Heat exchange system configured with a membrane contactor

Patent metadata

Field	Value
Publication number	US-9403102-B2
Application number	US-201213372121-A
Country	US
Kind code	B2
Filing date	Feb 13, 2012
Priority date	Feb 13, 2012
Publication date	Aug 2, 2016
Grant date	Aug 2, 2016

Abstract

A heat exchange system may include a first heat exchange circuit and a second heat exchange circuit. The first heat exchange circuit may circulate a first working fluid sequentially through a first heat exchanger, a second heat exchanger and a membrane contactor. The second heat exchange circuit may direct a second working fluid sequentially through the first heat exchanger and the membrane contactor, where the second working fluid includes solute and solvent. The first heat exchanger and the membrane contactor may transfer heat energy from the second working fluid to the first working fluid, and the second heat exchanger may transfer heat energy from the first working fluid to a third working fluid. The membrane contactor may extract a portion of the solvent from the second working fluid.

First claim

What is claimed is:

1. A heat exchange system, comprising:
a first heat exchange circuit that circulates a first working fluid sequentially through a first heat exchanger, a second heat exchanger and a membrane contactor; and
a second heat exchange circuit that directs a second working fluid sequentially through the first heat exchanger and the membrane contactor, the second working fluid comprising solute and solvent;
wherein the first heat exchanger and the membrane contactor transfer heat energy from the second working fluid to the first working fluid, and the second heat exchanger transfers heat energy from the first working fluid to a third working fluid;
wherein the membrane contactor extracts a portion of the solvent from the second working fluid; and
wherein the membrane contactor comprises
a first flow channel connected in-line with the first heat exchange circuit, the first flow channel comprising a channel sidewall;
a second flow channel connected in-line with the second heat exchange circuit, the second flow channel comprising a vapor diffusing membrane; and
a third flow channel that receives vapor of the extracted solvent that migrates across the vapor diffusion membrane from the first flow channel towards the channel sidewall.

2. The system of claim 1 , wherein the second working fluid comprises at least one of mineral water, brackish water, saline water, sea water, waste water, brine and manufacturing process fluid.

3. The system of claim 2 , wherein the extracted solvent comprises at least one of potable water and distilled water.

4. The system of claim 1 , further comprising a solver reservoir that receives the extracted solvent.

5. The system of claim 1 , further comprising a pre-cooler that receives the extracted solvent, and reduces temperature of the third working fluid that is directed into the second heat exchanger utilizing the extracted solvent.

6. The system of claim 5 , wherein the pre-cooler comprises at least one of a solvent mister and an evaporative cooler.

7. The system of claim 1 , wherein the first heat exchanger comprises an evaporator, the second heat exchanger comprises a condenser, and the first heat exchange circuit further comprises a turbine that is driven by the first working fluid.

8. The system of claim 7 , further comprising a pre-heater connected between the evaporator and the membrane contactor, wherein the pre-heater transfers heat energy from the second working fluid to the first working fluid.

9. The system of claim 7 , further comprising
a pre-heater that transfers heat energy from the second working fluid to the first working fluid;
a first valve that directs the first working fluid from the condenser to the pre-heater during a first mode of operation, and from the condenser to the membrane contactor during a second mode of operation; and
a second valve that directs the second working fluid from the evaporator to the pre-heater during the first mode of operations, and from the evaporator to the membrane contactor during the second mode of operation.

10. The system claim 1 , wherein the membrane contactor comprises a counter-flow membrane contactor.

11. The system of claim 1 , wherein the membrane contactor comprises at least one of a liquid gap membrane distillation device, an air gap membrane distillation device, and a direct contact membrane distillation device.

12. The system of claim 1 , wherein the membrane contactor comprises one of a sweeping gas distillation device and a vacuum membrane distillation device.

13. The system of claim 1 , wherein the first heat exchange circuit is configured in an organic Rankine cycle power system.

14. The system of claim 1 , wherein the third working fluid comprises air.

15. A heat exchange system, comprising:
a Rankine cycle power system that circulates a first working fluid sequentially through an evaporator, a turbine generator, a condenser and a membrane contactor; and
a heat exchange circuit that directs a second working fluid sequentially through the evaporator and the membrane contactor, the second working fluid comprising solute and solvent;
wherein the evaporator and the membrane contactor transfer heat energy from the second working fluid to the first working fluid, and the condenser transfers heat energy from the first working fluid to a third working fluid;
wherein the turbine generator is driven by the first working fluid and generates electrical power;
wherein the membrane contactor acts a portion of the solvent from the second working fluid; and
wherein the membrane contactor comprises
a first flow channel connected in-line with the first heat exchange circuit, the first flow channel comprising a channel sidewall;
a second flow channel connected in-line with the second heat exchange circuit, the second flow channel comprising a vapor diffusing membrane; and
a third flow channel that receives vapor of the extracted solvent that migrates across the vapor diffusion membrane from the first flow channel towards the channel sidewall.

16. The system of claim 15 , wherein
the second working fluid comprises at least one of mineral water, brackish water, saline water, sea water, waste water, brine and manufacturing process fluid; and
the extracted solvent comprises at least one of potable water and distilled water.

17. The system of claim 16 , further comprising a solvent reservoir that receives the extracted solvent.

18. The system of claim 16 , further comprising a pre-cooler that receives the extracted solvent, and reduces temperature of the third working fluid that is directed into the condenser utilizing the extracted solvent.

19. The system of claim 16 , wherein the membrane contactor comprises at least one of a liquid gap membrane distillation device, an air gap membrane distillation device, and a direct contact membrane distillation device.

Assignees

• Wu Hailing
• Ma Zidu
• United Technologies Corp

Inventors

• Wu Hailing
• Ma Zidu

Classifications

• Y02W10/37

  using solar energy · CPC title

• C02F1/16

  using waste heat from other processes · CPC title

• F28C3/08

  with change of state, e.g. absorption, evaporation, condensation (generating steam under pressure F22) · CPC title

• Y02E10/10

  Geothermal energy · CPC title

• F28D21/0015

  Heat and mass exchangers, e.g. with permeable walls · CPC title