Rigid polyurethane foam and multilayer thermal insulation assemblies containing the foam
Rigid polyurethane foams are made using a mixture of polyols that includes 4 to 33% by weight of triisopropanolamine. The mixture of polyols is reacted with an aromatic polyisocyanate in the presence of a blowing agent, a foam-stabilizing surfactant and a urethane catalyst to produce the foam. The foams are useful as thermal insulation layers in multilayer thermal insulation assemblies such as appliance cabinets and walls for industrial and commercial freezers and refrigerators.
1 . A rigid polyurethane foam which is the reaction product of a polyurethane-forming reaction mixture characterized by an isocyanate index of 95 to 150, the polyurethane-forming reaction mixture comprising
A) an aromatic polyisocyanate or mixture of aromatic polyisocyanates, the aromatic polyisocyanate or mixture of aromatic polyisocyanates having an isocyanate functionality of 2 to 4 and an isocyanate equivalent weight of 80 to 175;
B) a mixture of polyols, the mixture of polyols having an average hydroxyl equivalent weight of 125 to 225 and an average hydroxyl functionality of 3.5 to 6 hydroxyl groups per molecule, wherein triisopropanolamine constitutes 4 to 33 weight percent of the mixture of polyols, at least one polyether polyol having 6 to 8 hydroxyl groups and a hydroxyl equivalent weight of 150 to 300 and which does not contain nitrogen atoms constitutes 30 to 90 weight percent of the mixture of polyols, and the mixture of polyols contains no more than 12 weight percent of alkoxylated aromatic amine-initiated polyols;
C) one or more blowing agents in an amount sufficient to produce a foam density of at most 42 kg/m 3 and
D) at least one urethane catalyst and
E) at least one foam-stabilizing surfactant.
2 . The rigid polyurethane foam of claim 1 , wherein alkoxylated aromatic amine-initiated polyols constitute no more than 1 weight percent of the mixture of polyols.
3 . The rigid polyurethane foam of claim 1 wherein the at least one polyether polyol having 6 to 8, hydroxyl groups and a hydroxyl equivalent weight of 150 to 300 and which does not contain nitrogen atoms constitutes 30 to 90 weight percent of the mixture of polyols is one or more sorbitol-initiated polyether polyols that constitute 40 to 70 weight percent of the mixture of polyols.
4 . The rigid polyurethane foam of claim 3 wherein one or more polyether polyols having a hydroxyl equivalent weight of 300 to 750 and a hydroxyl functionality of 2 to 3 constitutes 5 to 35 weight percent of the mixture of polyols.
5 . The rigid polyurethane foam of claim 3 wherein triethanolamine and aliphatic amine-initiated polyols different than triisopropanolamine together constitute no more than 5 weight percent of the mixture of polyols.
6 . The rigid polyurethane foam of claim 3 wherein triisopropanolamine constitutes 6 to 20 weight percent of the mixture of polyols.
7 . A method of making a rigid polyurethane foam of claim 1 , comprising forming and curing a reaction mixture characterized by having an isocyanate index of 95 to 150 wherein the reaction mixture comprises
A) an aromatic polyisocyanate or mixture of aromatic polyisocyanates, the aromatic polyisocyanate or mixture of aromatic polyisocyanates having an isocyanate functionality of 2 to 4 and an isocyanate equivalent weight of 80 to 175;
B) a mixture of polyols, the mixture of polyols having an average hydroxyl equivalent weight of 125 to 225 and an average hydroxyl functionality of 3.5 to 6 hydroxyl groups per molecule, wherein triisopropanolamine constitutes 4 to 33 weight percent of the mixture of polyols, at least one polyether polyol having 6 to 8 hydroxyl groups and a hydroxyl equivalent weight of 150 to 300 and which does not contain nitrogen atoms constitutes 30 to 90 weight percent of the mixture of polyols, and the mixture of polyols contains no more than 12 weight percent of alkoxylated aromatic amine-initiated polyols;
C) one or more blowing agents in an amount sufficient to produce a foam density of at most 42 kg/m 3 and
D) at least one urethane catalyst and
E) at least one foam-stabilizing surfactant.
8 . A method of manufacturing a multilayer thermal insulation assembly, comprising
1) positioning an outer shell member and an inner shell member so as to define a cavity therebetween by holding the outer shell member and inner shell member in a mechanical apparatus that maintains them in a fixed position relative to each other;
2) introducing a polyurethane-forming reaction mixture characterized by an isocyanate index of 95 to 150 into the cavity;
3) curing the polyurethane-forming reaction mixture such that it expands and reacts to produce a polyurethane foam that fills the cavity and adheres to the outer shell member and to the inner shell member to produce the multilayer thermal insulation assembly,
4) and then demolding the multilayer thermal insulation assembly by removing it from the mechanical apparatus, wherein the reaction system comprises the polyurethane-forming reaction mixture comprising
A) an aromatic polyisocyanate or mixture of aromatic polyisocyanates, the aromatic polyisocyanate or mixture of aromatic polyisocyanates having an isocyanate functionality of 2 to 4 and an isocyanate equivalent weight of 80 to 175;
B) a mixture of polyols, the mixture of polyols having an average hydroxyl equivalent weight of 125 to 225 and an average hydroxyl functionality of 3.5 to 6 hydroxyl groups per molecule, wherein triisopropanolamine constitutes 4 to 33 weight percent of the mixture of polyols, at least one polyether polyol having 6 to 8 hydroxyl groups and a hydroxyl equivalent weight of 150 to 300 and which does not contain nitrogen atoms constitutes 30 to 90 weight percent of the mixture of polyols, and the mixture of polyols contains no more than 12 weight percent of alkoxylated aromatic amine-initiated polyols;
C) one or more blowing agents in an amount sufficient to produce a foam density of at most 42 kg/m 3 and
D) at least one urethane catalyst and
E) at least one foam-stabilizing surfactant.
9 . The method of claim 8 wherein step 4) is performed 2.5 to 20 minutes after step 2).
10 . The method of claim 8 wherein step 4) is performed 3 to 6 minutes after step 2).
11 . The method of claim 8 , wherein alkoxylated aromatic amine-initiated polyols constitute no more than 1 weight percent of the mixture of polyols.
12 . The method of claim 8 wherein the at a least one polyether polyol having 6 to 8 hydroxyl groups and a hydroxyl equivalent weight of 150 to 300 and which does not contain nitrogen atoms constitutes 30 to 90 weight percent of the mixture of polyols is one or more sorbitol-initiated polyether polyols that constitute to 70 weight percent of the mixture of polyols.
13 . The method of claim 8 wherein one or more polyether polyols having a hydroxyl equivalent weight of 300 to 750 and a hydroxyl functionality of 2 to 3 constitutes 5 to 35 weight percent of the mixture of polyols.
14 . The method of claim 8 wherein triethanolamine and aliphatic amine-initiated polyols different than triisopropanolamine together constitute no more than 5 weight percent of the mixture of polyols.
15 . The method of claim 8 wherein triisopropanolamine constitutes 6 to 20 weight percent of the mixture of polyols.