US20050090386A1 - Catalyst blends for producing low thermal desorption polyurethane foams - Google Patents
Catalyst blends for producing low thermal desorption polyurethane foams Download PDFInfo
- Publication number
- US20050090386A1 US20050090386A1 US10/998,791 US99879104A US2005090386A1 US 20050090386 A1 US20050090386 A1 US 20050090386A1 US 99879104 A US99879104 A US 99879104A US 2005090386 A1 US2005090386 A1 US 2005090386A1
- Authority
- US
- United States
- Prior art keywords
- catalyst
- gelling
- group
- blowing
- catalyst composition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 0 [4*]*([5*])CC Chemical compound [4*]*([5*])CC 0.000 description 40
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
- C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
- C08G18/1825—Catalysts containing secondary or tertiary amines or salts thereof having hydroxy or primary amino groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
- C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
- C08G18/1808—Catalysts containing secondary or tertiary amines or salts thereof having alkylene polyamine groups
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
- C08G18/4072—Mixtures of compounds of group C08G18/63 with other macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/48—Polyethers
- C08G18/4866—Polyethers having a low unsaturation value
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6666—Compounds of group C08G18/48 or C08G18/52
- C08G18/667—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/6681—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38
- C08G18/6688—Compounds of group C08G18/48 or C08G18/52 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/32 or C08G18/3271 and/or polyamines of C08G18/38 with compounds of group C08G18/3271
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
- C08G18/7614—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring
- C08G18/7621—Polyisocyanates or polyisothiocyanates cyclic aromatic containing only one aromatic ring being toluene diisocyanate including isomer mixtures
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/72—Polyisocyanates or polyisothiocyanates
- C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
- C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
- C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
- C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
- C08G18/7671—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/08—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2110/00—Foam properties
- C08G2110/0008—Foam properties flexible
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2110/00—Foam properties
- C08G2110/0041—Foam properties having specified density
- C08G2110/005—< 50kg/m3
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2110/00—Foam properties
- C08G2110/0083—Foam properties prepared using water as the sole blowing agent
Definitions
- the present invention relates to compositions and processes for making polyurethane foams. More particularly, it relates to compositions and processes incorporating tertiary amine catalysts capable of providing foams having reduced levels of odor and volatile emissions.
- Polyurethane foams are widely known and used in automotive, housing and other industries. Such foams are produced by reaction of a polyisocyanate with a polyol in the presence of a catalyst and a blowing agent, historically a chlorofluorocarbon (CFC) compound. Due to environmental concerns relating to CFC's, the use of water blown foam formulations, in which at least some of the blowing is performed with CO 2 generated by the reaction of water with the polyisocyanate, has become increasingly important. Such systems typically employ tertiary amine catalysts to accelerate both the blowing (reaction of water with isocyanate to generate CO 2 ) and gelling (reaction of polyol with isocyanate) reactions required to make a foam. However, known tertiary amine catalyst compositions may give rise to objectionable releases of volatile and often malodorous materials into the air during foam manufacture and/or thereafter. The present invention addresses the issue of how to reduce such emissions, using certain catalyst compositions.
- CFC chlorofluorocarbon
- the invention is a catalyst composition comprising:
- A represents CH or N
- R 1 represents hydrogen or the group
- n an integer between 1 and 3, inclusive
- R 2 and R 3 each represent hydrogen or a C1-C6 alkyl group
- R 6 represents H or 3-aminopropyl, provided that:
- R 4 and R 5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group and
- R 4 and R 5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group and
- R 7 , R 8 , and R 9 each independently represents a C1-C4 alkyl group
- R 10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
- n, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH 2 , —NH—CO—NH 2 , or
- the invention is a formulation for producing a polyurethane foam, the formulation comprising a polyol, a polyisocyanate, water, and a catalyst composition comprising:
- A represents CH or N
- R 1 represents hydrogen or the group
- n an integer between 1 and 3, inclusive
- R 2 and R 3 each represent hydrogen or a C1-C6 alkyl group
- R 6 represents H or 3-aminopropyl, provided that:
- R 4 and R 5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group and
- R 4 and R 5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group and
- R 7 , R 8 , and R 9 each independently represents a C1-C4 alkyl group
- R 10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
- n, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH 2 , —NH—CO—NH 2 , or
- the invention is a polyurethane foam comprising a product of a reaction between a polyol and a polyisocyanate, the reaction taking place in the presence of water and a catalyst composition comprising:
- A represents CH or N
- R 1 represents hydrogen or the group
- n an integer between 1 and 3, inclusive
- R 2 and R 3 each represent hydrogen or a C1-C6 alkyl group
- R 6 represents H or 3-aminopropyl, provided that:
- R 4 and R 5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group and
- R 4 and R 5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group
- R 7 , R 8 , and R 9 each independently represents a C1-C4 alkyl group
- R 10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
- n, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH 2 , —NH—CO—NH 2 , or
- the invention is a method of making a polyurethane foam, the method comprising mixing together a polyol, a polyisocyanate, water, and a catalyst composition comprising:
- A represents CH or N
- R 1 represents hydrogen or the group
- n an integer between 1 and 3, inclusive
- R 2 and R 3 each represent hydrogen or a C1-C6 alkyl group
- R 6 represents H or 3-aminopropyl, provided that:
- R 4 and R 5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group and
- R 4 and R 5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group
- R 7 , R 8 , and R 9 each independently represents a C1-C4 alkyl group
- R 10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
- n, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH 2 , —NH—CO—NH 2 , or
- Catalyst compositions according to the invention comprise a gelling catalyst and a blowing catalyst, both of which comprise tertiary amine groups.
- the gelling catalyst additionally comprises a primary or secondary amine group.
- the blowing catalyst additionally comprises one or more of a primary or secondary amine group, a hydroxyl group, and a urea group.
- the present invention provides catalyst compositions for making polyurethane foams, and methods for using these compositions.
- the catalyst compositions comprise mixtures of gelling catalysts selected from tertiary aminoalkyl substituted primary or secondary amines; and blowing catalysts selected from bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties.
- the catalyst compositions produce polyurethane foams that have low amine odor and low catalyst-derived emissions, as measured by thermal desorption testing techniques.
- the present invention provides catalyst compositions suitable for catalyzing the reaction between an isocyanate functionality and an active hydrogen-containing compound, i.e. an alcohol, a polyol, an amine or water.
- the catalyst compositions catalyze the urethane (gelling) reaction of polyol hydroxyl groups with isocyanate to make polyurethanes, and the blowing reaction of water with isocyanate to release carbon dioxide for making foamed polyurethanes.
- urethane (gelling) reaction of polyol hydroxyl groups with isocyanate to make polyurethanes
- the blowing reaction of water with isocyanate to release carbon dioxide for making foamed polyurethanes.
- polyurethane is intended to mean polyurethane and/or polyisocyanurate, as is understood in the art.
- a polyurethane foam can be a polyurethane and/or polyisocyanurate foam.
- formation of the foam is aided by incorporation in the reaction mixture of a suitable blowing agent, as is known in the art.
- a surfactant such as a silicone surfactant, is also included to help regulate foam formation, as is also known in the art.
- Polyurethane products made in accordance with the invention may be prepared using any suitable organic polyisocyanates well known in the art for making polyurethane foam including, for example, hexamethylene diisocyanates, isophorone diisocyanates, phenylene diisocyanates, toluene diisocyanates (TDI) and 4,4′-diphenylmethane diisocyanates (MDI).
- suitable organic polyisocyanates well known in the art for making polyurethane foam
- TDI phenylene diisocyanates
- MDI 4,4′-diphenylmethane diisocyanates
- mixtures of diisocyanates known commercially as “crude MDI”, marketed as PAPI by Dow Chemical, which contain about 60% of 4,4′-diphenylmethane diisocyanates along with other isomeric and analogous higher polyisocyanates.
