WO2017160361A1 - Polyisocyanurate catalysts for metal panels and spray foams - Google Patents

Polyisocyanurate catalysts for metal panels and spray foams Download PDF

Info

Publication number
WO2017160361A1
WO2017160361A1 PCT/US2016/066446 US2016066446W WO2017160361A1 WO 2017160361 A1 WO2017160361 A1 WO 2017160361A1 US 2016066446 W US2016066446 W US 2016066446W WO 2017160361 A1 WO2017160361 A1 WO 2017160361A1
Authority
WO
WIPO (PCT)
Prior art keywords
methyl
benzimidazole
benzotriazole
benzpyrazole
pyrrole
Prior art date
Application number
PCT/US2016/066446
Other languages
French (fr)
Inventor
Ernest L. Rister
Jennifer Chavez PRICE
Robert A. Grigsby
Original Assignee
Huntsman Petrochemical Llc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Huntsman Petrochemical Llc filed Critical Huntsman Petrochemical Llc
Publication of WO2017160361A1 publication Critical patent/WO2017160361A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/16Catalysts
    • C08G18/18Catalysts containing secondary or tertiary amines or salts thereof
    • C08G18/20Heterocyclic amines; Salts thereof
    • C08G18/2009Heterocyclic amines; Salts thereof containing one heterocyclic ring
    • C08G18/2018Heterocyclic amines; Salts thereof containing one heterocyclic ring having one nitrogen atom in the ring
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/16Catalysts
    • C08G18/22Catalysts containing metal compounds
    • C08G18/225Catalysts containing metal compounds of alkali or alkaline earth metals
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/4009Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
    • C08G18/4018Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/4205Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
    • C08G18/4208Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4804Two or more polyethers of different physical or chemical nature
    • C08G18/4816Two or more polyethers of different physical or chemical nature mixtures of two or more polyetherpolyols having at least three hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4829Polyethers containing at least three hydroxy groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/50Polyethers having heteroatoms other than oxygen
    • C08G18/5021Polyethers having heteroatoms other than oxygen having nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00Foam properties
    • C08G2110/0025Foam properties rigid

