WO2007003966A1 - Novel zirconium compound, catalyst and its use for polyurethane manufacture - Google Patents
Novel zirconium compound, catalyst and its use for polyurethane manufacture Download PDFInfo
- Publication number
- WO2007003966A1 WO2007003966A1 PCT/GB2006/050187 GB2006050187W WO2007003966A1 WO 2007003966 A1 WO2007003966 A1 WO 2007003966A1 GB 2006050187 W GB2006050187 W GB 2006050187W WO 2007003966 A1 WO2007003966 A1 WO 2007003966A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- deaa
- catalyst
- compound
- alkyl
- derived
- Prior art date
Links
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
- C08G18/22—Catalysts containing metal compounds
- C08G18/222—Catalysts containing metal compounds metal compounds not provided for in groups C08G18/225 - C08G18/26
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/22—Organic complexes
- B01J31/2204—Organic complexes the ligands containing oxygen or sulfur as complexing atoms
- B01J31/2208—Oxygen, e.g. acetylacetonates
- B01J31/2226—Anionic ligands, i.e. the overall ligand carries at least one formal negative charge
- B01J31/223—At least two oxygen atoms present in one at least bidentate or bridging ligand
- B01J31/2234—Beta-dicarbonyl ligands, e.g. acetylacetonates
-
- 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
-
- 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
- C08G18/22—Catalysts containing metal compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
- B01J2231/34—Other additions, e.g. Monsanto-type carbonylations, addition to 1,2-C=X or 1,2-C-X triplebonds, additions to 1,4-C=C-C=X or 1,4-C=-C-X triple bonds with X, e.g. O, S, NH/N
- B01J2231/341—1,2-additions, e.g. aldol or Knoevenagel condensations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
- B01J2531/48—Zirconium
-
- 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
- C08G2110/0025—Foam properties rigid
Definitions
- the present invention concerns a novel catalyst comprising a zirconium chelate, and its use to catalyse the reaction of an isocyanate-containing compound with an alcohol or an amine to form a polyurethane or a polyurea.
- Polyurethanes are typically made by reacting a polyisocyanate compound with a polyol in the presence of an organometallic catalyst.
- Catalysts for polyurethane manufacture are conventionally based on tin compounds such as dibutyl tin dilaurate or compositions of mercury such as phenyl mercuric neodecanoate. More recently, compounds based upon metals such as titanium or nickel have been used.
- Such compounds are of general formula RO-M(L 1 ) X (L 2 ) y (L 3 ) z where R is alkyl or a hydroxy-alkyl, hydroxyalkoxyalkyl, or (hydroxy)polyoxyalkyl group and up to 2 of L 1 to L 3 may represent an amide of acetoacetic acid.
- R is alkyl or a hydroxy-alkyl, hydroxyalkoxyalkyl, or (hydroxy)polyoxyalkyl group and up to 2 of L 1 to L 3 may represent an amide of acetoacetic acid.
- These compounds have a single labile -OR ligand and were believed to function as a cure catalyst by exchange or insertion of the polyol or of the isocyanate at the labile site on the organometallic composition, by displacement of the OR group.
- US-A-5846897 discloses zirconium compounds with diketones or alkylacetoacetates which catalyse the isocyanate - alcohol reaction having the chemical structure: Me (X1 , X2, X3, X4) wherein Me is zirconium (Zr) or hafnium (Hf) and X1 , X2, X3, and X4, are the same or different and selected from the group consisting of a diketone and an alkylacetoacetate having the structures: RICOCH 2 COR 2 and RIOCOCH 2 COR 2 wherein each of R 1 and R 2 is a branched or linear C1 -C20 hydrocarbon and at least one of X1 , X2, X3, and X4 is a diketone with structure (II) wherein the total number of carbons in R 1 + R 2 is at least 4.
- Patil et al J. Mater Chem 2003, 13, 2177 - 2184 have used zirconium bis(isopropoxide)bis(N,N- diethylacetoacetamide) as a precursor for the metal-organic chemical vapour deposition of zirconium dioxide.
- the catalyst is of formula Zr(L)(A 1 )(A 2 )(A 3 ) where L represents a ketoamide ligand, A 1 , A 2 & A 3 may be the same or different and each represent a ligand derived from a compound selected from the group consisting of:- an alcohol, a polyol, an alkyl acetoacetate, a diketone, a ketoamide, a carboxylic acid or ester thereof, an alkanolamine, a phosphoric acid ester and a sulphonic acid or ester thereof; provided that either: (i) none of A 1 , A 2 & A 3 represent a ligand -OR where R is alkyl or a hydroxy-alkyl, hydroxyalkoxyalkyl, or (hydroxy)polyoxyalkyl group, or
- a 1 , A 2 & A 3 represent a ligand -OR where R is alkyl or a hydroxy- alkyl, hydroxyalkoxyalkyl, or (hydroxy)polyoxyalkyl group.
- R is alkyl or a hydroxy- alkyl, hydroxyalkoxyalkyl, or (hydroxy)polyoxyalkyl group.
- a ligand derived from a compound in the sense that the ligand has been formed by the reaction of the compound with a zirconium compound to form the claimed catalyst or a precursor thereto.
- a ligand derived from an alcohol ROH is present in the catalyst as an alkoxide RO-
- a ligand derived from a carboxylic acid RCOOH is present in the catalyst as a carboxylate RCOO-.
- ligand L or A the compounds referred to as forming a ligand L or A will be present in the catalyst in their reacted form and generally not in the unreacted form of the compound. Most of the ligand-forming compounds herein react with a zirconium compound though a reactive -OH to form an -0-Zr- linkage in the catalyst.
