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

On the acid-catalyzed isomerization of light paraffins over a ZrO{sub 2}/SO{sub 4} system: The effect of hydration

Journal Article · · Journal of Catalysis
;  [1];  [2]
  1. Univ. of Turin (Italy)
  2. Univ. of Venice (Italy); and others

Over a superacid ZrO{sub 2}/SO{sub 4} system (ZS8; microcrystalline tetragonal, SO{sub 4} content {approximately}2.6 groups per nm{sup 2}), the isomerization of n-butane proceeds rapidly and with high yield of i-butane at 423 K, if the catalyst is calcined in dry air at {approximately}823 K. The active catalyst typically shows: all surface sulfates in a highly covalent form, a high concentration of strong (aprotic) Lewis acid sites, and a fairly low (though never null) concentration of (protonic) Broensted acid sites. A partial rehydration of the catalyst gradually converts the surface sulfates first into a less covalent form and then into an ionic form, decreases the concentration of strong Lewis sites, and increases (up to a factor of {approximately}10) the concentration of Broensted sites, while the catalytic activity is gradually extinguished. Initial activity and initial surface features can be recovered by repeating the catalyst activation step. 17 refs., 5 figs.

OSTI ID:
110986
Journal Information:
Journal of Catalysis, Journal Name: Journal of Catalysis Journal Issue: 1 Vol. 149; ISSN 0021-9517; ISSN JCTLA5
Country of Publication:
United States
Language:
English

Similar Records

Effects of water on the performance of sulfated zirconia catalysts for butane isomerization
Journal Article · Sat Nov 30 23:00:00 EST 1996 · Journal of Catalysis · OSTI ID:468697

Selective poisoning and deactivation of acid sites on sulfated zirconia catalysts for n-butane isomerization
Journal Article · Sun Dec 31 23:00:00 EST 1995 · Journal of Catalysis · OSTI ID:223994

Acid sites in sulfated and metal-promoted zirconium dioxide catalysts
Journal Article · Tue Jan 31 23:00:00 EST 1995 · Journal of Catalysis · OSTI ID:175724