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Rates for Poisoned Porous Catalysts

For one catalyst = 16. It is suspected that intrapellet diffusion strongly retards both dehydrogenations. Estimate the potential improvement in selectivity if diffusion resistance could be eliminated. Make the estimate for a concentration ratio (Cg/C ) = 1.0. Neglect differences in between ethane and ethylene. [Pg.457]

Solution Equation (11-93) is applicable for the diffusion-limited situation. The pellet selectivity for ethylene formation with respect to ethane disappearance is [Pg.457]

If diffusion resistance is eliminated, Eq. (11-92) gives the point as well as the pellet selectivity [Pg.457]

These selectivities give the ratio of rates of formation of ethylene and total disappearance of ethane (ethylene plus acetylene). If we start with pure CjHs, a mass balance requires that the rate of formation of acetylene with respect to disappearance of ethane be 1 — Sp. Hence eliminating diffusion resistance reduces the rate of formation of undesirable C2H2 from 0.45 to 0.06. [Pg.457]

The discussion has been limited to selectivities existing at one position or conversion (set of concentrations) in a reactor. Wheeler has extended the development to show cumulative selectivities that would exist at any level of conversion in the reactor efSuent. [Pg.457]


See other pages where Rates for Poisoned Porous Catalysts is mentioned: [Pg.457]    [Pg.457]    [Pg.459]    [Pg.461]   


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