LOW COLOR POLYURETHANE PREPOLYMERS FROM PARA-PHENYLENE DIISOCYANATE HAVING LOW FREE ISOCYANATE MONOMER CONTENT AND POLYURETHANES PREPARED THEREFROM
Co-distilling a mixture of para-phenylene diisocyanate (PPDI) and solvent, collecting the mixture of solvent and PPDI as a solution, reacting this solution with a polyol to form a prepolymer, and then removing unreacted PPDI by distillation in the presence of one or more solvents provides lower color prepolymer and higher quality polyurethane resin than a similar process that omits the co-distillation of PPDI and solvent prior to reaction with the polyol.
1 . A process for preparing a prepolymer containing less than 1 wt % free polyisocyanate monomer based on the total weight of the prepolymer from a mixture comprising PPDI and one or more polyols, which process comprises
i) subjecting a mixture comprising, based on the total weight of the mixture, from 5 to 85 wt % polyisocyanate monomer and from 15 to 95 wt % inert organic solvent, wherein 80 to 100% by weight of all polyisocyanate monomer present in the mixture is PPDI, to distillation under conditions wherein PPDI and the inert organic solvent co-distill, and collecting a distillate forming a solution comprising PPDI and inert organic solvent;
ii) preparing a reaction mixture comprising the solution collected as distillate in i) with one or more polyols, which reaction mixture comprises a stoichiometric ratio of isocyanate groups to hydroxyl groups of from 1.1 to 1 to 15:1, under conditions wherein PPDI and the one or more polyol react forming a prepolymer product mixture comprising prepolymer, unreacted PPDI and inert organic solvent, and
iii) subjecting the prepolymer product mixture to distillation conditions to remove unreacted PPDI and inert organic solvent to yield a prepolymer containing less than 1 wt % free polyisocyanate monomer.
2 . The process according to claim 1 wherein 90 to 100% by weight of all polyisocyanate monomer present in the mixture subjected to distillation in i), the reaction mixture and prepolymer product mixture in ii) and the prepolymer product mixture in iii) is PPDI.
3 . The process according to claim 1 wherein 98 to 100 wt % of the polyisocyanate monomer present in the mixture subjected to distillation in i) is PPDI.
4 . The process according to claim 1 , wherein the inert organic solvent present in the mixture subjected to distillation and collected as distillate in i), present in the reaction mixture and prepolymer product mixture of ii), and in the prepolymer product mixture subjected to distillation in iii) comprises one or more solvent having a boiling point at 760 torr of from 100° C. to 259° C.
5 . The process according to claim 1 , wherein the inert organic solvent present in the mixture subjected to distillation and collected as distillate in i), present in the reaction mixture and prepolymer product mixture of ii), and in the prepolymer product mixture subjected to distillation in iii) comprises one or more solvent having a boiling point at 760 torr of greater than 260° C.
6 . The process according to claim 1 , wherein 90 to 100% by weight of all inert organic solvent present in the mixture subjected to distillation and collected as distillate in i), present in the reaction mixture and prepolymer product mixture of ii), and in the prepolymer product mixture subjected to distillation in iii) has a boiling point at 760 torr of from 100° C. to 259° C.
7 . The process according to claim 1 , wherein the mixture subjected to distillation in i) comprises 10 to 60 wt % polyisocyanate monomer, and from 40 to 90 wt % inert organic solvent.
8 . The process according to claim 1 wherein 98 to 100% by weight of all polyisocyanate monomer present in the mixture subjected to distillation in i), the reaction mixture and prepolymer product mixture in ii) and the prepolymer product mixture in iii) is PPDI.
9 . The process according to claim 1 , wherein the distillation of i) and/or iii) is carried out under reduced pressure.
10 . The process according to claim 1 , wherein the distillation of i) and/or iii) comprises distillation conducted in a falling film evaporator, wiped film evaporator and/or short-path distiller.
11 . The process according to claim 9 , wherein the distillation of i) and/or iii) comprises distillation conducted in a falling film evaporator, wiped film evaporator and/or short-path distiller.
12 . The process according claim 1 , wherein the inert organic solvent present in the mixture and distillate of i), in the reaction mixture and prepolymer product mixture of ii) and in the prepolymer product mixture subjected to distillation in iii) comprises one or more compound selected from the group consisting of 1,2,3-trichlorobenzene, 1,2,4-trichlorobenzene, o-dichlorobenzene, m-dichlorobenzene, p-dichlorobenzene, dimethylglutarate, dimethyl adipate, diethyl adipate, dimethyl succinate, gamma-butyrolactone, delta-Valero lactone, propylene carbonate, N-methylpyrollidone and dimethyl phthalate.
13 . The process according to claim 12 wherein the organic solvent present in the mixture and distillate of i), the reaction mixture and prepolymer product mixture of ii) and the prepolymer product mixture subjected to distillation in iii) comprises one or more compound selected from the group consisting of 1,2,3-trichlorobenzene, 1,2,4-trichlorobenzene, o-dichlorobenzene, m-dichlorobenzene, p-dichlorobenzene, dimethylglutarate, dimethyl adipate, diethyl adipate, dimethyl succinate, gamma-butyrolactone, delta-Valero lactone, propylene carbonate and N-methylpyrollidone, and wherein no phthalate is present.
14 . The process according to claim 12 wherein the organic solvent present in the mixture and distillate of i), in the reaction mixture and prepolymer product mixture of ii) and in the prepolymer product mixture subjected to distillation in iii) comprises one or more of dimethylglutarate, dimethyl adipate, diethyl adipate, and dimethyl succinate.
15 . The process according to claim 1 , wherein the prepolymer obtained after iii) comprises less than 0.5 wt % free polyisocyanate monomer.
16 . The process according to claim 1 , wherein the prepolymer obtained comprises less than 0.1 wt % free polyisocyanate monomer.
17 . A prepolymer obtained by the process according to claim 1 .
18 . A polyurethane prepared by reacting the prepolymer according to claim 17 with a curative comprising one or more compounds selected from the group consisting of diols, triols, tetrols, diamines and diamine derivatives.