Selective recovery of c2+ hydrocarbons from natural gas for steam cracker feed in an integrated refinery and steam cracker complex using pressure swing adsorption
US-2015376525-A1 · Dec 31, 2015 · US
US11034903B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11034903-B2 |
| Application number | US-201916392314-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 23, 2019 |
| Priority date | Jun 27, 2018 |
| Publication date | Jun 15, 2021 |
| Grant date | Jun 15, 2021 |
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A process of treating a natural gas stream is provided comprising sending natural gas stream through a first adsorbent bed to remove water and heavy hydrocarbons (C8+) to produce a partially treated gas stream in which the first adsorbent bed is regenerated by a temperature swing adsorption process and then sending the partially treated gas stream through a second adsorption bed to remove carbon dioxide and lighter hydrocarbons (C7−) to produce a purified natural gas stream wherein said second adsorption bed is regenerated by a temperature pressure swing adsorption process.
Opening claim text (preview).
The invention claimed is: 1. A process of treating a natural gas stream comprising sending said natural gas stream through a first adsorbent bed to remove water and heavy hydrocarbons (C8+) to produce a partially treated gas stream wherein said first adsorbent bed is regenerated by a temperature swing adsorption process; and sending said partially treated gas stream through a second adsorption bed to remove carbon dioxide and lighter hydrocarbons (C7−) to produce a purified natural gas stream wherein said second adsorption bed is regenerated by a temperature pressure swing adsorption process. 2. The process of claim 1 wherein said natural gas stream comprises less than about 3 vol % carbon dioxide. 3. The process of claim 1 wherein a closed loop or semi-closed loop regeneration gas stream is used to regenerate said second adsorbent bed. 4. The process of claim 3 wherein a semi-closed loop regeneration gas stream is used to regenerate said second adsorbent bed. 5. The process of claim 1 wherein said temperature pressure swing adsorption process comprises a series of steps in order comprising adsorption, co-current depressurization, closed-loop heating, a purge with heating, a purge without heating, repressurization of the adsorbent bed and cooling with feed and then withdrawal of product. 6. The process of claim 1 wherein said temperature pressure swing adsorption process comprises a series of steps in order comprising adsorption, co-current depressurization, a first closed loop heating step and a second closed loop heating step, a depressurization step, a purge without heat, repressurization and cooling with feed and withdrawal of product. 7. The process of claim 5 wherein a portion of said product is used in said purge without heating step. 8. The process of claim 6 wherein a portion of said product stream is heated and sent through said adsorbent bed. 9. The process of claim 8 wherein a stream exiting said adsorbent bed is sent into said adsorbent bed or into a second adsorbent bed. 10. The process of claim 5 wherein said heating step is at a higher pressure than said purge step.
using four beds · CPC title
More than ten · CPC title
Recycled product or process gas · CPC title
Hydrocarbons · CPC title
Regeneration of a solvent, catalyst, adsorbent or any other component used to treat or prepare a fuel · CPC title
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