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Fischer-Tropsch transport effects

CO reactants and the H2O product of the synthesis step inhibit many of these secondary reactions. As a result, their rates are often higher near the reactor inlet, near the exit of high conversion reactors, and within transport-limited pellets. On the other hand, larger olefins that are selectively retained within transport-limited pellets preferentially react in secondary steps, whether these merely reverse chain termination or lead to products not usually formed in the FT synthesis. In later sections, we discuss the effects of olefin hydrogenation, oligomerization, and acid-type cracking on the carbon number distribution and on the functionality of Fischer-Tropsch synthesis products. We also show the dramatic effects of CO depletion and of low water concentrations on the rate and selectivity of secondary reactions during FT synthesis. [Pg.234]

E. Transport Effects and the Control of Selectivity in Fc-based Fischer-Tropsch Synthesis... [Pg.291]


See other pages where Fischer-Tropsch transport effects is mentioned: [Pg.84]    [Pg.27]    [Pg.38]    [Pg.395]    [Pg.228]    [Pg.275]    [Pg.277]    [Pg.5]    [Pg.101]    [Pg.218]    [Pg.247]    [Pg.2027]    [Pg.3]    [Pg.989]    [Pg.529]    [Pg.1026]   
See also in sourсe #XX -- [ Pg.228 , Pg.229 ]




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