Polymer/polyol compositions made from preformed polymer/polyols, processes for making same and processes for making polyurethane products therefrom

Claim 2

In a polymer/polyol composition which is convertible by reaction with a polyisocyanate to a polyurethane product wherein the polyol of said composition is normally liquid at the temperature at which said composition is converted to said polyurethane product and the polymer of said polymer/polyol is formed in situ in the polyol thereof from one or more polymerizable ethylenically unsaturated monomer, the improvement providing more stable dispersions of small particles of said polymer in the polyol, comprising, an improved dispersion of said polymer prepared by the in situ polymerization of one or more polymerizable ethylenically unsaturated monomers in a blend of a first polyol having a number average molecular weight of at least about 76 and a minor amount of a preformed polymer/polyol prepared by the in situ polymerization of one or more polymerizable ethylenically unsaturated monomers in a second polyol, wherein said preformed polymer/polyol and said improved dispersion have greater dispersion stabilities than the polymer/polyol having the same chemical composition as that of said novel dispersion and made in the same manner as said novel dispersion but in the absence of said preformed polymer/polyol and said preformed polymer/polyol has a viscosity of less than 40,000 cps at 25° C., said polymer being dispersed in said polyol.

Claim 3

Composition as claimed in claim 1 wherein said improved dispersion has a centrifugible solids of at least 10 percent less than that of said polymer/polyol having the same chemical composition as that of said novel dispersion and made in the same manner as said novel dispersion but in the absence of said preformed polymer/polyol.

Claim 4

Composition as claimed in claim 1 wherein said improved dispersion has a centrifugible solids of at least 30 percent less than that of said polymer/polyol having the same chemical composition as that of said novel dispersion and made in the same manner as said novel dispersion but in the absence of said preformed polymer/polyol.

Claim 5

Composition as claimed in claim 1 wherein said improved dispersion has a centrifugible solids of at least 50 percent less than that of said polymer/polyol having the same chemical composition as that of said novel dispersion and made in the same manner as said novel dispersion but in the absence of said preformed polymer/polyol.

Claim 6

Composition as claimed in claim 1 wherein said preformed polymer/polyol has a viscosity of not more than 35,000 cps at 25° C.

Claim 7

Composition as claimed in claim 1 wherein said preformed polymer/polyol has a viscosity of not more than 10,000 cps at 25° C.

Claim 8

Composition as claimed in claim 1 wherein said first and second polyols are different and said preformed polymer/polyol has a centrifugible solids of not more than about 20 wt-%.

Claim 9

Composition as claimed in claim 7 wherein said preformed polymer/polyol has a centrifugible solids of not more than about 10 wt-%.

Claim 10

Composition as claimed in claim 1 wherein said first polyol has a number average molecular weight of at least about 134 and said second polyol has a number average molecular weight of at least about 3000.

Claim 11

Composition as claimed in claim 1 wherein said first polyol has a number average molecular weight of less than 3000 and said second polyol has a number average molecular weight greater than that of said first polyol.

Claim 12

Composition as claimed in claim 1 wherein said blend comprises about 55 to about 95 wt-% of said first polyol and about 5 to about 45 wt-% of said preformed polymer/polyol.

Claim 13

Composition as claimed in claim 1 wherein said blend comprises about 70 to about 90 wt-% of said first polyol and about 10 to about 30 wt-% of said preformed polymer/polyol.

Claim 14

Composition as claimed in claim 1 wherein the total amount of polymer dispersed in said blend is about 4 to about 45 wt-% based on the weight of the composition.

Claim 15

Composition as claimed in claim 1 wherein the amount of polymer dispersed in said blend is about 15 to about 40 wt-% based on the weight of the composition.

Claim 16

Composition as claimed in claim 14 wherein said polymer comprises polymerized acrylonitrile.

Claim 17

Composition as claimed in claim 14 wherein said polymer comprises at least 75 wt-% polymerized styrene.

Claim 18

Composition as claimed in claim 15 wherein said polymer consists essentially of acrylonitrile.

Claim 19

Composition as claimed in claim 15 wherein said polymer also contains polymerized styrene.

Claim 20

Composition as claimed in claim 18 wherein the weight ratio of polymerized acrylonitrile to polymerized styrene in said polymer ranges from 20:80 to 100:0.

Claim 21

Composition as claimed in claim 18 wherein the weight ratio of polymerized acrylonitrile to polymerized styrene in said polymer ranges from 25:75 to 0:100.

Claim 22

Composition as claimed in claim 20 wherein said ratio is 25:75.

Claim 23

Composition as claimed in claim 19 wherein the weight ratio of polymerized acrylonitrile to polymerized styrene in said polymer ranges from about 40:60 to 85:15.

Claim 24

Composition as claimed in claim 18 wherein said polymer also contains polymerized methyl methacrylate.

Claim 25

Composition as claimed in claim 23 wherein the weight ratio of polymerized acrylonitrile to polymerized methyl methacrylate to polymerized styrene is about 25 to about 25 to about 50.

