Process for obtaining isobutene from a C4-hydrocarbon mixture

Patent metadata

Field	Value
Publication number	US-12448342-B2
Application number	US-202218280686-A
Country	US
Kind code	B2
Filing date	Mar 1, 2022
Priority date	Mar 8, 2021
Publication date	Oct 21, 2025
Grant date	Oct 21, 2025

Abstract

The invention relates to a process for obtaining isobutene from an isobutene containing C4-hydrocarbon mixture ( 1 ) in a plant comprising an etherification unit ( 3 ), a first distillation unit ( 5 ), an ether cleavage unit ( 10 ) and a second distillation unit ( 12 ), the process comprising: (a) contacting the C4-hydrocarbon mixture ( 1 ) with a primary alcohol ( 2 ) and reacting the mixture with the primary alcohol in the presence of an acidic catalyst to form the corresponding alkyl tert-butyl ether in the etherification unit ( 3 ); (b) distilling the reaction mixture ( 4 ) from the etherification unit ( 3 ) in the first distillation unit ( 5 ), a C4-hydrocarbon raffinate being withdrawn as the overhead product ( 6 ), and the alkyl tert-butyl ether being withdrawn as the bottom product ( 7 ); (c) vaporizing the bottom product from the first distillation unit ( 5 ) in an evaporator ( 8 ) obtaining a vapor stream ( 9 ); (d) reacting the vapor stream ( 9 ) of step (c) in the presence of an acidic catalyst obtaining isobutene and the primary alcohol as reaction products in the ether cleavage unit ( 10 ); (e) distilling the reaction mixture ( 11 ) from the ether cleavage unit ( 10 ) in the second distillation unit ( 12 ), isobutene being withdrawn as the overhead product ( 13 ), the primary alcohol and diisobutene being withdrawn as the bottom product ( 14 ) and being recycled to the etherification unit ( 3 ); wherein a purge stream ( 15 ) containing high boiling components with a normal boiling point higher than that of the alkyl tert-butyl ether is withdrawn from the evaporator ( 8 ) in step (c).

First claim

The invention claimed is:

1. A process for obtaining isobutene from an isobutene containing C4-hydrocarbon mixture in a plant comprising an etherification unit, a first distillation unit, an ether cleavage unit and a second distillation unit, the process comprising:
(a) contacting the C4-hydrocarbon mixture with a primary alcohol and reacting the C4-hydrocarbon mixture with the primary alcohol forming a reaction mixture in the presence of an acidic catalyst to form the corresponding alkyl tert-butyl ether in the etherification unit;
(b) distilling the reaction mixture from the etherification unit in the first distillation unit, a C4-hydrocarbon raffinate being withdrawn as an overhead product from the first distillation unit, and the alkyl tert-butyl ether being withdrawn as a bottom product from the first distillation unit;
vaporizing the bottom product from the first distillation unit in an evaporator obtaining a vapor stream;

(c) reacting the vapor stream of step (c) in the presence of an acidic catalyst obtaining a mixture comprising isobutene and the primary alcohol in the ether cleavage unit;
(d) distilling the mixture comprising isobutene and the primary alcohol from the ether cleavage unit in the second distillation unit, isobutene being withdrawn as an overhead product from the second distillation unit, the primary alcohol being withdrawn as a bottom product from the second distillation unit and being recycled to the etherification unit;
characterized in that a purge stream containing high boiling components with a normal boiling point higher than that of the alkyl tert-butyl ether is withdrawn from the evaporator in step (c).

2. The process according to claim 1 , wherein the plant further comprises a byproduct separation unit being fed by a part of the bottom product of the second distillation unit, wherein an alcohol product stream rich in the primary alcohol is separated from the part of the bottom product of the second distillation unit.

3. The process according to claim 2 , wherein the primary alcohol obtained from the part of the bottom product of the second distillation unit is recycled to the etherification unit.

4. The process according to claim 2 , wherein the purge stream from the evaporator in step (c) is fed to the byproduct separation unit.

5. The process according to claim 2 , wherein alkyl tert-butyl ether contained in the bottom product stream from the second distillation unit is separated in the byproduct purification unit and is recycled to the evaporator of step (c) for evaporation and/or to the ether cleavage unit.

6. The process according to claim 2 , wherein the bottom product of the second distillation unit fed to the byproduct separation unit is split up in at least three byproduct streams wherein a first byproduct stream is rich in diisobutene, a second byproduct stream is the alcohol product stream rich in the primary alcohol, and a third byproduct stream is rich in components with a normal boiling point higher than 110° C.

7. The process according to claim 6 , wherein the first byproduct stream is further split up in at least two further byproduct streams wherein a fourth byproduct stream is rich in diisobutene and a fifth byproduct stream is rich in alkyl tert-butyl ether.

8. The process according to claim 7 , wherein the mass fraction of diisobutene in the first byproduct stream ( 18 ) is at least 30 wt.-% and the mass fraction of diisobutene in the fourth byproduct stream ( 21 ) is at least 90 wt.-%.

9. The process according to claim 7 , wherein the fifth byproduct stream is at least partly recycled to the evaporator for evaporation and/or to the ether cleavage unit.

10. The process according to claim 2 , wherein the mass fraction of the primary alcohol in the alcohol product stream is at least 90 wt.-%.

11. The process according to claim 1 , wherein the first distillation unit comprises a distillation column, the bottom product being withdrawn as a side stream from the distillation column at a stage below the feed stage, and a purge stream rich in high-boiling components being withdrawn from the sump of the distillation column.

12. The process according to claim 11 , wherein the purge stream from the sump of the distillation column in the first distillation unit is fed to the byproduct separation unit.

13. The process according to claim 1 , wherein the evaporator is a natural circulation evaporator, particularly a Robert type evaporator, and wherein the purge stream is withdrawn from the liquid phase in the bottom of the evaporator.

14. The process according to claim 1 , wherein the primary alcohol is isobutanol, and the alkyl tert-butyl ether is isobutyl tert-butyl ether (IBTBE).

Assignees

• Basf Se

Inventors

• Thotla Suman
• Wagner Hans-Guenter
• Hugo Randolf
• Waters Gerrit
• Huebner Michael
• Neudert Markus
• Roussiere Thomas

Classifications

• C07C1/22

  by reduction · CPC title

• B01D3/143 Primary

  by two or more of a fractionation, separation or rectification step · CPC title

• C07C31/12

  containing four carbon atoms · CPC title

• C07C29/80

  by distillation · CPC title

• C07C29/10

  of ethers, including cyclic ethers, e.g. oxiranes · CPC title