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Hydrogen separation continued dehydrogenation

Skeletal catalysts are usually employed in slurry-phase reactors or fixed-bed reactors. Hydrogenation of cottonseed oil, oxidative dehydrogenation of alcohols, and several other reactions are performed in sluny phase, where the catalysts are charged into the liquid and optionally stirred (often by action of the gases involved) to achieve intimate mixing. Fixed-bed designs suit methanol synthesis from syngas and catalysis of the water gas shift reaction, and are usually preferred because they obviate the need to separate product from catalyst and are simple in terms of a continuous process. [Pg.153]


See other pages where Hydrogen separation continued dehydrogenation is mentioned: [Pg.134]    [Pg.524]    [Pg.85]    [Pg.257]    [Pg.61]    [Pg.79]    [Pg.443]    [Pg.589]    [Pg.172]    [Pg.589]    [Pg.45]    [Pg.5]    [Pg.5]    [Pg.1029]    [Pg.300]    [Pg.502]    [Pg.124]    [Pg.125]    [Pg.78]    [Pg.212]    [Pg.45]    [Pg.121]    [Pg.456]    [Pg.18]    [Pg.255]    [Pg.253]   


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