- the ketoamide ligand, L is derived from a ketoamide of general structure shown in Formula 1 , which is believed to react with the zirconium alkoxide or haloalkoxide through its "enol" form, shown in Formula 1', to form a ligand R 1 R 2 COCR 3 CR 4 O-.
- R 1 , R 2 and R 4 are independently selected from H, linear or branched alkyl or aryl.
- R 1 , R 2 and/or R 4 are alkyl groups, they preferably contain from 1 to 22 carbon atoms, more preferably from 1 to 8 C atoms.
- R 1 , R 2 and/or R 4 are aryl groups, they may be unsubstituted or substituted with alkyl, halogen or ether groups.
- aryl we include polycyclic aromatic groups. It is preferred that R 1 , R 2 and/or R 4 are not H, and tertiary amides, i.e. where neither R 1 nor R 2 is H are preferred.
- R 3 is selected from H or linear or branched alkyl, preferably containing from 1 to 22 carbon atoms, more preferably from 1 to 8 C atoms.
- L is preferably a ligand derived from a N,N-dialkyl acetoacetamide (DAAA) and a preferred dialkyl acetoacetamide comprises N,N-diethylacetoacetamide (DEAA).
- DAAA N,N-dialkyl acetoacetamide
- DEAA N,N-diethylacetoacetamide
- Other suitable ketoamides include acetoacetanilide, o-acetoacetaniside, 2'-benzoylacetanilide, 4'- chloroacetoacetanilide, p-acetoacetaniside, N,N-dimethylacetoacetamide,
- the reaction product may contain more than 1 mole of ketoamide per mole of zirconium when at least one of A 1 , A 2 & A 3 is derived from a ketoamide.
- the product may contain up to four moles of ketoamide bound to the zirconium atom to form a chelate.
- Each ketoamide ligand may be the same as or different from each other ketoamide ligand.
- each ketoamide ligand is derived from the same ketoamide compound.
- the product may also contain a free ketoamide compound, i.e. there may be more than 4 moles of ketoamide per mole of zirconium.
- the catalyst is a composition comprising from 1 to 10 moles, more preferably from 2 to 4 moles, of free ketoamide per mole of zirconium.
- One preferred such embodiment comprises a composition of formula [Zr(DEAA) 4 + 2DEAA].
- Zr(DEAA)X this means that the zirconium compound has x ligands derived from DEAA, which is present in the catalyst in its reacted form.
- a 1 , A 2 & A 3 may be the same or different and each represent a ligand derived from a compound selected from the group consisting of an alcohol, a polyol, an alkyl acetoacetate, a diketone, a ketoamide, a carboxylic acid or ester thereof, an alkanolamine or a phosphoric acid ester.
- the alcohol is of general formula R-OH where R is an alkyl or aryl (including polyaryl) group. Where R is aryl, we include phenol, napthol and substituted versions of these, e.g. alkylphenols such as dodecylphenol.
- R is alkyl, more preferably an alkyl group containing from 1 to 12 C atoms, and most preferably an alkyl group containing from 2 to 8 C atoms.
- each R may or may not be the same as the other(s).
- Preferred alcohols include, ethanol, isopropanol, n-propanol, tertiary butanol, n- butanol, 2-ethylhexanol, amyl alcohol, tert-amyl alcohol, hexanol, cyclohexanol, phenol, dodecylphenol and naphthol.
- the alcohol reacts with a zirconium compound to form an alkoxide or aryloxide RO- ligand.
- a zirconium compound to form an alkoxide or aryloxide RO- ligand.
- the catalyst has the general formula Zr(ketoamide) 2 (OR) 2 where R is alkyl, more preferably an alkyl group containing from 1 to 12 C atoms, and most preferably an alkyl group containing from 2 to 8 C atoms.
- the polyol may be a monomeric alcohol having more than one hydroxy group, for example ethylene glycol, 1 ,3-propylene glycol, 1 ,4-butane diol, or a dimeric or polymeric alcohol such as diethylene glycol, dipropylene glycol, polyethylene glycol, polypropylene glycol.
- the polyol also includes polyester polyols and polyether polyols of the type typically used in the manufacture of poyurethanes and which are commercially available. Hydroxy- functionalised resins may also be suitable for forming one or more of the A ligands in general formula 1. Such resins include hydroxyl-containing resins which are sold for use in printing inks, preferably having a hydroxyl number of from about 100 to about 500, especially from about 200 to about 400 mg KOH/g (tested according to DIN 53 240).
- Suitable synthetic resins include ketone- aldehyde resins especially ketone-formaldehyde resins such as hydrogenated acetophenone formaldehyde condensation resins, cyclohexanone-formaldehyde condensation resins and urethane-modified ketone aldehyde resins.
- ketone- aldehyde resins especially ketone-formaldehyde resins such as hydrogenated acetophenone formaldehyde condensation resins, cyclohexanone-formaldehyde condensation resins and urethane-modified ketone aldehyde resins.
- Such resins are available from Degussa AG as Synthetic Resins 1201 , CA and SK, for example.
- each molecule may bond multiply to the same zirconium atom or alternatively it may bond to more than one zirconium atom to form a bridge between the zirconium atoms. It is likely that in such compounds there is a mixture containing bridged and non-bridged structures.
- the catalyst is of general formula Zr(ketoamide) 2 (polyol) and/or Zr 2 (ketoamide) 4 (polyol) 2 and/or higher oligomeric bridged structures where (polyol) is in each case a ligand derived from the polyol by reaction of two hydroxy functions with zirconium to form two alkoxide bonds.
