Polyol purification process

Claim 2

In a method wherein a C 2 -C 4 alkylene oxide is reacted with an initiator to form an alkylene oxide polymer under alkaline conditions in the presence of a hydroxide, hydride or alkoxide of sodium or potassium and wherein the alkylene oxide polymer is thereafter neutralized with an acid component comprising sulfuric acid, phosphoric acid, acetic acid or oxalic acid and then passed through a filter to obtain a final alkylene oxide polymer product, the improvement which comprises: (a) recovering filter cake resulting from the filtration step; (b) mixing said filter cake with a treating agent comprising a lower aliphatic alcohol containing from about 1 to 4 carbon atoms and also containing from 0 up to about 40 wt. % of water; (c) filtering said mixture; and (d) recovering additional alkylene oxide polymer from said filtrate from said second filtration step.

Claim 3

A method as in claim 1 wherein the alkylene oxide comprises propylene oxide and the treating agent comprises methanol.

Claim 4

In a method as in claim 1 wherein the initiator has a functionality of from about 1 to about 4 and wherein the initiator is reacted under alkaline conditions with an alkylene oxide component consisting of from 100 to about 75 wt. % of propylene oxide and from 0 to about 25 wt. % of ethylene oxide to form a propylene oxide polymer having a molecular weight of up to about 10,000, such product having the formula: R--[O--C.sub.3 H.sub.6 O).sub.n (C.sub.2 H.sub.4 O--.sub.m H].sub.x wherein R is hydrogen or an aliphatic organic residue resulting from the removal of 1 to 4 hydroxyl groups corresponding to the value of x, wherein x has a value of 1 to 4, wherein n has a value from about 4 to about 50 and wherein m has a value of from 0 to about 5, (a) the improvement which comprises washing the filter cake obtained by the filtration of said product with an aqueous solution of methanol at a temperature within the range of about 25° to about 100° C. for a period of time within the range of from about 0.5 to about 5 hours; (b) thereafter refiltering said methanol filter cake mixture; and (c) recovering polyol from the filtrate from said second filtration step.

Claim 5

A method as in claim 3 wherein the filter cake is treated with an aqueous solution of methanol containing from about 10 to about 40 wt. % of water.

Claim 6

In a method for the manufacture of a polyol useful as a raw material in the making of polyurethane foam and wherein a trifunctional initiator containing three hydroxyl groups is reacted with an alkylene oxide component consisting of 100 to about 75 wt. % of propylene oxide and 0 to about 25 wt. % of ethylene oxide under alkaline conditions in the presence of a catalytic amount of a hydroxide, hydride or alkoxide of sodium or potassium to provide a polyoxy alkylene triol having a molecular weight within the range of about 1000 to 10,000 and a hydroxyl number within the range of about 15 to 150, and wherein the triol formed as a result of said reaction is neutralized with sulfuric, phosphoric, acetic or oxalic acid, filtered, and recovered, the improvement which comprises: (a) separately recovering the filter cake formed as a result of the filtration of said triol; (b) mixing from about 0.1 to about 10 parts by weight of filter cake with a treating agent comprising an aqueous solution of methanol containing from about 10 to about 40 wt. % of water at a temperature within the range of about 25° to about 100° C. for a period of time within the range of about 0.5 to about 5 hours; (c) filtering said methanol filter cake mixture in a second filtering operation; and (d) recovering additional triol from said filtrate from said second filtration step.

Claim 7

In a method for the manufacture of a polyol useful as a raw material in the making of polyurethane foam and wherein a trifunctional initiator containing three hydroxyl groups is reacted with an alkylene oxide component consisting of 100 to about 75 wt. % of propylene oxide and 0 to about 25 wt. % of ethylene oxide under alkaline conditions in the presence of a catalytic amount of a hydroxide, hydride or alkoxide of sodium or potassium to provide a polyoxy alkylene triol having a molecular weight within the range of about 1000 to 10,000 and a hydroxyl number within the range of about 15 to 150, and wherein the triol formed as a result of said reaction is neutralized with sulfuric, phosphoric, acetic or oxalic acid, filtered, and recovered, the improvement which comprises: (a) separately recovering the filter cake formed as a result of the filtration of said triol; (b) mixing from about 0.1 to about 10 parts by weight of filter cake with a treating agent comprising an aqueous solution of methanol containing from about 10 to about 40 wt. % of water at a temperature within the range of about 25° to about 100° C. for a period of time within the range of about 0.5 to about 5 hours; (c) filtering said methanol filter cake mixture in a second filtering operation; and (d) recovering additional triol from said filtrate from said second filtration step.

Claim 8

A method as in claim 5 wherein the filter cake is mixed with about 0.5 to about 2.5 parts by weight of said treating agent per part of said filter cake.

Claim 9

In a method for the manufacture of a polyol useful as a raw material in the making of polyurethane foam and wherein an initiator containing one to four hydroxyl groups is reacted with an alkylene oxide component consisting of 100 to about 75 wt. % of propylene oxide and 0 to about 25 wt. % of ethylene oxide under alkaline conditions in the presence of a hydroxide, hydride or alkoxide of sodium or potassium to provide a polyoxy alkylene polyol having a molecular weight within the range of about 1000 to 10,000 and a hydroxyl number within the range of about 15 to 150, and wherein the polyol formed as a result of said reaction is neutralized with an acid component composed of sulfuric acid, phosphoric acid, acetic acid or oxalic acid, filtered, and recovered, the improvement which consists of: (a) separately recovering the filter cake formed as a result of the filtration of said polyol; (b) mixing from about 0.1 to about 10 parts by weight of filter cake with a treating agent consisting of an aqueous solution of methanol containing from about 10 to about 40 wt. % of water at a temperature within the range of about 25° to about 100° C. for a period of time within the range of about 0.5 to about 5 hours; (c) filtering said methanol filter cake mixture in a second filtering operation; and (d) recovering additional polyol from said filtrate from said second filtration step.

Claim 10

In a method for the manufacture of a polyol useful as a raw material in the making of polyurethane foam and wherein an initiator containing one to four hydroxyl groups is reacted with an alkylene oxide component consisting of 100 to about 75 wt. % of propylene oxide and 0 to about 25 wt. % of ethylene oxide under alkaline conditions in the presence of a hydroxide, hydride or alkoxide of sodium or potassium to provide a polyoxy alkylene polyol having a molecular weight within the range of about 1000 to 10,000 and a hydroxyl number within the range of about 15 to 150, and wherein the polyol formed as a result of said reaction is neutralized with an acid component composed of sulfuric acid, phosphoric acid, acetic acid or oxalic acid, filtered, and recovered, the improvement which consists of: (a) separately recovering the filter cake formed as a result of the filtration of said polyol; (b) mixing from about 0.1 to about 10 parts by weight of filter cake with a treating agent consisting of an aqueous solution of methanol containing from about 10 to about 40 wt. % of water at a temperature within the range of about 25° to about 100° C. for a period of time within the range of about 0.5 to about 5 hours; (c) filtering said methanol filter cake mixture in a second filtering operation; and (d) recovering additional polyol from said filtrate from said second filtration step.

Claim 11

A method as in claim 7, wherein the filter cake is mixed with about 0.5 to about 2.5 parts by weight of said treating agent per part of said filter cake.