Hydrophobic air-gap membrane distillation

Patent metadata

Field	Value
Publication number	US-9751047-B2
Application number	US-201414517342-A
Country	US
Kind code	B2
Filing date	Oct 17, 2014
Priority date	Oct 17, 2014
Publication date	Sep 5, 2017
Grant date	Sep 5, 2017

Abstract

An energy-efficient liquid-gap distillation apparatus includes a source of a feed liquid; a distillation module comprising: (a) a feed-liquid chamber n fluid communication with the feed-liquid source to establish a flow of the feed liquid there through, wherein the feed-liquid chamber includes a selectively porous material that allows a component of the feed liquid to pass through the selectively porous material and exit the feed-liquid chamber in vapor form but not in liquid form; (b) a condensing surface maintained at a lower temperature than the feed liquid in the feed-liquid chamber, wherein the condensing surface is sufficiently hydrophobic to produce a contact angle with water of at least 150; and (c) a gap between the selectively porous material and the condensing surface. Vapor passing through the membrane can be condensed as jumping droplets at the condensing surface.

First claim

What is claimed is:

1. An apparatus for air-gap distillation comprising:
a feed-liquid source including a feed liquid;
a distillation module comprising:
a) a feed-liquid chamber containing feed liquid in fluid communication with the feed-liquid source to establish a flow of the feed liquid through the feed-liquid chamber, wherein the feed-liquid chamber includes a porous material that allows vapor phase to pass through and exit the feed liquid chamber, but not liquid phase, hereafter referred to as a selectively permeable material;
b) a condensing surface maintained at a lower temperature than the feed liquid in the feed-liquid chamber, wherein the condensing surface is sufficiently hydrophobic to produce a contact angle with water of at least 90°;
c) a gap between the selectively permeable material and the condensing surface, wherein the selectively permeable material separates the feed liquid in the feed-liquid chamber from the gap; and
d) a plurality of hydrophilic spacers in the gap, the hydrophilic spacers being spaced from one another, stretching across the gap, and extending away from the condensing surface in the gap, wherein the hydrophilic spacers are in contact with the condensing surface to wick liquid condensate away from the condensing surface.

2. An apparatus for air-gap distillation comprising:
a feed-liquid source including a feed liquid;
a distillation module comprising:
a) a first feed-liquid chamber in fluid communication with the feed-liquid source, the first feed-liquid chamber including a heat-transfer plate with a condensing surface, wherein the condensing surface is sufficiently hydrophobic to produce a contact angle with water of at least 90°;
b) a conduit coupled to the first feed-liquid chamber to extract the feed liquid after the feed liquid flows through the first feed-liquid chamber;
c) a heat source configured to heat the feed liquid in the conduit;
d) a second feed-liquid chamber coupled to the conduit and configured to receive the feed liquid after the feed liquid flows through the conduit and is heated by the heat source, wherein the second feed-liquid chamber includes a selectively permeable material that allows a component of the feed liquid to pass through the selectively permeable material and exit the second feed-liquid chamber in vapor form but not in liquid form, wherein one side of the selectively permeable material faces the condensing surface of the heat-transfer plate;
e) a gap between the condensing surface and the selectively permeable material; and
f) a plurality of hydrophilic spacers in the gap, the hydrophilic spacers being spaced from one another, stretching across the gap, and extending away from the condensing surface in the gap, wherein the hydrophilic spacers are in contact with the condensing surface to wick liquid condensate away from the condensing surface; and
a condensate collection receptacle in fluid communication with the gap.

3. The apparatus of claim 2 , wherein the feed liquid in the feed-liquid source comprises a volatile component and a less-volatile component.

4. The apparatus of claim 2 , wherein the feed liquid in the feed-liquid source comprises water.

5. The apparatus of claim 4 , wherein the feed liquid in the feed-liquid source further comprises at least one of the following: water including dissolved salts or minerals, water including suspended solute, water including suspended oil, water-alcohol mixture, and fruit juice.