- Zr(L) (A)(polyol) compound therefore refer to the empirical formula and include compounds in which bridged dimeric and oligomeric forms are present.
- Preferred examples of this type include Zr(DEAA) 2 (1 ,3-propanedioxide), Zr(DEAA) 2 (1 ,4-butanedioxide) and Zr(DEAA) 2 (diethyleneglycoxide).
- a 1 , A 2 and/or A 3 may each represent a ligand derived from an alkyl acetoacetate, i.e. an ester of an alkyl alcohol R 5 OH with acetoacetic acid wherein R 5 is a branched or linear C1 -C20 hydrocarbon; more preferably R 5 contains from 1 to 8 carbon atoms.
- Ethylacetoacetate (EAA) is a particularly preferred alkyl acetoacetate compound.
- Zr(EAA)n we mean a zirconium compound having n ligands derived from ethylacetoacetate.
- a 1 , A 2 and/or A 3 may each represent a ligand derived from a diketone which is preferably a ⁇ - diketone of general formula R 6 COCH 2 COR 7 wherein each of R 6 and R 7 is a branched or linear C1 -C20 hydrocarbon.
- Preferred diketones include acetylacetone (2,4-pentanedione), 2,4- heptanedione and alkyl-substituted versions thereof and 3,5-heptanedione and alkyl-substituted versions thereof.
- a 1 , A 2 and/or A 3 may each represent a ligand derived from a carboxylic acid or ester thereof.
- Suitable carboxylic acids include benzoic acid and alkyl carboxylic acids, for example a C 2 - C 30 carboxylic acid, especially a C 4 - C 22 carboxylic acid such as butyric, neodecanoic, stearic, isostearic, oleic or 2-ethyl-hexylcarboxylic acid.
- the carboxylic acid or ester may contain more than one carboxylic acid group such as malonic acid, tartaric acid and their esters, especially alkyl esters e.g. diethyl malonate.
- Hydroxycarboxylic acids such as lactic acid, citric acid, oxalic acid may also form suitable ligands with zirconium.
- a 1 , A 2 and/or A 3 may each represent a ligand derived from an alkanolamine, i.e. a compound of general formula HO(CH 2 ) X NR 8 2 where R 8 comprises HO(CH 2 )X or an alkyl group or hydrogen.
- X is an integer and preferably ranges from 1 to 8.
- Preferred alkanolamines include ethanolamine, diethanolamine and triethanolamine although others are suitable.
- a 1 , A 2 and/or A 3 may each represent a ligand derived from an organophosphorus compound having a P-OH group, particularly a phosphate ester, i.e. an alkyl or aryl acid phosphate, or a salt thereof comprising a dialkyl phosphate, a diaryl phosphate, a monoalkyl phosphate, a monoaryl phosphate or a mixture of two or more of a dialkyl phosphate, a diaryl phosphate, a monoalkyl phosphate and a mono aryl phosphate, a phosphonate ester or a salt thereof comprising an alkyl or aryl phosphonate or salts thereof, an alkyl or aryl pyrophosphate, an alkyl or aryl phosphonic acid or alkyl or aryl ester thereof or a salt thereof, a dialkyl or aryl phosphinic acid or salt thereof.
- a phosphate ester
- the organophosphorus compound contains a P-OH group, i.e. an acidic group or its salt, i.e. a P-O " M + group where M is metal or ammonium.
- Preferred organophosphorus compounds comprise an alkyl phosphate compound which may be a mono- or a di-alkyl phosphate or is conveniently a mixture of mono- and dialkyl phosphates, such mixtures being more readily available than pure mono- or a di-alkyl phosphates.
- Monoalkyl phosphates generally have a formula (R 9 O)PO(OH) 2 .
- Dialkyl phosphates generally have the formula (R 9 O)(R 10 O)PO(OH).
- R 9 , R 10 may be the same or different and represent a linear or branched alkyl group usually containing up to 8 carbon atoms and preferably containing up to 5 carbon atoms. Usually, but not necessarily, R 9 ,and R 10 are identical. Preferably R 9 , and R 10 are selected from n-butyl, sec-butyl, ferf-butyl, /so-propyl, n-propyl, ethyl, methyl, phenyl, amyl and ethyl-hexyl.
- Suitable phosphonate ester, phosphonic acid, phosphinic acid or salt thereof comprises an alkyl or aryl phosphonate, phosphonic acid or their salts and generally have a formula
- R 11 and R 12 each represent a hydrogen atom or an aryl group or an alkyl group containing up to 8 carbon atoms and preferably containing up to 5 carbon atoms and n is 1 or 2.
- a 1 , A 2 and/or A 3 may each represent a ligand derived from a sulphonic acid or ester thereof, i.e. a compound of general formula R 13 SO 3 H or its ester where R is aryl or alkyl.
- suitable sulphonic acids include methane sulphonic acid and substituted benzene sulphonic acids such as dodecylbenzene sulphonic acid. Salts of these sulphonic acids are also suitable, for example alkali metal salts such as the sodium salt and quaternary ammonium salts.
- the catalyst of the invention preferably comprises the reaction product of a zirconium alkoxide or haloalkoxide with a ketoamide compound and optionally with at least one other ligand- forming compound.
- the compounds of the invention may be made by reacting a zirconium compound such as an alkoxide, a halide or haloalkoxide with the ketoamide and then with the other compound(s) to form the A ligands if necessary. Where the A-ligands are alkoxide, these may form part of the starting zirconium compound.
