Optimized Liquid-Phase Oxidation

Abstract

Disclosed is an optimized process and apparatus for more efficiently and economically carrying out the liquid-phase oxidation of an oxidizable compound. Such liquid-phase oxidation is carried out in a bubble column reactor that provides for a highly efficient reaction at relatively low temperatures. When the oxidized compound is para-xylene and the product from the oxidation reaction is crude terephthalic acid (CTA), such CTA product can be purified and separated by more economical techniques than could be employed if the CTA were formed by a conventional high-temperature oxidation process.

1 . A process comprising: 
 (a) introducing a recycled solvent feed into at least one oxidation reactor;    (b) oxidizing an oxidizable compound in a liquid phase of a multi-phase reaction medium contained in a reaction zone of said oxidation reactor; and    (c) withdrawing a slurry comprising a liquid mother liquor and solid crude terephthalic acid (CTA) particles from said reaction zone, wherein a representative sample of said CTA particles contains less than about 5 ppmw of 2,7-dicarboxyfluorenone (2,7-DCF).    
     
     
         2 . The process of  claim 1  wherein said representative sample of said CTA particles dissolve in one minute to a concentration of at least about 500 ppm in THF when subjected to the timed dissolution test defined herein.  
     
     
         3 . The process of  claim 1  wherein said representative sample of said CTA particles have a time constant “C” greater than about 0.5 reciprocal minutes as determine by the timed dissolution model defined herein.  
     
     
         4 . The process of  claim 1  wherein said representative sample of said CTA particles dissolve in two minutes to a concentration of at least 700 ppm in THF when subjected to the timed dissolution test defined herein, wherein said representative sample of said CTA particles have a time constant “C” greater than 0.6 reciprocal minutes as determine by the timed dissolution model defined herein.  
     
     
         5 . The process of  claim 1  wherein said representative sample of said CTA particles have one or more of the following characteristics: 
 (i) contains less than about 6 ppmw of 4,4-dicarboxystilbene (4,4-DCS),    (ii) contains less than about 400 ppmw of isophthalic acid (IPA),    (iii) contains less than about 25 ppmw of 2,6-dicarboxyfluorenone (2,6-DCF),    (iv) has a percent transmittance at 340 nanometers (% T 340 ) greater than about 60.    
     
     
         6 . The process of  claim 1  wherein said representative sample of said CTA particles contains less than about 6 ppmw of 4,4-DCS and less than about 400 ppmw of IPA.  
     
     
         7 . The process of  claim 6  wherein said representative sample of said CTA particles contains less than about 25 ppmw of 2,6-DCF.  
     
     
         8 . The process of  claim 7  wherein said representative sample of said CTA particles has a % T 340  greater than about 60.  
     
     
         9 . The process of  claim 1  wherein said representative sample of said CTA particles has an average BET surface area greater than about 0.6 meter squared per gram.  
     
     
         10 . The process of  claim 1  wherein said representative sample of said CTA particles has a mean particle size in the range of from about 20 to about 150 microns.  
     
     
         11 . The process of  claim 1  wherein said representative sample of said CTA particles has a D(v,0.9) particle size in the range of from about 30 to about 150 microns.  
     
     
         12 . The process of  claim 1  wherein said oxidation reactor is a bubble column reactor.  
     
     
         13 . The process of  claim 1  wherein said oxidizable compound is para-xylene.  
     
     
         14 . A crude terephthalic acid product produced by the process of  claim 1.