Paraffin isomerization, paraffin disproportionation, and benzene alkylation catalyzed by aluminum chloride/sulfonic acid resins
The catalytic isomerization of n-butane at 298/sup 0/-413/sup 0/K and n-pentane at 343/sup 0/-413/sup 0/K in a packed-bed flow reactor at 1 atm in the presence of aluminum chloride/sulfonic acid resin was accompanied by disproportionation and cracking. The selectivity to isomerization products was approx. 40% for n-pentane and > 99% for n-butane. Kinetics of n-butane isomerization at 308/sup 0/-338/sup 0/K were determined by using a partially deactivated catalyst batch, and the dependence of the isomerization rate on the partial pressure of n-butane was fitted using a power-law or a Langmuir-Hinshelwood rate equation. Alkylations of benzene with propylene catalyzed by sulfonic acid resin at 328/sup 0/K and aluminum chloride/sulfonic acid resin at 295/sup 0/K gave isopropylbenzene and mono- to tetra-isopropylbenzenes, respectively. A catalyst deactivation model was developed and used to correlate the time-dependent behavior of n-butane isomerization and benzene propylation. The data indicated that Broensted acid sites are responsible for the activity of the supported aluminum chloride catalyst.
- OSTI ID:
- 6462048
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
400201 -- Chemical & Physicochemical Properties
400301* -- Organic Chemistry-- Chemical & Physicochemical Properties-- (-1987)
ALKANES
ALKYLATION
ALUMINIUM CHLORIDES
ALUMINIUM COMPOUNDS
AROMATICS
BENZENE
BUTANE
CATALYSTS
CHEMICAL REACTIONS
CHEMICAL REACTORS
CHLORIDES
CHLORINE COMPOUNDS
EQUATIONS
HALIDES
HALOGEN COMPOUNDS
HYDROCARBONS
ISOMERIZATION
KINETICS
MATHEMATICAL MODELS
ORGANIC ACIDS
ORGANIC COMPOUNDS
ORGANIC POLYMERS
ORGANIC SULFUR COMPOUNDS
OTHER ORGANIC COMPOUNDS
OXIDATION
PACKED BED
PARAFFIN
PENTANE
PETROCHEMICALS
PETROLEUM PRODUCTS
POLYMERS
REACTION KINETICS
REDUCTION
RESINS
SULFONIC ACIDS
WAXES