Selective hydrogenation method for hydrocarbons

• US 4,469,907 A
• Filed: 03/02/1983
• Issued: 09/04/1984
• Est. Priority Date: 03/02/1982
• Status: Expired due to Term

• Current Assignee: Sumitomo Chemical Company Limited
• Original Assignee: Sumitomo Chemical Company Limited
• Inventors: Higashio, Yasuhiko, Araki, Masashi
• Primary Examiner(s): Davis, Curtis R.
• Application Number:
  US06/471,401
• Time in Patent Office: 552 Days
• Field of Search: 585/259, 585/265, 585/275, 585/277, 208/143, 208/216
• US Class Current: 585/259
• CPC Class Codes: C07C 2523/44 Palladium
• CPC Class Codes: C07C 5/03 of non-aromatic carbon-to-carbon double bonds
• CPC Class Codes: C07C 5/08 of carbon-to-carbon triple bonds

Abstract

A selective hydrogenation method for highly saturated hydrocarbons by bringing a mixture of hydrocarbons of low hydrogenation degree having 4 or more carbon atoms containing the highly saturated hydrocarbons in the presence of a catalyst using a fixed bed reaction vessel, which comprises supplying a hydrogen gas in a state of plural splits along the flow direction of the fixed bed reaction vessel is disclosed. In accordance with this mehtod, only the highly unsaturated hydrocarbons are selectively hydrogenated without being accompanied by isomerization of olefins.

Claims

1. A method of selectively hydrogenating highly unsaturated hydrocarbons by bringing a mixture of hydrocarbons of low unsaturated degree having 4 or more carbon atoms containing said highly unsaturated hydrocarbons into contact with hydrogen in the presence of a catalyst using a fixed bed reaction vessel, which comprises supplying said hydrogen gas in a state of plural splits along the flow direction of said fixed bed reaction vessel.

2. A method as claimed in claim 1, wherein the flow rate of hydrogen gas in the 2nd split or later split or splits along the flow direction of said fixed bed reaction vessel is 5 to 100% of the previous split.

3. A method as claimed in claim 1 or 2, wherein using a fixed bed reaction vessel containing plural catalyst layers split into plural zones along the flow direction, hydrogen gas is independently supplied to each zone.

4. A method as claimed in any of claims 1, 2, or 3, wherein the hydrogenation reaction is performed in a vapor phase.

5. A method as claimed in any of claims 1, 2, or 3, wherein the total amount of hydrogen gas supplied is 1.1 to 2.0 moles per mole of said highly unsaturated hydrocarbons in the starting hydrocarbon mixture.

6. A method as claimed in any of claims 1 to 5, wherein a palladium catalyst is used as the catalyst.

9. The method of claim 1 wherein said hydrocarbons of low unsaturation degree comprise mainly 1-butene and 2-butene.

7. A method of selectively hydrogenating highly unsaturated hydrocarbons by bringing a mixture of hydrocarbons of low unsaturation degree having 4 or more carbon atoms containing said highly unsaturated hydrocarbons into contact with hydrogen in the presence of a catalyst using a fixed bed reaction vessel, which comprises performing the hydrogenation reaction in a vapor phase using a palladium catalyst by supplying a hydrogen gas in a state of plural splits along the flow direction of said fixed bed reaction vessel, the total amount of said hydrogen gas supplied being 1.1 to 2.0 moles per mole of said highly unsaturated hydrocarbons.

8. A method of treating a mixture of hydrocarbons of low unsaturation degree having 4 or more carbon atoms with hydrocarbons of high unsaturation degree to hydrogenate said hydrocarbons of high unsaturation degree without isomerizing said hydrocarbons of low unsaturation degree, said method comprising bringing said mixture into contact with hydrogen gas in the presence of a catalyst using a fixed bed reaction vessel, wherein said hydrogen gas is supplied in a state of plural splits along the flow direction of said fixed bed reaction vessel.