- isocyanates are the 2,4- and 2,6-TDI's individually or together as their commercially available mixtures. Also suitable are “prepolymers” of these polyisocyanates comprising a partially pre-reacted mixture of a polyisocyanate and a polyether or polyester polyol. Typically, the above polyisocyanates are used in an amount relative to the polyol to establish an isocyanate index in the range of 80 to 400.
- Suitable polyols for making polyurethane foams in conjunction with the catalyst compositions of the invention are those typically used in the art, including for example polyalkylene ether and polyester polyols.
- Polyalkylene ether polyols include poly(ethylene oxide) and poly(propylene oxide) polymers and copolymers with terminal hydroxyl groups derived from polyhydric compounds, for example diols and/or triols.
- Such diols and triols include, as non-limiting examples, ethylene glycol, propylene glycol, 1,3-butanediol, 1,4-butanediol, 1,6-hexanediol, neopentyl glycol, diethylene glycol, dipropylene glycol, pentaerythritol, glycerol, diglycerol, trimethylol propane, sugars such as sucrose, and other low molecular weight polyols.
- amine polyether polyols which can be prepared by reacting an amine, such as ethylenediamine, diethylenetriamine, tolylenediamine, diphenylmethanediamine, triethanolamine or the like, with ethylene oxide or propylene oxide.
- a single high molecular weight polyether polyol such as described above may be used.
- mixtures of such high molecular weight polyether polyols for example mixtures of different multifunctional materials and/or of compounds having different molecular weights or different chemical compositions, may be used.
- Useful polyester polyols include those produced by reacting a dicarboxylic acid with an excess of a diol, for example, adipic acid or phthalic acid anhydride with ethylene glycol or butanediol, or reacting a lactone such as caprolactone with an excess of a diol such as propylene glycol.
- the polyol component of the polyurethane formulation frequently comprises a polymer polyol.
- a polymer polyol Such polymer polyols my be used in polyurethane foams to increase the foam's resistance to deformation, i.e. to increase the load-bearing properties of the foam.
- One type of polymer polyol referred to in the art as a graft polyol, consists of a triol in which vinyl monomers are graft copolymerized. Styrene and acrylonitrile are the usual monomers of choice.
- a second type, a polyurea modified polyol is a polyol containing a polyurea dispersion formed by the reaction of a diamine and TDI.
- the TDI is typically used in excess, and therefore some of the TDI may react with both the polyol and polyurea.
- the second type of polymer polyol may for example be a material called a PIPA polyol, which is formed by the in-situ polymerization of TDI and alkanolamine in the polyol.
- polymer polyols may comprise 20-80% of the polyol portion of the polyurethane formulation. If polymer polyols constitute a part of the overall polyol charge, their weight is included in the total polyol weight for purposes of calculating the relative amounts of other ingredients according to the pphp (parts per hundred parts polyol) convention.
- Blowing agents used according to the invention for making polyurethane foams are any commonly used blowing agents known in the art. These include, as nonlimiting examples, HCFC (hydrochlorofluorocarbon) compounds, HFC (hydrofluorocarbon) compounds, chlorofluorocarbons, pentanes, and mixtures of these.
- the formulations contain water, typically at between 0.1 and 7 pphp (parts per hundred parts of polyol), more typically between 2.5 and 4.5 pphp, to produce CO 2 to help create a foam.
- Catalyst compositions according to the invention comprise mixtures of: 1) gelling catalysts selected from tertiary aminoalkyl substituted primary or secondary amines, and 2) blowing catalysts selected from bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties. It is important that a combination of gelling and blowing catalyst according to the invention be used, rather than either one alone or in combination with a catalyst not of this invention, in order to obtain the low odor and low volatiles emission provided by the invention. Detailed descriptions of the gelling and blowing catalysts follow.
- Gelling catalysts suitable for use according to the invention are represented by the general formula: in which:
- A represents CH or N
- R 1 represents hydrogen or the group
- n an integer between 1 and 3, inclusive
- R 2 and R 3 each represent hydrogen or a C1-C6 alkyl group
- R 6 represents H or 3-aminopropyl, provided that:
- R 4 and R 5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group and
- R 4 and R 5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group
- R 4 and R 5 are each a methyl group, A is nitrogen, and R 2 and R 3 are each hydrogen.
- A is CH, n is an integer between 1 and 3, inclusive, and R 4 and R 5 together constitute —CH 2 CH 2 N(CH 3 )CH 2 —.
- tertiary aminoalkyl substituted primary or secondary amines suitable for use according to the invention include 3-dimethylaminopropylamine, N,N,N′′,N′′-tetramethyldipropylenetriamine, and N,N-bis(3-dimethylaminopropyl)-1,3-propanediamine. Reference to the preparation of these compounds can be found in GB 1,338,275 and U.S. Pat. No. 4,248,930.
- Blowing catalysts suitable for use according to the invention are bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties, as represented by the general formula: wherein:
- R 7 , R 8 , and R 9 each independently represents a C1-C4 alkyl group
- R 10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
- n, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH 2 , —NH—CO—NH 2 , or
- the blowing catalyst according to the above structure is such that R 7 , R 8 , and R 9 are each a methyl group, m and p are each equal to 2, and q is either 2 or 3.
- the blowing catalyst may comprise one or more of N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether, N,N,N′-trimethyl-N′-3-aminopropylbis(aminoethyl) ether, and N,N,N′-trimethyl-N′-3-ureidopropylbis(aminoethyl) ether.
- Reference to the preparation of these compounds can be found in U.S. Pat. Nos. 4,433,170; 6,051,527; and 5,824,711; respectively.
- the gelling or the blowing catalyst may be in the form of a corresponding carboxylic acid salt.
- the catalyst as added to a polyurethane formulation may contain the carboxylic acid already present, or the acid may be added with one or more of the other ingredients in the formulation, thereby forming the salt in situ.
- a delayed onset of catalyst activity may be achieved. This may be beneficial in some applications, for example where a delay in viscosity increase is desired in order to facilitate mold filling.
- carboxylic acids are suitable for preparing salts of the gelling and/or blowing catalyst components according to the invention.
- Nonlimiting examples include formic acid, acetic acid, propionic acid, 2-ethylhexanoic acid, aryloxy-substituted carboxylic acids such as phenoxyacetic acid and (dichlorophenoxy)acetic acid, and halogenated acids such as 2-chloropropionic acid and a ring-halogenated aromatic carboxylic acids such as chlorobenzoic acid.
- suitable acids include hydroxy acids such as gluconic acid, hydroxyacetic acid, tartaric acid, and citric acid.
- a catalytically effective amount of the catalyst composition comprising the gelling and blowing catalysts is used in the polyurethane formulation. More specifically, suitable amounts of the catalyst composition may range from about 0.01 to 10 parts by wt per 100 parts polyol (pphp) in the polyurethane formulation, preferably 0.05 to 4 pphp. Suitable weight ratios of gelling catalyst to blowing catalyst in the catalyst composition depend inter alia upon the particular ingredients in the formulation, but are typically at least 2:1, preferably at least 4:1, and at most 10:1, preferably at most 6:1. For TDI-based polyurethane formulations, a ratio of 2:1 to 4:1 is typical, while for MDI-based formulations a ratio from 3:1 to 10:1 is typical.
- compositions according to the invention may also comprise other tertiary amines, organotin or carboxylate urethane catalysts, such as are well known in the urethane art.
