde.
  • the formaldehyde is obtained from paraformaldehyde.
  • the source of formaldehyde is paraformaldehyde that is thermally degraded to formaldehyde in the reaction vessel. It is envisioned that other means of providing formaldehyde to the reaction vessel may be utilized, for example, a stream of gaseous formaldehyde.
  • the methods of preparing the methylene beta-diketone takes place in the presence of a suitable catalyst.
  • a suitable catalyst it is envisioned that certain reactions may not required the presence of a catalyst.
  • the catalysts that may be used include, but are not limited to, basic catalysts such as potassium acetate, sodium acetate, zinc acetate, zinc diacetate dihydrate, aluminum acetate, calcium acetate, magnesium acetate, magnesium oxide, copper acetate, lithium acetate, aluminum oxide, or zinc oxide.
  • basic catalysts such as potassium acetate, sodium acetate, zinc acetate, zinc diacetate dihydrate, aluminum acetate, calcium acetate, magnesium acetate, magnesium oxide, copper acetate, lithium acetate, aluminum oxide, or zinc oxide.
  • the catalysts include, but are not limited to, acidic catalysts such as paratoluene sulfonic acid, dodecylbenzene sulfonic acid, boron trifluoride, zinc perchlorate, sulfated zirconium oxide, sulfated titanium oxide, lithium chloride, boron trifluoride etherate, ferric sulfate, zirconium oxychloride, cupric chloride, titanium tetrachloride, or zinc chloride.
  • acidic catalysts such as paratoluene sulfonic acid, dodecylbenzene sulfonic acid, boron trifluoride, zinc perchlorate, sulfated zirconium oxide, sulfated titanium oxide, lithium chloride, boron trifluoride etherate, ferric sulfate, zirconium oxychloride, cupric chloride, titanium tetrachloride, or zinc chloride.
  • Still other exemplary catalysts are heterogeneous catalysts. Still other exemplary catalysts are enzyme catalysts.
  • An exemplary enzyme is Novozym ® 435 available from Novozyme. Novozym 435 is an immobilized granulate, non-specific lipase particularly useful for ester production.
  • Neutral catalysts can also include silica and other insoluble surface-active agents.
  • amphoteric catalysts can include, but are not limited to, aluminum oxide, aluminum acetate, zinc acetate, magnesium acetate, and zinc oxide.
  • the present inventors have surprisingly and unexpectedly found that no catalyst is required to conduct the synthesis reaction of the invention.
  • the reaction can be conducted with all of the reactants added to the reaction vessel at the start of the reaction prior to adding heat.
  • the source of formaldehyde in this embodiment is preferably solid
  • This reaction surprisingly can be run rapidly and in a continuous mode and unexpectedly avoids the formation of— or substantially minimizes the formation of— deleterious side products, unwanted polymerization complexes and degradation of the monomer products.
  • the present invention contemplates that the synthesis reaction includes an acidic or non-acidic solvent, or optionally no solvent at all.
  • Non-acidic solvents can include, but are not limited to, tetrahydrofuran, chloroform, dichloromethane, toluene, heptane, ethyl acetate, n-butyl acetate, dibutyl ether and hexane.
  • Acidic solvents can include, but are not limited to acetic acid and propionic acid.
  • the acidic solvent is added just prior to recovery. In certain other embodiment, optionally no solvent is needed.
  • This zero- solvent approach will not only decrease the overall cost of production but will also help to lessen any negative impact on the environment caused by the methods of the invention, i.e., provides an environmentally-friendly approach to the synthesis of 2- methylene-l,3-disubstituted-propane-l,3-diones.
  • An advantage of this condition is the avoidance or minimization of the formation of impurities, e.g., ketals and other latent acid-forming species.
  • the present inventors have surprisingly and unexpectedly found that the synthesis reaction of the invention may be conducted in the absence of both a solvent and a catalyst.
  • the reaction can be conducted with all of the reactants added to the reaction vessel at the start of the reaction prior to adding heat and in the absence of a solvent.
  • the source of formaldehyde in this embodiment is preferably solid paraformaldehyde, and is added along with the other reactants, including the malonic ester, prior to adding heat.
  • This reaction surprisingly can be run rapidly and in a continuous mode and unexpectedly avoids the formation of— or substantially minimizes the formation of— deleterious side products, unwanted polymerization complexes and degradation of the monomer products.
  • Certain embodiments of the present invention provide monomers that are amenable to anionic polymerization. Therefore, to prevent unwanted polymerization and extend shelf life, certain exemplary embodiments include suitable acidic stabilizers, for example, trifhioromefhane sulfonic acid, maleic acid, methane sulfonic acid, difluoro acetic acid, trichloroacetic acid, phosphoric acid, dichloroacetic acid, chlorodifluoro or like acid. Acidic stabilizers can include any material which can be added to the monomer or polymer compositions to extend shelf-life, e.g., by up to, for example, 1 year or more.
  • Such acidic stabilizers may have a pKa in the range of, for example, between about -15 to about 5, or between about -15 to about 3, or between about -15 to about 1, or between -2 to about between about -2 to about 2, or between about 2 to about 5, or between about 3 to about 5.
  • the starting precursor is reacted with paraformaldehyde in the presence of a catalyst (e.g., zinc acetate dehydrate) at 60 °C -130 °C (e.g., 100 °C) for at least about 30 minutes.
  • a catalyst e.g., zinc acetate dehydrate
  • the resulting intermediate material e.g., oligomeric complex
  • the resulting crude monomer is then purified, for example by distillation, fractional distillation or other separation methods.
  • reaction complex For a typical lab scale reaction: a 3-neck 250 mL round bottom reaction flask was equipped with an overhead stirrer, a heating mantle, and a temperature probe connected to a temperature controller. The reaction flask was adequately vented to the back of the hood to reduce the possibility of pressure build-up. The beta-diketone (precursor), paraformaldehyde (1.8 equiv) and zinc acetate (0.001 equiv) were added to the reaction flask. The contents of the flask were mixed for approximately 2 minutes prior to the application of heat. After the initial mixing period the temperature controller was set to 100 °C. The heterogeneous reaction mixture was allowed to heat with the temperature for dissolution and onset of exotherm being noted. Once a rapid increase in temperature was observed, heating was discontinued. Once the exotherm subsided, the heating mantle was immediately removed and the reaction mixture (herein "reaction complex”) was allowed to cool to room
  • 4-neck suitable round bottom flask was equipped with a mechanical stirrer, heating mantle, a thermocouple connected to a temperature controller, an addition funnel, a Claisen adapter, and a vacuum adapter connected to a receiver one-neck round bottom flask which was placed in an ice-bath.
  • the system was evacuated to low pressure (1- 250 mmHg).
  • the oligomeric mixture was added to the addition funnel.
  • the reaction flask was then applied via the connected heating mantle to 150-270 °C. Once the temperature inside the flask reached the desired range, a drop-wise addition of the oligomer (reaction complex) to reaction flask was started. The addition rate was maintained so that the set temperature was maintained in the desired range.
  • This general reaction scheme was utilized to provide the examples provided herein. Due to the wide variety of example obtained, it is envisioned that this general reaction scheme can be utilized to provide a wide array of methylene beta-diketone monomers as set forth herein. Further, it is envisioned that modifications can be made to this general reaction scheme in order to improve efficiencies and purity of the product obtained.
  • the invention provides a method of preparing methylene beta-diketone monomers according to the reaction scheme disclosed herein.
  • the method for preparing the methylene beta-diketone monomers comprises: a) reacting a beta-diketone reactant having the structural formula:
  • the reaction may be initiated at temperatures between about 60 °C to about 130 °C, at atmospheric pressure. It is contemplated that the reaction conditions may be modified depending on the source of formaldehyde. For example, when paraformaldehyde is utilized within the reaction vessel, the initial temperature must be high enough to make free formaldehyde available for the reaction. If another source of formaldehyde is utilized, those having skill in the art will appreciate that the reaction conditions may be modified accordingly. Exemplary sources include paraformaldehyde, formalin, trioxane, gaseous formaldehyde, or any reaction or process in which formaldehyde is liberated.
  • the methylene beta-diketone monomer may be isolated from the reaction complex by contacting the reaction complex, or a portion thereof, with an energy transfer means to produce a vapor phase including the methylene beta- diketone monomer; and collecting the methylene beta-diketone monomer from the vapor phase.
  • the methylene beta-diketone monomer may be isolated from the reaction complex immediately, or the reaction complex may be stored, preferably refrigerated, until a later time.
  • the reaction complex is not acid stabilized prior to isolating the methylene beta-diketone monomer.
  • the reaction complex may be heated to a vapor phase and condensed in order to isolate the methylene beta-diketone monomer.
  • the reaction complex may be heated to a temperature between about 130 °C and about 300 °C.
  • the reaction complex, or a portion thereof may come in contact with an energy transfer means in order to facilitate isolation of the monomer.
  • the reaction complex, or portion thereof may be vaporized in a very short time, for example less than 15 minutes, preferably less than 1 minute, more preferably less than 30 seconds, and less than 1 second. Certain exemplary embodiments contemplate vaporizing the reaction complex in a continuous manner as it is formed during the reaction step.
  • Exemplary energy transfer means include a heat transfer agent, a heat exchanger, a laser, microwave energy, sonic energy, electromagnetic energy, and a source of radiation, or any combination thereof.
  • the energy transfer means operates to quickly vaporize the reaction complex (or portion thereof) to permit isolation of the monomer product.
  • an oligomeric complex may be formed, and the energy transfer means is utilized to "crack" or depolymerize the oligomer to allow isolation of the monomer.
  • the oligomeric complex may include oligomers of 2-12 units able to provide monomer product upon crack.
  • the heat transfer agent is a heated inert gas, one or more metal beads, one or more glass beads, one or more porcelain beads, sand, silica, silicone oil, mineral oil, a petroleum based heat transfer oil, a synthetic chemical based heat transfer oil, or a pre-formed portion of the reaction complex.
  • the heat exchanger is a shell and tube heat exchanger, a plate heat exchanger, and adiabatic wheel heat exchanger, a finned pipe heat exchanger, a plate fin heat exchanger, or a scraped surface heat exchanger.
  • the vapor phase of the reaction complex is condensed, and the condensate is subject to one or more further separation processes.
  • the separation process may include any of simple distillation, fractional distillation, flash distillation, steam distillation, vacuum distillation, short path distillation, thin-film distillation, reactive distillation, pervaporation, extractive distillation, flash evaporation, rotary evaporation, liquid/liquid extraction, centrifuging, or any combination thereof, and other techniques known to those having skill in the art.
  • the methylene beta-diketone monomers of the invention can be incorporated into any number of compositions and products including but not limited to reactive monomer-based compositions, reactive oligomer-based compositions and reactive polymer-based compositions.
  • Exemplary compositions can be analyzed by placing a drop of a monomer composition on a substrate (for example a glass slide or 4"xl" polycarbonate sample). Another glass slide or piece of polycarbonate is pressed on top over the monomer- covered area. The time is then immediately recorded from pressing the top-slide till the two slides are bonded tightly.
  • the exemplary composition is capable of bonding glass to a substrate in less than about 90 seconds, less than about 60 seconds, less than about 30 seconds or less than about 15 seconds.
  • the exemplary composition is capable of bonding polycarbonate to a substrate in less than about 90 seconds, less than about 60 seconds, less than about 45 seconds or less than about 30 seconds.
  • exemplary compositions can be analyzed by mixing 0.5 ml of monomer with 0.3 ml of 3% tertiary butyl ammonium fluoride (TBAF) in Dibutyl Phthalate solution. The time is recorded from adding the TBAF solution till the mixture become solid with vigorous stirring or mixing. In such embodiments, said composition solidifies upon addition of 3% tertiary butyl ammonium fluoride (TBAF) in Dibutyl Phthalate solution in less than about 15 seconds, less than about 10 seconds, or less than about 7 seconds.
  • TBAF tertiary butyl ammonium fluoride
  • the exemplary compositions can be analyzed by placing 0.5 ml of monomer into a test tube and cap with a cork stopper and keeping the test tubes containing monomers at 25°C, or in ovens at 55°C or 82°C.
  • the storage stability test is performed at atmospheric pressure. Time is recorded when the monomer became a gel or solid.
  • said composition remains stable at 25°C and at atmospheric pressure for more than 10 days, more than 15 days, more than 20 days, more than 25 days or more than 30 days.
  • said composition remains stable at 82°C and at atmospheric pressure for more than about 2 hours, more than about 3 hours, or more than about 4 hours.
  • compositions include, but are not limited to an adhesive, a coating, a sealant, a composite, or a surfactant.
  • polymer products include, but are not limited to, a sealant, a thermal barrier coating, a textile fiber, a water-treatment polymer, an ink carrier, a paint carrier, a packaging film, a molding, a medical polymer, a polymer film, a polymer fiber or a polymer sheet.
  • the exemplary compositions may be formulated to include one or more materials to extend the shelf-life as well as control the onset of cure of the materials.
  • the compositions are formulated such that the composition is stable for at least 1 month, or for at least 2 months, or for at least 3 months, or for at least 4 months, or for at least 5 months, or for at least 5-10 months, or for at least 10-20 months, or for at least 20-30 months.
  • the adhesive composition comprising the methylene beta-diketone monomers or other commercial compositions or products, are stable for at least one year.
  • Such formulation materials include acidic stabilizer, volatile acid stabilizers, acidic gases, free radical stabilizers, sequestering agents, cure accelerators and rheology modifiers.
  • Exemplary embodiments contemplate any suitable acidic stabilizer known in the art, including, for example, trifluoromethane sulfonic acid, maleic acid, methane sulfonic acid, difluoro acetic acid, trichloroacetic acid, phosphoric acid, dichloroacetic acid, chlorodifluoro or like acid.
  • Acidic stabilizers can include any material which can be added to the monomer or polymer compositions to extend shelf-life, e.g., by up to, for example, 1 year or more.
  • Such acidic stabilizers may have a pKa in the range of, for example, between about -15 to about 5, or between about -15 to about 3, or between about -15 to about 1, or between -2 to about between about -2 to about 2, or between about 2 to about 5, or between about 3 to about 5.
  • Volatile acid stabilizers include any material which can be added to the monomer or polymer compositions to extend shelf-life and stabilize the vapor phase above the composition upon storage, e.g., acidic gases. Such volatile acid stabilizers may have a boiling point, for example, less than about 200°C; less than about 170°C; or less than about 130°C.
  • Acidic gases include any gaseous material which can be added to the monomer or polymer compositions to extend shelf-life and stabilize the vapor phase above the composition upon storage.
  • Such acid gases can include, but are not limited to, S0 2 or BF 3 .
  • acidic stabilizer can be present in a concentration of about 0.1 ppm to about 100 ppm; about 0.1 ppm to about 25 ppm; or about 0.1 ppm to about 15 ppm.
  • Free radical stabilizers can include any material capable of stabilizing or inhibiting free radical polymerization of the material upon standing.
  • the free radical stabilizers are phenolic free radical stabilizers such as, HQ (hydroquinone), MEHQ (methyl- hydroquinone), BHT (butylated hydroxtoluene) and BHA (butylated hydroxyanisole).
  • the free radical stabilizers are present in a concentration of 0.1 ppm to 10,000 ppm; 0.1 ppm to 3000 ppm; or 0.1 ppm to 1500 ppm.
  • the free radical stabilizers are present in a concentration of 0.1 ppm to 1000 ppm; 0.1 ppm to 300 ppm; or 0.1 ppm to 150 ppm.
  • Sequestering agents include any material capable of enhancing the bonding of materials containing acid salts such as paper or wood.
  • sequestering agents include, but are not limited to crown ethers, silyl crowns, calixarenes and
  • Sequestering agents also enhance the utility of surface accelerators that are acid salts applied to surfaces to control the rate of cure of the materials.
  • Cure accelerators include any material capable of speeding the rate of cure of the methylene beta-diketone monomers. Cure accelerators also include any material capable of speeding the cure through volume of the applied composition. Such cure accelerators include but are not limited to sodium or potassium acetate; acrylic, maleic or other acid salts of sodium, potassium lithium copper and cobalt; salts such as tetrabutyl ammonium fluoride, chloride, or hydroxide; or chemically basic materials such as amines and amides, or salts of polymer bond acids, benzoate salts, 2,4-pentanedionate salts, sorbate salts , or propionate salts. Such cure accelerators can be added directly to the exemplary compositions or applied to the material to be bonded prior to addition of the composition.
  • Rheology modifiers include any material which can modify the viscosity of the exemplary compositions as well as thixotropic properties for greater utility in certain applications.
  • Rheology modifiers include, but are not limited to,
  • the exemplary compositions may include tougheners.
  • tougheners include, but are not limited to, acrylic rubbers; polyester urethanes; ethylene-vinyl acetates; fluorinated rubbers; isoprene-acrylonitrile polymers;
  • the tougheners include those disclosed in U.S. Pat. No.
  • the toughener is an elastomeric polymer which is a copolymer of methyl acrylate and ethylene, manufactured by DuPont, under the name of VAMAC, such as VAMAC N123 and VAMAC B-124.
  • VAMAC N123 and VAMAC B-124 are reported by DuPont to be a master batch of ethylene/acrylic elastomer.
  • the toughener may be the DuPont materials called VAMAC B-124, N123, VAMAC G, VAMAC VMX 1012 or VCD 6200.
  • the toughener may be a rubber toughening component having (a) reaction products of the combination of ethylene, methyl acrylate and monomers having carboxylic acid cure sites, (b) dipolymers of ethylene and methyl acrylate, and combinations of (a) and (b), which once the reaction products and/or dipolymers are formed are then substantially free of processing aids, such as the release agents octadecyl amine (reported by DuPont to be available commercially from Akzo Nobel under the tradename ARMEEN 18D), complex organic phosphate esters (reported by DuPont to be available commercially from R.T. Vanderbilt Co., Inc. under the tradename VANFRE VAM), stearic acid and/or polyethylene glycol ether wax, and anti-oxidants, such as substituted diphenyl amine (reported by DuPont to be available commercially from Uniroyal Chemical under the tradename
  • processing aids such as the release agents octadecyl amine (re
  • compositions containing methylene beta-diketone monomer may also optionally include other additives, such as plasticizing agents, thixotropic agents, natural or synthetic rubbers, filler agents, and reinforcing agents, etc.
  • additives are well known to those skilled in the art.
  • the exemplary compositions containing methylene beta-diketone monomer may optionally include at least one plasticizing agent that imparts flexibility to the polymer formed from the methylene beta-diketone monomer.
  • the plasticizing agent preferably contains little or no moisture and should not significantly affect the stability or polymerization of the monomer.
  • plasticizers are useful in polymerized compositions to be used in any application in which flexibility of the adhesive or polymer product is desirable.
  • plasticizers include, without limitation, acetyl tributyl citrate, dimethyl sebacate, triethyl phosphate, tri (2-ethylhexyl)phosphate, tri (p- cresyl) phosphate, glyceryl triacetate, glyceryl tributyrate, diethyl sebacate, dioctyl adipate, isopropyl myristate, butyl stearate, lauric acid, trioctyl trimellitate, dioctyl glutarate, and mixtures thereof.
  • Preferred plasticizers are tributyl citrate and acetyl tributyl citrate.
  • suitable plasticizers include polymeric plasticizers, such as polyethylene glycol (PEG) esters and capped PEG esters or ethers, polyester glutarates and polyester adipates.
  • plasticizing agents in amounts less than about 60 weight %, or less than about 50 weight %, or less than about 30 weight , or less than about 10 weight %, or less than about 5 weight %, or less than about 1 weight % or less, provides increased film strength (e.g., toughness) of the polymerized monomer over polymerized monomers not having plasticizing agents.
  • compositions containing methylene beta-diketone monomer may also optionally include at least one thixotropic agent, i.e., the property of exhibiting a high fluidity during deformation by force of a sprayer, roller or trowel, but losing the fluidity when left at rest.
  • thixotropic agents are known to the skilled artisan and include, but are not limited to, silica gels such as those treated with a silyl isocyanate. Examples of suitable thixotropic agents are disclosed in, for example, U.S. Pat. Nos.: 4,720,513 or 4,510,273, the disclosures of which are hereby incorporated in their entireties.
  • the exemplary compositions containing methylene beta-diketone monomer may also optionally include at least one natural or synthetic rubber to impart impact resistance, which is preferable especially for industrial compositions of the present invention.
  • Suitable rubbers are known to the skilled artisan. Such rubbers include, but are not limited to, dienes, styrenes, acrylonitriles, and mixtures thereof. Examples of suitable rubbers are disclosed in, for example, U.S. Pat. Nos. 4,313,865 and 4,560,723, the disclosures of which are hereby incorporated in their entireties.
  • compositions containing methylene beta-diketone monomer may also optionally comprise one or more other reinforcing agents (e.g., fibrous reinforcements) other than natural or synthetic rubber to impart impact resistance and/or to impart structural strength or to provide shape or form.
  • fibrous reinforcements include PGA microfibrils, collagen microfibrils, cellulosic microfibrils, and olefinic microfibrils.
  • suitable fibrous reinforcement include PGA microfibrils, collagen microfibrils, cellulosic microfibrils, and olefinic microfibrils.
  • the compositions may also contain colorants such as dyes, pigments, and pigment dyes.
  • suitable colorants include 6-hydroxy-5-[(4- sulfophenyl)axo]-2-naphthalene-sulfonic acid (FD+C Yellow No. 6); 9-(o- carboxyphenyl)-6-hydroxy-2,4,5,7-tetraiodo-3H-xanthen-3-one monohydrate (FD+C Red No. 3); and 2-(l,3-dihydro-3-oxo-5-sulfo-2H-indol-2-ylidene)-2,3-dihydro-3- oxo-lH-indo le-5-sulfonic acid (FD+C Blue No. 2), wherein the suitable colorant should not destabilize the monomer.
  • compositions containing methylene beta-diketone monomer may also optionally include at least one thickening agent.
  • suitable thickeners include, for example, polycyanoacrylates, polylactic acid, poly-l,4-dioxa-2-one, polyoxalates, polyglycolic acid, lactic-glycolic acid copolymers, polycaprolactone, lactic acid- caprolactone copolymers, poly-3-hydroxybutyric acid, polyorthoesters, polyalkyl acrylates, copolymers of alkylacrylate and vinyl acetate, polyalkyl methacrylates, and copolymers of alkyl methacrylates and butadiene.
  • alkyl methacrylates and acrylates are poly(2-ethylhexyl methacrylate) and poly(2-ethylhexyl acrylate), also poly(butylmethacrylate) and poly(butylacrylate), also copolymers of various acrylate and methacrylate monomers, such as poly(butylmethacrylate-co- methylacrylate).
  • difunctional monomelic cross-linking agents may be added to the monomer compositions of this invention.
  • Such crosslinking agents are known.
  • U.S. Pat. No. 3,940,362 to Overhults which is hereby incorporated in its entirety by reference, discloses such crosslinking agents.
  • compositions and additives contemplated herein include additional stabilizers, accelerators, plasticizers, fillers, opacifiers, inhibitors, thixotrophy conferring agents, dyes, fluorescence markers, thermal degradation reducers, adhesion promoters, thermal resistance conferring agents and combinations thereof, and the like, some of which are exemplified by U.S. Pat. Nos. 5,624,669; 5,582,834;
  • compositions and/or products Depending on whether the composition is a monomer-based composition (e.g. , inks, adhesives, coatings, sealants or reactive molding) or a polymer-based composition (e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants), one having ordinary skill in the art will have the knowledge and skill by which to formulate such compositions and/or products without undue experimentation having suitable amounts, levels and combinations of the above types of additives and components.
  • a monomer-based composition e.g. , inks, adhesives, coatings, sealants or reactive molding
  • polymer-based composition e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants
  • polymerizable compositions may be formulated to include additives such as acidic stabilizers, a free radical stabilizers, a sequestering agents, a cure accelerators, rheology modifiers, a plasticizing agents, a thixotropic agents, natural rubbers, synthetic rubbers, filler agents, reinforcing agents and the like.
  • additives are provided at levels sufficient to achieve the desired results which can readily be determined by those having skill in the art.
  • an acidic stabilizer is present in a concentration of about 0.1 ppm to about 100 ppm, about 0.1 ppm to about 25 ppm, or about 0.1 ppm to about 15 ppm, by weight of the composition.
  • a free radical stabilizer is present in a concentration selected from about 0.1 ppm to about 10000 ppm, about 0.1 ppm to about 3000 ppm, about 0.1 ppm to 1500 ppm, about 0.1 ppm to about 1000 ppm, about 0.1 ppm to about 300 ppm, or about 0.1 ppm to about 150 ppm, by weight of the composition.
  • a sequestering agent such as a crown ether, a silyl crown, a calixarene, a polyethylene glycol, or a combination thereof may be utilized.
  • a cure accelerator such as sodium acetate, potassium acetate, tetrabutyl ammonium fluoride, tetrabutyl ammonium chloride, tetrabutyl ammonium hydroxide, a benzoate salt, a 2,4-pentanedionate salt, a sorbate salt, and a propionate salt, may be utilized.
  • a rheology modifier such as
  • hydroxyethylcellulose ethyl hydroxyethylcellulose, methylcellulose, a polymeric thickener, and pyrogenic silica, may be utilized.
  • Exemplary polymerizable compositions are stable at 25°C and at atmospheric pressure for more than 10 days, more than 15 days, more than 20 days, more than 25 days, or more than 30 days. Certain exemplary embodiments may exhibit a shelf life of up to one year, or up to two years. Certain exemplary embodiments may be tested for stability at elevated temperature, e.g., 82°C, at atmospheric pressure. Certain exemplary embodiments may exhibit elevated temperature stability for more than 2 hours.
  • Certain exemplary embodiments disclosed herein relate to polymers and polymer products formed by polymerization of the polymerizable compositions comprising the methylene beta-diketone monomers.
  • Polymers and polymer products envisioned include coatings, paints, fibers, composites, textile fibers, water-treatment polymers, ink carriers, paint carriers, packaging films, moldings, medical polymers, polymer films, polymer fibers, polymer sheets, and the like.
  • the methylene beta-diketone monomers are capable of supporting a vast array of products due to the activity of the methylene group and the ability to vary the functional groups R, R as shown in the structure of the repeating unit:
  • R and R' are independently Q-C15 alkyl, C 2 -C 15 alkenyl, halo-(Ci-Ci 5 alkyl), C3-C5 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci 5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C 1 -C 15 alkyl, halo-(Ci-Ci 5 alkyl), C 3 -C6 cycloalkyl, halo-(C 3 -C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C
  • the reaction of the precursor beta-diketone with the source of formaldehyde may result in an oligomeric complex which is subsequently cracked to obtain the desired methylene beta-diketone monomer.
  • Certain oligomeric complexes are capable of being efficiently vaporized or "cracked" into high purity monomers of 2- methylene-l,3-disubstituted-propane-l,3-dione by rapid vaporization as described herein.
  • the invention provides an oligomeric complex prepared by reacting a l,3-disubstituted-propane-l,3-dione with a source of formaldehyde; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of an acidic or non-acidic solvent.
  • the oligomeric complex comprises between 2 and 12 repeat units that are able to yield monomer upon cracking
  • the invention further provides an oligomeric complex prepared by reacting a l,3-disubstituted-propane-l,3-dione with a source of formaldehyde in a substantial absence of acidic solvent; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of a non- acidic solvent.
  • the substantial absence of acidic solvent represents less than 1.0%, less than 0.5%, less than 0.2% or less than 0.1% by weight acidic solvent as compared to the total composition of the reaction mixture.
  • Potassium te/t-butoxide (97.5 g, 0.87 mol) was added to a 1 L 3-neck flask containing 150 mL dry dimethyl formamide and equipped with a mechanical stirrer and a thermocouple. The temperature was raised to 50 °C with stirring. Methyl butyrate (200 mL, 1.8 mol) and 2-pentanone (62 mL, 0.58 mol) were added as a mixture via 500 mL addition funnel over 2.5 h at 50 °C during which the yellow slurry turned to a clear brown solution. The reaction mixture was stirred for an additional 5 h at 50 °C at which point heating was turned off and the reaction mixture was allowed to stir for 14 h at room temperature.
  • the reaction mixture was quenched by slow addition into a 1 M HCl aq. solution (500 mL) at 0 °C, and the pH was adjusted with 1 M HCl aq. solution to about 5.
  • the reaction slurry was extracted with heptane (4 x 400 mL).
  • the combined organic layers were concentrated to 300 mL under reduced pressure.
  • the residue was washed with water (5 x 400 mL) followed by a brine wash.
  • the enriched organic layer was further concentrated under reduced pressure to afford a yellowish liquid which was purified by distillation at 65 °C, 2 Torr to afford 60 g of 85% pure (based on H NMR analysis) material (56% yield) as a clear liquid.
  • the l H NMR spectrum is shown in Figure 8.
  • the peak at 6.2 ppm is consistent with the geminal double bond of the product.
  • the 13C and DEPT-135 spectra are shown in Figure 9.
  • the peak at 129 ppm (CH 2 ) and at 150 ppm (quaternary) are consistent with the geminal double bond of the product.
  • reaction scheme disclosed herein is performed using an appropriate 1,3- disubtituted-propane-l,3-dione and a source formaldehyde to obtain the following monomers.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Adhesives Or Adhesive Processes (AREA)
  • Phenolic Resins Or Amino Resins (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Paints Or Removers (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)
  • Wrappers (AREA)
  • Macromonomer-Based Addition Polymer (AREA)
  • Polymerisation Methods In General (AREA)
  • Sealing Material Composition (AREA)

