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    • 4. 发明申请
    • ROOM TEMPERATURE CURABLE POLYMERS AND PRECURSORS THEREOF
    • 室温可固化聚合物及其前身
    • WO2009009654A1
    • 2009-01-15
    • PCT/US2008/069634
    • 2008-07-10
    • DOW GLOBAL TECHNOLOGIES INC.POPA, PaulLYSENKO, ZenonBABB, DavidKOONCE, WilliamSPILMAN, Gary
    • POPA, PaulLYSENKO, ZenonBABB, DavidKOONCE, WilliamSPILMAN, Gary
    • C08G18/42C08G18/71C09J175/06
    • C08G18/4288C08G18/4269C08G18/4277C08G18/718C08G2190/00C09J175/06
    • A polyester polyol, referred to hereinafter as a MHMS polyol comprises fatty acid based mer units wherein at least about 80 weight percent of the fatty acid based mer units are from methyl 9 (10) hydroxymethylstearate, or is prepared from an oil having fatty acids or fatty acid esters which are at least about 80 weight percent oleic acid or esters thereof and which has an average hydroxyl functionality of from 1.5 to 4. A reaction product, referred to herein after as MHMS alkoxysilane prepolymer, is produced from at least one such MHMS polyol and at least one isocyanate functional silane. The prepolymer is moisture cured to form a silylated MHMS polymer. The process of preparing a MHMS polyol comprises (A) reacting a fatty acid ester wherein at least about 80 weight percent of the fatty acid esters are methyl 9 (10) hydroxymethylstearate, or are prepared from an oil having fatty acids or fatty acid esters which are at least about 80 weight percent oleic acid or esters thereof with an initiator having at least 2 reactive groups selected from primary hydroxyl groups, amine groups, terminal isocyanate groups, terminal carbonyl groups or a combination thereof. The process of preparing at least one MHMS alkoxysilane prepolymer comprises steps of: (a) supplying at least one MHMS polyol; (b) supplying at least one isocyanate functional silane and (c) admixing the MHMS polyol and isocyanate functional silane or combination thereof, optionally in the presence of at least one catalyst to produce at least one MHMS alkoxysilane prepolymer. A process of preparing at least one silylated MHMS polymer comprises steps of: (a) supplying at least one MHMS alkoxysilane prepolymer; and (b) exposing it to moisture under conditions such that at least one silylated MHMS polymer is formed. Articles comprising the polyol, prepolymer, or polymer include elastomers, sealants, adhesives, coatings and the like.
    • 以下称为MHMS多元醇的聚酯多元醇包括脂肪酸基mer单元,其中至少约80重量%的脂肪酸​​基mer单元为9(10)羟甲基硬脂酸甲酯,或由具有脂肪酸或 至少约80重量%的油酸或其酯的脂肪酸酯,其平均羟基官能度为1.5-4。本文以下称为MHMS烷氧基硅烷预聚物的反应产物由至少一种这样的MHMS 多元醇和至少一种异氰酸酯官能的硅烷。 将预聚物水分固化以形成甲硅烷基化的MHMS聚合物。 制备MHMS多元醇的方法包括(A)脂肪酸酯,其中至少约80重量%的脂肪酸​​酯是甲基9(10)羟甲基硬脂酸酯,或由具有脂肪酸或脂肪酸酯的油制备, 至少约80重量%的油酸或其酯与具有至少2个选自伯羟基,胺基,末端异氰酸酯基,末端羰基或其组合的反应性基团的引发剂。 制备至少一种MHMS烷氧基硅烷预聚物的方法包括以下步骤:(a)供应至少一种MHMS多元醇; (b)提供至少一种异氰酸酯官能的硅烷和(c)任选地在至少一种催化剂的存在下混合MHMS多元醇和异氰酸酯官能的硅烷或其组合以产生至少一种MHMS烷氧基硅烷预聚物。 制备至少一种甲硅烷基化MHMS聚合物的方法包括以下步骤:(a)供应至少一种MHMS烷氧基硅烷预聚物; 和(b)在形成至少一种甲硅烷基化的MHMS聚合物的条件下将其暴露于水分。 包含多元醇,预聚物或聚合物的制品包括弹性体,密封剂,粘合剂,涂料等。
    • 5. 发明申请
    • AN ISOCYANATE TRIMERISATION CATALYST SYSTEM, A PRECURSOR FORMULATION, A PROCESS FOR TRIMERISING ISOCYANATES, RIGID POLYISOCYANURATE/POLYURETHANE FOAMS MADE THEREFROM, AND A PROCESS FOR MAKING SUCH FOAMS
    • WO2010054317A2
    • 2010-05-14
    • PCT/US2009/063733
    • 2009-11-09
    • DOW GLOBAL TECHNOLOGIES INC.ATHEY, PhillipWILMOT, NathanKEATON, RichardBABB, DavidBOYER, CecileMORLEY, Timothy
    • ATHEY, PhillipWILMOT, NathanKEATON, RichardBABB, DavidBOYER, CecileMORLEY, Timothy
    • C08G18/18
    • C08G18/4208C08G18/022C08G18/092C08G18/1858C08G18/1875C08G18/2027C08G18/2063C08G2101/0025C08G2105/02C08G2120/00
