IP Library Granted Patent US 12,320,101
Granted Patent B2
US 12,320,101 · App. 18/351,933 · Granted Jun 3, 2025

Water recovery system including integrated contactor with thermally-enhanced recovery

Inventors: David Roger Moore (Rexford, NY); Vitali Victor Lissianski (Schenectady, NY); Albert Santo Stella (Voorheesville, NY); Daniel Jason Erno (Clifton Park, NY)
Assignee: GE Infrastructure Technology LLC
E03B3/28B01D53/0407B01D53/0454B01D53/261B01D2257/80
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Quick Facts
Patent No.
US 12,320,101
App. No.
18/351,933
Granted
Jun 3, 2025
Kind
B2
Abstract

A water recovery system including a first fluid stream inlet providing for the flow of a first fluid stream, such as a humidified inlet gas, into the system and a second fluid stream inlet providing for the flow of a second fluid stream, such as a gas having a temperature greater than the humidified inlet gas, into the system. At least one contactor is in fluid communication with the first fluid stream inlet and the second fluid stream inlet. The at least one contactor defining therein a first fluidically-isolated, sorbent-integrated, fluid domain for flow of the first fluid stream and water adsorption, a second fluidically-isolated fluid domain for flow of the second fluid stream wherein the second fluidically-isolated fluid domain is in thermal communication with the first fluidically-isolated, sorbent-integrated, fluid domain and a third fluidically-isolated fluid domain for capture of a condensate and recycling of latent heat of condensation back to the first fluidically-isolated, sorbent-integrated, fluid domain.

Claims (42)

1. A water recovery system comprising:

a humid gas inlet configured to enable a humid gas to flow into the water recovery system and a thermal fluid inlet configured to enable a thermal fluid to flow into the water recovery system; and

at least one contactor in fluid communication with the humid gas inlet and the thermal fluid inlet, the at least one contactor comprising:

a sorbent flow path configured to receive the humid gas and adsorb water from the humid gas into a sorbent material;

a thermal flow path configured to receive the thermal fluid, wherein the thermal flow path is configured to transfer heat between the thermal fluid and the sorbent material; and

a condenser flow path configured to capture a condensate, wherein the condenser flow path is configured to transfer latent heat of condensation to the sorbent material.

2. The water recovery system of claim 1 , wherein the thermal fluid is an exhaust gas hotter than the humid gas.

3. The water recovery system of claim 1 , wherein the humid gas comprises a humid ambient air.

4. The water recovery system of claim 1 , wherein the sorbent material is configured to desorb the water in response to receiving the heat from the thermal fluid.

5. The water recovery system of claim 1 , wherein the condenser flow path is configured to receive water vapor desorbed from the sorbent material.

6. The water recovery system of claim 5 , wherein the condenser flow path is configured to cause the water vapor to condense within the condenser flow path to produce the condensate.

7. The water recovery system of claim 1 , comprising a fan configured to direct water vapor from the sorbent flow path to the condenser flow path.

8. The water recovery system of claim 1 , wherein the at least one contactor comprises:

a first contactor configured to:

adsorb the water from the humid gas into a first sorbent material in an adsorption mode of the first contactor;

desorb the water from the first sorbent material in a desorption mode of the first contactor; and

a second contactor configured to:

adsorb the water from the humid gas into a second sorbent material in the adsorption mode of the second contactor; and

desorb the water from the second sorbent material in the desorption mode of the second contactor,

wherein the water recovery system is configured to alternate between (1) the first contactor in the adsorption mode and the second contactor in the desorption mode, and (2) the first contactor in the desorption mode and the second contactor in the adsorption mode.

9. A contactor for a water recovery system comprising:

a sorbent flow path comprising a sorbent material configured to adsorb water from a humid gas;

a thermal flow path configured to receive a thermal fluid, wherein the thermal flow path is configured to transfer heat between the thermal fluid and the sorbent material; and

a condenser flow path configured to receive water vapor from the sorbent flow path wherein the condenser flow path is configured to transfer latent heat of condensation to the sorbent material.

10. The contactor of claim 9 , wherein the sorbent flow path, the thermal flow path, and the condenser flow path are parallel to one another.

11. The contactor of claim 9 , wherein the sorbent flow path, the thermal flow path, and the condenser flow path are fluidically isolated from one another.

12. The contactor of claim 9 , wherein the sorbent material is configured to adsorb the water in an adsorption mode, and the sorbent material is configured to desorb the water in a desorption mode.

