US2022143547A1PendingUtilityA1
Removal of mercury in a gas dehydration process using thermally stable chemical additives
Est. expiryNov 12, 2040(~14.3 yrs left)· nominal 20-yr term from priority
Inventors:Joshua Allen Thompson
B01D 2252/2023C10L 2290/06B01D 2257/602B01D 2252/2056B01D 2253/10B01D 53/96B01D 2251/304B01D 53/1493B01D 53/263B01D 53/64C10L 2230/02C10L 2290/141C10L 2290/547C10L 2290/541C10L 2290/48C10L 3/106B01D 53/1425B01D 2252/2026C10L 2290/542C10L 3/101B01D 2259/40083B01D 2256/245C10L 2290/46B01D 53/77C10L 2290/12C10L 2290/545
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Claims
Abstract
The present invention is directed to the removal of mercury in a gas dehydration process using thermally table chemical additives.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A process for removal of mercury in a gas dehydration system comprising (a) adding a complexing agent to a recirculated glycol solvent as part of the glycol solution feed to the dehydration liquid contactor and recirculating continuously with the glycol solvent, (b) selectively reacting the complexing agent with mercury in the wet natural gas to remove the mercury from the dry natural gas product, (c) and feeding the rich glycol with the complexing agent to a regenerator and continuously regenerating.
2 . The process of claim 1 , wherein the overhead of the regenerator containing water and mercury vapor is contacted with an adsorbent that captures mercury.
3 . The process of claim 2 , wherein the adsorbent is selected from the group consisting of activated carbon, alumina, silica, zeolite or supported metal.
4 . A process for removal of mercury in a gas dehydration system comprising (a) adding a complexing agent continuously prior to a liquid contactor, wherein inside the liquid contactor, the complexing agent dissolved in the lean glycol solvent selectively reacts with the mercury in the natural gas, producing a rich glycol solvent containing mercury, (b) and the rich glycol solvent is then sent to an adsorber where mercury and the complexing agent are removed using an adsorbent.
5 . The process of claim 4 wherein the adsorbent is selected from the group consisting of activated carbon, ion-exchange resin, alumina, silica, zeolite or supported metal.
6 . The process of claim 5 wherein the rich glycol with reduced complexing agent and no mercury is fed to a regenerator to remove water in the overhead and regenerate the glycol solvent.
7 . The process of claim 4 wherein A filter aid is then added after the liquid contactor, but prior to the expansion valve.
8 . The process of claim 7 wherein the filter aid is a mechanical filter, carbon filter, ultrafiltration filter or nanofiltration filter.Join the waitlist — get patent alerts
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