    • The instant invention provides an isocyanate trimerisation catalyst system, a precursor formulation, a process for trimerising isocyanates, rigid foams made therefrom, and a process for making such foams. The trimerisation catalyst system comprises: (a) an imidazolium or imidazolinium cation; and (b) an isocyanate-trimer inducing anion; wherein said trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73°C. The precursor formulation comprises: (1) at least 25 percent by weight of polyol, based on the weight of the precursor formulation; (2) less than 15 percent by weight of a trimerisation catalyst system, based on the weight of the precursor formulation, comprising; (a) an imidazolium or imidazolinium cation; and (c) an isocyanate-trimer inducing anion; wherein said trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73°C; and (3) optionally one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts, or combinations thereof. The process for trimerisation of isocyanates comprises the steps of: (1) providing one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanatetriisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture of any thereof; (2) providing a trimerisation catalyst system comprising; (a) an imidazolium or imidazolinium cation; and (b) an isocyanate-trimer inducing anion; (c) wherein said trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73°C; (3) trimerising said one or more monomers in the presence of said trimerisation catalyst; (4) thereby forming an isocyanurate trimer. The process for making the PIR foam comprises the steps of: (1) providing one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanatetriisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture any thereof; (2) providing polyol; (3) providing a trimerisation catalyst system comprising; (a) an imidazolium or imidazolinium cation; and (b) an isocyanate-trimer inducing anion; wherein said trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73°C; and (4) optionally providing one or more surfactants, one or more flame retardants, water, one or more antioxidants, one or more auxiliary blowing agents, one or more urethane catalysts, one or more auxiliary trimerisation catalysts, or combinations thereof; (5) contacting said one or more monomers, and said polyol, and optionally said one or more surfactants, and optionally said one or more flame retardants, and optionally said water, and optionally said one or more antioxidants, and optionally said one or more auxiliary blowing agents in the presence of said trimerisation catalyst system and optionally said one or more urethane catalysts, and optionally said one or more auxiliary trimerisation catalysts; (6) thereby forming said polyisocyanurate/polyurethane rigid foam. The PIR foam comprises the reaction product of one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanatetriisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture any thereof with polyol in the presence of a trimerisation catalyst system comprising an imidazolium or imidazolinium cation, and an isocyanate-trimer inducing anion, and optionally one or more surfactants, optionally one or more flame retardants, optionally water, optionally one or more antioxidants, optionally one or more auxiliary blowing agents, optionally one or more additional urethane catalysts, and optionally one or more auxiliary trimerisation catalysts, or optionally combinations thereof, wherein the trimerisation catalyst system has a trimerisation activation temperature in the range of equal to or less than 73°C. The PIR foam comprises the reaction product of one or more monomers selected from the group consisting of an isocyanate, a diisocyanate, a triisocyanatetriisocyanate, oligomeric isocyanate, a salt of any thereof, and a mixture any thereof with polyol in the presence of a trimerisation catalyst system comprising an imidazolium or imidazolinium cation, and an isocyanate- trimer inducing anion, and optionally one or more surfactants, optionally one or more flame retardants, optionally water, optionally one or more antioxidants, optionally one or more auxiliary blowing agents, optionally one or more additional polyurethane catalysts, and optionally one or more auxiliary trimerisation catalysts, or optionally combinations thereof, wherein the PIR foam has a polyisocyanurate trimer ratio (Abs 1410 /Abs 1595 ) of at least 5 at a depth of 12 mm from the rising surface of the rigid foam, measured via ATR-FTIR spectroscopy.