Catalyst and method

Claim 2

A catalyst prepared by (1) forming a mixture of a finely divided porous support comprising silica, alumina, zirconia, thoria, or magnesia or mixtures thereof and an alkyl magnesium compound; (2) heating said mixture for a time and at a temperature sufficient to react said support and said alkyl magnesium compound; (3) reacting, by heating, the product of (2) with a hydrocarbylhydrocarbyloxysilane; (4) reacting, by heating, the product of (3) with a titanium compound that contains a halide; or (5) reacting the product of (2) with the reaction product of a hydrocarbylhydrocarbyloxysilane and a titanium compound that contains halide; and (6) activating the catalyst product of (4) or (5) with a cocatalyst comprising hydrogen or an alkyl lithium, alkyl magnesium, alkyl aluminum, alkyl aluminum halide or alkyl zinc.

Claim 3

The catalyst of claim 1 wherein said alkyl magnesium compound is essentially free of aluminum alkyls.

Claim 4

The catalyst of claim 1 wherein the silane of (3) has the formula (RO) n Si(R) 4-n where the R groups may be the same or different, and are C 1 to C 20 alkyl, cycloalkyl, aryl, alkaryl, or aralkyl radicals, and n is a whole integer from 1 to 4.

Claim 5

The catalyst of claim 1 wherein said compound of (4) comprises the halide or oxyhalide of titanium.

Claim 6

The catalyst of claim 4 wherein said compound of (4) comprises titanium tetrachloride.

Claim 7

The catalyst of claim 1 wherein the reactants of steps (1)-(5) and their molar ratios are according to the following formula ##EQU3## in which M represents the transition metal molar concentration, M' represents the metal molar concentration of the metal reacted with the porous support and is fixed by the surface hydroxyl concentration of the porous support, Si represents the molar concentration of the hydrocarbyloxyhydrocarbylsilane compound, n is an integer corresponding to the number of hydrocarbyloxy groups attached to the silane compound and K is a number between about 0.5 to about 5.

Claim 8

The catalyst of claim 1 in which the cocatalyst is hydrogen, alkyl lithium, alkyl magnesium, alkyl aluminum, alkyl zinc or alkyl aluminum chloride in which each alkyl group has 1 to 12 carbon atoms.

Claim 9

The process of preparing an active polymerization catalyst comprising the steps of (1) forming a mixture of a finely divided porous support comprising silica, alumina, zirconia, thoria, or magnesia or mixtures thereof and an alkyl magnesium compound; (2) heating said mixture for a time and at a temperature sufficient to react said support and said alkyl metallic compound; (3) reacting, by heating, the product of (2) with a hydrocarbylhydrocarbyloxysilane; (4) reacting, by heating, the product of (3) with a titanium compound that contains halide or (5) reacting the product of (2) with the reaction product of a hydrocarbylhydrocarbyloxysilane and a titanium compound that contains chlorine; and (6) activating the catalyst product of (4) or (5) with a cocatalyst comprising hydrogen or an alkyl lithium,, alkyl magnesium, alkyl aluminum, alkyl aluminum halide or alkyl zinc.

Claim 10

The process of preparing an active polymerization catalyst comprising the steps of (1) forming a mixture of a finely divided porous support comprising silica, alumina, zirconia, thoria, or magnesia or mixtures thereof and an alkyl magnesium compound; (2) heating said mixture for a time and at a temperature sufficient to react said support and said alkyl metallic compound; (3) reacting, by heating, the product of (2) with a hydrocarbylhydrocarbyloxysilane; (4) reacting, by heating, the product of (3) with a titanium compound that contains halide or (5) reacting the product of (2) with the reaction product of a hydrocarbylhydrocarbyloxysilane and a titanium compound that contains chlorine; and (6) activating the catalyst product of (4) or (5) with a cocatalyst comprising hydrogen or an alkyl lithium,, alkyl magnesium, alkyl aluminum, alkyl aluminum halide or alkyl zinc.

Claim 11

The process of claim 8 wherein said alkyl magnesium compound is essentially free of aluminum alkyls.

Claim 12

The process of claim 8 wherein the silane of (3) has the formula (RO) n Si(R) 4-n where the R groups may be the same or different, and are C 1 to C 20 alkyl, cycloalkyl, aryl, alkaryl, or aralkyl radicals, and n is a whole integer from 1 to 4.

Claim 13

The process of claim 8 wherein said compound of (4) comprises the halide or oxyhalide of titanium.

Claim 14

The process of claim 11 wherein said compound of (4) comprises titanium tetrachloride.

Claim 15

The process of claim 8 wherein the reactants of steps (1)-(5) and their molar ratios are according to the following formula ##EQU4## in which M represents the transition metal molar concentration, M' represents the metal molar concentration of the metal reacted with the porous support and its concentration is fixed such that all the surface hydroxyls of the porous support are essentially reacted, Si represents the molar concentration of the hydrocarbyloxyhydrocarbylsilane compound, n is an integer corresponding to the number of hydrocarbyloxy groups attached to the silane compound and K is a number between about 0.5 and about 5.

Claim 16

The process of claim 8 in which the cocatalyst is hydrogen, alkyl lithium, alkyl magnesium, alkyl aluminum, alkyl zinc or alkyl aluminum halide in which each alkyl group has 1 to 12 carbon atoms.