Olefin trimerization
AssigneeNeste Oyj
InventorsAntti Pyhälahti, Jaana Kanervo
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Abstract
The present disclosure relates to a process and a production unit that are used to catalytically manufacture olefin trimers from olefin monomers, and wherein olefin dimers are recycled after dimerization reaction, and reacted with olefin monomers in an addition reaction.
Drawings
Claims19
A process for manufacturing olefin trimers comprising:
- feeding into a reactor containing a dimerization catalyst:
- olefin monomer feed and at least one oxygen-containing moderator;
- operating the reactor at a temperature selected from a range of 40-140° C. and at a pressure selected from a range of 10-40 bar for carrying out catalytic dimerization reactions between olefin monomers and olefin monomers, and addition reactions between olefin monomers and olefin dimers;
- withdrawing a reactor outlet stream from the reactor;
- and
- distilling the reactor outlet stream to separate at least one lighter product containing olefin dimers, and a heavier bottom product containing olefin trimers;
- wherein
- at least a portion of the at least one lighter product is recycled into the reactor for providing a recycle feed,
- olefin monomers are fed into the reactor predominantly as a fresh olefin monomer feed,
- amounts of the fresh olefin monomer feed and the recycle feed fed into the reactor are controlled such that a mass ratio of olefin monomers to olefin dimers entering the reactor is selected from a range of 1:8-1:15,
- and wherein catalytic reactions of the reactor are carried out at operational conditions wherein olefins remain in liquid phase.
A production unit configured for manufacturing olefin trimers, the production unit comprising:
- a. at least one reactor unit configured to receive an acid catalyst;
- b. at least one distillation column configured to separate isooctene from isododecene;
- c. at least one reactor feed line in fluid connection with the reactor unit and a reservoir for olefin monomers;
- d. at least one reactor outlet stream line in fluid connection with the reactor unit and the distillation column;
- e. at least one recycle line in fluid connection with the at least one distillation column and the at least one reactor unit;
- and
- f. a bottom product line in fluid connection with the at least one distillation column and a bottom product reservoir;
- wherein the production unit comprises:
- a first recycle line configured to recycle at least one of olefin monomers, diluent, and modifier through a first recycle line into the at least one reactor unit;
- and
- a second recycle line configured to recycle olefin dimers to the at least one reactor unit.
Dependencies are inferred from the claim text.