Claim 26

Composition as claimed in claim 1 wherein the number average molecular weight of the first polyol is in the range of about 76 to about 5000 and that of the second polyol is in the range of about 3000 to about 20000.

Claim 27

Composition as claimed in claim 1 wherein the number average molecular weight of the first polyol is in the range of about 134 to about 3000 and that of the second polyol is in the range of about 3000 to about 15000.

Claim 28

Composition as claimed in claim 1 wherein said preformed polymer/polyol is prepared by polymerization in the presence of a peroxyester free radical catalyst.

Claim 29

Composition as claimed in claim 27 wherein said polymerization of said polymerizable ethylenically unsaturated monomers in a blend of said first polyol and said preformed polymer/polyol is carried out in the presence of 2,2'-azo-bisisobutyronitrile.

Claim 30

In a process for producing a liquid polymer/polyol composition which is convertible by reaction with a polyisocyanate to a polyurethane product wherein the polyol of said composition is normally liquid at the temperature at which said composition is converted to said polyurethane product and said polymer is formed in situ in said polyol from one or more polymerizable ethylenically unsaturated monomers, the improvement utilizing first and second polyols and providing more stable dispersions of small particles of said polymer in said polyols, comprising, polymerizing one or more polymerizable ethylenically unsaturated monomers in the presence of a first free radical catalyst in said second polyol to form a preformed polymer/polyol having a viscosity of less than 40000 cps at 25° C.; mixing a major amount of said first polyol having a number average molecular weight of at least about 76 with a minor amount of said preformed polymer/polyol to form a mixture thereof; and polymerizing one or more polymerizable ethylenically unsaturated monomers in the presence of a second free radical catalyst in said mixture to form said composition in which said polymer is formed in situ from both said portions of said monomer or monomers and is dispersed in said polyols and wherein each of said preformed polymer/polyol and said more stable dispersion have a greater dispersion stability than the polymer/polyol having the same chemical composition as that of said more stable dispersion and made in the same manner as said more stable dispersion but in the absence of said preformed polymer/polyol.

Claim 31

In a process for producing a liquid polymer/polyol composition which is convertible by reaction with a polyisocyanate to a polyurethane product wherein the polyol of said composition is normally liquid at the temperature at which said composition is converted to said polyurethane product and said polymer is formed in situ in said polyol from one or more polymerizable ethylenically unsaturated monomers, the improvement utilizing first and second polyols and providing more stable dispersions of small particles of said polymer in said polyols, comprising, polymerizing one or more polymerizable ethylenically unsaturated monomers in the presence of a first free radical catalyst in said second polyol to form a preformed polymer/polyol having a viscosity of less than 40000 cps at 25° C.; mixing a major amount of said first polyol having a number average molecular weight of at least about 76 with a minor amount of said preformed polymer/polyol to form a mixture thereof; and polymerizing one or more polymerizable ethylenically unsaturated monomers in the presence of a second free radical catalyst in said mixture to form said composition in which said polymer is formed in situ from both said portions of said monomer or monomers and is dispersed in said polyols and wherein each of said preformed polymer/polyol and said more stable dispersion have a greater dispersion stability than the polymer/polyol having the same chemical composition as that of said more stable dispersion and made in the same manner as said more stable dispersion but in the absence of said preformed polymer/polyol.

Claim 32

Process as claimed in claim 29 wherein said mixture comprises about 55 to about 95 wt-% of said first polyol and about 5 to about 45 wt-% of said preformed polymer/polyol.

Claim 33

Process as claimed in claim 29 wherein said first and second free radical catalysts are the same.

Claim 34

Process as claimed in claim 29 wherein said second free radical catalyst is 2,2'-azo-bis-isobutyronitrile.

Claim 35

Process as claimed in claim 29 wherein said first free radical catalyst is a preoxyester free radical catalyst.

Claim 36

Process as claimed in claim 29 wherein said first free radical catalyst is a peroxyester free radical catalyst and said second free radical catalyst is 2,2'-azo-bis-isobutyronitrile.

Claim 37

A method for producing a polyurethane elastomer by reacting a mixture comprising (a) a polymer/polyol composition as claimed in claim 1 and (b) an organic polyisocyanate, in the presence of (c) a catalyst for the reaction of (a) and (b) to produce the polyurethane.

Claim 38

A method for producing a polyurethane foam by reacting and foaming a mixture comprising (a) the polymer/polyol composition claimed in claim 1, (b) an organic polyisocyanate, (c) a catalyst for the reaction of (a) and (b) to produce the polyurethane, (d) a blowing agent and (e) a foam stabilizer.

Claim 39

A method as claimed in claim 36 wherein the foam is a flexible foam, the reaction and foaming are preformed by the one-shot technique, the polymer/polyol composition contains an alkylene oxide adduct of a polyhydroxyalkane, the blowing agent is water and the water is used in an amount to provide a foam having a density of less than 1.75 pounds per cubic foot.

Claim 40

Method as claimed in claim 36 in which said polymer/polyol composition is that claimed in claim 18.

Claim 41

Method as claimed in claim 36 in which said polymer/polyol composition is that claimed in claim 20.