Process for the separation of glycols

Patent metadata

Field	Value
Publication number	US-10035744-B2
Application number	US-201515524276-A
Country	US
Kind code	B2
Filing date	Nov 4, 2015
Priority date	Nov 6, 2014
Publication date	Jul 31, 2018
Grant date	Jul 31, 2018

Abstract

The invention provides a process for the separation of MEG and 1,2-BDO from a first mixture comprising MEG and 1,2-BDO in a first solvent by the steps of: (i) combining said first mixture with a second solvent stream comprising a second solvent in a first extraction column; (ii) recovering (a) a second mixture of MEG and 1,2-BDO in the second solvent, wherein the molar ratio of MEG:1,2-BDO is lower in the second mixture than in the first mixture; and (b) a solution comprising MEG in the first solvent; (iii) combining said second mixture with a first washing stream, said first washing stream also comprising the first solvent in a second extraction column; (iv) recovering (c) a first extract stream comprising the second solvent and 1,2-BDO and (d) a third mixture comprising MEG and, optionally, 1,2-BDO in the first solvent.

First claim

That which is claimed is:

1. A process for the separation of monoethylene glycol (MEG) and 1,2-butanediol (1,2-BDO) from a first mixture comprising MEG and 1,2-BDO in a first solvent comprising water, by the steps of:
(i) combining said first mixture with a second solvent stream comprising a second solvent comprising one or more alkyl amines in a first extraction column;
(ii) recovering (a) a second mixture of MEG and 1,2-BDO in the second solvent, wherein the molar ratio of MEG:1,2-BDO is lower in the second mixture than in the first mixture; and (b) a solution comprising MEG in the first solvent;
(iii) combining said second mixture with a first washing stream, said first washing stream also comprising the first solvent in a second extraction column;
(iv) recovering (c) a first extract stream comprising the second solvent and 1,2-BDO and (d) a third mixture comprising MEG and, optionally, 1,2-BDO in the first solvent.

2. A process according to claim 1 , wherein the third mixture comprising MEG and, optionally, 1,2-BDO in the first solvent is provided to the first extraction column as a portion of the first mixture of MEG and 1,2-BDO in the first solvent.

3. A process according to claim 1 , further comprising the step of:
(v) providing the solution comprising MEG in the first solvent as a feed stream to a third extraction column and combining it therein with a further second solvent stream comprising the second solvent; and recovering (e) a second extract stream comprising the second solvent and MEG; and (f) a first solvent stream comprising the first solvent.

4. A process according to claim 3 , wherein at least a portion of the second extract stream comprising the second solvent and MEG is provided to the first extraction column as at least a portion of the second solvent stream comprising a second solvent.

5. A process as claimed in claim 1 , wherein the first mixture comprising MEG and 1,2-BDO is derived from the reaction product stream from a process for the hydrogenolysis of a saccharide-containing feedstock.

6. A process according to claim 1 , wherein the one or more alkyl amine contains carbon and nitrogen atoms in a ratio of at most 8:1.

7. A process according to claim 1 , wherein the one or more alkyl amine contains an aliphatic cyclic group either containing the amine nitrogen or attached to the amine nitrogen.

Assignees

• Shell Oil Co

Inventors

• Huizenga Pieter
• Fischer Kai Jürgen
• De Villiers Waldo Eugene
• Bus Karin
• Veldhuizen Dorien

Classifications

• B01D11/0426

  Counter-current multistage extraction towers in a vertical or sloping position · CPC title

• B01D11/0492

  Applications, solvents used · CPC title

• B01D2011/002

  Counter-current extraction · CPC title

• C07C29/86 Primary

  by liquid-liquid treatment · CPC title