Extruder systems and processes for production of petroleum coke

US11920099B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11920099-B2
Application numberUS-202117534165-A
CountryUS
Kind codeB2
Filing dateNov 23, 2021
Priority dateNov 23, 2021
Publication dateMar 5, 2024
Grant dateMar 5, 2024

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Systems and methods for production for consistently sized and shaped petroleum coke from vacuum residue, one method including supplying processed vacuum residue to an extruder; heating the processed vacuum residue throughout a horizontal profile of the extruder from an inlet to an outlet of the extruder; venting hydrocarbon off-gases from the extruder along the horizontal profile of the extruder from the inlet to the outlet of the extruder; and cutting consistently sized and shaped petroleum coke at the outlet of the extruder.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method of production for consistently sized and shaped petroleum coke from vacuum residue, the method comprising the steps of: fractionating vacuum residue in a coker fractionator, where the vacuum residue is produced in a vacuum distillation column at a temperature between about 430° C. to about 450° C. and a pressure of about 0.1 kPa, where fractionating the vacuum residue removes liquid propane gas, fuel gas, coker naphtha, light coker gas oil, and heavy coker gas oil to produce a processed vacuum reside, where the coker fractionator operates at a pressure between 1 psig to 50 psig and a temperature in a fractionator flash zone between 650° F. and 950° F.; supplying the processed vacuum residue to an extruder; heating the processed vacuum residue throughout a horizontal profile of the extruder from an inlet to an outlet of the extruder, wherein a temperature along the horizontal profile is between about 350° C. and about 450° C. and a pressure along the horizontal profile is 0.1 kPa and is consistent; venting hydrocarbon off-gases from the extruder along the horizontal profile of the extruder from the inlet to the outlet of the extruder; and recycling the hydrocarbon off-gases to the coker fractionator; and cutting consistently sized and shaped petroleum coke at the outlet of the extruder comprises the use of an automatically timed blade to cut the consistently sized and shaped petroleum coke. 2. The method according to claim 1 , wherein the method is carried out without the application of steam, hydrogen, or water. 3. The method according to claim 1 , where the step of venting is carried out in multiple stages along the horizontal profile of the extruder from the inlet to the outlet of the extruder. 4. The method according to claim 1 , wherein the speed of the automatically timed blade is adjusted based on rotational speed of an extrusion screw in the extruder and residence time of the processed vacuum residue in the extruder. 5. The method according to claim 1 , wherein the extruder includes an extrusion screw in an annulus, the extrusion screw selected from the group consisting of: a cylindrically-shaped extrusion screw and a conically-shaped extrusion screw. 6. The method according to claim 1 , wherein the step of heating the processed vacuum residue throughout a horizontal profile of the extruder from an inlet to an outlet of the extruder comprises a series of variable temperature heaters external to the extruder disposed along the horizontal profile of the extruder. 7. The method according to claim 1 , wherein the consistently sized and shaped petroleum coke is substantially circular in the cross section with a consistent depth and in the form of a puck shape. 8. The method according to claim 1 , wherein the steps of heating and venting require no vacuum or vacuum distillation and wherein coking reactions take place along the entire horizontal profile from the inlet to the outlet of the extruder. 9. The method according to claim 1 , wherein the method does not require the application of chemical additives during processing. 10. The method of claim 1 , wherein coking reactions occur along the entire horizontal profile of the extruder from the inlet to the outlet of the extruder.

Assignees

Inventors

Classifications

  • C10L5/08Primary

    without the aid of extraneous binders · CPC title

  • Cutting, disintegrating, shredding or grinding · CPC title

  • Molding or moulds · CPC title

  • C10B7/10Primary

    with conveyor-screws · CPC title

  • with conveyor-screws · CPC title

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What does patent US11920099B2 cover?
Systems and methods for production for consistently sized and shaped petroleum coke from vacuum residue, one method including supplying processed vacuum residue to an extruder; heating the processed vacuum residue throughout a horizontal profile of the extruder from an inlet to an outlet of the extruder; venting hydrocarbon off-gases from the extruder along the horizontal profile of the extrude…
Who is the assignee on this patent?
Saudi Arabian Oil Co
What technology area does this patent fall under?
Primary CPC classification C10L5/08. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 05 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 2 related publications on this page (citations in our corpus or others sharing the same primary CPC).