Methods and systems for improving the energy efficiency of carbon dioxide capture

Patent metadata

Field	Value
Publication number	US-10005027-B2
Application number	US-201615008964-A
Country	US
Kind code	B2
Filing date	Jan 28, 2016
Priority date	Jan 28, 2015
Publication date	Jun 26, 2018
Grant date	Jun 26, 2018

Abstract

A system for carbon dioxide capture from a gas mixture comprises an absorber that receives a lean solvent system stream (containing a chemical solvent, physical-solvent additive, and water) from the stripper, a stripper that receives the rich solvent stream from the absorber and produces the product carbon dioxide and the lean solvent through the use of a reboiler in fluid communication with a lower portion of the stripper, a condenser in fluid communication with a vapor outlet of the stripper, a cross-exchanger in fluid communication with a rich solvent system outlet from the absorber and a rich solvent system inlet on the stripper, and a splitter. The splitter is configured to separate the rich solvent system stream into a first portion and a second portion, where the first portion directly passes to the stripper and the second portion passes through the cross-exchanger prior to passing to the stripper.

First claim

What is claimed is:

1. A method for capturing carbon dioxide from a gas mixture comprising:
contacting a gaseous stream comprising carbon dioxide with a lean solvent system, wherein the lean solvent system comprises a chemical solvent, a physical solvent, and water;
absorbing at least a portion of the carbon dioxide in the lean solvent system to produce a rich solvent system;
transferring the rich solvent system to a stripper, wherein the stripper comprises a reboiler;
applying heat to the rich solvent system using the reboiler;
generating a first vapor stream within the reboiler while incurring a heat rate to regenerate the lean solvent system, wherein the first vapor stream comprises steam and at least a portion of the carbon dioxide from the rich solvent system;
passing a liquid stream from the reboiler to a flash vessel;
producing, in the flash vessel, a second vapor stream and the lean solvent system;
compressing the second vapor stream in a lean vapor compressor to produce a compressed lean vapor stream;
passing the compressed lean vapor stream to the stripper; and
transferring an overhead stream from the stripper to a condenser.

2. The method of claim 1 , wherein a heat duty of the condenser is reduced relative to a corresponding method in which the solvent system does not include the physical solvent, and reducing a heat duty of the reboiler relative to a corresponding process in which the solvent system does not include the physical solvent.

3. The method of claim 1 , wherein the heat rate of the method is reduced by at least 10% relative to a corresponding process in which the solvent system does not include the physical solvent.

4. The method of claim 1 , further comprising:
splitting the rich solvent into a first portion and a second portion;
transferring the first portion of the rich solvent to the stripper without passing through a cross exchanger; and
transferring the second portion of the rich solvent system through the cross exchanger prior to transferring the second portion to the stripper.

5. The method of claim 4 , wherein the first portion of the rich solvent enters the stripper above where the second portion enters the stripper.

6. The method of claim 1 , wherein absorbing at least the portion of the carbon dioxide in the lean solvent system occurs in an absorber, wherein an intercooler is in fluid communication with the absorber, and wherein the intercooler comprises a heat comprises exchanger, a fluid inlet, and a fluid outlet, wherein the method further comprises:
receiving a side stream from the absorber through the fluid inlet;
cooling the side stream in the heat exchanger; and
returning the cooled side stream to the absorber through the fluid outlet of the intercooler.

7. The method of claim 1 , wherein the lean solvent system comprises:
the chemical solvent in a concentration ranging from 20 wt % to 50 wt %,
wherein the physical solvent is a nonaqueous physical solvent, and where a molar ratio of the nonaqueous physical solvent to the chemical solvent is between about 0.01 to 0.7.

8. The method of claim 7 , wherein the nonaqueous physical solvent is selected from a group consisting of ethylene carbonate, propylene carbonate, n-methyl-2-pyrrolidone, sulfolane, ethylene glycol, 1,3-propylene glycol, diethylene glycol, triethylene glycol, sulfolane, N-methyl-2-pyrrolidone, isobutylene glycol, and combinations thereof.

