IP Library Granted Patent US 10,427,994
Granted Patent B2
US 10,427,994 · App. 15/505,593 · Granted Oct 1, 2019

Separation process for C8 aromatics mixture

Inventors: Attapong Thirasak (Bangkok Methropolis, TH); Alisa Kammafoo (Bangkok Methropolis, TH); Wiroon Tanthapanichakoon (Bangkok Methropolis, TH); Zhongyi Ding (Katy, TX); Sachin Joshi (Katy, TX); Arnat Prombunglum (Bangkok Methropolis, TH); Worawut Tamthaisong (Bangkok Methropolis, TH); Purachet Pitipuech (Bangkok Methropolis, TH)
Assignees: SCG CHEMICALS CO., LTD.; GTC TECHNOLOGY US, LLC
C07C7/08B01D3/36B01D3/38B01D3/40C07C7/06
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Quick Facts
Patent No.
US 10,427,994
App. No.
15/505,593
Granted
Oct 1, 2019
Kind
B2
Abstract

Process for the distillative separation of ethylbenzene from a mixture comprising ethylbenzene and at least one other C8 aromatic compound, comprising distilling said mixture in a distillation column in the presence of an extractive solvent, characterized in that the distillation column is operated at a sub-atmospheric pressure.

Claims (22)

1. A process for the distillative separation of ethylbenzene from a mixture comprising ethylbenzene and at least one other C8 aromatic compound, the process comprising:

adding at least one solvent to a distillation column, the at least one solvent including one or more of chloroform, carbon tetrachloride, dimethylamine, diethylamine, acetonitrile, acetaldehyde, 1-propanal, methyl isopropyl ketone, 3-methyl-2-pentanone, 3,3-dimethyl-2-butanone, 2-pentanone, 2-methylpropanal, 1-butanal, cyclopentanone, acetone, or ethanol;

adding one or more of water or steam to the distillation column; and

distilling said mixture in the distillation column in the presence of an extractive solvent, the at least one solvent, the one or more of water or steam, and at a sub-atmospheric pressure.

2. The process according to claim 1 wherein the extractive solvent has a boiling point above 150° C.

3. The process according to claim 1 wherein the extractive solvent comprises an organic compound selected from the group consisting of Cl-containing compounds, S-containing compounds, N-containing compounds, O-containing compounds, and mixtures thereof.

4. The process according to claim 3 wherein the extractive solvent includes at least one Cl-containing compound is selected from the group consisting of 2,4-dichlorobenzene, 1,2,3-trichlorobenzene, 1,2,4-trichlorobenzene, 1,2,4,5-tetrachlorobenzene, polychlorobenzenes, benzene hexachloride, 2,3,4,6-tetrachlorophenol, and 1,2,3-trichloropropane.

5. The process according to claim 3 , wherein the extractive solvent includes at least one S-containing compound selected from the group consisting of dimethylsulfoxide, sulfolane, methyl sulfolane, and mixtures thereof.

6. The process according to claim 3 , wherein the extractive solvent includes at least one N-containing compound selected from the group consisting of N-formylmorpholine, aniline, 2-pyrrolidinone, quinolone, n-methyl-2-pyrrolidone, n-methylaniline, benzonitrile, nitrobenzene, and mixtures thereof.

7. The process according to claim 3 , wherein the extractive solvent includes at least one O-containing compound is selected from the group consisting of methyl salicylate, methylbenzoate, n-methyl-2-pyrrolidone, 1,2-propanediol, 1,2-butanediol, 1,3-butanediol, benzaldehyde, phenol, tetrahydrofurfuryl alcohol, diethyl maleate, ethyl acetoacetate, 4-methoxy acetophenone, isophorone, 5-methyl-2-hexanone, 2-heptanone, cyclohexanone, 2-octanone, 2-nonanone, 3-heptanone, diisobutylketone, 5-nonanone, benzyl alcohol, and mixtures thereof.

8. The process according to claim 1 wherein the sub-atmospheric pressure is in a range of 10 to 900 mbar.

9. The process according to claim 8 wherein the sub-atmospheric pressure is in the range from 50 to 600 mbar.

10. The process according to claim 1 , wherein the distillation column is operated at temperature in the range of 50 to 250° C.

11. The process according to claim 1 wherein the mass ratio of the extractive solvent to the mixture comprising ethylbenzene and the at least one other C 8 aromatic compound is in the range of 1:1 to 10:1.

12. The process according to claim 1 wherein the at least one other C 8 aromatic compound comprises a compound selected from the group consisting of p-xylene, m-xylene, o-xylene, and mixtures thereof.

13. The process according to claim 1 , wherein the water and/or steam is added in an amount of 0.1 to 25 wt % based on mass flow of the extractive solvent used.

14. A process for the distillative separation of ethylbenzene from a mixture comprising ethylbenzene and at least one other C 8 aromatic compound, the process comprising:

adding at least one solvent to a distillation column, the at least one solvent including one or more of chloroform, carbon tetrachloride, dimethylamine, diethylamine, acetonitrile, acetaldehyde, 1-propanal, methyl isopropyl ketone, 3-methyl-2-pentanone, 3,3-dimethyl-2-butanone, 2-pentanone, 2-methylpropanal, 1-butanal, cyclopentanone, acetone, or ethanol;

adding one or more of water or steam to the distillation column; and

distilling said mixture in the distillation column in the presence of an extractive solvent, the at least one solvent, and the one or more of water or steam, at a sub-atmospheric pressure and a temperature in the range of 50 to 250° C.;

wherein the extractive solvent comprises an organic compound selected from the group consisting of 2,4-dichlorobenzene, 1,2,3-trichlorobenzene, 1,2,4-trichlorobenzene, 1,2,4,5-tetrachlorobenzene, polychlorobenzenes, benzene hexachloride, 2,3,4,6-tetrachlorophenol, and 1,2,3-trichloropropane.

15. The method of claim 14 , wherein the sub-atmospheric pressure is in a range of 10 to 900 mbar.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 6, 2021
From: SULZER GTC TECHNOLOGY US INC.
To: SULZER MANAGEMENT AG
Reel/Frame 055835/0708 →
CHANGE OF NAME Recorded Mar 15, 2021
From: GTC TECHNOLOGY US, LLC
To: SULZER GTC TECHNOLOGY US INC.
Reel/Frame 055626/0599 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 18, 2017
From: THIRASAK, ATTAPONG; KAMMAFOO, ALISA; TANTHAPANICHAKOON, WIROON; DING, ZHONGYI; JOSHI, SACHIN; PROMBUNGLUM, ARNAT; TAMTHAISONG, WORAWUT; PITIPUECH, PURACHET
To: SCG CHEMICALS CO., LTD.; GTC TECHNOLOGY US, LLC
Reel/Frame 042427/0371 →
Continuity (1)
Related Publication 20170240489A1 · Aug 24, 2017
Cited By (1)
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