Disproportionation/double-bond isomerization of olefins

• US 4,180,524 A
• Filed: 02/16/1978
• Issued: 12/25/1979
• Est. Priority Date: 02/16/1978
• Status: Expired due to Term

• Current Assignee: Phillips Petroleum Company (ConocoPhillips)
• Original Assignee: Phillips Petroleum Company (ConocoPhillips)
• Inventors: Reusser, Robert E., Hughes, William B.
• Primary Examiner(s): Hearn, Brian
• Application Number:
  US05/878,537
• Time in Patent Office: 677 Days
• Field of Search: 260/680 R, 260/683 D, 260/683.2, 252/467
• US Class Current: 585/644
• CPC Class Codes: B01J 23/24 Chromium, molybdenum or tungsten
• CPC Class Codes: B01J 23/36 Rhenium
• CPC Class Codes: C07C 6/04 at a carbon-to-carbon double bond
• CPC Class Codes: C07C 6/06 at a cyclic carbon-to-carbon double bond

Abstract

Double bond isomerization and disproportionation of olefins is obtained by contact with a catalyst in a single-stage composition containing a support, uranium, and at least one of tungsten, molybdenum, or rhenium.

Claims

1. A process for the treatment of an olefinic hydrocarbon which comprises contacting said olefinic hydrocarbon under effective double bond isomerization and disproportionation conditions with an activated calcined homogeneous catalyst compositions consisting essentially of support/uranium/at least one of molybdenum, tungsten, and rhenium, containing about 0.1 to 25 weight percent total of uranium, molybdenum, tungsten, and rhenium, each calculated as the metal, and a proportion of uranium:

molybdenum, tungsten, or rhenium of about 2;

1 to 0.1;

1, prepared by forming a homogenous composite of support, uranium, and at least one of molybdenum, tungsten, and rhenium, calcining said homogenous composite at elevated temperatures in a molecular-oxygen containing atmosphere, and thereafter activating at elevated temperature in a reducing atmosphere, thereby preparing said activated catalyst composition.

2. A process according to claim 1 wherein said catalyst composition consists essentially of a molecular hydrogen or carbon monoxide treated uranium/molybdenum, tungsten or rhenium/support catalyst composition which is prepared by steps comprising impregnating a solid support with water soluble salts of uranium and at least one of molybdenum, tungsten, or rhenium salts, calcining the resulting impregnated solid support at elevated temperatures in a molecular-oxygen containing atmosphere, and heating the calcined impregnated supported composition with hydrogen or carbon monoxide under reducing conditions at elevated temperatures.

3. The process in accordance with claim 2 wherein said calcining step is conducted at about 500°

to 800°

C., and said activation treatment with said molecular hydrogen or carbon monoxide is conducted at about 300°

to 500°

C.

4. The process of claim 1 wherein in said catalyst composition said support is alumina, silica, silica-alumina, zirconia, titania, thoria, magnesia silicate, zinc aluminate, or mixture thereof.

5. The process according to claim 1 wherein said olefinic hydrocarbon is

(1) Acyclic monoolefins, including those with aryl, cycloalkyl, and cycloalkenyl substituents, having 3-20 carbon atoms per molecule with no branching closer than about the 3-position to the double bond, no quaternary carbon atoms and no aromatic substitution closer than the 4-position to the double bond, and mixtures of such unsubstituted acyclic monoolefins;

(2) A mixture of ethylene and one or more acyclic unsubstituted internal monoolefins of (1);

(3) Acyclic, nonconjugated polyenes having from 5 to about 20 carbon atoms per molecule, containing from 2 to about 4 double bonds per molecule and having no double bond with branching nearer than the 3-position to that double bond, and having at least one double bond with no quaternary carbon atoms and no aromatic substitution nearer than the 4-position to that double bond, or mixtures of such polyenes;

(4) A mixture of ethylene and one or more acyclic polyenes of (3) which contain at least one internal double bond;

(5) Cyclopentene;

(6) Cyclic and bicyclic monoolefins having 7 to 12 ring carbon atoms, including those substituted with up to 3 alkyl groups having up to about 5 carbon atoms, with no branching closer than the 3-position and with no quaternary carbon atoms closer than the 4-position to the double bond, and mixtures of such olefins including mixtures wih cyclopentene;

(7 ) A mixture of one or more of the monocyclic olefins of (6) with either ethylene or with one or more unsubstituted acyclic monoolefins of (1);

(8) Cyclic and bicyclic nonconjugated polyenes having from 5 to about 12 ring carbon atoms, including those substituted with up to 3 alkyl groups having up to about 5 carbon atoms each, having at least one double bond with no branching closer than the 3-position and with no quaternary carbon atoms closer than the 4-position to that double bond, and mixtures thereof;

or

(9) A mixture of one or more monocyclic polyenes of (8) with one or more acyclic 1-olefins having from 2 to about 10 carbon atoms, having no branching nearer than the 3-position and no quaternary carbon atoms nearer than the 4-position to the double bond.