- Typical ingredients that may optionally be used in polyurethane foam formulations made with the catalyst compositions of the invention include flame retardants, chain extenders such as ethylene glycol and butanediol; crosslinkers such as diethanolamine, diisopropanolamine, triethanolamine and tripropanolamine; and cell stabilizers such as silicones.
- Preparation of polyurethane foams according to the invention can be carried out by conventional means for making polyurethane foam, using the catalyst compositions of this invention in place of previously used catalyst systems.
- NCO Index means isocyanate index, as that term is commonly used in the polyurethane art. Use of this term in a table of formulations indicates that the appropriate amount of polyisocyanate should be used in order to achieve a formulation having the indicated NCO index.
- Polyurethane foams were prepared using a variety of catalyst compositions, including some according to the invention and some according to standard industry practice. Thermal desorption of volatile materials was performed on the foams, according to dynamic headspace testing method VDA 278.
- VDA 278 is a standard polyurethane foam emission testing method used in the automotive industry to evaluate emissions from polyurethane foam under realistic conditions. In a dynamic headspace experiment, gas extraction is carried out continuously. By continuously removing the gas phase, volatile analytes are unable to re-establish equilibrium and ultimately all of the volatiles are removed from the sample, allowing a more accurate quantitative assessment.
- the test method consists of two consecutive steps.
- gaseous emissions i.e. emissions that contribute to contamination of the interior air of cars
- VOC gaseous emissions
- the foam sample is placed in a thermo desorption tube. While being continuously flushed with an inert gas, this tube is conditioned for 0.5 h at 90° C. Volatiles emitting from the foam are trapped at ⁇ 150° C. in a cryogenic trap. The trap is then heated to 280° C., transferring the volatiles to a gas chromatograph (GC) column, where they are separated.
- GC gas chromatograph
- condensable emissions i.e. emissions that contribute to fogging in cars
- FOG condensable emissions
- This analysis is performed on the sample after it has been submitted to the VOC test.
- the sample is conditioned at 120° C. for 60 minutes, volatiles are again trapped at ⁇ 150° C., and the cryogenic trap is heated to transfer the volatiles to the GC column, where they are separated.
- the emitted components are chemically identified by automated searching of a mass spectrum database.
- DABCO® DC 2525 silicone surfactant is available from Air Products and Chemicals, Inc. of Allentown, Pa.
- Table 1 represent an standard industrial MDI-seating formulations, except that formulations 2 and 3 use catalyst compositions according to the invention, as noted above. Foam was made with different catalyst packages. Use levels were matched to get equivalent foam reactivity profiles. Gelling catalysts B, C, and F were blended with blowing catalyst N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether (catalyst E) to control foam density.
- Table 2 shows the results when pad foams made according to the formulations of Table 1 were evaluated according to the VOC portion of the VDA 278 method.
- Formulation 1 2 3 Volatile Material Polypropylene glycol 137 ppm 116 ppm 10 ppm oligomers Siloxanes 20 ppm 21 ppm 2 ppm Others 14 ppm 10 ppm 41 ppm Decomposition — — — products from catalysts TOTAL 171 ppm 147 ppm 53 ppm
- Table 3 shows the results of pad foams evaluated according to the FOG portion of the VDA 278 method.
- Formulation 1 2 3 Volatile Materials
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Polyurethanes Or Polyureas (AREA)
Abstract
A catalyst composition for catalyzing a polyurethane forming reaction includes a gelling catalyst and a blowing catalyst selected such that the resulting polyurethane foam has a low level of volatile and/or malodorous material in it. The gelling catalysts are selected from tertiary aminoalkyl substituted primary or secondary amines; and the blowing catalysts are selected from bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties.
Description
- This application is a divisional of U.S. Ser. No. 10/695,515 filed on Oct. 27, 2003.
- The present invention relates to compositions and processes for making polyurethane foams. More particularly, it relates to compositions and processes incorporating tertiary amine catalysts capable of providing foams having reduced levels of odor and volatile emissions.
- Polyurethane foams are widely known and used in automotive, housing and other industries. Such foams are produced by reaction of a polyisocyanate with a polyol in the presence of a catalyst and a blowing agent, historically a chlorofluorocarbon (CFC) compound. Due to environmental concerns relating to CFC's, the use of water blown foam formulations, in which at least some of the blowing is performed with CO2 generated by the reaction of water with the polyisocyanate, has become increasingly important. Such systems typically employ tertiary amine catalysts to accelerate both the blowing (reaction of water with isocyanate to generate CO2) and gelling (reaction of polyol with isocyanate) reactions required to make a foam. However, known tertiary amine catalyst compositions may give rise to objectionable releases of volatile and often malodorous materials into the air during foam manufacture and/or thereafter. The present invention addresses the issue of how to reduce such emissions, using certain catalyst compositions.
- In one aspect, the invention is a catalyst composition comprising:
-
- A represents CH or N,
-
- n represents an integer between 1 and 3, inclusive,
- R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
- R6 represents H or 3-aminopropyl, provided that:
-
-
-
- R7, R8, and R9 each independently represents a C1-C4 alkyl group;
- R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
-
- In another aspect, the invention is a formulation for producing a polyurethane foam, the formulation comprising a polyol, a polyisocyanate, water, and a catalyst composition comprising:
-
- A represents CH or N,
-
- n represents an integer between 1 and 3, inclusive,
- R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
- R6 represents H or 3-aminopropyl, provided that:
-
-
-
- R7, R8, and R9 each independently represents a C1-C4 alkyl group;
- R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
-
- In yet another aspect, the invention is a polyurethane foam comprising a product of a reaction between a polyol and a polyisocyanate, the reaction taking place in the presence of water and a catalyst composition comprising:
- 1) a gelling catalyst represented by the general formula:
- in which:
- A represents CH or N,
-
- n represents an integer between 1 and 3, inclusive,
- R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
- R6 represents H or 3-aminopropyl, provided that:
-
-
-
- R7, R8, and R9 each independently represents a C1-C4 alkyl group;
- R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
-
- In a further aspect, the invention is a method of making a polyurethane foam, the method comprising mixing together a polyol, a polyisocyanate, water, and a catalyst composition comprising:
-
- A represents CH or N,
-
- n represents an integer between 1 and 3, inclusive,
- R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
- R6 represents H or 3-aminopropyl, provided that:
-
-
-
- R7, R8, and R9 each independently represents a C1-C4 alkyl group;
- R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
-
- Catalyst compositions according to the invention comprise a gelling catalyst and a blowing catalyst, both of which comprise tertiary amine groups. The gelling catalyst additionally comprises a primary or secondary amine group. The blowing catalyst additionally comprises one or more of a primary or secondary amine group, a hydroxyl group, and a urea group. Without wishing to be bound by any particular theory or explanation, it is believed that the presence of such functional groups provides hydrogen bonding ability with the polyol(s) and or polyisocyanate(s) used in making the polyurethane foams, as well as with chemical functionalities in the foams themselves, resulting in reduced volatility and odor when compared with related tertiary amine catalysts lacking these functional groups. It is further believed that these functional groups may allow reaction of these catalysts into the polyurethane foam, thereby preventing or at least reducing their release from the foams.
- The present invention provides catalyst compositions for making polyurethane foams, and methods for using these compositions. The catalyst compositions comprise mixtures of gelling catalysts selected from tertiary aminoalkyl substituted primary or secondary amines; and blowing catalysts selected from bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties. The catalyst compositions produce polyurethane foams that have low amine odor and low catalyst-derived emissions, as measured by thermal desorption testing techniques.
