Transition metal chelate polyol blends for use in polyurethane polymers - Patent Application 20070122999

Abstract

The present disclosure provides a liquid transition metal chelate polyol blend that can be used in isocyanate-reactive compositions and reaction mixtures for forming polyurethane polymers. The liquid transition metal chelate polyol blend includes a polyol, a transition metal compound having a transition metal ion, and a chelating agent having a nitrogen-based chelating moiety, wherein the liquid transition metal chelate polyol blend has a molar ratio of nitrogen to transition metal ion (moles of nitrogen:moles of transition metal ion) in the nitrogen-based chelating moiety of 8:1 to 1:1.

Description

[Technical Field]

[0001] The present disclosure relates generally to polyurethane polymers, and more particularly to polyurethane polymers with improved burn / smoke behavior. [Background technology]

[0002] Polyurethane rigid (PUR) foam has been used in construction as a high-performance insulation material since the 1960s. Continued technological development in Europe and the United States has led to a new generation of products called polyisocyanurate rigid (PIR) foam. Both PUR and PIR are polyurethane polymer foams made from two reactants: an isocyanate (e.g., methyldiphenyldiisocyanate, MDI) and a polyol. In PUR, the isocyanate and polyol are implemented in a nearly balanced ratio relative to equivalents, whereas in the production of PIR, an excess of isocyanate is used. The isocyanate partially reacts with itself, and the resulting PIR is a highly crosslinked synthetic material with a ring-like isocyanurate structure. The advanced linkage and ring structure ensure the high thermal stability of rigid PIR foam. PIR also has excellent thermal and dimensional stability.

[0003] PIR foams also feature very good fire resistance, thanks to their inherent charring behavior, which in turn is related to the excellent thermal stability of their isocyanurate chemical structure. To further enhance char formation, phosphorus-based flame retardants are typically added. When building products, such as insulating transition metal panels or insulation boards, are exposed to fire, the insulating PIR core rapidly forms a cohesive char, which helps protect the underlying material. This means that only a limited portion of the available combustible insulating material is exposed to the fire and actually contributes in terms of heat release and smoke.

[0004] The fire behavior of combustible thermosetting materials is a complex issue. As an example, halogenated flame retardants are highly effective at reducing heat release, but can worsen smoke opacity. Dow Patent Publication US2014 / 0206786 A1 describes the use of triethyl phosphate (TEP) as a smoke suppression additive compared to traditional halogenated flame retardants such as tris-(2-chloroisopropyl)phosphate (TCPP). Furthermore, as is well known, the composition of combustion effluent (even more so than the material itself) is highly dependent on fire conditions, particularly temperature, geometry, and ventilation, including oxygen availability. As noted above, even if the inherent charring behavior of polyisocyanurates limits and / or delays the amount of polymer burning (thus limiting and / or delaying heat and smoke release), it is still desirable to further modify the combustion / burning behavior, thereby reducing smoke opacity and smoke toxicity as much as possible.

[0005] Polyurethanes are also widely used in numerous coating, adhesive, sealant, and elastomer ("CASE") applications, as well as flexible polyurethane foams. It would be desirable to further modify the flammability / burning behavior of polyurethanes utilized as coatings, adhesives, sealants, elastomers, and flexible foams, thus reducing smoke opacity and smoke toxicity to the greatest extent possible, and optionally modifying other attributes such as antifungal, antibacterial, odor resistance, hardness, soundproofing, and abrasion resistance. Summary of the Invention

[0006] The present disclosure provides isocyanate-reactive compositions for forming polyurethane polymers, and liquid transition metal chelate polyol blends that can be used in reaction mixtures containing the isocyanate-reactive compositions. The polyurethane polymers and polyurethane polymer foams of the present disclosure can have improved smoke behavior with respect to the release of hydrogen cyanide (HCN) and carbon monoxide (CO) during a thermal decomposition event (e.g., a fire).

[0007] The liquid transition metal chelate polyol blend of the present disclosure includes a polyol, a transition metal compound having a transition metal ion, and a chelating agent having a nitrogen-based chelating moiety, wherein 0.05 weight percent (wt%) to 10.0 wt% of the transition metal ion is present from the transition metal compound, the wt% being based on the total weight of the liquid transition metal chelate polyol blend, and the liquid transition metal chelate polyol blend has 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams (g) of polyol in the liquid transition metal chelate polyol blend, and a ratio of 8.0:1.0 to 1.0:1.0. The nitrogen-based chelating moiety has a molar ratio of nitrogen to transition metal ion (moles nitrogen:moles transition metal ion), and in various embodiments, the molar ratio of nitrogen to transition metal ion (moles nitrogen:moles transition metal ion) in the nitrogen-based chelating moiety is preferably 4.0:1.0 to 1.0:1.0 (moles nitrogen:moles transition metal ion), more preferably 2.8:1.0 to 1.0:1.0, and most preferably 2.0:1.0 to 1.0:1.0. In various embodiments, the chelating agent is soluble in the polyol of the transition metal chelate polyol blend, and the liquid transition metal chelate polyol blend has from 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelate moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, preferably from 0.003 to 0.60 moles of nitrogen in the nitrogen-based chelate moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, more preferably from 0.006 to 0.40 moles of nitrogen in the nitrogen-based chelate moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, and most preferably from 0.01 to 0.20 moles of nitrogen in the nitrogen-based chelate moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend.

[0008] In various embodiments, the polyol is an aromatic polyester polyol having aromatic moieties comprising 5 weight percent (wt%) to 60 wt% of the total weight of the aromatic polyester polyol. In various embodiments, the polyester polyol is preferably an aromatic polyester polyol having aromatic moieties comprising 10 wt% to 40 wt% of the total weight of the aromatic polyester polyol. In various embodiments, the polyester polyol is most preferably an aromatic polyester polyol having aromatic moieties comprising 10 wt% to 20 wt% of the total weight of the aromatic polyester polyol.

[0009] In embodiments, the transition metal compound is selected from the group consisting of a transition metal carboxylate, a transition metal salt, a transition metal coordination compound, and combinations thereof. Preferably, the transition metal compound is a transition metal carboxylate. The transition metal ion is selected from the group consisting of copper, zinc, silver, iron, manganese, cobalt, nickel, zirconium, cadmium, mercury, palladium, titanium, vanadium, and combinations thereof. More preferably, the transition metal ion is selected from the group consisting of copper, zinc, silver, iron, manganese, cobalt, nickel, zirconium, and combinations thereof. Most preferably, the transition metal ion is selected from the group consisting of copper, zinc, iron, manganese, cobalt, nickel, zirconium, and combinations thereof. In embodiments, the transition metal compound may be selected from the group consisting of copper(II) 2-ethylhexanoate (CuEH), copper(I) acetate, copper(II) acetate, copper(II) acetate monohydrate (Cu(OAc)2H2O), copper(II) propionate, copper(II) isobutyrate (Cu(i-Bu)2), cobalt(II) acetate, nickel(II) acetate, silver(I) acetate, and combinations thereof.

[0010] In embodiments, the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of a diamine chelating moiety, a triamine chelating moiety, a tetraamine chelating moiety, and combinations thereof. Preferably, the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of 2,2'-bipyridine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, 2-[[2-(dimethylamino)ethyl]methylamino]ethanol, 1-[bis[3-(dimethylamino)propyl]amino-2-propanol], 1,2-ethanediamine polymers with methyloxirane, and combinations thereof.

[0011] The present disclosure also provides isocyanate-reactive compositions comprising the liquid transition metal chelate polyol blends provided herein, which can be used to form polyurethane polymers. In various embodiments, the isocyanate-reactive composition can further comprise a polyol different from the polyol in the liquid transition metal chelate polyol blend, where the isocyanate-reactive composition comprises 0.1 to 100 weight percent (wt%) (wt% based on the total weight of the isocyanate-reactive composition) of the liquid transition metal chelate polyol blend and up to 99.9% of a polyol different from the polyol in the liquid transition metal chelate polyol blend to form an isocyanate-reactive composition for polyurethane polymers. In additional embodiments, the isocyanate-reactive compositions of the present disclosure can optionally include a polyol (different from the polyol in the liquid transition metal chelate polyol blend), a phosphorus flame retardant, a catalyst, a blowing agent, water, a surfactant, or a combination thereof, and the isocyanate-reactive composition can be used to form polyurethane polymer foams. For example, the isocyanate-reactive compositions provided herein can include a blowing agent and a surfactant for use in forming polyurethane polymer foams.

[0012] In various embodiments, the isocyanate-reactive composition of the present disclosure may further comprise 0.1 wt. % to 7.0 wt. % phosphorus selected from the group consisting of phosphates, phosphonates, phosphinates, phosphites, and combinations thereof from flame retardant compounds, preferably halogen-free flame retardant compounds, where the wt. % of phosphorus is based on the total weight of the isocyanate-reactive composition. In various embodiments, the isocyanate-reactive composition of the present disclosure may comprise 0.05 wt. % to 10.0 wt. % transition metal ions from a liquid transition metal chelate polyol blend, where the wt. % of transition metal ions is based on the total weight of the liquid transition metal chelate polyol blend. In such embodiments, the isocyanate-reactive composition may have a molar ratio of transition metal ions to phosphorus (moles transition metal ions:moles phosphorus) of 0.05:1 to 5:1.

[0013]

[0010] Embodiments of the present disclosure also provide a reaction mixture for forming a polyurethane polymer, the reaction mixture comprising an isocyanate compound having an isocyanate moiety and an isocyanate-reactive composition provided herein, wherein the polyol comprises hydroxyl moieties, the reaction mixture having a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1. In additional embodiments, the reaction mixture can be used to form a polyurethane polymer foam, the reaction mixture comprising an isocyanate compound having an isocyanate moiety and an isocyanate-reactive composition provided herein, wherein the polyol comprises hydroxyl moieties, the reaction mixture having a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1. In additional embodiments, the reaction mixture can further comprise a compound selected from the group consisting of water, a catalyst, a surfactant, a blowing agent, or a combination thereof.