Definitions

  • the present disclosure provides a catalyst substantially free of nonylphenol comprising a Mannich condensation product prepared from a heterocyclic compound containing at least one -N(H)- group in the ring, an aldehyde, and a metal salt of an aminocarboxylic acid.
  • the catalyst according to the present disclosure exhibits high catalytic activity and is suitable for use in the preparation of polyurethane and polyisocyanurate foam.
  • polyisocyanurate and polyurethane foams are made by reacting a polyol and a polyisocyanate in the presence of a catalyst. Additional additives, such as blowing agents, surfactants and flame retardants, can also be present.
  • the reactions for forming the polyurethane or polyisocyanurate foam consist mainly of a urethane bond-forming reaction (gelling reaction) by the reaction of the polyol with the polyisocyanate, a urea group-forming reaction (blowing reaction) by the reaction of the polyisocyanate with water, and an isocyanurate ring-forming reaction (trimerization reaction) by trimerization of the polyisocyanate.
  • Known catalysts for accelerating the gelling reaction and/or blowing reaction include tertiary amine catalysts and organic metal catalysts.
  • tertiary amine catalysts those industrially used may, for example, be compounds such as triethylenediamine, N,N,N',N'-tetramethyl-1 ,6- hexanediamine, ⁇ , ⁇ -dimethylcyclohexylamine, bis(2-dimethylaminoethyl) ether, N,N,N',N",N"-pentamethyldiethylenetriamine, N-methylmorpholine and N- ethylmorpholine.
  • Organic metal catalysts generally include organolead, organoferric and organotin compounds, such as stannous chloride, and tin salts of carboxylic acids.
  • a catalyst substantially free of nonylphenol which is suitable for use in the preparation of a polyurethane or polyisocyanurate foam.
  • the catalyst according to the present disclosure includes a Mannich condensation product of: (i) a heterocyclic compound containing at least one -N(H)- group in the ring; (ii) an aldehyde; and (iii) a metal salt of an aminocarboxylic acid.
  • a polyurethane or polyisocyanurate foam composition that contains the catalyst according to the present disclosure.
  • a polyurethane or polyisocyanurate foam obtained by bringing together, under foam-forming conditions, a polyisocyanate, a polyol, a blowing agent and the catalyst according to the present disclosure.
  • compositions claimed herein through use of the term “comprising” may include any additional additive, adjuvant, or compound, unless stated to the contrary.
  • the term, “consisting essentially of if appearing herein excludes from the scope of any succeeding recitation any other component, step or procedure, except those that are not essential to operability and the term “consisting of, if used, excludes any component, step or procedure not specifically delineated or listed.
  • the articles “a” and “an” are used herein to refer to one or to more than one (i.e. to at least one) of the grammatical objects of the article.
  • an amine means one amine or more than one amine.
  • the phrases “in one embodiment”, “according to one embodiment” and the like generally mean the particular feature, structure, or characteristic following the phrase is included in at least one embodiment of the present disclosure, and may be included in more than one embodiment of the present disclosure. Importantly, such phrases do not necessarily refer to the same embodiment. If the specification states a component or feature “may”, “can”, “could”, or “might” be included or have a characteristic, that particular component or feature is not required to be included or have the characteristic.
  • substantially free means, when used with reference to the substantial absence of a material, that such a material is present, if at all, as an incidental impurity or by-product.
  • the material may be present in the composition of matter at an amount of no more than 100 ppm, in some instances less than 20 ppm and in still other instances less than 1 ppm.
  • the catalyst substantially free of nonylphenol according to the present disclosure exhibits surprisingly high catalytic activity. Moreover, since the catalyst is substantially free of nonylphenol, it's environmentally safe and can be used in countries and specific regions that have banned the use of nonylphenol.
  • the heterocyclic -N(H)- containing compounds useful in preparing the catalyst according to the present disclosure include heterocyclic compounds containing a 5- or 6-membered ring with one nitrogen hetero-atom or two or three adjacent nitrogen hetero-atoms, in which two adjacent carbon atoms of the heterocyclic ring may form part of a further 6-aromatic, heterocyclic or alicyclic ring system, wherein the heterocyclic compound contains at least one -N(H)- ring group.
  • the heterocyclic compound can contain other hetero-atoms, usually O or S. In some embodiments, the heterocyclic ring is unsaturated.
  • the 6-membered ring system comprises an aromatic ring system, for example, a benzene ring or naphthalene ring system.
  • this adjacent 6-membered ring system comprises a heterocyclic ring or an ethylenically unsaturated alicyclic ring system.
  • the 5- or 6-membered heterocyclic ring and the adjacent 6-membered ring system may be substituted or unsubstituted. In some embodiments, substitution occurs on carbon-atoms of the ring.
  • Substituents can include an alkyl group, an alkaryl group, an aryl group, an aralkyl group or an alkenyl group.
  • the alkyl group contains from 1-10 carbon atoms, for example, a methyl, ethyl, propyl, butyl, pentyl, or decyl group.
  • the aryl group contains from 6-10 carbon atoms, such as phenol or naphthyl.
  • the alkaryl group and aralkyl group contain from 7-10 carbon atoms, such as tolyl, xylyl or ethylphenyl.
  • the alkenyl group contains from 2-10 carbon atoms, such as ethenyl, propenyl, butenyl, or decenyl.
  • the heterocyclic compound containing at least one -N(H)- group in the ring is triazole, benzotriazole, 5-methyl benzotriazole, 5-ethyl benzotriazole, 5-butyl benzotriazole, 5-propyl benzotriazole, 5-dodecyl benzotriazole, 2-methyl benzotriazole, 2-ethyl benzotriazole, 2-butyl benzotriazole, 2-propyl benzotriazole, 2-dodecyl benzotriazole, 5,7-dimethyl benzotriazole, 5,7-diethyl benzotriazole, 5,7-dibutyl benzotriazole, 5,7-dipropyl benzotriazole, 5,7-didodecyl benzotriazole, naphthotriazole, 5-methyl naphthotriazole, 5-ethyl naphthotriazole, 5-butyl naphthotriazo
  • the heterocyclic compound containing at least one -N(H)- group is selected from pyrrole, 2-methyl pyrrole and 3-methyl pyrrole.
  • Representative aldehydes for use in the preparation of the Mannich condensation product include aliphatic aldehydes and aromatic aldehydes.
  • the aliphatic aldehydes include Ci to C 6 aldehydes, such as formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, valeraldehyde, and hexanal aldehyde.
  • Aromatic aldehydes which may be used include benzaldehyde and salicylaldehyde.
  • Illustrative heterocyclic aldehydes for use herein are furfural and thiophene aldehyde, etc.
  • formaldehyde-producing reagents such as paraformaldehyde, or aqueous formaldehyde solutions such as formalin.
  • the aldehyde is formaldehyde or formalin.
  • the aminocarboxylic acid is selected from an a-amino acid, a ⁇ -amino acid, a ⁇ -amino acid, a ⁇ -amino acid, a ⁇ -amino acid and a ⁇ -amino acid.
  • Examples of a-amino acids include glycine (aminoacetic acid), N- methylglycine (N-methylaminoacetic acid, sarcosine), N-ethylglycine, alanine (2- aminopropionic acid), N-methylalanine (2-(methylamino)propionic acid), N,N- dimethylalanine, N-ethylalanine, 2-methylalanine (2-aminoisobutyric acid), leucine (2-amino-4-methylpentan-1-oic acid), N-methylleucine, N,N- dimethylleucine, isoleucine (1-amino-2-methylpentanoic acid), N- methylisoleucine, valine (2-aminoisovaleric acid), a-methylvaline (2-amino-2- methylisovaleric acid), N-methylvaline (2-methylaminoisovaleric acid), proline (pyrrolidine-2-carboxylic acid
  • ⁇ -amino acids include 3-aminopropionic acid ( ⁇ -alanine), 3-methylaminopropionic acid, iminodipropionic acid, N-methyliminodipropionic acid, piperidine-3-carboxylic acid and N-methylpiperidine-3-carboxylic acid.
  • Examples of ⁇ -amino acids include 4-aminobutyric acid and 4- methylaminobutyric acid.
  • aminocarboxylic acids include piperidine-4-carboxylic acid and N-methylpiperidine-4-carboxylic acid.
  • suitable aminocarboxylic acids include N-mono-C-i ⁇ -alkylaminocarboxylic acids, in particular N-mono-Ci-C 4 -alkyl-a- aminocarboxylic acids.
  • the metal salt is generally an alkali metal or alkaline earth metal salt.
  • the metal salt is an alkali metal salt such as a sodium or potassium salt, of which sodium salts are most preferred.
  • the metal salt of the aminocarboxylic acid is a compound of the formula N ( CH 2 )x COOM
  • Ri , R 2 , and R 3 are, independently of one another, H or a C 1 -C3 alkyl group, M is sodium or potassium and x is an integer from 0 to 5.
  • the metal salt of the aminocarboxylic acid is the sodium salt of N-methylglycine.
  • the Mannich condensation product can be prepared by reacting the heterocyclic compound containing at least one -N(H)- group in the ring with the aldehyde and the metal salt of an aminocarboxylic acid.
  • the reaction occurs by contacting the heterocyclic compound containing at least one -N(H)- group in the ring, the aldehyde and the metal salt of an aminocarboxylic acid in a reaction zone.
  • the reactants may be contacted for a time and under conditions effective to react the aldehyde, reactive amine groups of the metal salt of the aminocarboxylic acid and the -N(H)- group(s) of the heterocyclic compound to form the Mannich condensation product containing heterocyclic nitrogen units bound to at least a portion of the aminocarboxylic acid through a hydrocarbylene group derived from the aldehyde (for e.g., a methylene (-CH 2 -) group derived from formaldehyde).
  • a hydrocarbylene group derived from the aldehyde for e.g., a methylene (-CH 2 -) group derived from formaldehyde.
  • the conditions of temperature and pressure under which the reaction occurs can vary widely, and generally temperatures from about 0°C to 80°C can be used.
  • the pressures in the reaction zone will be sufficient to maintain a liquid reaction medium, and generally pressures from about 0.1 kPa to 1000 kPa, such as from about 1 kPa to 100 kPa, can be employed.
  • the reaction can be carried out in a batchwise, continuous or semicontinuous manner, in one or more reaction zones.
  • the reaction can be conducted in any conventional apparatus such as stirred tank reactors, tubular flow reactors and the like.
  • the reactants can be charged to the reaction zone continuously or intermittently, together or sequentially, in any order.
  • the heterocyclic compound containing at least one -N(H)- group in the ring, and any carrier or solvent for the reaction will first be charged to the reaction zone, followed by the aldehyde reactant and then the metal salt of an aminocarboxylic acid, which can, if desired, be also introduced to the reaction zone as a mixture of the aldehyde and metal salt of an aminocarboxylic acid reactants.
  • the metal salt of an aminocarboxylic acid is not contacted with the heterocyclic compound containing at least one -N(H)- group in the ring reactant in the absence of the aldehyde when at reaction conditions.
  • the reaction can be accomplished using a wide range of ratios of reactants, and the metal salt of an aminocarboxylic acid:aldehyde:heterocyclic compound containing at least one -N(H) ⁇ group in the ring reactants may be generally charged in a ratio of from 1 :0.01 :0.01 to 1 :50:50, and in some embodiments from 1 :0.2:0.2 to 1 :10:10, and in still more embodiments from 1 :0.5:0.5 to 1 :5:5, molar equivalents of metal salt of an aminocarboxylic acid:moles of aldehyde:moles of heterocyclic compound containing at least one - N(H)-group.
  • the reaction can be conducted in bulk (no diluent or solvent) or in a diluent or solvent.
  • the reaction is conducted in a solvent.
  • diluents and solvents include ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, as well as polyethylene or polypropylene glycols in the 100-1000 molecular weight range, benzene, toluene and xylene. Water that is evolved during the reaction can be removed by azeotropic distillation during the course of the reaction or after the completion of the reaction.
  • the temperature and pressure can be maintained at about 80°C and about 40 mm Hg reduced pressure after completion of the reaction to remove water that has evolved.
  • Typical reaction times may range from about 0.5 to about 12 hours, although longer or shorter times can be used as necessary or as desired.
  • a polyurethane or polyisocyanurate foam composition containing an isocyanate, a polyol, a blowing agent and the catalyst substantially free of nonylphenol.
  • the polyurethane or polyisocyanurate foam compositions according to the present disclosure are usually divided up into two components.
  • the isocyanate portion is generally referred to as the A-side and the polyol portion is referred to as the B-side.
