Method for reducing the amount of high molecular weight organic sulfur picked-up by hydrocarbon streams transported through a pipeline
AssigneeExxonMobil Research and Engineering Company
InventorsJoseph L. Feimer, Bal K. Kaul, Lawrence J. Lawlor, Jeenok T. Kim, G. Bryce McGarvey
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Abstract
A process for removing relatively low levels of high molecular weight organic sulfur from hydrocarbon streams, particularly from streams that have picked-up such sulfur while being transported through a pipeline. The hydrocarbon stream containing the organic sulfur is passed through a bed of adsorbent material comprised of a high Ni content, high surface area material that also contains an effective amount of SiO2 or GeO2 and an alkaline earth metal.
Claims11
A process for removing high molecular weight organic sulfur species having a molecular weight of 200 and higher, from hydrocarbon streams by passing said hydrocarbon stream through a bed of adsorbent material, which adsorbent material has a Ni content from about 50 wt. % to about 90 wt. %, from about 5 to 20 wt. % of a Group IVA oxide selected from SiO2 and GeO2, from about 1 to 10 wt % of an alkaline-earth metal oxide, and contains substantially no aluminum compounds, wherein all weight percents are based on the total weight of the adsorbent, and which adsorbent has a BET surface area of about 200 m2/g to about 400 m2/g and a nickel surface area greater than 20 m2/g based on dynamic H2 chemisorption,
- wherein passing said hydrocarbon stream through a bed of adsorbent material is performed in multiple temperature steps starting at a first temperature of about 100° C. to about 150° C. and increasing at an effective rate until a final temperature of about 200° C. to 400° C. is reached, the temperature is held at each step for an effective amount of time. and the temperature is held at the first temperature for about 4 to 10 days.
A process for removing high molecular weight organic sulfur compounds having a molecular weight of 200 and higher, from hydrocarbon streams by contacting said hydrocarbon stream with an adsorbent material, which adsorbent material has a Ni content from about 50 wt. % to about 90 wt. % and a surface area of about 200 m2/g to about 400 m2/g, and contains substantially no aluminum compounds, wherein the contacting with the adsorbent material is performed in multiple temperature steps starting at about a first temperature about 100° C. and increasing at an effective rate until a final temperature of about 200° C. to 400° C. is reached, the temperature is held at each step for an effective amount of time, and the temperature is held at the first temperature for about 4 to 10 days.
Dependencies are inferred from the claim text.