# US 9,751,047 B2 · Hydrophobic air-gap membrane distillation > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 9,751,047 B2 - Document ID: US9751047B2 - Status: Granted - Kind: B2 - Application number: 14/517,342 - Filed: 2014-10-17 - Published: 2016-04-21 - Granted: 2017-09-05 - Earliest claimed: 2014-10-17 - Assignees: Massachusetts Institute of Technology - Applicants: Massachusetts Institute of Technology - Inventors: John H. Lienhard; David Elan Martin Warsinger; Jaichander Swaminathan - Web page: https://patentgrep.com/patent/US9751047B2 ## CPC - B01D 61/364: {Membrane distillation} - B01D 1/0035: {Solar energy (for treatment of water C02F1/14)} - B01D 3/145: {One step being separation by permeation} - B01D 61/366: {Apparatus therefor} - B01D 69/02: characterised by their properties - C02F 1/44: by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} - C02F 1/447: {by membrane distillation (distillation and evaporation without the use of membranes C02F1/04)} - F28F 13/04: by preventing the formation of continuous films of condensate on heat-exchange surfaces, e.g. by promoting droplet formation {(F28F13/18 takes precedence)} - B01D 2311/103: Heating - B01D 2313/221: Heat exchangers - B01D 2325/36: Hydrophilic membranes - B01D 2325/38: Hydrophobic membranes - C02F 2103/08: Seawater, e.g. for desalination - C02F 2201/002: Construction details of the apparatus - Y02W 10/37: using solar energy - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) - C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes) - F28F: DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION (water and air traps, air venting F16) - Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT ## 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. ## Claims ### Claim 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. ### Claim 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. ### Claim 3 (depends on 2) The apparatus of claim 2, wherein the feed liquid in the feed-liquid source comprises a volatile component and a less-volatile component. ### Claim 4 (depends on 2) The apparatus of claim 2, wherein the feed liquid in the feed-liquid source comprises water. ### Claim 5 (depends on 4) 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. ### Claim 6 (depends on 4) 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. ### Claim 7 (depends on 6) 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. ### Claim 8 (depends on 7) The apparatus of claim 7, wherein the polymer membrane comprises at least one of the following: polyvinylidene difluoride, polytetrafluoroethylene, and polypropylene. ### Claim 9 (depends on 2) The apparatus of claim 2, wherein the condensing surface includes copper oxide. ### Claim 10 (depends on 9) The apparatus of claim 9, wherein the copper oxide is coated with a silane. ### Claim 11 (depends on 10) The apparatus of claim 10, wherein the silane is fluorinated. ### Claim 12 (depends on 10) The apparatus of claim 10, wherein the condensing surface has a rugosity greater than 2. ### Claim 13 (depends on 2) 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. ### Claim 14 (depends on 2) The apparatus of claim 2, wherein the condensing surface is sufficiently hydrophobic to produce a contact angle with water of greater than 165°. ### Claim 15 (depends on 2) The apparatus of claim 2, wherein the condensing surface is more hydrophobic than the selectively permeable material. ### Claim 16 (depends on 2) 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. ### Claim 17 (depends on 2) The apparatus of claim 2, wherein the hydrophilic spacer comprises at least one of a polymer and a metal. ### Claim 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. ### Claim 19 (depends on 18) 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. ### Claim 20 (depends on 18) 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. ### Claim 21 (depends on 20) The method of claim 20, wherein the feed-liquid temperature is raised using a solar heat collector. ### Claim 22 (depends on 20) 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. ### Claim 23 (depends on 18) The method of claim 18, further comprising generating a below-ambient pressure in the gap when the method is performed. ### Claim 24 (depends on 23) The method of claim 23, wherein the below-ambient pressure is in a range from 10 kPa to 90 kPa absolute pressure. ### Claim 25 (depends on 18) The method of claim 18, wherein the vapor is condensed via jumping droplets. ### Claim 26 (depends on 18) The method of claim 18, wherein the vapor is condensed via drop-wise condensation.