Oligomerization of olefins in supercritical water

• US 4,465,888 A
• Filed: 04/14/1983
• Issued: 08/14/1984
• Est. Priority Date: 04/14/1983
• Status: Expired due to Fees

• Current Assignee: Standard Oil Company (BP PLC)
• Original Assignee: Standard Oil Company (BP PLC)
• Inventors: Paspek, Stephen C. Jr.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Pal, A.
• Application Number:
  US06/485,094
• Time in Patent Office: 488 Days
• Field of Search: 585/510, 585/520, 585/732, 526/80, 526/84
• US Class Current: 585/520
• CPC Class Codes: C07C 2/06 of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
• CPC Class Codes: Y02P 20/54 using solvents, e.g. supercritical solvents or ionic liquids

Abstract

Fuel range liquid hydrocarbons are produced by the oligomerization of olefins in a process comprising contacting the olefins containing 5 or less carbon atoms with a water containing medium at a temperature sufficient to cause oligomerization and at a pressure sufficient to maintain the density of the medium at about 0.5 to about 1.0 grams per milliliter.

Claims

1. A process for the oligomerization of olefins containing five or less carbon atoms to produce liquid hydrocarbons containing four to twenty carbon atoms, the process comprising contacting the olefins with a water containing medium at a temperature of greater than 200°

C. and a pressure from 0 to 7,000 psi whereby the temperature and pressure are sufficient to maintain the mixture of olefins and water containing medium about at or above the critical temperature and pressure of the mixture.

2. The process of claim 1, where the density of the water containing medium is about 0.05 to about 1.0 grams per milimeter.

3. The process of claim 1, where the density of the water containing medium is about 0.1 to about 0.4 grams per milliliter.

4. The process of claim 3, where the density of the water containing medium is about 0.2 to about 0.3 grams per milliliter.

5. The process of claim 1, where the olefins are in contact with the water containing medium at oligomerization conditions for a period of time in the range of about one minute to about six hours.

6. The process of claim 5, where the olefins are in contact with the water containing medium at oligomerization conditions for a period of time in the range of about three minutes to about six hours.

7. The process of claim 6, where the olefins are in contact with the water containing medium at oligomerization conditions for a period of time in the range of about five minutes to about one hour.

8. The process of claim 1, where the water to olefin weight ratio is about 0.25:

1 to about 50;

1.

9. The process of claim 8, where the water to olefin weight ratio is about 0.7:

1 to about 7;

1.

10. The process of claim 9, where the water to olefin weight ratio is about 1:

1 to about 2;

1.

11. The process of claim 1, where the temperature is about 375°

C. to about 500°

C. and the pressure is at least about 2000 psi.

12. The process of claim 1, where the olefins reacted in the process are introduced into the process in a feedstream with an olefin content of less than 100 percent.

13. The process of claim 12, where the olefins reacted in the process are introduced into the process in a refinery stream of coker off-gas or retort off-gas.

14. The process of claim 1 where the oligomerization occurs in a batch reactor.

15. The process of claim 1 where oligomerization occurs in a continuous flow reactor.