Depolymerization of polyurethanes under mild conditions
The present invention relates to an improved process for depolymerization of polyurethanes under mild conditions, wherein polyether polyols and polyamines can be recovered in high yields. The method is practiced by hydrolyzing a polyurethane by contacting with water in the presence of a base containing an alkali metal cation and/or an ammonium cation and having a pK b value at 25° C. of from 1 to 10 and a catalyst selected from the group consisting of quaternary ammonium salts containing an ammonium cation containing 6 to 30 carbon atoms and organic sulfonates containing at least 7 carbon atoms to yield an active hydrogen containing polyether.
1 . A method of hydrolyzing a polyurethane, the method comprising:
contacting said polyurethane with water in the presence of
a base, the base comprising an alkali metal cation and/or an ammonium cation and having a pK b value at 25° C. of from 1 to 10, and
a catalyst selected from the group consisting of a quaternary ammonium salt containing an ammonium cation containing 6 to 30 carbon atoms and an organic sulfonate containing at least 7 carbon atoms,
to yield an active hydrogen containing polyether and an organic polyamine,
wherein the base is selected from the group consisting of alkali metal phosphate, alkali metal hydrogen phosphate, alkali metal carbonate, alkali metal silicate, alkali metal hydrogen carbonate, alkali metal acetate, alkali metal sulfite, ammonium hydroxide, and a mixture thereof.
2 . The method of claim 1 , wherein an alkali metal of the base is selected from the group consisting of Na, K, Li, and a mixture thereof.
3 . The method of claim 1 , wherein the catalyst is a quaternary ammonium salt having the general structure
R 1 R 2 R 3 R 4 NX
wherein R 1 , R 2 , R 3 , and R 4 are the same or different, and are hydrocarbyl groups selected from alkyl, aryl, and arylalkyl, and
X is selected from the group consisting of halide, hydrogen sulfate, alkyl sulfate, carbonate, hydrogen carbonate, carboxylate, and hydroxide.
4 . The method of claim 3 , wherein
R 1 and R 2 are the same or different, and are alkyl groups with 1 to 12 carbon atoms, wherein the alkyl groups may be linear, branched, or cyclic, and saturated or unsaturated,
R 3 is selected from the group consisting of an alkyl group with 1 to 12 carbon atoms, an aryl group with 6 to 14 carbon atoms, and an aralkyl group with 7 to 14 carbon atoms, wherein the alkyl group may be linear, branched, or cyclic, and saturated or unsaturated,
R 4 is selected from the group consisting of an alkyl group with 3 to 12 carbon atoms, an aryl group with 6 to 14 carbon atoms, and an aralkyl group with 7 to 14 carbon atoms, wherein the alkyl groups may be linear, branched, or cyclic, and saturated or unsaturated, and
X is selected from the group consisting of halide, hydrogen sulfate, alkyl sulfate, carbonate, hydrogen carbonate, acetate, and hydroxide.
5 . The method of claim 3 , wherein
R 1 to R 4 are selected such that a sum of carbon atoms in the quaternary ammonium cation is 6 to 14, or
R 1 to R 4 are selected such that the sum of carbon atoms in the quaternary ammonium cation is 15 to 30.
6 . The method of claim 3 , wherein
R 1 to R 4 and X are selected such that a sum of carbon atoms in the quaternary ammonium salt is 6 to 14, or
R 1 to R 4 and X are selected such that the sum of carbon atoms in the quaternary ammonium salt is 15 to 30.
7 . The method according to claim 3 , wherein X is chloride, bromide, methylsulfate, ethylsulfate, or acetate.
8 . The method of claim 1 , wherein the catalyst is an organic sulfonate selected from the group consisting of an alkyl aryl sulfonate, an alpha-olefin sulfonate, a petroleum sulfonate, and a naphthalene sulfonate.
9 . The method of claim 1 , further comprising:
separating and recovering the organic polyamine and the active hydrogen containing polyether.
10 . The method of claim 1 , wherein the polyurethane is foamed.
11 . The method of claim 1 , wherein the polyurethane is reacted with the water, the base, and the catalyst,
at a temperature of from 80° C. to 200° C., and/or
for 1 minute to 14 hours, and/or
at atmospheric pressure.
12 . The method of claim 1 , wherein an amount of the catalyst is at least 0.5 weight percent, based on a weight of the polyurethane.
13 . The method of claim 1 , wherein a weight ratio of the base to the polyurethane is in a range of from 0.01 to 50.
14 . The method of claim 1 , wherein the base is in a form of a base solution comprising the base and water.
15 . The method according to claim 14 , wherein the base solution is a saturated base solution, and
wherein a weight ratio of the saturated base solution to the polyurethane is in a range of from 0.5 to 25.
16 . The method according to claim 1 , further comprising:
producing a polyurethane foam with the active hydrogen containing polyether and/or the organic polyamine.
17 . The method according to claim 1 , wherein the polyurethane is produced by reacting an active hydrogen containing polyether and an organic polyisocyanate.
18 . The method according to claim 1 , wherein the active hydrogen containing polyether is a polyether polyol.
19 . The method according to claim 1 , wherein the base has a pK b value at 25° C. of from 1.5 to 6.