Heavy oil conversion process with in-situ potassium sulfide generation
AssigneeExxonMobil Research and Engineering Company
InventorsDaniel P. Leta, Jonathan M. McConnachie, William C. Baird, Jr., Walter D. Vann, Jorge L. Soto
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Abstract
The present invention relates to a process for regeneration of alkali metal salt reagent used in desulfurization of heavy oil feedstreams. In particular, the present invention relates to a process utilizing potassium hydroxide as an external supply reagent to a heavy oil conversion process and in-situ conversion of the spent reactants utilized in such process into a potassium sulfide reagent for reintroduction into the heavy oil conversion process.
Claims21
A process for desulfurizing a heavy oil feedstream with a potassium sulfide reagent and regenerating the potassium sulfide reagent from spent potassium salt reaction products, comprising:
- a) mixing at least a portion of a heavy oil feedstream having an API gravity of about 19 or less with a desulfurization reagent solution comprising potassium sulfide to form a mixed oil/reagent feedstream;
- b) exposing at least a portion of the mixed oil/reagent feedstream to effective desulfurization conditions in a conversion reactor to form a desulfurized reactor outlet stream, thereby removing at least a portion of the sulfur from the heavy oil feedstream components of the mixed oil/reagent stream and converting at least a portion of the potassium sulfide in the mixed reagent stream to spent potassium salts comprising potassium hydrosulfide;
- c) adding a wash water to the desulfurized reactor outlet stream to form a desulfurized oil/water mixture;
- d) separating the desulfurized oil/water mixture into a separate oil phase and a separate water phase in at least one wash water vessel, wherein the water phase contains the majority of the spent potassium salts;
- e) extracting at least a portion of the separate oil phase from the wash water vessel as a desulfurized heavy oil product, and extracting at least a portion of the separate water phase from the wash water vessel as an aqueous spent potassium reagent stream;
- f) splitting the aqueous spent potassium reagent stream into a non-regenerative potassium hydrosulfide stream and a regenerative potassium hydrosulfide stream;
- g) sending the regenerative potassium hydrosulfide stream to a KOH conversion process, converting the majority of the potassium hydrosulfide to potassium hydroxide in the KOH conversion process, and producing an aqueous regenerated KOH stream from the KOH conversion process;
- h) combining at least a portion of the aqueous regenerated KOH stream with at least a portion of the non-regenerative potassium hydrosulfide stream to produce a partially regenerated potassium reagent stream containing potassium hydroxide and potassium hydrosulfide;
- i) sending the partially regenerated potassium reagent stream to a flash regeneration system wherein the partially regenerated potassium reagent stream is subject to a dehydration temperature of at least about 250° C. (482° F.), thereby converting at least a portion of the potassium hydroxide and potassium hydrosulfide in the partially regenerated potassium reagent stream to potassium sulfide;
- j) extracting a regenerated potassium sulfide reagent stream from the flash regeneration system;
- k) utilizing at least a portion of the regenerated potassium sulfide reagent stream in the desulfurization reagent solution of step a).
Dependencies are inferred from the claim text.