[0014] The present disclosure provides a process for preparing a liquid transition metal chelate polyol blend, the process including providing a polyol, providing a chelating agent having a nitrogen-based chelating moiety, and providing a transition metal compound having a transition metal ion. The process further includes blending the polyol, the chelating agent, and the transition metal compound to form a liquid transition metal chelate polyol blend having 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend. In various embodiments, the liquid transition metal chelate polyol blend has a molar ratio of nitrogen to transition metal ion (moles of nitrogen:moles of transition metal ion) in the nitrogen-based chelating moiety of 8.0:1.0 to 1.0:1.0.

[0015] The present disclosure also provides processes for preparing a reaction mixture for producing a polyurethane polymer, the process comprising providing an isocyanate-reactive composition provided herein, providing an isocyanate compound having isocyanate moieties, and combining the isocyanate-reactive composition with the isocyanate compound to form a reaction mixture having a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1. In various embodiments, combining the isocyanate-reactive composition with the isocyanate compound can further comprise combining water, a catalyst, a surfactant, a flame retardant, a blowing agent, an additive, or a combination thereof with the reaction mixture to form a polyurethane polymer, including a polyurethane foam. DETAILED DESCRIPTION OF THE INVENTION

[0016] The present disclosure provides isocyanate-reactive compositions for forming polyurethane polymers, and liquid transition metal chelate polyol blends that can be used in reaction mixtures containing the isocyanate-reactive compositions. The polyurethane polymers and polyurethane foams of the present disclosure can have improved smoke behavior with respect to the release of hydrogen cyanide (HCN) and carbon monoxide (CO) during a thermal decomposition event (e.g., a fire).

[0017] The liquid transition metal chelate polyol blend of the present disclosure includes a polyol, a transition metal compound having a transition metal ion, and a chelating agent having a nitrogen-based chelating moiety, wherein 0.05 weight percent (wt%) to 10.0 wt% of the transition metal ion is present from the transition metal compound, the wt% being based on the total weight of the liquid transition metal chelate polyol blend, and the liquid transition metal chelate polyol blend has 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams (g) of polyol in the liquid transition metal chelate polyol blend. In various embodiments, the liquid transition metal chelate polyol blend has a molar ratio of nitrogen to transition metal ion (moles nitrogen:moles transition metal ion) in the nitrogen-based chelate moiety of 8.0:1.0 to 1.0:1.0, and in various embodiments, the molar ratio of nitrogen to transition metal ion in the nitrogen-based chelate moiety is preferably 4.0:1.0 to 1.0:1.0 (moles nitrogen:moles transition metal ion), more preferably 2.8:1.0 to 1.0:1.0, and most preferably 2.0:1.0 to 1.0:1.0. As used herein, a liquid transition metal chelate polyol blend is in a liquid state at pressures of 80 to 25,000 KP and in a liquid state at temperatures above -10° C. and below 80° C., preferably below 60° C., more preferably below 40° C., and most preferably below 25° C. As used herein, a liquid transition metal chelate polyol blend contains no or a nominal amount of transition metal compound particles / solids such that the nominal amount of transition metal compound particles / solids is less than 0.10 weight percent (wt %), preferably less than 0.01 wt %, and more preferably less than 0.001 wt %, based on the weight of the liquid transition metal chelate polyol blend.

[0018] In various embodiments, the polyol in the transition metal chelate polyol blend is selected from the group consisting of polyester polyols, polyether polyols, polycarbonate polyols, polyether carbonate polyols, and combinations thereof. In some embodiments, the polyol is preferably a polyester polyol. In other embodiments, the polyol is preferably a polyether polyol.

[0019] The polyester polyols of the present disclosure can be homopolymers, random copolymers, block copolymers, segmented copolymers, and capped products that may contain initiator residues in the case of ring-opened polyester polyols. The polyester polyols can be aromatic, aliphatic, or cycloaliphatic, including hydrogenated products thereof. In various embodiments, the polyester polyols are aromatic polyester polyols having aromatic moieties comprising 5 weight percent (wt%) to 60 wt% of the total weight of the aromatic polyester polyol. In various embodiments, the polyester polyols are preferably aromatic polyester polyols having aromatic moieties comprising 10 wt% to 40 wt% of the total weight of the aromatic polyester polyol. In various embodiments, the polyester polyols are more preferably aromatic polyester polyols having aromatic moieties comprising 10 wt% to 20 wt% of the total weight of the aromatic polyester polyol. As used herein, an "aromatic moiety" refers to at least one cyclically conjugated molecular moiety in the form of a planar unsaturated ring of carbon atoms, covalently bonded to an isocyanate-reactive compound. The planar unsaturated ring of carbon atoms can have at least six carbon atoms. For illustrative purposes, C 12 H 14 The isocyanate-reactive compound bis(2-hydroxyethyl) terephthalate having a molecular formula of O6, and a formula weight of 254.2 grams / mole, and having a corresponding aromatic content of CH4 having a corresponding formula weight of 76.1 grams / mole, the aromatic portion of bis(2-hydroxyethyl) terephthalate being 29.9 weight percent (wt%).

[0020] Liquid polyester polyols can have low to medium number average molecular weights ranging from 100 to 5,000, preferably 200 to 2,500, more preferably 300 to 1,000, and most preferably 350 to 750. Number average molecular weights can be measured using end group analysis or gel permeation chromatography (GPC), as known in the art. Liquid polyester polyols can also have a number-averaged isocyanate-reactive group functionality (e.g., hydroxyl groups) per molecule of 1.8 to 4, such as 2 to 3, where each value is an average number. A variety of chemical structures can constitute liquid polyester polyols, with at least one requirement being the presence of at least two hydroxyl groups (i.e., diols) and that the liquid polyester polyol be in a liquid state at pressures of 80 to 25,000 KPa and at temperatures above -10°C and below 80°C.

[0021] In embodiments, the monomers used to form the liquid polyester polyols may include polyhydric alcohols, such as dihydric alcohols, trihydric alcohols, and / or higher hydrated alcohols, and polybasic acids, such as dibasic and / or tribasic acids, such as carboxylic acids and / or polycarboxylic anhydrides, or corresponding polycarboxylic acid esters, cyclic esters, or mixtures thereof, of lower alcohols, which react as known in the art to form the liquid polyester polyol reaction product. Exemplary polyhydric alcohols include, but are not limited to, ethylene glycol, propylene glycol-(1,2) and -(1,3), butylene glycol-(1,4) and -(2,3), hexanediol-(1,6), octanediol-(1,8), neopentyl glycol, cyclohexanedimethanol (1,4-bis-hydroxy-methylcyclohexane and other isomers), 2-methyl-1,3-propane-diol, glycerol, trimethylolpropane, hexanetriol-(1,2,6), butanetriol-(1,2,4), trimethylolethane, pentaerythritol, quinitol, mannitol and sorbitol, methyl glycoside, diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, dipropylene glycol, polypropylene glycol, dibutylene glycol, and polybutylene glycol. Polyhydric alcohols can also include polycarbonate polyols such as the reaction products of diols such as propanediol-(1,3), butanediol-(1,4) and / or hexanediol-(1,6), diethylene glycol, triethylene glycol, or tetraethylene glycol with diaryl carbonates such as diphenyl carbonate, dialiphatic carbonates such as dimethyl carbonate, or phosgene, or reaction products from the reaction of oxirane with carbon dioxide.

[0022] The polybasic acid may be aliphatic, cycloaliphatic, aromatic, and / or heterocyclic, and may be substituted, for example, by halogen atoms, and / or unsaturated. Suitable polybasic acids, anhydrides, and polycarboxylic acid esters of lower alcohols include, but are not limited to, succinic acid, adipic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, terephthalic acid, trimellitic acid, phthalic anhydride, trimellitic anhydride, tetrahydrophthalic anhydride, hexahydrophthalic anhydride, tetrachlorophthalic anhydride, endomethylenetetrahydrophthalic anhydride, glutaric anhydride, maleic acid, maleic anhydride, fumaric acid, dimeric and trimeric fatty acids such as oleic acid, optionally mixed with monomeric fatty acids, dimethyl terephthalate, and terephthalic acid bis-glycol esters.

[0023] The cyclic esters may be aliphatic, substituted, for example, by alkyl groups, and / or unsaturated. Suitable cyclic esters include, but are not limited to, ε-caprolactone, d,l-lactide, glycolide, δ-valerolactone, and pivolactone, among others.

[0024] The liquid polyester polyol may be aromatic, aliphatic, or cycloaliphatic, and may include hydrogenated products thereof. Preferred examples of liquid polyester polyols include, but are not limited to, polycaprolactone polyols, polypropiolactone polyols, polyglycolide polyols, polypivolylactone polyols, polyvalerolactone polyols, polyethylene adipate polyols, polypropylene adipate polyols, polybutylene adipate polyols, polyhexamethylene adipate polyols, polyneopentyl adipate polyols, polycyclohexanedimethylene adipate polyols, polyethylene succinate polyols, polypropylene succinate polyols, polybutylene succinate polyols, polyhexamethylene succinate polyols, polyneopentyl succinate polyols, polycyclohexanedimethyl succinate polyols, polyethylene azelate polyols, polypropylene azelate polyols, and the like. polyol, polybutylene azelate polyol, polyhexamethylene azelate polyol, polyneopentyl azelate polyol, polycyclohexanedimethylene azelate polyol, polyethylene sebacate polyol, polypropylene sebacate polyol, polybutylene sebacate polyol, polyhexamethylene sebacate polyol, polyneopentyl sebacate polyol, polycyclohexanedimethylene sebacate polyol, diethylene glycol / terephthalic acid polyol, polyethylene glycol / terephthalic acid polyol, diethylene glycol / phthalic acid or phthalic anhydride polyol, polyethylene glycol / phthalic acid or phthalic anhydride polyol, diethylene glycol / isophthalic acid polyol, polyethylene glycol / isophthalic acid polyol, and copolyester polyols thereof.