- The present invention provides catalyst compositions suitable for catalyzing the reaction between an isocyanate functionality and an active hydrogen-containing compound, i.e. an alcohol, a polyol, an amine or water. In particular, the catalyst compositions catalyze the urethane (gelling) reaction of polyol hydroxyl groups with isocyanate to make polyurethanes, and the blowing reaction of water with isocyanate to release carbon dioxide for making foamed polyurethanes. It should be noted however that neither of the two groups of catalysts described herein necessarily performs exclusively either gelling or blowing catalysis functions. Rather, these labels indicate the primary function of these catalyst components when used according to the invention.
- As used herein, the term “polyurethane” is intended to mean polyurethane and/or polyisocyanurate, as is understood in the art. Thus a polyurethane foam can be a polyurethane and/or polyisocyanurate foam. Typically, formation of the foam is aided by incorporation in the reaction mixture of a suitable blowing agent, as is known in the art. Typically a surfactant, such as a silicone surfactant, is also included to help regulate foam formation, as is also known in the art.
- Polyisocyanate
- Polyurethane products made in accordance with the invention may be prepared using any suitable organic polyisocyanates well known in the art for making polyurethane foam including, for example, hexamethylene diisocyanates, isophorone diisocyanates, phenylene diisocyanates, toluene diisocyanates (TDI) and 4,4′-diphenylmethane diisocyanates (MDI). Especially suitable are mixtures of diisocyanates known commercially as “crude MDI”, marketed as PAPI by Dow Chemical, which contain about 60% of 4,4′-diphenylmethane diisocyanates along with other isomeric and analogous higher polyisocyanates. Other suitable isocyanates are the 2,4- and 2,6-TDI's individually or together as their commercially available mixtures. Also suitable are “prepolymers” of these polyisocyanates comprising a partially pre-reacted mixture of a polyisocyanate and a polyether or polyester polyol. Typically, the above polyisocyanates are used in an amount relative to the polyol to establish an isocyanate index in the range of 80 to 400.
- Polyol
- Suitable polyols for making polyurethane foams in conjunction with the catalyst compositions of the invention are those typically used in the art, including for example polyalkylene ether and polyester polyols. Polyalkylene ether polyols include poly(ethylene oxide) and poly(propylene oxide) polymers and copolymers with terminal hydroxyl groups derived from polyhydric compounds, for example diols and/or triols. Such diols and triols include, as non-limiting examples, ethylene glycol, propylene glycol, 1,3-butanediol, 1,4-butanediol, 1,6-hexanediol, neopentyl glycol, diethylene glycol, dipropylene glycol, pentaerythritol, glycerol, diglycerol, trimethylol propane, sugars such as sucrose, and other low molecular weight polyols. Also useful are amine polyether polyols which can be prepared by reacting an amine, such as ethylenediamine, diethylenetriamine, tolylenediamine, diphenylmethanediamine, triethanolamine or the like, with ethylene oxide or propylene oxide.
- In the practice of this invention, a single high molecular weight polyether polyol such as described above may be used. Also, mixtures of such high molecular weight polyether polyols, for example mixtures of different multifunctional materials and/or of compounds having different molecular weights or different chemical compositions, may be used. Useful polyester polyols include those produced by reacting a dicarboxylic acid with an excess of a diol, for example, adipic acid or phthalic acid anhydride with ethylene glycol or butanediol, or reacting a lactone such as caprolactone with an excess of a diol such as propylene glycol.
- In addition to the polyester and polyether polyols noted above, the polyol component of the polyurethane formulation frequently comprises a polymer polyol. Such polymer polyols my be used in polyurethane foams to increase the foam's resistance to deformation, i.e. to increase the load-bearing properties of the foam. One type of polymer polyol, referred to in the art as a graft polyol, consists of a triol in which vinyl monomers are graft copolymerized. Styrene and acrylonitrile are the usual monomers of choice. A second type, a polyurea modified polyol, is a polyol containing a polyurea dispersion formed by the reaction of a diamine and TDI. The TDI is typically used in excess, and therefore some of the TDI may react with both the polyol and polyurea. The second type of polymer polyol may for example be a material called a PIPA polyol, which is formed by the in-situ polymerization of TDI and alkanolamine in the polyol. Depending on the load-bearing requirements and other parameters, polymer polyols may comprise 20-80% of the polyol portion of the polyurethane formulation. If polymer polyols constitute a part of the overall polyol charge, their weight is included in the total polyol weight for purposes of calculating the relative amounts of other ingredients according to the pphp (parts per hundred parts polyol) convention.
- Blowing Agent
- Blowing agents used according to the invention for making polyurethane foams are any commonly used blowing agents known in the art. These include, as nonlimiting examples, HCFC (hydrochlorofluorocarbon) compounds, HFC (hydrofluorocarbon) compounds, chlorofluorocarbons, pentanes, and mixtures of these. The formulations contain water, typically at between 0.1 and 7 pphp (parts per hundred parts of polyol), more typically between 2.5 and 4.5 pphp, to produce CO2 to help create a foam.
- Catalyst Composition
- Catalyst compositions according to the invention comprise mixtures of: 1) gelling catalysts selected from tertiary aminoalkyl substituted primary or secondary amines, and 2) blowing catalysts selected from bis(aminoalkyl) ethers comprising alkanol moieties, primary amine moieties, or ureido moieties derived from such primary amine moieties. It is important that a combination of gelling and blowing catalyst according to the invention be used, rather than either one alone or in combination with a catalyst not of this invention, in order to obtain the low odor and low volatiles emission provided by the invention. Detailed descriptions of the gelling and blowing catalysts follow.
- Gelling Catalysts
-
- A represents CH or N,
-
- n represents an integer between 1 and 3, inclusive,
- R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
- R6 represents H or 3-aminopropyl, provided that:
-
-
- In one embodiment of the invention, R4 and R5 are each a methyl group, A is nitrogen, and R2 and R3 are each hydrogen. In another embodiment of the invention, A is CH, n is an integer between 1 and 3, inclusive, and R4 and R5 together constitute —CH2CH2N(CH3)CH2—.
- Illustrative examples of tertiary aminoalkyl substituted primary or secondary amines suitable for use according to the invention include 3-dimethylaminopropylamine, N,N,N″,N″-tetramethyldipropylenetriamine, and N,N-bis(3-dimethylaminopropyl)-1,3-propanediamine. Reference to the preparation of these compounds can be found in GB 1,338,275 and U.S. Pat. No. 4,248,930.
- Blowing Catalysts
-
- R7, R8, and R9 each independently represents a C1-C4 alkyl group;
- R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
-
- In one embodiment of the invention, the blowing catalyst according to the above structure is such that R7, R8, and R9 are each a methyl group, m and p are each equal to 2, and q is either 2 or 3.
- In other embodiments, the blowing catalyst may comprise one or more of N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether, N,N,N′-trimethyl-N′-3-aminopropylbis(aminoethyl) ether, and N,N,N′-trimethyl-N′-3-ureidopropylbis(aminoethyl) ether. Reference to the preparation of these compounds can be found in U.S. Pat. Nos. 4,433,170; 6,051,527; and 5,824,711; respectively.
- In one embodiment of the invention, some or all of either the gelling or the blowing catalyst, or both, may be in the form of a corresponding carboxylic acid salt. It should be noted that the catalyst as added to a polyurethane formulation may contain the carboxylic acid already present, or the acid may be added with one or more of the other ingredients in the formulation, thereby forming the salt in situ. By providing the catalyst composition in the form of such a salt, a delayed onset of catalyst activity may be achieved. This may be beneficial in some applications, for example where a delay in viscosity increase is desired in order to facilitate mold filling.
