Vacuum sweep dehumidification system

Patent metadata

Field	Value
Publication number	US-10969124-B2
Application number	US-201816130800-A
Country	US
Kind code	B2
Filing date	Sep 13, 2018
Priority date	Sep 13, 2018
Publication date	Apr 6, 2021
Grant date	Apr 6, 2021

Abstract

An apparatus for removing water vapor from a feed gas is provided that comprises a membrane housing, a membrane that divides a first pressure side and a second pressure side of the membrane housing, a feed gas inlet and outlet on the first pressure side, a sweep gas inlet and outlet on the second pressure side, a sweep gas flow regulator, and a pump. In some embodiments the feed gas can be at ambient pressure and a pressure drop across the membrane can be less than about 1 atm.

First claim

What is claimed is:

1. An apparatus for removing water vapor from gas, comprising:
a membrane housing;
a membrane received by the housing, the membrane comprising a stack of membrane layers having at least six membrane layers, wherein intramembrane fractional spacing of open flow area to total area of the membrane is about 0.5 or greater;
a feed gas inlet that is upstream from the membrane and directs a feed gas at ambient pressure to perpendicularly contact and cross the membrane;
a feed gas outlet downstream of the membrane, where the feed gas has a pressure drop from the feed gas inlet to the feed gas outlet of less than 0.06 kPa;
a sweep gas inlet extending along the stack of membrane layers, the sweep gas inlet directing a sweep gas through and/or across the membrane;
a sweep gas outlet extending along the stack of membrane layers, the sweep gas outlet allowing the sweep gas to exit the membrane housing, each membrane layer extending between the sweep gas inlet and sweep gas outlet; and
wherein water vapor from the feed gas is drawn through and/or across the membrane and out of the membrane housing.

2. The apparatus of claim 1 , wherein each membrane layer of the membrane is comprised of hollow fibers and the sweep gas is directed through the hollow fibers.

3. The apparatus of claim 2 , wherein the hollow fibers have a diameter of about 0.5 mm to about 5 mm.

4. The apparatus of claim 1 , wherein the membrane is a hollow fiber membrane, capillary membrane, flat sheet membrane, or a combination thereof.

5. The apparatus of claim 1 , wherein the intramembrane fractional spacing is from about 0.5 to about 0.75.

6. The apparatus of claim 1 , wherein the membrane housing is situated inside a HVAC air duct.

7. The apparatus of claim 1 , wherein the membrane comprises at least 24 membrane layers.

8. The apparatus of claim 1 , further comprising a recycle loop that is in fluid communication with the sweep gas outlet and the feed gas inlet.

9. The apparatus of claim 1 , wherein the sweep gas has a pressure drop from the sweep gas inlet to the sweep gas outlet of less than 40 mmHg.

10. An apparatus for removing water vapor from gas, comprising:
a membrane housing having a feed gas end and a retentate end, the membrane housing comprising:
a sweep in manifold,
a sweep out manifold,
a membrane comprising at least six membrane layers stacked along a length of the sweep in manifold and the sweep out manifold, each membrane layer comprising hollow fibers distributed across a width of the membrane layer and coupled between the sweep in manifold and the sweep out manifold, wherein intramembrane fractional spacing of open flow area to total area of the membrane is about 0.5 or greater,
a feed gas pressure zone,
a sweep gas in pressure zone, and
a sweep gas out pressure zone;

wherein the sweep in manifold and the sweep out manifold are parallel to a feed gas flow and hold the hollow fibers of the at least six membrane layers perpendicular to the feed gas flow; and
wherein the sweep in manifold defines the sweep gas in pressure zone and the feed gas pressure zone and the sweep out manifold defines the sweep gas out pressure zone and the feed gas pressure zone;
a feed gas inlet directing a feed gas with a first humidity through the feed gas pressure zone to perpendicularly contact and cross the membrane to the retentate end, wherein the feed gas enters a first pressure space at ambient pressure with a pressure drop across the feed gas pressure zone of less than 0.06 kPa;
a feed gas outlet on the retentate end;
a sweep gas inlet directing a sweep gas with a second humidity into the sweep gas in pressure zone, through the membrane, and to the sweep gas out pressure zone;
a sweep gas outlet in the sweep gas out pressure zone, allowing permeate to exit the membrane housing; and
wherein water vapor from the feed gas is drawn through the membrane into a second pressure space as the permeate.

11. The apparatus of claim 10 , further comprising:
a sweep gas flow regulator to direct the sweep gas into the sweep gas in pressure zone; and
a sweep gas outlet vacuum pump located downstream from the sweep gas outlet that imparts a lower pressure in the sweep gas out pressure zone than the pressure in the sweep gas in pressure zone and the feed gas pressure zone.

12. The apparatus of claim 11 , wherein the sweep gas flow regulator is an expansion valve, a throttling device, a valve, a capillary tube, or an orifice.

13. The apparatus of claim 10 , further comprising a flow splitter to direct a re-directed portion of the feed gas exiting the first pressure space to the second pressure space as the sweep gas.

14. The apparatus of claim 10 , further comprising a water collection device to collect condensed water vapor from the feed gas.

15. The apparatus of claim 10 , wherein the intramembrane fractional spacing is from about 0.5 to about 0.75.

16. The apparatus of claim 10 , wherein the membrane is comprised of hollow fibers with a diameter of about 0.5 mm to about 5 mm.

17. The apparatus of claim 10 , wherein the membrane comprises polydimethylsiloxane, cellulose acetate, sulfonated polyethersulfone, polyethylene oxide, sulfonated poly(ether ether ketone), poly(vinylalcohol)-Ethylene Diamine Tetra (Methylene Phosphonic Acid), 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)amide, trimethyl(butyl)ammonium bis(trifluoromethylsulfonyl)amide, 1-ethyl-3-methylimidazolium (BF 4 ), or combinations thereof.

18. The apparatus of claim 10 , further comprising a recycle loop that is in fluid communication with the sweep gas outlet and the feed gas inlet.

19. The apparatus of claim 10 , wherein the sweep gas comprises a portion of the feed gas.

20. The apparatus of claim 10 , wherein the feed gas is air, oxygen, nitrogen, methane, biomethane, ethane, ethylene, ethanol, butane, butanol, or combinations thereof.

21. The apparatus of claim 10 , being part of an air conditioning system.

22. The apparatus of claim 10 , wherein fiber density is about 4 fibers per cm for a cross-sectional void space of 74%.

23. The apparatus of claim 10 , wherein the membrane comprises at least 24 membrane layers.

24. The apparatus of claim 10 , wherein the sweep gas has a pressure drop from the sweep gas in pressure zone to the sweep gas out pressure zone of less than 40 mmHg.

Assignees

• Univ Mississippi

Inventors

• Scovazzo Paul
• Scovazzo Anthony

Classifications

• B01D63/02

  Hollow fibre modules · CPC title

• B01D53/268

  by diffusion · CPC title

• F24F2003/144

  by dehumidification only · CPC title

• B01D2313/24

  Specific pressurizing or depressurizing means · CPC title

• F24F2003/1435

  comprising semi-permeable membrane · CPC title