[0025] More preferred examples of liquid polyester polyols include polycaprolactone polyols, polyethylene adipate polyols, polypropylene adipate polyols, polybutylene adipate polyols, polyhexamethylene adipate polyols, polycyclohexanedimethylene adipate polyols, polyethylene succinate polyols, polybutylene succinate polyols, diethylene glycol / terephthalic acid polyols, polyethylene glycol / terephthalic acid polyols, diethylene glycol / phthalic acid or phthalic anhydride polyols, polyethylene glycol / phthalic acid or phthalic anhydride polyols, diethylene glycol / isophthalic acid polyols, polyethylene glycol / isophthalic acid polyols, and copolyesters of diethylene glycol and / or polyethylene glycol terephthalate, isophthalate, and / or phthalate, optionally with the use of glycerol and / or trimethylolpropane when an average hydroxyl functionality of greater than 2.0 is desired. More preferred examples of liquid polyester polyols include diethylene glycol / terephthalic acid polyols, polyethylene glycol / terephthalic acid polyols, diethylene glycol / phthalic acid or phthalic anhydride polyols, polyethylene glycol / phthalic acid or phthalic anhydride polyols, diethylene glycol / isophthalic acid polyols, polyethylene glycol / isophthalic acid polyols, and copolyesters of diethylene glycol and / or polyethylene glycol terephthalate, isophthalate, and / or phthalate, optionally with glycerol and / or trimethylolpropane if an average hydroxyl functionality greater than 2.0 is desired. In various embodiments, the polyester polyols may also be uncapped or capped using ethylene oxide (EO) and / or propylene oxide (PO) to provide hydrophilic or hydrophobic structures, as is known in the art.Other examples of liquid polyester polyols include modified aromatic polyester polyols such as those offered under the trademark STEPANPOL PS-2352 (acid number 0.6-1.0 mg KOH / g, hydroxyl number 230-250 mg KOH / g, hydroxyl functionality 2.0, Stepan Company). Liquid polyesters may also contain a proportion of carboxyl end groups. Liquid polyester polyols formed with lactones, such as ε-caprolactone, or hydroxycarboxylic acids, such as 6-hydroxycaproic acid, may also be used.

[0026] Liquid polyether polyols can include those having at least two hydroxyl groups per molecule, such as two or three. They can be prepared, for example, by the polymerization of oxiranes / cyclic esters, such as ethylene oxide, propylene oxide, butylene oxide, styrene oxide, or epichlorohydrin, either by themselves in the presence of BF3, or by the chemical addition of these oxiranes, optionally as a mixture (such as a mixture of ethylene oxide and propylene oxide), to starting components having reactive hydrogen atoms, such as water, ammonia, alcohols, or amines, or sequentially. Examples of suitable starting components include ethylene glycol, propylene glycol-(1,3) or -(1,2), glycerol, trimethylolpropane, 4,4'-dihydroxydiphenylpropane, Novolac, aniline, ethanolamine, or ethylenediamine. Sucrose-based polyether polyols can also be used. In many cases, it is preferred to use polyethers containing a predominant amount of primary OH groups (up to 100% by weight of the OH groups present in the polyether). The polyether polyol or copolyether polyol should have a nominal functionality of at least 2.0. The nominal functionality is preferably 2.5 to 8, more preferably 2.5 to 7, or even 2.5 to 6. The hydroxyl equivalent weight of the polyether polyol or copolyether polyol is at least 85, preferably at least 100, more preferably 150 to 3,200, in some embodiments 250 to 3,000, and in certain embodiments 300 to 2,500. The polyol may also be formed from a blend of a diol and a triol, if such blend includes a blend of the diol and the triol. The diol may have a number average molecular weight (Mn) of 200 to 8,000 grams / mole, and the triol may have an average number molecular weight (Mn) of 250 to 6,500 grams / mole. Other examples of suitable polyether polyols include polymers or copolymers formed with propylene oxide having a hydroxyl equivalent weight of at least 75. The propylene oxide may be 1,3-propylene oxide, but is more commonly 1,2-propylene oxide.In the case of copolymers, the comonomers are other copolymerizable alkylene oxides, such as ethylene oxide, 2,3-butylene oxide, tetrahydrofuran, 1,2-hexane oxide, etc. The copolymers may contain 25% or more, 50% or more, and preferably 75% or more by weight of polymerized propylene oxide, based on the total weight of polymerized alkylene oxides. The copolymers preferably contain 75% or less, especially 50% or less by weight of polymerized ethylene oxide.

[0027] In various embodiments, the polyol may have a hydroxyl number of 10 mg KOH / g to 700 mg KOH / g. In still other embodiments, the polyol may have a hydroxyl number of 20 mg KOH / g to 500 mg KOH / g, or 30 mg KOH / g to 350 mg KOH / g. As used herein, hydroxyl number is the number of milligrams of potassium hydroxide equivalent to the hydroxyl content in one gram of polyol or other hydroxyl compound. The polyol may also have a number average isocyanate-reactive group functionality of 1.8 to 6, such as 2 to 4, or 2.2 to 3.0.

[0028] In various embodiments, the polyether polyols and / or polyester polyols may also be uncapped or capped using ethylene oxide (EO) and / or propylene oxide (PO) as known in the art to provide hydrophilic or hydrophobic structures.

[0029] In various embodiments, the liquid transition metal chelate polyol blend comprises 0.05 weight percent (wt%) to 10.0 wt% transition metal ions from the transition metal compound, where wt% is based on the total weight of the liquid transition metal chelate polyol blend. The liquid transition metal chelate polyol blend may also comprise 0.15 wt% to 6.0 wt% transition metal ions from the transition metal compound, or 0.5 wt% to 3.0 wt% transition metal ions from the transition metal compound, where wt% is based on the total weight of the liquid transition metal chelate polyol blend.

[0030] In an embodiment, the transition metal compound is selected from the group consisting of transition metal carboxylates, transition metal salts, transition metal coordination compounds, and combinations thereof, and the transition metal ion is selected from transition metals in Groups 4, 5, 6, 7, 8, 9, 10, 11, and 12 of Periods 4 and 5 of the Periodic Table (IUPAC Periodic Table of the Elements, November 28, 2016). Preferably, the transition metal compound is a transition metal carboxylate. Preferably, the transition metal ion is selected from the group consisting of copper, zinc, silver, iron, manganese, cobalt, nickel, zirconium, cadmium, mercury, palladium, titanium, vanadium, and combinations thereof. More preferably, the transition metal ion is selected from the group consisting of copper, zinc, silver, iron, manganese, cobalt, nickel, zirconium, and combinations thereof. Most preferably, the transition metal ion is selected from the group consisting of copper, zinc, iron, manganese, cobalt, nickel, and combinations thereof. Examples of transition metal compounds include copper(II) 2-ethylhexanoate, copper(II) acetate, copper(II) acetate monohydrate (Cu(OAc)2H2O), copper(I) acetate, copper butyrate, di-μ-hydroxo-bis[(N,N,N',N'-tetramethylethylenediamine)copper(II)] chloride, zinc stannate, zinc hydroxystannate, zinc(II) acetate, cobalt(II) acetate, nickel(II) acetate, silver(I) acetate, manganese(II) 2-ethylhexanoate, and combinations thereof. Preferably, the transition metal compound is selected from the group consisting of copper(II) 2-ethylhexanoate (CuEH), copper(II) acetate, copper(II) acetate monohydrate (Cu(OAc)2H2O), copper(II) propionate, copper(II) isobutyrate (Cu(i-Bu)2), cobalt(II) acetate, nickel(II) acetate, silver(I) acetate, and combinations thereof.

[0031] In embodiments, the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of a diamine chelating moiety, a triamine chelating moiety, a tetraamine chelating moiety, and combinations thereof. In some embodiments, the chelating agent having a nitrogen-based chelating moiety is selected from a tertiary polyamino compound having at least two tertiary nitrogens connected through a carbon atom. The chelating agent may preferably conform to Formula I: [ka] wherein R1, R2, R3, R4, and R5 are each independently a C1 to C8 alkyl group, an alkoxylate / polyalkoxylate (i.e., —(CHCHRO) where R is H or a C1 to C3 alkyl group and n is an integer from 1 to 10). n -H), and equivalents thereof, wherein x and x' are each independently an integer of 2 or 3, and y is an integer of 0, 1, or 2. More preferably, in Formula I, R1, R2, R3, R4, and R5 are each independently a C1-C3 alkyl group, an alkoxylate / polyalkoxylate as provided above, wherein the alkyl group is C1-C2, and x and x' are each independently an integer of 2 or 3, and y is an integer of 0 or 1. Most preferably, in Formula I, R1, R2, R3, R4, and R5 are each independently a C1-C3 alkyl group, an alkoxylate / polyalkoxylate as provided above, wherein the alkyl group is C1, and x and x' are each independently an integer of 2, and y is an integer of 0 or 1.

[0032] In embodiments, the chelating agent having a nitrogen-based chelating moiety may further have an isocyanate-reactive moiety. Preferred chelating agents having a nitrogen-based chelating moiety are diamines, triamines, and tetraamines, where the amine moiety is a tertiary amine.

[0033] Examples of chelating agents having a diamine chelating moiety as a nitrogen-based chelating moiety include 2,2'-bipyridine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N'-tetraethylethylenediamine, triethylenediamine (1,4-diazabicyclo[2.2.2]octane), N,N'-dimethylaminoethyl-N-methylethanolamine, N,N'-dimethylaminoethylmorpholine, N,N,N',N'-tetramethyl-1,3-butanediamine, N,N'-dimethylpiperazine, methylhydroxyethylpiperazine, N, N,N',N'-tetrakis-(2-hydroxypropyl)ethylenediamine, 2-[[2-(dimethylamino)ethyl]methylamino]ethanol, N,N,N'-trimethyl-N'-hydroxylethyl-bis(aminoethyl)ether; N,N-bis(3-dimethylamino-propyl)-N-isopropanolamine; bis-(dimethylaminopropyl)amino-2-propanol; N,N,N'-trimethylaminopropylethanolamine, 1,2-ethanediamine polymers with methyloxirane, and combinations thereof. Examples of chelating agents having a triamine chelating moiety as the nitrogen-based chelating moiety include VORANOL™ RA640 (available from DOW Inc.), a 1,2-ethanediamine polymer containing methyloxirane; N,N,N',N',N"-pentamethyldiethylenetriamine; N,N,N',N',N"-pentamethyldipropylenetriamine; 1-[bis[3-(dimethylamino)propyl]amino-2-propanol]; N,N'-dimethylaminoethyl (N-methylpiperzine); and combinations thereof. Examples of chelating agents having a tetramine chelating moiety as the nitrogen-based chelating moiety include 1,1,4,7,10,10-hexamethyltriethylenetetramine; tris[2-(dimethylamino)ethyl]amine; tris[2-(isopropylamino)ethyl]amine; and combinations thereof.Preferably, the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of 2,2'-bipyridine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, 2-[[2-(dimethylamino)ethyl]methylamino]ethanol, 1-[bis[3-(dimethylamino)propyl]amino-2-propanol, 1,2-ethanediamine polymers with methyloxirane (e.g., VORANOL™ RA640), and combinations thereof.