- Many carboxylic acids are suitable for preparing salts of the gelling and/or blowing catalyst components according to the invention. Nonlimiting examples include formic acid, acetic acid, propionic acid, 2-ethylhexanoic acid, aryloxy-substituted carboxylic acids such as phenoxyacetic acid and (dichlorophenoxy)acetic acid, and halogenated acids such as 2-chloropropionic acid and a ring-halogenated aromatic carboxylic acids such as chlorobenzoic acid. Further nonlimiting examples of suitable acids include hydroxy acids such as gluconic acid, hydroxyacetic acid, tartaric acid, and citric acid. It will be understood by those of ordinary skill in the art that certain acids in combination with certain gelling/blowing catalyst combinations, and under certain overall compositions of the polyurethane formulation, may detract from the low-emission performance of the catalyst compositions of the present invention. It will further be understood that the determination of acceptable combinations of acids with catalysts for a given application may therefore require some amount of routine experimentation, such as is within the ability of the skilled artisan, with such combinations still falling within the scope of the invention.
- A catalytically effective amount of the catalyst composition comprising the gelling and blowing catalysts is used in the polyurethane formulation. More specifically, suitable amounts of the catalyst composition may range from about 0.01 to 10 parts by wt per 100 parts polyol (pphp) in the polyurethane formulation, preferably 0.05 to 4 pphp. Suitable weight ratios of gelling catalyst to blowing catalyst in the catalyst composition depend inter alia upon the particular ingredients in the formulation, but are typically at least 2:1, preferably at least 4:1, and at most 10:1, preferably at most 6:1. For TDI-based polyurethane formulations, a ratio of 2:1 to 4:1 is typical, while for MDI-based formulations a ratio from 3:1 to 10:1 is typical.
- Variations in these ratios may be made according to the particular choice of other ingredients (polyols, polyisocyanates, etc.) in the polyurethane formulation, as commonly practiced in the art. Catalyst compositions according to the invention may also comprise other tertiary amines, organotin or carboxylate urethane catalysts, such as are well known in the urethane art.
- Other Ingredients
- Other typical ingredients that may optionally be used in polyurethane foam formulations made with the catalyst compositions of the invention include flame retardants, chain extenders such as ethylene glycol and butanediol; crosslinkers such as diethanolamine, diisopropanolamine, triethanolamine and tripropanolamine; and cell stabilizers such as silicones.
- Preparation of polyurethane foams according to the invention can be carried out by conventional means for making polyurethane foam, using the catalyst compositions of this invention in place of previously used catalyst systems.
- A typical polyurethane flexible foam formulation containing a catalyst composition comprising a gelling catalyst and a blowing catalyst according to the invention comprises the following components in parts by weight (pbw):
Flexible Foam Formulation pbw Polyol 20-100 Polymer Polyol 80-0 Silicone Surfactant 1-2.5 Blowing agent 2-4.5 Crosslinker 0.5-2 Catalyst Composition* 0.1-4 Polyisocyanate NCO Index = 70-115
*5:1 weight ratio of gelling catalyst to blowing catalyst
- As used in herein, the term “NCO Index” means isocyanate index, as that term is commonly used in the polyurethane art. Use of this term in a table of formulations indicates that the appropriate amount of polyisocyanate should be used in order to achieve a formulation having the indicated NCO index.
- The gelling and blowing catalysts used in the examples are abbreviated as shown in the following table.
Catalyst Structure B N,N-bis(3-dimethylaminopropyl)-N-isopropanolamine C N,N,N″,N″-tetramethyldipropylenetriamine E N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether F N,N-bis(3-dimethylaminopropyl)-1,3-propanediamine - Polyurethane foams were prepared using a variety of catalyst compositions, including some according to the invention and some according to standard industry practice. Thermal desorption of volatile materials was performed on the foams, according to dynamic headspace testing method VDA 278.
- VDA 278 is a standard polyurethane foam emission testing method used in the automotive industry to evaluate emissions from polyurethane foam under realistic conditions. In a dynamic headspace experiment, gas extraction is carried out continuously. By continuously removing the gas phase, volatile analytes are unable to re-establish equilibrium and ultimately all of the volatiles are removed from the sample, allowing a more accurate quantitative assessment.
- The test method consists of two consecutive steps. In the first step, gaseous emissions, i.e. emissions that contribute to contamination of the interior air of cars, are measured at 90° C. for 0.5 h (VOC). The foam sample is placed in a thermo desorption tube. While being continuously flushed with an inert gas, this tube is conditioned for 0.5 h at 90° C. Volatiles emitting from the foam are trapped at −150° C. in a cryogenic trap. The trap is then heated to 280° C., transferring the volatiles to a gas chromatograph (GC) column, where they are separated.
- In the second step, condensable emissions, i.e. emissions that contribute to fogging in cars, are measured (FOG). This analysis is performed on the sample after it has been submitted to the VOC test. The sample is conditioned at 120° C. for 60 minutes, volatiles are again trapped at −150° C., and the cryogenic trap is heated to transfer the volatiles to the GC column, where they are separated. After separation of the VOC- and FOG- emissions by GC, the emitted components are chemically identified by automated searching of a mass spectrum database.
- Evaluation of MDI Foam Thermal Desorption Testing According to VDA 278 Method
- Three machine mixed MDI pad foams (approximately 45 Kg/m3 density) were prepared according to the formulation in Table 1, each of the three including blowing catalyst E and one of gelling catalysts B, C, and F. Combinations 2 and 3 comprising gelling catalysts C and F, respectively, are according to the invention, while combination 1 comprising gelling catalyst B is not.
TABLE 1 MDI-formulation 1 2 3 Polyether polyol (OH No. = 28) 100 100 100 Water 3.5 3.5 3.5 Diethanolamine (crosslinker) 0.5 0.5 0.5 DABCO DC 2525 Silicone Surfactant 1.0 1.0 1.0 Catalyst B 0.8 Catalyst C 0.9 Catalyst F 0.6 Catalyst E 0.2 0.2 0.2 Cell opener* 1.5 1.5 1.5 MDI (32.5%) 59.0** 59.0** 59.0**
*Voranol CP 1421 polyether polyol, available from The Dow Chemical Company of Midland, MI
**Amount calculated to provide an NCO Index of 95.
- DABCO® DC 2525 silicone surfactant is available from Air Products and Chemicals, Inc. of Allentown, Pa.
- The formulations of Table 1 represent an standard industrial MDI-seating formulations, except that formulations 2 and 3 use catalyst compositions according to the invention, as noted above. Foam was made with different catalyst packages. Use levels were matched to get equivalent foam reactivity profiles. Gelling catalysts B, C, and F were blended with blowing catalyst N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether (catalyst E) to control foam density.
- Table 2 shows the results when pad foams made according to the formulations of Table 1 were evaluated according to the VOC portion of the VDA 278 method.
TABLE 2 Formulation 1 2 3 Volatile Material Polypropylene glycol 137 ppm 116 ppm 10 ppm oligomers Siloxanes 20 ppm 21 ppm 2 ppm Others 14 ppm 10 ppm 41 ppm Decomposition — — — products from catalysts TOTAL 171 ppm 147 ppm 53 ppm - The results show that at 90° C./0.5 h, lower emissions were observed for formulations 2 and 3 according to the invention than for formulation 1, in which the catalyst combination (gelling catalyst B plus blowing catalyst E) is not according to the invention. The results shown in Table 2 point up the fact that, as noted above, both the gelling and blowing catalyst must be defined as set forth above. In formulation 1, blowing catalyst E is according to the invention, but gelling catalyst B is not, and therefore the catalyst composition of B plus E is not according to the invention.
- Table 3 shows the results of pad foams evaluated according to the FOG portion of the VDA 278 method.
TABLE 3 Formulation 1 2 3 Volatile Materials Polypropylene glycol 164 ppm 216 ppm 24 ppm oligomers Siloxanes — 22 ppm — Decomposition 190 ppm — — products from catalysts Others 123 ppm 71 ppm 113 ppm TOTAL 477 ppm 309 ppm 137 ppm - The results shown in Table 3 reveal significantly higher FOG values for formulation 1 comprising catalyst compositions not according to the invention, than for formulations 2 and 3 comprising catalyst compositions according to the invention.