- Zirconium haloalkoxides may be represented by the formula Zr(OR) x .
- the haloalkoxides may be of mixed formulation and therefore x need not be an integer.
- the preferred halides are chloride and bromide, particularly chloride.
- the zirconium alkoxide or haloalkoxide is a zirconium alkoxide of formula Zr(OR) 4 , where R has the meaning described above. Each R may or may not be the same as each other R.
- the zirconium alkoxide is a tetra-alkyl alkoxide where all alkoxide groups are the same.
- Preferred zirconium alkoxides include tetra-i-propoxy zirconium, tetra- ethyl zirconium, tetra-n-propoxy zirconium and tetra-n-butoxy zirconium since these are readily available commercial materials.
- the zirconium alkoxide is a mixed alkoxide.
- This embodiment is particularly useful where one or more of the OR groups is derived from an alkoxide which is less readily available.
- Suitable zirconium alkoxides may therefore comprise Zr(isopropoxide) 2 (2-ethylhexoxide) 2 , Zr(n- butoxide) 2 (2-ethylhexoxide) 2 , Zr(n-butoxide) 2 (tert-amylalkoxide) 2 , Zr(isopropoxide) 2 (tert- amylalkoxide) 2 .
- the catalyst composition may additionally comprise a solvent or diluent.
- the solvent or diluent may be a compound that coordinates with the zirconium catalyst or it may be non-coordinating.
- the solvent may comprise an alcohol (which may be alcohol liberated in the reaction of a zirconium alkoxide with the ketoamide).
- Suitable solvents include polyols (e.g.
- a similar polyol to that used in a polyurethane reaction for which the compound is used as catalyst such as 1 ,4-butane diol, 1 ,3-propylene glycol, ethylene glycol, diethylene glycol, a polyethylene glycol, a polypropylene glycol, a polyester polyol, a ketoamide, particularly the ketoamide used to form the catalyst, ethylacetoacetate, acetylacetone, diethylmalonate or an excess of a compound used to form one of the A ligands.
- Examples of preferred catalysts comprise compounds of the following formulae:- Zr(DEAA) 2 (2- ethylhexoxide) 2 , Zr(n-butoxide) 2 (DEAA) 2 , Zr(n-propoxide) 2 (DEAA) 2 , Zr(DEAA) 2 (tert- amylalkoxide) 2, Zr(isopropoxide) 2 (DEAA) 2 , Zr(DEAA) 4 , Zr(t-butoxide) 2 (DEAA) 2 , Zr(DEAA) 4 ,
- These catalysts may also include additional quantities of at least one of the ligand-forming compounds which are assumed to be present in a non-complexed state. In particular free
- DEAA ethylacetoacetate, acetylacetone or polyol, especially diethylene glycol has been found to be of benefit.
- the catalyst does not comprise a compound of bismuth as a co- catalyst.
- the catalyst composition is useful in the manufacture of polyurethanes, i.e. as a cure catalyst for the reaction of a polyisocyanate with a compound containing an active hydrogen, especially a hydroxyl group, in particular a a polyol; or an amino compound.
- Applications of such polyurethanes are very diverse and include mouldings, foams, adhesives, coatings, cast or spray elastomers, casting resins etc.
- the catalyst composition may also be used to catalyse the reaction of a polyisocyanate binder with hydrous materials such as those derived from wood or plant fibres, e.g. as used in the manufacture of composite boards for the construction industry.
- Organic polyisocyanate compound or mixture of organic polyisocyanate compounds may be suitable provided said compounds have at least 2 isocyanate groups.
- Organic polyisocyanates include diisocyanates, particularly aromatic diisocyanates, and isocyanates of higher functionality.
- organic polyisocyanates include aliphatic isocyanates such as hexamethylene diisocyanate; and aromatic isocyanates such as m- and p-phenylene diisocyanate, tolylene-2,4- and tolylene- 2,6-diisocyanate, diphenylmethane-4,4'-diisocyanate, chlorophenylene- 2,4-diisocyanate, naphthylene-1 ,5-diisocyanate, diphenylene-4,4'- diisocyanate, 4,4'-diisocyanate-3,3'-dimethyl-diphenyl, 3-methyldiphenylmethane-4,4'-di- isocyanate and diphenyl ether diisocyanate; and cycloaliphatic diisocyanates such as cyclohexane-2,4- and -2,3-diisocyanate, 1-methylcyclohexyl-2,4- and -2,
- Modified polyisocyanates containing isocyanurate, carbodiimide or uretonimine groups may be used and are generally chosen when particular physical properties are desired.
- Blocked polyisocyanates like the reaction product of a phenol or an oxime and a polyisocyanate, may be used, where they have a deblocking temperature below the temperature applied in use.
- the organic polyisocyanate may also be an isocyanate-ended prepolymer made by reacting an excess of a diisocyanate or higher functionality polyisocyanate with a polyol such as, for example a polyether polyol or a polyester polyol.
- Water-emulsifiable organic polyisocyanates like those described in UK patent no. 1 444 933, in European patent publication no. 516 361 and in PCT patent publication no. 91/03082 can also be used.
- isocyanates may be used, for example a mixture of tolylene diisocyanate isomers such as the commercially available mixtures of 2,4- and 2,6-isomers and also the mixture of di- and higher polyisocyanates.
- Mixtures of diisocyanates known commercially as "crude MDI" contain about 60% of 4,4'-diphenylmethane diisocyanate along with other isomeric and analogous higher polyisocyanates.
- Polyisocyanate mixtures may optionally contain monofunctional isocyanates such as p-ethyl phenylisocyanate.
