Patent Publication Number: US-4222932-A

Title: Polyarylene arylate compositions

Description:
This invention relates to a stabilizer for polyarylene esters, to a stabilized polyarylene ester composition and to a method of stabilizing polyarylene esters, and more particularly to a stabilizer comprising an isocyanate and a phosphite, to a polyarylene ester stabilized with an isocyanate and a phosphite and to a method of stabilizing polyarylene esters with an isocyanate and a phosphite. 
     Polyarylene esters have many superior properties which make them useful as engineering thermoplastics including good mechanical properties, high heat distortion temperature, good fire retardancy and good solvent resistance. Despite these superior properties, polyarylene esters have a serious deficiency in their lack of hydrolytic stability. To some extent this deficiency has been overcome by adding a phosphite stabilizer. 
     I have now discovered that polyarylene esters can be more effectively stabilized by adding an aromatic isocyanate and an aliphatic phosphite compound in a synergistically effective amount. More specifically, the polyarylene esters are stabilized against hydrolytic and/or thermal degradation by the addition of a synergistically effective amount of a mixture of an armatic isocyanate and an aliphatic phosphite. Other aspects of the invention are directed to the mixture of isocyanate and phosphite suitable for stabilizing the polyarylene ester, to molded articles produced from the stabilized polyarylene ester and to an a process of stabilizing the polyarylene ester by mixing the polyarylene ester in powder or pellet form with a synergistically effective amount of a stabilizing mixture of isocyanate and phosphite followed by melt blending of the admixture. 
     The polyarylene ester is the condensation product of at least one C 8  to C 25  armoatic dicarboxylic acid and at least one C 6  to C 25  diphenol. While essentially any suitable C 8  to C 25  aromatic dicarboxylic acid and admixture thereof can be used in the preparation of the polyarylene esters, the preferred aromatic dicarboxylic acids are selected from the group consisting of isophthalic acid, terephthalic acid, bibenzoic acid, naphthalene dicarboxylic acid, bis(4-carboxyphenyl)methane, 1,2-bis(4-carboxyphenyl)ethane, 2,2-bis(4-carboxyphenyl)propane, bis(4-carboxyphenyl)oxide, bis(4-carboxyphenyl)sulfide and bis(4-carboxyphenyl)sulfone and alkyl and halogen substitutive derivatives thereof. Similarly, while essentially any suitable C 6  to C 25  diphenol and admixture thereof can be used in the preparation of the polyarylene esters, the preferred diphenols are selected from the group consisting of resorcinol, hydroquinone, diphenol, dihydroxynaphthalene, bis(4-hydroxyphenyl)methane, 1,2-bis(4-hydroxyphenyl)ethane, bis(4-hydroxyphenyl)sulfide, 2,2-bis(4-hydroxyphenyl)propane, bis(4-hydroxyphenyl)oxide and bis(4-hydroxyphenyl)sulfone and alkyl and halogen substitutive derivatives thereof. Among the especially preferred polyarylene esters are the condensation products of bis(4-hydroxyphenyl)methane, 1,2-bis(4-hydroxyphenyl)ethane and 2,2-bis(4-hydroxyphenyl)propane and isophthalic and terephthalic acids. 
     The weight average molecular weight of the polyarylene esters is at least about 10,000 and is preferably in the range of about 20,000 to about 100,000. The molecular weight is selected to provide a balance in processability and mechanical properties of the polyarylene ester. 
     The polyarylene ester can be produced by an convenient method such as by melt condensation or solvent condensation of mixtures of aromatic dicarboxylic acids and diphenol diesters selected to provide polyarylene esters of the desired molecular weight and processability. They can be produced by melt or solution polymerization of selected mixtures of phenol esters of aromatic dicarboxylic acids and diphenols and by interfacial polymerization of salts of diphenols and aromatic dicarboxylic acid dihalides. Thus, while the combination is formally a condensate of diacid and diphenol, in practice the reactants are diacids and diphenol esters, or phenyl esters of diacids and diphenols, or salts of diphenols and diacid halides. 
     A preferred method of peparation is the melt condensation of mixtures of aromatic dicarboxylic acids and diphenol diesters. Another preferred method is the melt condensation of mixtures of aromatic dicarboxylic acids and diphenol diesters to a prepolymer stage followed by solid state polymerization to advance the polymer to the desired molecular weight. When the polyarylene ester is prepared by these preferred methods, the polyester molecules are terminated by phenolic ester and aromatic carboxylic acid groups. The concentration of armoatic carboxylic acid groups is generally at least about 5 microequivalents per gram of polyester and with polyesters in the preferred molecular weight range the concentration is generally in the range of about 10 to about 200 microequivalents per gram of polyester. 
     The polyarylene ester is stabilized with a synergistic amount of an isocyanate and an aliphatic phosphite. The amount of isocyanate used is preferably from about 0.1 to about 3 equivalents per equivalent of free carboxyl in the polyarylene ester, and preferably is in the range of about 0.5 to about 2 equivalents. When more than 3 equivalents of isocyanate per equivalent of free carboxyl is used the polyarylene ester tends to develop excessive color. Indeed even when the amount of isocyanate is less than 2 equivalents per equivalent of free carboxyl, a considerable increase in color is observed if it is used as the only stabilizer. However, when the combination of isocyanate and phosphite is used, as well as an improvement in hydrolytic stability which is demonstrated by a significant retention of molecular weight, there is a marked decrease in discoloration of the polyester. The ratio of phosphite to isocyanate can range widely from about 0.01 to about 10 equivalents per equivalent of isocyanate and is preferably in the range of about 0.1 to about 1.0 equivalents. High ratios of phosphite may adversely affect the color and the mechanical properties of the polyester although they may improve its flame retardancy. 
