Coke drum additive injection

US9969937B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9969937-B2
Application numberUS-201314030219-A
CountryUS
Kind codeB2
Filing dateSep 18, 2013
Priority dateSep 21, 2012
Publication dateMay 15, 2018
Grant dateMay 15, 2018

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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.

A process for producing coke that may include: heating a coker feedstock to a coking temperature to produce a heated coker feedstock; feeding the heated coker feedstock to a coking drum; feeding a coking additive, such as at least one hydroconversion or hydrocracking catalyst, to the coking drum; and subjecting the heated coker feedstock to thermal cracking in the coking drum to crack a portion of the coker feedstock to produce a cracked vapor product and produce a coke product.

First claim

Opening claim text (preview).

What is claimed: 1. A process for producing coke, the process comprising: heating a coker feedstock to a coking temperature to produce a heated coker feedstock; mixing the heated coker feedstock and a coking additive comprising at least one hydroconversion or hydrocracking catalyst via a mixing tee to produce a mixture, wherein the mixing tee comprises at least two intersecting flow conduits and an injection nozzle extending into a perpendicular intersection of the at least two intersecting flow conduits, wherein the mixing comprises passing the heated coker feedstock annularly over the injection nozzle and injecting the coking additive via the injection nozzle into the heated coker feedstock; feeding the mixture to a bottom head of a coking drum; subjecting the heated coker feedstock to thermal cracking in the coking drum to crack a portion of the coker feedstock to produce a cracked vapor product and produce a coke product. 2. The process of claim 1 , wherein the coke product has a VCM concentration in the range from about 5% to about 50% by weight, as measured by ASTM D3175t. 3. The process of claim 1 , wherein the coke product comprises at least one of sponge coke, needle coke, and shot coke. 4. The process of claim 1 , wherein mixing the heated coker feedstock comprises feeding the heated coker feedstock to the mixing tee for a selected time period prior to feeding the coking additive to the mixing tee. 5. The process of claim 1 , further comprising admixing the coking additive with a carrier medium. 6. The process of claim 5 , wherein the carrier medium comprises a hydrocarbon or a mixture of hydrocarbons. 7. The process of claim 6 , wherein the carrier medium comprises a mixture including one or more hydrocarbons having a boiling point in the range from about 500° F. to about 950° F. 8. A process for producing coke, the process comprising: heating a coker feedstock to a coking temperature to produce a heated coker feedstock; mixing the heated coker feedstock and a coking additive comprising at least one hydroconversion or hydrocracking catalyst via a mixing tee to produce a mixture, wherein the mixing tee comprises at least two intersecting flow conduits and an injection nozzle extending into a perpendicular intersection of the at least two intersecting flow conduits, and wherein the mixing comprises passing the heated coker feedstock annularly over the injection nozzle and injecting the coking additive via the injection nozzle into the heated coker feedstock; feeding the mixture to a bottom head of a coking drum; and subjecting the heated coker feedstock to cracking in the coking drum to crack a portion of the coker feedstock to produce a cracked vapor product and produce a coke product. 9. The process of claim 8 , wherein the coking additive is a solid. 10. The process of claim 8 , wherein the coking additive is a slurry. 11. The process of claim 8 , wherein the mixing tee is immediately upstream of the coking drum proximate the bottom head of the coking drum.

Assignees

Inventors

Classifications

  • C10G11/00Primary

    Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils (cracking in direct contact with molten metals or salts C10G9/34) · CPC title

  • Coking (in order to produce liquid products mainly) · CPC title

  • containing additives · CPC title

  • Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material (cracking oils C10G) · CPC title

  • Charging devices · CPC title

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What does patent US9969937B2 cover?
A process for producing coke that may include: heating a coker feedstock to a coking temperature to produce a heated coker feedstock; feeding the heated coker feedstock to a coking drum; feeding a coking additive, such as at least one hydroconversion or hydrocracking catalyst, to the coking drum; and subjecting the heated coker feedstock to thermal cracking in the coking drum to crack a portion…
Who is the assignee on this patent?
Lummus Technology Inc
What technology area does this patent fall under?
Primary CPC classification C10G11/00. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 15 2018 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).