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Catalytic boiling-point distribution

Figure 1. Boiling point distribution of products from catalytic cracking... Figure 1. Boiling point distribution of products from catalytic cracking...
Catalytic aromatisation of aliphatic hydrocarbons was first described by researchers at Mobil.2s In this process, termed M-2 forming , alkanes from ethane to high boiling point naphthalenes can be aromatised. The most effective catalyst for aromatisation was found to be the medium pore HZSM-5.26 Large pore zeolite and amorphous silica-alumina with broad pore size distributions gave only low yields of aromatics due to rapid coke formation. [Pg.24]


See other pages where Catalytic boiling-point distribution is mentioned: [Pg.268]    [Pg.214]    [Pg.372]    [Pg.323]    [Pg.124]    [Pg.214]    [Pg.73]    [Pg.269]    [Pg.189]    [Pg.214]    [Pg.905]    [Pg.591]    [Pg.299]    [Pg.501]   


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Boiling point distribution

Distribution points

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