13. A water recovery system comprising:

a humid gas inlet configured to enable a humid gas to flow into the water recovery system;

a first contactor configured to:

adsorb water from the humid gas when operating in an adsorption mode;

desorb the water when operating in a desorption mode; and

alternate between operating in the adsorption mode and the desorption mode; and

a second contactor configured to:

adsorb water from the humid gas when operating in the adsorption mode while the first contactor is operating in the desorption mode; and

desorb the water when operating in the desorption mode while the first contactor is operating in the adsorption mode, wherein the first contactor and/or the second contactor comprises:

a sorbent flow path configured to receive the humid gas and adsorb the water from the humid gas into a sorbent material when operating in the adsorption mode;

a thermal flow path configured to receive a thermal fluid, wherein the thermal flow path is configured to transfer heat between the thermal fluid and the sorbent material when operating in the desorption mode; and

a condenser flow path configured to capture a condensate and transfer latent heat of condensation to the sorbent material.

14. The water recovery system of claim 13 , wherein the sorbent material is configured to desorb the water as water vapor in response to heat transfer from the thermal fluid to the sorbent material.

15. The water recovery system of claim 14 , wherein the condenser flow path is configured to receive the water vapor and cause the water vapor to condense within the condenser flow path.

16. The water recovery system of claim 13 , comprising a thermal fluid inlet configured to enable a thermal fluid to flow into the water recovery system, wherein the first contactor and/or the second contactor is configured to receive the humid gas when operating in the adsorption mode, and the first contactor and/or the second contactor is configured to receive the thermal fluid when operating in the desorption mode.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 8, 2024
From: GENERAL ELECTRIC COMPANY
To: GE INFRASTRUCTURE TECHNOLOGY LLC
Reel/Frame 067029/0518 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 23, 2024
From: MOORE, DAVID ROGER; LISSIANSKI, VITALI VICTOR; STELLA, ALBERT SANTO; ERNO, DANIEL JASON
To: GENERAL ELECTRIC COMPANY
Reel/Frame 066879/0105 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 23, 2024
From: GENERAL ELECTRIC COMPANY
To: GE INFRASTRUCTURE TECHNOLOGY LLC
Reel/Frame 067095/0218 →
Continuity (2)
Continuation 17168845 · Feb 5, 2021
Related Publication 20230358025A1 · Nov 9, 2023
References Cited (28)
US 6336957B1 · Tsymerman · 2002 [cited by applicant]
US 7000410B2 · Hutchinson · 2006 [cited by applicant]
US 8163066B2 · Eisenberger · 2012 [cited by applicant]
US 8506679B2 · Hodgson · 2013 [cited by examiner]
US 9146040B2 · DeValve · 2015 [cited by examiner]
US 10279306B2 · Gebald et al. · 2019 [cited by applicant]
US 10357739B2 · Friesen · 2019 [cited by examiner]
US 10683644B2 · Kim et al. · 2020 [cited by applicant]
US 11739506B2 · Moore · 2023 [cited by examiner]
US 20070028769A1 · Eplee · 2007 [cited by examiner]
US 20080289495A1 · Eisenberger et al. · 2008 [cited by applicant]
US 20100024651A1 · Bansal · 2010 [cited by applicant]
US 20120097029A1 · Hodgson · 2012 [cited by examiner]
US 20140271420A1 · Kirchman · 2014 [cited by applicant]
US 20160109143A1 · Kogan et al. · 2016 [cited by applicant]
US 20170203249A1 · Gebald et al. · 2017 [cited by applicant]
US 20180043295A1 · Friesen · 2018 [cited by examiner]
EP 0232840A2 · 1987 [cited by applicant]
EP 3653282A1 · 2020 [cited by applicant]
WO 2013117827A1 · 2013 [cited by applicant]
WO 2015005791A1 · 2015 [cited by applicant]
WO 2019082000A1 · 2019 [cited by applicant]
WO 2019161114A1 · 2019 [cited by applicant]
WO 2019191651A1 · 2019 [cited by applicant]
WO 2020113281A1 · 2020 [cited by applicant]
Shi, Xiaoyang, et al., “Sorbents for the Direct Capture of C02 from Ambient Air”, Angewandte Chemie International Edition, vol. 59, Issue:18, pp. 1-25. [cited by applicant]
Lackner, K.S,, “Capture of carbon dioxide from ambient air”, The European Physical Journal Special Topics 176, 2009. [cited by applicant]
Samari, M., Ridha, F., Mano Vic, V. et al., “Direct capture of carbon dioxide from air via lime-based sorbents”, Mitig Adapt Strateg Glob Change 25, 25-41 (2020). [cited by applicant]