Rate/kinetic selective multiple bed adsorption process cycle
US-11883775-B2 · Jan 30, 2024 · US
US9505683B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9505683-B2 |
| Application number | US-201414283859-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 21, 2014 |
| Priority date | May 31, 2013 |
| Publication date | Nov 29, 2016 |
| Grant date | Nov 29, 2016 |
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A process for treatment of a natural gas stream, or other methane containing stream that passes through a guard bed for removal of mercury and hydrolysis of COS, followed by treatment with an absorbent unit containing an amine solvent for removal of carbon dioxide and hydrogen sulfide. The gas is then dried by a molecular sieve bed. The regeneration gas for the molecular sieve adsorbent bed is chilled to remove liquid hydrocarbons and sulfur compounds. The process is accomplished without the use of an absorbent unit to remove the sulfur compounds.
Opening claim text (preview).
The invention claimed is: 1. A process for treating a natural gas stream comprising: a) sending said natural gas stream to an adsorbent guard bed to remove mercury to produce a first stream; b) sending the first stream to a solvent absorbent bed unit to remove carbon dioxide and hydrogen sulfide to produce a second stream; c) sending the second stream to a second adsorbent bed to remove water and organic sulfur compounds to produce a third stream; d) wherein after said second stream has passed to said second adsorbent bed, regenerating the second adsorbent bed with a heated gas stream comprising said third stream to remove water and sulfur from the second adsorbent bed, then cooling and drying said second adsorbent bed to further remove water and organic sulfur compounds. 2. The process of claim 1 wherein said organic sulfur compounds comprise carbonyl sulfide and within said natural gas stream said carbonyl sulfide is hydrolyzed in said adsorbent guard bed to hydrogen sulfide. 3. The process of claim 1 wherein said adsorbent guard bed comprises a metal oxide adsorbent. 4. The process of claim 2 wherein a majority of said carbonyl sulfide within said natural gas stream is hydrolyzed in said adsorbent guard bed to hydrogen sulfide and a portion of said carbonyl sulfide is removed in said second adsorbent bed. 5. The process of claim 1 wherein said heated gas exits said second adsorbent bed and then said heated gas is cooled to remove water and to produce a cooled gas stream. 6. The process of claim 5 wherein liquid hydrocarbons that were in said natural gas stream are removed from said cooled gas stream. 7. The process of claim 6 wherein organic sulfur compounds and hydrogen sulfide are removed from said cooled gas stream.
Working-up natural gas or synthetic natural gas · CPC title
Water · CPC title
of water · CPC title
Absorption of impurities during preparation or upgrading of a fuel · CPC title
Cross-Sectional Technologies · mapped topic
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