Process for the preparation of high density ethylene polymers in fluid bed reactor
AssigneeUnion Carbide Corporation
InventorsBurkhard E. Wagner, George L. Goeke, Frederick J. Karol
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AssigneeUnion Carbide Corporation
InventorsBurkhard E. Wagner, George L. Goeke, Frederick J. Karol
Estimating the term…
A catalytic process for preparing ethylene polymers having a density of .gtoreq.0.94 to .ltoreq.0.97 and a melt flow ratio of about .gtoreq.22 to .ltoreq.32 in a low pressure gas phase process at a productivity of .gtoreq.50,000 pounds of polymer per pound of Ti with a catalyst formed from selected organoaluminum compounds and a precursor composition of the formula Mg.sub.m Ti.sub.1 (OR).sub.n X.sub.p (ED).sub.q wherein ED is a selected electron donor compound m is .gtoreq.0.5 to .ltoreq.56 n is 0, 1 or 2 p is .gtoreq.2 to .ltoreq.116 q is >1.5 m+2 R is a C.sub.1 to C.sub.14 aliphatic or aromatic hydrocarbon radical, or COR' wherein R' is a C.sub.1 to C.sub.14 aliphatic or aromatic hydrocarbon radical, and X is selected from the group consisting of Cl, Br, I or mixtures thereof, which catalyst is in particulate form and impregnated in a porous inert carrier material.
A continuous catalytic process for producing ethylene homopolymers or copolymers containing .gtoreq.97 mol percent of ethylene and .ltoreq.3 mol percent of one or more C.sub.3 to C.sub.8 alpha olefins with a Ti containing catalyst at a productivity of .gtoreq.50,000 pounds of polymer per pound of Ti under a pressure of <1000 psi in a gas phase fluid bed reaction
Dependencies are inferred from the claim text.