Polymerization catalyst systems and processes using alkyl lithium compounds as a cocatalyst

Abstract

A catalyst system composition comprising a chromium compound supported on a silica-titania support, wherein said catalyst system has been reduced with carbon monoxide, and a cocatalyst selected from the group consisting of i) alkyl lithium compounds, ii) dialkyl aluminum alkoxides in combination with at least one metal alkyl selected from the group consisting of alkyl zinc compounds, alkyl aluminum compounds, alkyl boron compounds, and mixtures thereof and iii) mixtures thereof can be used to polymerize olefins to produce a low density polymer with a decreased melt index and/or high load melt index. This catalyst system also can be used with a Ziegler-Natta catalyst system to polymerize olefins. Polymerization processes using these catalyst system compositions are also provided. Polymers resulting from polymerization processes using the inventive catalyst and cocatalyst systems have a decreased high load melt index, decreased melt index, increased fluff bulk density, and are useful as components to make bi-modal molecular weight resins for film and/or blow molding applications.

1 - 29 . (canceled)  
     
     
         30 . A polymerization process comprising contacting at least one mono-1-olefin under polymerization reaction conditions with a catalyst composition to produce a polymer, the catalyst composition comprising: 
 1) the product resulting from the combination of: 
 a) a chromium catalyst having a pore volume of at least 1.8 cc/g and a surface area of at least 400 m 2 /g produced by contacting a chromium-containing, titanium-containing, silica-containing solid with carbon monoxide under conditions such that a substantial portion of the chromium is in the divalent state after contacting with carbon monoxide; and  
 b) a cocatalyst, wherein the cocatalyst is an alkyl lithium or aryl lithium compound; and  
   2) a Ziegler-Natta catalyst composition produced by combining a halide of titanium, vanadium, or zirconium and an organoaluminum compound.    
     
     
         31 . A polymerization process according to  claim 30  wherein the cocatalyst comprises an alkyl lithium compound.  
     
     
         32 . A polymerization process according to  claim 31  wherein the alkyl lithium compound has 1 to 12 carbon atoms.  
     
     
         33 . A polymerization process according to  claim 31  wherein said alkyl lithium compound has 1 to 5 carbon atoms.  
     
     
         34 . A polymerization process according to  claim 33  wherein said alkyl lithium compound comprises n-butyl lithium.  
     
     
         35 . A polymerization process according to  claim 34  wherein the alkyl lithium compound is used in an amount so as to give an atom ratio of lithium to chromium in the range of about 0.5:1 to 10:1.  
     
     
         36 . A polymerization process according to  claim 34  wherein the chromium catalyst contains about 0.5 to about 5 weight percent chromium and about 0.1 to 7 weight percent titanium.  
     
     
         37 . A polymerization process according to  claim 30  wherein said lithium compound is used in an amount so as to give an atom ratio of lithium to chromium within a range of about 0.5:1 to about 10:1.  
     
     
         38 . A polymerization process according to  claim 30  wherein the chromium catalyst is prepared by calcining a chromium-containing, titanium-containing, silica-containing solid with oxygen at a temperature in the range of about 400 to about 900 degrees C. to convert a substantial portion of the chromium to the hexavalent state and then contacting the calcined product with carbon monoxide at a temperature in the range of about 300 to about 500 degrees C. to convert a substantial portion of the chromium to the divalent state.  
     
     
         39 . A polymerization process according to  claim 30 , wherein the mono-1-olefin has from about 2 to about 8 carbon atoms per molecule.  
     
     
         40 . A polymerization process according to  claim 39 , wherein the mono-1-olefin is ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, or any mixture thereof.  
     
     
         41 . A polymerization process according to  claim 40 , wherein the mono-1-olefin is ethylene.  
     
     
         42 . A polymerization process according to  claim 30 , wherein a copolymer is produced by polymerizing ethylene and about 0.5 to about 20 mole percent of one or more comonomers selected from mono-1-olefins having from about 3 to about 8 carbon atoms per molecule.  
     
     
         43 . A polymerization process according to  claim 42 , wherein said comonomer is propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 4-methyl-1-pentene, or any mixture thereof.  
     
     
         44 . A polymerization process according to  claim 30 , wherein the polymerization is carried out at a temperature within a range of about 66 to about 110° C.  
     
     
         45 . A polymerization process according to  claim 30 , wherein the polymerization reaction conditions comprise slurry polymerization conditions.  
     
     
         46 . A polymerization process according to  claim 45 , wherein the contacting is conducted in a loop reactor zone.  
     
     
         47 . A polymerization process according to  claim 46 , wherein the contacting is conducted in the presence of a diluent that comprises, in major part, isobutane.  
     
     
         48 . A polymer produced by the process of  claim 30 .  
     
     
         49 . A polymer produced by the process of  claim 42 .  
     
     
         50 . A polymerization process comprising contacting at least one mono-1-olefin under polymerization reaction conditions with a catalyst composition to produce a polymer, the catalyst composition comprising: 
 1) the product resulting from the combination of: 
 a) a chromium catalyst having a pore volume of at least 1.8 cc/g and a surface area of at least 400 m 2 /g; and  
 b) a cocatalyst, wherein the cocatalyst is an alkyl lithium or aryl lithium compound; and  
   2) a Ziegler-Natta catalyst composition produced by combining a halide of titanium, vanadium, or zirconium and an organoaluminum compound;    wherein the chromium catalyst consists essentially of a chromium-containing, titanium-containing, silica-containing solid that has been contacted with carbon monoxide under conditions such that a substantial portion of the chromium is in the divalent state after contacting with carbon monoxide.    
     
     
         51 . A polyethylene composition having a density within a range of about 0.925 to about 0.960 g/cc and a high load melt index within a range of about 1 to about 20 g/10 minutes.  
     
     
         52 . A polyethylene composition according to  claim 51 , wherein the composition has a density within a range of about 0.945 to about 0.954 g/cc and a high load melt index within a range of about 5 to about 15 g/10 minutes.  
     
     
         53 . A bimodal polymer having a density within a range of about 0.925 to about 0.960 g/cc and a high load melt index within a range of about 1 to about 20 g/10 minutes.  
     
     
         54 . A bimodal polymer according to  claim 53 , wherein the composition has a density within a range of about 0.945 to about 0.954 g/cc and a high load melt index within a range of about 5 to about 15 g/10 minutes.