Abstract

The present invention provides methylene beta-diketone monomers, methods for producing the same, and compositions and products formed therefrom. In the method for producing the methylene beta-diketones of the invention, a beta-diketone is reacted with a source of formaldehyde in a modified Knoevenagel reaction optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form reaction complex. The reaction complex may be an oligomeric complex. The reaction complex is subjected to further processing, which may be vaporization by contact with an energy transfer means in order to isolate the beta-diketone monomer. The present invention further compositions and products formed from methylene beta-diketone monomers of the invention, including monomer-based products (e.g., inks, adhesives, coatings, sealants or reactive molding) and polymer-based products (e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants).

Description

TITLE
METHYLENE BETA-DIKETONE MONOMERS, METHODS FOR MAKING METHYLENE BETA-DIKETONE MONOMERS, POLYMERIZABLE
COMPOSITIONS AND PRODUCTS FORMED THEREFROM CROSS REFERENCE TO RELATED APPLCIATIONS
This application claims priority to Provisional Patent Applications 61/549,104, filed October 19, 2011 ; 61/549,092, filed October 19, 2011 ; and 61/549,152 entitled, filed October 19, 2011 , the contents of which in their entirety are hereby incorporated herein by reference. INCORPORATION BY REFERENCE
All documents cited or referenced herein and all documents cited or referenced in the herein cited documents, together with any manufacturer' s instructions, descriptions, product specifications, and product sheets for any products mentioned herein or in any document incorporated by reference herein, are hereby incorporated by reference, and may be employed in the practice of the invention.
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to a new class of methylene beta-diketone monomers, to methods of producing or synthesizing such monomers, and to the use and application of such monomers as commercial products and compositions, including, for example, monomer-based products (e.g., inks, adhesives, coatings, sealants or reactive molding) and polymer-based products (e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants).
The new monomers relate to a platform of methylene beta-diketone monomers having the general structural formula:
Figure imgf000004_0001
Products produced with such monomers include, for example, polymerizable compositions and polymers formed therefrom, e.g., inks, adhesives, coatings, sealants, reactive moldings, fibers, films, sheets, medical polymers, composite polymers and surfactants. 2. Background
Methylene malonate monomers have been disclosed for example in U.S.
Patent Nos.: U.S. Patent Nos. 2,313,501 ; 2,330,033; 3,221,745; 3,523,097; 3,557, 185; 3,758,550; 3,975,422; 4,049,698; 4,056,543; 4,160,864; 4,931,584; 5,142,098;
5,550,172; 6,106,807; 6,211,273; 6,245,933; 6,420,468; 6,440,461 ; 6,512,023;
6,610,078; 6,699,928; 6,750,298; and Patent Publications 2004/0076601 ;
WO/2012/054616A2; WO2012/054633A2.
As described in certain of those publications, methylene malonates have the potential to form the basis of a large-scale platform of raw materials useful in a wide variety of chemical products.
It is envisioned that methylene beta-diketone monomers and their associated monomeric and polymeric -based products would be useful in industrial, consumer, and medical applications. Specifically, methylene beta-diketone monomers would provide a benefit over other monomers in that the incorporation of a ketone group adjacent to the active methylene group reduces the susceptibility of degradation of the monomer upon utilization or further functionalization. Indeed, unlike many other monomers, methylene beta-diketone monomers and their products can be produced via sustainable routes as well as be designed to be environmentally benign, biologically benign and as such many of the products can be generally regarded as "green."
Thus, there exists a need in the art for methods of synthesizing novel methylene beta-diketone monomers, formulating novel polymerizable compositions, and providing polymer products based on this platform. SUMMARY OF THE INVENTION
The purpose and advantages of the present invention will be set forth in and apparent from the description that follows. Additional advantages of the invention will be realized and attained by the methods and systems particularly pointed out in the written description and claims hereof, as well as from the appended drawings. In one aspect, the invention provides a methylene beta-diketone monomer has a structure:
Figure imgf000006_0001
wherein Ri and R2 are independently C1-Q5 alkyl, C2-C15 alkenyl, halo-(Ci- Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-Cg cycloalkyl), heterocyclyl, heterocyclyl-(Ci- Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Cis alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(d- Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-Cg cycloalkyl), heterocyclyl, heterocyclyl-(Ci- Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by Q- Ci5 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl),
heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In another aspect, the invention provides a method of making a methylene beta-diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula:
Figure imgf000007_0001
under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; and b) isolating a methylene beta-diketone monomer from the reaction complex, wherein the methylene beta-diketone monomer has the structural formula:
Figure imgf000007_0002
wherein each instance of Ri and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by Ci- Cis alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl),
heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In certain embodiments, the methods of the invention herein include the step of isolating the methylene beta-diketone by: i. contacting the reaction complex, or a portion thereof, with an energy transfer means to produce a vapor phase including the methylene beta- diketone monomer; and
ii. collecting the methylene beta-diketone monomer from the vapor phase.
In other embodiments, the methods of the invention herein include isolating the methylene beta-diketone by: i. heating the reaction complex, or a portion thereof, to a temperature between about 130°C and about 300°C to produce a vapor phase including the methylene beta-diketone monomer; and
ii. collecting the methylene beta-diketone monomer from the vapor phase.
In still other embodiments, the methods of the invention are performed under reaction conditions of: a) an initiating temperature of between about 60 °C and about 130 °C; b) atmospheric pressure.
In another aspect, the invention provides a method of preparing a methylene beta- diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula:
Figure imgf000009_0001
under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; b) contacting the reaction complex, or a portion thereof, with an energy transfer means at a temperature between about 150°C and about 300°C to provide the reaction complex, or portion thereof, as a vapor phase; and c) isolating a methylene beta-diketone monomer from the reaction complex or portion thereof, wherein the methylene beta-diketone monomer has the structural formula:
Figure imgf000010_0001
wherein each instance of Ri and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein each instance of Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-Q5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In another aspect, the invention provides a polymerizable composition comprising a methylene beta-diketone monomer of the invention. In certain embodiments, the polymerizable composition is capable of bonding glass to a substrate in a time period of less than about 90 seconds, less than about 60 seconds, less than about 30 seconds, or less than about 15 seconds.
In certain other embodiments, the polymerizable composition comprising a methylene beta-diketone monomer further comprises at least one additive selected from the group consisting of an acidic stabilizer, a free radical stabilizer, a sequestering agent, a cure accelerator, a rheology modifier, a plasticizing agent, a thixotropic agents, a natural rubber, a synthetic rubbers, a filler agent and a reinforcing agent.
In another aspect, the invention provides an adhesive product comprising a methylene beta-diketone monomer of the invention.
In certain embodiments, the adhesive products have a shelf life of at least one year.
In another aspect, the invention provides a polymer formed by polymerization of one or more methylene beta-diketone monomers or a polymerizable composition thereof.
In certain embodiments, the polymers of the invention are useful as a sealant, a coating, a textile fiber, a water-treatment polymer, an ink carrier, a paint carrier, a packaging film, a molding, a medical polymer, a polymer film, a polymer fiber, or a polymer sheet.
In certain other embodiments, the polymers of the invention have repeat units of the formula:
Figure imgf000012_0001
wherein R and R' are independently Q-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-Ce cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In another aspect, the invention provides an oligomeric complex prepared by reacting a beta-diketone with a source of formaldehyde; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of an acidic or non-acidic solvent. In certain embodiments, the oligomeric complex has between 2 and 12 repeat units having the structural formula:
Figure imgf000013_0001
wherein R and R' are independently Q-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-Q5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In still another aspect, the invention provides a methylene beta-diketone monomer prepared according to the methods of the invention.
BRIEF DESCRIPTION OF THE DRAWINGS
So that those having ordinary skill in the art to which the subject invention pertains will more readily understand how to make and use the invention as described herein, preferred embodiments thereof will be described in detail below, with reference to the drawings, wherein: Figures 1 and 2 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of 5,5-dimethylhexane-2,4-dione and formaldehyde.
Figure 3 depicts an NMR spectrum demonstrating evidence of a methylene diketone reaction product formed by the reaction of heptane-3,5-dione with formaldehyde.
Figure 4 depicts an NMR spectrum demonstrating evidence of a methylene beta-diketone reaction product formed by the reaction of 5-methylhexane-2,4-dione with formaldehyde.
Figures 5 and 6 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of l-phenylbutane-l,3-dione with formaldehyde.
Figure depicts is an NMR spectrum demonstrating evidence of a methylene diketone reaction product formed by the reaction of l,3-diphenylpropane-l,3-dione with formaldehyde.
Figures 8 and 9 depict NMR spectra demonstrating evidence of a methylene diketone reaction product formed by the reaction of nonane-4,6-dione with formaldehyde. DETAILED DESCRIPTION OF THE INVENTION
Overview
The present invention provides new and nonobvious improvements and modifications in the use and application of the Knoevenagel reaction in order to produce methylene beta-diketone monomers:
R
Figure imgf000015_0001
2. Cracking at 150-270 °C
Modified Knoevenagel Reaction
While the above reaction scheme shows a direct condensation reaction, it has been discovered that an intermediary species (oligomeric complex) may be formed in certain instances. The oligomeric complex may then be cracked to yield the monomer product. As those having skill in the art will appreciate, the reaction scheme may also yield side reactions and undesired products, and unreacted starting material from which the methylene beta-diketone monomers are subsequently isolated.
Definitions Unless defined otherwise, all technical and scientific terms used herein have the meaning commonly understood by a person skilled in the art to which this invention belongs. The following references provide one of skill with a general definition of many of the terms used in this invention: Singleton et ah, Dictionary of Microbiology and Molecular Biology (2nd ed. 1994); The Cambridge Dictionary of Science and Technology (Walker ed., 1988); The Glossary of Genetics, 5th Ed., R. Rieger et al. (eds.), Springer Verlag (1991); and Hale & Marham, The Harper Collins Dictionary of Biology (1991). As used herein, the following terms have the meanings ascribed to them below, unless specified otherwise.
As used herein, the term "methylene beta-diketone monomer" refers to a compound having the core formula C(0)-C(=CH2)-C(0) .
As used here, the term "beta-diketone" refers to a compound having the core formula— -C(0)-CH2-C(0) .
As used herein, the term "reaction complex" refers to the materials which result after reacting a beta-diketone starting material with a source of formaldehyde. Such reaction complexes may comprise, without limitation, methylene beta-diketone monomers, oligomeric complexes, irreversible complex impurities, starting materials, or latent acid-forming impurities.
As used herein, the term "reaction vessel" refers to any container in which the reactants, solvents, catalysts or other materials may be combined for reaction. Such reaction vessels can be made of any material known to one of skill in the art such as metal, ceramic or glass.
As used herein, the term "vapor phase" refers to a gaseous phase which may comprise, without limitation, vaporized methylene beta-diketone monomer, vaporized starting materials; vaporized solvents, or vaporized impurities.
As used herein, the term "recovering" or "obtaining" or "isolating" refers to the removal of the monomer from the reaction mixture, vapor phase, or condensed vapor phase by one of the methods described herein, although the desired product may not be in a purified form. The term "crack" is also used to indicate depolymerization of an oligomeric complex. The desired methylene beta-diketone monomer may be obtained by "cracking" an oligomeric complex found in the reaction complex.
As used herein, the term "sterically hindered" refers to a compound in which the size of groups within the molecule prevents chemical reactions that are observed in related smaller molecules.
As used herein, the terms "volatile" and "non-volatile" refers to a compound which is capable of evaporating readily at normal temperatures and pressures, in the case of volatile; or which is not capable of evaporating readily at normal temperatures and pressures, in the case of non-volatile.
As used herein, the term "energy transfer means" refers to a means which is capable of volatizing a reaction complex, usually by, but not limited to, rapidly heating the reaction complex to temperatures from about 150°C to about 300°C. Such energy transfer means include, but are not limited to, heat transfer agents, heat transfer surfaces, lasers, and sources of radiation.
As used herein, the term "heat transfer agent" refers to a material which is capable of achieving a high temperature and transferring that temperature to a reaction mixture. Such heat transfer agents are typically able to reach temperatures from about 150°C to about 300°C and include, but are note limited to silica, silicone oil, mineral oil, a petroleum based heat transfer oil or a synthetic chemical based heat transfer oil. In certain embodiments, the heat transfer agent can be pre-formed reaction complex.
As used herein the term "pre-formed reaction complex" refers to a reaction complex as defined herein which is prepared by reacting step (a) as described herein in advance of the vaporization step (b). Such pre-formed reaction complexes can be formed up to a year, up to six months, up to 3 months, up to 1 month, up to 2 weeks, up to 1 week, up to 3 days, or up to 1 day in advance of the vaporization step (b). In such instances, the vaporization step (b) is performed on a newly prepared reaction complex. In certain aspects the pre-formed reaction complex can refer to an oligomeric complex as defined herein.
As used herein the term "substantial absence" as in "substantial absence of acidic solvent" refers to a reaction mixture comprising less than 1% by weight of the particular component as compared to the total reaction mixture. In certain embodiments, a "substantial absence" refers to less than 0.7%, less than 0.5%, less than 0.4%m less than 0.3%, less than 0.2% or less than 0.1% by weight of the of the particular component as compared to the total reaction mixture. In certain other embodiments, a "substantial absence" refers to less than 1.0%, less than 0.7%, less than 0.5%, less than 0.4%m less than 0.3%, less than 0.2% or less than 0.1% by volume of the of the particular component as compared to the total reaction mixture.
As used herein, the term "stabilized," e.g., in the context of "stabilized" molecules of the invention or compositions comprising same, refers to the tendency of the molecules of the invention (or their compositions) to substantially not polymerize with time, to substantially not harden, form a gel, thicken, or otherwise increase in viscosity with time, and/or to substantially show minimal loss in cure speed (i.e., cure speed is maintained) with time.
As used herein, the term "shelf-life," e.g., as in the context of the molecules of the invention having an improved "shelf-life," refers to the molecules of the invention which are stabilized for a given period of time, e.g., 1 month, 6 months, or even 1 year or more.
Description of Exemplary Embodiments
Methylene beta-diketone monomers in accordance with the present invention may be made by a modified Knoevenagel condensation reaction of a beta-diketone with formaldehyde under suitable reaction conditions. The general reaction scheme is provided below.
Figure imgf000019_0001
2. Cracking at 150-270 °C
Modified Knoevenagel Reaction
Methylene beta-diketone monomers In one aspect, the invention provides a methylene beta-diketone monomer having the structural formula:
Figure imgf000019_0002
wherein each instance of Ri and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-Q5 alkyl), heteroaryl, C1-C15 alkoxy, d- Ci5 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In certain embodiments, the invention provides a methylene beta-diketone monomer having the structural formula:
Figure imgf000020_0001
wherein each instance of Ri and R2 are independently Q-C6 alkyl, halo-(Ci-C6 alkyl), C3-C6 cycloalkyl, aryl, or heteroaryl, each of which may be optionally substituted by halo or Ci-C6 alkoxy.
In still other embodiments, the invention provides a methylene beta-diketone monomer having the structural formula:
Figure imgf000021_0001
wherein each instance of Ri and R2 are independently Ci-C6 alkyl or aryl.
Reactants
The reaction for making methylene beta-diketone monomers of the invention includes at least two basic reactants: a beta-diketone precursor and a source of formaldehyde.
In certain embodiments, the methylene beta-diketone precursors in accordance with exemplary embodiments disclosed herein include beta-diketones able to undergo a condensation reaction at the alpha carbon. Beta-diketone precursors include, but are not limited to, molecules having the structural formula:
Figure imgf000021_0002
wherein each instance of Ri and R2 are independently C1-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by Q- Cis alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl),
heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
In certain other embodiments, the present invention contemplates the following specifically identified beta-diketone precursors: l,3-dimefhyl-propane-l,3- diones, l,3-diethyl-propane-l,3-diones, l-ethyl-3-methyl-propane-l,3-diones, 1,3- dipropyl-propane-l,3-diones, l,3-dibutyl-propane-l,3-diones, and 1,3-diphenyl- propane-l,3-diones, among others.
The beta-diketone precursor may be derived or obtained from any source, including any commercial source, derived from nature, other compounds, synthesized by other processes, etc. In certain embodiments, the beta-diketone precursors are obtained from "green" sources. For example, the beta-diketone precursors can be derived from biological sources, such as via fermentation production systems whereby microorganisms generate the beta-diketone precursors is direct metabolic byproducts of fermentation— or whereby the microorganisms generate metabolic byproducts of fermentation that can be then converted inexpensively to the desired beta- diketone precursors. These fermentation production systems are well-known in the art and may utilize either— or both— microorganisms derived from nature or engineered microorganisms that are specifically designed to produce the desired beta- diketone precursors products, e.g., recombinant or engineered Escherichia coli.
The beta-diketone precursor is reacted with a source of formaldehyde. The methods of the invention also contemplate any suitable source of formaldehyde. For example, the formaldehyde may be synthesized, derived from another chemical species (e.g., paraformaldehyde), or obtained from nature or from some other suitable source. In certain embodiments, the formaldehyde is introduced in the form of a gas. Commercial sources of formaldehyde and paraformaldehyde are readily available, which may include, for example, trioxane and formalin (e.g., aqueous formaldehyde). The source of formaldehyde may be paraformaldehyde, formalin, trioxane or gaseous formaldehyde. In certain embodiments, the formaldehyde is obtained from paraformaldehyde. In an exemplary embodiment, the source of formaldehyde is paraformaldehyde that is thermally degraded to formaldehyde in the reaction vessel. It is envisioned that other means of providing formaldehyde to the reaction vessel may be utilized, for example, a stream of gaseous formaldehyde.
Catalysts
In certain embodiments, the methods of preparing the methylene beta-diketone takes place in the presence of a suitable catalyst. However, it is envisioned that certain reactions may not required the presence of a catalyst.
In certain embodiments, the catalysts that may be used include, but are not limited to, basic catalysts such as potassium acetate, sodium acetate, zinc acetate, zinc diacetate dihydrate, aluminum acetate, calcium acetate, magnesium acetate, magnesium oxide, copper acetate, lithium acetate, aluminum oxide, or zinc oxide.
In further embodiments, the catalysts include, but are not limited to, acidic catalysts such as paratoluene sulfonic acid, dodecylbenzene sulfonic acid, boron trifluoride, zinc perchlorate, sulfated zirconium oxide, sulfated titanium oxide, lithium chloride, boron trifluoride etherate, ferric sulfate, zirconium oxychloride, cupric chloride, titanium tetrachloride, or zinc chloride.
Still other exemplary catalysts are heterogeneous catalysts. Still other exemplary catalysts are enzyme catalysts. An exemplary enzyme is Novozym ® 435 available from Novozyme. Novozym 435 is an immobilized granulate, non-specific lipase particularly useful for ester production. Neutral catalysts can also include silica and other insoluble surface-active agents.
In still further embodiments, amphoteric catalysts can include, but are not limited to, aluminum oxide, aluminum acetate, zinc acetate, magnesium acetate, and zinc oxide.
In still other embodiments, the present inventors have surprisingly and unexpectedly found that no catalyst is required to conduct the synthesis reaction of the invention. Specifically, in this embodiment, the reaction can be conducted with all of the reactants added to the reaction vessel at the start of the reaction prior to adding heat. The source of formaldehyde in this embodiment is preferably solid
paraformaldehyde, and is added along with the other reactants, including the malonic ester, prior to adding heat. This reaction surprisingly can be run rapidly and in a continuous mode and unexpectedly avoids the formation of— or substantially minimizes the formation of— deleterious side products, unwanted polymerization complexes and degradation of the monomer products.
Solvents
The present invention contemplates that the synthesis reaction includes an acidic or non-acidic solvent, or optionally no solvent at all.
Non-acidic solvents can include, but are not limited to, tetrahydrofuran, chloroform, dichloromethane, toluene, heptane, ethyl acetate, n-butyl acetate, dibutyl ether and hexane.
Acidic solvents can include, but are not limited to acetic acid and propionic acid.
In certain embodiments, the acidic solvent is added just prior to recovery. In certain other embodiment, optionally no solvent is needed. This zero- solvent approach will not only decrease the overall cost of production but will also help to lessen any negative impact on the environment caused by the methods of the invention, i.e., provides an environmentally-friendly approach to the synthesis of 2- methylene-l,3-disubstituted-propane-l,3-diones. An advantage of this condition is the avoidance or minimization of the formation of impurities, e.g., ketals and other latent acid-forming species.
In still other embodiments, the present inventors have surprisingly and unexpectedly found that the synthesis reaction of the invention may be conducted in the absence of both a solvent and a catalyst. Specifically, in this embodiment, the reaction can be conducted with all of the reactants added to the reaction vessel at the start of the reaction prior to adding heat and in the absence of a solvent. The source of formaldehyde in this embodiment is preferably solid paraformaldehyde, and is added along with the other reactants, including the malonic ester, prior to adding heat. This reaction surprisingly can be run rapidly and in a continuous mode and unexpectedly avoids the formation of— or substantially minimizes the formation of— deleterious side products, unwanted polymerization complexes and degradation of the monomer products.
Stabilization
Certain embodiments of the present invention provide monomers that are amenable to anionic polymerization. Therefore, to prevent unwanted polymerization and extend shelf life, certain exemplary embodiments include suitable acidic stabilizers, for example, trifhioromefhane sulfonic acid, maleic acid, methane sulfonic acid, difluoro acetic acid, trichloroacetic acid, phosphoric acid, dichloroacetic acid, chlorodifluoro or like acid. Acidic stabilizers can include any material which can be added to the monomer or polymer compositions to extend shelf-life, e.g., by up to, for example, 1 year or more. Such acidic stabilizers may have a pKa in the range of, for example, between about -15 to about 5, or between about -15 to about 3, or between about -15 to about 1, or between -2 to about between about -2 to about 2, or between about 2 to about 5, or between about 3 to about 5.
Reaction Conditions
In certain embodiments of the present invention, the starting precursor is reacted with paraformaldehyde in the presence of a catalyst (e.g., zinc acetate dehydrate) at 60 °C -130 °C (e.g., 100 °C) for at least about 30 minutes. The resulting intermediate material (e.g., oligomeric complex) is then thermally depolymerized to the vinyl containing product by addition to a hot surface set from 150 °C to 270 °C. The resulting crude monomer is then purified, for example by distillation, fractional distillation or other separation methods.
For a typical lab scale reaction: a 3-neck 250 mL round bottom reaction flask was equipped with an overhead stirrer, a heating mantle, and a temperature probe connected to a temperature controller. The reaction flask was adequately vented to the back of the hood to reduce the possibility of pressure build-up. The beta-diketone (precursor), paraformaldehyde (1.8 equiv) and zinc acetate (0.001 equiv) were added to the reaction flask. The contents of the flask were mixed for approximately 2 minutes prior to the application of heat. After the initial mixing period the temperature controller was set to 100 °C. The heterogeneous reaction mixture was allowed to heat with the temperature for dissolution and onset of exotherm being noted. Once a rapid increase in temperature was observed, heating was discontinued. Once the exotherm subsided, the heating mantle was immediately removed and the reaction mixture (herein "reaction complex") was allowed to cool to room
temperature to afford the oligomeric mixture. To isolate the methylene beta-diketone monomer from the reaction complex, a
4-neck suitable round bottom flask was equipped with a mechanical stirrer, heating mantle, a thermocouple connected to a temperature controller, an addition funnel, a Claisen adapter, and a vacuum adapter connected to a receiver one-neck round bottom flask which was placed in an ice-bath. The system was evacuated to low pressure (1- 250 mmHg). The oligomeric mixture was added to the addition funnel. The reaction flask was then applied via the connected heating mantle to 150-270 °C. Once the temperature inside the flask reached the desired range, a drop-wise addition of the oligomer (reaction complex) to reaction flask was started. The addition rate was maintained so that the set temperature was maintained in the desired range. After the addition was complete, the heating mantle was turned off and the system was allowed to cool to room temperature, at this point the system was opened to atmospheric pressure. An aliquot was then taken for analysis and the remaining cracked distillate was either distilled further via fractional distillation to improve purity or placed in a refrigerator.
This general reaction scheme was utilized to provide the examples provided herein. Due to the wide variety of example obtained, it is envisioned that this general reaction scheme can be utilized to provide a wide array of methylene beta-diketone monomers as set forth herein. Further, it is envisioned that modifications can be made to this general reaction scheme in order to improve efficiencies and purity of the product obtained.
Methods of synthesis
In another aspect, the invention provides a method of preparing methylene beta-diketone monomers according to the reaction scheme disclosed herein. In certain embodiments, the method for preparing the methylene beta-diketone monomers comprises: a) reacting a beta-diketone reactant having the structural formula:
Figure imgf000028_0001
under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; and b) isolating a methylene beta-diketone monomer from the reaction complex, wherein the methylene beta-diketone monomer has the structural formula:
Figure imgf000029_0001
wherein Ri and R2 are defined above.
