Hydrogenation process comprising a catalytic distillation zone comprising a reaction zone with distribution of hydrogen

• US 6,084,141 A
• Filed: 09/17/1998
• Issued: 07/04/2000
• Est. Priority Date: 12/27/1995
• Status: Expired due to Term

• Current Assignee: Institut Francais Du Petrole
• Original Assignee: Institut Francais Du Petrole
• Inventors: Montecot, Francoise, DiDillon, Blaise, Cosyns, Jean, Nocca, Jean-Luc, Viltard, Jean-Charles, Travers, Christine, Cameron, Charles, Mikitenko, Paul, Dorbon, Michel
• Primary Examiner(s): Yildirim, Bekir L.
• Application Number:
  US09/154,756
• Time in Patent Office: 656 Days
• Field of Search: 585/258, 585/260, 585/250, 585/263, 585/264, 585/266, 585/275
• US Class Current: 585/263
• CPC Class Codes: B01D 3/009 in combination with chemical reactions
• CPC Class Codes: B01J 8/0257 in a cylindrical annular shaped bed
• CPC Class Codes: B01J 8/0278 Feeding reactive fluids for solid material B01J8/0015
• CPC Class Codes: C07C 11/09 Isobutene
• CPC Class Codes: C07C 5/02 by hydrogenation simultaneous hydrogenation and dehydrogenation C07C5/52
• CPC Class Codes: C07C 5/2767 Changing the number of side-chains
• CPC Class Codes: C10G 45/00 Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
• CPC Class Codes: C10G 45/40 containing platinum group metals or compounds thereof
• CPC Class Codes: C10G 45/44 Hydrogenation of the aromatic hydrocarbons
• CPC Class Codes: C10G 49/002 Apparatus for fixed bed hydrotreatment processes
• CPC Class Codes: Y02P 20/10 Process efficiency
• CPC Class Codes: Y10S 203/06 Reactor-distillation

Abstract

The invention concerns a reactive distillation process comprising a distillation zone, associated with a reaction zone which is at least in part internal to said distillation zone and comprises at least one catalytic bed in which the feed is transformed in the presence of a catalyst and at least one gas stream containing hydrogen, characterized in that each catalytic bed in the internal portion of said reaction zone is traversed by said gas stream and liquid in ascending co-current mode. The invention particularly concerns selective hydrogenation processes for light unsaturated hydrocarbons, mainly any olefins and benzene, comprised in a mixture, the major portion of which is constituted by hydrocarbons containing at least five carbon atoms per molecule.

Claims

1. A process for the treatment of a feed, a major portion of which is constituted by hydrocarbons containing at least 5 carbon atoms per molecule and comprising at least one unsaturated compound containing at most six carbon atoms per molecule including benzene, and treating said feed in a distillation zone comprising a stripping zone and a rectification zone, associated with a hydrogenation reaction zone which is at least partially internal to said distillation zone, in which at least a portion of the unsaturated compounds containing at most six carbon atoms per molecule and contained in the feed are hydrogenated in a catalytic bed in the presence of a hydrogenation catalyst and at least one gas stream comprising hydrogen to cause an effluent which is highly depleted in unsaturated compounds containing at most six carbon atoms per molecule to leave overhead of the distillation zone and an effluent which is depleted in unsaturated compounds containing at most six carbon atoms per molecule to leave from the bottom of the distillation zone, characterized in that each catalytic bed of the internal portion of the hydrogenation zone is traversed by an ascending co-current of said gas stream and liquid, and in that the vapour from the distillation zone is maintained substantially completely out of contact with the catalyst.

2. A process according to claim 1 in which, for each catalytic bed in the internal portion of the reaction zone, the liquid is distributed in a zone located below the catalytic bed and the gas stream is distributed in a zone located below or in the catalytic bed.

3. A process according to claim 2, in which the bottom effluent from the distillation zone is mixed with the overhead effluent from said zone.

4. A process according to claim 1, wherein the gas stream is introduced at a location substantially at a level where the liquid is distributed, the gas and liquid being introduced separately into the catalytic bed.

5. A process according to claim 4, in which the gas stream is introduced directly into the catalytic bed.

6. A process according to claim 4, in which the gas stream is introduced means is located below the catalytic bed.

7. A process according to claim 5, in which the gas stream is introduced proximate to where the liquid is distributed.

8. A process according to claim 4, in which the bottom effluent from the distillation zone is mixed with the overhead effluent from said zone.

9. A process according to claim 1, in which the hydrogenation zone is completely internal to the distillation zone.

10. A process according to claim 9, in which the bottom effluent from the distillation zone is mixed with the overhead effluent from said zone.

11. A process according to claim 1, in which the major portion of said gas stream is hydrogen.

12. A process according to claim 1, in which the bottom effluent from the distillation zone is mixed with the overhead effluent from said zone.

13. A process according to claim 12, in which the mixture obtained, after any required stabilisation, is used as a fuel either directly or by incorporation with fuel fractions.

14. A process according to claim 1, in which the internal portion of the reaction zone is at least partially incorporated in the rectification zone.

15. A process according to claim 1, wherein the major portion of the unsaturated compounds containing at most six carbon atoms per molecule are hydrogenated.