Preparation of homopolymers and copolymers of ethene by Phillips catalysis

Claim 1

In a process for the production of a supported catalyst (1) for Phillips catalysis, consisting of a carrier which is laden with chromium in oxide form, phorphorus in oxide form and aluminum in oxide form, by (1.1) in a first stage, preparing a catalyst intermediate (1.1) laden with the desired amounts of chromium, phosphorus and aluminum from (1.1.a) a finely divided, porous silicate carrier, (1.1.b) a selected, specific chromium compound, (1.1.c) a selected, specific phosphorus compound and (1.1.d) a selected, specific aluminum compound, and then (1.2) in a second stage, keeping the catalyst intermediate (1.1) obtained from the first stage in an anhydrous gas stream containing oxygen in a concentration of more than 10% by volume for from 10 to 1000 minutes at from 300° to 900° C. and thus converting it into the actual supported catalyst (1), the improvement which comprises; (1.1) in the first stage, preparing a catalyst intermediate by a method in which first, (1.1.1) in a first substage, a suspension is prepared from (1.1.1.1) a finely divided, porous silicate carrier which has a particle diameter of from 1 to 400 μm, a pore volume of from 0.5 to 3 cm 3 /g and a surface area of from 100 to 1000 m 2 /g, and (1.1.1.2) an inert organic solvent, with thorough mixing, and with the proviso that from 150 to 5000 parts by weight of the solvent (1.1.1.2) are employed per 100 parts by weight of the carrier (1.1.1.1), thereafter (1.1.2) in a second substage, (1.1.2.1.) in a solvent of the type defined under (1.1.1.2) (1.1.2.2) a chromium compound of the formula ##STR2## where R is alkyl of not more than 12 carbon atoms and R 1 is alkyl of not more than 12 carbon atoms, or hydrogen, is combined with (1.1.2.3) an aluminum compound of the formula AlR 3 2 , where R 2 is alkyl of not more than 12 carbon atoms, with thorough mixing, at from 0° to 100° C., with the proviso that there are from 0.5 to 10 parts by weight of aluminum from the aluminum compound (1.1.2.3) and from 5 to 500 parts by weight of solvent (1.1.2.1) per part by weight of chromium from the chromium compound (1.1.2.2), and the entire mixture is kept at the stated temperature for form 5 to 300 minutes, thereafter (1.1.3) in a third substage, (1.1.3.1) the suspension resulting from substage (1.1.1) is combined with (1.1.3.2) a phosphorus compound of the formula P(O)(OR 3 ) 3 or P(O)H(OR 3 ) 2 , where R 3 is alkyl, aryl or cycloalkyl of not more than 12 carbon atoms, or hydrogen, with the proviso that one or more radicals R are not hydrogen, and (1.1.3.3) the product obtained from substage (1.1.2), with thorough mixing at from 0° to 60° C., with the proviso that from 0.1 to 5 parts by weight of chromium from the chromium compound (1.1.2.2) and from 0.5 to 10 parts by weight of phosphorus from the phosphorus compound (1.1.3.2) are employed per 100 parts by weight of the carrier (1.1.1.1), and the entire mixture is kept at the stated temperature for from 5 to 300 minutes, and finally (1.1.4) in a fourth substage, the suspension obtained in substage (1.1.3) is evaporated to dryness at no higher than 150° C., under atmospheric or reduced pressure, and thereafter (1.2) in the second stage, the catalyst intermediate obtained from the first stage (1.1) is converted to the actual supported catalyst by a method in which first, (1.2.1) in a first substage, the catalyst intermediate obtained from the first stage (1.1) is kept in a stream of anhydrous nitrogen, at from 150° to 300° C. for from 60 to 500 minutes, thereafter (1.2.2) in a second substage, the intermediate obtained from substage (1.2.1) is kept in an anhydrous gas stream containing oxygen in a concentration of more than 10% by volume for from 10 to 1000 minutes at from 300° to 900° C., and finally (1.2.3) in a third substage, the intermediate obtained from substage (1.2.2) is kept in a stream of anhydrous nitrogen for from 10 to 300 minutes at from 50° to 400° C.