In certain embodiments, the reaction may be initiated at temperatures between about 60 °C to about 130 °C, at atmospheric pressure. It is contemplated that the reaction conditions may be modified depending on the source of formaldehyde. For example, when paraformaldehyde is utilized within the reaction vessel, the initial temperature must be high enough to make free formaldehyde available for the reaction. If another source of formaldehyde is utilized, those having skill in the art will appreciate that the reaction conditions may be modified accordingly. Exemplary sources include paraformaldehyde, formalin, trioxane, gaseous formaldehyde, or any reaction or process in which formaldehyde is liberated.
In other embodiments, the methylene beta-diketone monomer may be isolated from the reaction complex by contacting the reaction complex, or a portion thereof, with an energy transfer means to produce a vapor phase including the methylene beta- diketone monomer; and collecting the methylene beta-diketone monomer from the vapor phase.
In still other embodiments, the methylene beta-diketone monomer may be isolated from the reaction complex immediately, or the reaction complex may be stored, preferably refrigerated, until a later time. In an exemplary embodiment, the reaction complex is not acid stabilized prior to isolating the methylene beta-diketone monomer.
In other embodiments, the reaction complex, or a portion thereof, may be heated to a vapor phase and condensed in order to isolate the methylene beta-diketone monomer. The reaction complex may be heated to a temperature between about 130 °C and about 300 °C.
In still other embodiments, the reaction complex, or a portion thereof, may come in contact with an energy transfer means in order to facilitate isolation of the monomer. In an exemplary embodiment, the reaction complex, or portion thereof, may be vaporized in a very short time, for example less than 15 minutes, preferably less than 1 minute, more preferably less than 30 seconds, and less than 1 second. Certain exemplary embodiments contemplate vaporizing the reaction complex in a continuous manner as it is formed during the reaction step.
Exemplary energy transfer means include a heat transfer agent, a heat exchanger, a laser, microwave energy, sonic energy, electromagnetic energy, and a source of radiation, or any combination thereof. The energy transfer means operates to quickly vaporize the reaction complex (or portion thereof) to permit isolation of the monomer product. For example, an oligomeric complex may be formed, and the energy transfer means is utilized to "crack" or depolymerize the oligomer to allow isolation of the monomer. In certain embodiments, the oligomeric complex may include oligomers of 2-12 units able to provide monomer product upon crack.
In certain exemplary embodiments, the heat transfer agent is a heated inert gas, one or more metal beads, one or more glass beads, one or more porcelain beads, sand, silica, silicone oil, mineral oil, a petroleum based heat transfer oil, a synthetic chemical based heat transfer oil, or a pre-formed portion of the reaction complex.
In certain other embodiments, the heat exchanger is a shell and tube heat exchanger, a plate heat exchanger, and adiabatic wheel heat exchanger, a finned pipe heat exchanger, a plate fin heat exchanger, or a scraped surface heat exchanger.
In still other embodiments, the vapor phase of the reaction complex is condensed, and the condensate is subject to one or more further separation processes. For example, the separation process may include any of simple distillation, fractional distillation, flash distillation, steam distillation, vacuum distillation, short path distillation, thin-film distillation, reactive distillation, pervaporation, extractive distillation, flash evaporation, rotary evaporation, liquid/liquid extraction, centrifuging, or any combination thereof, and other techniques known to those having skill in the art.
Compositions
The methylene beta-diketone monomers of the invention can be incorporated into any number of compositions and products including but not limited to reactive monomer-based compositions, reactive oligomer-based compositions and reactive polymer-based compositions. Exemplary compositions can be analyzed by placing a drop of a monomer composition on a substrate (for example a glass slide or 4"xl" polycarbonate sample). Another glass slide or piece of polycarbonate is pressed on top over the monomer- covered area. The time is then immediately recorded from pressing the top-slide till the two slides are bonded tightly. In such embodiments, the exemplary composition is capable of bonding glass to a substrate in less than about 90 seconds, less than about 60 seconds, less than about 30 seconds or less than about 15 seconds.
Similarly, the exemplary composition is capable of bonding polycarbonate to a substrate in less than about 90 seconds, less than about 60 seconds, less than about 45 seconds or less than about 30 seconds.
Alternatively, exemplary compositions can be analyzed by mixing 0.5 ml of monomer with 0.3 ml of 3% tertiary butyl ammonium fluoride (TBAF) in Dibutyl Phthalate solution. The time is recorded from adding the TBAF solution till the mixture become solid with vigorous stirring or mixing. In such embodiments, said composition solidifies upon addition of 3% tertiary butyl ammonium fluoride (TBAF) in Dibutyl Phthalate solution in less than about 15 seconds, less than about 10 seconds, or less than about 7 seconds.
Alternatively still, the exemplary compositions can be analyzed by placing 0.5 ml of monomer into a test tube and cap with a cork stopper and keeping the test tubes containing monomers at 25°C, or in ovens at 55°C or 82°C. In each case the storage stability test is performed at atmospheric pressure. Time is recorded when the monomer became a gel or solid. In such embodiments, said composition remains stable at 25°C and at atmospheric pressure for more than 10 days, more than 15 days, more than 20 days, more than 25 days or more than 30 days. Similarly, said composition remains stable at 82°C and at atmospheric pressure for more than about 2 hours, more than about 3 hours, or more than about 4 hours.
Exemplary compositions include, but are not limited to an adhesive, a coating, a sealant, a composite, or a surfactant. Additionally polymer products include, but are not limited to, a sealant, a thermal barrier coating, a textile fiber, a water-treatment polymer, an ink carrier, a paint carrier, a packaging film, a molding, a medical polymer, a polymer film, a polymer fiber or a polymer sheet.
In each case, the exemplary compositions may be formulated to include one or more materials to extend the shelf-life as well as control the onset of cure of the materials. In certain embodiments, the compositions are formulated such that the composition is stable for at least 1 month, or for at least 2 months, or for at least 3 months, or for at least 4 months, or for at least 5 months, or for at least 5-10 months, or for at least 10-20 months, or for at least 20-30 months. Preferably, the adhesive composition comprising the methylene beta-diketone monomers or other commercial compositions or products, are stable for at least one year.
Such formulation materials include acidic stabilizer, volatile acid stabilizers, acidic gases, free radical stabilizers, sequestering agents, cure accelerators and rheology modifiers. Exemplary embodiments contemplate any suitable acidic stabilizer known in the art, including, for example, trifluoromethane sulfonic acid, maleic acid, methane sulfonic acid, difluoro acetic acid, trichloroacetic acid, phosphoric acid, dichloroacetic acid, chlorodifluoro or like acid. Acidic stabilizers can include any material which can be added to the monomer or polymer compositions to extend shelf-life, e.g., by up to, for example, 1 year or more. Such acidic stabilizers may have a pKa in the range of, for example, between about -15 to about 5, or between about -15 to about 3, or between about -15 to about 1, or between -2 to about between about -2 to about 2, or between about 2 to about 5, or between about 3 to about 5.
Volatile acid stabilizers include any material which can be added to the monomer or polymer compositions to extend shelf-life and stabilize the vapor phase above the composition upon storage, e.g., acidic gases. Such volatile acid stabilizers may have a boiling point, for example, less than about 200°C; less than about 170°C; or less than about 130°C.
Acidic gases include any gaseous material which can be added to the monomer or polymer compositions to extend shelf-life and stabilize the vapor phase above the composition upon storage. Such acid gases can include, but are not limited to, S02 or BF3. For each of these acidic stabilizing materials, such acidic stabilizer can be present in a concentration of about 0.1 ppm to about 100 ppm; about 0.1 ppm to about 25 ppm; or about 0.1 ppm to about 15 ppm.
Free radical stabilizers can include any material capable of stabilizing or inhibiting free radical polymerization of the material upon standing. In one embodiment, the free radical stabilizers are phenolic free radical stabilizers such as, HQ (hydroquinone), MEHQ (methyl- hydroquinone), BHT (butylated hydroxtoluene) and BHA (butylated hydroxyanisole). In certain embodiments, the free radical stabilizers are present in a concentration of 0.1 ppm to 10,000 ppm; 0.1 ppm to 3000 ppm; or 0.1 ppm to 1500 ppm. In certain other embodiments, particularly where a free radical or ultraviolet cure will be utilized, the free radical stabilizers are present in a concentration of 0.1 ppm to 1000 ppm; 0.1 ppm to 300 ppm; or 0.1 ppm to 150 ppm.
Sequestering agents include any material capable of enhancing the bonding of materials containing acid salts such as paper or wood. Such sequestering agents include, but are not limited to crown ethers, silyl crowns, calixarenes and
polyethylene glycols. Sequestering agents also enhance the utility of surface accelerators that are acid salts applied to surfaces to control the rate of cure of the materials.
Cure accelerators include any material capable of speeding the rate of cure of the methylene beta-diketone monomers. Cure accelerators also include any material capable of speeding the cure through volume of the applied composition. Such cure accelerators include but are not limited to sodium or potassium acetate; acrylic, maleic or other acid salts of sodium, potassium lithium copper and cobalt; salts such as tetrabutyl ammonium fluoride, chloride, or hydroxide; or chemically basic materials such as amines and amides, or salts of polymer bond acids, benzoate salts, 2,4-pentanedionate salts, sorbate salts , or propionate salts. Such cure accelerators can be added directly to the exemplary compositions or applied to the material to be bonded prior to addition of the composition.
Rheology modifiers include any material which can modify the viscosity of the exemplary compositions as well as thixotropic properties for greater utility in certain applications. Rheology modifiers include, but are not limited to,
hydroxyethylcellulose, ethyl hydroxyethylcellulose, methylcellulose, polymeric thickeners, pyrogenic silica or a combination thereof. In certain embodiments, the exemplary compositions may include tougheners. Such tougheners include, but are not limited to, acrylic rubbers; polyester urethanes; ethylene-vinyl acetates; fluorinated rubbers; isoprene-acrylonitrile polymers;
chloro sulfonated polyethylenes; homopolymers of polyvinyl acetate; and reaction products of the combination of ethylene, methyl acrylate and monomers having carboxylic acid cure sites, which once formed are then substantially free of processing aids and anti-oxidants; and combinations thereof. In certain embodiments, the tougheners include those disclosed in U.S. Pat. No. 4,440,910 (O'Connor), directed to rubber toughened cyanoacrylate compositions through the use of certain organic polymers as toughening additives that are elastomeric, i.e., rubbery, in nature, such as acrylic rubbers; polyester urethanes; ethylene-vinyl acetates; fluorinated rubbers; isoprene-acrylonitrile polymers; chlorosulfonated polyethylenes; and homopolymers of polyvinyl acetate. In certain embodiments, the toughener is an elastomeric polymer which is a copolymer of methyl acrylate and ethylene, manufactured by DuPont, under the name of VAMAC, such as VAMAC N123 and VAMAC B-124. VAMAC N123 and VAMAC B-124 are reported by DuPont to be a master batch of ethylene/acrylic elastomer. In other embodiments, the toughener may be the DuPont materials called VAMAC B-124, N123, VAMAC G, VAMAC VMX 1012 or VCD 6200. In other instances, the toughener may be a rubber toughening component having (a) reaction products of the combination of ethylene, methyl acrylate and monomers having carboxylic acid cure sites, (b) dipolymers of ethylene and methyl acrylate, and combinations of (a) and (b), which once the reaction products and/or dipolymers are formed are then substantially free of processing aids, such as the release agents octadecyl amine (reported by DuPont to be available commercially from Akzo Nobel under the tradename ARMEEN 18D), complex organic phosphate esters (reported by DuPont to be available commercially from R.T. Vanderbilt Co., Inc. under the tradename VANFRE VAM), stearic acid and/or polyethylene glycol ether wax, and anti-oxidants, such as substituted diphenyl amine (reported by DuPont to be available commercially from Uniroyal Chemical under the tradename
NAUGARD 445). Commercial examples of such rubber tougheners include VAMAC VMX 1012 and VCD 6200 rubbers, and these may be used too.
The exemplary compositions containing methylene beta-diketone monomer may also optionally include other additives, such as plasticizing agents, thixotropic agents, natural or synthetic rubbers, filler agents, and reinforcing agents, etc. Such additives are well known to those skilled in the art.
The exemplary compositions containing methylene beta-diketone monomer may optionally include at least one plasticizing agent that imparts flexibility to the polymer formed from the methylene beta-diketone monomer. The plasticizing agent preferably contains little or no moisture and should not significantly affect the stability or polymerization of the monomer. Such plasticizers are useful in polymerized compositions to be used in any application in which flexibility of the adhesive or polymer product is desirable.
Examples of suitable plasticizers include, without limitation, acetyl tributyl citrate, dimethyl sebacate, triethyl phosphate, tri (2-ethylhexyl)phosphate, tri (p- cresyl) phosphate, glyceryl triacetate, glyceryl tributyrate, diethyl sebacate, dioctyl adipate, isopropyl myristate, butyl stearate, lauric acid, trioctyl trimellitate, dioctyl glutarate, and mixtures thereof. Preferred plasticizers are tributyl citrate and acetyl tributyl citrate. In embodiments, suitable plasticizers include polymeric plasticizers, such as polyethylene glycol (PEG) esters and capped PEG esters or ethers, polyester glutarates and polyester adipates.
The addition of plasticizing agents in amounts less than about 60 weight %, or less than about 50 weight %, or less than about 30 weight , or less than about 10 weight %, or less than about 5 weight %, or less than about 1 weight % or less, provides increased film strength (e.g., toughness) of the polymerized monomer over polymerized monomers not having plasticizing agents.
The exemplary compositions containing methylene beta-diketone monomer may also optionally include at least one thixotropic agent, i.e., the property of exhibiting a high fluidity during deformation by force of a sprayer, roller or trowel, but losing the fluidity when left at rest. Suitable thixotropic agents are known to the skilled artisan and include, but are not limited to, silica gels such as those treated with a silyl isocyanate. Examples of suitable thixotropic agents are disclosed in, for example, U.S. Pat. Nos.: 4,720,513 or 4,510,273, the disclosures of which are hereby incorporated in their entireties.
The exemplary compositions containing methylene beta-diketone monomer may also optionally include at least one natural or synthetic rubber to impart impact resistance, which is preferable especially for industrial compositions of the present invention. Suitable rubbers are known to the skilled artisan. Such rubbers include, but are not limited to, dienes, styrenes, acrylonitriles, and mixtures thereof. Examples of suitable rubbers are disclosed in, for example, U.S. Pat. Nos. 4,313,865 and 4,560,723, the disclosures of which are hereby incorporated in their entireties.
The exemplary compositions containing methylene beta-diketone monomer may also optionally comprise one or more other reinforcing agents (e.g., fibrous reinforcements) other than natural or synthetic rubber to impart impact resistance and/or to impart structural strength or to provide shape or form. Examples of such agents are well known in the art. Examples of suitable fibrous reinforcement include PGA microfibrils, collagen microfibrils, cellulosic microfibrils, and olefinic microfibrils. The compositions may also contain colorants such as dyes, pigments, and pigment dyes. Examples of suitable colorants include 6-hydroxy-5-[(4- sulfophenyl)axo]-2-naphthalene-sulfonic acid (FD+C Yellow No. 6); 9-(o- carboxyphenyl)-6-hydroxy-2,4,5,7-tetraiodo-3H-xanthen-3-one monohydrate (FD+C Red No. 3); and 2-(l,3-dihydro-3-oxo-5-sulfo-2H-indol-2-ylidene)-2,3-dihydro-3- oxo-lH-indo le-5-sulfonic acid (FD+C Blue No. 2), wherein the suitable colorant should not destabilize the monomer.
The exemplary compositions containing methylene beta-diketone monomer may also optionally include at least one thickening agent. Suitable thickeners include, for example, polycyanoacrylates, polylactic acid, poly-l,4-dioxa-2-one, polyoxalates, polyglycolic acid, lactic-glycolic acid copolymers, polycaprolactone, lactic acid- caprolactone copolymers, poly-3-hydroxybutyric acid, polyorthoesters, polyalkyl acrylates, copolymers of alkylacrylate and vinyl acetate, polyalkyl methacrylates, and copolymers of alkyl methacrylates and butadiene. Examples of alkyl methacrylates and acrylates are poly(2-ethylhexyl methacrylate) and poly(2-ethylhexyl acrylate), also poly(butylmethacrylate) and poly(butylacrylate), also copolymers of various acrylate and methacrylate monomers, such as poly(butylmethacrylate-co- methylacrylate).
To improve the cohesive strength of adhesives formed from the compositions containing methylene beta-diketone monomer, difunctional monomelic cross-linking agents may be added to the monomer compositions of this invention. Such crosslinking agents are known. U.S. Pat. No. 3,940,362 to Overhults, which is hereby incorporated in its entirety by reference, discloses such crosslinking agents.
Other compositions and additives contemplated herein, include additional stabilizers, accelerators, plasticizers, fillers, opacifiers, inhibitors, thixotrophy conferring agents, dyes, fluorescence markers, thermal degradation reducers, adhesion promoters, thermal resistance conferring agents and combinations thereof, and the like, some of which are exemplified by U.S. Pat. Nos. 5,624,669; 5,582,834;
5,575,997; 5,514,371 ; 5,514,372; 5,312,864 and 5,259,835, the disclosures of all of which are hereby incorporated in their entirety by reference.
Depending on whether the composition is a monomer-based composition (e.g. , inks, adhesives, coatings, sealants or reactive molding) or a polymer-based composition (e.g., fibers, films, sheets, medical polymers, composite polymers and surfactants), one having ordinary skill in the art will have the knowledge and skill by which to formulate such compositions and/or products without undue experimentation having suitable amounts, levels and combinations of the above types of additives and components.
Additionally, polymerizable compositions may be formulated to include additives such as acidic stabilizers, a free radical stabilizers, a sequestering agents, a cure accelerators, rheology modifiers, a plasticizing agents, a thixotropic agents, natural rubbers, synthetic rubbers, filler agents, reinforcing agents and the like. Such additives are provided at levels sufficient to achieve the desired results which can readily be determined by those having skill in the art. For certain exemplary embodiments, an acidic stabilizer is present in a concentration of about 0.1 ppm to about 100 ppm, about 0.1 ppm to about 25 ppm, or about 0.1 ppm to about 15 ppm, by weight of the composition.
For certain exemplary embodiments, a free radical stabilizer is present in a concentration selected from about 0.1 ppm to about 10000 ppm, about 0.1 ppm to about 3000 ppm, about 0.1 ppm to 1500 ppm, about 0.1 ppm to about 1000 ppm, about 0.1 ppm to about 300 ppm, or about 0.1 ppm to about 150 ppm, by weight of the composition.
For certain exemplary embodiments, a sequestering agent, such as a crown ether, a silyl crown, a calixarene, a polyethylene glycol, or a combination thereof may be utilized.
For certain exemplary embodiments, a cure accelerator, such as sodium acetate, potassium acetate, tetrabutyl ammonium fluoride, tetrabutyl ammonium chloride, tetrabutyl ammonium hydroxide, a benzoate salt, a 2,4-pentanedionate salt, a sorbate salt, and a propionate salt, may be utilized.
For certain exemplary embodiments, a rheology modifier, such as
hydroxyethylcellulose, ethyl hydroxyethylcellulose, methylcellulose, a polymeric thickener, and pyrogenic silica, may be utilized.
Exemplary polymerizable compositions are stable at 25°C and at atmospheric pressure for more than 10 days, more than 15 days, more than 20 days, more than 25 days, or more than 30 days. Certain exemplary embodiments may exhibit a shelf life of up to one year, or up to two years. Certain exemplary embodiments may be tested for stability at elevated temperature, e.g., 82°C, at atmospheric pressure. Certain exemplary embodiments may exhibit elevated temperature stability for more than 2 hours.
Certain exemplary embodiments disclosed herein relate to polymers and polymer products formed by polymerization of the polymerizable compositions comprising the methylene beta-diketone monomers.
Polymers and polymer products envisioned include coatings, paints, fibers, composites, textile fibers, water-treatment polymers, ink carriers, paint carriers, packaging films, moldings, medical polymers, polymer films, polymer fibers, polymer sheets, and the like. As discussed earlier, the methylene beta-diketone monomers are capable of supporting a vast array of products due to the activity of the methylene group and the ability to vary the functional groups R, R as shown in the structure of the repeating unit:
Figure imgf000042_0001
wherein R and R' are independently Q-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C5 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
Oligomeric Complex Products
The reaction of the precursor beta-diketone with the source of formaldehyde may result in an oligomeric complex which is subsequently cracked to obtain the desired methylene beta-diketone monomer. Certain oligomeric complexes are capable of being efficiently vaporized or "cracked" into high purity monomers of 2- methylene-l,3-disubstituted-propane-l,3-dione by rapid vaporization as described herein.
As such, the invention provides an oligomeric complex prepared by reacting a l,3-disubstituted-propane-l,3-dione with a source of formaldehyde; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of an acidic or non-acidic solvent. In certain embodiments, the oligomeric complex comprises between 2 and 12 repeat units that are able to yield monomer upon cracking
The invention further provides an oligomeric complex prepared by reacting a l,3-disubstituted-propane-l,3-dione with a source of formaldehyde in a substantial absence of acidic solvent; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of a non- acidic solvent. In certain embodiments, the substantial absence of acidic solvent represents less than 1.0%, less than 0.5%, less than 0.2% or less than 0.1% by weight acidic solvent as compared to the total composition of the reaction mixture. EXAMPLES
The structures, materials, compositions, and methods described herein are intended to be representative examples of the invention, and it will be understood that the scope of the invention is not limited by the scope of the examples. Those skilled in the art will recognize that the invention may be practiced with variations on the disclosed structures, materials, compositions and methods, and such variations are regarded as within the ambit of the invention.
Analytical Methods
The structures of monomers of this invention were confirmed using one or more of the following procedures.
NMR
Samples were diluted in deuterated chloroform prior to 1H NMR spectroscopy at 300 MHz (Bruker). A more concentrated sample was also prepared in a solution of 0.01 M Cr(III) acetoacetonate in deuterated chloroform and was analyzed by quantitative 13C NMR spectroscopy at 75 MHz. Samples were not purified.
Abbreviations and Acronyms
A comprehensive list of the abbreviations used by organic chemists of ordinary skill in the art appears in The ACS Style Guide (third edition) or the Guidelines for Authors for the Journal of Organic Chemistry. The abbreviations contained in said lists, and all abbreviations utilized by organic chemists of ordinary skill in the art are hereby incorporated by reference. For purposes of this invention, the chemical elements are identified in accordance with the Periodic Table of the Elements, CAS version, Handbook of Chemistry and Physics, 67th Ed., 1986-87.
More specifically, when the following abbreviations are used throughout this disclosure, they have the following meanings: atm atmosphere br s broad singlet
C Celsius d doublet dd doublet of doublets MM substituted 3-methylene-2,4-pentanebeta-ketoester
HQ hydroquinone
GC-MS Gas Chromatography-Mass Spectroscopy g gram h hour, hours XH NMR proton nuclear magnetic resonance
J coupling constant (NMR spectroscopy)
L liter
M mol'L"1 (molar) m multiplet
MHz megahertz
min minute, minutes
mL milliliter
mM millimolar
mol mole
MS mass spectrum, mass spectroscopy
m/z mass-to-charge ratio
N equivalents*!^1 (normal)
NMR Nuclear Magentic Resonance
pH negative logarithm of hydrogen ion concentration q quartet
rt room temperature
s singlet
t triplet
RB, RBF round bottom flask
The following concrete examples were made in accordance with the general reaction scheme set forth above, unless otherwise noted.
Example 1. Reaction of 5,5-dimethylhexane-2,4-dione and formaldehyde:
The reaction scheme disclosed herein was performed using 5,5- dimethylhexane-2,4-dione and formaldehyde (obtained from paraformaldehyde). The following monomer was obtained.
Figure imgf000047_0001
The two small peaks at 5.75 and 6.2 ppm in the 1H spectrum (Figure 1) and the peaks at 126 (CH2) and 150 ppm (quaternary) in the 13C spectrum (Figure 2) are consistent with the geminal CH2 functionality of the desired structure (below). The DEPT-135 spectrum (Figure 2) is also shown.
Example 2. Reaction of heptane-3,5-dione and formaldehyde:
The reaction scheme disclosed herein was performed using heptane-3,5-dione and formaldehyde (obtained from paraformaldehyde). The following monomer was obtained.
Figure imgf000047_0002
The peak at 6.2 ppm in the H NMR spectrum (Figure 3) is consistent with the geminal CH2 peak of the product:
Example 3. Reaction of 5-methylhexane-2,4-dione and formaldehyde:
The reaction scheme disclosed herein was performed using 5-methylhexane- 2,4-dione and formaldehyde (obtained from paraformaldehyde). The following monomer was obtained.
Figure imgf000048_0001
The peaks at 6.2 and 6.3 ppm in the H NMR spectrum in Figure 4 are consistent with the geminal CH2 peak of the product.
Example 4. Reaction of l-phenylbutane-l,3-dione and formaldehyde:
The reaction scheme disclosed herein was performed using 1-phenylbutane- 1,3-dione and formaldehyde (obtained from paraformaldehyde). The following monomer was obtained.
Figure imgf000048_0002
The peaks at 6.1 and 6.6 ppm in the 1H NMR spectrum of Figure 5 are consistent with the geminal CH2 peak of the product. The peaks at 130 ppm (CH2) and 148 ppm (quaternary) in the 13C and DEPT-135 NMR spectra in Figure 6 are also consistent with the product.
Example 5. Reaction of l,3-diphenylpropane-l,3-dione and formaldehyde:
The reaction scheme disclosed herein was performed using 1,3- diphenylpropane-l,3-dione and formaldehyde (obtained from paraformaldehyde). The following monomer was obtained.
Figure imgf000049_0001
The peak at 6.2 ppm in the 1H NMR spectrum in Figure 7 is consistent with the geminal CH2 peak of the product shown. The peak at 0 ppm is due to
hexamethyldisiloxane, which was added as an internal standard.
Example 6. Reaction of nonane-4,6-dione and formaldehyde:
Potassium te/t-butoxide (97.5 g, 0.87 mol) was added to a 1 L 3-neck flask containing 150 mL dry dimethyl formamide and equipped with a mechanical stirrer and a thermocouple. The temperature was raised to 50 °C with stirring. Methyl butyrate (200 mL, 1.8 mol) and 2-pentanone (62 mL, 0.58 mol) were added as a mixture via 500 mL addition funnel over 2.5 h at 50 °C during which the yellow slurry turned to a clear brown solution. The reaction mixture was stirred for an additional 5 h at 50 °C at which point heating was turned off and the reaction mixture was allowed to stir for 14 h at room temperature. The reaction mixture was quenched by slow addition into a 1 M HCl aq. solution (500 mL) at 0 °C, and the pH was adjusted with 1 M HCl aq. solution to about 5. The reaction slurry was extracted with heptane (4 x 400 mL). The combined organic layers were concentrated to 300 mL under reduced pressure. The residue was washed with water (5 x 400 mL) followed by a brine wash. The enriched organic layer was further concentrated under reduced pressure to afford a yellowish liquid which was purified by distillation at 65 °C, 2 Torr to afford 60 g of 85% pure (based on H NMR analysis) material (56% yield) as a clear liquid.
The following monomer was obtained.
Figure imgf000050_0001
The lH NMR spectrum is shown in Figure 8. The peak at 6.2 ppm is consistent with the geminal double bond of the product. The 13C and DEPT-135 spectra are shown in Figure 9. The peak at 129 ppm (CH2) and at 150 ppm (quaternary) are consistent with the geminal double bond of the product.
Example 7. Additional Examples :
The reaction scheme disclosed herein is performed using an appropriate 1,3- disubtituted-propane-l,3-dione and a source formaldehyde to obtain the following monomers.
Figure imgf000051_0001
Figure imgf000052_0001
Equivalents
Those skilled in the art will recognize, or be able to ascertain using no more than routine experimentation, many equivalents to the specific embodiments of the invention described herein. Such equivalents are intended to be encompassed by this invention.

