Jingguang G. Chen - Hockessin DE Leo D. Brown - Baton Rouge LA Gary B. McVicker - Califon NJ Edward S. Ellis - Fairfax VA Michele S. Touvelle - Baton Rouge LA Darryl P. Klein - Ellicott City MD David E. W. Vaughan - Flemington NJ
Assignee:
ExxonMobil Research and Engineering Company - Annandale NJ
International Classification:
C10G 4500
US Classification:
208213, 208217, 585826, 502 34, 502 38, 502 53
Abstract:
A process to regenerate metal oxide desulfurization sorbents using an oxidizing and reducing atmosphere. The sorbents may be mono- or multi-metallic in nature, and preferably comprise Cu, Ni and/or Co. If desired, secondary metals may be incorporated to increase regeneration efficiency and/or capacity. Other additives may be used to suppress hydrocarbon cracking. A sorbent containing Zn may be combined with an Fe, Co, Ni, Mo, or W catalyst or a noble metal catalyst and combinations thereof.
Regeneration Of Iron-Based Hydrogen Sulfide Sorbents
Jingguang G. Chen - Hockessin DE Leo D. Brown - Baton Rouge LA Gary B. McVicker - Califon NJ Edward S. Ellis - Fairfax VA Michele S. Touvelle - Baton Rouge LA Darryl P. Klein - Ellicott City MD David E. W. Vaughan - Flemington NJ
Assignee:
ExxonMobil Research Engineering Company - Annandale NJ
A process to regenerate iron-based hydrogen sulfide sorbents using steam. The steam is preferably mixed with hydrogen-containing gas and/or an inert gas, such as nitrogen. In a preferred embodiment, the sorbent is first exposed to the steam and then exposed to a hydrogen-containing gas at regeneration conditions.
Use Of Hydrogen To Regenerate Metal Oxide Hydrogen Sulfide Sorbents
Jingguang Chen - Hockessin DE, US Leo Brown - Baton Rouge LA, US William Baird - Baton Rouge LA, US Gary McVicker - Califon NJ, US Edward Ellis - Fairfax VA, US Michele Touvelle - Centreville VA, US Darryl Klein - Ellicott City MD, US David Vaughan - State College PA, US
A process to regenerate a spent hydrogen sulfide sorbent comprised of a sorbent metal selected from Fe, Ni, Co, and Cu on a refractory oxide support using hydrogen gas. The sorbent metal component may be mono- or multi-metallic in nature, and preferably comprise Ni and/or Co. If desired, secondary metals may be incorporated to increase regeneration efficiency and/or capacity. Other additives suppress hydrocarbon cracking.