Emulsifiable isocyanate compositions
a polyisocyanate and composition technology, applied in the field of polyisocyanate derived adducts, can solve the problems of water present, isocyanate group reaction, reducing the working life of emulsifiable polyisocyanate, etc., and achieve the effect of increasing stability and improving stability
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first embodiment
[0047] The first embodiment entails a single step procedure wherein a mono-hydroxy functional monol is reacted with a polyisocyanate to produce the adduct. The total amount of monol added is a stoichiometric equivalent or more with respect to the polyisocyanate. Preferably, the polyols are Carbowax MPEG and Ucon polyols, alone or in combination. The amount of polyol added is sufficient to consume about 99%, preferably 100% of the isocyanate functionality so as to not leave any isocyanate reactive functionality in the resulting polyisocyanate derived adduct.
[0048] The alchol(s) are added at a controlled rate to the polyisocyanate in order to maintain the reaction temperature between about 50.degree. C. to about 100.degree. C., preferably about 70.degree. C. to about 80.degree. C., most preferably below about 85.degree. C. The total amount of monol added to the polyisocyanate is from about 0.95 of an equivalent per equivalent of polyisocyanate, preferably from about 0.99 to 1.03 of mo...
second embodiment
[0050] The second embodiment for manufacture of the polyisocyanate derived adducts of the invention entails a two step procedure. Step one entails reacting a di-hydroxy functional polyol with polyisocyanate to make a polyisocyanate terminated intermediate at a reaction temperature of about 70.degree. C. to about 80.degree. C. The amount of di-hydroxy functional polyol reacted with the polyisocyanate is less than one stoichiometric equivalent with respect to the polyisocyanate. The amount of polyol reacted with the polyisocyanate is preferably not less than about 0.85 of an equivalent per equivalent of isocyanate, more preferably from about 0.90 to 0.97 of polyol to isocyanate equivalent. In step two, a mono-hydroxy functional alchol is reacted with the polyisocyanate terminated intermediate made in the first step. The amount of mono-hydroxy functional monol employed is sufficient to consume about 99%, preferably 100% of the isocyanate functionality without leaving any of the remaini...
example 1
[0062] A round-bottom flask and a stir blade are preheated to 60.degree. C. for further use. 26.31 g of Rubinate 44 is placed into the preheated round-bottom flask equipped with stir blade, stir bearing, stir shaft, nitrogen inlet, thermocouple, temperature controller, heating mantle, and a stopper to produce a reaction mixture. 73.69 g Carbowax MPEG 350 at a temperature of 60.degree. C. is added into the flask to produce a reaction mixture. The reaction temperature is increased from 60.degree. C. to 75.degree. C. over 60 minutes at the heating rate of 0.25.degree. C. / min., and the reaction mixture is allowed to react for 2-3 hours at 75.degree. C. to produce a polyisocyanate derived adduct. The reaction end, identified by infrared analysis, is indicated by no evidence of isocyanate. The structure of the resulting polyisocyanate derived adduct is Carbowax MPEG 350 capped 4,4' MDI. The adduct has a number average molecular weight of 950 as determined by gel permeation chromatography....
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Abstract
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