[0034] In various embodiments, the chelating agent having a nitrogen-based chelating moiety is soluble in the polyol in the transition metal chelate polyol blend, such that the liquid transition metal chelate polyol blend has from 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, preferably from 0.003 to 0.60 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, more preferably from 0.006 to 0.40 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend, and most preferably from 0.01 to 0.20 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams of polyol in the liquid transition metal chelate polyol blend.

[0035] The liquid transition metal chelate polyol blends have a molar ratio of nitrogen to transition metal ion (moles nitrogen:moles transition metal ion) in the nitrogen-based chelating moiety of 8:0:1:0 to 1.0:1.0, and in various embodiments, the molar ratio of nitrogen to transition metal ion in the nitrogen-based chelating moiety is preferably 4.0:1.0 to 1.0:1.0 (moles nitrogen:moles transition metal ion), more preferably 2.8:1.0 to 1.0:1.0, and most preferably 2.0:1.0 to 1.0:1.0.

[0036] In various embodiments, the liquid transition metal chelate polyol blends of the present disclosure have little or no effect on the reaction between isocyanates and isocyanate-reactive compositions. In PIR systems, the liquid transition metal chelate polyol blends preferably do not reduce the isocyanurate content in the polyurethane foam by more than 50% compared to the same polyurethane foam formulation without the transition metal compound. More preferably, the transition metal compounds do not reduce the isocyanurate content in the polyurethane foam by more than 40% compared to the same polyurethane foam formulation without the transition metal compound. More preferably, the transition metal compounds do not reduce the isocyanurate content in the polyurethane foam by more than 30% compared to the same polyurethane foam formulation without the transition metal compound. Most preferably, the transition metal compounds do not reduce the isocyanurate content in the polyurethane foam by more than 25% compared to the same polyurethane foam formulation without the transition metal compound.

[0037] The present disclosure provides a process for preparing a liquid transition metal chelate polyol blend, the process including providing a polyol, providing a chelating agent having nitrogen-based chelating moieties, and providing a transition metal compound having a transition metal ion. The process further includes combining the polyol, the chelating agent, and the transition metal compound to form a liquid transition metal chelate polyol blend having 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moieties per 100 grams of polyol in the liquid transition metal chelate polyol blend. In various embodiments, the liquid transition metal chelate polyol blend has a molar ratio of nitrogen to transition metal ion (moles nitrogen:moles transition metal ion) in the nitrogen-based chelate moiety of 8:0:1:0 to 1.0:1.0, and in various embodiments, the molar ratio of nitrogen to transition metal ion in the nitrogen-based chelate moiety is preferably 4.0:1.0 to 1.0:1.0 (moles nitrogen:moles transition metal ion), more preferably 2.8:1.0 to 1.0:1.0, and most preferably 2.0:1.0 to 1.0:1.0. In various embodiments, the blending to form the liquid transition metal chelate polyol blend can be carried out at atmospheric pressure (e.g., 101.23 KPa) and at a temperature below 100°C, preferably below 80°C, more preferably below 60°C, and most preferably below 40°C.

[0038] The present disclosure also provides an isocyanate-reactive composition comprising the liquid transition metal chelate polyol blend provided herein, optionally a catalyst and a flame retardant, where the isocyanate-reactive composition can be used to form a polyurethane polymer. Embodiments of the present disclosure also include an isocyanate-reactive composition having the liquid transition metal chelate polyol blend provided herein, further comprising a polyol (different from the polyol in the liquid transition metal chelate polyol blend), a phosphorus flame retardant, a catalyst, a blowing agent, water, a surfactant, or a combination thereof, where the isocyanate-reactive composition can be used to form a polyurethane foam. For example, the isocyanate-reactive composition provided herein can include a blowing agent and a surfactant for use in forming a polyurethane polymer foam. Amounts (e.g., weight percentages) of each of the catalyst, water, surfactant, flame retardant, and blowing agent useful in the isocyanate-reactive composition, along with examples of each, are provided herein in the context of the reaction mixture for forming the polyurethane polymer of the present disclosure discussed below.

[0039] In various embodiments, the isocyanate-reactive composition can further include a polyol different from the polyol in the liquid transition metal chelate polyol blend, where the isocyanate-reactive composition includes 0.1 to 100 weight percent (wt %) (wt % based on the total weight of the isocyanate-reactive composition) of the liquid transition metal chelate polyol blend and up to 99.9% of a polyol different from the polyol of the liquid transition metal chelate polyol blend to form an isocyanate-reactive composition for a polyurethane polymer. In various embodiments, the polyol used with the liquid transition metal chelate polyol blend to help form the isocyanate-reactive composition can be selected from the group consisting of polyester polyols, polyether polyols, polycarbonate polyols, polyether carbonate polyols, and combinations thereof.

[0040] The polyols, which are different from the polyols in the liquid transition metal chelate polyol blend, may have a number average molecular weight of 100 g / mol to 10,000 g / mol. Other number average molecular weight values ​​are also possible. For example, the polyols may have number average molecular weights ranging from lower limits of 100, 200, 300, 350, or 400 g / mol to upper limits of 500, 750, 1,000, 2,000, or 10,000 g / mol. The number average molecular weight values ​​reported herein are determined by end-group analysis, gel permeation chromatography, and other methods known in the art. The polyols used with the liquid transition metal chelate polyol blends useful in forming the isocyanate-reactive compositions may also contain an aromatic moiety. As used herein, an "aromatic moiety" is at least one cyclically conjugated molecular moiety in the form of a planar unsaturated ring of carbon atoms, covalently bonded to the polyol compound. The planar unsaturated ring of carbon atoms may have at least six carbon atoms.

[0041] In embodiments, the isocyanate-reactive composition may further comprise 0.1 wt. % to 7.0 wt. % phosphorus from the flame retardant compound, where the wt. % of phosphorus is based on the total weight of the isocyanate-reactive composition. Preferably, the isocyanate-reactive composition comprises 0.5 wt. % to 5.0 wt. % phosphorus from the flame retardant compound (where the wt. % of phosphorus is based on the total weight of the isocyanate-reactive composition). More preferably, the isocyanate-reactive composition comprises 1.0 wt. % to 3.0 wt. % phosphorus from the flame retardant compound (where the wt. % of phosphorus is based on the total weight of the isocyanate-reactive composition). The isocyanate-reactive composition may further comprise 0.05 wt. % to 10.0 wt. % transition metal, where the transition metal is derived from a transition metal compound provided herein having a transition metal ion, where the wt. % of the transition metal is based on the total weight of the liquid transition metal chelate polyol blend. Preferably, the isocyanate-reactive composition may further comprise 0.15 wt.% to 6.0 wt.% transition metal from the transition metal compound provided herein having a transition metal ion (the weight percent of the transition metal is based on the total weight of the liquid transition metal chelate polyol blend), most preferably 0.5 wt.% to 3.0 wt.% transition metal from the transition metal compound provided herein having a transition metal ion (the weight percent of the transition metal is based on the total weight of the liquid transition metal chelate polyol blend). At a given weight percent, the isocyanate-reactive composition may have a molar ratio of transition metal ion to phosphorus (moles of transition metal ion:moles of phosphorus) of 0.05:1 to 5:1. Preferably, the molar ratio of transition metal ion to phosphorus (moles of transition metal:moles of phosphorus) is 0.1:1 to 2:1. More preferably, the molar ratio of transition metal ion to phosphorus (moles of transition metal:moles of phosphorus) is 0.5:1 to 1:1.

[0042] In embodiments provided herein, the isocyanate-reactive composition may have a flame retardant compound, preferably a halogen-free flame retardant compound, selected from the group consisting of phosphates, phosphonates, phosphinates, and combinations thereof. Examples of phosphates include trialkyl phosphates, triaryl phosphates, phosphate esters, and resorcinol bis(diphenyl phosphate). As used herein, a trialkyl phosphate has at least one alkyl group having 2 to 12 carbon atoms. The other two alkyl groups of the trialkyl phosphate, including linear or branched alkyl groups, cyclic alkyl groups, alkoxyethyl, hydroxyl alkyl, hydroxyl alkoxy alkyl groups, and linear or branched alkylene groups, may independently be the same or different from the first alkyl group and contain 1 to 8 carbon atoms. Examples of the other two alkyl groups of the trialkyl phosphate include, for example, methyl, ethyl, propyl, butyl, n-propyl, isopropyl, n-butyl, isobutyl, sec-butyl, tert-butyl, butoxyethyl, isopentyl, neopentyl, isohexyl, isoheptyl, cyclohexyl, propylene, 2-methylpropylene, neopentylene, hydroxymethyl, hydroxyethyl, hydroxypropyl, or hydroxybutyl. Blends of different trialkyl phosphates can also be used. The three alkyl groups of the trialkyl phosphate can be the same. The alkyl groups can be halogenated alkyl groups, and preferably, the alkyl groups are halogen-free alkyl groups. The trialkyl phosphate can be tris(2-chloro-1-methylethyl)phosphate (TCPP), tris[2-chloro-1-(chloromethyl)ethyl]phosphate (TDCP), tris(p-tert-butylphenyl)phosphate (TBPP), and tris(2-chloroethyl)phosphate (TCEP). The trialkyl phosphate is preferably triethyl phosphate (TEP).

[0043] Examples of phosphonates include diethyl (hydroxymethyl) phosphonate, dimethyl methyl phosphonate, and diethyl ethyl phosphonate. Examples of phosphinates include metal salts of organic phosphinates such as aluminum methyl ethyl phosphinate, aluminum diethyl phosphinate, zinc methyl ethyl phosphinate, and zinc diethyl phosphinate. Examples of additional halogen-free flame retardant compounds include resorcinol diphosphate, 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide, ammonium polyphosphate, and combinations thereof.

