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Naphtha reforming catalyst, coke formation over

Coke Formation over Naphtha-Reforming Catalyst 241... [Pg.241]

On the other hand, there is the question of the close relationship between coke formation (catalyst stability) and aromatics cyclization (catalyst selectivity) over the acid sites present in the zeolites. On naphtha reforming, coke formation is a bifunctional reaction requiring the dehydrogenation capacity of the metallic function and the condensation capacity of the acidic function. Therefore, it is interesting to... [Pg.465]

The pyrolysis of hydrocarbons follows the thermal cracking mechanism (4). Apart from the pressure, the conditions in the tubular steam reformer and in the preheater are not far from that of a steam cracker in an ethylene plant. With low catalyst activity, the pyrolysis route may take over. This is the situation in case of severe sulphur poisoning or in attempts to use non-metal catalysts so far showing very low activity (1). Non metal catalysts have mainly been based on alkaline oxides being active for gasification of coke precursors. However, it has been difficult to avoid the formation of olefins and other pyrolysis products (1,2,5). In fact, it was demonstrated (2,4) that co-production of syngas and light olefins was possible from heavy gas oil and naphtha over a potassium promoted zirconia catalyst. [Pg.82]


See other pages where Naphtha reforming catalyst, coke formation over is mentioned: [Pg.247]    [Pg.251]    [Pg.247]    [Pg.251]    [Pg.495]    [Pg.518]    [Pg.297]    [Pg.97]    [Pg.160]    [Pg.160]   
See also in sourсe #XX -- [ Pg.239 , Pg.240 , Pg.241 , Pg.242 , Pg.243 , Pg.244 , Pg.245 , Pg.246 , Pg.247 , Pg.248 , Pg.249 , Pg.250 , Pg.251 ]




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Catalyst, reformer

Catalysts catalyst coking

Catalysts coke

Coke formation

Coke formation catalysts

Coked catalyst

Coked reforming catalyst

Naphtha

Reforming catalyst

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