- Such mixtures are well-known in the art and include the crude phosgenation products containing methylene bridged polyphenyl polyisocyanates, including diisocyanate, triisocyanate and higher polyisocyanates together with any phosgenation by-products.
- Preferred isocyanates are those wherein the isocyanate is an aromatic diisocyanate or polyisocyanate of higher functionality such as a pure diphenylmethane diisocyanate or a mixture of methylene bridged polyphenyl polyisocyanates containing diisocyanates, tri isocyanates and higher functionality polyisocyanates.
- Methylene bridged polyphenyl polyisocyanates are well known in the art. They are prepared by phosgenation of corresponding mixtures of polyamines. For convenience, polymeric mixtures of methylene bridged polyphenyl polyisocyanates containing diisocyanate, triisocyanate and higher functionality polyisocyanates are referred to hereinafter as polymeric MDI.
- Polyisocyanates suitable for use with the organometallic complexes of the invention include SUPRASECTM DNR, SUPRASECTM 2185, RUBINATETM M and RUBINATETM 1840, all available from Huntsman Polyurethanes.
- the polyisocyanate is liquid at room temperature.
- Suitable polyisocyanates are well known in the art.
- the polyol component may be any suitable for the manufacture of polyurethanes and includes polyester-polyols, polyester-amide polyols, polyether-polyols, polythioetherpolyols, polycarbonate polyols, polyacetal polyols, polyolefin polyols polysiloxane polyols, dispersions or solutions of addition or condensation polymers in polyols of the types described above, often referred to as "polymer" polyols.
- polyester-polyols polyester-amide polyols
- polyether-polyols polythioetherpolyols
- polycarbonate polyols polyacetal polyols
- polyolefin polyols polysiloxane polyols dispersions or solutions of addition or condensation polymers in polyols of the types described above, often referred to as "polymer" polyols.
- a mixture of polyols is used to manufacture polyurethane having particular physical properties.
- the polyol or polyols is selected to have a molecular weight, backbone type and hydroxy functionality which is tailored to the requirements of the formulator.
- the polyol includes a chain extender, which is often a relatively short-chain diol such as 1 ,4-butane diol or diethylene glycol or a low molecular weight polyethylene glycol.
- chain extender in commercial use, such as diamines, e.g. MOCA (4,4-methylene bis (2-chloroaniline)) may also be used.
- Suitable polyols include the polyalkylene ether- and polyester-polyols.
- the polyalkylene ether polyols include the poly(alkylene oxide) polymers such as poly( ethylene oxide) and poly(propylene oxide) polymers and copolymers with terminal hydroxyl groups derived from polyhydric compounds, including diols and triols; for example, among others, ethylene glycol, propylene glycol, 1 ,3-butane diol, 1 ,4-butane diol, 1 ,6-hexane diol, neopentyl glycol, diethylene glycol, dipropylene glycol, pentaerythritol, glycerol, diglycerol, trimethylol propane and like low molecular weight polyols.
- High molecular weight polyether polyol may be used. Also, mixtures of high molecular weight polyether polyols such as mixtures of di- and tri-functional materials optionally with lower molecular weight or different chemical composition materials may be used.
- Useful polyester polyols include polylactones, e.g.
- polycaprolactone and those produced by reacting a dicarboxylic acid (which may be an aliphatic or aromatic dicarboxylic acid or anhydride) with an excess of a diol, for example, adipic acid with ethylene glycol or butanediol, terephthalic acid or anhydride with ethylene glycol or butane diol, or by reacting a lactone with an excess of a diol such as reacting caprolactone with propylene glycol.
- a dicarboxylic acid which may be an aliphatic or aromatic dicarboxylic acid or anhydride
- a diol for example, adipic acid with ethylene glycol or butanediol, terephthalic acid or anhydride with ethylene glycol or butane diol
- a lactone with an excess of a diol such as reacting caprolactone with propylene glycol.
- Compounds additional to the polyisocyanate, polyol, and catalyst(s) may be present in the polyurethane reaction mixture.
- Such compounds include release agents, fillers, colourants, cross-linkers, chain extenders, blowing agents, fungicides, waxes, impact modifiers, surfactants, plasticisers, water, coupling agents and fire retardants. This list is not exhaustive. The invention will be further described in the following examples.
- Tetra-n-propoxy zirconium in n-propanol solution 14Og, 0.316 moles was placed in a rotary evaporator and 2-ethyl-1-hexanol (2-EHA) (82g, 0.63 moles) was added , followed by N 1 N- diethylacetoacetamide (DEAA) (99.4g, 0.63 moles). The mixture was stirred for 15-20 minutes at 70 0 C , then distilled under vacuum to remove all free n-propanol (111g). NMR analysis indicated a 100% product of Zr(O-CH 2 CH 2 (C 2 H 5 )C 4 Hg) 2 (OC(CH 3 )CHCON(C 2 H5)2)2.
- N,N-diethylacetoacetamide (4 moles, 629g) was slowly added to a solution of zirconium(IV) propoxide (1 mole, 323g) in 1-propanol (2 moles, 12Og) at ambient temperature. The mixture was then stirred for an additional 15 minutes at 45°C before excess 1-propanol (5 moles, 30Og) is distilled off under reduced pressure at a temperature of 60 to 70 0 C. The resulting product contains Zr(OC(CH 3 )CHCON(C 2 H 5 ) 2 ) 4 (1mole) and approx 1 mole of 1-propanol. The propanol may be completely removed by recrystallising solid Zr(DEAA) 4 from toluene solution using heptane.
