Low temperature transport and storage of amine gas treatment solutions

Patent metadata

Field	Value
Publication number	US-9458367-B2
Application number	US-201313793298-A
Country	US
Kind code	B2
Filing date	Mar 11, 2013
Priority date	Mar 14, 2012
Publication date	Oct 4, 2016
Grant date	Oct 4, 2016

Abstract

A liquid aminoether acid gas absorbent which is subject to freezing in a cold climatic zone though which the aminoether is to be shipped is rendered freeze-resistant by mixing the aminoether with water prior to transport through the cold climatic zone; the aminoether/water mixture typically contains 10 to 40 weight percent water, based on the weight of the aminoether. The aminoether/water mixture can also be stored in the cold climatic zone without being externally maintained at a temperature above the inherent freezing point of the aminoether.

First claim

The invention claimed is:

1. A method for transporting a liquid aminoether acid gas absorbent having a pour point not lower than −20° F. for use in an acid gas treatment process through a first and second climatic zone, wherein the aminoether absorbent is transported as a mixture, said mixture consisting essentially of the aminoether absorbent and water, wherein the aminoether absorbent is mixed with water prior to being transported through the second climatic zone to form an aminoether/water mixture with about 10 to 40 weight percent water, based on the weight of the aminoether; wherein the aminoether/water mixture is transported from the first climatic zone to the second climatic zone, the first climatic zone being warmer relative to the second climatic zone, the first climatic zone having an ambient temperature at which the aminoether remains unfrozen, the second climatic zone having an ambient temperature below the freezing point of the aminoether itself and water itself, the concentration of water in the aminoether/water mixture being sufficient to depress the freezing point of the mixture to a temperature below the ambient temperature of the second climatic zone; wherein the first climatic zone and the second climatic zone are in different geographic locations.

2. A method according to claim 1 in which the aminoether/water mixture is stored at a location in the second climatic zone at a temperature below the freezing point of the aminoether itself.

3. A method according to claim 1 in which the aminoether comprises a diethylene glycol derivative or triethylene glycol derivative containing a severely hindered amino group and having an Es value (Taft) of at least 1.75.

4. A method according to claim 1 in which the aminoether comprises tertiary-alkylamino diethylene glycol or a tertiary-alkylamino triethylene glycol.

5. A method according to claim 4 in which the aminoether comprises a mono-tertiary-alkylamino diethylene glycol, a mono-tertiary-alkylamino triethylene glycol, a bis-(tertiary-alkylamino) diethylene glycol or a bis-tertiary-alkylamino triethylene glycol.

6. A method according to claim 5 in which the tertiary alkylamino group comprises a tertiary-butylamino group.

7. A method according to claim 5 in which the aminoether comprises a mixture of bis-(tertiarybutylaminoethoxy)-ethane (BTEE) and ethoxyethoxyethanol-tertiary-butylamine (EEETB).

8. A method according to claim 5 in which the aminoether comprises a mixture in which the weight ratio of the diamino compound to the monoamino in the mixture is from 0.23:1 to 2.3:1.

9. A method according to claim 1 in which the aminoether comprises a alkoxy-tert-alkylamino-ether.

10. A method for storing a liquid aminoether acid gas absorbent for use in an acid gas treatment process in a cold climatic zone having an ambient temperature below the freezing point of the aminoether itself and water itself, wherein the aminoether adsorbent is stored as a mixture, said mixture consisting essentially of the aminoether adsorbent and water, wherein the aminoether absorbent is mixed with water prior to storage in the cold climatic zone to form an aminoether/water mixture with about 10 to 45 weight percent water, based on the weight of the aminoether; the concentration of water in the aminoether/water mixture being sufficient to depress the freezing point of the mixture to a temperature below the ambient temperature of the cold climatic zone.

11. A method according to claim 10 in which the aminoether/water mixture is transported from a first, relatively warmer climatic zone to the cold climatic zone, the first climatic zone having an ambient temperature at which the aminoether remains unfrozen, the concentration of water in the aminoether/water mixture being sufficient to depress the freezing point of the mixture to a temperature below the ambient temperature of the cold climatic zone; wherein the first, relatively warmer climatic zone is in a different geographic location than the cold climatic zone.

12. A method according to claim 11 in which the aminoether/water mixture is transported from the first climatic zone to the location in the cold climatic zone at a temperature below the freezing point of the aminoether itself.

13. A method according to claim 10 in which the aminoether comprises an ethylene glycol or polyethylene glycol compound containing a severely hindered amino group having an Es value (Taft) of at least 1.75.

14. A method according to claim 10 in which the aminoether comprises tertiary-alkylamino diethylene glycol or a tertiary-alkylamino triethylene glycol.

15. A method according to claim 14 in which the aminoether comprises a mono-tertiary-alkylamino diethylene glycol, a mono-tertiary-alkylamino triethylene glycol, a di- tertiary-alkylamino diethylene glycol or a di -tertiary-alkylamino triethylene glycol.

16. A method according to claim 15 in which the tertiary alkylamino group comprises a tertiary-butylamino group.

17. A method according to claim 15 in which the aminoether comprises a mixture of bis-(tertiarybutylaminoethoxy)-ethane (BTEE) and ethoxyethoxyethanol-tertiarybutylamine (EEETB).

18. A method according to claim 15 in which the aminoether comprises a mixture in which the weight ratio of the diamino compound to the monoamino is from 0.23:1 to 2.3:1.

19. A method according to claim 11 in which the aminoether comprises an alkoxy-tert-alkylamino-ether.

Assignees

• Siskin Michael
• Fedich Robert Basil
• Daage Michel
• Exxonmobil Res & Eng Co

Inventors

• Siskin Michael
• Fedich Robert Basil
• Daage Michel

Classifications

• B01D2252/2025

  Ethers or esters of alkylene glycols, e.g. ethylene or propylene carbonate · CPC title

• Y10T137/0391

  Affecting flow by the addition of material or energy · CPC title

• B01D53/1468 Primary

  Removing hydrogen sulfide · CPC title

• B01D2252/504

  Mixtures of two or more absorbents · CPC title

• B01D2252/2023

  Glycols, diols or their derivatives · CPC title