[0044] The present disclosure also provides a reaction mixture for forming a polyurethane polymer. The reaction mixture includes an isocyanate compound having an isocyanate moiety and an isocyanate-reactive composition provided herein having a hydroxyl moiety (e.g., from a polyester polyol), wherein the reaction mixture has a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1. For polyurethane rigid (PUR) and polyisocyanurate (PIR), preferably, the molar ratio of isocyanate moieties to hydroxyl moieties is 1.2:1 to 7:1, more preferably, the molar ratio of isocyanate moieties to hydroxyl moieties is 1.5:1 to 5:1, and most preferably, the molar ratio of isocyanate moieties to hydroxyl moieties is 2:1 to 4:1. For flexible polyurethane foams, preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 0.90:1 to 1.20:1, more preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 0.95:1 to 1.15:1, and most preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 1:1 to 1.10:1. For two-component polyurethane adhesives, sealants, coatings, and elastomers, preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 0.95:1 to 1.35:1, more preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 0.98:1 to 1.10:1, and most preferably the molar ratio of isocyanate moieties to hydroxyl moieties is 1:1 to 1.05:1.

[0045] In various embodiments, the isocyanate compound has a number average molecular weight of 150 g / mol to 750 g / mol. Other number average molecular weight values ​​are possible. For example, the isocyanate-reactive compound may have a number average molecular weight ranging from a lower limit of 150, 200, 250, or 300 g / mol to an upper limit of 350, 400, 450, 500, or 750 g / mol. In some embodiments, when the isocyanate compound is an isocyanate prepolymer resulting from the reaction of an isocyanate-reactive compound with a molar excess of a polyisocyanate compound or a polymeric isocyanate compound under conditions that do not result in gelation or solidification, the isocyanate prepolymer may have a number average molecular weight greater than 750 g / mol, which can be calculated from the number average molecular weights of each component and their relative masses used to prepare the prepolymer. Number average molecular weight values ​​reported herein are determined by end-group analysis, gel permeation chromatography, and other methods known in the art. The isocyanate compound may be monomeric and / or polymeric, as known in the art. Additionally, the isocyanate compound may have an isocyanate equivalent weight of 80 to 1750. In certain embodiments, the isocyanate has a viscosity of 5 to 50,000 mPa·s at 25°C, as measured using a Brookfield DVE viscometer. Other viscosity values ​​may also be possible. For example, the isocyanate-reactive compound may have a lower viscosity limit of 5, 10, 30, 60, or 150 mPa·s, each measured at 25°C using a Brookfield DVE viscometer. . s~Upper limit 500, 2500, 10,000, or 50,000 mPa . It may have a viscosity of s.

[0046] As used herein, polymeric isocyanate compounds contain two or more -NCO groups per molecule and are also considered isocyanate compounds. In various embodiments, the polymeric isocyanate compound is selected from aliphatic diisocyanates, alicyclic diisocyanates, aromatic diisocyanates, polyisocyanates, isocyanate prepolymers, and combinations thereof. In various embodiments, the polymeric isocyanate compound has a number average molecular weight of 150 g / mol to 750 g / mol. In addition, polymeric isocyanate compounds, including so-called MDI products, which are mixtures of isomers of diphenylmethane diisocyanate (MDI) in monomeric MDI, or so-called polymeric MDI products, which are mixtures of polymethylene polyphenylene polyisocyanates in monomeric MDI, may have an isocyanate equivalent weight of 80 to 150, preferably 100 to 145, and more preferably 110 to 140.

[0047] Examples of polymeric isocyanate compounds of the present disclosure include, but are not limited to, methylene diphenyl diisocyanate (MDI), polymethylene polyphenylisocyanate containing MDI, polymeric MDI (PMDI), 1,6 hexamethylene diisocyanate (HDI), 2,4- and / or 2,6-toluene diisocyanate (TDI), 1,5-naphthalene diisocyanate (NDI), tetramethylene-1,4-diisocyanate, cyclohexane-1,4-diisocyanate, hexahydrotoluene diisocyanate, hydrogenated MDI (HDI), and the like. 124,4'-dimethyldiphenylmethane-2,2',5,5'-tetraisocyanate, methylenebicyclohexyl isocyanate (HMDI), methoxyphenyl-2,4-diisocyanate, 4,4'-biphenylene diisocyanate, 3,3'-dimethyoxy-4,4'-biphenyl diisocyanate, 3,3'-dimethyldiphenylmethane-4,4'-diisocyanate, 4,4',4"-triphenylmethane diisocyanate, polymethylene polyphenyl isocyanate, hydrogenated polymethylene polyphenyl polyisocyanate, toluene-2,4,6-triisocyanate, and 4,4'-dimethyldiphenylmethane-2,2',5,5'-tetraisocyanate, methylenebicyclohexyl isocyanate (HMDI), isophorone diisocyanate (IPDI), and combinations thereof. Suitable isocyanates may also be The isocyanates may also include other aromatic and / or aliphatic polyfunctional isocyanates, including those containing phenyl, tolyl, xylyl, naphthyl, or diphenyl moieties, or combinations thereof, such as the trimethylolpropane adduct of xylylene diisocyanate, the trimethylolpropane adduct of toluene diisocyanate, 4,4'-diphenyldimethane diisocyanate (MDI), xylylene diisocyanate (XDI), 4,4'-diphenyldimethylmethane diisocyanate, di- and tetraalkyldiphenylmethane diisocyanates, 4,4'-dibenzyl diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, and combinations thereof.Suitable aliphatic polymeric isocyanate compounds include the trimer of hexamethylene diisocyanate, the trimer of isophorone diisocyanate, the biuret of hexamethylene diisocyanate, hydrogenated polymeric methylene diphenyl diisocyanate, hydrogenated methylene diphenyl diisocyanate, hydrogenated MDI, tetramethylxylol diisocyanate (TMXDI), 1-methyl-2,4-diisocyanato-cyclohexane, 1,6-diisocyanato-2,2,4-trimethylhexane, 1-isocyanatomethyl-3-isocyanato-1,5,5-trimethylcyclohexane, tetramethoxybutane 1,4-diisocyanate, butane 1,4-diisocyanate, hexane 1,6-diisocyanate, dicyclohexylmethane diisocyanate, cyclohexane 1,4-diisocyanate, and combinations thereof. Examples of other polymeric isocyanate compounds include additional aliphatic, cycloaliphatic, polycyclic, or aromatic per se, such as hydrogenated xylene diisocyanate (HXDI), p-phenylene diisocyanate (PPDI), 3,3'-dimethyldiphenyl-4,4'-diisocyanate (DDDI), 2,2,4-trimethylhexamethylene diisocyanate (TMDI), isophorone diisocyanate (IPDI), 4,4'-dicyclohexylmethane diisocyanate (H12MDI), and norbornane diisocyanate (NDI). As well as the above isocyanates, modified polyisocyanates may also be utilized, including, among others, uretdione, isocyanurate, carbodiimide, uretonimine, allophanate, or biuret structures, and combinations thereof. The polyols provided herein can be pre-reacted with an organic polyisocyanate to form a prepolymer or quasi-prepolymer containing isocyanate groups. The prepolymer or quasi-prepolymer can have, for example, an isocyanate content of 1 to 20 weight percent. In some embodiments, the isocyanate content is at least 2.5%, or at least 4% and up to 15%, up to 12%, or up to 10%.

[0048] In addition to providing a reaction mixture, the present disclosure also provides a process for preparing a reaction mixture for producing a polyurethane polymer. As discussed herein, the reaction mixture for forming a polyurethane polymer includes an isocyanate compound having isocyanate moieties and an isocyanate-reactive composition as discussed herein, in which the polyol includes hydroxyl moieties, the reaction mixture having a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1 (among other values ​​discussed herein). The process for preparing a reaction mixture for producing a polyurethane polymer includes providing an isocyanate-reactive composition as provided herein, providing an isocyanate compound as provided herein having isocyanate moieties, and combining the isocyanate-reactive composition and the isocyanate compound to form a reaction mixture having a molar ratio of isocyanate moieties to hydroxyl moieties of 0.90:1 to 7:1 (among other values ​​discussed herein). The combining of the isocyanate-reactive composition with the isocyanate compound may further include combining water, a catalyst, a surfactant, a blowing agent, a phosphorus-containing flame retardant compound, and combinations thereof with the reaction mixture to form a polyurethane polymer, including a subset of polyurethane polymer foams. Resulting from the process may be a polyurethane polymer or a polyurethane polymer foam formed with the reaction mixture provided herein.

[0049] In various embodiments provided herein, the catalyst may be present in the reaction mixture in an amount of 0.01 to 1.5 wt %, based on the total weight of the reaction mixture. The catalyst may be selected from the group consisting of organic tertiary amines, tertiary phosphines, potassium acetate, urethane-based catalysts, and combinations. As known in the art, the catalyst may also include organotin compounds.

[0050] The catalyst may be a blowing catalyst, a gelling catalyst, a trimerization catalyst, or a combination thereof. As used herein, blowing catalysts and gelling catalysts may be distinguished by their tendency to favor either the urea (blow) reaction in the case of a blowing catalyst, or the urethane (gel) reaction in the case of a gelling catalyst. A trimerization catalyst may be utilized to promote the isocyanurate reaction in the composition. Both blowing catalysts and gelling catalysts are utilized in the preparation of rigid and flexible polyurethane foams. Many non-foam or non-microcellular polyurethanes, such as coatings, adhesives, sealants, and elastomers, utilize gelling catalysts.

[0051] Examples of blowing catalysts, e.g., catalysts that may tend to favor the blowing reaction, include, but are not limited to, short-chain tertiary amines or tertiary amines containing oxygen. The amine catalyst may not be sterically hindered. For example, blowing catalysts include bis-(2-dimethylaminoethyl)ether, pentamethyldiethylene-triamine, triethylamine, tributylamine, N,N-dimethylaminopropylamine, dimethylethanolamine, N,N,N',N'-tetramethylethylenediamine, and combinations thereof. An example of a commercially available blowing catalyst is POLYCAT™ 5 from Evonik, among other commercially available blowing catalysts.

