Method for producing butadiene through oxidative dehydrogenation reaction

Patent metadata

Field	Value
Publication number	US-2016326071-A1
Application number	US-201515110666-A
Country	US
Kind code	A1
Filing date	Jun 9, 2015
Priority date	Jun 11, 2014
Publication date	Nov 10, 2016
Grant date	—

Abstract

The present invention relates to a method for producing butadiene through an oxidative dehydrogenation reaction, the method including steps of a) introducing a first stream which includes C4 fraction, steam, oxygen (O 2 ), and nitrogen (N 2 ) into a reactor which is filled with catalyst to perform oxidative dehydrogenation reaction; b) selectively absorbing butadiene, which is obtained from the reactor, into an absorption solvent, and separating and removing C4 mixture other than the dutadiene and light gas product; and c) recovering and purifying the butadiene. Through integration of the gas separating and purifying steps by using the single absorption solvent during production of butadiene, equipment costs and operating costs accruing from repeated introduction and removal of solvent are reduced, thereby ensuring economic competitiveness of the process.

First claim

1 . A method for producing butadiene through an oxidative dehydrogenation reaction, the method comprising:
a) a step for introducing a first stream which includes C4 fraction, steam, oxygen (O 2 ), and nitrogen (N 2 ) into a reactor which is filled with catalyst to perform an oxidative dehydrogenation reaction; b) a step for selectively absorbing butadiene into an absorption solvent from a reactant which is obtained from the reactor, and separating and removing C4 mixture other than the butadiene and light gas product; and c) a step for recovering and purifying the butadiene.

2 . The method of claim 1 , further comprising:
d) a step for recycling and reintroducing into the reactor a second stream which includes one or more selected from the group consisting of C4 mixture other than the butadiene; and nitrogen and carbon dioxide (CO 2 ) which are among the light gas product which is separated in the step b), and discharging a third stream which includes a purge to the outside of the system.

3 . The method of claim 1 , wherein the absorption solvent is a polar aprotic solvent.

4 . The method of claim 1 , wherein the absorption solvent is one selected from the group consisting of dimethylformamide (DMF), methylpyrrolidone (NMP), acetonitrile (ACN), dimethylacetamide (DMA), and dimethyl sulfoxide (DMSO), or a mixture of at least two thereof.

5 . The method of claim 1 , wherein the C4 fraction is a single compound or a mixture, which includes one or more selected from the group consisting of n-butane, trans-2-butene, cis-2-butene, and 1-butene.

Assignees

• Lg Chemical Ltd

Inventors

• Kim Mi Kyung
• Lee Jeong Seok
• Lee Jae Ik
• Kim Dae Hyeon
• Lee Jong Ku

Classifications

• C07C2523/31

  combined with bismuth · CPC title

• C07C5/48

  with oxygen as an acceptor · CPC title

• C07C2523/18

  Arsenic, antimony or bismuth · CPC title

• C07C2523/28

  Molybdenum · CPC title

• C07C7/11 Primary

  by absorption, i.e. purification or separation of gaseous hydrocarbons with the aid of liquids · CPC title