Desulfurization system with novel sorbent transfer mechanism

Abstract

A hydrocarbon desulfurization system employing regenerable solid sorbent particulates in a fluidized bed desulfurization reactor. The sulfur-loaded sorbent particulates are continuously withdrawn from the reactor and transferred to a regenerator. A novel solids transport mechanism provides for the safe and effective transfer of the sulfur-loaded sorbent particulates from the high pressure hydrocarbon environment of the reactor to the low pressure oxygen environment of the regenerator.

Description

RELATED APPLICATIONS [0001] This application is a continuation of U.S. patent application Ser. No. 10 / 120,700, filed Apr. 11, 2002, which is hereby incorporated by reference herein.BACKGROUND OF THE INVENTION [0002] This invention relates to a method and apparatus for removing sulfur from hydrocarbon-containing fluid streams. In another aspect, the invention concerns an improved system for transferring solid sorbent particulates between vessels in a hydrocarbon desulfurization unit. [0003] Hydrocarbon-containing fluids such as gasoline and diesel fuels typically contain a quantity of sulfur. High levels of sulfurs in such automotive fuels is undesirable because oxides of sulfur present in automotive exhaust may irreversibly poison noble metal catalysts employed in automobile catalytic converters. Emissions from such poisoned catalytic converters may contain high levels of non-combusted hydrocarbons, oxides of nitrogen, and / or carbon monoxide, which, when catalyzed by sunlight, form ...

AI Technical Summary

Benefits of technology

[0009] Accordingly, it is an object of the present invention to provide a novel hydrocarbon desulfurization system which employs a fluidized bed reactor and provides for continuous regeneration of the solid sorbent particulates.

Problems solved by technology

High levels of sulfurs in such automotive fuels is undesirable because oxides of sulfur present in automotive exhaust may irreversibly poison noble metal catalysts employed in automobile catalytic converters.

However, most conventional sulfur removal processes, such as hydrodesulfurization, tend to saturate olefins and aromatics in the cracked-gasoline and thereby reduce its octane number (both research and motor octane number).

In removing sulfur from diesel fuel by hydrodesulfurization, the cetane is improved but there is a large cost in hydrogen consumption.

The different pressures and atmospheres in the reactor and regenerator present a variety of challenges when continuously withdrawing and regenerating sulfur-loaded sorbent particulates from the reactor.

For example, the pressure differential between the reactor and regenerator can make it difficult to maintain the proper pressures in the reactor and regenerator while continuously transferring sulfur-loaded solid particulates from the reactor to the regenerator.

Such isolation of the hydrocarbon environment in the reactor from the oxygen environment in the regenerator can be difficult to maintain during continuous transfer of sulfur-loaded sorbent particulates from the reactor to the regenerator.

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