[0052] Examples of gelation catalysts, e.g., catalysts that may tend to favor the gelation reaction, include, but are not limited to, organometallic compounds, cyclic tertiary amines, and / or long-chain amines, e.g., those containing several nitrogen atoms, and combinations thereof. Organometallic compounds include organotin compounds such as tin(II) salts of organic carboxylic acids, e.g., tin(II) diacetate, tin(II) dioctanoate, tin(II) diethylhexanoate, and tin(II) dilaurate, and dialkyltin(IV) salts of organic carboxylic acids, e.g., dibutyltin diacetate, dibutyltin dilaurate, dibutyltin maleate, and dioctyltin diacetate. Bismuth salts of organic carboxylic acids can also be used as gelation catalysts, e.g., bismuth octoate. Cyclic tertiary amines and / or long-chain amines include dimethylbenzylamine, triethylenediamine, and combinations thereof, and combinations thereof. Examples of commercially available gelling catalysts are POLYCAT™ 8 and DABCO® T-12 from Evonik, among other commercially available gelling catalysts.

[0053] Examples of trimerization catalysts include, among others, N,N,N',N",N"-pentamethyldiethylenetriamine (PMDETA); N,N',N"-tris(3-dimethylaminopropyl)hexahydro-s-triazine; N,N-dimethylcyclohexylamine; 1,3,5-tris(N,N-dimethylaminopropyl)-s-hexahydrotriazine; [2,4,6-tris(dimethylaminomethyl)phenol]; potassium acetate, potassium octoate; tetraalkylammonium hydroxides such as tetramethylammonium hydroxide; sodium hydroxide. alkali metal hydroxides such as sodium; alkali metal alkoxides such as sodium methoxide and potassium isopropoxide; and alkali metal salts of long-chain fatty acids having 10 to 20 carbon atoms, and combinations thereof. Some commercially available trimerization catalysts include DABCO® TMR-2, TMR-7, DABCO® K2097; DABCO® K15, POLYCAT™ 41, and POLYCAT™ 46, each from Evonik, among other commercially available trimerization catalysts.

[0054] In various embodiments provided herein, water may be present in the reaction mixture in an amount of 0.1 to 1.5 wt %, based on the total weight of the reaction mixture.

[0055] In various embodiments, the surfactant may be present in the reaction mixture in an amount of 0.1 to 10 wt %, based on the total weight of the reaction mixture. Examples of suitable surfactants include silicone-based surfactants and organic surfactants. Some representative materials are generally polysiloxane polyoxyl alkylene block copolymers, such as those disclosed in U.S. Pat. Nos. 2,834,748, 2,917,480, and 2,846,458, the disclosures of which are incorporated herein by reference in their entireties. Organic surfactants containing polyoxyethylene-polyoxybutylene block copolymers, such as those described in U.S. Pat. No. 5,600,019, the disclosure of which is incorporated herein by reference in its entirety, are also included. Other surfactants include polyethylene glycol ethers of long-chain alcohols, tertiary amine or alkanolamine salts of long-chain aryl acid sulfate esters, alkyl sulfonates, alkylaryl sulfonic acids, and combinations thereof.

[0056] In various embodiments, the blowing agent may be present in the reaction mixture for forming a polyurethane polymer foam in an amount of 1.0 to 15 wt %, based on the total weight of the reaction mixture. In addition to other blowing agents provided herein, blowing agents known in the art may be selected from the group consisting of water, volatile organic substances, dissolved inert gases, and combinations thereof. Examples of blowing agents include hydrocarbons such as butane, isobutane, 2,3-dimethylbutane, n- and i-pentane isomers, hexane isomers, heptane isomers, and cycloalkanes, including cyclopentane, cyclohexane, and cycloheptane; HCFC-142b (1-chloro-1,1-difluoroethane), HCFC-141b (1,1-dichloro-1-fluoroethane), and HCFC-22 (chlorodifluoromethane). , HFC-245fa (1,1,1,3,3-pentafluoropropane), HFC-365mfc (1,1,1,3,3-pentafluorobutane), HFC227ea (1,1,1,2,3,3,3-heptafluoropropane), HFC-134a (1,1,1,2-tetrafluoroethane), HFC-125 (1,1,1,2,2-pentafluoroethane), HFC-143 (1,1,2-trifluoroethane), H FC143A (1,1,1-trifluoroethane), HFC-152 (1,1-difluoroethane), HFC-227ea (1,1,1,2,3,3,3-heptafluoropropane), HFC-236ca (1,1,2,2,3,3-hexafluoropropane), HFC236fa (1,1,1,3,3,3-hexafluoroethane), HFC245ca (1,1,2,2,3-pentafluoropentane), HFC356 Hydrofluorocarbons such as MFF (1,1,1,4,4,4-hexafluorobutane) and HFC365MFC (1,1,1,3,3-pentafluorobutane); hydrofluoroolefins such as cis-1,1,1,4,4,4-hexafluoro-2-butene, 1,3,3,3-tetrafluoropropene, and trans-1-chloro-3,3,3-trifluoropropene; and chemical blowing agents such as formic acid and water.The blowing agent can be ethyl acetate; methanol; ethanol; halogen-substituted alkanes such as methylene chloride, chloroform, ethylidene chloride, vinylidene chloride, monofluorotrichloromethane, chlorodifluoromethane, or dichlorodifluoromethane; butane; hexane; heptane; other volatile organic substances such as diethyl ether; and gases such as nitrogen; air; and carbon dioxide.

[0057] In addition to water, catalyst, blowing agent, surfactant, and combinations thereof, the reaction mixture may further include a filler along with other additives. The total amount of such other additives may be from 0.01% to 30.0% by weight. The use of other additives for polyurethane polymer compositions is also known and may be used with the present disclosure.

[0058] As discussed herein, the liquid transition metal chelate polyol blends have a molar ratio of nitrogen to transition metal ions in the nitrogen-based chelating moieties (moles of nitrogen:moles of transition metal ions) of 8:0:1:0 to 1.0:1.0, and in various embodiments, the molar ratio of nitrogen to transition metal ions in the nitrogen-based chelating moieties is preferably 4.0:1.0 to 1.0:1.0 (moles of nitrogen:moles of transition metal ions), more preferably 2.8:1.0 to 1.0:1.0, and most preferably 2.0:1.0 to 1.0:1.0. While other molar ratios of nitrogen to transition metal ion in the nitrogen-based chelating moiety may be used, it is desirable to maximize the amount of transition metal ion (e.g., copper) relative to nitrogen that can be delivered to the reaction mixture so that the reaction rate of the isocyanate and isocyanate-reactive moieties in the isocyanate-reactive composition or reaction mixture of the present disclosure for producing polyurethane polymers and / or polyurethane polymer foams is not unduly affected by the higher catalytic amine chelating agent content resulting from the higher nitrogen to transition metal ion molar ratio, such that the foaming, gelling, and / or trimerization reactions in the foaming process are unbalanced, resulting in a foam with essentially reduced foaming characteristics, such as a lack of insulating characteristics, increased density, and / or other foaming attributes, while still fitting reaction rate parameters such as cream time, gel time, and tack-free time within the processing parameters of the foaming process and associated equipment.

[0059] In this embodiment, the reaction kinetic parameters of the polyurethane foam of the reaction mixture provided herein are determined using a wooden tongue depressor. A total of 80 grams (g) of the reaction mixture containing the isocyanate compound and the isocyanate-reactive composition is poured into a 500 mL beaker. The cream time is defined as the time from preparation of the reaction mixture until a discernible initiation of foaming occurs, such as a visual change in the reactants (a color change and / or the onset of rising). The gel time (or string time) is defined as the time from preparation of the reaction mixture until a change from a fluid to a solid state is reached. This is determined by repeatedly dipping and withdrawing a wooden tongue depressor into the reaction mixture. The gel time is reached as soon as a string forms while withdrawing the wooden tongue depressor from the reaction mixture. The tack-free time is defined as the time from preparation of the foam reaction mixture until the foam surface becomes tack-free. This is determined by placing a wooden tongue depressor on the foam surface. The tack-free time is reached when lifting the wooden tongue depressor does not result in delamination or rupture of the foam surface, in other words, when the foam surface is no longer tacky.

[0060] In various embodiments, the combination of the liquid transition metal chelate polyol blend and optional catalyst provides similar reaction kinetic parameters for polyurethane foam formulations containing an isocyanate compound and an isocyanate-reactive composition to typical polyurethane foam formulations of the same type without the liquid transition metal chelate polyol blend. Foam systems containing the liquid transition metal chelate polyol blend preferably have a cream time of within 10 seconds, more preferably within 5 seconds, and most preferably within 2 seconds compared to the cream time of a typical polyurethane foam of the same type without the liquid transition metal chelate polyol blend. Foam systems containing the liquid transition metal chelate polyol blend preferably have a gel time of within 20 seconds, more preferably within 10 seconds, and most preferably within 8 seconds compared to the gel time of a typical polyurethane foam of the same type without the liquid transition metal chelate polyol blend. Foam systems containing the liquid transition metal chelate polyol blend preferably have a tack-free time of within 20 seconds, more preferably within 10 seconds, and most preferably within 8 seconds compared to the tack-free time of a typical polyurethane foam of the same type without the liquid transition metal chelate polyol blend.

[0061] For typical PIR foam systems with or without a liquid transition metal chelate polyol blend, the cream time is preferably in the range of 1 to 20 seconds, more preferably in the range of 3 to 15 seconds, even more preferably in the range of 5 to 12 seconds, and most preferably in the range of 6 to 10 seconds. For typical PIR foam systems with or without a liquid transition metal chelate polyol blend, the gel time is preferably in the range of 15 to 60 seconds, more preferably in the range of 18 to 50 seconds, even more preferably in the range of 20 to 40 seconds, and most preferably in the range of 25 to 35 seconds. For typical PIR foam systems with or without a liquid transition metal chelate polyol blend, the tack-free time is preferably in the range of 30 to 120 seconds, more preferably in the range of 40 to 90 seconds, even more preferably in the range of 50 to 80 seconds, and most preferably in the range of 55 to 70 seconds.