     By isocyanates I mean monoisocyanates, monoisothiocyanates, diisocyanates, diisothiocyanates, polyisocyanates and polyisothiocyanates of molecular weight less than about 1000. 
     Basically, any aromatic isocyanate of the above types are suitable for the manufacture of the stabilized polyarylene esters. As an example of aromatic monoisocyanates, mention may be made of phenyl isocyanate, tolyl isocyanates, xylyl isocyanates, biphenyl isocyanates, and naphthyl isocyanates. Examples of aromatic diisocyanates are phenylene diisocyanates, tolylene diisocyanates, xylylene diisocyanates, biphenyl diisocyanates, naphthylene diisocyanates, 4,4&#39;-diphenylmethane diisocyanate, 4,4&#39;-diphenylsulfone diisocyanate, 4,4&#39;-diphenylether diisocyanate and the like. In place of the above it is possible to use the corresponding isothiocyanates. 
     Masked isocyanates or isocyanate-donating compounds may be used as a means of introducing the isocyanate without exposing it to the hydrolyzing effect of atmospheric moisture. Masked isocyanates are for example dimeric isocyanates and isocyanate donating compounds are for example adducts of isocyanates with acidic compounds containing OH, NH, CH or SH such as the adducts of tolylene-2,4-diisocyanate with phenol, pyrrolidone or caprolactam. 
     The phosphite components of the invention are aliphatic phosphites of boiling point greater than about 300° C. and of molecular weight less than about 2000. They includes phosphites defined by the following six structures: ##STR1## where R 1  is a substituted or unsubstituted alkyl, cycloalkyl or aralkyl radical having 1-18 carbon atoms. Examples of such radicals include methyl, ethyl, propyl, butyl, 2,2-dimethylbutyl, 2,2-dimethylhexyl, n-pentyl, n-hexyl, cyclopentyl, cyclohexyl, 2-ethylhexyl, n-octyl, iso-octyl, n-nonyl, n-decyl, iso-decyl, dodecyl or lauryl, hexadecyl or stearyl, phenylethyl, tolylethyl, cyclohexylethyl and the like. Such compounds include triisooctyl phosphite, triisodecyl phosphite, trilauryl phosphite and tristearyl phosphite. ##STR2## where R 1  is a radical as defined above and R 2  and R 3  are hydrogen or R 1  radials or substituted or unsubstituted aryl radicals having 6-18 carbon atoms such as phenyl, tolyl, naphthyl and the like. Preferred compounds include lauryl neopentyl glycol phosphite, stearyl neopentyl glycol phosphite and phenylethyl neopentyl glycol phosphite. ##STR3## where R 4  is a polyvalent substituted or unsubstituted alkyl, cycloalkyl or aralkyl radical or a poly(alkylene oxide) radical having 2-12 carbon atoms and n is an integer of 2-4, and R 2  and R 3  are radicals as defined above. 
     Examples of divalent alkyl radicals having 2-12 carbon atoms include ethylene, propylene, 2,2-dimethyl trimethylene, decamethylene, and the like. 
     Examples of divalent poly(alkylene oxide) radicals having 2-12 carbon atoms include ##STR4## 
     A preferred compound is bis(neopentylglycol)triethylene glycol diphosphite corresponding to the structure: ##STR5## where R 1  is a radical as defined above. 
     Preferred compounds include di(stearyl) pentaerythritol diphosphite corresponding to the structure, ##STR6## di(isodecyl) pentaerythritol diphosphite and di(lauryl) pentaerythritol diphosphite. ##STR7## where R 1  is a radical as defined above, and ##STR8## where R 4  is a divalent radical as defined above. A preferred compound is dipentaerythritol diphosphite corresponding to the structure ##STR9## 
     These phosphites and methods for their preparation are well known in the art. Of the six groups set forth above, the cyclic phosphites of groups 4, 5 and 6 are especially preferred. 
     The compositions of this invention can be formed according to methods well known in the art, such as melt blending, extrusion, and the like. The order of addition of the components of the composition is immaterial. In a preferred embodiment, pellets of polyarylene ester are coated by tumbling the pellets with a mixture of isocyanate and phosphite until the mixture is absorbed by the polyester. The admixture is then placed in the hopper of an extruder and extruded under high back pressure. In another preferred embodiment the polyarylene ester is tumble mixed with the phosphite at a temperature above the melting point of the phosphite until the phosphite is absorbed by the polyester. The polyester is then cooled to room temperature and is tumble mixed with the isocyanate until it has in turn been absorbed. The admixture is then placed in the hopper of an extruder and extruded under high back pressure. 
     The compositions of this invention can be extruded into sheets or molded into various articles by conventional molding techniques, such as injection molding. 
     The compositions of this invention can contain various other materials useful for modifying the properties of the composition. For example, the composition can contain mold release agents, glass fibers, flame retardants, pigments, stabilizers, extenders and numerous other materials commonly incorporated into molding plastics. 
     The invention is further described and illustrated in the examples which follow. The examples should not be construed as limiting the scope of the invention to their details. All parts and percentages are by weight unless otherwise indicated. 
    