  • each of the remaining components of the foam composition may be included in either the A-side or B- side or they can be included as a separate component(s).
  • the isocyanate in the foam composition may be selected from a wide variety of isocyanates, including those that are well known to one skilled in the art.
  • isocyanates including those that are well known to one skilled in the art.
  • organic polyisocyanates, modified multi-functional polyisocyanates, isocyanate-based prepolymers, and mixtures thereof may be employed. These may further include aliphatic and cycloaliphatic isocyanates, and in particular aromatic and, more particularly, multifunctional aromatic isocyanates.
  • Polyphenyl polymethylene polyisocyanates (PMDI) may also be used.
  • the isocyanate includes 2,4- and 2,6- toluenediisocyanate and the corresponding isomeric mixtures; 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanate and the corresponding isomeric mixtures; mixtures of 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanates and polyphenyl polymethylene polyisocyanates (PMDI); and mixtures of PMDI and toluene diisocyanates.
  • PMDI polyphenyl polymethylene polyisocyanates
  • aliphatic and cycloaliphatic isocyanate compounds such as 1 ,6-hexamethylenediisocyanate; 1-isocyanato ⁇ 3,5,5- trimethyl-1 ,3-isocyaantomethylcyclohexane; 2,4- and 2,6-hexahydrotoluene- diisocyanate and their corresponding isomeric mixtures; and 4,4'-, 2,2'- and 2,4'- dicyclohexyl-methanediisocyanate and their corresponding isomeric mixtures. Also useful is 1 ,3-tetra-methylene xylene diisocyanate.
  • the isocyanate is a so-called modified multifunctional polyisocyanate, that is, a product which is obtained through chemical reaction of the above diisocyanates and/or polyisocyanates.
  • modified multifunctional polyisocyanate that is, a product which is obtained through chemical reaction of the above diisocyanates and/or polyisocyanates.
  • examples include polyisocyanates containing esters, ureas, biurets, allophanates and, preferably, carbodiimides and/or uretonomine, and isocyanurate and/or urethane group-containing diisocyanates or polyisocyanates.
  • Liquid polyisocyanates containing carbodiimide groups, uretonomine groups and/or isocyanurate rings, having isocyanate group (NCO) contents of from 120 to 40 weight percent, or from 20 to 35 weight percent, can also be used.
  • Suitable isocyanate-based prepolymers are prepolymers having NCO contents of from 2 to 40 weight percent, or from 4 to 30 weight percent. These prepolymers are prepared by reaction of the di- and/or polyisocyanates with materials including lower molecular weight diols and triols, but also can be prepared with multivalent active hydrogen compounds such as di- and tri-amines and di- and tri-thiols.
  • aromatic polyisocyanates containing urethane groups which may have NCO contents of from 5 to 40 weight percent, or 20 to 35 weight percent, obtained by reaction of diisocyanates and/or polyisocyanates with, for example, polyols such as lower molecular weight diols, triols, oxyalkylene glycols, dioxyalkylene glycols, or polyoxyalkylene glycols having molecular weights up to about 800.
  • polyols can be employed individually or in mixtures as di- and/or polyoxyalkylene glycols.
  • diethylene glycols, dipropylene glycols, polyoxyethylene glycols, ethylene glycols, propylene glycols, butylene glycols, polyoxypropylene glycols and polyoxypropylene polyoxyethylene glycols can be used.
  • Polyester polyols can also be used, as well as alkyl diols such as butane diol.
  • Other diols also useful include bishydroxyethyl- or bishydroxypropyl-bisphenol A, cyclohexane dimethanol, and bishydroxyethyl hydroquinone.
  • the isocyanate may be used in an amount sufficient to provide an isocyanate index of at least 80.
  • Isocyanate index is calculated as the number of reactive isocyanate groups provided by the isocyanate divided by the number of isocyanate-reactive groups in the polyurethane or polyisocyanurate foam composition (including those contained by blowing agents such as water) and multiplying by 100. Water is considered to have two isocyanate-reactive groups per molecule for purposes of calculating isocyanate index.
  • the isocyanate index is from about 80 to about 600.
  • the isocyanate index may generally be from about 80 to 150.
  • the isocyanate index may generally be greater than about 150 and up to about 600.
  • Polyols which may be present in the foam composition include one or more polyester or polyether polyols of the kind typically employed in processes to make polyurethane or polyisocyanurate foam.
  • Other compounds having at least two isocyanate reactive hydrogen atoms may also be present, for example: polythioether polyols; condensate adducts of phenol and formaldehyde with one or more alkylene oxides including ethylene oxide, propylene oxide, and butylene oxide; polyester amides and polyacetals containing hydroxyl groups; aliphatic polycarbonates containing hydroxyl groups; amine terminated polyoxyalkylene polyethers; and graft dispersion polyols. Mixtures of two or more of the aforesaid materials may also be employed.
  • polyester polyol as used herein includes any minor amounts of unreacted polyol remaining after the preparation of the polyester polyol and/or unesterified polyol (for example, glycol) added after the preparation of the polyester polyol.
  • Polyester polyols can be produced, for example, from organic dicarboxylic acids with 2 to 12 carbons, including aliphatic dicarboxylic acids with 4 to 6 carbons, and divalent and multivalent alcohols, including diols, with 2 to 12 carbons, such as, 2 to 6 carbons.
  • dicarboxylic acids examples include succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, maleic acid, fumaric acid, phthalic acid, isophthalic acid, and terephthalic acid.
  • the dicarboxylic acids can be used individually or in mixtures. Instead of the free dicarboxylic acids, the corresponding dicarboxylic acid derivatives may also be used, such as dicarboxylic acid mono- or di-esters of alcohols with 1 to 4 carbons, or dicarboxylic acid anhydrides.
  • Dicarboxylic acid mixtures of succinic acid, glutaric acid and adipic acid in quantity ratios of 20-35:35-50:20-32 parts by weight may also be used.
  • divalent and multivalent alcohols include ethanediol, diethylene glycol, 1 ,2- and 1 ,3- propanediol, dipropylene glycol, 1 ,4-butanediol, 1 ,5-pentanediol, 1 ,6-hexanediol, 1 ,10-decanediol, glycerine and trimethylolpropanes, tripropylene glycol, tetraethylene glycol, tetrapropylene glycol, tetramethylene glycol, 1 ,4- cyclohexane-dimethanol, ethanediol, diethylene glycol, 1 ,4-butanediol, 1 ,5- pentanediol,
  • Polyether polyols that may be used include those which can be obtained by known methods, For example, polyether polyols can be produced by anionic polymerization with alkali hydroxides such as sodium hydroxide or potassium hydroxide or alkali alcoholates, such as sodium methylate, sodium ethylate, or potassium ethylate or potassium isopropylate as catalysts and with the addition of at least one initiator molecule containing 2 to 8, such as 3 to 8, reactive hydrogens or by cationic polymerization with Lewis acids such as antimony pentachloride, boron trifluoride etherate, etc., or bleaching earth as catalysts from one or more alkylene oxides with 2 to 4 carbons in the alkylene radical.
  • alkali hydroxides such as sodium hydroxide or potassium hydroxide or alkali alcoholates, such as sodium methylate, sodium ethylate, or potassium ethylate or potassium isopropylate
  • initiator molecule containing 2 to 8 such as 3 to 8
  • alkylene oxide such as 1 ,3-propylene oxide, 1 ,2- and 2,3-butylene oxide, amylene oxides, styrene oxide, and preferably ethylene oxide and 1 ,2-propylene oxide and mixtures of these oxides.
  • the polyalkylene polyether polyols may be prepared from other starting materials such as tetrahydrofuran and alkylene oxide-tetrahydrofuran mixtures; epihalohydrins such as epichlorohydrin; as well as aralkylene oxides such as styrene oxide.
  • the polyalkylene polyether polyols may have either primary or secondary hydroxyl groups, preferably secondary hydroxyl groups from the addition of propylene oxide onto an initiator because these groups are slower to react. Included among the polyether polyols are polyoxyethylene glycol, polyoxypropylene glycol, polyoxybutylene glycol, polytetramethylene glycol, block copolymers, for example, combinations of polyoxypropylene and polyoxyethylene glycols, poly-1 ,2-oxybutylene and polyoxyethylene glycols, poly-1 ,4- tetramethylene and polyoxyethylene glycols, and copolymer glycols prepared from blends or sequential addition of two or more alkylene oxides.
  • the polyalkylene polyether polyols may be prepared by any known process such as, for example, the process disclosed by Wurtz in 1859 and Encyclopedia of Chemical Technology, Vol. 7, pp. 257-262, published by Interscience Publishers, Inc. (1951) or in U.S. Pat. No. 1 ,922,459.
  • the polyether polyol includes the alkylene oxide addition products of polyhydric alcohols such as ethylene glycol, propylene glycol, dipropylene glycol, trimethylene glycol, 1 ,2- butanediol, 1 ,5- pentanediol, 1 ,6-hexanediol, 1 ,7-heptanediol, hydroquinone, resorcinol glycerol, glycerine, 1 , 1 ,1-trimethylol-propane, 1 ,1 ,1-trimethylolethane, pentaerythritol, 1 ,2,6-hexanetriol, a-methyl glucoside, sucrose, and sorbitol.
  • polyhydric alcohols such as ethylene glycol, propylene glycol, dipropylene glycol, trimethylene glycol, 1 ,2- butanediol, 1 ,5- pentanediol, 1
  • polyhydric alcohol compounds derived from phenol such as 2,2- bis(4-hydroxyphenyl)-propane, commonly known as Bisphenol A. Also included may be a polyol which is initiated with a compound having at least two primary or secondary amine groups, a polyhydric alcohol having 4 or more hydroxyl groups, such as sucrose, or a mixture of initiators employing a polyhydric alcohol having at least 4 hydroxyl groups and compounds having at least two primary or secondary amine groups.
  • Suitable organic amine initiators which may be condensed with alkylene oxides include aromatic amines-such as aniline, N- alkylphenylene-diamines, 2,4'-, 2,2'-, and 4,4'-methylenedianiline, 2,6- or 2,4- toluenediamine, vicinal toluenediamines, o-chloro-aniline, p-aminoaniline, 1 ,5- diaminonaphthalene, methylene dianiline, the various condensation products of aniline and formaldehyde, and the isomeric diaminotoluenes; and aliphatic amines such as mono-, di-, and trialkanolamines, ethylene diamine, propylene diamine, diethylenetriamine, methylamine, triisopropanolamine, 1 ,3- diaminopropane, 1 ,3-diaminobutane, and 1 ,4-diaminobutane
  • polyether polyols contemplated for use in this disclosure are alkylene oxide adducts of a phenol/formaldehyde/alkanolamine resin, frequently called "Mannich" polyols such as disclosed in U.S. Pat. Nos. 4,883,826; 4,939,182; and 5, 120,815.
  • the amount of polyol to be used relative to the isocyanate normally should be such that the isocyanate groups are present in at least an equivalent amount, and preferably, in slight excess, compared to the free hydroxyl groups.
  • the components will be proportioned so as to provide from about 0.9 to about 1.5 mole equivalents of isocyanate groups per mole equivalent of hydroxyl groups.
  • the mole equivalents of isocyanate to hydroxyl groups can be as low as 0.4.
  • a blowing agent which may be selected based in part upon the desired density of the final foam.
  • hydrocarbon blowing agents may be selected.
  • hydrocarbon or fluorine-containing hydrohalocarbon blowing agents may be used, and in some instances may serve to reduce, or further reduce, viscosity, and thereby enhance processability.
  • the blowing agent is an unsaturated halogenated hydroolefin such as a hydrofluoroolefin (HFO), hydrochlorofluoroolefin (HCFO), or mixtures thereof.
  • HFO hydrofluoroolefin
  • Preferred hydrofluoroolefin (HFO) blowing agents contain 3, 4, 5, or 6 carbons, and include but are not limited to pentafluoropropenes, such as 1 ,2,3,3,3-pentafluoropropene (HFO-1225ye); tetrafluoropropenes, such as 1 ,3,3,3-tetrafluoropropene (HFO-1234ze, E and Z isomers), 2,3,3,3- tetrafluoropropene (HFO-1234yf), and 1 ,2,3,3-tetrafluoropropene (HFO-1234ye); trifluoropropenes, such as 3,3,3-trifluoropropene (
  • hydrocarbons and/or non- fluorine-containing hydrohalocarbons may be used in an amount of about 0.5 parts by weight to about 30 parts by weight, or about 1 part by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s).
  • Another blowing agent that may be used is formic acid or another carboxylic acid.
  • the formic acid or other carboxylic acid may be used in an amount of from about 0.5 parts by weight to about 8 parts by weight, based on 100 parts by weight of polyol(s). It is also contemplated that other aliphatic mono- and polycarboxylic acids may be employed, such as those disclosed in U.S. Pat. No. 5,143,945, which is incorporated herein by reference in its entirety, and including isobutyric acid, ethylbutyric acid, ethylhexanoic acid, and combinations thereof.
  • water may also be optionally selected as a blowing agent.