6. The process according to claim 5 wherein said effective conditions include a contacting temperature of about 10°

to 600°

C., a pressure of about 0 to 15 mPa, and a feed rate of about 0.1 to 1000 weight hourly space velocity.

7. The process according to claim 6 wherein said olefin is an acyclic monoolefin of at least three carbon atoms per molecule.

8. The process according to claim 6 wherein said olefin hydrocarbon is an acyclic polyene of at least three carbon atoms per molecule.

9. The process according to claim 6 wherein said olefinic hydrocarbon is a cyclic monoolefin of at least four carbon atoms per molecule.

10. The process according to claim 6 wherein said olefin hydrocarbon is a cyclic polyene of at least four carbon atoms per molecule.

11. The process according to claim 6 wherein said olefin is an acyclic monoolefin of at least three carbon atoms per molecule in admixture with ethylene.

12. The process according to claim 6 wherein said olefin hydrocarbon is an acyclic polyene of at least three carbon atoms per molecule in admixture with ethylene.

13. The process according to claim 6 wherein said olefinic hydrocarbon is a cyclic monoolefin of at least four carbon atoms per molecule in admixture with ethylene.

14. The process according to claim 6 wherein said olefin hydrocarbon is a cyclic polyene of at least four carbon atoms per molecule in admixture with ethylene.

15. The process according to claim 6 wherein said olefinic hydrocarbon is an acyclic olefin and is selected from the group consisting of propylene, 1-butene, isobutene, 2-butene, 1-pentene, 2-pentene, 1-hexene, 2-hexene, 4-octene, 2-nonene, 3-decene, 4-dodecene, 1-hexadecene, 1-dodecene, 1-hexadecene, 2-methyl-1-butene, 3-methyl-1-butene, 4-methyl-1-pentene, 1-eicosene, 1-phenyl-2-butene, 3-eicosene, 8-ethyl-2-decene, vinylcyclohexane, 4-vinylcyclohexene, and mixtures thereof.

16. The process according to claim 6 wherein said olefinic hydrocarbon is a cyclic olefin and is selected from the group consisting of cyclopentene, cyclooctene, cyclodecene, 3,3,5,5-tetramethylcyclononene, 1,5-cyclooctadiene, 1,5,9-cyclododecatriene, 2-methyl-6-ethyl-1,4-cyclooctadiene, and mixtures thereof.

17. The process according to claim 6 wherein said olefinic hydrocarbon is 2,4,4-trimethyl-1-pentene.

18. The process according to claim 17 wherein said 2,4,4-trimethyl-1-pentene is in admixture with ethylene.

19. The process according to claim 18 wherein said catalyst is a silica support/uranium/tungsten promoted activated, calcined catalyst composition.

20. The process according to claim 19 wherein said activated, calcined composition contains a weight percent ratio of about 0.464/0.435/10 tungsten/uranium/silica.

21. The process according to claim 6 wherein said process further employs a feed stream diluted with an inert diluent comprising a saturated aliphatic or cycloaliphatic hydrocarbon.

22. The process according to claim 1 wherein said olefinic hydrocarbon is

(1) propylene, 1-pentene, 2-pentene, 1-butene, 2-butene, isobutene 2-methyl-1-butene, 3-methyl-1butene, 1-pentene, 2-pentene, 2-hexene, 1-hexene, 4-octene, 2-nonene, 4-methyl-1-pentene, 3-decene, 8-ethyl-2-decene, 1-dodecene, 4-dodecene, 1-hexadecene, vinylcyclohexane, 4-vinylcyclohexene, 1-phenyl-2-butene, 3-eicosene, 1-eicosene, or mixtures;

(2) ethylene and 2-butene, ethylene and 2-pentene, ethylene and 3-hexene, ethylene and 3-heptene, ethylene and 4-methyl-2-pentene, ethylene and 4-octene, ethylene and 4-dodecene, or mixtures;

(3) 1,4-pentadiene, 1,5-hexadiene, 2,5-octadiene, 1,7-octadiene, 2,6-decadiene, 1,5,9-dodecatriene, 4-methyl-1,6-heptadiene, 1,6-octadiene, or mixtures;

(4) ethylene and 1,6-octadiene, ethylene and 1,5-decadiene, or mixtures;

(5) cyclopentene;

(6) cycloheptene, cyclooctene, 4-methylcyclooctene, 3-methyl-5-ethylcyclodecene, cyclononene, cyclododecene, norbornene, or mixtures;

(7) ethylene and cycloheptene, ethylene and cyclooctene, propylene and cyclodecene, pentene-2 and cyclooctene, ethylene and cyclododecene, or mixtures;

(8) 1,5-cyclooctadiene, 1,5,9-cyclododecatriene, 1,4-cycloheptadiene, norbornadiene, or mixtures;

(9) 1,5-cyclooctadiene and ethylene, 1,5,9-cyclodecatriene and ethylene, 1,5,9-cyclododecatriene and pentene-1, or mixtures.

23. The process of claim 1 wherein said support is silica.