US2004225104A1PendingUtilityA1

Catalyst systems for polycondensation reactions

Priority: Dec 10, 1999Filed: Jun 7, 2004Published: Nov 11, 2004
Est. expiryDec 10, 2019(expired)· nominal 20-yr term from priority
C08G 63/82B01J 23/06B01J 21/10B01J 21/005B01J 23/007
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Claims

Abstract

The invention pertains to new catalyst systems for polycondensation reactions, for example for producing polyethylene terephthalate. In accordance with the invention, complex compounds with hydrotalcite-analogous structures of general formula [M(II) 1−x M(III) x (OH) 2 ] x+ (A n− x/n ).mH 2 O are used, wherein M(II) represents divalent metals, preferably Mg or Zn or NI or Cu or Fe(II) or Co, and M(III) represents trivalent metals, for example Al or Fe(III), and A represents anions, preferably carbonates or borates. These catalysts can be calcinated and can be used in combination with phosphorus compounds that contain at least one hydrolyzable phosphorus-oxygen bond.

Claims

exact text as granted — not AI-modified
1 . Catalyst systems for polycondensation reactions, characterized in that they are untreated or calcinated hydrotalcite-analogous derivatives of the general formula  
       [M(II) 1−x M(III) x (OH) 2 ] x+ (A n−   x/n ).mH 2 O  
       wherein M(II): divalent metals, M(III): trivalent metals, and A: anions, alone or in combination with phosphorus compounds that contain at least one hydrolyzable phosphorus-oxygen bond.  
     
     
         2 . Catalyst systems for polycondensation reactions in accordance with  claim 1 , characterized in that M(II) is Mg or Zn or Ni or Cu or Fe(II) or Co.  
     
     
         3 . Catalyst systems for polycondensation reactions according to claims  1  or  2 , characterized in that M(III) is Al or Fe(III).  
     
     
         4 . Catalyst systems for polycondensation reactions according to any of  claims 1  to  3 , characterized in that A are carbonates, titanyls or borates.  
     
     
         5 . Catalyst systems for polycondensation reactions according to any of  claims 1  to  4 , characterized in that the calcination of the hydrotalcite-analogous compounds is carried out at temperatures of 200° C. to 800° C., preferably at 400° C. to 650° C.  
     
     
         6 . Catalyst systems for polycondensation reactions in accordance with any of  claims 1  to  5 , characterized in that the polycondensation is carried out with the catalysts under vacuum in liquid phase at temperatures of 230° C. to 280° C. and in solid phase at temperatures of 170 to 240° C.  
     
     
         7 . Catalyst systems for polycondensation reactions in accordance with any of claims  1  through  6 , characterized in that the particle sizes of the hydrotalcites used are in the range of 0.1 to 50 μm, preferably 0.5 to 5 μm.  
     
     
         8 . Catalyst systems for polycondensation reactions in accordance with  claim 1 , characterized in that as the phosphorus compounds, phosphoric acid esters or esters of phosphorous acid are used.  
     
     
         9 . Catalyst systems for polycondensation reactions in accordance with  claim 8 , characterized in that the catalyst system is used in the proportion, hydrotalcite to phosphorus compound, of 1:0.5 to 1:4, preferably of 1:1 to 1:2.  
     
     
         10 . A polycondensation product made using a catalyst as described in any of claims  1  through  9  characterized in that the product is substantially free of heavy metals.  
     
     
         11 . A polycondensation product as in  claim 10  further characterized in that the product is suitable for use in bottles, sheets, films or fibers.

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