    
     EXAMPLE 1 
     Preparation and Formulation of Polyisophthalate of 2,2-Bis(4-Hydroxyphenyl)Propane 
     An equimolar mixture of 2,2-bis(4-acetoxyphenyl)propane (Bisphenol A diacetate) and isophthalic acid is heated gradualy to 290° C. in a stirred vessel under gradually increasing vacuum to remove the acetic acid which is liberated. When the melt viscosity of the condensate reaches a level such that stirring becomes difficult the melt is drained from the reaction vessel and crystallized. The crystallized polymer is subjected to solid state polymerization under vacuum at 280° C. until the inherent viscosity reaches 0.65 dl/g (in 40/60 by weight tetrachloroethane/phenol solution at 25° C.). The polymer is then extruded at 350° C. and pelletized. The polymer has an inherent viscosity of 0.62 and a carboxylic acid content of 40 microequivalents per gram (μeq./g), determined by potentiometric titration of a solution of the polymer in a 2,6-dimethylphenol/chloroform/ethanol mixture with an ethanolic solution of potassium hydroxide. 
     The pellets are dried in a vacuum oven to &lt;0.02% mixture and then stored under nitrogen. The polymer pellets are used to prepare the following formulations. 
     Control #1--The polymer pellets without additives. 
     Control #2--To 100 parts of polymer pellets at room temperature, 1.33 parts of m-tolyl isocyanate are added. This equals 100 microequivalents of isocyanate per gram of polymer. The mixture is stirred until all the isocyanate is absorbed by the polymer. 
     Control #3--To 100 parts of polymer pellets at 75° C., 0.5 parts of di(stearyl)pentaerythritol diphosphite is added. The mixture is stirred to disperse the phosphite ester. 
     Example 1--To 100 parts of polymer pellets at 75° C., 0.5 parts of di(stearyl)pentaerythritol diphosphite is added. The mixture is stirred and cooled to room temperature, then 1.33 parts of m-tolyl isocyanate are added. The mixture is stirred until all the isocyanate is absorbed. 
     A. EXTRUSION OF THE FORMULATIONS 
     Each of the above formulations is extruded at 300° C. using a 1&#34; laboratory extruder equipped with a two stage screw and a vent open to the atmosphere. The open vent allows the CO 2  which is generated by the reaction of isocyanate and carboxylic acids to escape. The extrudates are pelletized, after which inherent viscosity and residual carboxylic acid content are measured as described above. 
     B. DETERMINATION OF HYDROLYTIC STABILITY 
     Samples of the extruded pellets are placed in open dishes and aged at 150° C. in an atmosphere that is nearly pure steam plus a minor amount of air. Samples are removed periodically and tested for inherent viscosity. 
     The properties of the formulations as obtained from the extruder and after aging in 150° C. steam for 72 hours are given in Table I. It is seen that the formulation of this invention, Example 1, is more resistant to hydrolysis than the controls. It is also seen that the use of isocyanate alone, without added phosphite ester results in a highly colored extrudate. 
     
