Processes and apparatuses for separating chlorides from n-butane

US12378171B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12378171-B2
Application numberUS-202318512747-A
CountryUS
Kind codeB2
Filing dateNov 17, 2023
Priority dateNov 18, 2022
Publication dateAug 5, 2025
Grant dateAug 5, 2025

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

Processes and apparatuses for separating chlorides from a butane product stream by removing chlorides from a portion of said feed stream in a rectification section of the separation zone. The rectification section may be in a rectification column which may be combined with a stripper column. Alternatively, a wall may be used to provide the rectification section in a fractionation column. The processes and apparatuses can be used in both new designs and revamped designs.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for separating chlorides from a butane product stream, the process comprising: separating, in a separation zone, a feed stream comprising light hydrocarbons, propane, isobutane, n-butane, chlorides, and C5+ hydrocarbons into a stream comprising light hydrocarbons, propane, isobutane, and n-butane and a liquid stream comprising an alkylate effluent with C5+ hydrocarbons; and, removing chlorides from a liquid or vapor portion of said feed stream in a rectification section of the separation zone, the rectification section providing a butane product stream. 2. The process of claim 1 , wherein the separation zone comprises a fractionation column, and wherein the rectification section comprises a rectification column. 3. The process of claim 2 , wherein a bottoms stream from the rectification column is passed back to the fractionation column. 4. The process of claim 3 , wherein a side draw stream from the rectification column comprises the butane product stream. 5. The process of claim 3 , wherein an overhead stream from the rectification column is condensed to provide the butane product stream. 6. The process of claim 1 , wherein the separation zone comprises a fractionation column, and further comprises a stripping section. 7. The process of claim 6 , wherein the stripping section and the rectification section are in the fractionation column. 8. The process of claim 6 , wherein the separation zone comprises a second column and both the stripping section and the rectification section are in the second column. 9. The process of claim 6 , wherein the separation zone further comprises a first column comprising the rectification section and a second column comprising the stripping section. 10. The process of claim 9 , wherein a bottoms stream from the second column is passed to the first column. 11. The process of claim 9 , wherein the first column and the second column produce a common overhead stream. 12. The process of claim 9 , wherein the first column and the second column are disposed on top of each other. 13. The process of claim 6 , wherein the separation zone comprises a second column and wherein the second column comprises the stripping section and the fractionation column comprises the rectification section. 14. A process for separating chlorides from a butane product stream, the process comprising: separating, in a separation zone comprising a deisobutanizer column, a feed stream comprising light hydrocarbons, propane, isobutane, n-butane, chlorides, and C5+ hydrocarbons into a stream comprising light hydrocarbons, propane, isobutane, and n-butane and a liquid stream comprising an alkylate effluent with C5+ hydrocarbons; and, passing a side draw stream from the deisobutanizer column to a rectification column, the side draw stream comprising liquid or vapor; passing a bottoms stream from the rectification column to the deisobutanizer column, the bottoms stream comprising organic chlorides; passing a vapor or liquid stream from the rectification column to the deisobutanizer column or another lower pressure vessel, the vapor or liquid stream comprising HCl, iso-butane, and n-butane; recovering a butane product stream from the deisobutanizer column; and, passing the butane product stream to an adsorbent zone having an adsorbent configured to remove chlorides and provide a chloride lean butane product stream. 15. The process of claim 14 , wherein the butane product stream from the deisobutanizer column is a side draw stream. 16. The process of claim 14 , further comprising: cooling an overhead stream from the rectification column to provide the vapor or liquid stream and the butane product stream. 17. A process for separating chlorides from an n-butane stream, the process comprising: separating, in a separation zone comprising a separation column a feed stream comprising light hydrocarbons, propane, isobutane, n-butane, chlorides, and C5+ hydrocarbons into a stream comprising light hydrocarbons, propane, isobutane, and n-butane, and a liquid stream comprising an alkylate effluent with C5+ hydrocarbons; and, removing organic chlorides from the feed stream in a rectification section; and, removing HCl from the feed stream in a stripper section. 18. The process of claim 17 , wherein the separation zone comprises a first column comprising the rectification section and a second column comprising the stripper section. 19. The process of claim 17 , wherein the rectification section is disposed within the separation column. 20. The process of claim 17 , wherein the separation zone comprises a second column and both the stripper section and the rectification section are in the second column.

Assignees

Inventors

Classifications

  • by two or more of a fractionation, separation or rectification step · CPC title

  • Chlorine · CPC title

  • B01D53/02Primary

    by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title

  • Hydrocarbons · CPC title

  • by adsorption, i.e. purification or separation of hydrocarbons with the aid of solids, e.g. with ion-exchangers · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US12378171B2 cover?
Processes and apparatuses for separating chlorides from a butane product stream by removing chlorides from a portion of said feed stream in a rectification section of the separation zone. The rectification section may be in a rectification column which may be combined with a stripper column. Alternatively, a wall may be used to provide the rectification section in a fractionation column. The pr…
Who is the assignee on this patent?
Uop Llc
What technology area does this patent fall under?
Primary CPC classification B01D53/02. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Aug 05 2025 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 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).