[0062] In various embodiments, the reaction mixture can be used to form either a polyurethane polymer or a polyurethane polymer foam. The process for preparing the reaction mixture for producing a polyurethane polymer or polyurethane polymer foam can be accomplished through any known process technique in the art. Generally, the polyurethane polymer foams of the present disclosure can be produced by discontinuous or continuous processes, including processes commonly referred to as discontinuous panel processes (DCP) and continuous lamination, in which the foaming reaction and subsequent curing are carried out in a mold or on a conveyor. The processes provided herein for forming either a polyurethane polymer or a polyurethane polymer foam can be carried out at temperatures between 15°C and 80°C and at mixing pressures between 80 KPa and 25,000 kPa. The blending of the polyurethane foam components can be carried out using known mixing devices. The density of the resulting polyurethane polymer foam can be greater than 10 kg / m. 3 or more, preferably 15 kg / m 3 More preferably, 25 kg / m 3 More than 35 kg / m, most preferably 35 kg / m 3 At the same time, typically 200 kg / m 3 Less than 100 kg / m 3 Less than or equal to 70 kg / m 3 Below 50 kg / m, most preferably 3 It can be the following:

[0063] In various embodiments, the polyurethane polymer foams of the present disclosure provide low smoke generation and high thermal stability as determined in accordance with ASTM E662 "Test Method for Specific Optical Density of Smoke Generated by Solid Materials." A lower maximum specific optical density (Max Ds) value indicates less smoke generation. A lower % mass loss value indicates higher thermal stability. Max Ds can be 400 or less, preferably 200 or less, more preferably 100 or less, and even most preferably 50 or less. % mass loss can be 50% or less, preferably 45% or less, more preferably 40% or less, and even most preferably 30% or less.

[0064] The polyurethane polymer foam of the present disclosure may have low thermal conductivity for applications such as building insulation. The thermal conductivity of rigid foam is expressed by the K-factor. The K-factor is a measure of thermal insulation properties. The K-factor of the foam prepared may be 30.0 mW / m K or less, preferably 27.0 mW / m K or less, more preferably 24.0 mW / m K or less, and most preferably 22.0 mW / m K or less. The thermal conductivity (K-factor) is 75 ° Measured using ASTM C-518-17 at an average temperature of 100°F.

[0065] The applications of polyurethane polymer foams produced by the present disclosure are known in the industry. For example, polyurethane polymer foams can be used for insulation in building walls and roofs, garage doors, transport trucks and railroad cars, and refrigeration facilities. The polyurethane polymer foams disclosed herein can have a combination of properties desirable for these applications. For example, the polyurethane polymer foams disclosed herein can advantageously provide desirable low thermal conductivity, smoke density, thermal stability, and improved combustion characteristics with reduced HCN and CO emissions.

[0066] The liquid transition metal chelate polyol blends and polyurethane polymers of the present disclosure may also be useful, for example, as coatings, elastomers, sealants, binders, adhesives, or flexible foams. For use as coatings, elastomers, sealants, binders, or adhesives, the reactants are preferably formulated into a two-component (2K) system, where one component contains a polyisocyanate (more preferably an isocyanate-terminated prepolymer or quasi-prepolymer) and the other component, an isocyanate-reactive composition, contains at least one liquid transition metal chelate polyol blend that imparts antifungal, antibacterial, odor resistance, hardness, abrasion resistance, burn / burn behavior modification, or the like, to the cured polyurethane product. For use as coatings, elastomers, sealants, binders, or adhesives, the liquid transition metal chelate polyol blends, including other optional polyols, can be pre-reacted with an organic polyisocyanate to form a prepolymer or quasi-prepolymer containing isocyanate groups and utilized as a one-component (1K) cure system.

[0067] Some embodiments of the present disclosure will now be described in detail in the following examples. [Example]

[0068] Some embodiments of the present disclosure are detailed in the following examples, in which all parts and percentages are by weight unless otherwise specified. The following materials and tests are used in the examples:

[0069] material Materials used in the examples and / or comparative examples include the following:

[0070] Polyol A is a polyester polyol (aromatic polyester polyol from terephthalic acid, polyethylene glycol 200, and diethylene glycol) with a hydroxyl number of 220 mg KOH / g, a functionality of 2, and a total content of aromatic moieties of 14.8 wt %.

[0071] Polyol B is a polyester polyol (aromatic polyester polyol from terephthalic acid, polyethylene glycol 200, glycerol, and diethylene glycol) with a hydroxyl number of 315 mg KOH / g, a functionality of 2.4, and a total content of aromatic moieties of 17.4 wt %.

[0072] Polyethylene glycol 200 (PEG 200) available from TCI America.

[0073] 2,2'-Bipyridine (BIPY) available from Sigma-Aldrich.

[0074] 2-[[2-(dimethylamino)ethyl]methylamino]ethanol (TMDAOH) available from TCI America.

[0075] 1-[bis[3-(dimethylamino)propyl]amino-2-propanol] available from Sigma-Aldrich.

[0076] VORANOL™ RA640 polyol, available from Dow Inc., is an amine-initiated polyol with a hydroxyl number of 654 mg KOH / g and a viscosity of 21,500 cSt at 25°C.

[0077] N,N,N',N'-Tetramethylethylenediamine (TMEDA) available from TCI America.

[0078] Triethyl phosphate (TEP) is a flame retardant from LANXESS.

[0079] POLYCAT® 5 is an N,N,N′,N′,N″-pentamethyldiethylenetriamine (PMDTA) catalyst from Evonik Industries AG.

[0080] POLYCAT® 46 is a catalyst from Evonik Industries AG.

[0081] The silicone surfactant is a silicone hard foam surfactant from Evonik Industries AG.

[0082] The water is deionized water with a resistivity of 10 MΩ×cm (million ohms) at 25°C.

[0083] Cyclopentane (c-pentane) is a blowing agent from Sigma-Aldrich.

[0084] PAPI™ 580N is a polymethylene polyphenylisocyanate from Dow Inc. containing methylene diphenyl diisocyanate (MDI) with 30.8% isocyanate.

[0085] Copper(II) hydroxide (Cu(OH)2), technical grade, available from Sigma Aldrich.

[0086] Copper(I) oxide (CuO), technical grade, available from Sigma Aldrich.

[0087] Copper(II) 2-ethylhexanoate (CuEH) available from Sigma Aldrich.

[0088] Copper(II) acetate monohydrate (Cu(OAc)2H2O) available from Acros Organics.

[0089] Copper(II) i-butyrate (Cu(I-But)2) available from Strem Chemical.

[0090] Cobalt(II) acetate tetrahydrate (Co(OAc)24H2O) available from Acros Organics.

[0091] Nickel(II) acetate tetrahydrate (Ni(OAc)24H2O) available from Acros Organics.

[0092] Silver(I) acetate (Ag(OAc)) available from Fisher Scientific.

[0093] Preparation of liquid transition metal chelate polyol blends. Prepare each liquid transition metal chelate polyol blend (LPB) in Table 1 by mixing the polyol, transition metal compound, and chelating agent in the amounts seen in Table 1 in a 250 mL plastic container using a FlackTekSpeedMixer™ DAC600 FVZ at 3000 rpm for 45 seconds. The container is then placed in a preheated convection oven at 80°C for 1 hour (hours). After 1 hour, mix the LPB again for 45 seconds with the FlackTekSpeedMixer™ at 3000 rpm.

[0094] To form the transition metal-containing LPB, an organic transition metal salt is used as the transition metal compound, and a derivative of an amine-based chelating agent is used as the chelating agent, and the molar ratio (N / M) of nitrogen (N) from the amine-based chelating agent to the transition metal (M) from the organic transition metal salt is greater than 1.1, as shown in Table 1. [Table 1]

[0095] Preparation of polyurethane foams using liquid transition metal chelate polyol blends The following components (Table 2) are used in a reaction mixture to form the polyurethane foams of the invention examples (EX) and comparative examples (C Ex). The amount of each component is provided in parts by weight (PBW), based on the total weight of the reaction mixture used to form the polyurethane foam. [Table 2]

[0096] Polyurethane foams are prepared as follows: A reaction mixture containing 80 grams (g) of each EX and C EX listed in Table 2 is prepared in a 500 mL beaker. The components of the isocyanate-reactive composition listed in Table 2 are mixed using a rotary mixer at 3000 rpm for 10 seconds (s). The isocyanate-reactive composition and isocyanate are then mixed again in the beaker at 3000 rpm for 5 seconds at room temperature (23°C, 50% relative humidity). After 24 hours (h), any foam portions that have risen above the flat surface of the top of the beaker are removed, and a 2.54 cm x 2.54 cm x 2.54 cm central core is then excised. The cream time is defined as the time from preparation of the reaction mixture until a discernible initiation of foaming occurs, such as a visual change in the reactants (color change and / or the onset of rising). The gel time (or string time) is defined as the time from preparation of the reaction mixture until the transition from a fluid to a solid state is reached. This is determined by repeatedly dipping and withdrawing a wooden tongue depressor into the reaction mixture. The gel time is reached as soon as a string forms while withdrawing the wooden tongue depressor from the reaction mixture. The tack-free time is defined as the time from preparation of the foam reaction mixture until the foam surface becomes tack-free. This is determined by placing a wooden tongue depressor on the foam surface. The tack-free time is reached when lifting the wooden tongue depressor does not result in delamination or rupture of the foam surface, in other words, when the foam surface is no longer tacky.

[0097] Smoke gas composition analysis Pyrolysis tests were performed using a Frontier Labs 2020D pyrolyzer attached to an Agilent 6890GC equipped with a flame ionization detector (FID). Approximately 200–250 μg of sample was weighed into a silica-lined Frontier Labs stainless steel cup. Pyrolysis was performed in single-shot mode by dropping the sample cup into an oven and analyzing under air conditions at 600 °C for 2 minutes, followed by an additional 2 minutes under helium conditions. A micro-cryo-trapping device (MCT) was used to capture volatile products released from the sample at the head of the separation column. Separation was achieved using a 10 m x 0.32 mm i.d. x 5 μm PoraBond Q column from Agilent with an HP-1 (10 m x 0.53 mm x 2.65 μm) guard column. Back inlet pressure was used for backflush purposes (0.5 m x 0.53 mm guard column, using the back inlet as a head pressure tee to the PoraBond Q and HP-1 columns). HCN was detected by a rear FID detector, and the HCN concentration was compared using the HCN peak area normalized by sample weight.