  • the water is, in some non-limiting embodiments, present in an amount of from about 0.1 parts by weight to about 40 parts by weight, or from about 0. 5 parts by weight to about 20 parts by weight, or from about 0.25 parts by weight to about 5 parts by weight, or from about 0.5 parts by weight to about 3 parts by weight, based on 100 parts by weight of polyol(s).
  • the amount of water used may not exceed 3 parts by weight water, or not more than 2.5 parts by weight of water, or not more than 1 part by weight of water, based on 100 parts by weight of polyol(s). Omission of water may be desirable in some non-limiting embodiments.
  • catalysts substantially free of nonylphenol may optionally be included in the foam composition.
  • the additional catalyst(s) are also substantially free of nonylphenol.
  • an amine catalyst may be included, including any organic compound which contains at least one tertiary nitrogen atom and is capable of catalyzing the hydroxyl/isocyanate reaction between the isocyanate and polyol.
  • Typical classes of amines include the N- alkylmorpholines, N-alkyl-alkanolamines, ⁇ , ⁇ -dialkylcyclohexylamines, and alkylamines where the alkyl groups are methyl, ethyl, propyl, butyl and isomeric forms thereof, and heterocyclic amines.
  • Typical but non-limiting thereof are triethylenediamine, tetramethylethylenediamine, bis(2-dimethylaminoethyl)ether, triethylamine, tripropylamine, tributylamine, triamylamine, pyridine, quinoline, dimethylpiperazine, piperazine, ⁇ , ⁇ -dimethylcyclohexylamine, N-ethyl- morpholine, 2-methylpropanediamine, methyltriethyl-enediamine, 2,4,6- tridimethylamino-methyl)phenol, N,N',N"-tris(dimethylamino-propyl)sym- hexahydrotriazine, and mixtures thereof.
  • the tertiary amines from which selection may be made may include bis(2-dimethylamino-ethyl)ether, dimethylcyclohexylamine, ⁇ , ⁇ -dimethyl-ethanolamine, triethylenediamine, triethylamine, 2,4,6-tri(dimethylaminomethyl)phenol, ⁇ , ⁇ ', ⁇ -ethylmorpholine, and mixtures thereof.
  • Non-amine catalyst may also be included in foam compositions of the present disclosure.
  • Typical of such catalysts are organometallic compounds of bismuth, lead, tin, titanium, iron, antimony, uranium, cadmium, cobalt, thorium, aluminum, mercury, zinc, nickel, cerium, molybdenum, vanadium, copper, manganese, zirconium, and combinations thereof. Included for illustrative purposes only are bismuth nitrate, lead 2-ethylhexoate, lead benzoate, lead naphthenate, ferric chloride, antimony trichloride, antimony glycolate, combinations thereof, and the like.
  • Embodiments include the stannous salts of carboxylic acids, such as stannous acetate, stannous octoate, stannous 2- ethylhexoate, 1-methylimidazole, and stannous laurate, as well as the dialkyl tin salts of carboxylic acids, such as dibutyl tin diacetate, dibutyl tin dilaurate, dibutyl tin dimaleate, dioctyl tin diacetate, combinations thereof and the like.
  • carboxylic acids such as stannous acetate, stannous octoate, stannous 2- ethylhexoate, 1-methylimidazole, and stannous laurate
  • dialkyl tin salts of carboxylic acids such as dibutyl tin diacetate, dibutyl tin dilaurate, dibutyl tin dimaleate, dioctyl tin diacetate
  • the amount of catalyst substantially free of nonylphenol (and optional catalyst(s)) added to the foam composition is a catalytically sufficient amount.
  • the amount of catalyst substantially free of nonylphenol (and optional catalyst(s)) that is included in the foam composition is from about 0.5 parts by weight to about 15 parts by weight, in another embodiment from about 0.75 part by weight to about 12 parts by weight, and in still another embodiment from about 1 part by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s).
  • the foam composition can also comprise additives.
  • additives include: cell stabilizers, such as organopolysiloxane surfactants; flame retardants such as halogenated organophosphorous compounds; chain extenders such as ethylene glycol and butane diol; crosslinkers such as glycerol, trimethylolpropane, pentaerythritol, sucrose, sorbitol, or mixtures thereof; fillers and pigments, such as calcium carbonate, titanium dioxide, iron oxide, chromium oxide, azo/diazo dyes, phthalocyanines, dioxazines, carbon black barium sulfate, graphite, microspheres, alumina trihydrate, wollastonite, prepared glass fibers (dropped or continuous), and polyester fibers and other polymeric fibers, as well as various combinations thereof; odor masks, biocides, antioxidants, UV stabilizers such as hydroxybenzotriazoles, zinc dibutyl thiocarbamate
  • Each additive may constitute from 0.01 parts by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s).
  • Fillers and pigments may be used in quantities as high as up to about 50 parts by weight, based on 100 parts by weight of polyol(s).
  • polyurethane or polyisocyanurate foams using the foam compositions described herein may follow any of the methods well known in the art for preparing polyurethane and polyisocyanurate foam, for example, as described in Saunders and Frisch, "Volumes I and II Polyurethanes Chemistry and Technology” (1962, John Wiley and Sons, New York, N.Y.), or Gum et al., “Reaction Polymers” (1992, Oxford University Press, New York, N.Y.), or Klempner and Sendijarevic, "Polymeric Foams and Foam Technology” (2004, Hanser Gardner Publications, Cincinnati, Ohio). In general, the various components are brought together and mixed using manual or mechanical mixing means to form the foam.
  • the polyol and catalyst are preblended to form a single component which is fed as one stream to a conventional mixing head and admixed with the isocyanate which is fed as a separate stream to the mixing head.
  • the blowing agent can be fed as a separate stream to the mixing head or blended with one or other, or both, of the other components prior to feeding the latter to the mixing head.
  • the foams subsequently produced can be rigid, flexible, or semi-rigid, and can have a closed cell structure, an open cell structure or a mixture of open and closed cells and may vary in density of from about 0.5 pounds per cubic foot to about 60 pounds per cubic foot, such as from about 1.0 to 20.0 pounds per cubic foot, and in other embodiments from about 1.5 to 6.0 pounds per cubic foot.
  • the foams are suitable for use in a wide range of applications including appliance insulation (e.g., insulating refrigerators or water heaters), structural insulation (e.g. spray foams or lamination foams for commercial or residential insulation), cushioning, flotation, packaging, adhesives, void filling, crafts and decorative, and shock absorption.
  • appliance insulation e.g., insulating refrigerators or water heaters
  • structural insulation e.g. spray foams or lamination foams for commercial or residential insulation
  • cushioning e.g. spray foams or lamination foams for commercial or residential insulation
  • cushioning flotation
  • packaging e.g. spray foams or lamination foams for commercial or residential insulation
  • adhesives e.g. spray foams or lamination foams for commercial or residential insulation
  • Such foam is typically prepared by intimately mixing the reaction components, for example, a B-side containing a polyol/blowing agent/catalyst according to the present disclosure and an A-side containing an isocyanate (i.e., two streams); or a B-side containing a polyol/blowing agent, a C-side containing the catalyst according to the present disclosure, and an A-side containing a polyisocyanate component (at least three streams, wherein the polyol/blowing agent and catalyst according to the present disclosure mix just prior to contact thereof with the polyisocyanate component) at room temperature or at a slightly elevated temperature for a short period of time.
  • a B-side containing a polyol/blowing agent/catalyst according to the present disclosure and an A-side containing an isocyanate (i.e., two streams); or a B-side containing a polyol/blowing agent, a C-side containing the catalyst according to the present disclosure, and an A
  • Mixing of streams may be carried out either in a spray apparatus, a mixhead with or without a static mixer, or a vessel.
  • the mixture is then sprayed or otherwise deposited onto a substrate.
  • This substrate may be, for example, a rigid or flexible facing sheet made of foil or another material, including another layer of similar or dissimilar polyurethane or polyisocyanurate which is being conveyed, continuously or discontinuously, along a production line, or directly onto a conveyor belt.
  • the mixture may be poured into an open mold or distributed via laydown equipment into an open mold or simply deposited at or into a location for which it is destined, i.e., a pour-in-place application, such as between the interior and exterior walls of a structure.
  • a pour-in-place application such as between the interior and exterior walls of a structure.
  • a second sheet may be applied on top of the deposited mixture.
  • the mixture may be injected into a closed mold, with or without vacuum assistance for cavity-filling. If a mold is employed, it is most typically heated.
  • such applications above may be accomplished using the known one-shot, prepolymer or semi-prepolymer techniques used together with conventional mixing methods.
  • the mixture on reacting, takes the shape of the mold or adheres to the substrate to produce a polyurethane or polyisocyanurate foam of a more-or-less predefined structure, which is then allowed to cure in place or in the mold, either partially or fully.
  • Suitable conditions for promoting the curing include a temperature of typically from 20°C to 50°C, such as from 35°C to 75°C, and including from 45°C to 55°C.
  • Such temperatures will usually permit the sufficiently cured foam to be removed from the mold, where such is used, typically within from about 1 to 10 minutes and more typically within from 1 to 5 minutes after mixing of the reactants.
  • Optimum cure conditions will depend upon the particular components, including catalysts and quantities used in preparing the foam and also the size and shape of the article manufactured.
  • the result may be a rigid foam in the form of slabstock, a molding, a filled cavity, including but not limited to a pipe or insulated wall or hull structure, a sprayed foam, a frothed foam, or a continuously- or discontinuously- manufactured laminate product, including but not limited to a laminate or laminated product formed with other materials, such as hardboard, plasterboard, plastics, paper, metal, or a combination thereof.
  • Example 1 Preparation of Catalyst Substantially Free of Nonylphenol.
  • Example 2 Preparation of Catalyst Substantially Free of Nonylphenol.
  • Methylpyrrole was dissolved in diethylene glycol and then reacted with sodium sarcosine and formaldehyde in the amounts shown below at 80°C to form a Mannich condensation product, Excess water was then stripped at 80°C and 40 mmHg reduced pressure. The resulting product was a thick pasty brown semi-solid and was confirmed by C 3 NMR to be a mixture of Mannich condensates: sodium 2-aminoacetomethylpyrrole and disodium bis-2-6-(2- aminoacetomethylpyrrole).
  • Methylpyrrole was dissolved in diethylene glycol and then reacted with sodium sarcosine and formaldehyde in the amounts shown below at 80°C to form a Mannich condensation product. Excess water was then stripped at 80°C and 40 mmHg reduced pressure. The resulting product was a slightly viscous pourable liquid and was confirmed by C13 NMR to be a Mannich condensate having a mono functional sarcosine substitution on the pyrrole ring.
  • Foams were prepared from the following components
  • Example 1 catalyst substantially free of nonylphenol.
  • the catalyst was added to the B-side and mixed for 10 seconds.
  • the A-side and B-side were then mixed together for 10 seconds to produce foams having the following properties:
  • Foams were prepared from the following components:
  • Example 3 catalyst substantially free of nonylphenol.
  • the catalyst was added to the B-side and mixed for 10 seconds.
  • the A-side and B-side were then mixed together for 10 seconds to produce foams having the following properties:
  • inventive catalysts substantially free of nonylphenol are surprisingly more active (approx. 50%) than the state of the art catalysts prepared from nonylphenol. Also surprising was that less inventive catalyst was required to provide the same catalytic activity as the state of the art catalyst.
  • Example 6 Rigid spray foam made with inventive catalysts using low global warming blowing agents with good heat aged stability were prepared from the following components:
  • Terol 250 polyol an aromatic polyester polyol.
  • 6 TCPP is trichloropropylphosphate.
  • Example 1 catalyst substantially free of nonylphenol.
  • a firm time is the measure of cure - it is the time that a foam no longer yields when a constant force is applied to the surface of the foam.
  • the following components were used in this example:
  • TCPP1 is trichloropropylphosphate.
  • PHT4-diol2 is tetrabromophthalicanhydride.
  • Example 1 catalyst substantially free of nonylphenol. 54.4% of the A-side and 45.6% of the B-side were mixed together for 8 seconds to produce foams having the following properties:

Landscapes

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

Abstract

The present disclosure provides a catalyst substantially free of nonylphenol comprising a Mannich condensation product of (i) a heterocyclic compound containing at least one -N(H)- group in the ring; (ii) an aldehyde; and (iii) a metal salt of an aminocarboxylic acid. The catalyst substantially free of nonylphenol may be used in the preparation of polyurethane or polyisocyanurate foam.

Description

POLYISOCYANURATE CATALYSTS FOR METAL PANELS
AND SPRAY FOAMS
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application claims priority to United States Provisional Serial No. 62/309,555 filed March 17, 2016. The noted application is incorporated herein by reference.
STATEMENT REGARDING FEDERALLY SPONSORED
RESEARCH OR DEVELOPMENT
[0002] Not applicable.
FIELD OF THE INVENTION
[0003] The present disclosure provides a catalyst substantially free of nonylphenol comprising a Mannich condensation product prepared from a heterocyclic compound containing at least one -N(H)- group in the ring, an aldehyde, and a metal salt of an aminocarboxylic acid. The catalyst according to the present disclosure exhibits high catalytic activity and is suitable for use in the preparation of polyurethane and polyisocyanurate foam.
BACKGROUND
[0004] Typically, polyisocyanurate and polyurethane foams are made by reacting a polyol and a polyisocyanate in the presence of a catalyst. Additional additives, such as blowing agents, surfactants and flame retardants, can also be present. The reactions for forming the polyurethane or polyisocyanurate foam consist mainly of a urethane bond-forming reaction (gelling reaction) by the reaction of the polyol with the polyisocyanate, a urea group-forming reaction (blowing reaction) by the reaction of the polyisocyanate with water, and an isocyanurate ring-forming reaction (trimerization reaction) by trimerization of the polyisocyanate. [0005] Known catalysts for accelerating the gelling reaction and/or blowing reaction include tertiary amine catalysts and organic metal catalysts. Among such tertiary amine catalysts, those industrially used may, for example, be compounds such as triethylenediamine, N,N,N',N'-tetramethyl-1 ,6- hexanediamine, Ν,Ν-dimethylcyclohexylamine, bis(2-dimethylaminoethyl) ether, N,N,N',N",N"-pentamethyldiethylenetriamine, N-methylmorpholine and N- ethylmorpholine. Organic metal catalysts generally include organolead, organoferric and organotin compounds, such as stannous chloride, and tin salts of carboxylic acids.
[0006] Also effective as catalysts are Mannich condensation products formed from nonylphenol, formaldehyde and a primary or secondary amine. However, in recent years, nonylphenol and related chemical forms of nonylphenol have raised concerns because of their effects on the endocrine system. Such concerns have led to many regulations and restrictions on the use of nonylphenol throughout the world.
[0007] Thus, there exists a need to develop new catalysts which are nonylphenol-free having the same or higher catalytic activity than state of the art catalysts based on nonylphenol.
SUMMARY
[0008] In one aspect, there is provided a catalyst substantially free of nonylphenol which is suitable for use in the preparation of a polyurethane or polyisocyanurate foam. The catalyst according to the present disclosure includes a Mannich condensation product of: (i) a heterocyclic compound containing at least one -N(H)- group in the ring; (ii) an aldehyde; and (iii) a metal salt of an aminocarboxylic acid. [0009] In a second aspect, there is provided a polyurethane or polyisocyanurate foam composition that contains the catalyst according to the present disclosure.
[0010] In a third aspect, there is provided a process for preparing a polyurethane or polyisocyanurate foam utilizing the catalyst according to the present disclosure.
[0011] In a fourth aspect, there is provided a polyurethane or polyisocyanurate foam obtained by bringing together, under foam-forming conditions, a polyisocyanate, a polyol, a blowing agent and the catalyst according to the present disclosure.
DETAILED DESCRIPTION
[0012] If appearing herein, the term "comprising" and derivatives thereof are not intended to exclude the presence of any additional component, step or procedure, whether or not the same is disclosed herein. In order to avoid any doubt, all compositions claimed herein through use of the term "comprising" may include any additional additive, adjuvant, or compound, unless stated to the contrary. In contrast, the term, "consisting essentially of if appearing herein, excludes from the scope of any succeeding recitation any other component, step or procedure, except those that are not essential to operability and the term "consisting of, if used, excludes any component, step or procedure not specifically delineated or listed. The term "or", unless stated otherwise, refers to the listed members individually as well as in any combination.
[0013] The articles "a" and "an" are used herein to refer to one or to more than one (i.e. to at least one) of the grammatical objects of the article. By way of example, "an amine" means one amine or more than one amine. The phrases "in one embodiment", "according to one embodiment" and the like generally mean the particular feature, structure, or characteristic following the phrase is included in at least one embodiment of the present disclosure, and may be included in more than one embodiment of the present disclosure. Importantly, such phrases do not necessarily refer to the same embodiment. If the specification states a component or feature "may", "can", "could", or "might" be included or have a characteristic, that particular component or feature is not required to be included or have the characteristic.
[0014] The term "substantially free" means, when used with reference to the substantial absence of a material, that such a material is present, if at all, as an incidental impurity or by-product. For instance in some embodiments, the material may be present in the composition of matter at an amount of no more than 100 ppm, in some instances less than 20 ppm and in still other instances less than 1 ppm.
[0015] The catalyst substantially free of nonylphenol according to the present disclosure exhibits surprisingly high catalytic activity. Moreover, since the catalyst is substantially free of nonylphenol, it's environmentally safe and can be used in countries and specific regions that have banned the use of nonylphenol.
[0016] In one aspect, the heterocyclic -N(H)- containing compounds useful in preparing the catalyst according to the present disclosure include heterocyclic compounds containing a 5- or 6-membered ring with one nitrogen hetero-atom or two or three adjacent nitrogen hetero-atoms, in which two adjacent carbon atoms of the heterocyclic ring may form part of a further 6-aromatic, heterocyclic or alicyclic ring system, wherein the heterocyclic compound contains at least one -N(H)- ring group. The heterocyclic compound can contain other hetero-atoms, usually O or S. In some embodiments, the heterocyclic ring is unsaturated.
[0017] In one embodiment, the 6-membered ring system, part of which may be formed by two adjacent carbon atoms of the heterocyclic ring, comprises an aromatic ring system, for example, a benzene ring or naphthalene ring system. In other embodiments, this adjacent 6-membered ring system comprises a heterocyclic ring or an ethylenically unsaturated alicyclic ring system.
[0018] The 5- or 6-membered heterocyclic ring and the adjacent 6-membered ring system, if present, may be substituted or unsubstituted. In some embodiments, substitution occurs on carbon-atoms of the ring. Substituents can include an alkyl group, an alkaryl group, an aryl group, an aralkyl group or an alkenyl group. In one embodiment, the alkyl group contains from 1-10 carbon atoms, for example, a methyl, ethyl, propyl, butyl, pentyl, or decyl group. In another embodiment, the aryl group contains from 6-10 carbon atoms, such as phenol or naphthyl. In still another embodiment, the alkaryl group and aralkyl group contain from 7-10 carbon atoms, such as tolyl, xylyl or ethylphenyl. In yet another embodiment, the alkenyl group contains from 2-10 carbon atoms, such as ethenyl, propenyl, butenyl, or decenyl.
[0019] In one particular embodiment, the heterocyclic compound containing at least one -N(H)- group in the ring is triazole, benzotriazole, 5-methyl benzotriazole, 5-ethyl benzotriazole, 5-butyl benzotriazole, 5-propyl benzotriazole, 5-dodecyl benzotriazole, 2-methyl benzotriazole, 2-ethyl benzotriazole, 2-butyl benzotriazole, 2-propyl benzotriazole, 2-dodecyl benzotriazole, 5,7-dimethyl benzotriazole, 5,7-diethyl benzotriazole, 5,7-dibutyl benzotriazole, 5,7-dipropyl benzotriazole, 5,7-didodecyl benzotriazole, naphthotriazole, 5-methyl naphthotriazole, 5-ethyl naphthotriazole, 5-butyl naphthotriazole, 5-propyl naphthotriazole, 5-dodecyl naphthotriazole, imidazole,
4- methyl imidazole, 4-ethyl imidazole, 4-butyl imidazole, 4-propyl imidazole, 4- dodecyl imidazole, 5-methyl imidazole, 5-ethyl imidazole, 5-butyl imidazole, 5- propyl imidazole, 5-dodecyl imidazole, benzimidazole, 5-methyl benzimidazole,
5- ethyl benzimidazole, 5-butyl benzimidazole, 5-propyl benzimidazole, 5-dodecyl benzimidazole, 2-methyl benzimidazole, 2-ethyl benzimidazole, 2-butyl benzimidazole, 2-propyl benzimidazole, 2-dodecyl benzimidazole, 5,7-dimethyl benzimidazole, 5,7-diethyl benzimidazole, 5,7-dibutyl benzimidazole, 5,7-dipropyl benzimidazole, 5,7-didodecyl benzimidazole, pyrrole, 2-methyl pyrrole, 2-ethyl pyrrole, 2-butyl pyrrole, 2-propyl pyrrole, 2-dodecyl pyrrole 3-methyl pyrrole, 3- ethyl pyrrole, 3-butyl pyrrole, 3-propyl pyrrole, 3-dodecyl pyrrole, 5-methyl benzpyrrole, pyrazole, 5-methyl benzpyrazole, 5-ethyl benzpyrazole, 5-butyl benzpyrazole, 5-propyl benzpyrazole, 5-dodecyl benzpyrazole, 7-methyl benzpyrazole, 6-ethyl benzpyrazole, 7-butyl benzpyrazole, 6-propyl benzpyrazole, 7-dodecyl benzpyrazole, 5,7-dimethyl benzpyrazole, 5,7-diethyl benzpyrazole, 5,7-dibutyl benzpyrazole, 5,7-dipropyl benzpyrazole, 5,7-didodecyl benzpyrazole, 2-pyrroline, 3-pyrroline, 3-pyrazoline, carbazole, 5-methyl carbazole, indole, 3-methyl indole, 3-ethyl indole, 3-butyl indole, 3-propyl indole,
3- dodecyl indole, 4-methyl indole, 4-ethyl indole, 4-butyl indole, 4-propyl indole,
4- dodecyl indole, purine, phenothiazine, phenoxazine or perimidine.
[0020] In one specific embodiment, the heterocyclic compound containing at least one -N(H)- group is selected from pyrrole, 2-methyl pyrrole and 3-methyl pyrrole.
[0021] Representative aldehydes for use in the preparation of the Mannich condensation product include aliphatic aldehydes and aromatic aldehydes. The aliphatic aldehydes include Ci to C6 aldehydes, such as formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, valeraldehyde, and hexanal aldehyde. Aromatic aldehydes which may be used include benzaldehyde and salicylaldehyde. Illustrative heterocyclic aldehydes for use herein are furfural and thiophene aldehyde, etc. Also useful are formaldehyde-producing reagents such as paraformaldehyde, or aqueous formaldehyde solutions such as formalin. In one particular embodiment, the aldehyde is formaldehyde or formalin.
[0022] According to one aspect, the aminocarboxylic acid is selected from an a-amino acid, a β-amino acid, a γ-amino acid, a δ-amino acid, a ε-amino acid and a ζ-amino acid. [0023] Examples of a-amino acids include glycine (aminoacetic acid), N- methylglycine (N-methylaminoacetic acid, sarcosine), N-ethylglycine, alanine (2- aminopropionic acid), N-methylalanine (2-(methylamino)propionic acid), N,N- dimethylalanine, N-ethylalanine, 2-methylalanine (2-aminoisobutyric acid), leucine (2-amino-4-methylpentan-1-oic acid), N-methylleucine, N,N- dimethylleucine, isoleucine (1-amino-2-methylpentanoic acid), N- methylisoleucine, valine (2-aminoisovaleric acid), a-methylvaline (2-amino-2- methylisovaleric acid), N-methylvaline (2-methylaminoisovaleric acid), proline (pyrrolidine-2-carboxylic acid), N-methylproline, serine (2-amino-3- hydroxypropan-1-oic acid), N-methylserine, 2-(methylamino)isobutyric acid, piperidine-2-carboxylic acid and N-methylpiperidine-2-carboxylic acid.
[0024] Examples of β-amino acids include 3-aminopropionic acid (β-alanine), 3-methylaminopropionic acid, iminodipropionic acid, N-methyliminodipropionic acid, piperidine-3-carboxylic acid and N-methylpiperidine-3-carboxylic acid.
[0025] Examples of γ-amino acids include 4-aminobutyric acid and 4- methylaminobutyric acid.
[0026] Other aminocarboxylic acids include piperidine-4-carboxylic acid and N-methylpiperidine-4-carboxylic acid.
[0027] In one particular embodiment suitable aminocarboxylic acids include N-mono-C-i^-alkylaminocarboxylic acids, in particular N-mono-Ci-C4-alkyl-a- aminocarboxylic acids.
[0028] The metal salt is generally an alkali metal or alkaline earth metal salt. In one particular embodiment the metal salt is an alkali metal salt such as a sodium or potassium salt, of which sodium salts are most preferred.
[0029] According to one particular embodiment, the metal salt of the aminocarboxylic acid is a compound of the formula N (CH 2)x COOM
R H
where Ri , R2, and R3 are, independently of one another, H or a C1-C3 alkyl group, M is sodium or potassium and x is an integer from 0 to 5.
[0030] In another particular embodiment, the metal salt of the aminocarboxylic acid is the sodium salt of N-methylglycine.
[0031] The Mannich condensation product can be prepared by reacting the heterocyclic compound containing at least one -N(H)- group in the ring with the aldehyde and the metal salt of an aminocarboxylic acid. In one embodiment, the reaction occurs by contacting the heterocyclic compound containing at least one -N(H)- group in the ring, the aldehyde and the metal salt of an aminocarboxylic acid in a reaction zone. The reactants may be contacted for a time and under conditions effective to react the aldehyde, reactive amine groups of the metal salt of the aminocarboxylic acid and the -N(H)- group(s) of the heterocyclic compound to form the Mannich condensation product containing heterocyclic nitrogen units bound to at least a portion of the aminocarboxylic acid through a hydrocarbylene group derived from the aldehyde (for e.g., a methylene (-CH2-) group derived from formaldehyde).
[0032] The conditions of temperature and pressure under which the reaction occurs can vary widely, and generally temperatures from about 0°C to 80°C can be used. The pressures in the reaction zone will be sufficient to maintain a liquid reaction medium, and generally pressures from about 0.1 kPa to 1000 kPa, such as from about 1 kPa to 100 kPa, can be employed.
[0033] The reaction can be carried out in a batchwise, continuous or semicontinuous manner, in one or more reaction zones. The reaction can be conducted in any conventional apparatus such as stirred tank reactors, tubular flow reactors and the like.
[0034] The reactants can be charged to the reaction zone continuously or intermittently, together or sequentially, in any order. Generally, the heterocyclic compound containing at least one -N(H)- group in the ring, and any carrier or solvent for the reaction, will first be charged to the reaction zone, followed by the aldehyde reactant and then the metal salt of an aminocarboxylic acid, which can, if desired, be also introduced to the reaction zone as a mixture of the aldehyde and metal salt of an aminocarboxylic acid reactants. In some embodiments, the metal salt of an aminocarboxylic acid is not contacted with the heterocyclic compound containing at least one -N(H)- group in the ring reactant in the absence of the aldehyde when at reaction conditions.
[0035] The reaction can be accomplished using a wide range of ratios of reactants, and the metal salt of an aminocarboxylic acid:aldehyde:heterocyclic compound containing at least one -N(H)~ group in the ring reactants may be generally charged in a ratio of from 1 :0.01 :0.01 to 1 :50:50, and in some embodiments from 1 :0.2:0.2 to 1 :10:10, and in still more embodiments from 1 :0.5:0.5 to 1 :5:5, molar equivalents of metal salt of an aminocarboxylic acid:moles of aldehyde:moles of heterocyclic compound containing at least one - N(H)-group.