Claims

WHAT IS CLAIMED IS:
1. A method of preparing a methylene beta-diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula:
Figure imgf000053_0001
with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; and b) isolating a methylene beta-diketone monomer from the reaction complex, wherein the methylene beta-diketone monomer has the structural formula:
Figure imgf000053_0002
wherein each instance of Ri and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-Cg cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, d- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, Ci- Ci5 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
2. The method according to Claim 1 wherein in step (b), isolating the methylene beta- diketone monomer comprises: i. contacting the reaction complex, or a portion thereof, with an energy transfer means to produce a vapor phase including the methylene beta-diketone monomer; and ii. collecting the methylene beta-diketone monomer from the vapor phase.
3. The method according to Claim 2 wherein in step (b)(ii), collecting the methylene beta-diketone monomer includes condensing the vapor phase to a condensate.
4. The method of Claim 1, wherein in step (b), isolating the methylene beta- diketone monomer comprises: iii. heating the reaction complex, or a portion thereof, to a temperature between about 130°C and about 300°C to produce a vapor phase including the methylene beta-diketone monomer; and
iv. collecting the methylene beta-diketone monomer from the vapor phase.
5. The method according to Claim 1 wherein the reaction conditions include: a) an initiating temperature of between about 60 °C and about 130 °C; and b) atmospheric pressure.
6. The method according to Claim 2 wherein in step (b)(i), the reaction complex or the portion thereof is substantially vaporized in a time period selected from less than 15 minutes, less than 1 minute, less than 30 seconds, or less than 1 second.
7. The method of Claim 2, wherein the reaction complex is vaporized continuously upon formation in step (a).
8. A method of preparing a methylene beta-diketone monomer comprising: a) reacting a beta-diketone reactant having the structural formula:
Figure imgf000056_0001
under suitable reaction conditions for sufficient time with a source of formaldehyde, optionally in the presence of an acidic or basic catalyst, and optionally in the presence of an acidic or non-acidic solvent, to form a reaction complex; b) contacting the reaction complex, or a portion thereof, with an energy transfer means at a temperature between about 150°C and about 300°C to provide the reaction complex, or portion thereof, as a vapor phase; and
C) isolating a methylene beta-diketone monomer from the reaction complex or portion thereof, wherein the methylene beta-diketone monomer has the structural formula:
Figure imgf000056_0002
wherein each instance of Ri and R2 are independently Q-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci- Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, Ci- Ci5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein Ri and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-G5 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-Q5 alkyl), heteroaryl, C1-C15 alkoxy, Q- Ci5 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
9. The method according to Claim 1 or 8 wherein the source of formaldehyde includes paraformaldehyde, formalin, tiroxane or gaseous formaldehyde, or any combination thereof.
10. The method according to Claim 1 or 8, wherein the reacting step (a) is performed at about 60 °C to about 130 °C.
11. The method according to Claim 2 or 8 wherein the energy transfer means is at least one member of the group selected from a heat transfer agent, a heat exchanger, a laser, microwave energy, sonic energy, electromagnetic energy, and a source of radiation.
12. The method of Claim 11, wherein the heat transfer agent is a heated inert gas, one or more metal beads, one or more glass beads, one or more porcelain beads, sand, silica, silicone oil, mineral oil, a petroleum based heat transfer oil, a synthetic chemical based heat transfer oil, or a pre-formed portion of the reaction complex.
13. The method of Claim 11, wherein the heat exchanger is a shell and tube heat exchanger, a plate heat exchanger, and adiabatic wheel heat exchanger, a finned pipe heat exchanger, a plate fin heat exchanger, or a scraped surface heat exchanger.
14. The method of Claim 8, wherein isolating the methylene beta-diketone monomer includes condensing the vapor phase to a condensate.
15. The method of Claim 3 or 14, further including subjecting the condensate to a separation process selected from simple distillation, fractional distillation, flash distillation, steam distillation, vacuum distillation, short path distillation, thin-film distillation, reactive distillation, pervaporation, extractive distillation, flash evaporation, rotary evaporation, liquid/liquid extraction, centrifuging, or any combination thereof
16. The method according to Claim 8 wherein in step (b) the reaction complex, or portion thereof, is substantially vaporized in a time period selected from less than 15 minutes, less than 1 minute, less than 30 seconds, or less than 1 second.
17. The method of claim 1 or 8, wherein isolating the methylene beta-diketone monomer includes utilizing gas chromatography.
18. The method of Claim 2 or 14, wherein isolating the methylene beta-diketone monomer includes subjecting the condensate to liquid chromatography.
19. The method according to Claim 1 or 8, wherein the catalyst is a basic catalyst selected from the group consisting of potassium acetate, sodium acetate, zinc acetate, zinc diacetate dihydrate, aluminum acetate, calcium acetate, magnesium acetate, magnesium oxide, copper acetate, lithium acetate, aluminum oxide, or zinc oxide.
20. The method of Claim 1 or 8, wherein the catalyst is an acidic catalyst and is paratoluene sulfonic acid, dodecylbenzene sulfonic acid, borontrifluoride, zinc perchlorate, sulfated zirconium oxide, sulfated titanium oxide, lithium chloride, boron trifluoride etherate, ferric sulfate, zirconium oxychloride, cupric chloride, titanium tetrachloride, or zinc chloride.
21. The method of Claim 1 or 8, wherein the non-acidic solvent is tetrahydrofuran, chloroform, dichloromethane, toluene, heptane, ethyl acetate, n-butyl acetate or hexane.
22. The method of Claim 1 or 8, wherein the reaction complex comprises one or more oligomeric complexes.
23. The method of Claim 22, wherein the one or more oligomeric complexes are capable of forming the methylene beta-diketone monomer upon cracking.
24. The method of Claim 22, wherein the one or more oligomeric complexes independently comprise between 2 and 12 units able to yield methylene beta-diketone monomer upon depolymerization.
25. A methylene beta-diketone monomer having the structural formula:
Figure imgf000060_0001
wherein R1 and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy - (Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci- Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci- Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein R1 and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, Ci- Ci5 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
26. The methylene beta-diketone monomer according to Claim 25 having the following structural formula:
Figure imgf000060_0002
27. The methylene beta-diketone monomer according to Claim 26 being formed as a product of a reaction between 5,5-dimethylhexane-2,4-dione and formaldehyde.
28. The methylene beta-diketone monomer according to Claim 25 having the following structural formula:
29. The methylene beta-diketone monomer according to Claim 28 being formed as a product of a reaction between heptane-3,5-dione and formaldehyde.
30. The methylene beta-diketone monomer according to Claim 25 having the following structural formula:
Figure imgf000061_0002
31. The methylene beta-diketone monomer according to Claim 30 being formed as a product of a reaction between 5-methylhexane-2,4-dione and formaldehyde.
32. The methylene beta-diketone monomer according to Claim 25 having following structural formula:
Figure imgf000062_0001
33. The methylene beta-diketone monomer according to Claim 32 being formed as a product of a reaction between l-phenylbutane-l,3-dione and formaldehyde.
34. The methylene beta-diketone monomer according to Claim 25 having the following structural formula:
Figure imgf000062_0002
35. The methylene beta-diketone monomer according to Claim 34 being formed as a product of a reaction between l,3-diphenylpropane-l,3-dione and formaldehyde.
36. The methylene beta-diketone monomer according to Claim 25 having the following structural formula:
Figure imgf000063_0001
37. The methylene beta-diketone monomer according to Claim 36 being formed as a product of a reaction between nonane-4,6-dione and formaldehyde.
38. The methylene beta-diketone monomer according to Claim 25 having the formula:
Figure imgf000063_0002
Figure imgf000064_0001
39. A methylene beta-diketone monomer prepared according to any one of the methods of Claims 1- 24 and having the structural formula:
Figure imgf000064_0002
wherein R1 and R2 are independently C1-C15 alkyl, C2-C15 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Cis alkyl), or alkoxy - (Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci- Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-Gs cycloalkyl), heterocyclyl, heterocyclyl-(Ci- Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester; or wherein R1 and R2 are taken together with the atoms to which they are bound to form a 5-7 membered heterocyclic ring which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, Q- Ci5 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
40. A polymerizable composition comprising a methylene beta-diketone monomer of any one of Claims 25-39 wherein the composition is capable of bonding glass to a substrate in a time period selected from less than about 90 seconds, less than about 60 seconds, less than about 30 seconds, or less than about 15 seconds.
41. A polymerizable composition comprising a methylene beta-diketone monomer of any one of Claims 25-39 and at least one additive selected from the group consisting of an acidic stabilizer, a free radical stabilizer, a sequestering agent, a cure accelerator, a rheology modifier, a plasticizing agent, a thixotropic agents, a natural rubber, a synthetic rubber, a filler agent and a reinforcing agent.
42. The polymerizable composition according to Claim 40 or 41 wherein the composition is at least one member of the group consisting of an adhesive, an ink, a paint, a coating, a sealant, a composite, or a surfactant.
43. The polymerizable composition according to Claim 40 or 41 wherein said composition remains stable at 25 °C and at atmospheric pressure for a time period selected from more than 10 days, more than 15 days, more than 20 days, more than 25 days, more than 30 days.
44. The polymerizable composition according to Claim 40 or 41 wherein said composition remains stable at 82 °C and at atmospheric pressure for more than 2 hours.
45. The polymerizable composition according to Claim 41 comprising the acidic stabilizer, wherein the acidic stabilizer is present in a concentration of about 0.1 ppm to about 100 ppm, about 0.1 ppm to about 25 ppm, about 0.1 ppm to about 15 ppm, by weight of the composition.
46. The polymerizable composition according to Claim 41 comprising the free radical stabilizer, wherein the free radical stabilizer is present in a concentration selected from about 0.1 ppm to about 10000 ppm; about 0.1 ppm to about 3000 ppm; about 0.1 ppm to 1500 ppm; about 0.1 ppm to about 1000 ppm, about 0.1 ppm to about 300 ppm; about 0.1 ppm to about 150 ppm, by weight of the composition.
47. The polymerizable composition according to Claim 41 comprising the sequestering agent, wherein the sequestering agent is a crown ether, a silyl crown, a calixarene, a polyethylene glycol, or a combination thereof.
48. The polymerizable composition according to claim 41 comprising the cure accelerator, wherein the cure accelerator is at least one member of the group selected from sodium acetate, potassium acetate, tetrabutyl ammonium fluoride, tetrabutyl ammonium chloride, tetrabutyl ammonium hydroxide, a benzoate salt, a 2,4- pentanedionate salt, a sorbate salt, and a propionate salt.
49. The polymerizable composition according to claim 41 comprising the rheology modifier, wherein the rheology modifier is at least one member of the group selected from hydroxyethylcellulose, ethyl hydroxyethylcellulose, methylcellulose, a polymeric thickener, and pyrogenic silica.
50. An adhesive product comprising a methylene beta-diketone monomer according to any one of Claims 25-39.
51. The adhesive product according to Claim 50 having a shelf life of at least one year.
52. A polymer formed by polymerization of a polymerizable composition according to Claim 40 or 41.
53. The polymer according to Claim 52 wherein the polymer is at least one member a sealant, a coating, a textile fiber, a water-treatment polymer, an ink carrier, a paint carrier, a packaging film, a molding, a medical polymer, a polymer film, a polymer fiber, or a polymer sheet.
54. A polymer having repeat units of the formula:
Figure imgf000068_0001
wherein R and R' are independently Q-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C3-G5 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Ci5 alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-Q5 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
55. An oligomeric complex prepared by reacting a beta-diketone reactant with a source of formaldehyde; optionally in the presence of heat transfer agent; optionally in the presence of an acidic or basic catalyst; and optionally in the presence of an acidic or non-acidic solvent.
56. The oligomeric complex according to Claim 55, having between 2 and 12 repeat units having the structural formula:
Figure imgf000069_0001
wherein R and R' are independently Q-C15 alkyl, C2-Q5 alkenyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl-(Cl-C15 alkyl), heteroaryl or heteroaryl-(Ci-Ci5 alkyl), or alkoxy -(Cl-15 alkyl), each of which may be optionally substituted by C1-C15 alkyl, halo-(Ci-Ci5 alkyl), C3-C6 cycloalkyl, halo-(C3-C6 cycloalkyl), heterocyclyl, heterocyclyl-(Ci-Cis alkyl), aryl, aryl -(C1-C15 alkyl), heteroaryl, C1-C15 alkoxy, C1-C15 alkylthio, hydroxyl, nitro, azido, cyano, acyloxy, carboxy, or ester.
PCT/US2012/060840 2010-10-20 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom WO2013059479A2 (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
EP18152189.9A EP3339301A3 (en) 2011-10-19 2012-10-18 Methods for making methylene beta-diketone monomers
JP2014537250A JP2014532625A (en) 2011-10-19 2012-10-18 Methylene β-diketone monomer, process for producing methylene β-diketone monomer, polymerizable composition and product made therefrom
CA2853073A CA2853073A1 (en) 2011-10-19 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
US14/352,369 US9221739B2 (en) 2011-10-19 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
MX2014004782A MX360462B (en) 2011-10-19 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom.
EP12842121.1A EP2768897B1 (en) 2011-10-19 2012-10-18 Methods for making methylene beta-diketone monomers
US14/868,795 US9828324B2 (en) 2010-10-20 2015-09-29 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
US15/661,893 US10414839B2 (en) 2010-10-20 2017-07-27 Polymers including a methylene beta-ketoester and products formed therefrom
US15/678,533 US20170342011A1 (en) 2010-10-20 2017-08-16 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
US16/455,040 US20190315892A1 (en) 2010-10-20 2019-06-27 Polymers including a methylene beta-ketoester and products formed therefrom

Applications Claiming Priority (6)

Application Number Priority Date Filing Date Title
US201161549104P 2011-10-19 2011-10-19
US201161549152P 2011-10-19 2011-10-19
US201161549092P 2011-10-19 2011-10-19
US61/549,092 2011-10-19
US61/549,152 2011-10-19
US61/549,104 2011-10-19

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US14/075,334 Continuation-In-Part US20140248485A1 (en) 2010-10-20 2013-11-08 Synthesis of methylene malonates substantially free of impurities

Related Child Applications (2)

Application Number Title Priority Date Filing Date
US14/352,369 A-371-Of-International US9221739B2 (en) 2011-10-19 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
US14/868,795 Continuation-In-Part US9828324B2 (en) 2010-10-20 2015-09-29 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom

Publications (2)

Publication Number Publication Date
WO2013059479A2 true WO2013059479A2 (en) 2013-04-25
WO2013059479A3 WO2013059479A3 (en) 2013-07-11

Family

ID=48141622

Family Applications (3)

Application Number Title Priority Date Filing Date
PCT/US2012/060840 WO2013059479A2 (en) 2010-10-20 2012-10-18 Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
PCT/US2012/060830 WO2013059473A2 (en) 2011-10-19 2012-10-18 Multifunctional monomers, methods for making multifunctional monomers, polymerizable compositions and products formed therefrom
PCT/US2012/060837 WO2013066629A1 (en) 2010-10-20 2012-10-18 Methylene beta-ketoester monomers, methods for making methylene beta-ketoester monomers, polymerizable compositions and products formed therefrom

