Process of sulfating select polymers

Abstract

A process for sulfating alkoxylated amines, alkoxylated polyols, hydrophobic polyamine ethoxylate polymers, via the use of sulfuric acid.

1 . A process for sulfating oligomers and polymers comprising the steps of:
 a) sulfating an oligomer or polymer selected from the group consisting of alkoxylated amines, alkoxylated polyols, hydrophobic polyamine ethoxylate polymers, and any mixture thereof; by the addition of sulfuric acid to make a sulfated oligomer and water mixture;   b) optionally driving off the water from the sulfated oligomer or polymer and water mixture to make a dried sulfated oligomer or polymer mixture;   c) neutralizing the sulfated oligomer or polymer mixture of step (a) or optionally the dried sulfated oligomer or polymer mixture of step (b) by mixing with neutralization agent.   
   
   
       2 . The process of  claim 1  wherein the sulfation of step a) may further sulfate the oligomer or polymer by adding sulfuric acid, dimethyl sulfate, water and a non-sulfating acid, to make a oligomer or polymer mixture, such that the oligomer or polymer mixture has a pH of 2. 
   
   
       3 . The process of  claim 1  wherein the process comprises the driving step of b) and further comprises driving off the water by heating the sulfated oligomer or polymer and water mixture at a temperature from 20 to 150° C. 
   
   
       4 . The process of  claim 3  wherein the driving step of b) further comprises driving off the water by heating the sulfated oligomer or polymer and water mixture at a temperature from 20° C. to 85° C. such that the oligomer/polymer is liquid. 
   
   
       5 . The process of  claim 4  wherein the driving step of b) is at a temperature of 80° C. 
   
   
       6 . The process of  claim 1  wherein the driving step of b) comprises adding an inert solvent that azeotropes with water. 
   
   
       7 . The process of  claim 6  wherein the inert solvent is selected from benzene. 
   
   
       8 . The process of  claim 3  wherein the driving step of b) further comprises driving off the water by having a pressure from about 66.7 Pa to about 50.7 kPa. 
   
   
       9 . The process of  claim 1  wherein the driving step of b) is such that the dried oligomer or polymer mixture comprises from 0.01 wt % to about 20 wt % by weight of the dried oligomer or polymer mixture of water. 
   
   
       10 . The process of  claim 2  wherein the driving step of b) is such that the dried oligomer or polymer mixture comprises from 0.01 wt % to about 20 wt % by weight of the dried oligomer or polymer mixture of water. 
   
   
       11 . The process of  claim 10  wherein the driving step of b) is such that the dried oligomer or polymer mixture comprises from 0 wt % to 20% by weight of the dried oligomer or polymer mixture of methanol. 
   
   
       12 . The process of  claim 1  wherein the sulfuric acid is added to the oligomer or polymer selected from the group consisting of alkoxylated amines, alkoxylated polyols, hydrophobic polyamine ethoxylate polymers, and any mixture thereof; in a molar amount according to formula (I):
   Mole amount of oligomer/polymer*# site available for sulfation*desired % level of sulfation for # sites available for sulfation.   
   
   
       13 . A method of determining the molar amount of sulfuric acid for sulfation of an oligomer or polymer selected from the group consisting of alkoxylated amines, alkoxylated polyols, hydrophobic polyamine ethoxylate polymers, and any mixture thereof; via the use of formula (I):
   Mole amount of oligomer/polymer*# site available for sulfation*desired % level of sulfation for # sites available for sulfation.