Simulated moving bed reactor forp-xylene production: Optimal particle size-Reference-Cited by-同舟云学术

Simulated moving bed reactor forp-xylene production: Optimal particle size

Published:2015-09-29 Issue:12 Volume:93 Page:2205-2213
ISSN:0008-4034
Container-title:The Canadian Journal of Chemical Engineering
language:en
Short-container-title:Can. J. Chem. Eng.

Author:

Gonçalves Jonathan C.¹,Rodrigues Alírio E.¹

Affiliation:

1. LSRE - Laboratory of Separation and Reaction Engineering - Associate Laboratory LSRE/LCM; Faculdade de Engenharia; Universidade do Porto; Porto Portugal

Publisher

Wiley

Subject

General Chemical Engineering

Reference28 articles.

1. Reactive separations for process intensification: an industrial perspective

2. Simulated moving bed reactor for isomerization and separation of p-xylene

3. Intensification of Paraxylene Production using a Simulated Moving Bed Reactor

4. A new process combining adsorption and enzyme reaction for producing higher-fructose syrup

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