Family Applications After (2)

Application Number Title Priority Date Filing Date
PCT/US2012/060830 WO2013059473A2 (en) 2011-10-19 2012-10-18 Multifunctional monomers, methods for making multifunctional monomers, polymerizable compositions and products formed therefrom
PCT/US2012/060837 WO2013066629A1 (en) 2010-10-20 2012-10-18 Methylene beta-ketoester monomers, methods for making methylene beta-ketoester monomers, polymerizable compositions and products formed therefrom

Country Status (6)

Country Link
US (7) US9527795B2 (en)
EP (6) EP3339301A3 (en)
JP (3) JP2014532625A (en)
CA (3) CA2853068A1 (en)
MX (3) MX360463B (en)
WO (3) WO2013059479A2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9144796B1 (en) 2009-04-01 2015-09-29 Johnson Matthey Public Limited Company Method of applying washcoat to monolithic substrate
US9315597B2 (en) * 2014-09-08 2016-04-19 Sirrus, Inc. Compositions containing 1,1-disubstituted alkene compounds for preparing polymers having enhanced glass transition temperatures
DE102017204525A1 (en) 2016-03-23 2017-09-28 Basf Se Laminated laminates for flexible packaging
WO2018086860A1 (en) 2016-11-09 2018-05-17 Basf Se Polyurethane-vinyl hybrid polymers, methods of making them and their use
WO2019137853A1 (en) 2018-01-09 2019-07-18 Basf Se Compositions comprising polymerizable vinyl compounds, inorganic or organic fillers and their use
DE102019219214A1 (en) 2018-12-17 2020-06-18 Basf Se Compositions comprising multifunctional vinyl compounds in mini-emulsion and their use as crosslinkers for polymers

Families Citing this family (67)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9828324B2 (en) 2010-10-20 2017-11-28 Sirrus, Inc. Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
US10414839B2 (en) 2010-10-20 2019-09-17 Sirrus, Inc. Polymers including a methylene beta-ketoester and products formed therefrom
US9249265B1 (en) 2014-09-08 2016-02-02 Sirrus, Inc. Emulsion polymers including one or more 1,1-disubstituted alkene compounds, emulsion methods, and polymer compositions
US9279022B1 (en) 2014-09-08 2016-03-08 Sirrus, Inc. Solution polymers including one or more 1,1-disubstituted alkene compounds, solution polymerization methods, and polymer compositions
MX360463B (en) 2011-10-19 2018-11-05 Sirrus Inc Methylene beta-ketoester monomers, methods for making methylene beta-ketoester monomers, polymerizable compositions and products formed therefrom.
JP6345644B2 (en) * 2012-03-30 2018-06-20 シラス・インコーポレイテッド Ink formulations and coating formulations and polymerizable systems for making them
EP3153530B1 (en) 2012-03-30 2021-02-24 Sirrus, Inc. Composite and laminate articles and polymerizable systems for producing the same
US10047192B2 (en) 2012-06-01 2018-08-14 Sirrus, Inc. Optical material and articles formed therefrom
WO2014078689A1 (en) 2012-11-16 2014-05-22 Bioformix Inc. Plastics bonding systems and methods
US10607910B2 (en) 2012-11-30 2020-03-31 Sirrus, Inc. Composite compositions for electronics applications
EP2943462B1 (en) 2013-01-11 2018-06-27 Sirrus, Inc. Method to obtain methylene malonate via bis(hydroxymethyl) malonate pathway
US9416091B1 (en) 2015-02-04 2016-08-16 Sirrus, Inc. Catalytic transesterification of ester compounds with groups reactive under transesterification conditions
US10501400B2 (en) 2015-02-04 2019-12-10 Sirrus, Inc. Heterogeneous catalytic transesterification of ester compounds with groups reactive under transesterification conditions
US9334430B1 (en) 2015-05-29 2016-05-10 Sirrus, Inc. Encapsulated polymerization initiators, polymerization systems and methods using the same
US9217098B1 (en) 2015-06-01 2015-12-22 Sirrus, Inc. Electroinitiated polymerization of compositions having a 1,1-disubstituted alkene compound
EP3445830A1 (en) 2016-04-21 2019-02-27 Zephyros Inc. Malonates and derivatives for in-situ films
US9518001B1 (en) 2016-05-13 2016-12-13 Sirrus, Inc. High purity 1,1-dicarbonyl substituted-1-alkenes and methods for their preparation
WO2017210084A1 (en) 2016-06-03 2017-12-07 Sirrus, Inc. Water absorbing or water soluble polymers, intermediate compounds, and methods thereof
JP2019522064A (en) * 2016-06-03 2019-08-08 シラス・インコーポレイテッド Water-absorbing or water-soluble polymers, intermediate compounds, and methods thereof
US10196481B2 (en) 2016-06-03 2019-02-05 Sirrus, Inc. Polymer and other compounds functionalized with terminal 1,1-disubstituted alkene monomer(s) and methods thereof
US10428177B2 (en) 2016-06-03 2019-10-01 Sirrus, Inc. Water absorbing or water soluble polymers, intermediate compounds, and methods thereof
US9617377B1 (en) 2016-06-03 2017-04-11 Sirrus, Inc. Polyester macromers containing 1,1-dicarbonyl-substituted 1 alkenes
CN109219642A (en) * 2016-06-03 2019-01-15 赛鲁斯股份有限公司 With the functionalized polymer of end 1,1- disubstituted olefin monomer and other compounds and methods
US9567475B1 (en) 2016-06-03 2017-02-14 Sirrus, Inc. Coatings containing polyester macromers containing 1,1-dicarbonyl-substituted 1 alkenes
WO2018022780A1 (en) 2016-07-26 2018-02-01 Ppg Industries Ohio, Inc. Polyurethane coating compositions containing 1,1-di-activated vinyl compounds and related coatings and processes
EP3490784B1 (en) 2016-07-26 2022-10-12 PPG Industries Ohio, Inc. Three-dimensional printing processes using 1,1-di-activated vinyl compounds
US11130867B2 (en) 2016-07-26 2021-09-28 Ppg Industries Ohio, Inc. Curable compositions containing 1,1-di-activated vinyl compounds and related coatings and processes
EP3490726B1 (en) * 2016-07-26 2022-11-30 PPG Industries Ohio, Inc. Multi-layer curable compositions containing 1,1-di-activated vinyl compound products and related processes
ES2930531T3 (en) 2016-07-26 2022-12-16 Ppg Ind Ohio Inc Particles having surfaces functionalized with 1,1-diactivated vinyl compounds
US10961403B2 (en) 2016-07-26 2021-03-30 Ppg Industries Ohio, Inc. Electrodepositable coating compositions containing 1,1-di-activated vinyl compounds
ES2930756T3 (en) 2016-07-26 2022-12-21 Ppg Ind Ohio Inc Acid-Catalyzed Curable Coating Compositions Containing 1,1-Diactivated Vinyl Compounds and Related Coatings and Processes
US11634524B2 (en) 2016-07-26 2023-04-25 Ppg Industries Ohio, Inc. Acid-catalyzed curable coating compositions containing 1,1 di-activated vinyl compounds and related coatings and processes
EP3515973A1 (en) 2016-09-19 2019-07-31 Zephyros Inc. Malonate and cyanoacrylate adhesives for joining dissimilar materials
EP3515994B1 (en) 2016-09-19 2024-01-24 Zephyros Inc. Method for sealing porous substrates
US10934411B2 (en) 2016-09-30 2021-03-02 Ppg Industries Ohio, Inc. Curable compositions containing 1,1-di-activated vinyl compounds that cure by pericyclic reaction mechanisms
MY176736A (en) * 2017-05-18 2020-08-20 Namics Corp Resin composition
US11591425B2 (en) 2017-06-02 2023-02-28 Arkema France Curable compositions and uses thereof
CN107225048B (en) * 2017-07-01 2019-07-12 山东金城柯瑞化学有限公司 Coal flotation agent
WO2019055710A1 (en) 2017-09-13 2019-03-21 Zephyros, Inc. Composite structures for localized stiffening
JP6427848B1 (en) * 2017-10-17 2018-11-28 ナミックス株式会社 Resin composition
US11230617B2 (en) 2017-10-31 2022-01-25 Namics Corporation Resin composition
EP3732257A1 (en) * 2017-12-27 2020-11-04 Basf Se A composition, its preparation method, and the use of the composition in construction application
JP2021510755A (en) * 2018-01-12 2021-04-30 シラス・インコーポレイテッド Emulsion polymer crosslinked with a compound containing two or more dicarbonyl substituted 1 alkene units
KR102540734B1 (en) 2018-02-01 2023-06-08 삼성디스플레이 주식회사 Organic light emitting display apparatus and method of manufacturing thereof
CN111954659A (en) * 2018-04-03 2020-11-17 赛鲁斯股份有限公司 Heterogeneously catalyzed transesterification of ester compounds comprising groups reactive under transesterification conditions
US11028294B2 (en) 2018-08-10 2021-06-08 International Business Machines Corporation Armonk, New York Acrylate-cyanoacrylate monomers
WO2020068916A1 (en) 2018-09-26 2020-04-02 Swimc Llc Curable coating compositions
EP3865519B1 (en) 2018-10-05 2023-04-19 Namics Corporation Resin composition
EP3865520B1 (en) * 2018-10-09 2024-02-28 Namics Corporation Curing agent composition for curing 2-methylene-1,3-dicarbonyl compound
JP7219594B2 (en) * 2018-11-15 2023-02-08 株式会社日本触媒 PSA COMPOSITION, ARTICLES CONTAINING THE SAME, AND METHOD FOR MANUFACTURING ADHESIVE PRODUCTS
JP7191979B2 (en) 2018-11-15 2022-12-19 株式会社日本触媒 Acrylic resin composition, crosslinked product and method for producing crosslinked product
WO2020123579A1 (en) 2018-12-11 2020-06-18 Sirrus, Inc. Polymerization of 1,1-dicarbonyl 1-alkenes
WO2020123581A1 (en) 2018-12-11 2020-06-18 Sirrus, Inc. Emulsion polymers of 1,1-dicarbonyl 1-alkenes of controlled particle size
WO2020158756A1 (en) * 2019-01-29 2020-08-06 株式会社日本触媒 Curing agent, method for producing cement structure with coating film, shrinkage reduction method and drying suppression method for cement molded body, and method for suppressing penetration of deterioration factor into cement structure
WO2020167621A1 (en) 2019-02-14 2020-08-20 Sirrus, Inc. Particles encapsulated with dicarbonyl-substituted-1- alkenes
WO2021014219A2 (en) 2019-07-19 2021-01-28 Arkema France Curable compositions useful for obtaining non-sensitizing cured products
CN114391025B (en) * 2019-10-18 2023-07-07 纳美仕有限公司 Polymerizable composition and curable resin composition using same
CN110903194B (en) * 2019-12-11 2022-02-25 南京恒道医药科技有限公司 Method for continuously preparing voriconazole intermediate ethyl 2-fluoro-3-oxopentanoate
CN111044647A (en) * 2019-12-20 2020-04-21 广电计量检测(合肥)有限公司 Sample pretreatment and quantitative analysis method for detecting linear alkylbenzene in water body
WO2021150844A1 (en) 2020-01-24 2021-07-29 Sirrus, Inc. Compositions containing 1,1-disubstituted activated alkenes useful in additive manufacturing and articles formed therefrom
WO2021162938A1 (en) 2020-02-10 2021-08-19 Sirrus, Inc. Copolymers of dicarbonyl substituted-1-alkene and olefins and methods to make them
WO2021231288A1 (en) 2020-05-15 2021-11-18 Nippon Shokubai Co., Ltd. Improved dicarbonyl substituted-1-alkene compositions
WO2021252594A1 (en) 2020-06-11 2021-12-16 Nippon Shokubai Co., Ltd. Polyesters prepared from 1,1-diester-1-alkenes containing a strong acid and stabilizer
WO2022126268A1 (en) * 2020-12-17 2022-06-23 The Royal Institution For The Advancement Of Learning / Mcgill University Chemical additives and their use thereof for modifying mechanical properties of pvc and preventing the formation of surface defects during pvc calendering
KR20240141242A (en) 2022-02-07 2024-09-26 나믹스 가부시끼가이샤 Resin composition and curable resin composition using the same
WO2023149445A1 (en) * 2022-02-07 2023-08-10 ナミックス株式会社 Liquid polymerizable composition and curable resin composition using same
EP4286677A1 (en) 2022-06-02 2023-12-06 Linde GmbH Method of operating an internal combustion engine and corresponding arrangement

