Segmented reactor for homogeneous regeneration of spent ionic liquid
US-10005057-B1 · Jun 26, 2018 · US
US12378171B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12378171-B2 |
| Application number | US-202318512747-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 17, 2023 |
| Priority date | Nov 18, 2022 |
| Publication date | Aug 5, 2025 |
| Grant date | Aug 5, 2025 |
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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.
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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.
by two or more of a fractionation, separation or rectification step · CPC title
Chlorine · CPC title
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
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