Process for the selective hydrogenation and isomerization of hydrocarbons

• US 5,281,753 A
• Filed: 04/21/1992
• Issued: 01/25/1994
• Est. Priority Date: 04/21/1992
• Status: Expired due to Fees

• Current Assignee: Engelhard Corporation (BASF SE)
• Original Assignee: Engelhard Corporation (BASF SE)
• Inventors: Olson, Bruce A., Boyum, Asmund A.
• Primary Examiner(s): Pal, Asok
• Application Number:
  US07/871,881
• Time in Patent Office: 644 Days
• Field of Search: 585/259, 585/260
• US Class Current: 585/259
• CPC Class Codes: C07C 2521/04 Alumina
• CPC Class Codes: C07C 2523/44 Palladium
• CPC Class Codes: C07C 5/05 Partial hydrogenation
• CPC Class Codes: C07C 5/2556 with metals

Abstract

A process for the selective hydrogenation and simultaneous isomerization of hydrocarbons in a feed stream (12) containing a mixture of hydrocarbons of varying degrees of unsaturation and having 4 or more carbon atoms. The process comprises contacting the mixture with hydrogen gas under hydrogenating and isomerizing conditions in the presence of a suitable catalyst (2, 3, and 4) in a multistage packed bed catalytic reactor (1). The process comprises supplying the hydrogen gas (20) in increasing molar ratio amounts relative to the remaining unreacted diolefin concentration in at least three points (24, 26 and 28) spaced apart along the flow direction of the feed stream through the reactor.

Claims

1. A process for the selective hydrogenation of diolefin hydrocarbons and simultaneous isomerization of mono-olefin hydrocarbons in a feed stream containing a mixture of hydrocarbons of varying depress of unsaturation including diolefins and having 4 or more carbon atoms, comprising contacting said mixture with hydrogen gas under hydrogenating and isomerizing conditions in the presence of a suitable catalyst in a multi-stage packed bed catalytic reactor which process comprises supplying said hydrogen gas to said reactor at a plurality of supply points spaced apart along the flow direction of said feed stream through said reactor, the molar ratio of hydrogen gas to unreacted diolefin at the first or starting supply point being sub-stoichiometric, and the molar ratio of hydrogen gas added to unreacted diolefin at a subsequent supply point being in excess of stoichiometric with respect to the unreacted diolefin at that point.

2. The process of claim 1 wherein said plurality of supply points comprises said first supply point, and at least a second and a third supply point spaced along the flow direction of the feed stream, and wherein the molar ratio of hydrogen gas to unreacted diolefin at the second supply point is stoichiometric and the molar ratio of hydrogen gas to unreacted diolefin at the third supply point is excess of stoichiometric, with respect to the unreacted diolefin at the respective points.

3. The process of claim 1 or claim 2 wherein said mixture of hydrocarbons comprising varying degrees of unsaturation contains 4 to 6 carbon atoms.

4. The process of claim 3 wherein said hydrocarbons of varying degrees of unsaturation comprise butadiene.

5. The process of claim 3 wherein said hydrocarbons of varying degrees of unsaturation comprise pentadiene.

6. The process of claim 3 wherein said mixture of hydrocarbons comprises butadiene and butene.

7. The process of claim 3 wherein said mixture of hydrocarbons comprises pentadiene and pentene.

8. The process of claim 1 or claim 2 which is carried out in the liquid and/or vapor-liquid mixed phase.

9. The process of claim 1 or claim 2 wherein the catalyst comprises at least one Group VIII Noble metal on a carrier.

10. The process of claim 9 wherein the catalyst is palladium on alumina.

11. The process of claim 1 or claim 2 wherein the hydrogen gas is supplied in a state of plural splits to the reactor.

13. The process of claim 2 wherein said hydrogen gas is supplied to said reactor in increasing amounts of substiochiometric, stoichiometric and amounts in excess of stoichiometric relative to the amount required to convert any remaining butadiene to butenes in three points spaced apart along the flow direction of said feed stream through said reactor.

12. A process for the selective hydrogenation of diolefin hydrocarbons to mono-olefin hydrocarbons and simultaneous isomerization of mono-olefin hydrocarbons in a feed stream containing a mixture of butadiene and butenes comprising contacting said mixture with hydrogen gas under hydrogenating and isomerizing conditions in the presence of a catalyst composition comprising a Group VIII Noble metal on a carrier in a multi-stage packed bed catalytic reactor, which process comprises performing the hydrogenation and isomerization process in a liquid and/or vapor-liquid mixed phase by supplying said hydrogen gas to said reactor in at least three supply points spaced apart along the flow direction of said feed stream through said reactor in molar ratio amounts starting with sub-stoichiometric at the first supply point and increasing to stoichiometric and then to excess of stoichiometric relative to any unreacted butadiene content remaining in said feed stream at successive respective supply points.

14. A process for the selective hydrogenation of diolefin hydrocarbons and simultaneous isomerization of mono-olefin hydrocarbons in a feed stream containing a mixture of pentadiene and pentenes comprising contacting said mixture with hydrogen gas under hydrogenating and isomerizing conditions in the presence of a catalyst composition comprising a Group VIII Noble metal on a carrier in a multi-stage packed bed catalytic reactor, which process comprises performing the hydrogenation and isomerization process in a liquid and/or vapor-liquid mixed phase by supplying said hydrogen gas to said reactor in at least three supply points spaced apart along the flow direction of said feed stream through said reaction in molar ratio amounts starting with sub-stiochiometirc at the first supply point and increasing to stoichiometric and then to excess of stoichiometric relative to any unreacted pentadiene content remaining in said feed stream at successive respective supply points.

15. The process of claim 14 wherein said hydrogen gas is supplied to said reactor in increasing amounts of substoichiometric, stoichiometric and amounts in excess of stoichiometric relative to the amount required to convert any remaining pentadiene to pentenes in three points spaced apart along the flow direction of said feed stream through said reactor.