Family Cites Families (275)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB432628A (en) 1933-12-23 1935-07-23 John David Kendall Improvements in or relating to the production of compounds containing an ethylenic linkage, or a polymethine chain
US2277479A (en) 1938-08-13 1942-03-24 Gen Electric Acetoacetic ester-formaldehyde resins
US2230033A (en) * 1939-01-04 1941-01-28 James W Hackett Foot exerciser
US2245567A (en) * 1939-06-23 1941-06-17 Eastman Kodak Co Manufacture of unsaturated ketones
US2313501A (en) 1939-08-15 1943-03-09 Eastman Kodak Co Process for preparing methylene dialkyl malonates
US2212506A (en) 1939-08-15 1940-08-27 Eastman Kodak Co Preparation of methylene dialkyl malonates
US2403791A (en) 1939-11-16 1946-07-09 Gen Electric Interpolymers of a methylene malonic ester and an unsaturated alkyd resin
US2330033A (en) 1939-11-16 1943-09-21 Gen Electric Method of preparing methylene malonic esters
US2569767A (en) * 1946-05-27 1951-10-02 L D Caulk Company Dental material and method
US2730457A (en) 1953-06-30 1956-01-10 Ncr Co Pressure responsive record materials
US3042710A (en) * 1960-10-03 1962-07-03 Borden Co Ethenoid carbonyl compounds
DE1569968B1 (en) 1960-10-19 1969-11-06 Eastman Kodak Co Use of highly purified monomeric esters of methylenemalonic acid as autopolymerizable adhesives
US3197318A (en) 1960-11-07 1965-07-27 Borden Co 2-methylenemalonic acid ester contact adhesive compositions
GB965767A (en) * 1960-11-17 1964-08-06 Hoyt Harrison Todd Method of fusing materials to metal surfaces
FR1290837A (en) 1960-12-23 1962-04-20 Air Liquide New reducto-oxidizable anthraquinone polymers, their preparation processes and their application to the manufacture of hydrogen peroxide
GB975733A (en) 1961-12-18 1964-11-18 Ici Ltd Process for preventing haze formation in fermented beverages
US3203915A (en) 1962-07-02 1965-08-31 Dal Mon Research Co Oxygen convertible polymeric compositions
US3221745A (en) 1962-09-12 1965-12-07 Eastman Kodak Co Method of bonding body tissue together using methylenemalonic acid esters
US3427250A (en) 1963-03-25 1969-02-11 Polaroid Corp Microscopic capsules and process for their preparation
US3489663A (en) 1965-10-19 1970-01-13 Owens Illinois Inc Electrolytic polymerization
US3557185A (en) 1967-03-06 1971-01-19 Toa Gosei Chem Ind Stabilized alpha-cyanoacrylate adhesive compositions
US4105688A (en) 1968-05-09 1978-08-08 Lonza, Ltd. Process for the production of malonic acid dinitrile and purification thereof
US3595869A (en) 1968-05-15 1971-07-27 Merck & Co Inc Process for preparing a diastereomer of an optically active ester or amide of (cis-1,2-epoxypropyl)-phosphonic acid
US3591676A (en) 1968-11-01 1971-07-06 Eastman Kodak Co Surgical adhesive compositions
DE2027502C3 (en) 1970-05-29 1980-06-19 Schering Ag, 1000 Berlin Und 4619 Bergkamen Process for the production of cyanoacrylic acid esters
US3677989A (en) 1970-06-16 1972-07-18 Union Carbide Corp Ethylene/acrylic acid copolymer emulsions
DE2042610C3 (en) 1970-08-27 1979-03-15 Wacker-Chemie Gmbh, 8000 Muenchen Process for the preparation of methylene malonic ester
US3940362A (en) 1972-05-25 1976-02-24 Johnson & Johnson Cross-linked cyanoacrylate adhesive compositions
US3975422A (en) 1972-11-21 1976-08-17 Johnson & Johnson Preparation of bis (2-cyanoacrylate)monomers
US3923836A (en) 1973-07-18 1975-12-02 Smithkline Corp Chroman and chromene compounds
US3973438A (en) 1973-08-21 1976-08-10 Westinghouse Electric Corporation Composition for forming thermo-particulating coating which protects electrical apparatus
US4079058A (en) 1973-08-29 1978-03-14 Dynamit Nobel Ag Process of performing cyclization reactions using benzyl or pyridylamino malonic acid derivatives
CH582655A5 (en) 1973-10-18 1976-12-15 Lonza Ag
US3945891A (en) 1974-06-20 1976-03-23 Fmc Corporation Distillation process for purification of triaryl phosphate esters
US3966562A (en) 1974-07-31 1976-06-29 Agency Of Industrial Science & Technology Multi-stage flash distillation plant
US4018656A (en) 1974-09-03 1977-04-19 Bechtel International Corporation Thermal softening and distillation by regenerative method
US4004984A (en) 1975-02-07 1977-01-25 Aktiebolaget Atomenergi Distillation plant
US4148693A (en) 1975-02-26 1979-04-10 Williamson William R Horizontal cylindrical distillation apparatus
US3978422A (en) 1975-02-28 1976-08-31 Alpha Engineering Corporation Broadband automatic gain control amplifier
US3995489A (en) 1975-04-15 1976-12-07 Westinghouse Electric Corporation Malonic acid derivative composition for forming thermoparticulating coating
US4046943A (en) 1975-04-15 1977-09-06 Westinghouse Electric Corporation Malonic acid derivative composition for forming thermoparticulating coating
US4001345A (en) 1975-06-02 1977-01-04 Ppg Industries, Inc. Distillation of methylchloroform
SU614742A3 (en) 1975-06-02 1978-07-05 Динамит Нобель Аг (Фирма) Method of obtaining c1-c4 dialkyl esters of malonic acid
US4036985A (en) 1975-07-16 1977-07-19 Jose Amato Mono substituted malonic acid diamides and process of preparing them
US4083751A (en) 1975-08-11 1978-04-11 Occidental Petroleum Corporation Continuous feed pyrolysis chamber for decomposing solid waste
DE2647452A1 (en) 1975-11-07 1977-05-18 Ciba Geigy Ag NEW HYDROXYBENZYLMALONIC ACID DERIVATIVES
US4186060A (en) 1976-04-28 1980-01-29 Fogel S J Method and apparatus for high volume distillation of liquids
US4282067A (en) 1976-04-28 1981-08-04 Jerome Katz Apparatus for high volume distillation of liquids
US4319964A (en) 1976-04-28 1982-03-16 Jerome Katz Apparatus for high volume distillation of liquids
US4186058A (en) 1976-04-28 1980-01-29 Fogel S J Method and apparatus for high volume distillation of liquids
US4035243A (en) 1976-04-28 1977-07-12 Jerome Katz Method and apparatus for high volume distillation of liquids
US4154914A (en) 1976-05-01 1979-05-15 Toyo Seal Kogyo Kabushiki Kaisha (Toyo Seal Industries Co., Ltd.) Process for producing acrylic rubber by copolymerizing acrylic ester and malonic acid derivative having active methylene group
US4236975A (en) 1976-06-11 1980-12-02 Phillips Petroleum Company Recovery of methyl heptafluorobutyrate from water by distillation
US4224112A (en) 1976-06-11 1980-09-23 Phillips Petroleum Company Recovery of 1,1-dihydroheptafluorobutanol from water by distillation
US4229263A (en) 1976-06-11 1980-10-21 Phillips Petroleum Company Recovery of methyl heptafluorobutyrate from methanol by distillation
US4080238A (en) 1976-07-14 1978-03-21 Pratt & Lambert, Inc. One-liquid cold setting adhesive with encapsulated catalyst initiator
US4049698A (en) 1976-08-05 1977-09-20 Eastman Kodak Company Process for producing methylene malonic esters
US4118422A (en) 1976-08-23 1978-10-03 Texaco Development Corp. Polyols from 2,3-morpholinediones
US4056543A (en) 1976-09-07 1977-11-01 Eastman Kodak Company Process of preparing substituted acrylates
US4160864A (en) 1976-09-07 1979-07-10 Eastman Kodak Company Adhesive compositions comprising methyl allyl methylenemalonate
US4282071A (en) 1977-04-25 1981-08-04 The Dow Chemical Company Anhydrous separation of volatile aluminum chloride complex from an ethylbenzene production stream by distillation
DE2861955D1 (en) 1977-12-02 1982-09-02 Ciba Geigy Ag Malonic acid derivatives of sterically hindered piperidines, process for their preparation and stabilised organic matter
US4176012A (en) 1978-01-10 1979-11-27 Bryant Jeffrey J Adjacent loop distillation
US4243493A (en) 1978-02-03 1981-01-06 Mannesmannrohren-Werke A.G. Process for transportation and distillation of petroleum with methanol
US4256908A (en) 1978-07-03 1981-03-17 Ube Industries, Ltd. Process for preparing diesters of malonic acid
JPS5647471A (en) 1979-09-28 1981-04-30 Japan Synthetic Rubber Co Ltd Instantaneous adhesive composition
JPS5667383A (en) 1979-11-08 1981-06-06 Mitsui Petrochem Ind Ltd Thixotropic agent
US4440601A (en) 1980-01-28 1984-04-03 Jerome Katz Method and apparatus for high volume fractional distillation of liquids
US4291171A (en) 1980-08-20 1981-09-22 The United States Of America As Represented By The Secretary Of The Navy Esters of 2-fluoro-2,2-dinitroethylmalonate and 2,2-dinitropropylmalonate
DE3105718A1 (en) 1981-02-17 1982-09-02 Hoechst Ag, 6000 Frankfurt FOR FOODSTUFFS, ESPECIALLY SAUSAGE PRODUCTS, SUITABLE SMOKE-PERMITTING TUBULAR SLEEVE WITH A STITCHED STITCH AND METHOD FOR THE PRODUCTION THEREOF
US4329479A (en) 1981-04-07 1982-05-11 Nihon Nohyaku Co., Ltd. Process for producing 1,3-dithiol-2-ylidene malonic acid dialkyl esters
US4450067A (en) 1981-04-30 1984-05-22 Mobil Oil Corporation Distillation-induced extraction process
US4897473A (en) 1981-05-01 1990-01-30 Union Carbide Chemicals And Plastics Company Inc. Homologation of carbonyloxy containing compounds
US4444928A (en) 1981-08-14 1984-04-24 Ciba-Geigy Corporation Polymeric malonic acid derivatives
JPS5867647A (en) 1981-10-15 1983-04-22 Ube Ind Ltd Preparation of malonic diester
US4440910A (en) 1982-01-18 1984-04-03 Loctite Corporation Toughened cyanoacrylates containing elastomeric rubbers
GB2115031B (en) 1982-01-29 1985-09-18 Andres Galvez Figari Cast floors
JPS597193A (en) 1982-07-02 1984-01-14 Shionogi & Co Ltd Isomerization of malonylmethyl group
EP0103233B1 (en) 1982-08-31 1987-11-25 Daikin Kogyo Co., Ltd. A method to trap the enolate ion of the malonic acid or its derivatives
US4411740A (en) 1982-09-20 1983-10-25 Dow Corning Corporation Separation of chlorosilanes by extractive distillation
DE3241512A1 (en) 1982-11-10 1984-05-10 Bayer Ag, 5090 Leverkusen SUBSTITUTED MALONIC ACID DIAMOND, METHOD FOR THE PRODUCTION THEREOF AND THEIR USE AS A PEST CONTROL
FR2540739A1 (en) 1983-02-11 1984-08-17 Elf France DEVICE AND FACILITIES FOR THIN-FILM EVAPORATION DISTILLATION, ESPECIALLY FOR HYDROCARBONS, AND METHOD OF IMPLEMENTING SAID DEVICE
US4517105A (en) 1983-03-07 1985-05-14 Aluminum Company Of America Metalworking lubricant composition containing a novel substituted malonic acid diester
AT379602B (en) * 1983-07-11 1986-02-10 Vianova Kunstharz Ag METHOD FOR PRODUCING CROSSLINKING COMPONENTS FOR LACQUER BINDING AGENTS
US4503074A (en) 1983-08-08 1985-03-05 Merck & Co., Inc. Halogenated geminal diesters
US4767503A (en) 1983-08-29 1988-08-30 Allied Corporation Removal of light impurities from caprolactam by distillation with water
US4728701A (en) * 1983-09-19 1988-03-01 Jarvis Marvin A Process for the polymerization of acrylates
US4560723A (en) 1983-11-14 1985-12-24 Minnesota Mining And Manufacturing Company Cyanoacrylate adhesive composition having sustained toughness
AT380008B (en) 1983-12-23 1986-03-25 Chemie Linz Ag METHOD FOR PRODUCING MONO OR BISCARBONYL COMPOUNDS
DE3400401A1 (en) 1984-01-07 1985-08-22 Bayer Ag, 5090 Leverkusen SUBSTITUTED MALONIC ACID DERIVATIVES, METHOD FOR THE PRODUCTION THEREOF AND THEIR USE AS A PEST CONTROL
US4720543A (en) 1985-06-06 1988-01-19 Georgetown University 1a-7-substituted derivatives of mitomycin and uses thereof
US4613658A (en) 1985-10-15 1986-09-23 University Of Southern Mississippi Vinyl monomers capable of forming side-chain liquid crystalline polymers and the resulting polymers
US4724053A (en) 1985-12-20 1988-02-09 Polaroid Corporation, Patent Dept. Method for the electropolymerization of conductive polymers
CA1222845A (en) * 1986-02-06 1987-06-09 Progressive Chemical Research Ltd. Silicone-sulfone and silicone-fluorocarbon-sulfone gas permeable contact lenses and compositions thereof
US5292937A (en) 1986-03-31 1994-03-08 Rhone-Poulenc Inc. Use of malonic acid derivative compounds for retarding plant growth
JPS62260879A (en) 1986-05-07 1987-11-13 Matsumoto Seiyaku Kogyo Kk Adhesive composition
US4783242A (en) 1986-05-22 1988-11-08 The Dow Chemical Company Distillation system and process
IT1196500B (en) 1986-07-16 1988-11-16 Eniricerche Spa MALONIC ACID DERIVATIVES AND METHODS FOR THEIR SYNTHESIS
JPS6342135A (en) 1986-08-08 1988-02-23 Shinkawa Ltd Wire bonding method
JPS63159385A (en) 1986-08-29 1988-07-02 Nippon Nohyaku Co Ltd Malonic acid derivative, production and use thereof
US5446195A (en) 1986-09-02 1995-08-29 West Point Pepperell Water-soluble active methylenes as formaldehyde scavengers
HU197574B (en) 1986-10-09 1989-04-28 Chinoin Gyogyszer Es Vegyeszet Process for production of derivatives of 3,7-dihydro-3-methil-7-//1,2,4-oxadiasole/-3-il/alkylenil/-1h-purin-2,6-dion and medical compositions containing these substances
US4736056A (en) 1986-12-15 1988-04-05 Smith Oliver W Process for the production of malonic acid derivative compounds
JPH087443B2 (en) * 1986-12-29 1996-01-29 凸版印刷株式会社 High resolution positive type radiation sensitive resist
FR2611705B1 (en) 1987-03-05 1989-07-13 Union Pharma Scient Appl PROCESS FOR THE PREPARATION OF MONESTERS OR DIESTERS OF ENDOETHANO-9, 10 DIHYDRO-9, 10 ANTHRACENE BICARBOXYLIC ACID-11, 11, NOVEL MONESTERS OR DIESTERS THUS PREPARED AND THE USE THEREOF FOR THE PREPARATION OF ASYMENEMRICAL SYMMETRICS
US4828882A (en) 1987-03-16 1989-05-09 Canadian Patents & Developments Limited Particle encapsulation technique
DE3733552A1 (en) 1987-10-03 1989-04-13 Herberts Gmbh CATHODICALLY DETACHABLE WAFER ACID DYED COATING AGENT AND THE USE THEREOF
US5021486A (en) 1989-03-21 1991-06-04 Ciba-Geigy Corporation Hindered amine-substituted malonic acid derivatives of s-triazine
JPH02281013A (en) 1989-04-24 1990-11-16 Cemedine Co Ltd Diketone compound copolymer
DE3934190A1 (en) 1989-10-13 1991-04-18 Basf Ag MALONIC ACID DYES AND THEIR POLYCONDENSATION PRODUCTS
DE4009621A1 (en) 1990-03-26 1991-10-02 Henkel Kgaa (ALPHA) -CYANACRYLATE ADHESIVE COMPOSITIONS
US5284987A (en) 1990-06-15 1994-02-08 Amoco Corporation Preparation of a dimethyltetralin in a distillation reactor
US5227027A (en) 1990-08-23 1993-07-13 Topper Robert T High efficiency water distillation apparatus using a heat pump system and process for use thereof
US5064507A (en) 1990-09-27 1991-11-12 Allied-Signal Inc. Distillation process for recovery of high purity phenol
MX9200216A (en) 1991-01-21 1992-08-01 Lonza Ag PROCEDURE FOR THE PREPARATION OF MALONIC ACID ANHYDRIDE.
DE4114733A1 (en) 1991-05-06 1992-11-12 Huels Chemische Werke Ag METHOD FOR PRODUCING SUBSTITUTED MALONESTERANILIDES AND MALONIC ACID MONOANILIDES
JPH0517723A (en) 1991-07-10 1993-01-26 Three Bond Co Ltd Adhesive composition
US5259835A (en) 1991-08-29 1993-11-09 Tri-Point Medical L.P. Wound closure means and method using flowable adhesive
US5391624A (en) 1992-02-10 1995-02-21 S. C. Johnson & Son, Inc. Thermosettable compositions
US5328687A (en) 1993-03-31 1994-07-12 Tri-Point Medical L.P. Biocompatible monomer and polymer compositions
US5624669A (en) 1993-03-31 1997-04-29 Tri-Point Medical Corporation Method of hemostatic sealing of blood vessels and internal organs
US5567761A (en) 1993-05-10 1996-10-22 Guertin Bros. Coatings And Sealants Ltd. Aqueous two-part isocyanate-free curable, polyurethane resin systems
KR970010594B1 (en) 1993-10-16 1997-06-28 한국과학기술연구원 Platinum complexes of malonic acid derivatives and process for the preparation thereof
AU672337B2 (en) 1993-10-27 1996-09-26 Nippon Paint Co., Ltd. Curable resin composition for coating uses
EP0671409A3 (en) 1994-03-11 1996-06-12 Hoechst Ag Malonic acid derivatives having anti-adhesive properties.
DE4408248A1 (en) 1994-03-11 1995-09-14 Hoechst Ag Physiologically acceptable and physiologically degradable carbohydrate mimetics, process for their preparation and their use
BR9508139A (en) 1994-06-28 1999-11-30 Tri Point Medical Corp Process, process of regulating a biodegradation rate in vivo of a polymer and of joining together two surfaces in vivo, biocompatible composition, adhesive, sealant and surgical implant and delivery system for a therapeutic agent
US5550172A (en) 1995-02-07 1996-08-27 Ethicon, Inc. Utilization of biocompatible adhesive/sealant materials for securing surgical devices
DE19508049C2 (en) 1995-02-23 1997-02-06 Schering Ag Use of methylene malon diester derivatives for the production of gas-containing microparticles
JPH08231564A (en) * 1995-02-28 1996-09-10 Nippon Shokubai Co Ltd Phosphoric acid ester, its production and phosphoric acid ester polymer
US5614650A (en) 1995-03-07 1997-03-25 Sandler; Stanley R. Zirconium compounds of sulfonic acids
US5928611A (en) 1995-06-07 1999-07-27 Closure Medical Corporation Impregnated applicator tip
DE19541213A1 (en) 1995-11-04 1997-05-07 Rwe Dea Ag Process for the chemical conversion of substances in a reaction column
JPH09258448A (en) 1996-03-19 1997-10-03 Fujitsu Ltd Resist composition and production of semiconductor device using same
US6054606A (en) 1996-05-22 2000-04-25 Nippon Paint Co., Ltd. Method for preparing malonate group-containing acrylate monomers
DE19623142A1 (en) 1996-06-10 1997-12-11 Huels Chemische Werke Ag Enantiomerically enriched malonic acid monoesters substituted by a tertiary hydrocarbon radical and their preparation
DE19629372A1 (en) 1996-07-20 1998-01-22 Degussa Malonic acid or salt preparation
FR2755136B1 (en) 1996-10-25 1999-01-22 Virsol PROCESS FOR THE PREPARATION OF METHYLIDENE MALONATE NANOPARTICLES, NANOPARTICLES CONTAINING ONE OR MORE BIOLOGICALLY ACTIVE MOLECULES AND PHARMACEUTICAL COMPOSITIONS CONTAINING THEM
US6121689A (en) 1997-07-21 2000-09-19 Miguel Albert Capote Semiconductor flip-chip package and method for the fabrication thereof
DE19704449A1 (en) 1997-02-06 1998-08-13 Huels Chemische Werke Ag Process for the production of malonic and alkylmalonic acids
DE69834562T2 (en) 1997-02-20 2007-05-10 Mitsubishi Rayon Co., Ltd. PROCESS FOR THE PRODUCTION OF MALONIC ACID DERIVATIVES
DE19711762A1 (en) 1997-03-21 1998-09-24 Huels Chemische Werke Ag Process for the preparation of bishydroxymethyl compounds
DE19724074C2 (en) 1997-06-07 2000-01-13 Metallgesellschaft Ag Process for high-temperature short-term distillation of residual oils