9. The method of claim 7 , wherein the nonaqueous physical solvent has a dielectric constant that is greater than that of water at an operating temperature in which the solvent is in use.

10. The method of claim 7 , wherein a carbon dioxide loading in the solvent system is greater than about 0.4.

11. The method of claim 7 , wherein the chemical solvent is selected from a group consisting of an alkanolamine and an alkaline carbonate.

12. The method of claim 7 , wherein the chemical solvent comprises an alkanolamine, and wherein the alkanolamine is selected from a group consisting of monoethanolamine A (MEA), 2-amine-2-methyl-1 propanol (AMP), diglycolamine (DGA), and combinations thereof.

13. The method of claim 7 , wherein the nonaqueous physical solvent has a dielectric constant greater than 7.

14. The method of claim 13 , wherein the nonaqueous physical solvent has a dielectric constant greater than or equal to 15.

15. A method for capturing carbon dioxide from a gas mixture comprising:
providing a rich solvent to a stripper;
applying heat to the rich solvent system using a reboiler;
generating a first vapor stream within the reboiler while incurring a heat rate to regenerate a lean solvent system, wherein the first vapor stream comprises steam and at least a portion of the carbon dioxide from the rich solvent system;
passing a liquid stream from the reboiler to a flash vessel;
producing, in the flash vessel, a second vapor stream and the lean solvent system;
compressing the second vapor stream in a lean vapor compressor to produce a compressed lean vapor stream; and
passing the compressed lean vapor stream to the stripper; wherein providing a rich solvent to a stripper comprises: contacting a gaseous stream comprising carbon dioxide with the lean solvent system, wherein the lean solvent system comprises a chemical solvent, a physical solvent, and water, where a molar ratio of the physical solvent to the chemical solvent is between about 0.01 to 0.7, and wherein the physical solvent has a dielectric constant greater than 7; absorbing at least a portion of the carbon dioxide in the lean solvent system to produce the rich solvent system; and transferring the rich solvent system to the stripper, wherein the stripper comprises the reboiler.

16. The method of claim 15 , further comprising transferring an overhead stream from the stripper to a condenser; wherein a heat duty of the condenser is reduced relative to a corresponding method in which the solvent system does not include the physical solvent, and reducing a heat duty of the reboiler relative to a corresponding process in which the solvent system does not include the physical solvent.

17. The method of claim 15 , further comprising:
splitting the rich solvent into a first portion and a second portion;
transferring the first portion of the rich solvent to the stripper without passing through a cross exchanger; and
transferring the second portion of the rich solvent system through the cross exchanger prior to transferring the second portion to the stripper.

18. The method of claim 17 , wherein the first portion of the rich solvent enters the stripper above where the second portion enters the stripper.

19. The method of claim 17 , wherein absorbing at least the portion of the carbon dioxide in the lean solvent system occurs in an absorber, wherein an intercooler is in fluid communication with the absorber, and wherein the intercooler comprises a heat exchanger, a fluid inlet, and a fluid outlet, wherein the method further comprises:
receiving a side stream from the absorber through the fluid inlet;
cooling the side stream in the heat exchanger, and
returning the cooled side stream to the absorber through the fluid outlet of the intercooler.

Assignees

• Fluor Tech Corp
• Fluor Tech Corporaticn

Inventors

• Mathias Paul M
• Reddy Satish

Classifications

• B01D53/78

  with gas-liquid contact · CPC title

• Y02C10/04

  Cross-Sectional Technologies · mapped topic

• B01D2252/2026

  Polyethylene glycol, ethers or esters thereof, e.g. Selexol · CPC title

• Y02A50/2342

  Cross-Sectional Technologies · mapped topic

• B01D53/1493

  Selection of liquid materials for use as absorbents · CPC title