Sprayable, cross-linked trimer polymer and method of use and preparation

Claim 2

A process of preparing a sprayable polyisocyanurate composition, which composition is prepared by mixing and reacting together substantially equal volumes of an A side mixture and a B side mixture, the A side mixture comprising 60 to 100 parts of a MDI having an average functionality of less than about 2.4 and 0 to 40 parts of a polyether triol having a molecular weight of from about 1000 to 6000 and a hydroxyl number of less than about 50, and the B side mixture comprising from about 5 to 40 parts of diethylene glycol, about 50 to 90 parts of a polyether triol having a molecular weight of from 1000 to 6000 and a hydroxyl number of about 50 or less, a catalytic amount of a trimerization catalyst to provide for the rapid exothermic trimerization reaction of the A and B mixtures on mixing, and a catalytic amount of a heat-activated catalyst activated at about 140° F., to provide, on mixing and reacting, a composition which reacts within about 5 seconds, creams within 10 seconds and is substantially cured within 30 seconds.

Claim 3

The process of claim 1 wherein the MDI has an average functionality of about 2.0 or less.

Claim 4

The process of claim 1 wherein the polyether triol has a hydroxyl number of 30 or less.

Claim 5

The process of claim 1 wherein the triol on the B side mixture is present in an amount of from 60 to 80 parts and the diethylene glycol is present in an amount of 20 to 30 parts.

Claim 6

The process of claim 1 wherein the trimerization catalyst is a potassium fatty-acid salt.

Claim 7

The process of claim 5 wherein the potassium fatty-acid salt is potassium octoate.

Claim 8

The process of claim 1 wherein the heat-activated catalyst comprises an acid-blocked phenolic amine salt.

Claim 9

The process of claim 7 wherein the phenolic amine salt comprises a diazobicycloundec-5,-ene phenol blocked salt.

Claim 10

The process of claim 1 wherein the trimerization catalyst is present in an amount of from about 0.1 to 5 parts.

Claim 11

The process of claim 1 wherein the heat-activated catalyst is present in an amount of from about 0.01 to 2.0 parts.

Claim 12

The process of claim 1 which comprises a sprayable, foamable composition which includes a blowing amount of a fluorocarbon blowing agent, a cell-control amount of a surfactant and a tetravalent tin catalyst, to provide a cream time after mixing of less than about 10 seconds.

Claim 13

The process of claim 11 which includes spraying the sprayable foamable composition onto a substrate to provide, after spraying and reacting, a cured foam coating layer on a substrate.

Claim 14

The process of claim 11 which includes spraying the sprayable polyisocyanurate composition onto the surface of a polyisocyanurate rigid foam material to provide a cured coating on at least one surface of the polyisocyanurate foam material.

Claim 15

The process of claim 11 which includes spraying the sprayable polyisocyanurate composition onto a rigid foam board material to provide a cured coating layer on at least one surface thereof.

Claim 16

The process of claim 11 which includes spraying substantially equal volumes of A and B side mixtures in fixed-volume spray equipment to provide, on spraying and reacting, a cured polyisocyanurate composition.

Claim 17

The process of claim 11 wherein the cream-time catalyst is present in an amount of from about 0.1 to 3.0 parts.

Claim 18

The cured composition of claim 1.

Claim 19

The cured foam composition of claim 11.

Claim 20

The process of claim 1 which includes spraying the sprayable polyisocyanurate composition onto a substrate, to provide a thin, solid, cured, coating layer.

Claim 21

A process of preparing a sprayable polyisocyanurate composition, which composition is prepared by mixing and reacting together substantially equal volumes of an A side mixture and a B side mixture, the A side mixture comprising 60 to 100 parts of a MDI having an average functionality of less than about 2.4 and 0 to 40 parts of a polyether triol having a molecular weight of from about 1000 to 6000 and a hydroxyl number of less than about 50, and the B side mixture comprising from 20 to 30 parts of diethylene glycol, 60 to 80 parts of a polyether triol having a molecular weight of from 1000 to 6000 and a hydroxyl number of about 50 or less, a catalytic amount of a potassium octoate trimerization catalyst to provide for the rapid exothermic trimerization reaction of the A and B mixtures on mixing, and a catalytic amount of a heat-activated, diazobicycloundec-5,-ene phenol blocked salt catalyst activated at about 140° F., to provide, on mixing and reacting, a sprayable composition.

Claim 22

A process of preparing a sprayable polyisocyanurate composition, which composition is prepared by mixing and reacting together substantially equal volumes of an A side mixture and a B side mixture, the A side mixture comprising 60 to 100 parts of a MDI having an average functionality of less than about 2.4 and 0 to 40 parts of a polyether triol having a molecular weight of from about 1000 to 6000 and a hydroxyl number of less than about 50, and the B side mixture comprising from 20 to 30 parts of diethylene glycol, 60 to 80 parts of a polyether triol having a molecular weight of from 1000 to 6000 and a hydroxyl number of about 50 or less, a catalytic amount of a potassium octoate trimerization catalyst to provide for the rapid exothermic trimerization reaction of the A and B mixtures on mixing, and a catalytic amount of a heat-activated, diazobicycloundec-5,-ene phenol blocked salt catalyst activated at about 140° F., to provide, on mixing and reacting, a sprayable composition.

Claim 23

A process of preparing a sprayable, foamable, polyisocyanurate composition, which composition is prepared by mixing and reacting together substantially equal volumes of an A side mixture and a B side mixture, the A side mixture comprising 60 to 100 parts of a MDI having an average functionality of less than about 2.4 and 0 to 40 parts of a polyether triol having a molecular weight of from about 1000 to 6000 and a hydroxyl number of less than about 50, and the B side mixture comprising from 20 to 30 parts of diethylene glycol, 60 to 80 parts of a polyether triol having a molecular weight of from 1000 to 6000 and a hydroxyl number of about 50 or less, a catalytic amount of a potassium octoate trimerization catalyst, to provide for the rapid exothermic trimerization reaction of the A and B mixtures on mixing, a catalytic amount of a heat-activated diazobicycloundec-5,-ene phenol block salt catalyst activated at about 140° F., a blowing amount of a fluorocarbon blowing agent, a cell-control amount of a surfactant and a tetravalent tin catalyst, to provide, on mixing and reacting, a sprayable composition.

Claim 24

A process of preparing a sprayable, foamable, polyisocyanurate composition, which composition is prepared by mixing and reacting together substantially equal volumes of an A side mixture and a B side mixture, the A side mixture comprising 60 to 100 parts of a MDI having an average functionality of less than about 2.4 and 0 to 40 parts of a polyether triol having a molecular weight of from about 1000 to 6000 and a hydroxyl number of less than about 50, and the B side mixture comprising from 20 to 30 parts of diethylene glycol, 60 to 80 parts of a polyether triol having a molecular weight of from 1000 to 6000 and a hydroxyl number of about 50 or less, a catalytic amount of a potassium octoate trimerization catalyst, to provide for the rapid exothermic trimerization reaction of the A and B mixtures on mixing, a catalytic amount of a heat-activated diazobicycloundec-5,-ene phenol block salt catalyst activated at about 140° F., a blowing amount of a fluorocarbon blowing agent, a cell-control amount of a surfactant and a tetravalent tin catalyst, to provide, on mixing and reacting, a sprayable composition.

Claim 25

The process of claim 21 which includes spraying the sprayable polyisocyanurate composition onto the surface of a rigid foam board material, to form a coating layer on at least one surface thereof.

Claim 26

The process of claim 21 wherein the cured foam material comprises a rigid, closed-cell, polyisocyanurate foam material having a density of less than about 12 pounds per cubic foot.