Process for producing spiroglycol

Abstract

In the production of spiroglycol by the reaction of pentaerythritol and hydroxypivalaldehyde in water in the presence of an acid catalyst, (A) a total content of amines and amine salts in hydroxypivalaldehyde is reduced to 1.5% by weight or lower; (B) seed crystals are added to the reaction system before initiating the reaction and/or during the reaction in an amount from 1.5 to 30% by weight on the basis of the total feed amount of pentaerythritol, hydroxypivalaldehyde, water, the acid catalyst and the seed crystals, each being fed into the reaction system; (C) the pH of the reaction system is kept from 0.1 to 4.0 from initiation of the reaction to completion of the reaction; and (D) the sum of a maximum theoretical amount of spiroglycol to be synthesized from pentaerythritol and hydroxypivalaldehyde to be fed into the reaction system and an amount of spiroglycol contained in the seed crystals to be added to the reaction system is controlled within a range from 5 to 35% by weight on the basis of the total feed amount. The spiroglycol produced has an increased particle size. By washing the spiroglycol with a basic solution, the heat stability is improved.

1 . A process for producing a spiroglycol by a reaction of pentaerythritol and hydroxypivalaldehyde in water in the presence of an acid catalyst, in which 
 (A) a total content of amines and amine salts in hydroxypivalaldehyde is reduced to 1.5% by weight or lower;    (B) seed crystals are added to a reaction system before initiating the reaction and/or during the reaction in an amount from 1.5 to 30% by weight on the basis of a total amount of pentaerythritol, hydroxypivalaldehyde, water, the acid catalyst and the seed crystals, each being fed into the reaction system;    (C) a pH of the reaction system is kept from 0.1 to 4.0 from initiation of the reaction to completion of the reaction; and    (D) a sum of a maximum theoretical amount of spiroglycol to be synthesized from pentaerythritol and hydroxypivalaldehyde to be fed into the reaction system and an amount of spiroglycol contained in the seed crystals to be added to the reaction system is controlled within a range from 5 to 35% by weight on the basis of the total amount of pentaerythritol, hydroxypivalaldehyde, water, the acid catalyst and the seed crystals, each being fed into the reaction system.    
   
   
       2 . The process according to  claim 1 , wherein 98% by weight or lower of a reaction mother liquor obtained by separating spiroglycol crystals from a reaction product liquid is reused in the next reaction.  
   
   
       3 . The process according to  claim 1 , wherein hydroxypivalaldehyde is added to the reaction system over 0.5 to 24 h.  
   
   
       4 . The process according to  claim 1 , wherein the seed crystals are mainly made of spiroglycol.  
   
   
       5 . The process according to  claim 1 , wherein the amines and amine salts are triethylamine and triethylamine salt of formic acid.  
   
   
       6 . The process according to  claim 1 , wherein crystals of spiroglycol are washed with a basic solution after separated from a reaction production liquid.  
   
   
       7 . The process according to  claim 6 , wherein a 1% methanol solution of the spiroglycol after washed with the basic solution has a pH of 7.0 to 12.0.  
   
   
       8 . The process according to  claim 6 , wherein a content of bases and/or salts resulted from a reaction of acids and the bases remaining in the spiroglycol after washed with the basic solution and dried is 10 to 1000 ppm.  
   
   
       9 . The process according to  claim 6 , wherein the basic solution is a solution of an inorganic base in water and/or an organic solvent.  
   
   
       10 . The process according to  claim 6 , wherein a concentration of the base in the basic solution is 10 ppm to 50% by weight.