Temperature swing adsorption process and apparatus with closed loop regeneration
US-10399007-B2 · Sep 3, 2019 · US
US10821394B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10821394-B2 |
| Application number | US-201816013747-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 20, 2018 |
| Priority date | Jun 20, 2018 |
| Publication date | Nov 3, 2020 |
| Grant date | Nov 3, 2020 |
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A process is provided to treat a natural gas stream by removing heavier hydrocarbons comprising C5, C6 and heavier hydrocarbons. The process involves sending a natural gas stream through an adsorbent bed to remove heavier hydrocarbons and producing a product stream comprising C1 to C4 hydrocarbons. A portion of the product stream is sent through a regeneration heater to produce a heated regeneration gas stream which is sent through the adsorbent bed to desorb the heavier hydrocarbons. Then the regeneration gas stream is cooled and sent to a separation unit such as a distillation column to divide the regeneration gas stream into a liquid stream comprising heavier hydrocarbons and a recovered regeneration gas stream.
Opening claim text (preview).
The invention claimed is: 1. A process to treat a natural gas stream by removing heavier hydrocarbons comprising C5, C6 and heavier hydrocarbons, said process comprising: sending said natural gas stream through an adsorbent bed to remove said heavier hydrocarbons and producing a product stream comprising C1 to C4 hydrocarbons; sending a portion of said product stream through a regeneration heater to produce a heated regeneration gas stream; sending said heated regeneration gas stream through said adsorbent bed to desorb said heavier hydrocarbons; and cooling said regeneration gas stream and sending a cooled regeneration gas stream to a separation unit to divide said regeneration gas stream into a liquid stream comprising heavier hydrocarbons and a recovered regeneration gas stream, wherein said separation unit comprises a reflux absorber or a distillation column. 2. The process of claim 1 wherein said recovered regeneration gas stream is combined with said product stream. 3. The process of claim 1 wherein said natural gas stream passes through a filter coalescer before entering said adsorbent bed. 4. The process of claim 1 wherein said recovered regeneration gas stream is sent through a chiller or condenser. 5. The process of claim 4 wherein said chiller or condenser produces a liquid stream to be returned to said separation unit. 6. The process of claim 1 wherein said liquid stream comprising heavier hydrocarbons is sent to a reboiler of the distillation column to produce a liquid heavy hydrocarbon stream and a lighter gas stream. 7. The process of claim 6 wherein said lighter gas stream is returned to said distillation column. 8. A process for treating a natural gas stream comprising sending said natural gas stream through an adsorbent bed containing an adsorbent to remove C5, C6 and heavier hydrocarbons and producing a product gas stream comprising C1 to C4 hydrocarbons; regenerating said adsorbent bed by sending a regeneration gas stream through said adsorbent bed to produce a contaminated gas stream; cooling said contaminated gas stream; and sending a cooled contaminated gas stream to a reflux absorber or to a distillation column without chilling said cooled contaminated gas stream by a refrigeration means. 9. The process of claim 8 wherein a recovered regeneration gas stream exits said reflux absorber or said distillation column. 10. The process of claim 9 wherein said recovered regeneration gas stream is sent through a chiller or condenser to recycle a liquid stream. 11. The process of claim 9 wherein said recovered regeneration gas stream is combined with said product gas stream.
Recycling of a stream within the process or apparatus to reuse elsewhere therein · CPC title
Heat exchange, direct or indirect · CPC title
Adsorption of impurities during preparation or upgrading of a fuel · CPC title
Hydrocarbons · CPC title
using a single bed · CPC title
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