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Shell based hydrogen plant

Several processes have been developed based on the oxidation approach, but, with some exceptions, such as the Linde Clintox process (Heisel and Marold, 1992) these have not been commercial successes because of the complexity of SO2 recovery processes and their comparatively low SO2 removal efficiencies. Hydrogen sulfide, on the other hand, can be removed at very high efficiency by a number of processes, including the selective amine processes discussed in Chapter 2. Processes that involve the conversion of Claus plant tail gas sulfur compounds to H2S and the removal of this H2S are discussed in the following sections. Processes reviewed include Parson s Beavon Sulfur Removal (BSR) process. Shell s SCOT process, FB and D Technologies Sulften process, the TPA Resulf process, and the Exxon Flexsorb SE Plus process. [Pg.717]


See other pages where Shell based hydrogen plant is mentioned: [Pg.182]    [Pg.356]    [Pg.214]    [Pg.137]    [Pg.222]    [Pg.214]    [Pg.152]    [Pg.318]    [Pg.53]    [Pg.64]    [Pg.558]    [Pg.211]    [Pg.979]    [Pg.649]    [Pg.114]    [Pg.110]    [Pg.210]    [Pg.181]    [Pg.113]   


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