Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
265 words
A method of forming a liquid, low viscosity, low molecular weight, cross-linkable, stable polyurethane prepolymer which possesses excellent shelf-life and storage-life and which comprises: reacting an aliphatic polyisocyanate with a polyhydroxy compound having a molecular weight of from about 62 to about 3000, selected from the group consisting of triols, mixtures of triols and diols, and mixtures of tetrols and diols, the NCO/OH ratio of said aliphatic polyisocyanate to said polyhydroxy compound being from about 0.7:1 to about 6:1, the reaction between said aliphatic polyisocyanate and said polyhydroxy compound taking place in the presence of a suitable inert, non-reactive organic solvent at a reaction temperature of from about 0° C. to about 70° C. for a reaction time of from about 1/2 hour to about 12 hours in the presence of from about 0.00005% by weight to about 0.8% by weight of a catalyst, based on the total weight of the reaction mixture; terminating said reaction short of completion at a precent completion of reaction of from about 30% to about 80% by lowering the temperature of the reaction mixture to a substantially non-active state, whereby there is formed a liquid, low viscosity, low molecular weight, cross-linkable stable polyurethane prepolymer containing from about 2% by weight to about 30% by weight of unreacted NCO and from about 0.05% by weight to about 10% by weight of unreacted OH in said reaction mixture and having excellent shelf-life and storage-life; and maintaining said reaction mixture at said lowered temperature after said reaction is terminated short of completion, whereby said reaction does not proceed to any material extent.
Claim 2
Independent Claim
265 words
A method of forming a liquid, low viscosity, low molecular weight, cross-linkable, stable polyurethane prepolymer which possesses excellent shelf-life and storage-life and which comprises: reacting an aliphatic polyisocyanate with a polyhydroxy compound having a molecular weight of from about 62 to about 3000, selected from the group consisting of triols, mixtures of triols and diols, and mixtures of tetrols and diols, the NCO/OH ratio of said aliphatic polyisocyanate to said polyhydroxy compound being from about 0.7:1 to about 6:1, the reaction between said aliphatic polyisocyanate and said polyhydroxy compound taking place in the presence of a suitable inert, non-reactive organic solvent at a reaction temperature of from about 0° C. to about 70° C. for a reaction time of from about 1/2 hour to about 12 hours in the presence of from about 0.00005% by weight to about 0.8% by weight of a catalyst, based on the total weight of the reaction mixture; terminating said reaction short of completion at a precent completion of reaction of from about 30% to about 80% by lowering the temperature of the reaction mixture to a substantially non-active state, whereby there is formed a liquid, low viscosity, low molecular weight, cross-linkable stable polyurethane prepolymer containing from about 2% by weight to about 30% by weight of unreacted NCO and from about 0.05% by weight to about 10% by weight of unreacted OH in said reaction mixture and having excellent shelf-life and storage-life; and maintaining said reaction mixture at said lowered temperature after said reaction is terminated short of completion, whereby said reaction does not proceed to any material extent.
Claim 3
Dependent Claim
22 words
A method as defined in claim 1, wherein said NCO/OH ratio is in the range of from about 1.6:1 to about 4:1.
Claim 4
Dependent Claim
24 words
A method as defined in claim 1, wherein said reaction temperature is in the range of from about 0° C. to about 40° C.
Claim 5
Dependent Claim
24 words
A method as defined in claim 1, wherein said reaction time is in the range of from about 1/2 hour to about 5-1/2 hours.
Claim 6
Dependent Claim
13 words
A method as defined in claim 1, wherein said polyisocyanate is a diisocyanate.
Claim 7
Dependent Claim
121 words
A method as defined in claim 1, wherein the viscosity of said reaction mixture at the time of termination of reaction is: from about 10 centipoises to about 100 centipoises for reaction mixtures having a solids content of from about 20% to about 50%; from about 20 centipoises to about 400 centipoises for reaction mixtures having a solids content of from about 50% to about 70%; and in excess of 400 centipoises for reaction mixtures having a solids content greater than 70% and up to 100% but still being flowable and readily pourable and usable, said centipoise values being obtained with a Brookfield No. 2 spindle at 20 r.p.m. at room temperatures with xylene as the suitable inert, non-reactive organic solvent.
Claim 8
Dependent Claim
39 words
A method as defined in claim 1 wherein the reaction is carried out in the presence of from about 0.0005% by weight to about 0.36% by weight of a catalyst, based on the total weight of the reaction mixture.
Claim 9
Dependent Claim
24 words
A method as defined in claim 1, wherein said reaction temperature is in the range of from about 21° C. to about 39° C.
Claim 10
Dependent Claim
25 words
A method as defined in claim 1, wherein said polyurethane prepolymer contains from about 0.1% by weight to about 6% by weight of unreacted OH.
Claim 11
Dependent Claim
25 words
A method as defined in claim 1, wherein said polyurethane prepolymer contains from about 0.18% by weight to about 2% by weight of unreacted OH.
Claim 12
Dependent Claim
27 words
A method as defined in claim 1, wherein said aliphatic polyisocyanate is mixed with said suitable inert, non-reactive organic solvent and said polyhydroxy compound is added thereto.