[0098] GC conditions: front injection port: 300°C; 1:1 split injector; pressure ramp: 4.9 psi for 1.5 min, then hold at 50 psi / min to 3.1 psi; rear injection port: 4 psi; GC oven: 40°C for 3 min, hold at 30°C / min to 240°C; FID: 250°C, H2 flow: 40 mL / min, air flow: 450 mL / min, makeup gas (N2): 30 mL / min, 50 Hz.

[0099] Relative isocyanurate content measurement Attenuated Total Reflectance Fourier Transform Infrared Spectroscopy (ATR-FTIR) was performed on a Nicolet iS50 FT-IR instrument equipped with a SMART iTX single-bounce diamond ATR. Sixteen scans were acquired in the spectral range of 4000-600 cm-1 at a resolution of 4 cm-1. A rectangular cross section (10 mm x 60 mm) was cut from the center of the molded polyurethane foam sample. Three cross sections were run on the cross section, and the three measurements of the characteristic peak were averaged. The relative isocyanurate content was calculated by the characteristic peak height of the isocyanurate group (~1409 cm-1), normalized by this peak height ratio of a transition metal-free control. -1 ) and the characteristic peak height of the phenyl group (~1595 cm -1 ) is defined as the ratio of

[0100] result As can be seen in Table 2, a significant reduction in HCN production is achieved with foams containing copper-containing liquid transition metal chelate polyol blends. The examples show similar reactivity to C EX A. The inventions described in the original claims of this application are set forth below. [1] A liquid transition metal chelate polyol blend comprising: A polyol, 0.05 weight percent (wt. %) to 10.0 wt. % transition metal ions from a transition metal compound, said wt. % based on the total weight of the liquid transition metal chelate polyol blend; a chelating agent having a nitrogen-based chelating moiety, wherein the liquid transition metal chelate polyol blend has 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams (g) of polyol in the liquid transition metal chelate polyol blend, and a molar ratio of nitrogen in the nitrogen-based chelating moiety to the transition metal ion of 8.0:1.0 to 1.0:1.0. [2] The liquid transition metal chelate polyol blend according to [1], wherein the polyol is an aromatic polyester polyol having aromatic moieties, and the aromatic moieties constitute 5 weight percent (wt%) to 60 wt% of the total weight of the aromatic polyester polyol. [3] the transition metal compound is selected from the group consisting of a transition metal carboxylate, a transition metal salt, a transition metal coordination compound, and combinations thereof, and the transition metal ion is selected from the group consisting of copper, zinc, silver, iron, manganese, cobalt, nickel, zirconium, and combinations thereof; or The transition metal compound may be copper(II) 2-ethylhexanoate (CuEH), copper(II) acetate, copper(II) acetate monohydrate (Cu(OAc) 2 H 2 O), copper(II) propionate, copper(II) isobutyrate (Cu(i-Bu) 2 ), cobalt(II) acetate, nickel(II) acetate, silver(I) acetate, and combinations thereof. [4] The liquid transition metal chelate polyol blend of [1], wherein the nitrogen-based chelating moiety is selected from the group consisting of diamine chelating moieties, triamine chelating moieties, tetraamine chelating moieties, and combinations thereof. [5] The liquid transition metal chelate polyol blend of [1], wherein the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of 2,2'-bipyridine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, 2-[[2-(dimethylamino)ethyl]methylamino]ethanol, 1-[bis[3-(dimethylamino)propyl]amino-2-propanol], 1,2-ethanediamine polymers with methyloxirane, and combinations thereof. [6] An isocyanate-reactive composition comprising: [1] to [5], and a liquid transition metal chelate polyol blend. and a polyol different from the polyol in the liquid transition metal chelate polyol blend, wherein the isocyanate-reactive composition comprises 0.1 to 100 weight percent (wt %) of the liquid transition metal chelate polyol blend, said wt % being based on the total weight of the isocyanate-reactive composition, and up to 99.9% wt % of the polyol different from the polyol of the liquid transition metal chelate polyol blend to form the isocyanate-reactive composition. [7] further comprising 0.1 wt. % to 7.0 wt. % phosphorus from a flame retardant compound selected from the group consisting of phosphates, phosphonates, phosphinates, phosphites, and combinations thereof, said wt. % based on the total weight of the isocyanate-reactive composition; or further comprising a catalyst, a blowing agent, and a surfactant for use in forming a polyurethane polymer foam; or 7. The isocyanate-reactive composition of [6], optionally further comprising water for use in forming the polyurethane polymer foam. [8] A reaction mixture for forming a polyurethane polymer or a reaction mixture for forming a polyurethane foam, comprising: an isocyanate compound having an isocyanate moiety; and the isocyanate-reactive composition according to any one of [6] to [7], wherein the polyol comprises hydroxyl moieties, and the reaction mixture has a molar ratio of the isocyanate moieties to the hydroxyl moieties of 0.90:1 to 7:1. [9] A process for preparing a liquid transition metal chelate polyol blend, said process comprising: Providing a polyol; providing a chelating agent having a nitrogen-based chelating moiety; providing a transition metal compound having a transition metal ion; and combining the polyol, the chelating agent, and the transition metal compound to form the liquid transition metal chelate polyol blend having 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moieties per 100 grams of polyol in the liquid transition metal chelate polyol blend and having a molar ratio of nitrogen in the nitrogen-based chelating moieties to the transition metal ion of 8.0:1.0 to 1.0:1.0.

[10] A process for preparing a reaction mixture for producing a polyurethane polymer, said process comprising: Providing an isocyanate-reactive composition according to any one of [6] to [7]; Providing an isocyanate compound having an isocyanate moiety; and combining the isocyanate-reactive composition with the isocyanate compound to form the reaction mixture having a molar ratio of the isocyanate moieties to the hydroxyl moieties of from 0.90:1 to 7:1.

Claims

1. 1. A liquid transition metal chelate polyol blend comprising: A polyol, 0.05 weight percent (wt %) to 10.0 wt % transition metal ions from a transition metal compound, said wt % based on the total weight of said liquid transition metal chelate polyol blend; a chelating agent having a nitrogen-based chelating moiety, wherein the liquid transition metal chelate polyol blend has 0.001 to 1.0 moles of nitrogen in the nitrogen-based chelating moiety per 100 grams (g) of polyol in the liquid transition metal chelate polyol blend and a molar ratio of nitrogen in the nitrogen-based chelating moiety to the transition metal ion of 8.0:1.0 to 1.0:1.0; The transition metal compound is copper(II) 2-ethylhexanoate (CuEH), copper(II) acetate monohydrate (Cu(OAc) ２ H ２ O), copper(II) isobutyrate (Cu(i-Bu) ２ ), and combinations thereof; the molar ratio (N / M) of nitrogen (N) from the amine chelating agent to the transition metal (M) from the organic transition metal salt is greater than 1.1; the nominal amount of transition metal compound particles / solids is less than 0.01 weight percent (wt %) based on the weight of the liquid transition metal chelate polyol blend; the liquid transition metal chelate polyol blend is in a liquid state at a pressure of 80 to 25,000 Kpa and at a temperature of greater than -10°C and less than 80°C; the polyol is an aromatic polyester polyol having aromatic moieties, the aromatic moieties comprising 5 weight percent (wt%) to 60 wt% of the total weight of the aromatic polyester polyol; Liquid transition metal chelate polyol blend.

2. 10. The liquid transition metal chelate polyol blend of claim 1, wherein the nitrogen-based chelating moiety is selected from the group consisting of diamine chelating moieties, triamine chelating moieties, tetraamine chelating moieties, and combinations thereof.

3. 2. The liquid transition metal chelate polyol blend of claim 1, wherein the chelating agent having a nitrogen-based chelating moiety is selected from the group consisting of 2,2'-bipyridine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, 2-[[2-(dimethylamino)ethyl]methylamino]ethanol, 1-[bis[3-(dimethylamino)propyl]amino-2-propanol], 1,2-ethanediamine polymers with methyloxirane, and combinations thereof.

4. 1. An isocyanate-reactive composition comprising: A liquid transition metal chelate polyol blend according to any one of claims 1 to 3; and a polyol different from the polyol in the liquid transition metal chelate polyol blend, wherein the isocyanate-reactive composition comprises 0.1 to 100 weight percent (wt %) of the liquid transition metal chelate polyol blend, said wt % being based on the total weight of the isocyanate-reactive composition, and up to 99.9% wt % of the polyol different from the polyol of the liquid transition metal chelate polyol blend to form the isocyanate-reactive composition.

5. or further comprising 0.1 wt. % to 7.0 wt. % phosphorus from a flame retardant compound selected from the group consisting of phosphates, phosphonates, phosphinates, phosphites, and combinations thereof, said wt. % based on the total weight of said isocyanate-reactive composition; or further comprising a catalyst, a blowing agent, and a surfactant for use in forming a polyurethane polymer foam; or 5. The isocyanate-reactive composition of claim 4, optionally further comprising water for use in forming the polyurethane polymer foam.

6. 1. A reaction mixture for forming a polyurethane polymer or a reaction mixture for forming a polyurethane foam, comprising: an isocyanate compound having an isocyanate moiety; and the isocyanate-reactive composition of any one of claims 4-5, wherein the polyol comprises hydroxyl moieties, and the reaction mixture has a molar ratio of the isocyanate moieties to the hydroxyl moieties of from 0.90:1 to 7:

1.

7. A process for preparing the liquid transition metal chelate polyol blend of any one of claims 1 to 3, said process comprising: Providing a polyol; providing a chelating agent having a nitrogen-based chelating moiety; providing a transition metal compound having a transition metal ion; and combining said polyol, said chelating agent, and said transition metal compound to form said liquid transition metal chelate polyol blend having 0.001 to 1.0 moles of nitrogen in said nitrogen-based chelating moieties per 100 grams of said polyol in said liquid transition metal chelate polyol blend, and having a molar ratio of nitrogen in said nitrogen-based chelating moieties to said transition metal ion of 8.0:1.0 to 1.0:1.

0.

8. 1. A process for preparing a reaction mixture for producing a polyurethane polymer, said process comprising: Providing an isocyanate-reactive composition according to any one of claims 4 to 5; Providing an isocyanate compound having an isocyanate moiety; and combining the isocyanate-reactive composition with the isocyanate compound to form the reaction mixture having a molar ratio of the isocyanate moieties to the hydroxyl moieties of from 0.90:1 to 7:1.

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