6. The apparatus of claim 4 , wherein the selectively permeable material has a contact angle with the water of the feed liquid of greater than 90° and allows vapor phase to pass through while preventing liquid feed from passing through.

7. The apparatus of claim 6 , wherein the selectively permeable material comprises at least one of the following: a polymer membrane, a porous ceramic material, a porous carbon material, a porous metal material, and a porous graphene material.

8. The apparatus of claim 7 , wherein the polymer membrane comprises at least one of the following: polyvinylidene difluoride, polytetrafluoroethylene, and polypropylene.

9. The apparatus of claim 2 , wherein the condensing surface includes copper oxide.

10. The apparatus of claim 9 , wherein the copper oxide is coated with a silane.

11. The apparatus of claim 10 , wherein the silane is fluorinated.

12. The apparatus of claim 10 , wherein the condensing surface has a rugosity greater than 2.

13. The apparatus of claim 2 , wherein the condensing surface comprises a composition selected from at least one of the following: acrylics, amides, carbonates, dienes, esters, ethers, fluorocarbons, olefins, styrenes, vinyl acetals, vinyl esters, vinyl keytones, and vinylpuridine polymers.

14. The apparatus of claim 2 , wherein the condensing surface is sufficiently hydrophobic to produce a contact angle with water of greater than 165°.

15. The apparatus of claim 2 , wherein the condensing surface is more hydrophobic than the selectively permeable material.

16. The apparatus of claim 2 , wherein the gap has a thickness, extending from the selectively permeable material to the condensing surface of less than 5 mm.

17. The apparatus of claim 2 , wherein the hydrophilic spacer comprises at least one of a polymer and a metal.

18. A method for air-gap distillation, comprising:
flowing a feed liquid through a first feed-liquid chamber of a distillation module, wherein the first feed-liquid chamber includes a condensing surface that is sufficiently hydrophobic to produce a contact angle of at least 150° with water;
heating the feed liquid;
flowing the heated feed liquid through a second feed-liquid chamber of the distillation module, wherein the second feed-liquid chamber includes a selectively permeable material that includes an outer surface in fluid communication with a gap between the selectively permeable material and the first feed-liquid chamber;
permeating a vapor component from the feed liquid in the second feed-liquid chamber through the selectively permeable material into the gap between the selectively permeable material and the condensing surface;
condensing the vapor component of the feed liquid as a jumping droplet from the condensing surface in the gap to produce a liquid condensate in the gap;
removing the liquid condensate from the condensing surface via wicking along a plurality of hydrophilic spacers in the gap, the hydrophilic spacers being spaced from one another, stretching across the gap, and extending away from the condensing surface in the gap, wherein the hydrophilic spacers are in contact with the condensing surface; and
removing from the second feed-liquid chamber a brine remaining from the feed liquid after the vapor component permeates through the selectively permeable material.

19. The method of claim 18 , wherein the vapor component passes through pores in the selectively permeable material, while the flow of liquid-phase components from feed liquid through the pores is prevented.

20. The method of claim 18 , wherein the feed liquid entering the second feed-liquid chamber is at a temperature in a range from 40° C. to 100° C.

21. The method of claim 20 , wherein the feed-liquid temperature is raised using a solar heat collector.

22. The method of claim 20 , wherein the feed liquid entering the second feed-liquid chamber is pressurized as its temperature is increased to a range from 100° C. to 140° C.

23. The method of claim 18 , further comprising generating

Assignees

• Massachusetts Inst Technology

Inventors

• Lienhard John H
• Warsinger David Elan Martin
• Swaminathan Jaichander

Classifications

• B01D1/0035

  Solar energy (for treatment of water C02F1/14) · CPC title

• B01D2325/36

  Hydrophilic membranes · CPC title

• B01D69/02

  characterised by their properties · CPC title

• B01D2313/38

  Operations & Transport · mapped topic

• B01D61/364 Primary

  Membrane distillation · CPC title