Thermally integrated distillation systems and processes using the same

Patent metadata

Field	Value
Publication number	US-10399004-B2
Application number	US-201615259796-A
Country	US
Kind code	B2
Filing date	Sep 8, 2016
Priority date	Sep 8, 2016
Publication date	Sep 3, 2019
Grant date	Sep 3, 2019

Abstract

Processes and systems for separating a mixture of three or more chemical components into multiple product streams each enriched in one of the components are provided herein. In some aspects, the present invention relates to processes for the separation of a chemical mixture including at least a heavy key component, an intermediate key component, and a light key component to form a product stream enriched in the light key component, a product stream enriched in the intermediate key component, and a product stream enriched in the heavy key component. Systems described herein may include one or more thermally coupled distillation columns including, for example, a dividing wall column, or a plurality of distillation columns arranged in a thermally integrated configuration.

First claim

The invention claimed is:

1. A method for separating a ternary mixture comprising a light key component, a heavy key component, and at least one intermediate key component, wherein said mixture has a distillation boundary on a distillation region diagram that intersects a heterogeneous, minimum boiling binary azeotrope between said intermediate key component and said heavy key component that has a higher boiling point than the light key component, said method comprising:
(a) introducing a feed stream comprising said mixture into a thermally integrated distillation system comprising a rectification zone, a first stripping zone, a second stripping zone, and a decantation zone;
(b) withdrawing first and second overhead vapor streams from said first and said second stripping zones respectively;
(c) introducing said first and said second overhead vapor streams into said rectification zone;
(d) withdrawing a rectification liquid stream from said rectification zone;
(e) introducing said rectification liquid stream into said decantation zone;
(f) separating said rectification liquid stream in said decantation zone into a first liquid phase enriched in said heavy key component and a second liquid phase enriched in said intermediate key component, wherein said first and said second liquid phases have compositions that are in different distillation regions of said distillation region diagram;
(g) introducing a first liquid stream comprising at least a portion of said first liquid phase into one of said first stripping zone and said second stripping zone;
(h) introducing a second liquid stream comprising at least a portion of said second liquid phase into the other of said first stripping zone and said second stripping zone;
(i) recovering a first bottoms product stream enriched in said heavy key component from said first stripping zone;
(j) recovering a second bottoms product stream enriched in said intermediate key component from said second stripping zone; and
(k) recovering a first overhead product stream enriched in said light key component from said rectification zone.

2. The method of claim 1 , wherein said introducing of step (a) includes feeding said feed stream into said first stripping zone, said second stripping zone, said rectification zone, and/or said decantation zone.

3. The method of claim 1 , wherein said introducing of step (a) includes feeding said feed stream into said first stripping zone, and wherein said feed stream has a composition in a distillation region of said distillation region diagram that contains a heavy key component vertex.

4. The method of claim 1 , wherein said introducing of step (a) includes feeding said feed stream into said second stripping zone and wherein said feed stream has a composition in a distillation region of said distillation region diagram that contains an intermediate key component vertex.

5. The method of claim 1 , wherein said introducing of step (a) includes feeding said feed stream into said rectification zone, and wherein said feed stream has a higher concentration of said light key component than of said intermediate key component or said heavy key component.

6. The method of claim 1 , wherein said introducing of step (a) includes feeding said feed stream into said decantation zone, wherein said separating of step (f) further comprises separating said feed stream to form said first liquid phase and said second liquid phase.

7. The method of claim 1 , wherein said light key component and said intermediate key component form a minimum boiling binary azeotrope.

8. The method of claim 1 , wherein said light key component and said heavy key component forms a minimum boiling binary azeotrope.

9. The method of claim 1 , wherein said distillation boundary intersects a light key component vertex of said distillation region diagram.

10. The method of claim 1 , wherein said mixture further comprises one or more components having a higher volatility than said light key component, one or more components having a lower volatility than said heavy key component, and/or one or more additional intermediate components.

11. The method of claim 1 , wherein said thermally integrated distillation system comprises a dividing wall distillation column, wherein said rectification zone is located within an upper portion of an internal volume of said dividing wall distillation column, wherein said first stripping zone and said second stripping zone are located within a lower portion of said internal volume of said dividing wall distillation column, and wherein said first and said second stripping zones are separated by a dividing wall.

12. The method of claim 11 , wherein said decantation zone is located within said internal volume of said dividing wall distillation column between said rectification zone and said first and said second stripping zones.

13. The method of claim 11 , wherein said decantation zone is located outside said internal volume of said dividing wall distillation column.

14. The method of claim 1 , wherein said thermally integrated distillation system comprises a first distillation column, a second distillation column, and a third distillation column, wherein said rectification zone, said first stripping zone, and said second stripping zone are respectively defined within said first, said second, and said third distillation columns, and wherein said decantation zone is located outside each of said first, said second, and said third distillation columns.

15. The method of claim 1 , wherein said mixture comprises at least one of the following groups of components selected from the group consisting of (i) through (x) below:
(i) n-butylamine/water/n-butanol/dibutylamine/tributylamine;
(ii) n-butyraldehyde/water/2-ethylhexenal;
(iii) propionaldehyde/water/2-methylpentenal;
(iv) propionaldehyde/n-butyraldehyde/water;
(v) acetone/water/n-butanol;
(vi) acetone/ethanol/water/n-butanol;
(vii) methanol/methacrolein/water;
(viii) methanol/water/methyl methacrylate;
(ix) acetone/water/ketone; and
(x) methanol/water/xylene/dimethyterephthalate.

Assignees

• Eastman Chem Co

Inventors

• Hoyme Craig Alan
• Huss Robert Scott

Classifications

• C07C67/54

  by distillation · CPC title

• C07C45/84

  by azeotropic distillation · CPC title

• B01D3/141

  where at least one distillation column contains at least one dividing wall · CPC title

• C07C7/06

  by azeotropic distillation · CPC title

• B01D3/143 Primary

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