- The results detailed above indicate that, under foam thermal desorption testing conditions, foam made with gelling catalyst B (not of this invention) in combination with blowing catalyst E (formulation 1) evolved significantly more volatile species than the combinations, according to the invention, of gelling catalyst C or F with blowing catalyst E (formulations 2 and 3). In the particular case of formulation 1, it is seen that catalyst decomposition products contributed heavily to emissions during VDA 278 testing. The results shown in Example 1 demonstrate that combinations of gelling catalysts and blowing catalysts according to the invention provide polyurethane foams having low levels of volatile emissions.
- Although the invention is illustrated and described herein with reference to specific embodiments, the invention is not intended to be limited to the details shown. Rather, it is intended that the scope of the claims that follow includes various modifications that may be made in the details while nevertheless achieving the effects of this invention.
Claims (14)
1. A catalyst composition comprising:
1) a gelling catalyst represented by the general formula:
in which:
A represents CH or N,
R1 represents hydrogen or the group
n represents an integer between 1 and 3, inclusive,
R2 and R3 each represent hydrogen or a C1-C6 alkyl group, and
R6 represents H or 3-aminopropyl, provided that:
when A is N, R4 and R5 each represents a C1-C6 alkyl group or together represent a C2-C5 alkylene group which may contain a ring amine moiety —NR—, where R is hydrogen, a C1-C4 alkyl group, or the group
when A is CH, R4 and R5 together represent a C2-C5 alkylene group containing a ring amine moiety —NR—, where R is a C1-C4 alkyl group or the group
and
2) a blowing catalyst according to the general formula:
wherein:
R7, R8, and R9 each independently represents a C1-C4 alkyl group;
R10 represents H, a C1-C4 alkyl group, a C6-C20 aryl group, or a C6-C20 aralkyl group;
m, p, and q each independently represents an integer between 1 and 4, inclusive; and Z represents —OH, —NH2, —NH—CO—NH2, or
2. The catalyst composition of claim 1 , wherein R4 and R5 are each a methyl group, A is nitrogen, and R2 and R3 are each hydrogen.
3. The catalyst composition of claim 1 , wherein R7, R8, and R9 are each a methyl group, m and p are each equal to 2, and q is either 2 or 3.
4. The catalyst composition of claim 1 , wherein A is CH, n is an integer between 1 and 3, inclusive, and R4 and R5 together constitute —CH2CH2N(CH3)CH2—.
5. The catalyst composition of claim 1 , wherein the gelling catalyst comprises N, N, N″, N″-tetramethyldipropylenetriamine.
6. The catalyst composition of claim 1 , wherein the gelling catalyst comprises 3-dimethylaminopropylamine.
7. The catalyst composition of claim 1 , wherein the gelling catalyst comprises N, N-bis(3-dimethylaminopropyl)-1,3-propanediamine.
8. The catalyst composition of claim 1 , wherein the blowing catalyst comprises N,N,N′-trimethyl-N′-2-hydroxyethylbis(aminoethyl) ether.
9. The catalyst composition of claim 8 , wherein the gelling catalyst comprises N,N,N″,N″-tetramethyldipropylenetriamine.
10. The catalyst composition of claim 8 , wherein the gelling catalyst comprises 3-dimethylaminopropylamine.
11. The catalyst composition of claim 8 , wherein the gelling catalyst comprises N,N-bis(3-dimethylaminopropyl)-1,3-propanediamine.
12. The catalyst composition of claim 1 , wherein the blowing catalyst comprises N,N,N′-trimethyl-N′-3-aminopropylbis(aminoethyl) ether.
13. The catalyst composition of claim 1 , wherein the blowing catalyst comprises N,N,N′-trimethyl-N′-3-ureidopropylbis(aminoethyl) ether.
14. The catalyst composition of claim 1 , further comprising a carboxylic acid that forms a salt with one or both of the gelling catalyst and the blowing catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/998,791 US20050090386A1 (en) | 2003-10-27 | 2004-11-29 | Catalyst blends for producing low thermal desorption polyurethane foams |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/695,515 US6858654B1 (en) | 2003-10-27 | 2003-10-27 | Catalyst blends for producing low thermal desorption polyurethane foams |
US10/998,791 US20050090386A1 (en) | 2003-10-27 | 2004-11-29 | Catalyst blends for producing low thermal desorption polyurethane foams |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/695,515 Division US6858654B1 (en) | 2003-10-27 | 2003-10-27 | Catalyst blends for producing low thermal desorption polyurethane foams |
Publications (1)
Publication Number | Publication Date |
---|---|
US20050090386A1 true US20050090386A1 (en) | 2005-04-28 |
Family
ID=34136855
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/695,515 Expired - Lifetime US6858654B1 (en) | 2003-10-27 | 2003-10-27 | Catalyst blends for producing low thermal desorption polyurethane foams |
US10/998,791 Abandoned US20050090386A1 (en) | 2003-10-27 | 2004-11-29 | Catalyst blends for producing low thermal desorption polyurethane foams |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/695,515 Expired - Lifetime US6858654B1 (en) | 2003-10-27 | 2003-10-27 | Catalyst blends for producing low thermal desorption polyurethane foams |
Country Status (9)
Country | Link |
---|---|
US (2) | US6858654B1 (en) |
EP (1) | EP1528072B1 (en) |
JP (1) | JP2005133097A (en) |
KR (1) | KR100613676B1 (en) |
CN (1) | CN100358928C (en) |
AT (1) | ATE339456T1 (en) |
BR (1) | BRPI0404607A (en) |
DE (1) | DE602004002361T2 (en) |
MX (1) | MXPA04010630A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110009512A1 (en) * | 2008-03-20 | 2011-01-13 | Huntsman Petrochemical Llc | Reduction of aldehydes in amines |
US10815351B2 (en) | 2012-03-30 | 2020-10-27 | Evonik Operations Gmbh | Polyurethane foam production process, pre-mix, formulation, and product |
US11104757B2 (en) | 2014-09-12 | 2021-08-31 | Evonik Operations Gmbh | Low emissions polyurethane foam made with isocyanate reactive amine catalysts |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005024144A1 (en) * | 2005-05-23 | 2006-11-30 | Basf Ag | Process for the production of viscoelastic flexible polyurethane foams |
US7528200B2 (en) * | 2006-02-01 | 2009-05-05 | Ardes Enterprises, Inc. | Epoxy hardener systems based on aminobis(methylene-ethyleneurea) |
JP4948853B2 (en) * | 2006-03-06 | 2012-06-06 | 花王株式会社 | Manufacturing method of rigid polyurethane foam |
US7666919B2 (en) | 2006-03-14 | 2010-02-23 | Air Products And Chemicals, Inc. | Aromatic diacid ester diols and substituted carbamates thereof for minimizing deterioration of polyurethane foams |
US20070238799A1 (en) * | 2006-04-06 | 2007-10-11 | Inolex Investment Corporation | Odorless polyester polyol, odorless polyurethane foam and method for making the same |
US8143321B2 (en) * | 2006-07-13 | 2012-03-27 | Air Products And Chemicals, Inc. | N,N,N,′-trimethyl-bis-(aminoethyl) ether and its derivatives as catalysts for polyurethanes |