WO1999001420A1 (en) 1997-07-03 1999-01-14 Taito Co., Ltd. Process for the preparation of 2-aminomalonic acid derivatives and intermediates used in the process
BR9704357A (en) 1997-08-13 1999-05-11 Trikem Sa Process for the production of malonic acid and malonic acid esters
US6353268B1 (en) 1997-08-22 2002-03-05 Micron Technology, Inc. Semiconductor die attachment method and apparatus
FR2774096B1 (en) 1998-01-29 2000-04-07 Virsol NOVEL SURFACTANT COPOLYMERS BASED ON METHYLIDENE MALONATE
US6291703B1 (en) 1998-02-09 2001-09-18 Ciba Specialty Chemicals Corporation Preparation of substituted hydroxyhydrocinnamate esters by continuous transesterification using reactive distillation
FR2775284B1 (en) * 1998-02-20 2000-04-21 Rhodia Chimie Sa PROCESS FOR THE PREPARATION OF KETONIC AROMATIC COMPOUNDS
AU2900999A (en) 1998-03-09 1999-09-27 Corning Incorporated Optical waveguide having non absorbing cladding region
FR2778100B1 (en) 1998-04-29 2001-05-04 Virsol NOVEL POLY (METHYLIDENE MALONATE) MICROSPHERES, PROCESS FOR THEIR PREPARATION AND PHARMACEUTICAL COMPOSITIONS CONTAINING THEM
WO1999055394A1 (en) * 1998-04-30 1999-11-04 Closure Medical Corporation Adhesive applicator with polymerization agents and/or bioactive material
US6512023B1 (en) 1998-06-18 2003-01-28 Closure Medical Corporation Stabilized monomer adhesive compositions
JP2000019936A (en) 1998-07-06 2000-01-21 Central Glass Co Ltd Manufacture of hologram and apparatus therefor
US6632518B1 (en) 1998-10-14 2003-10-14 E. I. Du Pont De Nemours And Company Fluoropolymer film structures and laminates produced therefrom
ATE253090T1 (en) 1998-12-07 2003-11-15 Bayer Ag COAGULATES OF AQUEOUS PURE DISPERSIONS AND THEIR USE
CA2358578A1 (en) 1999-01-02 2000-07-13 Aventis Pharma Deutschland Gmbh Novel malonic acid derivatives, processes for their preparation, their use and pharmaceutical compositions containing them (inhibition of factor xa activity)
JP2000199936A (en) * 1999-01-06 2000-07-18 Konica Corp Heat-developing photosensitive material
FR2788516B1 (en) 1999-01-14 2001-04-06 Virsol PROCESS FOR THE PREPARATION OF METHYLIDENE MALONATE POLYMER
FR2789314B1 (en) 1999-02-09 2001-04-27 Virsol WOUND SUTURE MATERIAL BASED ON METHYLIDENE MALONATE
US6197482B1 (en) 1999-05-14 2001-03-06 Eastman Kodak Company Polymer overcoat for imaging elements
AU768969B2 (en) 1999-05-27 2004-01-15 Nederlandse Organisatie Voor Toegepast- Natuurwetenschappelijk Onderzoek Tno Method for the purification of a liquid by membrane distillation, in particular for the production of desalinated water from seawater or brackish water or process water
US6210474B1 (en) 1999-06-04 2001-04-03 Eastman Kodak Company Process for preparing an ink jet ink
US6225038B1 (en) 1999-11-04 2001-05-01 Eastman Kodak Company Thermally processable imaging element
US6245933B1 (en) 1999-11-19 2001-06-12 Closure Medical Corporation Transesterification method for making cyanoacrylates
DE19959587B4 (en) 1999-12-10 2006-08-24 Lurgi Lentjes Ag Process for the gentle short-term distillation of residual oils
US6183593B1 (en) 1999-12-23 2001-02-06 Closure Medical Corporation 1,1-disubstituted ethylene adhesive compositions containing polydimethylsiloxane
AUPQ540200A0 (en) 2000-02-02 2000-02-24 Aquadyne Incorporated Water distillation systems
EP1254105A1 (en) 2000-02-10 2002-11-06 Lonza AG Method for producing alkoxy malonic acid dinitriles
EP1123915B1 (en) 2000-02-10 2004-07-28 Nippon Shokubai Co., Ltd. Process for producing alpha, beta-unsaturated carboxylic acid esters and catalyst for use in such process
EP1127884A1 (en) 2000-02-26 2001-08-29 Aventis Pharma Deutschland GmbH Novel malonic acid derivatives, processes for their preparation, their use as inhibitor of factor XA activity and pharmaceutical compositions containing them
EP1303578A2 (en) 2000-06-22 2003-04-23 The Lubrizol Corporation Acylating agents and dispersants for lubricating oil and fuels
JP5327825B2 (en) 2000-07-14 2013-10-30 メタボリックス,インコーポレイテッド Polyurethanes obtained from hydroxyalkanoates and isocyanates
US20040005314A1 (en) 2001-07-27 2004-01-08 Enrique Escandon Apo-2l receptor agonist and cpt-11 synergism
FR2812551B1 (en) 2000-08-07 2003-03-28 Virsol PHARMACEUTICAL FORM COMPRISING A METHYLIDENE MALONATE-BASED SUPPORT MATERIAL AND A CELL REGULATING FACTOR
ATE282650T1 (en) 2000-10-17 2004-12-15 Michelin Soc Tech METHOD FOR PRODUCING A DIENE ELASTOMER BY ANIONIC POLYMERIZATION
US6545097B2 (en) 2000-12-12 2003-04-08 Scimed Life Systems, Inc. Drug delivery compositions and medical devices containing block copolymer
US20020151629A1 (en) 2001-02-08 2002-10-17 Buffkin Halbert C. Protective coating
US7450290B2 (en) 2001-06-25 2008-11-11 University Of Washington Electropolymerization of enhanced electrochromic (EC) polymer film
JP3976663B2 (en) 2001-11-01 2007-09-19 横浜ゴム株式会社 One-component moisture-curing urethane resin composition
US6896838B2 (en) 2001-11-21 2005-05-24 Closure Medical Corporation Halogenated polymeric containers for 1, 1-disubstituted monomer compositions
US6767980B2 (en) 2002-04-19 2004-07-27 Nippon Shokubai Co., Ltd. Reactive diluent and curable resin composition
ATE415387T1 (en) 2002-05-15 2008-12-15 Genzyme Corp METHOD FOR PRODUCING BENZONITRILES AND BENZIMIDOIC ACID DERIVATIVES
US7629416B2 (en) 2002-08-12 2009-12-08 Exxonmobil Chemical Patents Inc. Plasticized polyolefin compositions
AU2003301426A1 (en) 2002-10-18 2004-05-04 Meiji Seika Kaisha, Ltd. Malonic acid monoesters and process for producing the same
US7056540B2 (en) 2002-10-29 2006-06-06 Council Of Scientific And Industrial Research Enzymatic process for the preparation of optically active alcohols from ketones using tuberous root Daucus carota
US6826341B2 (en) 2002-11-04 2004-11-30 Fitel Usa Corp. Systems and methods for reducing splice loss in optical fibers
TW200422397A (en) 2002-12-26 2004-11-01 Matsushita Electric Ind Co Ltd Water-soluble lubricant for metal working, and method and apparatus for metal working being suitable for using the same
DE10308504A1 (en) * 2003-02-26 2004-09-09 Basf Ag Enzymatic production of (meth) acrylic acid esters
EP1475367B1 (en) 2003-05-08 2010-07-07 Bayer MaterialScience AG Distillation process for separating diisocyanatodiphenylmethane isomers
US6767857B1 (en) 2003-05-29 2004-07-27 Fina Technology, Inc. Process for forming a Ziegler-Natta catalyst system having a controlled morphology
GB0317268D0 (en) 2003-07-23 2003-08-27 Viral Asa A Compounds
DE602004019933D1 (en) 2003-08-04 2009-04-23 Zeon Corp POLYMERIZABLE COMPOSITION AND FORM BODY USING THE SAME
US7226957B1 (en) 2003-11-03 2007-06-05 University Of Iowa Research Foundation Method for producing polymers with controlled molecular weight and end group functionality using photopolymerization in microemulsions
JP2005170803A (en) 2003-12-08 2005-06-30 Daicel Chem Ind Ltd New monomethyl malonate derivative and method for producing the same
US20050228074A1 (en) 2004-04-05 2005-10-13 Bridgestone Corporation Amphiphilic polymer micelles and use thereof
US7170188B2 (en) 2004-06-30 2007-01-30 Intel Corporation Package stress management
US7305850B2 (en) 2004-07-23 2007-12-11 Velocys, Inc. Distillation process using microchannel technology
WO2006019658A2 (en) 2004-07-23 2006-02-23 Velocys Inc. Distillation process using microchannel technology
US9598527B2 (en) 2004-09-01 2017-03-21 Ppg Industries Ohio, Inc. Polyurethanes, articles and coatings prepared therefrom and methods of making the same
EP1784302B1 (en) 2004-09-01 2016-07-06 Encapsys, Llc Encapsulated cure systems
US7371804B2 (en) 2004-09-07 2008-05-13 Ophthonix, Inc. Monomers and polymers for optical elements
US8075906B2 (en) 2005-02-01 2011-12-13 Boston Scientific Scimed, Inc. Medical devices having polymeric regions with copolymers containing hydrocarbon and heteroatom-containing monomeric species
WO2006107900A2 (en) 2005-04-01 2006-10-12 Visyx Technologies, Inc. Monitoring by means of an on-line sensor and fluidic operations involving unit separation and reaction operations
WO2007018736A2 (en) 2005-07-22 2007-02-15 Appleton Papers Inc. Encapsulated structural adhesive
US7919543B2 (en) 2005-08-16 2011-04-05 Electronics For Imaging, Inc. Inkjet inks, methods for applying inkjet ink, and articles printed with inkjet inks
DE602006012593D1 (en) * 2005-08-24 2010-04-15 Nippon Catalytic Chem Ind Radiation crosslinkable compositions and crosslinked products made therefrom
US7771567B2 (en) 2005-09-02 2010-08-10 Rives Michael L Salt water distillation system
US20070092483A1 (en) 2005-10-21 2007-04-26 Pollock Polymer Group Surgical adhesive compostion and process for enhanced tissue closure and healing
US7626477B2 (en) 2005-11-28 2009-12-01 General Electric Company Cold mass cryogenic cooling circuit inlet path avoidance of direct conductive thermal engagement with substantially conductive coupler for superconducting magnet
WO2007069746A1 (en) 2005-12-16 2007-06-21 Yoshihiro Watanabe Article such as surfboard and production method thereof
AU2007235408A1 (en) 2006-04-07 2007-10-18 E.I. Du Pont De Nemours And Company Processes for chemical synthesis of lipochitooligosaccharides
WO2007120630A2 (en) 2006-04-10 2007-10-25 Abm Associates Llc Activated anaerobic adhesive and use thereof
US7659423B1 (en) 2006-04-18 2010-02-09 Loctite (R&D) Limited Method of preparing electron deficient olefins in polar solvents
US8722831B2 (en) 2006-05-29 2014-05-13 Denki Kagaku Kogyo Kabushiki Kaisha Process for production of cross copolymers, cross copolymers obtained by the process, and use thereof
US8138270B2 (en) 2006-08-16 2012-03-20 Asahi Kasei Chemicals Corporation Process for producing block copolymer, and block copolymer or hydrogenated product thereof
US8332435B2 (en) 2006-10-03 2012-12-11 Salesforce.Com, Inc. Method and system for customizing a user interface to an on-demand database service
FR2907131B1 (en) 2006-10-12 2008-11-21 Commissariat Energie Atomique METHOD FOR FORMING ORGANIC FILMS ON CONDUCTIVE OR SEMICONDUCTOR SURFACES OF ELECTRICITY FROM AQUEOUS SOLUTIONS IN TWO STEPS
ATE425876T1 (en) 2006-11-30 2009-04-15 Fujifilm Corp INK JET RECORDING INK COMPOSITION AND INK JET RECORDING METHOD
JP2008174494A (en) 2007-01-19 2008-07-31 Nippon Shokubai Co Ltd Methylenemalonic acid composition and method for stabilizing the same
JP2008189776A (en) 2007-02-02 2008-08-21 Fujifilm Corp Active radiation-curable polymerizable composition, ink composition, inkjet recording method, printed matter, preparation method of lithographic printing plate, and lithographic printing plate
EP2122334B1 (en) 2007-02-06 2018-01-24 Medtronic Minimed, Inc. Method for polymerizing a monomer solution within a cavity to generate a smooth polymer surface
JP5243072B2 (en) 2007-03-30 2013-07-24 富士フイルム株式会社 Ink composition, and image recording method and image recorded material using the same
US8168213B2 (en) 2007-05-15 2012-05-01 Boston Scientific Scimed, Inc. Medical devices having coating with improved adhesion
US7742670B2 (en) 2007-10-01 2010-06-22 Corning Cable Systems Llc Index-matching gel for nanostructure optical fibers and mechanical splice assembly and connector using same
KR20090064862A (en) 2007-12-17 2009-06-22 광주과학기술원 Anionic polymerization of functionalized styrene derivatives directly containing pyridine and synthesis of block copolymers
US8138610B2 (en) 2008-02-08 2012-03-20 Qimonda Ag Multi-chip package with interconnected stacked chips
JP2009192309A (en) 2008-02-13 2009-08-27 Shinko Electric Ind Co Ltd Semiconductor inspection device
EP2263999A4 (en) 2008-03-18 2012-11-07 Mitsui Chemicals Agro Inc Method for producing fluorine-containing acylacetic acid derivative, method for producing fluorine-containing pyrazolecarboxylic acid ester derivative, and method for producing fluorine-containing pyrazolecarboxylic acid derivative
DE112009000690T5 (en) 2008-03-27 2011-03-24 Nisshin Steel Co., Ltd. Inkjet ink composition for etch resists
US8318060B2 (en) 2008-07-22 2012-11-27 University Of New Hampshire Microencapsulation of amines
GB2463065B (en) * 2008-09-01 2012-11-07 Loctite R & D Ltd Transferable curable non-liquid film on a release substrate
US9220811B2 (en) 2008-09-22 2015-12-29 Boston Scientific Scimed, Inc. Implantable or insertable medical devices
DE102009000861A1 (en) 2009-02-13 2010-08-19 Henkel Ag & Co. Kgaa Process for the preparation of cyanoacrylates
US8106234B2 (en) 2009-05-07 2012-01-31 OptMed, Inc Methylidene malonate process
US8993795B2 (en) 2009-05-07 2015-03-31 Optmed Inc Methylidene malonate process
US7829738B1 (en) 2009-05-19 2010-11-09 Nalco Company Production of N,N-dialklylaminoethyl (meth)acrylates
EP2436702B1 (en) 2009-05-29 2014-12-17 JX Nippon Oil & Energy Corporation Isobutylene-based polymer and method for producing same
DE102009027545A1 (en) 2009-07-08 2011-02-03 Henkel Ag & Co. Kgaa Process for the preparation of cyanoacrylates in the presence of transition metal catalysts
JP5671302B2 (en) 2009-11-10 2015-02-18 富士フイルム株式会社 Curable composition for imprint, pattern forming method and pattern
WO2011070739A1 (en) 2009-12-07 2011-06-16 住友ベークライト株式会社 Epoxy resin composition for semiconductor encapsulation, cured product thereof, and semiconductor device using epoxy resin composition
JP2011122005A (en) * 2009-12-08 2011-06-23 Sony Corp Anti-reflection film, method for producing the same, and coating liquid of ultraviolet-curable resin material composition
US9931296B2 (en) 2010-04-03 2018-04-03 Praful Doshi Medical devices including medicaments and methods of making and using same
EA023440B1 (en) 2010-06-23 2016-06-30 Тотал Ресерч Энд Текнолоджи Фелюи Dehydration of alcohols on poisoned acidic catalysts
US8554938B2 (en) 2010-08-31 2013-10-08 Millind Mittal Web browser proxy-client video system and method
US9249265B1 (en) 2014-09-08 2016-02-02 Sirrus, Inc. Emulsion polymers including one or more 1,1-disubstituted alkene compounds, emulsion methods, and polymer compositions
US8884051B2 (en) 2010-10-20 2014-11-11 Bioformix Inc. Synthesis of methylene malonates using rapid recovery in the presence of a heat transfer agent
ES2529671T3 (en) 2010-12-20 2015-02-24 Dsm Ip Assets B.V. Bio-renewable aqueous composition of vinyl polymer
US20130019520A1 (en) 2011-02-02 2013-01-24 Brown University Methods of Making Fatty Acids and Fatty Acid Alkyl Esters
CN102901754A (en) 2011-07-27 2013-01-30 中国科学院电子学研究所 Electropolymerization molecular imprinting technology-based double-parameter composite micro-sensor and preparation thereof
MX360463B (en) 2011-10-19 2018-11-05 Sirrus Inc Methylene beta-ketoester monomers, methods for making methylene beta-ketoester monomers, polymerizable compositions and products formed therefrom.
EP3153530B1 (en) 2012-03-30 2021-02-24 Sirrus, Inc. Composite and laminate articles and polymerizable systems for producing the same
CA2869108A1 (en) 2012-03-30 2013-10-03 Bioformix Inc. Methods for activating polymerizable compositions, polymerizable systems, and products formed thereby
JP6345644B2 (en) 2012-03-30 2018-06-20 シラス・インコーポレイテッド Ink formulations and coating formulations and polymerizable systems for making them
US10047192B2 (en) 2012-06-01 2018-08-14 Sirrus, Inc. Optical material and articles formed therefrom
WO2013184255A1 (en) 2012-06-04 2013-12-12 Biosynthetic Technologies, Llc Processes for preparing estolide base oils and lubricants that include transesterification
KR102192090B1 (en) 2012-10-19 2020-12-16 프리에토 배터리, 인크. Detection of defects in solid-polymer coatings
WO2014078689A1 (en) 2012-11-16 2014-05-22 Bioformix Inc. Plastics bonding systems and methods
US10607910B2 (en) 2012-11-30 2020-03-31 Sirrus, Inc. Composite compositions for electronics applications
EP2943462B1 (en) 2013-01-11 2018-06-27 Sirrus, Inc. Method to obtain methylene malonate via bis(hydroxymethyl) malonate pathway
US9334430B1 (en) 2015-05-29 2016-05-10 Sirrus, Inc. Encapsulated polymerization initiators, polymerization systems and methods using the same
US9217098B1 (en) 2015-06-01 2015-12-22 Sirrus, Inc. Electroinitiated polymerization of compositions having a 1,1-disubstituted alkene compound
DE102017204525A1 (en) 2016-03-23 2017-09-28 Basf Se Laminated laminates for flexible packaging
EP3445830A1 (en) 2016-04-21 2019-02-27 Zephyros Inc. Malonates and derivatives for in-situ films
US20180010014A1 (en) 2016-07-11 2018-01-11 Zephyros, Inc. Compositions for adhesive applications
US11130867B2 (en) 2016-07-26 2021-09-28 Ppg Industries Ohio, Inc. Curable compositions containing 1,1-di-activated vinyl compounds and related coatings and processes
ES2930756T3 (en) 2016-07-26 2022-12-21 Ppg Ind Ohio Inc Acid-Catalyzed Curable Coating Compositions Containing 1,1-Diactivated Vinyl Compounds and Related Coatings and Processes
WO2018022780A1 (en) 2016-07-26 2018-02-01 Ppg Industries Ohio, Inc. Polyurethane coating compositions containing 1,1-di-activated vinyl compounds and related coatings and processes
EP3490784B1 (en) 2016-07-26 2022-10-12 PPG Industries Ohio, Inc. Three-dimensional printing processes using 1,1-di-activated vinyl compounds
US10961403B2 (en) 2016-07-26 2021-03-30 Ppg Industries Ohio, Inc. Electrodepositable coating compositions containing 1,1-di-activated vinyl compounds
ES2930531T3 (en) 2016-07-26 2022-12-16 Ppg Ind Ohio Inc Particles having surfaces functionalized with 1,1-diactivated vinyl compounds
EP3490726B1 (en) 2016-07-26 2022-11-30 PPG Industries Ohio, Inc. Multi-layer curable compositions containing 1,1-di-activated vinyl compound products and related processes
EP3515994B1 (en) 2016-09-19 2024-01-24 Zephyros Inc. Method for sealing porous substrates
EP3515973A1 (en) 2016-09-19 2019-07-31 Zephyros Inc. Malonate and cyanoacrylate adhesives for joining dissimilar materials
US10894856B2 (en) 2016-11-09 2021-01-19 Basf Se Polyurethane-vinyl hybrid polymers, methods of making them and their use

