Process and plant for the conversion of olefinic C4 cuts to polyisobutene and to propylene
AssigneeInstitut Francais du Petrole
InventorsJean-Alain Chodorge, Dominique Commereuc, Jean Cosyns, Didier Duee, Bernard Torck
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Abstract
The present invention concerns a process for the conversion of an olefinic C4 cut to polyisobutene and to propylene by metathesis. The process comprises three successive steps: (1) selective hydrogenation of diolefins with simultaneous isomerisation of 1-butene to 2-butenes, (2) polymerisation of the isobutene, including optional prior extraction of the isobutene, (3) metathesis of 2-butene with ethylene. Part or all of the C4 cut may originate from the metathesis of an olefinic C5 cut with ethylene after hydroisomerisation of the C5 cut. Application to C4 and C5 steam cracking cuts.
Claims9
An apparatus for converting an olefinic C4 cut comprising diolefins, 1-butene, isobutene and acetylenic impurities to polyisobutene and to propylene, comprising:
- a) a first selective hydrogenation zone having a catalyst bed for introduction of the C4 cut, for hydrogenating diolefins anid acetylenic impurities and simultaneously isomerizing 1-butene to 2-butenes;
- b) in downstream connection with the first selective hydrogenation zone, a first polymerization and separation zone containing at least one acid catalyst for polymerizing the isobutene in the effluent from the tirst selective hydrogenation zone to polyisobutene and separating the polyisobutene from a residual C4 cut;
- c) in downstream connection with the first polymerization and separation zone, a first metathesis zone conraining at least one catalyst for metathesis of the residual C4 cut from the first polymerization and separation zone with ethylene to produce propylene and for separating a propylene metathesis product from by-products;
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- d) a section for treating an olefinic C5 cut to produce at least a portion of the olefinic C4 cut to be converted, said C5 cut containing diolefins, alpha olefins containing 5carbon atoms and acetylenic impurities, the section comprising:
- 1) a second selective hydrogenation zone comprising at least one bed of a catalyst for hydrogenating diolefins and acerylenic impurities and simultaneously isomerizing alpha olefins containing 5 carbon atoms to 2-pentenes and 2-methyl-2-buttene;
- 2) in downstream connection with the second selective hydrogenation zone, a second metathesis zone containing at least one catalyst for metathesis of thre effluent of the second selective hydrogenation zone with ethylene and for separating from the metathesis product propylene, a mixture of 1-butene and isobutene and by-product, and
- 3) a connection for supplying the mixture of 1-butene and isobutene obtained from the second metathesis zone as at least a portion of the olefinic C4 cut in the first selective hydrogenation zone.
Dependencies are inferred from the claim text.