Catalytic conversion process for aromatic feedstocks with hydrog

Catalyst – solid sorbent – or support therefor: product or process – Regenerating or rehabilitating catalyst or sorbent – Gas or vapor treating

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585466, 585467, 585471, 585475, 585481, B01J 2938, C07C 266, C07C 522

Patent

active

045088365

ABSTRACT:
In the process of converting an aromatic feedstock to an alkyl-substituted mono-nuclear aromatic product by contacting the feedstock with a coke-selectivated ZSM-5 type catalyst at elevated temperature under conversion process coking conditions to produce said alkyl-1-substituted mononuclear aromatic product selectively, the improvement which comprises:
regenerating the process coked catalyst in contact with a non-oxidizing atmosphere comprising an effective amount of hydrogen at a temperature of about 800.degree. F. to 1200.degree. F. to restore activity of the catalyst while retaining selectivity. Advantageously, the conversion involves alkylation, disproportionation and/or isomerization to produce at least one lower alkyl or dialkyl benzene product.

REFERENCES:
patent: 3412013 (1968-11-01), Bowles
patent: 4001346 (1977-01-01), Chu
patent: 4086287 (1978-04-01), Kaeding et al.
patent: 4088706 (1978-05-01), Kaeding
patent: 4117026 (1978-09-01), Haag et al.
patent: 4128592 (1978-12-01), Kaeding
patent: 4358395 (1982-11-01), Haag et al.

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