System and method to separate gases using high viscosity liquid sorbents in a spray contactor

Patent metadata

Field	Value
Publication number	US-11826695-B2
Application number	US-202117509816-A
Country	US
Kind code	B2
Filing date	Oct 25, 2021
Priority date	Oct 25, 2021
Publication date	Nov 28, 2023
Grant date	Nov 28, 2023

Abstract

A gas separation system has system input inlet configured to receive a stream mixture including a target gas, one or more spray generators positioned to spray a non-sprayable liquid to change a concentration of the target gas in the non-sprayable liquid, one or more system outlets positioned to outlet an output material, wherein at least one of the system outlets outputs a material having a lower amount of the target gas than the input stream mixture, and a recirculating path connected to the one or more outputs and the input inlet to allow recirculation of the non-sprayable liquid. A method of performing gas separation includes absorbing a target gas from an input stream in a non-sprayable capture liquid, and releasing the target gas in an output gas stream by spraying the non-sprayable capture liquid into a heated volume using a spray generator. A method of performing gas separation includes receiving an input stream that includes a target gas, using one or more spray generators to apply a non-sprayable liquid as a spray to the input stream to change a concentration of the target gas in the liquid, and outputting the liquid with the changed concentration through an outlet.

First claim

What is claimed is:

1. A gas separation system comprising:
a system input inlet configured to receive a stream mixture including a target gas;
one or more spray generators positioned to spray a non-sprayable liquid to change a concentration of the target gas in the non-sprayable liquid;
one or more system outlets positioned to outlet an output material, wherein at least one of the system outlets outputs a material having a lower amount of the target gas than the input stream mixture; and
a recirculating path connected to the one or more system outputs and the input inlet to allow recirculation of the non-sprayable liquid.

2. The gas separation system as claimed in claim 1 , wherein the one or more spray generators comprise at least one spray generator head, each head comprising:
two opposed, counter-rotating rollers having a nip between the two rollers; and
a fluid source to provide the non-sprayable capture liquid into the nip, the two counter-rotating rollers to stretch the non-sprayable capture liquid until the non-sprayable capture liquid breaks into droplets to form the spray.

3. The gas separation system as claimed in claim 1 , wherein the non-sprayable liquid comprises a non-Newtonian fluid.

4. The gas separation system as claimed in claim 1 , wherein the non-sprayable capture liquid is one or more selected from the group consisting of: aqueous amines with amine loading of greater than 20 wt %, polymeric amines, oligomeric amines, amines having a molecular weight of greater than 100 g/mol, solutions containing ionic liquids, phase change materials, CO 2 -binding organic liquids with water concentration of less than 80 wt % at the temperature of CO 2 capture, liquids having a specific heat capacity of less than 110 J/mol/K, and aminosilicones.

5. The gas separation system as claimed in claim 1 , wherein the one or more spray generators comprises one or more regenerating spray contactors, wherein an inlet to the one or more regenerating spray contactors is positioned to receive a gas-solvated liquid of the non-sprayable liquid and the target gas, the one or more regenerating spray contactors to apply the gas-solvated liquid as a spray to release the target gas from the non-sprayable liquid to at least two regenerator spray contactor outlets to output the gas and the non-sprayable liquid.

6. The gas separation system as claimed in claim 5 , further comprising a heat source positioned to apply heat to the gas-solvated liquid to release the target gas from the gas-solvated liquid.

7. The gas capture system as claimed in claim 5 , wherein an outlet of the regenerating spray contactor comprises one of the one or more system outlets for gas released from the gas-solvated liquid, and a liquid outlet connected to the recirculation path to recirculate the non-sprayable liquid from which the target gas has been released.

8. The gas separation system as claimed in claim 1 , further comprising a carbon utilization system within the gas separation system, the utilization system having one or more of the spray generators positioned to apply a gas-solvated liquid to other input materials, the utilization system further having one or more utilization outlets, wherein the one or more utilization outlets comprises at least a liquid outlet connected to the recirculation path to recirculate a post utilization non-sprayable liquid and an outlet for desired utilization products derived from the target gas.

9. The gas separation system as claimed in claim 1 , wherein an inlet to the one or more of the spray generators comprises the system input inlet positioned to receive the input stream mixture, and the one or more of the spray generators is positioned to apply the non-sprayable liquid to the input stream mixture, the spray generator having one or more spray contactor outlets to output a gas-solvated liquid and an output gas stream having less of the target gas than the input stream mixture, the spray contactor outlets comprises one of either system outlets or outlets internal to the system.

10. The gas separation system as claimed in claim 1 , wherein the non-sprayable liquid capture has a viscosity in a range of 1 mPa-s to 10,000 Pa-s.

11. The gas separation system as claimed in claim 1 , wherein the non-sprayable liquid comprises a high-viscosity liquid having non-Newtonian strain hardening behavior in extension.

12. The gas separation system as claimed in claim 1 , wherein the one or more spray generators are configured to spray the non-sprayable liquid as droplets with an average size of 1 to 500 microns and where the total surface area generated per unit volume of capture solution ranges from 12 to 6000 m 2 /L.

13. The gas separation system as claimed in claim 1 , wherein the gas separation system is positioned to receive the input stream mixture including either nitrogen or carbon dioxide.

Assignees

• Palo Alto Res Ct Inc
• Xerox Corp

Inventors

• Chintapalli Mahati
• Unidad Jerome
• Murphy Kathryn F
• Neelakantan Ravi
• Pandey Rahul
• Meckler Stephen Matthew
• Johnson David Mathew

Classifications

• B01D53/1493 Primary

  Selection of liquid materials for use as absorbents · CPC title

• B01D53/1425

  Regeneration of liquid absorbents · CPC title

• B01D53/1475 Primary

  Removing carbon dioxide · CPC title

• B01D53/185

  Liquid distributors · CPC title

• B01D2252/204

  Amines · CPC title