IP Library Granted Patent US 9,637,422
Granted Patent B2
US 9,637,422 · App. 14/000,095 · Granted May 2, 2017

Method for preparing high purity isobutene using glycolether

Inventors: Myeong-Seok Kim (Daejon, KR); Jae-Hoon Uhm (Daejeon, KR); Min-Sup Park (Daejeon, KR); Hyoung-Jae Seo (Daejeon, KR); Kyoung-Tae Min (Daejeon, KR)
Assignee: DAELIM INDUSTRIAL CO., LTD.
C07C1/22C07B37/06C07C1/20C07C41/06C07C2531/10Y02P20/582
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Quick Facts
Patent No.
US 9,637,422
App. No.
14/000,095
Granted
May 2, 2017
Kind
B2
Abstract

Disclosed is a method of preparing isobutene in which high-purity isobutene is separated (prepared) from a C 4 mixture by cracking glycol ether prepared from a C 4 mixture (in particular, C 4 raffinate-1) containing isobutene and a glycol. The method includes cracking glycol ether into isobutene and glycol at a temperature between 50° C. and 300° C. in the presence of a strongly acidic catalyst. The glycol ether may be prepared by reaction between a C 4 mixture containing isobutene and glycol in the presence of an acid catalyst.

Claims (11)

1. A method of preparing isobutene, comprising the sequential steps of:

a) reacting a C 4 mixture containing isobutene with glycol in the presence of an acid catalyst to provide a glycol ether, wherein said glycol ether comprises glycol di-t-butyl ether and glycol mono-t-butyl ether, and wherein an amount of glycol di-t-butyl ether is larger than an amount of glycol mono-t-butyl ether;

b) separating said glycol ether from the unreacted C 4 mixture and glycol; and

c) cracking said glycol ether into isobutene and glycol at a temperature between 50° C. and 300° C. in the presence of a strongly acidic catalyst, wherein the glycol di-t-butyl ether of said glycol ether is completely decomposed.

2. The method according to claim 1 , wherein the cracking is performed in a glycol ether cracking reactor or a reactive distillation column.

3. The method according to claim 1 , wherein the acid catalyst is a strongly acidic solid ion exchange resin containing a sulfonic acid group.

4. The method according to claim 1 , wherein the glycol is a compound represented by Formula 1 below:

wherein R 1 and R 2 are each independently a hydrogen atom or a C 1 -C 5 alkyl group, and n is an integer of 0 to 4.

5. The method according to claim 1 , wherein the cracking is continuously or non-continuously performed.

6. The method according to claim 1 , wherein the C 4 mixture of step (a) comprises isobutene in an amount of between 30 wt % and 50 wt %.

7. The method according to claim 1 , wherein a molar ratio of glycol to isobutene in step (a) is from 1:1 to 5:1.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 16, 2021
From: DAELIM INDUSTRIAL CO., LTD.
To: DL CHEMICAL CO., LTD.
Reel/Frame 057189/0449 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 21, 2013
From: KIM, MYEONG-SEOK; UHM, JAE-HOON; PARK, MIN-SUP; SEO, HYOUNG-JAE; MIN, KYOUNG-TAE
To: DAELIM INDUSTRIAL CO., LTD.
Reel/Frame 031074/0924 →
Priority Claims (1)
KR 10-2011-0014521 · Feb 18, 2011 · national
Continuity (1)
Related Publication 20130324781A1 · Dec 5, 2013