System and method of co2 thermal swing adsorption with wet regeneration and hot drying
US-2024058740-A1 · Feb 22, 2024 · US
US2020002633A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020002633-A1 |
| Application number | US-201916392314-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 23, 2019 |
| Priority date | Jun 27, 2018 |
| Publication date | Jan 2, 2020 |
| Grant date | — |
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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).
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.
Temperature swing adsorption · CPC title
Pressure swing adsorption · CPC title
Co-current · CPC title
Recycled product or process gas · CPC title
Carbon dioxide · CPC title
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