Butadiene preparation method providing excellent catalyst reproducibility

Patent metadata

Field	Value
Publication number	US-10730809-B2
Application number	US-201716098077-A
Country	US
Kind code	B2
Filing date	Sep 21, 2017
Priority date	Oct 28, 2016
Publication date	Aug 4, 2020
Grant date	Aug 4, 2020

Abstract

A method of preparing butadiene that includes supplying butene, oxygen, nitrogen, and steam into a reactor filled with a metal oxide catalyst, and performing an oxidative dehydrogenation reaction at a temperature of 300 to 450° C. as a reaction step; after the reaction step, maintaining supplying the butene, oxygen, nitrogen, and steam within a range within which the flow rate change of the butene, oxygen, nitrogen, and steam is less than ±40%, or stopping supplying the butene, and cooling the reactor to a temperature range of 200° C. or lower and higher than 70° C. as a first cooling step; and after the first cooling step, stopping supplying the butene, oxygen, nitrogen, and steam or stopping at least supplying the butene, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step.

First claim

The invention claimed is:

1. A method of preparing butadiene, comprising:
supplying butene, oxygen, nitrogen, and steam to a reactor filled with a metal oxide catalyst, and performing an oxidative dehydrogenation reaction at a temperature of 300 to 450° C. as a reaction step;
after the reaction step, reducing the temperature of the reactor via a two-step process to prevent catalyst deactivation, by either:
1) cooling the reactor by:
(a) maintaining supply of the butene, oxygen, nitrogen, and steam within a range within which a flow rate change of each of the butene, oxygen, nitrogen, and steam is less than ±40%, and cooling the reactor to a temperature in a range of 200° C. or lower and higher than 70° C. as a first cooling step, and
(b) after the first cooling step, stopping supply of at least the butene, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step; or

(2) cooling the reactor by:
(c) stopping supply of the butene while supply of the oxygen, nitrogen, and steam is maintained, and cooling the reactor to a temperature in a range of 200° C. or lower and higher than 70° C. as a first cooling step; and
(d) after the first cooling step,
(i) maintaining supply of the oxygen, nitrogen, and steam, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step, or
(ii) stopping supply of the oxygen, nitrogen, and/or steam, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step.

2. The method according to claim 1 , wherein, in the second cooling step (b), either supply of the butene and steam is stopped, or supply of the butene, oxygen, nitrogen, and steam is stopped.

3. The method according to claim 2 , wherein an activity reduction rate is −1% or more.

4. The method according to claim 1 , wherein, in the first cooling step, the reactor is cooled to a temperature of 200° C. to 100° C.

5. The method according to claim 1 , wherein the metal oxide catalyst comprises:
iron (Fe); and
at least one metal (A) selected from Cu, Ti, V, Cr, K, Al, Zr, Cs, Ca, Be, Zn, Mg, Mn, and Co.

6. The method according to claim 5 , wherein an atomic ratio of iron (Fe) to at least one metal (A) in the metal oxide catalyst is from 1.5:1 to 4:1.

7. The method according to claim 1 , wherein a molar ratio of butene: oxygen: nitrogen: steam supplied to the reactor is 1:0.1 to 2:1 to 10:1 to 30.

8. The method according to claim 1 , wherein, in the oxidative dehydrogenation reaction, gas hourly space velocity (GHSV) is 20 to 150 h −1 .

9. The method according to claim 1 , wherein, in the second cooling step, the reactor is cooled to a temperature of 70 to 30° C.

10. The method according to claim 1 , further comprising a step of restarting supply of the butene, oxygen, nitrogen, and steam and then performing the oxidative dehydrogenation reaction again at a temperature of 300 to 450° C., after the second cooling step.

11. The method according to claim 1 , wherein an activity reduction rate is −1% or more.

12. The method according to claim 1 , further comprising a step of restarting supply of the butene, oxygen, nitrogen, and steam and then performing the oxidative dehydrogenation reaction again at a temperature of 300 to 450° C., after the second cooling step, wherein an activity reduction rate is −1% or more.

13. A method of preparing butadiene, comprising:
supplying butene, oxygen, nitrogen, and steam to a reactor filled with a metal oxide catalyst containing more than 92% by weight and 99.9 by weight or less of a spinel ferrite (AFe 2 O 4 ) where A is at least one metal selected from among Cu, Ti, V, Cr, K, Al, Zr, Cs, CA, Be, Zn, Mg, Mn, and Co, and 0.1 by weight or more and less than 8% by weight of an alpha ferrite (α-Fe2O3), and performing an oxidative dehydrogenation reaction at a temperature of 300 to 450° C. as a reaction step;
after the reaction step, reducing the temperature of the reactor via a two-step process to prevent catalyst deactivation, by either:
1) cooling the reactor by:
(a) maintaining supply of the butene, oxygen, nitrogen, and steam within a range within which a flow rate change of each of the butene, oxygen, nitrogen, and steam is less than ±40%, and cooling the reactor to a temperature in a range of 200° C. or lower and higher than 70° C. as a first cooling step, and
(b) after the first cooling step, stopping supply of at least the butene, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step; or

2) cooling the reactor by:
(c) stopping supply of the butene while supply of the oxygen, nitrogen, and steam is maintained, and cooling the reactor to a temperature in a range of 200° C. or lower and higher than 70° C. as a first cooling step; and
(d) after the first cooling step,
(i) maintaining supply of the oxygen, nitrogen, and steam, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step, or
(ii) stopping supply of the oxygen, nitrogen, and/or steam, and cooling the reactor to a temperature of 70° C. or lower as a second cooling step.

14. The method according to claim 1 , wherein, in the second cooling step (b), either supply of the butene and steam is stopped, or supply of the butene, oxygen, nitrogen, and steam is stopped.

15. The method according to claim 13 , wherein, in the first cooling step, the reactor is cooled to a temperature of 200° C. to 100° C.

16. The method according to claim 13 , wherein an atomic ratio of iron (Fe) to at least one metal (A) in the metal oxide catalyst is from 1.5:1 to 4:1.

17. The method according to claim 13 , wherein a molar ratio of butene: oxygen: nitrogen: steam supplied to the reactor is 1:0.1 to 2:1 to 10:1 to 30.

18. The method according to claim 13 , wherein, in the oxidative dehydrogenation reaction, gas hourly space velocity (GHSV) is 20 to 150 h −1 .

19. The method according to claim 13 , wherein, in the second cooling step, the reactor is cooled to a temperature of 70 to 30° C.

Assignees

• Lg Chemical Ltd

Inventors

• Suh Myung Ji
• Ko Dong Hyun
• Kang Jun Han
• Cha Kyong Yong
• Hwang Ye Seul
• Han Jun Kyu
• Han Sang Jin

Classifications

• C07C11/16

  with four carbon atoms · CPC title

• C07C7/20

  Use of additives, e.g. for stabilisation · CPC title

• C07C2/76 Primary

  by condensation of hydrocarbons with partial elimination of hydrogen · CPC title

• B01J23/862

  Iron and chromium · CPC title

• B01J23/8472

  Vanadium · CPC title