- Example 3 N,N-diethylacetoacetamide (60 moles, 9.4 kg) was slowly added to a solution of zirconium(IV) propoxide (10 moles, 3.2kg) in 1 -propanol (20 moles, 1.2 kg) at ambient temperature. The mixture was then stirred for an additional 15 minutes at 45°C and all 1-propanol (48.6 moles, 2.9 kg) is distilled off under reduced pressure at a temperature of 60 to 70 0 C. The resulting product contains Zr(OC(CH 3 )CHCON(C 2 H 5 ) 2 ) 4 + free N,N-diethylacetoacetamide at a ratio of 1 mole : 2 moles.
- Tetra-n-propoxy zirconium in n-propanol solution 90.8g, 0.205 moles was placed in a rotary evaporator and tert-butanol (30.3g, 0.41 moles) was added, followed by DEAA (64.5g, 0.41 moles). The mixture was stirred for 15-20 minutes at 70 0 C, then distilled under vacuum to remove all free n-propanol (73g). The resulting product contains Zr(O-C(CH 3 ) 3 ) 2 (OC(CH 3 )CHCON(C 2 H 5 ) 2 ) 2 .
- Example 5 The catalysts of Examples 1 and 4 were used in a polyurethane casting formulation. 7Og of polyol (commercial mixture of a primary and secondary polyol) was placed in a speed mixer cup, mixed with the catalyst (based on polyol 3% or 5%), then mixed with 72.16 g of polyisocyanate prepolymer (DesmodurTM W, aliphatic isocyanate ( methylene bis(4-cyclohexyl isocyanate)) for 10 seconds. A portion of the mixture was then poured onto a surface at room temperature; the rest (approx 135 g) was left in the beaker also at room temperature (about 20 - 25 0 C). The gel time (time to no string) and tack free time was measured. The results are shown in Table 1.
- the faster gel time and tack-free time in the beaker is due to the retention of heat from the exothermic reaction between the isocyanate and the polyol.
- the heat can dissipate more easily because the coating is relatively thin compared with the mass in the beaker.
- the catalyst made in Example 2 was used in the preparation of a rigid foam using a commercial polyol/polyisocyanate system.
- the polyol (45g) was placed in a mixer cup with a blowing catalyst (bis(dimethylaminoethyl)ether (DMEA)) (0.27g) and the catalyst of the invention, mixed for 10 seconds and then an isocyanate (45g) was added.
- DMEA bis(dimethylaminoethyl)ether
- the mixture was placed in a beaker and the cream-time, string-time, time till the foam finished rising and tack-free time was observed.
- DMEA bis(dimethylaminoethyl)ether
- a commercial polyol (6000 MW) was mixed with the catalyst of Example 1 and then with a plasticiser / polyisocyanate mixture. The mixture was mixed a high speed for 10 seconds and left to cure at room temperature. A comparison using a commercial mercury-based gelling catalyst (ThorcatTM 535) was also run. The results are shown in Table 3.
- VERTECTM NPZ tetra-n-propoxy zirconium in n-propanol (443g, 1 mole of metal) was placed into a reaction flask purged with nitrogen, fitted with a stirrer, thermometer, and condenser and mounted in a water bath. N,N-diethylacetoacetamide (314.42g, 2 mole) was added to the reactor via a dropping funnel whilst stirring and an exothermic reaction could be observed. N-Propanol (NPA) (225.65g, 3.76 mole) was removed form the product, Zr(DEAA) 2 (NPA) 2 , under reduced pressure (70°C/30"Hg).
- VERTECTM NPZ (443g, 1mole) was placed into a reaction flask purged with nitrogen, fitted with a stirrer, thermometer, and condenser and mounted in a water bath.
- N,N-diethylacetoacetamide (628.84g, 4 mole) was added to the reactor via a dropping funnel whilst stirring and an exothermic reaction could be observed.
- Diethylene glycol (DEG) 106.12g, 1mole
- N-Propanol (354g, 5.9mole) was removed form the product, Zr(DEAA) 4 + DEG, under reduced pressure (70°C/30"Hg).