[0036] The reaction can be conducted in bulk (no diluent or solvent) or in a diluent or solvent. In one particular embodiment, the reaction is conducted in a solvent. Examples of diluents and solvents include ethylene glycol, propylene glycol, diethylene glycol, dipropylene glycol, as well as polyethylene or polypropylene glycols in the 100-1000 molecular weight range, benzene, toluene and xylene. Water that is evolved during the reaction can be removed by azeotropic distillation during the course of the reaction or after the completion of the reaction. For instance in one embodiment, the temperature and pressure can be maintained at about 80°C and about 40 mm Hg reduced pressure after completion of the reaction to remove water that has evolved. Typical reaction times may range from about 0.5 to about 12 hours, although longer or shorter times can be used as necessary or as desired.
[0037] According to another aspect of the present disclosure, there is provided a polyurethane or polyisocyanurate foam composition containing an isocyanate, a polyol, a blowing agent and the catalyst substantially free of nonylphenol. The polyurethane or polyisocyanurate foam compositions according to the present disclosure are usually divided up into two components. The isocyanate portion is generally referred to as the A-side and the polyol portion is referred to as the B-side. Thus, in embodiments where the polyurethane or polyisocyanurate foam composition includes an A-side containing an isocyanate and a B-side containing a polyol, each of the remaining components of the foam composition may be included in either the A-side or B- side or they can be included as a separate component(s).
[0038] The isocyanate in the foam composition may be selected from a wide variety of isocyanates, including those that are well known to one skilled in the art. For example, organic polyisocyanates, modified multi-functional polyisocyanates, isocyanate-based prepolymers, and mixtures thereof may be employed. These may further include aliphatic and cycloaliphatic isocyanates, and in particular aromatic and, more particularly, multifunctional aromatic isocyanates. Polyphenyl polymethylene polyisocyanates (PMDI) may also be used. [0039] In one embodiment, the isocyanate includes 2,4- and 2,6- toluenediisocyanate and the corresponding isomeric mixtures; 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanate and the corresponding isomeric mixtures; mixtures of 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanates and polyphenyl polymethylene polyisocyanates (PMDI); and mixtures of PMDI and toluene diisocyanates. Also useful herein are aliphatic and cycloaliphatic isocyanate compounds, such as 1 ,6-hexamethylenediisocyanate; 1-isocyanato~3,5,5- trimethyl-1 ,3-isocyaantomethylcyclohexane; 2,4- and 2,6-hexahydrotoluene- diisocyanate and their corresponding isomeric mixtures; and 4,4'-, 2,2'- and 2,4'- dicyclohexyl-methanediisocyanate and their corresponding isomeric mixtures. Also useful is 1 ,3-tetra-methylene xylene diisocyanate.
[0040] In another embodiment, the isocyanate is a so-called modified multifunctional polyisocyanate, that is, a product which is obtained through chemical reaction of the above diisocyanates and/or polyisocyanates. Examples include polyisocyanates containing esters, ureas, biurets, allophanates and, preferably, carbodiimides and/or uretonomine, and isocyanurate and/or urethane group-containing diisocyanates or polyisocyanates. Liquid polyisocyanates containing carbodiimide groups, uretonomine groups and/or isocyanurate rings, having isocyanate group (NCO) contents of from 120 to 40 weight percent, or from 20 to 35 weight percent, can also be used. These include, for example, polyisocyanates based on 4,4'-2,4'- and/or 2,2'-diphenylmethane diisocyanate and the corresponding isomeric mixtures, 2,4- and/or 2,6-toluenediisocyanate and the corresponding isomeric mixtures; mixtures of diphenylmethane diisocyanates and PMDI; and mixtures of toluenediisocyanates and PMDI and/or diphenylmethane diisocyanates.
[0041] Suitable isocyanate-based prepolymers are prepolymers having NCO contents of from 2 to 40 weight percent, or from 4 to 30 weight percent. These prepolymers are prepared by reaction of the di- and/or polyisocyanates with materials including lower molecular weight diols and triols, but also can be prepared with multivalent active hydrogen compounds such as di- and tri-amines and di- and tri-thiols. Individual examples include aromatic polyisocyanates containing urethane groups, which may have NCO contents of from 5 to 40 weight percent, or 20 to 35 weight percent, obtained by reaction of diisocyanates and/or polyisocyanates with, for example, polyols such as lower molecular weight diols, triols, oxyalkylene glycols, dioxyalkylene glycols, or polyoxyalkylene glycols having molecular weights up to about 800. These polyols can be employed individually or in mixtures as di- and/or polyoxyalkylene glycols. For example, diethylene glycols, dipropylene glycols, polyoxyethylene glycols, ethylene glycols, propylene glycols, butylene glycols, polyoxypropylene glycols and polyoxypropylene polyoxyethylene glycols can be used. Polyester polyols can also be used, as well as alkyl diols such as butane diol. Other diols also useful include bishydroxyethyl- or bishydroxypropyl-bisphenol A, cyclohexane dimethanol, and bishydroxyethyl hydroquinone.
[0042] The isocyanate may be used in an amount sufficient to provide an isocyanate index of at least 80. Isocyanate index is calculated as the number of reactive isocyanate groups provided by the isocyanate divided by the number of isocyanate-reactive groups in the polyurethane or polyisocyanurate foam composition (including those contained by blowing agents such as water) and multiplying by 100. Water is considered to have two isocyanate-reactive groups per molecule for purposes of calculating isocyanate index. In one embodiment, the isocyanate index is from about 80 to about 600. For polyurethane foam applications, the isocyanate index may generally be from about 80 to 150. For polyisocyanurate foam applications, the isocyanate index may generally be greater than about 150 and up to about 600.
[0043] Polyols which may be present in the foam composition include one or more polyester or polyether polyols of the kind typically employed in processes to make polyurethane or polyisocyanurate foam. Other compounds having at least two isocyanate reactive hydrogen atoms may also be present, for example: polythioether polyols; condensate adducts of phenol and formaldehyde with one or more alkylene oxides including ethylene oxide, propylene oxide, and butylene oxide; polyester amides and polyacetals containing hydroxyl groups; aliphatic polycarbonates containing hydroxyl groups; amine terminated polyoxyalkylene polyethers; and graft dispersion polyols. Mixtures of two or more of the aforesaid materials may also be employed.
[0044] The term "polyester polyol" as used herein includes any minor amounts of unreacted polyol remaining after the preparation of the polyester polyol and/or unesterified polyol (for example, glycol) added after the preparation of the polyester polyol. Polyester polyols can be produced, for example, from organic dicarboxylic acids with 2 to 12 carbons, including aliphatic dicarboxylic acids with 4 to 6 carbons, and divalent and multivalent alcohols, including diols, with 2 to 12 carbons, such as, 2 to 6 carbons. Examples of dicarboxylic acids include succinic acid, glutaric acid, adipic acid, suberic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, maleic acid, fumaric acid, phthalic acid, isophthalic acid, and terephthalic acid. The dicarboxylic acids can be used individually or in mixtures. Instead of the free dicarboxylic acids, the corresponding dicarboxylic acid derivatives may also be used, such as dicarboxylic acid mono- or di-esters of alcohols with 1 to 4 carbons, or dicarboxylic acid anhydrides. Dicarboxylic acid mixtures of succinic acid, glutaric acid and adipic acid in quantity ratios of 20-35:35-50:20-32 parts by weight may also be used. Examples of divalent and multivalent alcohols include ethanediol, diethylene glycol, 1 ,2- and 1 ,3- propanediol, dipropylene glycol, 1 ,4-butanediol, 1 ,5-pentanediol, 1 ,6-hexanediol, 1 ,10-decanediol, glycerine and trimethylolpropanes, tripropylene glycol, tetraethylene glycol, tetrapropylene glycol, tetramethylene glycol, 1 ,4- cyclohexane-dimethanol, ethanediol, diethylene glycol, 1 ,4-butanediol, 1 ,5- pentanediol, 1 ,6-hexanediol, or mixtures of at least two of these diols, especially mixtures of 1 ,4-butanediol, 1 ,5-pentanediol, and 1 ,6-hexanediol. Furthermore, polyester polyols of lactones, for example, ε-caprolactone or hydroxycarboxylic acids, for example, ω-hydroxycaproic acid, may also be used.
[0045] Polyether polyols that may be used include those which can be obtained by known methods, For example, polyether polyols can be produced by anionic polymerization with alkali hydroxides such as sodium hydroxide or potassium hydroxide or alkali alcoholates, such as sodium methylate, sodium ethylate, or potassium ethylate or potassium isopropylate as catalysts and with the addition of at least one initiator molecule containing 2 to 8, such as 3 to 8, reactive hydrogens or by cationic polymerization with Lewis acids such as antimony pentachloride, boron trifluoride etherate, etc., or bleaching earth as catalysts from one or more alkylene oxides with 2 to 4 carbons in the alkylene radical. Any suitable alkylene oxide may be used such as 1 ,3-propylene oxide, 1 ,2- and 2,3-butylene oxide, amylene oxides, styrene oxide, and preferably ethylene oxide and 1 ,2-propylene oxide and mixtures of these oxides. The polyalkylene polyether polyols may be prepared from other starting materials such as tetrahydrofuran and alkylene oxide-tetrahydrofuran mixtures; epihalohydrins such as epichlorohydrin; as well as aralkylene oxides such as styrene oxide. The polyalkylene polyether polyols may have either primary or secondary hydroxyl groups, preferably secondary hydroxyl groups from the addition of propylene oxide onto an initiator because these groups are slower to react. Included among the polyether polyols are polyoxyethylene glycol, polyoxypropylene glycol, polyoxybutylene glycol, polytetramethylene glycol, block copolymers, for example, combinations of polyoxypropylene and polyoxyethylene glycols, poly-1 ,2-oxybutylene and polyoxyethylene glycols, poly-1 ,4- tetramethylene and polyoxyethylene glycols, and copolymer glycols prepared from blends or sequential addition of two or more alkylene oxides. The polyalkylene polyether polyols may be prepared by any known process such as, for example, the process disclosed by Wurtz in 1859 and Encyclopedia of Chemical Technology, Vol. 7, pp. 257-262, published by Interscience Publishers, Inc. (1951) or in U.S. Pat. No. 1 ,922,459.
[0046] In one particular embodiment, the polyether polyol includes the alkylene oxide addition products of polyhydric alcohols such as ethylene glycol, propylene glycol, dipropylene glycol, trimethylene glycol, 1 ,2- butanediol, 1 ,5- pentanediol, 1 ,6-hexanediol, 1 ,7-heptanediol, hydroquinone, resorcinol glycerol, glycerine, 1 , 1 ,1-trimethylol-propane, 1 ,1 ,1-trimethylolethane, pentaerythritol, 1 ,2,6-hexanetriol, a-methyl glucoside, sucrose, and sorbitol. Also included within the term "polyhydric alcohol" are compounds derived from phenol such as 2,2- bis(4-hydroxyphenyl)-propane, commonly known as Bisphenol A. Also included may be a polyol which is initiated with a compound having at least two primary or secondary amine groups, a polyhydric alcohol having 4 or more hydroxyl groups, such as sucrose, or a mixture of initiators employing a polyhydric alcohol having at least 4 hydroxyl groups and compounds having at least two primary or secondary amine groups. Suitable organic amine initiators which may be condensed with alkylene oxides include aromatic amines-such as aniline, N- alkylphenylene-diamines, 2,4'-, 2,2'-, and 4,4'-methylenedianiline, 2,6- or 2,4- toluenediamine, vicinal toluenediamines, o-chloro-aniline, p-aminoaniline, 1 ,5- diaminonaphthalene, methylene dianiline, the various condensation products of aniline and formaldehyde, and the isomeric diaminotoluenes; and aliphatic amines such as mono-, di-, and trialkanolamines, ethylene diamine, propylene diamine, diethylenetriamine, methylamine, triisopropanolamine, 1 ,3- diaminopropane, 1 ,3-diaminobutane, and 1 ,4-diaminobutane. Preferable amines include monoethanolamine, vicinal toluenediamines, ethylenediamines, and propylenediamine.
[0047] Yet another class of polyether polyols contemplated for use in this disclosure are alkylene oxide adducts of a phenol/formaldehyde/alkanolamine resin, frequently called "Mannich" polyols such as disclosed in U.S. Pat. Nos. 4,883,826; 4,939,182; and 5, 120,815. [0048] The amount of polyol to be used relative to the isocyanate normally should be such that the isocyanate groups are present in at least an equivalent amount, and preferably, in slight excess, compared to the free hydroxyl groups. In some embodiments, the components will be proportioned so as to provide from about 0.9 to about 1.5 mole equivalents of isocyanate groups per mole equivalent of hydroxyl groups. However, for certain foams the mole equivalents of isocyanate to hydroxyl groups can be as low as 0.4.
[0049] Also included in the foam composition is a blowing agent, which may be selected based in part upon the desired density of the final foam. In certain non-limiting embodiments hydrocarbon blowing agents may be selected. For example, hydrocarbon or fluorine-containing hydrohalocarbon blowing agents may be used, and in some instances may serve to reduce, or further reduce, viscosity, and thereby enhance processability. Among these are, for example, butane, isobutane, 2,3-dimethylbutane, n- and i-pentane isomers, hexane isomers, heptane isomers, cycloalkanes including cyclopentane, cyclohexane, cycloheptane, and combinations thereof, HFC-245fa (1 ,1 ,1 ,3,3- pentafluoropropane), HFC-365mfc (1 ,1 ,1 ,3,3-penta-fluorobutane), HFC-227ea (1 ,1 ,1 ,2,3,3,3-heptafluoropropane), HFC-134a (1 ,1 ,1 ,2-tetrafluoroethane), combinations of two or more of the above, and the like. In one particular embodiment, the blowing agent is an unsaturated halogenated hydroolefin such as a hydrofluoroolefin (HFO), hydrochlorofluoroolefin (HCFO), or mixtures thereof. Preferred hydrofluoroolefin (HFO) blowing agents contain 3, 4, 5, or 6 carbons, and include but are not limited to pentafluoropropenes, such as 1 ,2,3,3,3-pentafluoropropene (HFO-1225ye); tetrafluoropropenes, such as 1 ,3,3,3-tetrafluoropropene (HFO-1234ze, E and Z isomers), 2,3,3,3- tetrafluoropropene (HFO-1234yf), and 1 ,2,3,3-tetrafluoropropene (HFO-1234ye); trifluoropropenes, such as 3,3,3-trifluoropropene (HFO-1243zf); tetrafluorobutenes, such as (HFO- 1345); pentafluorobutene isomers, such as (HFO-1354); hexafluorobutene isomers, such as (HFO-1336); heptafluorobutene isomers, such as (HFO-1327); heptafluoropentene isomers, such as (HFO-1447); octafluoropentene isomers, such as (HFO-1438); nonafluoropentene isomers, such as (HFO-1429); and hydrochlorofluoroolefins, such as 1-chloro-3,3,3- trifluoropropene (HCFO-1233zd) (E and Z isomers), 2-chloro-3,3,3- trifluoropropene (HCFO-1233xf), HCFO-1223, 1 ,2-dichloro-1 ,2-difluoroethene (E and Z isomers), 3,3-dichloro-3-fluoropropene, 2-chloro-1 , 1 , 1 , 4,4,4- hexafluorobutene-2 (E and Z isomers), and 2-chloro-1 , 1 ,1 , 3,4,4,4- heptafluorobutene-2 (E and Z isomers). These hydrocarbons and/or non- fluorine-containing hydrohalocarbons may be used in an amount of about 0.5 parts by weight to about 30 parts by weight, or about 1 part by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s).
[0050] Another blowing agent that may be used is formic acid or another carboxylic acid. The formic acid or other carboxylic acid may be used in an amount of from about 0.5 parts by weight to about 8 parts by weight, based on 100 parts by weight of polyol(s). It is also contemplated that other aliphatic mono- and polycarboxylic acids may be employed, such as those disclosed in U.S. Pat. No. 5,143,945, which is incorporated herein by reference in its entirety, and including isobutyric acid, ethylbutyric acid, ethylhexanoic acid, and combinations thereof.