JP2010530469A (en) * | 2007-06-19 | 2010-09-09 | ハンツマン ペトロケミカル エルエルシー | Reactive amine catalysts for polyurethane |
US20110077376A1 (en) * | 2008-05-30 | 2011-03-31 | Katsumi Tokumoto | Process for producing hydroxyalkyltriethylenediamine, and catalyst composition for the production of polyurethane resin using it |
WO2012072441A1 (en) * | 2010-11-29 | 2012-06-07 | Huntsman Corporation Hungary Zrt. | Blowing catalyst |
US9968919B2 (en) | 2011-06-29 | 2018-05-15 | Evonik Degussa Gmbh | Reducing emissions in polyurethane foam |
US10106638B2 (en) * | 2011-07-29 | 2018-10-23 | Evonik Degussa Gmbh | Reduced emissions low density spray polyurethane foam |
US10081700B2 (en) | 2015-05-05 | 2018-09-25 | Evonik Degussa Gmbh | Delayed action gelling catalyst compositions and methods for making polyurethane polymers |
CN107922579B (en) * | 2015-06-01 | 2021-06-08 | 赢创运营有限公司 | Reactive amine catalysts for polyurethane applications |
EP3954722A1 (en) | 2020-07-30 | 2022-02-16 | Evonik Operations GmbH | Process and composition for the production of flexible polyurethane foam |
Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4007140A (en) * | 1972-11-01 | 1977-02-08 | Imperial Chemical Industries Limited | Tertiary amines as catalysts in polyurethane manufacture |
US4012445A (en) * | 1974-04-23 | 1977-03-15 | Union Carbide Corporation | Beta-amino carbonyl catalysts for polyurethane preparation |
US4049591A (en) * | 1976-10-18 | 1977-09-20 | Texaco Development Corporation | Foams and elastomers prepared in the presence of high tertiary amine content polyurethane catalysts |
US4094827A (en) * | 1976-10-18 | 1978-06-13 | Texaco Development Corporation | Substituted ureas as polyurethane catalysts |
US4101470A (en) * | 1976-11-11 | 1978-07-18 | Texaco Development Corp. | Urethane catalysts |
US4143071A (en) * | 1976-10-18 | 1979-03-06 | Texaco Development Corp. | High tertiary amine content compositions useful as polyurethane catalysts |
US4194069A (en) * | 1978-10-16 | 1980-03-18 | Texaco Development Corporation | Urea derivative and use as polyurethane catalyst |
US4242467A (en) * | 1979-06-12 | 1980-12-30 | Texaco Development Corporation | Urea derivatives and use as polyurethane catalysts |
US4248930A (en) * | 1977-07-16 | 1981-02-03 | Bayer Aktiengesellschaft | The production of polyurethane resins and laminates |
US4330656A (en) * | 1978-10-06 | 1982-05-18 | Bayer Aktiengesellschaft | Activated isocyanate prepolymers and a process for the production of elastomeric polyurethane resins |
US4338408A (en) * | 1981-07-20 | 1982-07-06 | Texaco Inc. | Polyurethanes using bis(aminoethyl)ether derivatives as catalysts |
US4430455A (en) * | 1981-03-09 | 1984-02-07 | Abbott Laboratories | N'-(2-Hydroxyalkyl)-N, N, N'-trimethyl-propylene diamines as catalysts for polyurethane foams |
US4433170A (en) * | 1981-07-20 | 1984-02-21 | Texaco Inc. | Novel bis(aminoethyl)ether derivatives useful as polyurethane catalysts |
US4644017A (en) * | 1984-09-25 | 1987-02-17 | Bayer Aktiengesellschaft | Process for the production of polyisocyanate addition products and composite polyisocyanate addition products |
US4735970A (en) * | 1986-03-11 | 1988-04-05 | Bayer Aktiengesellschaft | Process for the production of a cellular polyurethane |
US5200434A (en) * | 1991-12-30 | 1993-04-06 | Union Carbide Chemicals & Plastics Technology Corporation | Amide derivatives of alkylene oxide polyethers and their uses in polyurethane foam manufacture |
US5756557A (en) * | 1997-05-06 | 1998-05-26 | Air Products And Chemicals, Inc. | Aminomethyl pyrrolidine urea compositions for the production of polyurethanes |
US5824711A (en) * | 1997-05-05 | 1998-10-20 | Air Products And Chemicals, Inc. | N,N,N'-trimethylbis (Aminoethyl) ether substituted urea compostions for the production of polyurethanes |
US5859079A (en) * | 1997-05-21 | 1999-01-12 | Air Products And Chemicals, Inc. | Polyurethane catalyst compositions for improving foam performance |
US6051527A (en) * | 1995-09-27 | 2000-04-18 | Air Products And Chemicals, Inc. | Aminopropylbis(aminoethyl) ether compositions for the production of polyurethanes |
US6201033B1 (en) * | 1997-05-05 | 2001-03-13 | Air Products And Chemical, Inc. | Reactive catalyst compositions for improving water blown polyurethane foam performance |
US6307102B1 (en) * | 1997-10-15 | 2001-10-23 | Tosoh Corporation | Amine catalyst for producing polyurethane and polyisocyanurate |
US6737446B1 (en) * | 2003-01-03 | 2004-05-18 | Air Products And Chemicals, Inc. | Tertiary amino alkyl amide catalysts for improving the physical properties of polyurethane foams |
US6747069B1 (en) * | 2003-03-10 | 2004-06-08 | Air Products And Chemicals, Inc. | Tertiary alkanolamine polyurethane catalysts derived from long chain alkyl and fatty carboxylic acids |
US6759447B1 (en) * | 2003-01-06 | 2004-07-06 | Air Products And Chemicals, Inc. | Physical properties of polyurethane foams using tertiary amino alkyl amide catalysts |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2116535A1 (en) | 1970-04-09 | 1971-12-09 | Dow Chemical Co | Polyurethane products and processes for making them |
DE3027796A1 (en) | 1980-07-23 | 1982-02-18 | Bayer Ag, 5090 Leverkusen | Opt. foamed polyurethane prodn. - catalysed by di:alkyl-aminoalkyl-urea deriv. catalysts generating no amine smell |
US5240970A (en) * | 1993-01-08 | 1993-08-31 | Air Products And Chemicals, Inc. | Quaternary ammonium carboxylate inner salt compositions as controlled activity catalysts for making polyurethane foam |
DE4412677A1 (en) * | 1994-04-13 | 1995-10-19 | Basf Ag | Process for the production of polyurethane foams in the presence of aminoalkyl or aminophenyl imidazoles as a catalyst and the use of these catalysts for the production of polyisocyanate polyaddition products |
US5756558A (en) * | 1996-07-03 | 1998-05-26 | Air Products And Chemicals, Inc. | Hydroxyalkylbis(aminoethyl) ether compositions for the production of polyurethanes |
EP1092737B1 (en) | 1999-10-13 | 2003-09-24 | Tosoh Corporation | Catalyst composition for the production of a polyurethane resin, and method for producing a polyurethane resin |
TWI296630B (en) * | 2001-10-31 | 2008-05-11 | Tosoh Corp | Process for the production of flexible polyurethane foams |
-
2003
- 2003-10-27 US US10/695,515 patent/US6858654B1/en not_active Expired - Lifetime
-
2004
- 2004-10-21 EP EP04025047A patent/EP1528072B1/en not_active Revoked
- 2004-10-21 DE DE602004002361T patent/DE602004002361T2/en active Active
- 2004-10-21 AT AT04025047T patent/ATE339456T1/en not_active IP Right Cessation
- 2004-10-22 BR BR0404607-2A patent/BRPI0404607A/en not_active IP Right Cessation
- 2004-10-22 CN CNB2004100861859A patent/CN100358928C/en active Active
- 2004-10-26 KR KR1020040085549A patent/KR100613676B1/en active IP Right Grant