                       TABLE I                                                     
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                                  Inherent Vis-                           
        Inherent --COOH           cosity after Aging                      
        Viscosity                                                         
                 Unaged   Color   72 hr. in                               
Sample  Unaged   μeq/g.                                                
                          Unaged  150° C. Steam                    
______________________________________                                    
Control #1                                                                
        .60      40       Lt. Amber                                       
                                  .20                                     
Control #2                                                                
        .56      3        Dk. Brown                                       
                                  .22                                     
Control #3                                                                
        .61      32       Lt. Amber                                       
                                  .26                                     
Example 1                                                                 
        .59      3        Amber   .39                                     
______________________________________                                    
 
    
     EXAMPLE 2 
     Another sample of polyisophthalate of 2,2-bis(4-hydroxyphenyl)propane is prepared essentially as in Example 1. This polymer has an inherent viscosity of 0.66 and a carboxylic acid content of 30 μeq/g. The dried polyester pellets are used to prepare the various formulations listed in Table II. The methods of addition of the additives, extrusion of the mixture and aging in steam are as described in Example 1. From the results it can be seen that: 
     1. An excessive amount of either isocyanate or phosphite ester results in highly colored extrudate and/or less than optimum hydrolytic stability. 
     2. A minimum of about 8 microequivalents of the hexavalent phosphite ester per gram of polyester is required for optimum color and hydrolytic stability. 
     
                       TABLE II                                                    
______________________________________                                    
                               Inherent                                   
              Properties After Viscosity                                  
Additives     Extrusion        After                                      
Iso-                  In-                Aging                            
cyan- μeq/g.                                                           
              Phos-   herent             72 hr. in                        
ate   Poly-   phite   Vis-  --COOH       150° C.                   
(1)   mer     Wt. %   cosity                                              
                            μeq/g                                      
                                   Color Steam                            
______________________________________                                    
None  --      None    .61   30     Lt.   .17                              
                                   Amber                                  
mTI   35      0.1     .65   2      Lt.   .36                              
                                   Amber                                  
&#34;     35      0.3     .64   3      Lt.   .37                              
                                   Amber                                  
&#34;     50       0.05   .63   2      Dk.   .29                              
                                   Brown                                  
&#34;     50      0.3     .62   --     Lt.   .45                              
                                   Amber                                  
&#34;     50      0.5     .60   --     Lt.   .34                              
                                   Amber                                  
&#34;     100     0.1     .58   2      Brown .25                              
&#34;     100     0.3     .58   --     &#34;     .33                              
&#34;     150     0.5     .55   --     &#34;     .26                              
pTI   50      0.3     .66   4      Lt.   .40                              
                                   Amber                                  
2,5-D 50      0.3     .63   --     Brown .40                              
______________________________________                                    
 (1) mTI and pTI = mtolyl isocyanate and ptolyl isocyanate, 2,5D =        
 2,5dichlorophenyl isocyanate.                                            
 