- VERTECTM NPZ (100.0Og, 0.2272 mol) was placed into a reaction flask, fitted with a condenser and mounted in a temperature controlled water bath. While spinning the flask, N 1 N- diethylacetoacetamide (71.46g, 0.4544 mol) was added to the reactor via a dropping funnel, this was left to blend for IOmins at which point a slight exotherm was noticed. Then 1 ,3-propanediol (17.3Og, 0.2272mol) was added drop-wise to the reactor and blended for a further IOmins. N-propanol (68.29g, 1.14mol) was removed from the product, Zr(DEAA) 2 (1 ,3-propanediol), under reduced pressure (87°C/29" Hg). Example 11 Shelf life tests
- 0.1 % catalyst was added to a commercial polyester polyol, mixed and allowed to age at 40 0 C for 0, 4 and 7 days before reacting the polyol containing the catalyst with a commercial modified MDI polyisocyanate. The formulation was then poured into a preheated aluminium dish and allowed to cure at 80 0 C during which time the hardness was measured at intervals up to one hour. The results are shown in Table 4.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Polyurethanes Or Polyureas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020087002730A KR101319112B1 (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
AU2006264653A AU2006264653B2 (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
JP2008520010A JP5436855B2 (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compounds, catalysts and their use for polyurethane production |
US11/994,704 US8586696B2 (en) | 2005-07-04 | 2006-07-04 | Zirconium compound, catalyst and its use for polyurethane manufacture |
EP06744367.1A EP1899061B1 (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
CN2006800281649A CN101232943B (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and use for polyurethane manufacture |
CA2613743A CA2613743C (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
BRPI0612399-6A BRPI0612399A2 (en) | 2005-07-04 | 2006-07-04 | process for manufacturing a polyurethane, composition, and catalyst compound |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB0513616.3A GB0513616D0 (en) | 2005-07-04 | 2005-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
GB0513616.3 | 2005-07-04 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007003966A1 true WO2007003966A1 (en) | 2007-01-11 |
Family
ID=34856578
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB2006/050187 WO2007003966A1 (en) | 2005-07-04 | 2006-07-04 | Novel zirconium compound, catalyst and its use for polyurethane manufacture |
Country Status (10)
Country | Link |
---|---|
US (1) | US8586696B2 (en) |
EP (1) | EP1899061B1 (en) |
JP (1) | JP5436855B2 (en) |
KR (1) | KR101319112B1 (en) |
CN (1) | CN101232943B (en) |
AU (1) | AU2006264653B2 (en) |
BR (1) | BRPI0612399A2 (en) |
CA (1) | CA2613743C (en) |
GB (1) | GB0513616D0 (en) |
WO (1) | WO2007003966A1 (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007119078A1 (en) * | 2006-04-13 | 2007-10-25 | Johnson Matthey Plc | Adhesion promoting compound |
WO2011051246A1 (en) * | 2009-10-28 | 2011-05-05 | Bayer Materialscience Ag | Catalysts and use of same |
WO2011098781A1 (en) * | 2010-02-11 | 2011-08-18 | Johnson Matthey Plc | Method of preparing a polymer and compositions therefor |
WO2011098780A2 (en) | 2010-02-11 | 2011-08-18 | Johnson Matthey Plc | Composition and method of preparation |
US8318830B2 (en) | 2007-10-17 | 2012-11-27 | Basf Se | Photolatent catalysts based on organometallic compounds |
US20140343226A1 (en) * | 2011-12-12 | 2014-11-20 | Sika Technology Ag | Bismuth-containing catalyst for polyurethane compositions |
EP2791154B1 (en) * | 2011-12-12 | 2016-08-31 | Sika Technology AG | Dioxomolybdenum(vi) complexes as catalysts for polyurethane compositions |
US9593196B2 (en) | 2011-12-12 | 2017-03-14 | Sika Technology Ag | Zinc(II) complex compounds as catalysts for polyurethane compositions |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BRPI0810304B1 (en) * | 2007-05-23 | 2021-02-02 | Huntsman International Llc | process for the production of lignocellulosic composite articles |
US20110256314A1 (en) * | 2009-10-23 | 2011-10-20 | Air Products And Chemicals, Inc. | Methods for deposition of group 4 metal containing films |
EP2604617A1 (en) * | 2011-12-12 | 2013-06-19 | Sika Technology AG | Iron(III) complexes as catalysts for polyurethane compositions |
EP2604618A1 (en) * | 2011-12-12 | 2013-06-19 | Sika Technology AG | Metal complexes as catalysts for polyurethane compositions |
TW201527422A (en) * | 2013-10-15 | 2015-07-16 | Lubrizol Advanced Mat Inc | Thermoplastic polyurethanes made with tin-free catalysts |
CN106986976A (en) * | 2016-01-20 | 2017-07-28 | 新纶科技(常州)有限公司 | A kind of carbon monoxide-olefin polymeric |
US20200248041A1 (en) * | 2017-09-26 | 2020-08-06 | Sika Technology Ag | Activator for accelerated adhesion development |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5846897A (en) | 1997-03-19 | 1998-12-08 | King Industries, Inc. | Zirconium urethane catalysts |
WO2004044027A1 (en) | 2002-11-13 | 2004-05-27 | Johnson Matthey Plc | Catalyst and process |
WO2005058996A1 (en) * | 2003-12-18 | 2005-06-30 | Johnson Matthey Plc | Catalyst and method of making polyurethane materials |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1444933A (en) | 1973-04-03 | 1976-08-04 | Ici Ltd | Emulsions of organic isocyanates |
GB9111559D0 (en) | 1991-05-29 | 1991-07-17 | Ici Plc | Polyisocyanate composition |
GB9117070D0 (en) | 1991-08-08 | 1991-09-25 | Ici Plc | Polyisocyanate compositions |
US5902835A (en) * | 1998-05-28 | 1999-05-11 | Air Products And Chemicals, Inc. | Group IVB metal blowing catalyst compositions for the production of polyurethane foams |
-
2005
- 2005-07-04 GB GBGB0513616.3A patent/GB0513616D0/en not_active Ceased
-
2006
