Reducing energy consumption in MEG reclamation

Patent metadata

Field	Value
Publication number	US-12378177-B2
Application number	US-202017756449-A
Country	US
Kind code	B2
Filing date	Dec 1, 2020
Priority date	Dec 2, 2019
Publication date	Aug 5, 2025
Grant date	Aug 5, 2025

Abstract

A method is described herein, comprising vaporizing a glycol material by thermal contact with a heating medium to form a vaporized glycol stream, increasing a pressure of the vaporized glycol stream to form a pressurized glycol stream, and increasing a temperature of the heating medium by thermally contacting the heating medium with the pressurized glycol stream.

First claim

What is claimed is:

1. A method, comprising:
vaporizing, in a vaporizer, a first liquid via heat transfer from a second liquid to form a vaporized stream that exits the vaporizer, the vaporized stream including monoethylene glycol (MEG);
increasing a pressure of at least a portion of the vaporized stream to form a pressurized vapor stream;
withdrawing a portion of the second liquid from the vaporizer;
increasing a temperature of the portion of the second liquid by transferring heat from the pressurized vapor stream to the portion of the second liquid without mixing the pressurized vapor stream with the portion of the second liquid; and
returning the portion of the second liquid to the vaporizer after the increasing of the temperature of the portion of the second liquid.

2. The method of claim 1 , wherein the heat is transferred from the pressurized vapor stream to the portion of the second liquid via a thermal contactor, and at least a portion of the pressurized vapor stream condenses in the thermal contactor during the transfer of the heat.

3. The method of claim 1 , wherein the at least a portion of the vaporized stream is a distillation overhead stream.

4. The method of claim 1 , wherein the increasing the pressure of the at least a portion of the vaporized stream includes:
treating the vaporized stream to form a treated stream; and
compressing the treated stream.

5. The method of claim 4 , wherein treating the vaporized stream includes distilling the vaporized stream, wherein the treated stream is an overhead stream of the distillation.

6. A method, comprising:
vaporizing, in a vaporizer, a first liquid via heat transfer from a second liquid to form a vaporized stream that exits the vaporizer, the vaporized stream including monoethylene glycol (MEG);
increasing a pressure of the vaporized stream to form a pressurized vapor stream;
withdrawing a portion of the second liquid from the vaporizer, wherein the pressurized vapor stream has a dew point temperature higher than the portion of the second liquid;
increasing a temperature of the portion of the second liquid by transferring heat from the pressurized vapor stream to the portion of the second liquid in a thermal contactor without mixing the pressurized vapor stream with the portion of the second liquid, such that at least a portion of the pressurized vapor stream condenses in the thermal contactor; and
returning the portion of the second liquid to the vaporizer after the increasing of the temperature of the portion of the second liquid.

7. The method of claim 6 , wherein increasing the pressure of the vaporized stream includes:
treating the vaporized stream to form a treated stream; and
compressing the treated stream.

8. The method of claim 7 , wherein treating the vaporized stream includes distilling the vaporized stream, wherein the treated stream is an overhead stream of the distillation.

9. The method of claim 6 , further comprising adjusting a temperature of the pressurized vapor stream prior to transferring the heat from the pressurized vapor stream to the portion of the second liquid.

10. The method of claim 9 , wherein adjusting the temperature of the pressurized vapor stream includes heating the pressurized vapor stream.

11. The method of claim 10 , wherein heating the pressurized vapor stream includes vaporizing condensate formed by the increasing the pressure of the vaporized stream to form the pressurized vapor stream.

12. The method of claim 6 , wherein the first liquid and the vaporized stream include water and MEG, and wherein increasing the pressure of the vaporized stream to form a pressurized vapor stream includes:
distilling the vaporized stream to form a purified MEG stream; and
increasing a pressure of the purified MEG stream to form the pressurized vapor stream.

13. The method of claim 1 , wherein the first liquid includes MEG and the second liquid is immiscible with MEG.

14. The method of claim 1 , wherein the first liquid and the second liquid are a same liquid that includes MEG.

15. The method of claim 1 , wherein the pressurized vapor stream has a dew point temperature higher than the portion of the second liquid.

16. The method of claim 1 , further comprising introducing the first liquid into the vaporizer before vaporizing the first liquid.

17. The method of claim 16 , wherein the first liquid includes MEG and water.

18. The method of claim 6 , wherein the first liquid includes MEG and the second liquid is immiscible with MEG.

19. The method of claim 6 , wherein the first liquid and the second liquid are a same liquid that includes MEG.

Assignees

• Schlumberger Technology Corp
• Cameron Int Corp

Inventors

• Knight David John
• Langley Steven
• BUSSELL Bryan

Classifications

• B01D1/2856 Primary

  The compressed vapour is used for heating a reboiler or a heat exchanger outside an evaporator · CPC title

• B01D1/0041

  Use of fluids · CPC title

• C07C29/80 Primary

  by distillation · CPC title