Etherification process with hydrogen rejuvenation

Organic compounds -- part of the class 532-570 series – Organic compounds – Oxygen containing

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203DIG6, C07C 4106

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active

051664542

ABSTRACT:
A multistage process for etherifying C.sub.4.sup.+ aliphatic hydrocarbon feedstock containing isoalkane including the step of contacting the hydrocarbon feedstock with dehydrogenation catalyst at elevated temperature under dehydrogenation reaction conditions to obtain C.sub.4.sup.+ isoalkene and hydrogen, and separating dehydrogenation effluent to obtain an olefinic stream rich in isoalkene and a hydrogen stream.
The olefinic stream and aliphatic alcohol are contacted in an esterification stage under partial etherification conditions with a regenerable inorganic metal oxide acid solid catalyst to convert a major amount of the isoalkene to C.sub.5.sup.+ tertiary-alkyl ether. In the preferred embodiment, effluent recovered from the first stage containing ether product, unreacted alcohol and unreacted olefin including isoalkene is charged to a second stage catalytic distillation column containing solid acid resin etherification catalyst in a plurality of fixed bed catalysis-distillation zones to complete substantially full etherification of isoalkene.
At least a portion of recovered hydrogen is employed for contacting the regenerable etherification catalyst to remove feedstock impurity and coke and to restore acid activity. In the manufacture of MTBE, the alcohol consists essentially of methanol and the C4+ feedstock consists predominantly of C.sub.4 hydrocarbons containing isobutane. The first etherification stage catalyst may comprise medium pore zeolite and the second stage catalyst may comprise polymeric sulfonic acid resin.

REFERENCES:
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patent: 4906788 (1990-03-01), Scott et al.
patent: 5013329 (1991-05-01), Bell et al.
patent: 5015782 (1991-05-01), Harandi et al.
Chu et al., Ind. Eng. Chem. Res. 1987, 26, 365-369.

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