Method and apparatus for separating alkyl aromatic hydrocarbon

Patent metadata

Field	Value
Publication number	US-9896397-B2
Application number	US-201314411289-A
Country	US
Kind code	B2
Filing date	Jun 25, 2013
Priority date	Jun 29, 2012
Publication date	Feb 20, 2018
Grant date	Feb 20, 2018

Abstract

A method for separating an alkyl aromatic hydrocarbon, the method having a step of adding a first diluent and an extractant having a superacid to a mixture comprising the alkyl aromatic hydrocarbon and one or more isomers thereof to carry out an acid-base extraction to thereby form a complex of the alkyl aromatic hydrocarbon with the superacid, and thereafter separating the complex from the mixture, and a step of adding an eliminating agent having a relative basicity in a range of 0.06 to 10 with respect to the alkyl aromatic hydrocarbon and a second diluent to the complex, and carrying out complex exchange of the alkyl aromatic hydrocarbon for the eliminating agent to thereby separate the alkyl aromatic hydrocarbon from the complex.

First claim

The invention claimed is:

1. A method for separating an alkyl aromatic hydrocarbon comprising:
adding a first diluent and an extractant comprising a superacid to a mixture comprising the alkyl aromatic hydrocarbon and one or more isomers thereof to carry out an acid-base extraction to thereby form a complex of the alkyl aromatic hydrocarbon with the superacid, and thereafter separating the complex from the mixture; and
adding an eliminating agent having a relative basicity in a range of 0.06 to 10 with respect to the alkyl aromatic hydrocarbon and a second diluent to the complex, and carrying out a complex exchange of the alkyl aromatic hydrocarbon for the eliminating agent to thereby separate the alkyl aromatic hydrocarbon from the complex.

2. The method according to claim 1 , further comprising adding as the extractant a complex of the eliminating agent with the superacid formed by the complex exchange together with the second diluent to the mixture to thereby recycle the complex.

3. The method according to claim 1 , comprising adding an eliminating agent having the relative basicity in a range of 0.1 to 2.0 with respect to the alkyl aromatic hydrocarbon and the second diluent to the complex to carry out a complex exchange of the alkyl aromatic hydrocarbon for the eliminating agent to thereby separate the alkyl aromatic hydrocarbon from the complex.

4. The method according to claim 1 , wherein the mixture comprising the alkyl aromatic hydrocarbon and one or more isomers thereof is C8 alkylbenzenes, C9 alkylbenzenes or C10 alkylbenzenes.

5. The method according to claim 4 , wherein the mixture comprising the alkyl aromatic hydrocarbon and one or more isomers thereof is C8 alkylbenzenes, and the alkyl aromatic hydrocarbon is m-xylene.

6. The method according to claim 1 , wherein the superacid is a mixed superacid of a Bronsted acid and a Lewis acid.

7. The method according to claim 6 , wherein the complex of the eliminating agent with the superacid is added in such an amount that (the number of moles of the alkyl aromatic hydrocarbon in the mixture)/(the number of moles of the Lewis acid in the complex) is in a range of 0.5 to 1.5.

8. The method according to claim 6 , wherein the first diluent is added in such an amount that (the volume of the first diluent)/(the number of moles of the Lewis acid in the superacid) is in a range of 50 mL/mol to 500 mL/mol.

9. The method according to claim 6 , wherein the eliminating agent is added in an amount in a range of 1 to 15 in molar ratio with respect to the Lewis acid in the complex of the alkyl aromatic hydrocarbon with the superacid.

10. The method according to claim 1 , wherein an amount of the second diluent with respect to the eliminating agent is in a range of 0.001 to 1 in terms of mass.

11. The method according to claim 1 , wherein the eliminating agent has a boiling point of 145° C. to 400° C.

12. The method according to claim 6 , wherein the Lewis acid is at least one selected from the group consisting of boron trifluoride, tantalum pentafluoride, niobium pentafluoride, titanium tetrafluoride, phosphorus pentafluoride, antimony pentafluoride and tungsten hexafluoride.

13. The method according to claim 6 , wherein the Bronsted acid is hydrogen fluoride, and the Lewis acid is boron trifluoride.

14. The method according to claim 1 , wherein the first and/or second diluent is an aliphatic saturated hydrocarbon and/or an alicyclic saturated hydrocarbon.

15. The method according to claim 1 , wherein the first and/or second diluent is at least one selected from the group consisting of isohexane, 3-methylpentane, 2-methylhexane, 2-ethylhexane, decalin, tetrahydrodicyclopentadiene, ethylcyclohexane, methylcyclohexane and methylcyclopentane.

16. The method according to claim 6 , wherein a proportion of the Bronsted acid with respect to the Lewis acid in the superacid is in a range of 5 to 20 in molar ratio.

Assignees

• Mitsubishi Gas Chemical Co

Inventors

• Nishiuchi Junya
• Nagao Shinichi
• Tanaka Yoshitaka
• Kitamura Mitsuharu
• Oka Hiroaki

Classifications

• B01D11/04

  of solutions which are liquid · CPC title

• C07C7/152

  by forming adducts or complexes · CPC title

• C07C7/10 Primary

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

• B01D11/043

  with stationary contacting elements, sieve plates or loose contacting elements · CPC title

• C07C7/04

  by distillation · CPC title