Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

The disproportionation of xylenes over a cay zeolite catalyst

Journal Article · · Int. Chem. Eng.; (United States)
OSTI ID:5996627
The disproportionation of xylenes over a CaY zeolite catalyst was studied at 300/sup 0/-500/sup 0/C, 15 kg-f/sq cm, and 0.61/hr space velocity in a single-pass reactor over a single 50 cc portion of catalyst. The average conversion of m-xylene after five hours increased with increasing temperature to a maximum of 72% at 400/sup 0/-450/sup 0/C and then dropped off to 45% at 500/sup 0/C. During the initial contact, conversion at 500/sup 0/C was 74%, but this fell to 18% after five hours. The amount of deactivating coke formed after five hours was 3% of the catalyst weight at 300/sup 0/-350/sup 0/C and 12-15% at 450/sup 0/-500/sup 0/C. The main disproportionation products were toluene and trimethylbenzenes, the latter fraction being 8-10% hemimellitene, 20-25% mesitylene, and 68-72% pseudocumene. The yield of trimethylbenzenes reached 22 mole % at 400/sup 0/C and declined to 9 mole % at 500/sup 0/C. The yield of tetramethylbenzenes (50-51% isodurene, 38% durene, and 7-12% prehnitol) also peaked at 400/sup 0/C. At 400/sup 0/-450/sup 0/C, disproportionation accounted for 45% and isomerization to o- and p-xylene for 26% of the products. In the case of o-xylene, total conversion was 88-90% at 450/sup 0/-475/sup 0/C; isomerization accounted for 55% and disproportionation for only 35% of the yields. All the product yields were increased by increasing pressure. Table and graph.
Research Organization:
Inst. of Organic Chemistry, Academy of Science, USSR
OSTI ID:
5996627
Journal Information:
Int. Chem. Eng.; (United States), Journal Name: Int. Chem. Eng.; (United States) Vol. 18:1; ISSN INCEA
Country of Publication:
United States
Language:
English