IP Library Granted Patent US 10,407,362
Granted Patent B2
US 10,407,362 · App. 15/557,678 · Granted Sep 10, 2019

Diene production method

Inventors: Nobuhiro Kimura (Tokyo, JP); Junji Wakabayashi (Tokyo, JP); Sosuke Higuchi (Tokyo, JP)
Assignee: JXTG NIPPON OIL & ENERGY CORPORATION
C07C5/25B01J23/31B01J23/681B01J23/686B01J23/8872B01J29/123B01J29/143B01J35/0006C07B61/00C07C5/2556C07C5/48C07C7/04C07C11/08C07C11/16B01J2523/00C07C2521/04C07C2521/08C07C2523/04C07C2523/28C07C2523/31C07C2523/44C07C2523/745C07C2523/75C07C2523/755C07C2523/887C07C2529/12C07C2529/14
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Quick Facts
Patent No.
US 10,407,362
App. No.
15/557,678
Granted
Sep 10, 2019
Kind
B2
Abstract

A method for producing diene comprises a step 1 of obtaining a straight chain internal olefin by removing a branched olefin from a raw material including at least the branched olefin and a straight chain olefin; and a step 2 of producing diene from the internal olefin by oxidative dehydrogenation using a first catalyst and a second catalyst, and the first catalyst has a complex oxide including bismuth, molybdenum and oxygen, and the second catalyst includes at least one selected from the group consisting of silica and alumina.

Claims (36)

1. A method for producing diene, comprising:

obtaining a straight chain internal olefin by removing a branched olefin from a raw material including at least the branched olefin and a straight chain olefin; and

producing diene from the internal olefin by oxidative dehydrogenation using a dehydrogenation catalyst and an isomerization catalyst,

wherein

the dehydrogenation catalyst has a complex oxide including bismuth, molybdenum and oxygen, and

the isomerization catalyst includes at least one selected from the group consisting of silica-alumina and zeolites, and

a volume ratio between the dehydrogenation catalyst and the isomerization catalyst (volume of the dehydrogenation catalyst/volume of the isomerization catalyst) is 1.5 to 20.

2. The method for producing diene according to claim 1 , wherein

at least a part of the straight chain olefin is a terminal olefin, and

in obtaining the straight chain internal olefin, reactive distillation is performed to remove the branched olefin from the raw material and to isomerize the terminal olefin to the internal olefin.

3. The method for producing diene according to claim 1 , wherein

the isomerization catalyst has a support and an element supported on the support,

the support includes at least one selected from the group consisting of silica and alumina, and

the element supported on the support is at least one selected from the group consisting of Group 10 elements of the periodic table and Group 11 elements of the periodic table, and lanthanoids.

4. The method for producing diene according to claim 3 , wherein Ni is the Group 10 element of the periodic table, Cu, Ag or Au is the Group 11 element of the periodic table, and La is the lanthanoid.

5. The method for producing diene according to claim 3 , wherein Ag is supported on the support as the Group 11 element of the periodic table.

6. The method for producing diene according to claim 1 ,

wherein the isomerization catalyst includes silica and alumina, and

a total acid amount of the isomerization catalyst measured by ammonia temperature programmed desorption is 0.11 mmol/g or less.

7. The method for producing diene according to claim 1 ,

wherein the isomerization catalyst includes silica and alumina, and

the isomerization catalyst has a ratio A 2 /A 1 of 0.03 or more of an amount A 2 of acid sites measured in a temperature range of 600° C. or higher to an amount A 1 of all acid sites measured by ammonia temperature programmed desorption.

8. The method for producing diene according to claim 1 , wherein

the isomerization catalyst includes silica and alumina, and

a molar ratio of Si to Al (Si/Al) in the second catalyst is 100 or more.

9. The method for producing diene according to claim 1 , wherein

assuming that a mass content of the branched olefin in the raw material is C 1 and a mass content of the straight chain olefin in the raw material is C 2 ,

C 2 /C 1 is 0.1 to 5.0.

10. The method for producing diene according to claim 1 , wherein

the straight chain olefin includes butene.

11. The method for producing diene according to claim 1 , wherein

the raw material is obtained by fluid catalytic cracking of a heavy oil fraction, and

a number of carbon atoms of the branched olefin or the straight chain olefin is 4.

12. The method for producing diene according to claim 1 , wherein

the raw material is obtained by thermal decomposition of naphtha, and

a number of carbon atoms of the branched olefin or the straight chain olefin is 4.

Assignments (2)
CHANGE OF NAME Recorded Aug 25, 2020
From: JXTG NIPPON OIL ENERGY CORPORATION
To: ENEOS CORPORATION
Reel/Frame 053596/0282 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 12, 2017
From: KIMURA, NOBUHIRO; WAKABAYASHI, JUNJI; HIGUCHI, SOSUKE
To: JXTG NIPPON OIL & ENERGY CORPORATION
Reel/Frame 043564/0155 →
Priority Claims (2)
JP 2015-058331 · Mar 20, 2015 · national
JP 2015-110059 · May 29, 2015 · national
Continuity (1)
Related Publication 20180050970A1 · Feb 22, 2018