    
     EXAMPLE 3 
     Another sample of polyisophthalate of 2,2-bis(4-hydroxyphenyl)propane is prepared by the method of Example 1. It has an inherent viscosity of 0.60 and a carboxylic acid content of 60 μeq/g. Portions are mixed with various isocyanates and phosphite esters then extruded and tested as in Examples 1 and 2. The formulations and results are given in Table III. The results show that: 
     1. Both diisocyanates and monoisocyanates, or combinations of the two are effective stabilizers when used in combination with a phosphite ester of the type described in this invention. 
     2. An aromatic phosphite ester is less effective when used in combination with an isocyanate since it causes the development of a dark brown discoloration. 
     3. An aliphatic isocyanate is rather ineffective when it is used in combination with phosphite ester since it gave little improvement in stability of the polyester. 
     
                                           TABLE III                               
__________________________________________________________________________
                    Properties After                                      
                                    Inherent Viscosity                    
Additives           Extrusion       After Aging 72 hr.                    
Isocyanate                                                                
      μ eq/g.                                                          
           Phosphite                                                      
                % by                                                      
                    Inherent                                              
                         --COOH     in 150° C.                     
(1)   Polymer                                                             
           (2)  Weight                                                    
                    Viscosity                                             
                         μ eq/g.                                       
                              Color Steam                                 
__________________________________________________________________________
None  --   None --  .60  62   Lt. Amber                                   
                                    .15                                   
TDI   75   DSPDP                                                          
                0.2 .83   2   Brown .44                                   
TDI   35                                                                  
           &#34;    0.2 .67  --   Amber .40                                   
mTI   35                                                                  
ODI   75   &#34;    0.2 .60  --   Lt. Amber                                   
                                    .20                                   
mTI   90   TNPP 0.3 .56  --   Dk. Brown                                   
                                    .35                                   
__________________________________________________________________________
 (1) TDI = tolylene2,4-diisocyanate                                       
 mTI = mtolyl isocyanate                                                  
 ODI = octadecyl isocyanate.                                              
 (2) DSPDP = di(stearyl) pentaerythritol                                  
 TNPP = tris(nonylphenyl) phosphite.                                      
 
    
     EXAMPLE 4 
     A polyarylene ester is prepared from 1,2-bis(4-acetoxyphenyl)ethane and isophthalic acid in a manner similar to that described in Example 1. Formulations of this polymer (BPE-I) commercially available polyethylene terephthalate (PET), and polytetramethylene terephthalate (PBT) are prepared by mixing them with an isocyanate and a phosphite ester. The admixtures are extruded and tested by the procedures of Example 1. The results are given in Table IV. It can be seen that the isocyanate-phosphite ester stabilizer is effective in improving the hydrolytic stability of the all aromatic polyarylene ester but not effective with the polyalkylene esters, polyethylene and polytetramethylene terephthalates. 
     
                       TABLE IV                                                    
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                Properties After                                          
                             Inherent                                     
Additives       Extrusion    Viscosity After                              
       mTI                           Aging 72 hr. in                      
Polymer                                                                   
       μeq/g.                                                          
               DSPDP    ηinh                                          
                             Color   150° C. Steam                 
______________________________________                                    
BPE-I  0       0        .91  Lt. Amber                                    
                                     .27                                  
&#34;      50      0.3      .87  &#34;       .43                                  
PET    0       0        .52  White   .19                                  
&#34;      50      0.3      .56  Amber   .19                                  
PBT    0       0        .87  White   .36                                  
&#34;      50      0.3      .65  Amber   .33                                  
______________________________________                                    
 BPE-I  polyisophthalate of 1,2bis(4-hydroxyphenyl)ethane.                
 PET  polyethylene terephthalate.                                         
 PBT  polybutylene terephthalate.                                         
 mTI  mtolyl isocyanate.                                                  
 DSPDP  di(stearyl)pentaerythritol diphosphite.