초록 ▼

A process and reactor system is disclosed for hydrotreating a low sulfur containing olefinic distillate and conventional feedstock to a catalytic hydrodesulfurization. The process comprises passing a minor portion of the olefinic distillate to a first hydrotreating zone in admixture with conventiona

A process and reactor system is disclosed for hydrotreating a low sulfur containing olefinic distillate and conventional feedstock to a catalytic hydrodesulfurization. The process comprises passing a minor portion of the olefinic distillate to a first hydrotreating zone in admixture with conventional CHD feedstock. A major portion of the olefinic distillate is passed to a second hydrotreating zone in combination with the effluent from the first zone. In this manner the exotherm attributable to olefins hydrogenation is controlled within limits sufficient to avoid very frequent catalyst regeneration.

대표청구항 ▼

A process for hydrogenation of low sulfur containing olefins-rich hydrocarbon feedstock, comprising: (a) reacting a hydrocarbon mixture comprising a minor portion of said olefins-rich hydrocarbon feedstock and sulfur-containing liquid hydrocarbon in a first catalytic hydrodesulfurization zone in con

A process for hydrogenation of low sulfur containing olefins-rich hydrocarbon feedstock, comprising: (a) reacting a hydrocarbon mixture comprising a minor portion of said olefins-rich hydrocarbon feedstock and sulfur-containing liquid hydrocarbon in a first catalytic hydrodesulfurization zone in contact with catalyst particles at a temperature between 260°and 400°C. and pressure between 2800 kPa and 7000 kPa, said minor portion being in an amount sufficient to maintain said first zone hydrogenation exotherm under hydrodesulfurization and olefins hydrogenation conditions whereby catalyst deactivation is reduced; (b) passing step (a) reaction effluent stream to a second catalytic hydrodesulfurization one containing catalyst particles under hydrodesulfurization and olefins hydrogenation conditions at a temperature between 260°and 400°C. and pressure between 2800 kPa and 7000 kPa in admixture with a major portion of said olefins-rich hydrocarbon feedstock at low temperature; (c) recovering hydrogenated desulfurized liquid hydrocarbons.