- 2004-10-26 MX MXPA04010630A patent/MXPA04010630A/en active IP Right Grant
- 2004-10-27 JP JP2004312674A patent/JP2005133097A/en active Pending
- 2004-11-29 US US10/998,791 patent/US20050090386A1/en not_active Abandoned
Patent Citations (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4007140A (en) * | 1972-11-01 | 1977-02-08 | Imperial Chemical Industries Limited | Tertiary amines as catalysts in polyurethane manufacture |
US4012445A (en) * | 1974-04-23 | 1977-03-15 | Union Carbide Corporation | Beta-amino carbonyl catalysts for polyurethane preparation |
US4049591A (en) * | 1976-10-18 | 1977-09-20 | Texaco Development Corporation | Foams and elastomers prepared in the presence of high tertiary amine content polyurethane catalysts |
US4094827A (en) * | 1976-10-18 | 1978-06-13 | Texaco Development Corporation | Substituted ureas as polyurethane catalysts |
US4143071A (en) * | 1976-10-18 | 1979-03-06 | Texaco Development Corp. | High tertiary amine content compositions useful as polyurethane catalysts |
US4101470A (en) * | 1976-11-11 | 1978-07-18 | Texaco Development Corp. | Urethane catalysts |
US4248930A (en) * | 1977-07-16 | 1981-02-03 | Bayer Aktiengesellschaft | The production of polyurethane resins and laminates |
US4330656A (en) * | 1978-10-06 | 1982-05-18 | Bayer Aktiengesellschaft | Activated isocyanate prepolymers and a process for the production of elastomeric polyurethane resins |
US4194069A (en) * | 1978-10-16 | 1980-03-18 | Texaco Development Corporation | Urea derivative and use as polyurethane catalyst |
US4242467A (en) * | 1979-06-12 | 1980-12-30 | Texaco Development Corporation | Urea derivatives and use as polyurethane catalysts |
US4430455A (en) * | 1981-03-09 | 1984-02-07 | Abbott Laboratories | N'-(2-Hydroxyalkyl)-N, N, N'-trimethyl-propylene diamines as catalysts for polyurethane foams |
US4433170A (en) * | 1981-07-20 | 1984-02-21 | Texaco Inc. | Novel bis(aminoethyl)ether derivatives useful as polyurethane catalysts |
US4338408A (en) * | 1981-07-20 | 1982-07-06 | Texaco Inc. | Polyurethanes using bis(aminoethyl)ether derivatives as catalysts |
US4644017A (en) * | 1984-09-25 | 1987-02-17 | Bayer Aktiengesellschaft | Process for the production of polyisocyanate addition products and composite polyisocyanate addition products |
US4735970A (en) * | 1986-03-11 | 1988-04-05 | Bayer Aktiengesellschaft | Process for the production of a cellular polyurethane |
US5200434A (en) * | 1991-12-30 | 1993-04-06 | Union Carbide Chemicals & Plastics Technology Corporation | Amide derivatives of alkylene oxide polyethers and their uses in polyurethane foam manufacture |
US6051527A (en) * | 1995-09-27 | 2000-04-18 | Air Products And Chemicals, Inc. | Aminopropylbis(aminoethyl) ether compositions for the production of polyurethanes |
US6232356B1 (en) * | 1997-05-05 | 2001-05-15 | Air Products And Chemicals, Inc. | Reactive catalyst compositions for improving water blown polyurethane foam performance |
US5824711A (en) * | 1997-05-05 | 1998-10-20 | Air Products And Chemicals, Inc. | N,N,N'-trimethylbis (Aminoethyl) ether substituted urea compostions for the production of polyurethanes |
US6201033B1 (en) * | 1997-05-05 | 2001-03-13 | Air Products And Chemical, Inc. | Reactive catalyst compositions for improving water blown polyurethane foam performance |
US5756557A (en) * | 1997-05-06 | 1998-05-26 | Air Products And Chemicals, Inc. | Aminomethyl pyrrolidine urea compositions for the production of polyurethanes |
US5859079A (en) * | 1997-05-21 | 1999-01-12 | Air Products And Chemicals, Inc. | Polyurethane catalyst compositions for improving foam performance |
US6307102B1 (en) * | 1997-10-15 | 2001-10-23 | Tosoh Corporation | Amine catalyst for producing polyurethane and polyisocyanurate |
US6737446B1 (en) * | 2003-01-03 | 2004-05-18 | Air Products And Chemicals, Inc. | Tertiary amino alkyl amide catalysts for improving the physical properties of polyurethane foams |
US6759447B1 (en) * | 2003-01-06 | 2004-07-06 | Air Products And Chemicals, Inc. | Physical properties of polyurethane foams using tertiary amino alkyl amide catalysts |
US6747069B1 (en) * | 2003-03-10 | 2004-06-08 | Air Products And Chemicals, Inc. | Tertiary alkanolamine polyurethane catalysts derived from long chain alkyl and fatty carboxylic acids |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20110009512A1 (en) * | 2008-03-20 | 2011-01-13 | Huntsman Petrochemical Llc | Reduction of aldehydes in amines |
US10815351B2 (en) | 2012-03-30 | 2020-10-27 | Evonik Operations Gmbh | Polyurethane foam production process, pre-mix, formulation, and product |
US11104757B2 (en) | 2014-09-12 | 2021-08-31 | Evonik Operations Gmbh | Low emissions polyurethane foam made with isocyanate reactive amine catalysts |
Also Published As
Publication number | Publication date |
---|---|
JP2005133097A (en) | 2005-05-26 |
KR20050040105A (en) | 2005-05-03 |
US6858654B1 (en) | 2005-02-22 |
KR100613676B1 (en) | 2006-08-21 |
CN100358928C (en) | 2008-01-02 |
EP1528072B1 (en) | 2006-09-13 |
DE602004002361T2 (en) | 2007-09-20 |
BRPI0404607A (en) | 2005-06-21 |
DE602004002361D1 (en) | 2006-10-26 |
CN1621426A (en) | 2005-06-01 |
EP1528072A1 (en) | 2005-05-04 |
ATE339456T1 (en) | 2006-10-15 |
MXPA04010630A (en) | 2005-10-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US10464876B2 (en) | Processes, products, and compositions having tetraalkylguanidine salt of aromatic carboxylic acid | |
EP1878492B1 (en) | N,N,N'-Trimethyl-bis-(aminoethyl) ether and its derviatives as catalysts for polyurethanes | |
US6858654B1 (en) | Catalyst blends for producing low thermal desorption polyurethane foams | |
EP1534766B1 (en) | Process for preparing polyurethane foam | |
EP1018525B1 (en) | Process for preparing polyurethane foam | |
EP2196493B1 (en) | Catalyst composition for water blown, low density, rigid polyurethane foam | |
US9321892B2 (en) | Blowing agent enhancers for polyurethane foam production | |
EP1443065B1 (en) | Low acid organometallic catalyst for the production of flexible, semi-flexible and rigid polyurethane foams | |
WO2002066531A2 (en) | Process to enhance polyurethane foam performance | |
EP1332167B1 (en) | Process to improve polyurethane foam performance | |
US20150158968A1 (en) | Production of low-emission flexible polyurethane foams | |
EP0533071B1 (en) | Amine-boron adducts as reduced odor catalyst compositions for the production of polyurethanes | |
JP2010530469A (en) | Reactive amine catalysts for polyurethane | |
JP3826469B2 (en) | Manufacturing method of rigid isocyanurate foam | |
JP3849178B2 (en) | Manufacturing method of rigid isocyanurate foam | |
JPH10219015A (en) | Production of hard spray foam | |
MXPA98003525A (en) | Compositions of aminometil pyrrolidine urea parala polyurette production |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: EXPRESSLY ABANDONED -- DURING EXAMINATION |