Method for producing butadiene

Patent metadata

Field	Value
Publication number	US-11447435-B2
Application number	US-201917050031-A
Country	US
Kind code	B2
Filing date	Jul 10, 2019
Priority date	Nov 30, 2018
Publication date	Sep 20, 2022
Grant date	Sep 20, 2022

Abstract

An exemplary embodiment of the present application provides a method for preparing butadiene, the method comprising a process of performing an oxidative dehydrogenation reaction by introducing a reactant comprising butene, oxygen, nitrogen, and steam into a reactor which is filled with a catalyst, in which during a first start-up of the oxidative dehydrogenation reaction, the oxygen is introduced into the reactor before the butene, or the oxygen is introduced into the reactor simultaneously with the butene.

First claim

The invention claimed is:

1. A method for producing butadiene, the method comprising performing an oxidative dehydrogenation reaction step by introducing a reactant comprising butene, oxygen, nitrogen, and steam into a reactor which is filled with a catalyst,
wherein during a first start-up of the oxidative dehydrogenation reaction:
(1) oxygen and nitrogen are first simultaneously introduced into the reactor, and then steam is introduced into the reactor, and then butene is finally introduced into the reactor; or
(2) nitrogen and steam are first simultaneously introduced into the reactor, then oxygen and butene are simultaneously introduced into the reactor; or
(3) steam and oxygen are first simultaneously introduced into the reactor, then nitrogen is introduced into the reactor, and then butene is finally introduced into the reactor;
wherein when at least a part of the reactant comprising butene, oxygen, nitrogen, and steam is stopped from being supplied, the oxidative dehydrogenation reaction is stopped and a purge process is performed by introducing one or more of air and steam into the reactor where the temperature during the oxidative dehydrogenation reaction is maintained at the time of the purge process.

2. The method of claim 1 , wherein the steam is wastewater distillation steam recycled from a product obtained from the oxidative dehydrogenation reaction, and
the wastewater distillation steam is introduced into the reactor simultaneously with oxygen in step (3) during the first start-up.

3. The method of claim 1 , wherein the steam to be introduced into the reactor during the purge process is wastewater distillation steam recycled from a product obtained from the oxidative dehydrogenation reaction, and
the wastewater distillation steam is introduced into the reactor simultaneously with oxygen during the purge process.

4. The method of claim 1 , wherein during a restart of the oxidative dehydrogenation reaction after the purge process is completed, the reactant comprising butene, oxygen, nitrogen, and steam is introduced into the reactor in the same manner as during the first start-up.

5. The method of claim 1 , wherein the oxidative dehydrogenation reaction is performed at a temperature of 250° C. to 500° C., and
when the oxygen in the reactant comprising the butene, the oxygen, the nitrogen, and the steam is stopped from being supplied to the reactor, the method comprises cooling the temperature of the reactor to 300° C. or less prior to the purge process.

6. The method of claim 1 , wherein the oxidative dehydrogenation reaction process is performed using two reactors including a first reactor and a second reactor connected in series, and
the reactant comprising butene, oxygen, nitrogen, and steam is introduced into the first reactor.

7. The method of claim 6 , wherein the butene comprises a C4 mixture, and the C4 mixture and oxygen are introduced into the first reactor at a molar ratio of the C4 mixture: oxygen of 1:0.4 to 1.0.

8. The method of claim 7 , wherein oxygen with a molar ratio of 0.1 to 0.45 based on 1 mole of the C4 mixture to be introduced into the first reactor is further introduced into the second reactor.

9. The method of claim 6 , wherein the first reactor and the second reactor each independently comprise one or more of a bismuth-molybdenum-based catalyst and a ferrite-based catalyst.

10. The method of claim 9 , wherein the ferrite-based catalyst is represented by the following Formula 1:
[Formula 1]
AFe 2 O 4
in Formula 1, A is Cu, Ra, Ba, Sr, Ca, Cu, Be, Zn, Mg, Mn, Co, or Ni.

11. The method of claim 9 , wherein the bismuth-molybdenum-based catalyst is represented by the following Formula 2:
[Formula 2]
Mo a Bi b C c D d E e O f
in Formula 2,
C is one or more of trivalent cation metal components,
D is one or more of divalent cation metal components,
E is one or more of monovalent cation metal components, and
when a is 12, b is 0.01 to 2, c is 0.001 to 2, d is 5 to 12, e is 0 to 1.5, and f is a value determined to match the valence by the other components.

Assignees

• Lg Chemical Ltd

Inventors

• Suh Myungji
• Kang Jun Han
• Cha Kyong Yong
• Ko Dong Hyun

Classifications

• B01J23/31

  combined with bismuth · CPC title

• B01J37/038

  to form slurries or suspensions, e.g. a washcoat · CPC title

• B01J21/04 Primary

  Alumina · CPC title

• B01J2219/0004

  Processes in series · CPC title

• B01J2523/68

  Molybdenum · CPC title