Artigo Revisado por pares

Simulation of xylene recovery loops in large scale aromatic plants

1978; Elsevier BV; Volume: 2; Issue: 1 Linguagem: Inglês

10.1016/0098-1354(78)80002-7

ISSN

1873-4375

Autores

A. M. Fayon, G.L. Imperiali,

Tópico(s)

Catalysis for Biomass Conversion

Resumo

Steady-state process simulation is used to study a xylene recovery loop in a large aromatics plant. The process configuration follows closely that of Mobil's aromatics facility in Naples, Italy. The simulation includes rigorous tower calculations and specially written subroutines for unique process components. Process questions examined are the optimal cycle length for isomerization catalyst, the value of ethylbenzene recovery, and the preferred process configuration.

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