Hydrodesulfurization process with upstaged reactor zones

Claim 1

A process for the hydrodesulfurization of a metal- and sulfur-containing asphaltenic feed oil comprising (a) passing said oil and hydrogen downwardly through at least three fixed bed catalytic hydrodesulfurization zones connected in series so the reaction effluent from each of said zones is passed downwardly through the next zone in said series; (b) the hydrodesulfurization reaction in said zones being conducted at a temperature of 600° to 900° F., a hydrogen pressure of 500 to 5,000 psi, and with a catalyst in each of said zones comprising supported Group VI-B and Group VIII metals; (c) said feed oil being charged directly to one of said series zones, the zone receiving said feed oil constituting the upstream zone in the series, the reaction effluent from said upstream zone being passed downwardly through the first succeeding downstream zone and the reaction effluent from said first succeeding downstream zone being passed downwardly through the second succeeding downstream zone; (d) removing the upstream zone from service upon catalyst deactivation therein and charging said feed oil directly to said first succeeding downstream zone, (e) removing deactivated catalyst from and charging fresh catalyst to said removed upstream zone, (f) subsequently removing said first succeeding catalyst zone from service upon catalyst deactivation therein, returning said upstream zone containing fresh catalyst to said series as the final zone receiving said reaction effluent in said series, and charging said feed oil directly to said second succeeding downstream zone, (g) removing deactivated catalyst from and charging fresh catalyst to said removed first succeeding zone so that said first succeeding catalyst zone is being subsequently returned to said series as the final zone receiving said reaction effluent in said series, and (h) continuing said sequence so that each downstream zone becomes in succession an upstream zone and upon catalyst deactivation is removed from said series for catalyst replacement and subsequent return to said series as the final zone receiving said reaction effluent in the series.