[0051] In addition to, or in lieu of, the blowing agents above, water may also be optionally selected as a blowing agent. The water is, in some non-limiting embodiments, present in an amount of from about 0.1 parts by weight to about 40 parts by weight, or from about 0. 5 parts by weight to about 20 parts by weight, or from about 0.25 parts by weight to about 5 parts by weight, or from about 0.5 parts by weight to about 3 parts by weight, based on 100 parts by weight of polyol(s). In some embodiments, when preparing a polyurethane or polyisocyanurate foam, in order to facilitate and give desirable processing characteristics, the amount of water used may not exceed 3 parts by weight water, or not more than 2.5 parts by weight of water, or not more than 1 part by weight of water, based on 100 parts by weight of polyol(s). Omission of water may be desirable in some non-limiting embodiments.
[0052] In addition to the catalyst substantially free of nonylphenol, other catalysts may optionally be included in the foam composition. In one embodiment, the additional catalyst(s) are also substantially free of nonylphenol.
[0053] According to another embodiment, an amine catalyst may be included, including any organic compound which contains at least one tertiary nitrogen atom and is capable of catalyzing the hydroxyl/isocyanate reaction between the isocyanate and polyol. Typical classes of amines include the N- alkylmorpholines, N-alkyl-alkanolamines, Ν,Ν-dialkylcyclohexylamines, and alkylamines where the alkyl groups are methyl, ethyl, propyl, butyl and isomeric forms thereof, and heterocyclic amines. Typical but non-limiting thereof are triethylenediamine, tetramethylethylenediamine, bis(2-dimethylaminoethyl)ether, triethylamine, tripropylamine, tributylamine, triamylamine, pyridine, quinoline, dimethylpiperazine, piperazine, Ν,Ν-dimethylcyclohexylamine, N-ethyl- morpholine, 2-methylpropanediamine, methyltriethyl-enediamine, 2,4,6- tridimethylamino-methyl)phenol, N,N',N"-tris(dimethylamino-propyl)sym- hexahydrotriazine, and mixtures thereof. The tertiary amines from which selection may be made may include bis(2-dimethylamino-ethyl)ether, dimethylcyclohexylamine, Ν,Ν-dimethyl-ethanolamine, triethylenediamine, triethylamine, 2,4,6-tri(dimethylaminomethyl)phenol, Ν,Ν',Ν-ethylmorpholine, and mixtures thereof.
[0054] Non-amine catalyst may also be included in foam compositions of the present disclosure. Typical of such catalysts are organometallic compounds of bismuth, lead, tin, titanium, iron, antimony, uranium, cadmium, cobalt, thorium, aluminum, mercury, zinc, nickel, cerium, molybdenum, vanadium, copper, manganese, zirconium, and combinations thereof. Included for illustrative purposes only are bismuth nitrate, lead 2-ethylhexoate, lead benzoate, lead naphthenate, ferric chloride, antimony trichloride, antimony glycolate, combinations thereof, and the like. Embodiments include the stannous salts of carboxylic acids, such as stannous acetate, stannous octoate, stannous 2- ethylhexoate, 1-methylimidazole, and stannous laurate, as well as the dialkyl tin salts of carboxylic acids, such as dibutyl tin diacetate, dibutyl tin dilaurate, dibutyl tin dimaleate, dioctyl tin diacetate, combinations thereof and the like.
[0055] The amount of catalyst substantially free of nonylphenol (and optional catalyst(s)) added to the foam composition is a catalytically sufficient amount. In one embodiment, the amount of catalyst substantially free of nonylphenol (and optional catalyst(s)) that is included in the foam composition is from about 0.5 parts by weight to about 15 parts by weight, in another embodiment from about 0.75 part by weight to about 12 parts by weight, and in still another embodiment from about 1 part by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s).
[0056] If desired, the foam composition can also comprise additives. Examples include: cell stabilizers, such as organopolysiloxane surfactants; flame retardants such as halogenated organophosphorous compounds; chain extenders such as ethylene glycol and butane diol; crosslinkers such as glycerol, trimethylolpropane, pentaerythritol, sucrose, sorbitol, or mixtures thereof; fillers and pigments, such as calcium carbonate, titanium dioxide, iron oxide, chromium oxide, azo/diazo dyes, phthalocyanines, dioxazines, carbon black barium sulfate, graphite, microspheres, alumina trihydrate, wollastonite, prepared glass fibers (dropped or continuous), and polyester fibers and other polymeric fibers, as well as various combinations thereof; odor masks, biocides, antioxidants, UV stabilizers such as hydroxybenzotriazoles, zinc dibutyl thiocarbamate, 2,6- ditertiarybutyl catechol, hydroxybenzophenones, hindered amines and phosphites; antistatic agents; viscosity modifiers and combinations thereof. [0057] Each additive, except fillers and pigments, may constitute from 0.01 parts by weight to about 10 parts by weight, based on 100 parts by weight of polyol(s). Fillers and pigments may be used in quantities as high as up to about 50 parts by weight, based on 100 parts by weight of polyol(s).
[0058] The preparation of polyurethane or polyisocyanurate foams using the foam compositions described herein may follow any of the methods well known in the art for preparing polyurethane and polyisocyanurate foam, for example, as described in Saunders and Frisch, "Volumes I and II Polyurethanes Chemistry and Technology" (1962, John Wiley and Sons, New York, N.Y.), or Gum et al., "Reaction Polymers" (1992, Oxford University Press, New York, N.Y.), or Klempner and Sendijarevic, "Polymeric Foams and Foam Technology" (2004, Hanser Gardner Publications, Cincinnati, Ohio). In general, the various components are brought together and mixed using manual or mechanical mixing means to form the foam. Generally, the polyol and catalyst are preblended to form a single component which is fed as one stream to a conventional mixing head and admixed with the isocyanate which is fed as a separate stream to the mixing head. The blowing agent can be fed as a separate stream to the mixing head or blended with one or other, or both, of the other components prior to feeding the latter to the mixing head. The foams subsequently produced can be rigid, flexible, or semi-rigid, and can have a closed cell structure, an open cell structure or a mixture of open and closed cells and may vary in density of from about 0.5 pounds per cubic foot to about 60 pounds per cubic foot, such as from about 1.0 to 20.0 pounds per cubic foot, and in other embodiments from about 1.5 to 6.0 pounds per cubic foot. The foams are suitable for use in a wide range of applications including appliance insulation (e.g., insulating refrigerators or water heaters), structural insulation (e.g. spray foams or lamination foams for commercial or residential insulation), cushioning, flotation, packaging, adhesives, void filling, crafts and decorative, and shock absorption. [0059] In one particular embodiment, the polyurethane or polyisocyan urate foam prepared according to the process of this disclosure is a rigid, closed-cell foam. Such foam is typically prepared by intimately mixing the reaction components, for example, a B-side containing a polyol/blowing agent/catalyst according to the present disclosure and an A-side containing an isocyanate (i.e., two streams); or a B-side containing a polyol/blowing agent, a C-side containing the catalyst according to the present disclosure, and an A-side containing a polyisocyanate component (at least three streams, wherein the polyol/blowing agent and catalyst according to the present disclosure mix just prior to contact thereof with the polyisocyanate component) at room temperature or at a slightly elevated temperature for a short period of time. Mixing of streams may be carried out either in a spray apparatus, a mixhead with or without a static mixer, or a vessel. The mixture is then sprayed or otherwise deposited onto a substrate. This substrate may be, for example, a rigid or flexible facing sheet made of foil or another material, including another layer of similar or dissimilar polyurethane or polyisocyanurate which is being conveyed, continuously or discontinuously, along a production line, or directly onto a conveyor belt.
[0060] In alternative embodiments the mixture may be poured into an open mold or distributed via laydown equipment into an open mold or simply deposited at or into a location for which it is destined, i.e., a pour-in-place application, such as between the interior and exterior walls of a structure. In the case of deposition on a facing sheet, a second sheet may be applied on top of the deposited mixture. In other embodiments, the mixture may be injected into a closed mold, with or without vacuum assistance for cavity-filling. If a mold is employed, it is most typically heated.
[0061] In general, such applications above may be accomplished using the known one-shot, prepolymer or semi-prepolymer techniques used together with conventional mixing methods. The mixture, on reacting, takes the shape of the mold or adheres to the substrate to produce a polyurethane or polyisocyanurate foam of a more-or-less predefined structure, which is then allowed to cure in place or in the mold, either partially or fully. Suitable conditions for promoting the curing include a temperature of typically from 20°C to 50°C, such as from 35°C to 75°C, and including from 45°C to 55°C. Such temperatures will usually permit the sufficiently cured foam to be removed from the mold, where such is used, typically within from about 1 to 10 minutes and more typically within from 1 to 5 minutes after mixing of the reactants. Optimum cure conditions will depend upon the particular components, including catalysts and quantities used in preparing the foam and also the size and shape of the article manufactured.
[0062] The result may be a rigid foam in the form of slabstock, a molding, a filled cavity, including but not limited to a pipe or insulated wall or hull structure, a sprayed foam, a frothed foam, or a continuously- or discontinuously- manufactured laminate product, including but not limited to a laminate or laminated product formed with other materials, such as hardboard, plasterboard, plastics, paper, metal, or a combination thereof.
EXAMPLES
[0063] Example 1. Preparation of Catalyst Substantially Free of Nonylphenol.
Pyrrole was dissolved in diethylene glycol and then reacted with sodium sarcosine and formaldehyde in the amounts shown below at 80°C to form a Mannich condensation product. Excess water was then stripped at 80°C and 40 mmHg reduced pressure. The resulting slightly viscous and amber to brown liquid was confirmed by C13 NMR to be the Mannich condensate sodium 2- aminoacetomethylpyrrole. Net 417.1 grams.
Diethylene Glycol 220.8 grams
Pyrrole 67.1 grams
Sodium Sarcosine (40% water) 305.5 grams Formaldehyde (55%) 57.3 grams
[0064] Example 2. Preparation of Catalyst Substantially Free of Nonylphenol.
Methylpyrrole was dissolved in diethylene glycol and then reacted with sodium sarcosine and formaldehyde in the amounts shown below at 80°C to form a Mannich condensation product, Excess water was then stripped at 80°C and 40 mmHg reduced pressure. The resulting product was a thick pasty brown semi-solid and was confirmed by C 3 NMR to be a mixture of Mannich condensates: sodium 2-aminoacetomethylpyrrole and disodium bis-2-6-(2- aminoacetomethylpyrrole).
Diethylene Glycol 220.8 grams
Methylpyrrole 81 .1 grams
Sodium Sarcosine (40% water) 416.6 grams
Formaldehyde (55%) 76.4 grams
[0065] Example 3. Preparation of Catalyst Substantially Free of Nonylphenol.
Methylpyrrole was dissolved in diethylene glycol and then reacted with sodium sarcosine and formaldehyde in the amounts shown below at 80°C to form a Mannich condensation product. Excess water was then stripped at 80°C and 40 mmHg reduced pressure. The resulting product was a slightly viscous pourable liquid and was confirmed by C13 NMR to be a Mannich condensate having a mono functional sarcosine substitution on the pyrrole ring.
Diethylene Glycol 352.3 grams
Methylpyrrole 81 .1 grams
Sodium Sarcosine (40% water) 305.5 grams Formaldehyde (55%) [0066] Example 4. Foam Preparation.
Foams were prepared from the following components
A-Side
Figure imgf000025_0001
1 JEFFOL®SD-361 polyol, a sucrose diethylene glycol initiated PO polyol adduct.
2 JEFFOL®FX31 -240 polyol, a glycerol initiated PO polyol adduct.
3 Hydrofluorocarbon 141 b.
4 Tegostab® B 8404 silicone surfactant.
5 JEFFCAT® TR-52 catalyst, a Mannich condensate prepared from nonylphenol.
6 Example 1 catalyst substantially free of nonylphenol. The catalyst was added to the B-side and mixed for 10 seconds. The A-side and B-side were then mixed together for 10 seconds to produce foams having the following properties:
Figure imgf000026_0001
[0067] Example 5. Foam Preparation.
Foams were prepared from the following components:
A-Side
Figure imgf000026_0002
State of the art 6.0 g
Catalyst5
Inventive Catalyst" 6.0 g 4.0 g
1 JEFFOL®SD-361 polyol, a sucrose diethylene glycol initiated PO polyol adduct.
2 JEFFOL®FX31 -240 polyol, a glycerol initiated PO polyol adduct.
3 Hydrofluorocarbon 141 b.
4 Tegostab® B 8404 silicone surfactant.
5 JEFFCAT® TR-52 catalyst, a Mannich condensate prepared from nonylphenol.
6 Example 3 catalyst substantially free of nonylphenol.
The catalyst was added to the B-side and mixed for 10 seconds. The A-side and B-side were then mixed together for 10 seconds to produce foams having the following properties:
Figure imgf000027_0001
[0068] As shown above, the inventive catalysts substantially free of nonylphenol are surprisingly more active (approx. 50%) than the state of the art catalysts prepared from nonylphenol. Also surprising was that less inventive catalyst was required to provide the same catalytic activity as the state of the art catalyst.
[0069] Example 6. Rigid spray foam made with inventive catalysts using low global warming blowing agents with good heat aged stability were prepared from the following components:
Figure imgf000028_0001
1 Terol 250 polyol, an aromatic polyester polyol.
2 JEFFOL®R425-X polyol, an aromatic amino polyether polyol.
3 JEFFOL®SG-522 polyol, a sucrose glycerin polyether polyol. 4 Tegostab® EP-69-A silicone surfactant.
5 SURFONIC®N-95 emulsifier, a nonylphenol ethoxylate emulsifier.
6 TCPP is trichloropropylphosphate.
7 PHDT-4 diol is tetrabromophthalicanhydride.
8 JEFFCAT®DMDEE catalyst, a dimorpholinodiethylether.
9 Dabco® Dc-120 catalyst, a 1 ,2-dimethylimidazole.
10 Example 1 catalyst substantially free of nonylphenol.
11 Example 2 catalyst substantially free of nonylphenol.
12 Example 3 catalyst substantially free of nonylphenol.
13 Solstice® HF01233zd(E) blowing agent.
52.5% by weight of the A-side and 47.5% by weight of the B-side were mixed together for 3 seconds to produce foams having the following properties:
Figure imgf000029_0001
[0070] Example 7.
Metal panel formulations using inventive catalyst Example 1 were prepared and foams exhibiting improved firm times were produced. A firm time is the measure of cure - it is the time that a foam no longer yields when a constant force is applied to the surface of the foam. The following components were used in this example:
Figure imgf000029_0002
Rubinate® M polyisocyanate.
Figure imgf000030_0001
I JEFFOL®SG360 polyol.
2 JEFFOL®G30-240 polyol.
3 Terol 250 polyol.
TCPP1 is trichloropropylphosphate.
5 PHT4-diol2 is tetrabromophthalicanhydride.
6 TEGOSTAB®B8490 surfactant.
7 JEFFCAT®TR-90 catalyst.
8 JEFFCAT®ZF-20 catalyst.
9 JEFFCAT®Z-1 10 catalyst.
10 Cyclopentane.
I I Example 1 catalyst substantially free of nonylphenol. 54.4% of the A-side and 45.6% of the B-side were mixed together for 8 seconds to produce foams having the following properties:
Figure imgf000031_0001
[0071] While the foregoing is directed to embodiments of the present disclosure, other and further embodiments of the disclosure may be devised without departing from the basic scope thereof, and the scope thereof is determined by the claims that follow.