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
None
See also references of EP2768897A4

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9144796B1 (en) 2009-04-01 2015-09-29 Johnson Matthey Public Limited Company Method of applying washcoat to monolithic substrate
US9315597B2 (en) * 2014-09-08 2016-04-19 Sirrus, Inc. Compositions containing 1,1-disubstituted alkene compounds for preparing polymers having enhanced glass transition temperatures
DE102017204525A1 (en) 2016-03-23 2017-09-28 Basf Se Laminated laminates for flexible packaging
WO2018086860A1 (en) 2016-11-09 2018-05-17 Basf Se Polyurethane-vinyl hybrid polymers, methods of making them and their use
US10894856B2 (en) 2016-11-09 2021-01-19 Basf Se Polyurethane-vinyl hybrid polymers, methods of making them and their use
WO2019137853A1 (en) 2018-01-09 2019-07-18 Basf Se Compositions comprising polymerizable vinyl compounds, inorganic or organic fillers and their use
DE102019219214A1 (en) 2018-12-17 2020-06-18 Basf Se Compositions comprising multifunctional vinyl compounds in mini-emulsion and their use as crosslinkers for polymers

Also Published As

Publication number Publication date
US9969822B2 (en) 2018-05-15
WO2013059479A3 (en) 2013-07-11
JP2014534969A (en) 2014-12-25
MX2014004782A (en) 2015-03-20
WO2013066629A1 (en) 2013-05-10
EP3339301A3 (en) 2018-08-08
MX360463B (en) 2018-11-05
WO2013059473A2 (en) 2013-04-25
EP2768917A2 (en) 2014-08-27
EP3293216A1 (en) 2018-03-14
EP2768872B1 (en) 2017-11-22
US20140288230A1 (en) 2014-09-25
MX2014004781A (en) 2015-03-20
US20180327525A1 (en) 2018-11-15
CA2853079A1 (en) 2013-05-10
US10604601B2 (en) 2020-03-31
US20140329980A1 (en) 2014-11-06
EP3339301A2 (en) 2018-06-27
CA2853068A1 (en) 2013-04-25
EP2768897B1 (en) 2019-01-23
EP2768897A2 (en) 2014-08-27
US9512058B2 (en) 2016-12-06
MX360462B (en) 2018-11-05
US10611861B2 (en) 2020-04-07
EP2768917B1 (en) 2018-12-05
MX2014004780A (en) 2015-03-20
US20140275400A1 (en) 2014-09-18
EP2768872A4 (en) 2015-08-26
EP3517523A1 (en) 2019-07-31
WO2013059473A3 (en) 2015-06-25
JP2015517973A (en) 2015-06-25
US20170073438A1 (en) 2017-03-16
US9221739B2 (en) 2015-12-29
EP2768897A4 (en) 2015-08-12
US20170050914A1 (en) 2017-02-23
US9527795B2 (en) 2016-12-27
JP6267643B2 (en) 2018-01-24
EP2768872A1 (en) 2014-08-27
MX370256B (en) 2019-12-09
EP2768917A4 (en) 2016-10-05
US20180346615A1 (en) 2018-12-06
CA2853073A1 (en) 2013-04-25
JP2014532625A (en) 2014-12-08

Similar Documents

Publication Publication Date Title
EP2768897B1 (en) Methods for making methylene beta-diketone monomers
US9828324B2 (en) Methylene beta-diketone monomers, methods for making methylene beta-diketone monomers, polymerizable compositions and products formed therefrom
EP2630116B1 (en) Synthesis of methylene malonates using rapid recovery in the presence of a heat transfer agent
US10414839B2 (en) Polymers including a methylene beta-ketoester and products formed therefrom

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12842121

Country of ref document: EP

Kind code of ref document: A2

WWE Wipo information: entry into national phase

Ref document number: 14352369

Country of ref document: US

ENP Entry into the national phase

Ref document number: 2014537250

Country of ref document: JP

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: MX/A/2014/004782

Country of ref document: MX

ENP Entry into the national phase

Ref document number: 2853073

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 2012842121

Country of ref document: EP

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 12842121

Country of ref document: EP

Kind code of ref document: A2