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Laminar-flow reactor size determination

Another synthesis process proposed to receive benefits from operating with monolith catalysts is the conversion of methanol for gasoline production [16,17J. The catalyst used was the ZSM-5 zeolite. However, rather than binding the catalyst onto the wall by use of a washcoat, it was uniformly crystallized on the cordierite honeycomb (62 cells/cm ) wall surfaces (up to 30% by weight), similar to the method described in the patent assigned to Lachman and Patil [18]. The effects of methanol partial pressure on conversion and temperature on hydrocarbon selectivity were determined. Three regimes of mass transfer resistances are experienced in this reaction reactant transfer to the reactor walls within the monolith channels through the laminar flow, diffusion resistance at the surface between zeolite crystals on the walls, and diffusion into the zeolite molecular-size pores to the active sites within the crystals, where the reaction rate limit is anticipated. [Pg.200]


See other pages where Laminar-flow reactor size determination is mentioned: [Pg.608]    [Pg.574]    [Pg.39]    [Pg.334]    [Pg.286]    [Pg.574]    [Pg.112]    [Pg.569]    [Pg.358]    [Pg.574]    [Pg.37]    [Pg.648]    [Pg.1346]    [Pg.560]   
See also in sourсe #XX -- [ Pg.397 ]




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