Claims

Claims:
1. A catalyst comprising a Mannich condensation product of: (i) a heterocyclic compound containing at least one -N(H)- group in the ring; (ii) an aldehyde; and (iii) a metal salt of an aminocarboxylic acid and wherein the catalyst is substantially free of nonylphenol.
2. The catalyst according to claim 1 , wherein the heterocyclic compound containing at least one -N(H)- group in the ring is a 5- or 6-membered ring with one nitrogen hetero-atom or two or three adjacent nitrogen hetero-atoms, in which two adjacent carbon atoms of the heterocyclic ring may form part of a further 6-aromatic, heterocyclic or alicyclic ring system.
3. The catalyst according to claim 2, wherein at least one carbon atom on the, 5- or 6-membered ring is substituted with an alkyl group, an alkaryl group, an aryl group, an aralkyl group or an alkenyl group.
4. The catalyst according to claim 2, wherein the heterocyclic compound containing at least one -N(H)- group in the ring is triazole, benzotriazole, 5-methyl benzotriazole, 5-ethyl benzotriazole, 5-butyl benzotriazole, 5-propyl benzotriazole, 5- dodecyl benzotriazole, 2-methyl benzotriazole, 2-ethyl benzotriazole, 2-butyl benzotriazole, 2-propyl benzotriazole, 2-dodecyl benzotriazole, 5,7-dimethyI benzotriazole, 5,7-diethyl benzotriazole, 5,7-dibutyl benzotriazole, 5,7-dipropyl benzotriazole, 5,7-didodecyl benzotriazole, naphthotriazole, 5-methyl naphthotriazole, 5-ethyl naphthotriazole, 5-butyl naphthotriazole, 5-propyl naphthotriazole, 5-dodecyl naphthotriazole, imidazole, 4-methyl imidazole, 4-ethyl imidazole, 4-butyl imidazole, 4-propyl imidazole, 4-dodecyl imidazole, 5-methyl imidazole, 5-ethyl imidazole, 5-butyl imidazole, 5-propyl imidazole, 5-dodecyl imidazole, benzimidazole, 5-methyl benzimidazole, 5-ethyl benzimidazole, 5-butyl benzimidazole, 5-propyl benzimidazole, 5-dodecyl benzimidazole, 2-methyl benzimidazole, 2-ethyl benzimidazole, 2-butyl benzimidazole, 2-propyl benzimidazole, 2-dodecyl benzimidazole, 5,7-dimethyl benzimidazole, 5,7-diethyl benzimidazole, 5,7-dibutyl benzimidazole, 5,7-dipropyl benzimidazole, 5,7-didodecyl benzimidazole, pyrrole, 2-methyl pyrrole, 2-ethyl pyrrole, 2-butyl pyrrole, 2-propyl pyrrole, 2-dodecyl pyrrole 3-methyl pyrrole, 3-ethyl pyrrole, 3-butyl pyrrole, 3-propyl pyrrole, 3-dodecyl pyrrole, 5-methyl benzpyrrole, pyrazole, 5-methyl benzpyrazole,
5- ethyl benzpyrazole, 5-butyl benzpyrazole, 5-propyl benzpyrazole, 5-dodecyl benzpyrazole, 7-methyl benzpyrazole, 6-ethyl benzpyrazole, 7-butyl benzpyrazole,
6- propyl benzpyrazole, 7-dodecyl benzpyrazole, 5,7-dimethyl benzpyrazole, 5,7- diethyl benzpyrazole, 5,7-dibutyl benzpyrazole, 5,7-dipropyl benzpyrazole, 5,7- didodecyl benzpyrazole, 2-pyrroline, 3-pyrroline, 3-pyrazoline, carbazole, 5-methyl carbazole, indole, 3-methyl indole, 3-ethyl indole, 3-butyl indole, 3-propyl indole, 3- dodecyl indole, 4-methyl indole, 4-ethyl indole, 4-butyl indole, 4-propyl indole, 4- dodecyl indole, purine, phenothiazine, phenoxazine or perimidine.
5. The catalyst according to claim 1 , wherein the heterocyclic compound containing at least one -N(H)- group is selected from pyrrole, 2-methyl pyrrole and 3-methyl pyrrole.
6. The catalyst according to claim 1 , wherein the aldehyde is formaldehyde.
7. The catalyst according to claim 1 , wherein the metal salt of an aminocarboxylic acid is a compound of the formula
Figure imgf000033_0001
R. I!
where Ri , R2, and R3 are, independently of one another, H or a C1-C3 alkyl group, M is sodium or potassium and x is an integer from 0 to 5.
8. The catalyst according to claim 7, wherein x is 0.
9. A polyurethane or polyisocyanurate foam composition comprising a polyisocyanate, a polyol, a blowing agent and the catalyst according to claim 1.
10. The polyurethane or polyisocyanurate foam composition according to claim 9, further comprising an additional catalyst wherein the additional catalyst is substantially free of nonylphenol.
1 1. The polyurethane or polyisocyanurate foam composition according to claim 9, further comprising at least one cell stabilizer, flame retardant, chain extender, crosslinker, filler, pigment, odor mask, biocide, antioxidant, UV stabilizer, antistatic agent or viscosity modifier.
12. A process for preparing a polyurethane or polyisocyanurate foam comprising contacting a polyisocyanate, polyol, blowing agent and the catalyst according to claim 1.
13. A foam obtained from the process of claim 12.
14. The foam according to claim 13, wherein the foam is a rigid foam in the form of slabstock, a molding, a filled cavity, a sprayed foam, a frothed foam, or a continuously- or discontinuously-manufactured laminate product.
15. A process for preparing a catalyst substantially free of nonylphenol comprising the step of reacting a heterocyclic compound containing at least one -N(H)- group in the ring with an aldehyde and a metal salt of an aminocarboxylic acid at a temperature from 0°C to 80°C.
PCT/US2016/066446 2016-03-17 2016-12-14 Polyisocyanurate catalysts for metal panels and spray foams WO2017160361A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201662309555P 2016-03-17 2016-03-17
US62/309,555 2016-03-17

Publications (1)

Publication Number Publication Date
WO2017160361A1 true WO2017160361A1 (en) 2017-09-21

Family

ID=59851727

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2016/066446 WO2017160361A1 (en) 2016-03-17 2016-12-14 Polyisocyanurate catalysts for metal panels and spray foams

Country Status (1)

Country Link
WO (1) WO2017160361A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109135530A (en) * 2018-07-03 2019-01-04 南京理工大学 DAPBI modified aqueous polyurethane coating and preparation method thereof
EP3805285A1 (en) * 2019-10-08 2021-04-14 Evonik Operations GmbH Preparation of polyurethane rigid foam
CN112805312A (en) * 2018-08-21 2021-05-14 亨茨曼国际有限公司 Catalyst for PIR/PUR foam production
WO2022098940A1 (en) * 2020-11-06 2022-05-12 Huntsman Petrochemical Llc Method for producing secondary and tertiary amines

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2950262A (en) * 1955-08-03 1960-08-23 Pittsburgh Plate Glass Co Preparation of foamed polyurethane using salt of mannich base as catalyst
US3297597A (en) * 1963-06-17 1967-01-10 Jefferson Chem Co Inc Production of rigid polyurethane foam
US3998766A (en) * 1974-12-26 1976-12-21 Basf Wyandotte Corporation Urethane modified carbodimide-isocyanurate foams from organic polyisocyanates and oxyalkylated mannich polyols
US4086213A (en) * 1976-08-26 1978-04-25 Air Products And Chemicals, Inc. Tertiary amino acid and tertiary amino acid-nitrile delayed action catalyst compositions
US4487852A (en) * 1983-10-25 1984-12-11 Texaco Inc. Modified Mannich condensates and manufacture of rigid polyurethane foam with alkoxylation products thereof
US4654376A (en) * 1985-10-24 1987-03-31 Texaco Inc. Polyurethane foams based on amino polyols
US6495722B1 (en) * 2001-09-17 2002-12-17 Huntsman Petrochemical Corporation Mannich polyols for rigid spray foams
WO2015110404A1 (en) * 2014-01-22 2015-07-30 Huntsman International Llc Process for making rigid polyurethane or urethane-modified polyisocyanurate foams

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2950262A (en) * 1955-08-03 1960-08-23 Pittsburgh Plate Glass Co Preparation of foamed polyurethane using salt of mannich base as catalyst
US3297597A (en) * 1963-06-17 1967-01-10 Jefferson Chem Co Inc Production of rigid polyurethane foam
US3998766A (en) * 1974-12-26 1976-12-21 Basf Wyandotte Corporation Urethane modified carbodimide-isocyanurate foams from organic polyisocyanates and oxyalkylated mannich polyols
US4086213A (en) * 1976-08-26 1978-04-25 Air Products And Chemicals, Inc. Tertiary amino acid and tertiary amino acid-nitrile delayed action catalyst compositions
US4487852A (en) * 1983-10-25 1984-12-11 Texaco Inc. Modified Mannich condensates and manufacture of rigid polyurethane foam with alkoxylation products thereof
US4654376A (en) * 1985-10-24 1987-03-31 Texaco Inc. Polyurethane foams based on amino polyols
US6495722B1 (en) * 2001-09-17 2002-12-17 Huntsman Petrochemical Corporation Mannich polyols for rigid spray foams
WO2015110404A1 (en) * 2014-01-22 2015-07-30 Huntsman International Llc Process for making rigid polyurethane or urethane-modified polyisocyanurate foams

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109135530A (en) * 2018-07-03 2019-01-04 南京理工大学 DAPBI modified aqueous polyurethane coating and preparation method thereof
CN109135530B (en) * 2018-07-03 2020-06-19 南京理工大学 DAPBI modified waterborne polyurethane coating and preparation method thereof
CN112805312A (en) * 2018-08-21 2021-05-14 亨茨曼国际有限公司 Catalyst for PIR/PUR foam production
CN112805312B (en) * 2018-08-21 2023-03-21 亨茨曼国际有限公司 Catalyst for PIR/PUR foam production
EP3805285A1 (en) * 2019-10-08 2021-04-14 Evonik Operations GmbH Preparation of polyurethane rigid foam
WO2021069164A1 (en) * 2019-10-08 2021-04-15 Evonik Operations Gmbh Production of rigid polyurethane foam
CN114555669A (en) * 2019-10-08 2022-05-27 赢创运营有限公司 Production of rigid polyurethane foams
WO2022098940A1 (en) * 2020-11-06 2022-05-12 Huntsman Petrochemical Llc Method for producing secondary and tertiary amines

Similar Documents

Publication Publication Date Title
US9987775B2 (en) Production of polyisocyanurate foam panels
WO2017160362A1 (en) Metal salts of aminio acid triazines as polyurethane and polyisocyanurate catalysts
EP3097132B1 (en) Process for making rigid polyurethane or urethane-modified polyisocyanurate foams
KR101238100B1 (en) Method for producing rigid polyurethane foams
EP3280751B1 (en) Polyol premix composition for rigid polyurethane foams
EP2652000B1 (en) Polyurethane and polyisocyanurate foams
KR101475959B1 (en) Method for the production of rigid polyurethane foams
WO2017160361A1 (en) Polyisocyanurate catalysts for metal panels and spray foams
US6534556B2 (en) Sprayable autofrothing polyisocyanate foam and delivery system
KR102338624B1 (en) Method for producing polyurethane rigid foams and polyisocyanurate rigid foams
US20060135634A1 (en) Low amine emission polyurethane foam
SG192583A1 (en) Polyester polyols based on aromatic dicarboxylic acids and rigid polyurethane foams produced therefrom
GB2365436A (en) Polyol composition containing a hydrocarbon blowing agent
US6013690A (en) Low density rigid polyurethane foams having improved substrate adhension characteristics
US20190389996A1 (en) Hfo containing pu formulation
US20110237770A1 (en) Viscosity reducing agents for polyether polyols
US20230183444A1 (en) A process for recycling a polyurethane material
EP3458491A1 (en) Process for preparing polyisocyanurate rigid foams
CN112805312A (en) Catalyst for PIR/PUR foam production
CN111630080B (en) Polyisocyanurate comprising foam with long cream time and fast curing behaviour
AU2021295848A1 (en) Polyisocyanurate resin foam having high compressive strength, low thermal conductivity, and high surface quality
CN114555669A (en) Production of rigid polyurethane foams
RU2575124C2 (en) Polyurethane and polyisocyanurate foam plastics
MXPA98005176A (en) Low density rigid polyurethane foams that have accession characteristics to the substratometer
MXPA98004862A (en) Compositions of polymeric mdi to be used in thermoformab foams

Legal Events

Date Code Title Description
NENP Non-entry into the national phase

Ref country code: DE

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

Ref document number: 16894790

Country of ref document: EP

Kind code of ref document: A1

122 Ep: pct application non-entry in european phase

Ref document number: 16894790

Country of ref document: EP

Kind code of ref document: A1