Processes for removing contaminants from a dehydrogenation effluent
US-9517447-B1 · Dec 13, 2016 · US
US9962682B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9962682-B2 |
| Application number | US-201615346619-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 8, 2016 |
| Priority date | Jun 1, 2015 |
| Publication date | May 8, 2018 |
| Grant date | May 8, 2018 |
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A process for the providing a regenerant gas stream for a regenerable adsorbent used to remove water and hydrogen sulfide from a reactor effluent in a catalytic dehydrogenation process is described. The reactor effluent is compressed in a compressor to provide a compressed effluent. The compressed effluent may be treated to remove chlorides, and then passed to a dryer zone having a regenerable adsorbent. A regenerant gas stream is used to desorb the water and hydrogen sulfide and the spent regenerant stream may be passed to a cleaning zone having a sorbent configured to remove hydrogen sulfide from the spent regenerant stream. The cleaned regenerant gas stream may be recycled to the dryer zone to desorb and/or regenerate the regenerable adsorbent.
Opening claim text (preview).
The invention claimed is: 1. A process for cleaning a spent regenerant stream, the process comprising: removing water and hydrogen sulfide from a reactor effluent stream in a first zone; regenerating a regenerable adsorbent in the first zone with a regenerant gas stream to provide a spent regenerant stream, the spent regenerant stream including water and hydrogen sulfide from the first zone; removing the hydrogen sulfide from the spent regenerant stream in a second zone comprising a regenerant cleaning zone to provide a cleaned regenerant stream, the regenerant cleaning zone including one or more vessels having a solid adsorbent including a metal oxide configured to selectively immobilize hydrogen sulfide; and, regenerating a regenerable adsorbent with at least a portion of the cleaned regenerant stream. 2. The process of claim 1 wherein regenerable adsorbent that is regenerating with the at least a portion of the cleaned regenerant stream is in the first zone. 3. The process of claim 1 further comprising: cooling the cleaned regenerant stream before regenerating the regenerable adsorbent with the cleaned regenerant stream. 4. The process of claim 1 further comprising: removing water from the cleaned regenerant stream before regenerating the regenerable adsorbent with the cleaned regenerant stream. 5. The process of claim 1 further comprising: passing the cleaned regenerant stream to a hydrocarbon removal zone before regenerating the regenerable adsorbent with the cleaned regenerant stream. 6. The process of claim 1 further comprising: cooling the spent regenerant stream. 7. The process of claim 6 wherein the spent regenerant stream is cooled in the regenerant cleaning zone. 8. A process for cleaning a spent regenerant stream, the process comprising: removing water and hydrogen sulfide from a reactor effluent stream in a first zone, the reactor effluent stream including olefins; regenerating a regenerable adsorbent in the first zone with a regenerant gas stream to provide a spent regenerant stream, the spent regenerant stream including water and hydrogen sulfide from the first zone; removing the hydrogen sulfide from the spent regenerant stream in a second zone comprising a regenerant cleaning zone to provide a cleaned regenerant stream, the regenerant cleaning zone including one or more vessels having a solid adsorbent including a metal oxide configured to selectively immobilize hydrogen sulfide, the second zone different than the first zone; and, regenerating a regenerable adsorbent in the first zone with at least a portion of the cleaned regenerant stream. 9. The process of claim 8 further comprising: cooling the cleaned regenerant stream before regenerating the regenerable adsorbent. 10. The process of claim 8 further comprising: removing water from the cleaned regenerant stream before regenerating the regenerable adsorbent with the cleaned regenerant stream. 11. The process of claim 8 further comprising: passing the cleaned regenerant stream to a hydrocarbon removal zone before regenerating the regenerable adsorbent with the cleaned regenerant stream. 12. The process of claim 8 further comprising: cooling the spent regenerant stream. 13. The process of claim 12 wherein the spent regenerant stream is cooled in the regenerant cleaning zone.
using two beds · CPC title
Hydrogen sulfide · CPC title
of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425 · CPC title
with stationary reactants · CPC title
by using a purge gas (B01D2259/4009 takes precedence) · CPC title
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