Sulfiding and reoxidation of chromium catalyst

Claim 2

A process for activating a catalyst consisting essentially of a chromium component and a silica-containing base comprising a first step wherein said catalyst is contacted with a sulfur-containing ambient at a temperature of at least 370° C. and a subsequent second step wherein it is contacted with an oxygen-containing oxidizing ambient at a temperature within the range of 400°-900° C.

Claim 3

A method according to claim 1 wherein said catalyst is heated in the presence of oxygen prior to said contact with said sulfur-containing ambient.

Claim 4

A method according to claim 2 wherein after said heating in the presence of oxygen, a nitrogen ambient is introduced to flush out the air prior to said introduction of said sulfur-containing ambient.

Claim 5

A method according to claim 3 wherein said nitrogen flush is carried out for less than 30 minutes.

Claim 6

A method according to claim 2 wherein said contact with said sulfur-containing ambient is at a temperature within the range of 600°-900° C. and said reoxidation is carried out at a temperature within the range of 450°-700° C., which reoxidation temperature is also at least 50° C. lower than said temperature for contact with said sulfur-containing ambient.

Claim 7

A method according to claim 5 wherein said contact with said sulfur-containing ambient is for a time within the range of 10 minutes to 3 hours and said reoxidation step is carried out for a time within the range of 1 to 4 hours.

Claim 8

A method according to claim 1 wherein said catalyst is heated in air to a temperature within the range of 250°-1000° C. over a time period of at least 5 minutes prior to said contact with said sulfur-containing ambient.

Claim 9

A method according to claim 1 wherein said sulfur-containing ambient comprises a sulfur-containing material and an oxygen-containing compound.

Claim 10

A method according to claim 8 wherein said oxygen-containing compound is selected from acetic acid, methanol or water vapor and said sulfur-containing material is selected from dimethyl sulfide, methylmercaptan, diethyl sulfide, and carbon disulfide.

Claim 11

A method according to claim 1 wherein said sulfur-containing ambient comprises carbon disulfide

Claim 12

A method according to claim 1 wherein said sulfur-containing ambient comprises carbonyl sulfide.

Claim 13

A method according to claim 1 wherein said silica-containing base is a cogel formed by adding a titanium compound to a mineral acid, introducing a alkali metal silicate into the acid containing said titanium compound to form a hydrogel, aging the hydrogel for a time of greater than one hour, washing the thus aged hydrogel to produce a substantially alkali metal free hydrogel, forming a mixture comprising the thus washed hydrogel and a normally liquid oxygen-containing water soluble organic compound, and separating said organic compound and water from said mixture to form a xerogel, and wherein said chromium is imparted by impregnation of said hydrogel with an aqueous chromium acetate solution.

Claim 14

A method according to claim 1 wherein said resulting reoxidized catalyst contains less than 0.4 weight percent sulfur.

Claim 15

A method according to claim 1 wherein said contacting with said sulfur-containing ambient and said subsequent contact with an oxygen-containing ambient is carried out in a continuous activator.

Claim 16

A process according to claim 1 wherein said silica-containing base is a silica-titania cogel containing about 2 weight percent titania based on the weight of said cogel, said chromium-containing compound being present in an amount sufficient to give about 0.5 to 1 weight percent chromium based on the weight of said base, said sulfur-containing ambient is carbonyl sulfide and wherein said contacting with said carbonyl sulfide is carried out at a temperature within the range of 600°-900° C. for a time within the range of 10 minutes to 3 hours and wherein said oxidizing ambient is air and said contact with said air is carried out at a temperature within the range of 450°-700° C. for a time within the range of 1 to 4 hours and wherein said chromium-containing catalyst is heated in air at a temperature within the range of 700°-925° C. prior to said contact with said carbonyl sulfide.

Claim 17

A catalyst produced by the method of claim 15.

Claim 18

A catalyst produced by the method of claim 1.