Arco Chemical Technology, L.p.

Glenn E Cozzone

John A Sofranko

David W Leyshon

Anne Mae Gaffney

C Andrew Jones

John C Jubin, Jr

W Wayne Wentzheimer

Low value feed hydrocarbons are converted to high octane value tertiary ethers using a multiple riser fluidized solids catalytic reactor wherein in a first riser the hydrocarbon feed is converted to iso and linear C.sub.4 and C.sub.5 olefins, the iso-olefins are etherified, the linear C.sub.4 and C.sub.5 olefins are isomerized to iso C.sub.4 and C.sub.5 olefins in a second riser of the fluidized solids reactor, iso C.sub.4 and C.sub.5 olefins from the second riser are also etherified to high octane value tertiary ethers, and catalyst from both risers is regenerated in a common regeneration zone.

Hydrocarbon conversion

Thermoset polymers such as polyurethanes and unsaturated polyester resins may be conveniently converted into useful volatile lower molecular weight organic compounds. Fillers can be recovered from filled thermoset resins using the process of the invention, which employs a zeolite-containing particulate catalyst.

Process for reclaiming a thermoset polymer

The present invention relates to the conversion of saturated paraffin hydrocarbons having 4 or more carbon atoms to olefins having fewer carbon atoms. In particular, the invention provides for contact of a mixture of 40 to 95 wt % paraffin hydrocarbons having 4 or more carbon atoms and 5 to 60 wt % olefins having 4 or more carbon atoms with solid zeolitic catalyst such as ZSM-5 at conditions effective to form propylene and the separation of light olefins from the reaction mixture.

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West Chester, PA, United States of America

Glenn E Cozzone