Gas dehydration composition and process to reduce solvent losses

Patent metadata

Field	Value
Publication number	US-12128353-B2
Application number	US-201816631380-A
Country	US
Kind code	B2
Filing date	Jul 24, 2018
Priority date	Aug 16, 2017
Publication date	Oct 29, 2024
Grant date	Oct 29, 2024

Abstract

The present invention relates to a dehydration composition and method of use thereof for drying gas streams, in particular natural gas streams, wherein the dehydration composition comprises a (a) glycol and (b) an additive selected so as to increase the viscosity, surface tension, and/or specific gravity of the dehydration composition. Said dehydration composition and method results in the reduction of solvent loss during the dehydration step in a gas dehydration unit.

First claim

What is claimed is:

1. A process to reduce glycol loss in a gas dehydration unit comprising a dehydration column, wherein the dehydration column is positioned vertically and has a wet gas inlet at the bottom of the column and a dry gas outlet at the top of the column, said column comprising:
(i) a contact zone in an absorption section of the column having two or more bubble trays, wherein there is an upper most and a lower most bubble tray,
(ii) a demister located between the upper most bubble tray and the gas outlet, and
(iii) a gas dehydration composition which enters the column above the upper most bubble tray and below the demister, and exits the column below the lower most bubble tray, said gas dehydration composition comprising at least 50 weight percent of a glycol,

said process comprising the steps of:
(A) contacting a wet gas counter-currently in the contact zone of the dehydration column with a lean gas dehydration composition to form a dry gas and a water rich dehydration composition and
(B) having the dry gas pass through the demister prior to exiting the dehydration column'

wherein the gas dehydration composition is modified to increase the droplet size of the dehydration solvent entrained in the dry gas entering the demister by controlling one or more liquid properties of the gas dehydration composition, which property is selected from the group consisting of viscosity, surface tension, density and combinations thereof.

2. The process of claim 1 wherein the gas dehydration unit is a natural gas dehydration unit and the gas is natural gas.

3. The gas dehydration composition of the process of claim 1 wherein
(a) the glycol is monoethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, monopropylene glycol, dipropylene glycol, tripropylene glycol, or tetrapropylene glycol.

4. The process of claim 1 wherein the gas dehydration composition further comprises one or more component selected from:
(c) an alkanolamine, a phosphate acid or salt compound, a borate acid or salt compound, a sweetening agent, a low temperature viscosity improver, a corrosion inhibitor, an antifoaming agent, or mixtures thereof.

5. The gas dehydration composition of the process of claim 1 wherein
(a) the glycol is triethylene glycol, monoethylene glycol, diethylene glycol, tripropylene glycol, or mixtures thereof.

6. The gas dehydration composition of the process of claim 1 wherein the gas dehydration composition further includes sodium tetraborate.

7. The process of claim 1 wherein the modified gas dehydration composition has a viscosity at 25° C. of 54 Cp or more.

8. The process of claim 1 wherein the droplet size of the gas dehydration composition is increased by the addition of a modifier selected from the group consisting of glycerine, diglycerine, triglycerine, erythritol, pentaerythritol, trimethylolmethane, or mixtures thereof, and where the modifier is added in an amount such that the gas dehydration composition comprises at least 25 weight percent of the modifier.

9. The process of claim 8 wherein the modifier is glycerine.

10. The gas dehydration composition of the process of claim 9 wherein the glycol is triethylene glycol and the gas dehydration composition includes from 50 to 75 weight percent of triethylene glycol and from 25 to 50 weight percent of glycerine.

11. The gas dehydration composition of the process of claim 10 wherein the gas dehydration composition further comprising from 0.1 to 10 weight percent of sodium tetraborate.

12. The gas dehydration composition of the process of claim 11 wherein the gas dehydration composition consists essentially of triethylene glycol, glycerine, and sodium tetraborate.

13. The process of claim 1 wherein the average particle diameter of the gas dehydration composition droplets entrained in the dry gas entering the demister is increased by at least thirty percent compared to the unmodified gas dehydration composition.

14. A process to reduce glycol loss in a gas dehydration unit comprising a dehydration column, wherein the dehydration column is positioned vertically and has a wet gas inlet at the bottom of the column and a dry gas outlet at the top of the column, said column comprising:
(i) a contact zone in an absorption section of the column having two or more bubble trays, wherein there is an upper most and a lower most bubble tray,
(ii) a demister located between the upper most bubble tray and the gas outlet, and
(iii) a gas dehydration composition which enters the column above the upper most bubble tray and below the demister, and exits the column below the lower most bubble tray, said gas dehydration composition comprising at least 50 weight percent of a glycol, said process comprising the steps of:
(A) contacting a wet gas counter-currently in the contact zone of the dehydration column with a lean gas dehydration composition to form a dry gas and a water rich dehydration composition and
(B) having the dry gas pass through the demister prior to exiting the dehydration column'

wherein the gas dehydration composition is modified to increase the droplet size of the dehydration solvent entrained in the dry gas entering the demister by controlling one or more liquid properties of the gas dehydration composition, which property is selected from the group consisting of viscosity, surface tension, density and combinations thereof; and
wherein the droplet size of the gas dehydration composition is increased by the addition of a modifier selected from the group consisting of glycerine, diglycerine, triglycerine, erythritol, pentaerythritol, trimethylolmethane, or mixtures thereof, and where the modifier is added in an amount such that the gas dehydration composition comprises at least 25 weight percent of the modifier.

Assignees

• Dow Global Technologies Llc

Inventors

• Laroche Christophe R
• Dowdle John R
• Klinker Eric J

Classifications

• C10L2290/541

  Absorption of impurities during preparation or upgrading of a fuel · CPC title

• C10L2290/08

  Drying or removing water · CPC title

• C10L3/106

  of water · CPC title

• B01D2252/606

  Anticorrosion agents · CPC title

• B01D2252/50

  Combinations of absorbents · CPC title