- 2006-07-04 AU AU2006264653A patent/AU2006264653B2/en not_active Ceased
- 2006-07-04 KR KR1020087002730A patent/KR101319112B1/en active IP Right Grant
- 2006-07-04 CN CN2006800281649A patent/CN101232943B/en not_active Expired - Fee Related
- 2006-07-04 WO PCT/GB2006/050187 patent/WO2007003966A1/en active Application Filing
- 2006-07-04 CA CA2613743A patent/CA2613743C/en not_active Expired - Fee Related
- 2006-07-04 US US11/994,704 patent/US8586696B2/en not_active Expired - Fee Related
- 2006-07-04 BR BRPI0612399-6A patent/BRPI0612399A2/en not_active Application Discontinuation
- 2006-07-04 EP EP06744367.1A patent/EP1899061B1/en not_active Not-in-force
- 2006-07-04 JP JP2008520010A patent/JP5436855B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5846897A (en) | 1997-03-19 | 1998-12-08 | King Industries, Inc. | Zirconium urethane catalysts |
WO2004044027A1 (en) | 2002-11-13 | 2004-05-27 | Johnson Matthey Plc | Catalyst and process |
WO2005058996A1 (en) * | 2003-12-18 | 2005-06-30 | Johnson Matthey Plc | Catalyst and method of making polyurethane materials |
Non-Patent Citations (2)
Title |
---|
PATIL ET AL., J. MATER CHEM, vol. 13, 2003, pages 2177 - 2184 |
PATIL, U. ET AL: "Synthesis and structure of mixed isopropoxide-beta-ketoester and beta-ketoamide zirconium complexes: Potential precursor for MOCVD or ZrO2", JOURNAL OF MATERIALS CHEMISTRY, vol. 13, no. 9, 2003, pages 2177 - 2184, XP002402040 * |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007119078A1 (en) * | 2006-04-13 | 2007-10-25 | Johnson Matthey Plc | Adhesion promoting compound |
US8722811B2 (en) | 2006-04-13 | 2014-05-13 | Dorf Ketal Chemicals (India) Pvt. Ltd | Adhesion promoting compound |
US8318830B2 (en) | 2007-10-17 | 2012-11-27 | Basf Se | Photolatent catalysts based on organometallic compounds |
WO2011051246A1 (en) * | 2009-10-28 | 2011-05-05 | Bayer Materialscience Ag | Catalysts and use of same |
GB2490450A (en) * | 2010-02-11 | 2012-10-31 | Johnson Matthey Plc | Glycerol complex composition and method of preparation |
GB2490288A (en) * | 2010-02-11 | 2012-10-24 | Johnson Matthey Plc | Method of preparing a polymer and compositions therefor |
WO2011098780A3 (en) * | 2010-02-11 | 2011-12-29 | Johnson Matthey Plc | Glycerol complex composition and method of preparation |
WO2011098780A2 (en) | 2010-02-11 | 2011-08-18 | Johnson Matthey Plc | Composition and method of preparation |
WO2011098781A1 (en) * | 2010-02-11 | 2011-08-18 | Johnson Matthey Plc | Method of preparing a polymer and compositions therefor |
US20140343226A1 (en) * | 2011-12-12 | 2014-11-20 | Sika Technology Ag | Bismuth-containing catalyst for polyurethane compositions |
EP2791154B1 (en) * | 2011-12-12 | 2016-08-31 | Sika Technology AG | Dioxomolybdenum(vi) complexes as catalysts for polyurethane compositions |
US9593196B2 (en) | 2011-12-12 | 2017-03-14 | Sika Technology Ag | Zinc(II) complex compounds as catalysts for polyurethane compositions |
RU2650115C2 (en) * | 2011-12-12 | 2018-04-09 | Сикэ Текнолоджи Аг | Complex zinc (ii) compounds as catalysts for polyurethane compositions |
CN108752550A (en) * | 2011-12-12 | 2018-11-06 | Sika技术股份公司 | Zinc (II) complex compound as the catalyst for urethane composition |
US10246545B2 (en) * | 2011-12-12 | 2019-04-02 | Sika Technology Ag | Bismuth-containing catalyst for polyurethane compositions |
Also Published As
Publication number | Publication date |
---|---|
KR101319112B1 (en) | 2013-10-17 |
JP5436855B2 (en) | 2014-03-05 |
BRPI0612399A2 (en) | 2011-02-22 |
US20080312402A1 (en) | 2008-12-18 |
KR20080034450A (en) | 2008-04-21 |
EP1899061A1 (en) | 2008-03-19 |
AU2006264653A1 (en) | 2007-01-11 |
JP2008545058A (en) | 2008-12-11 |
CA2613743C (en) | 2013-09-24 |
US8586696B2 (en) | 2013-11-19 |
EP1899061B1 (en) | 2014-08-13 |
CN101232943A (en) | 2008-07-30 |
AU2006264653B2 (en) | 2011-08-04 |
GB0513616D0 (en) | 2005-08-10 |
CN101232943B (en) | 2013-02-13 |
CA2613743A1 (en) | 2007-01-11 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2006264653B2 (en) | Novel zirconium compound, catalyst and its use for polyurethane manufacture | |
WO2005058996A1 (en) | Catalyst and method of making polyurethane materials | |
CA2687836C (en) | Water-stable catalysts for polyurethane manufacture | |
JP3655773B2 (en) | Group IVB metal foam catalyst composition for the production of polyurethane foam | |
US20100311937A1 (en) | Method and catalyst for the manufacture of a polyurethane | |
US20060020099A1 (en) | Catalyst and process | |
US20060189478A1 (en) | Organometallic catalyst compositions and process for polyurethane manufacture using said catalyst | |
US20040147706A1 (en) | Organometallic compositons |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2613743 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2006744367 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2008520010 Country of ref document: JP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 234/DELNP/2008 Country of ref document: IN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2006264653 Country of ref document: AU Ref document number: 200680028164.9 Country of ref document: CN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020087002730 Country of ref document: KR |
|
ENP | Entry into the national phase |
Ref document number: 2006264653 Country of ref document: AU Date of ref document: 20060704 Kind code of ref document: A |
|
WWP | Wipo information: published in national office |
Ref document number: 2006264653 Country of ref document: AU |
|
WWP | Wipo information: published in national office |
Ref document number: 2006744367 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11994704 Country of ref document: US |
|
ENP | Entry into the national phase |
Ref document number: PI0612399 Country of ref document: BR Kind code of ref document: A2 Effective date: 20080104 |