Desulfurization and novel sorbents for same
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[0095] The following examples are intended to be illustrative of the present invention and to teach one of ordinary skill in the art to make and use the invention. These examples are not intended to limit the invention in any way.
example i
[0096] A solid reduced cobalt metal sorbent was produced by dry mixing 20.02 pounds of diatomite silica and 25.03 zinc oxide in a mix Muller for 15 minutres to produce a first mixture. While still mixing, a solution containing 6.38 pounds of Disperal alumina (Condea), 22.5 pounds of deionized water and 316 grams of glacial acetic acid were added to the mix Muller to produce a second mixture. After adding these components, mixing continued for an additional 30 minutes. This second mixture was then dried at 300° F. for 16 hours and then calcined at 1175° F. for one hour to form a third mixture. This third mixture was then particularized by granulation using a Stokes Pennwalt granulator fitted with a 50 mesh screen. 200 grams of the resulting granulated mix was then impregnated with 148 grams of cobalt nitrate hexahydrate dissolved in 43 grams of hot (200° F.) deionized water to produce a particulate impregnated mix. The impregnated particulate was dried at 300° F. for one hour and the...
example ii
[0098] The solid reduced cobalt sorbent as prepared in Example I was tested for its desulfurization ability as follows.
[0099] A one inch quartz reactor tube was loaded with the indicated amounts of the sorbent of Example I. This solid reduced cobalt sorbent was placed on a frit in the middle of the reactor. Gaseous cracked-gasoline having about 345 parts per million sulfur by weight of the sulfur-containing compounds based on the weight of the gaseous cracked-gasoline and having about 95 weight percent thiophenic compounds (such as for example, alkyl benzothiphenes, alkyl thiophenes, benzothiophene and thiophene) based on the weight of sulfur-containing compounds in the gaseous cracked-gasoline was pumped upwardly through the reactor. The rate was 13.4 milliliters per hour. This produced sulfurized solid sorbent and desulfurized gaseous cracked-gasoline.
[0100] In Run 1, hydrogen was added to the gasoline feed at a partial pressure of 6.6 psi (out of a total pressure of 15 psi) res...
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