US20210069639A1 - Water vapor harvesting materials and devices - Google Patents

Water vapor harvesting materials and devices Download PDF

Info

Publication number
US20210069639A1
US20210069639A1 US17/049,421 US201917049421A US2021069639A1 US 20210069639 A1 US20210069639 A1 US 20210069639A1 US 201917049421 A US201917049421 A US 201917049421A US 2021069639 A1 US2021069639 A1 US 2021069639A1
Authority
US
United States
Prior art keywords
water
harvesting material
atmospheric water
atmospheric
hydrogel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
US17/049,421
Other versions
US10960347B1 (en
Inventor
Peng Wang
Renyuan Li
Yifeng Shi
Mengchun WU
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
King Abdullah University of Science and Technology KAUST
Original Assignee
King Abdullah University of Science and Technology KAUST
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by King Abdullah University of Science and Technology KAUST filed Critical King Abdullah University of Science and Technology KAUST
Priority to US17/049,421 priority Critical patent/US10960347B1/en
Assigned to KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY reassignment KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LI, RENYUAN, SHI, YIFENG, WANG, PENG, WU, Mengchun
Publication of US20210069639A1 publication Critical patent/US20210069639A1/en
Application granted granted Critical
Publication of US10960347B1 publication Critical patent/US10960347B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • EFIXED CONSTRUCTIONS
    • E03WATER SUPPLY; SEWERAGE
    • E03BINSTALLATIONS OR METHODS FOR OBTAINING, COLLECTING, OR DISTRIBUTING WATER
    • E03B3/00Methods or installations for obtaining or collecting drinking water or tap water
    • E03B3/28Methods or installations for obtaining or collecting drinking water or tap water from humid air
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0027Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/06Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/261Drying gases or vapours by adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/263Drying gases or vapours by absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/28Selection of materials for use as drying agents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0222Compounds of Mn, Re
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0225Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0225Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
    • B01J20/0229Compounds of Fe
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0233Compounds of Cu, Ag, Au
    • B01J20/0237Compounds of Cu
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/024Compounds of Zn, Cd, Hg
    • B01J20/0244Compounds of Zn
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0288Halides of compounds other than those provided for in B01J20/046
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0274Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04 characterised by the type of anion
    • B01J20/0296Nitrates of compounds other than those provided for in B01J20/04
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/046Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing halogens, e.g. halides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/28Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
    • B01J20/28014Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
    • B01J20/28026Particles within, immobilised, dispersed, entrapped in or on a matrix, e.g. a resin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3202Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
    • B01J20/3206Organic carriers, supports or substrates
    • B01J20/3208Polymeric carriers, supports or substrates
    • B01J20/321Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions involving only carbon to carbon unsaturated bonds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/30Processes for preparing, regenerating, or reactivating
    • B01J20/32Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
    • B01J20/3231Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
    • B01J20/3234Inorganic material layers
    • B01J20/3236Inorganic material layers containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/02Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
    • C08J3/03Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
    • C08J3/075Macromolecular gels
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/30Alkali metal compounds
    • B01D2251/302Alkali metal compounds of lithium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/402Alkaline earth metal or magnesium compounds of magnesium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/40Alkaline earth metal or magnesium compounds
    • B01D2251/404Alkaline earth metal or magnesium compounds of calcium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2251/00Reactants
    • B01D2251/60Inorganic bases or salts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/112Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/20Organic adsorbents
    • B01D2253/202Polymeric adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/25Coated, impregnated or composite adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/80Water
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40083Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
    • B01D2259/40088Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
    • B01D2259/40098Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating with other heating means
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2333/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2333/24Homopolymers or copolymers of amides or imides
    • C08J2333/26Homopolymers or copolymers of acrylamide or methacrylamide

Definitions

  • Embodiments of the subject matter disclosed herein generally relate to a device, materials, and method for harvesting atmospheric water vapor using a polymeric hydrogel that includes a deliquescent salt and a photothermal agent.
  • Water is essential for life on this planet. Many regions of the world, however, do not have ready access to water. Further, even regions that have access to water, the available water may not be suitable for human consumption. For example, the available water may be salinated water from the ocean, which contains too much sodium for consumption in the amounts required to sustain human life.
  • an atmospheric water harvesting device should include a water sorbent capable of adsorbing large amounts of water from the air, even in relatively low humidity conditions, and capable of releasing the adsorbed water under relatively low temperatures.
  • Conventional desiccants such as silica gel, zeolite, activated alumina, typically have wide water vapor sorption window, but to efficiently release the captured water, they require high temperatures (>160° C.), which are typically beyond what simple solar photothermal based heating devices are capable of offering.
  • Document [ 1 ] discloses solid super desiccants formed from a sodium polyacrylate powder with a lithium chloride solution.
  • the desiccants can be regenerated, i.e., the absorbed water can be released, at temperatures less than 80° C.
  • Document [ 1 ] does not disclose how much lower than 80° C. the desiccants can be regenerated, heating the super desiccants to approximately 80° C. using solar radiation would require very strong sun rays.
  • the solution disclosed in Document [1] can produce water only under limited environmental conditions.
  • Document [2] discloses a hydrogel composite desiccant composed of porous Poly(N-isopropylacrylamide) impregnated by hygroscopic salt in the form of calcium chloride (CaCl 2 ). Specifically, the calcium chloride is impregnated in a thermo-responsive polymer matrix-double network Al-alginate/PNIPPAm hydrogel.
  • the hydrogel composite desiccant is a thermo-responsive polymer, which is a temperature-induced phase transfer material. When the temperature is low, the polymer exhibits hydrophilic wetting behavior in which water can be absorbed into the crosslink structure. When the temperature is higher than certain value (known as the lower critical solution temperature, LOST), the polymer converts into hydrophobic wetting behavior in which the polymer chain will shrink and extrude water.
  • LOST lower critical solution temperature
  • PNIPAAm is an electrostatically crosslinked hydrogel
  • the ion strength (i.e., concentration of salt solution) of infiltrated solution will significantly influence its phase-conversion property, which appears to be the reason why Document [2] discloses that very limited salt can be loaded into the hydrogel.
  • an atmospheric water harvesting material which includes a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent.
  • an atmospheric water harvesting material there is a method for forming an atmospheric water harvesting material.
  • a polymeric hydrogel matrix comprising a photothermal agent is formed.
  • the polymeric hydrogel matrix comprising the photothermal agent is then freeze-dried.
  • the freeze-dried polymeric hydrogel matrix comprising the photothermal agent is immersed in a solution containing deliquescent salt to form a polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt.
  • the polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt is then dried.
  • an atmospheric water harvesting device which includes a condensation chamber having a light admitting upper surface and a water outlet.
  • the device also includes an atmospheric water harvesting chamber, arranged below the condensation chamber, containing an atmospheric water harvesting material and having a bottom surface with an opening to accept ambient air and an upper surface having an opening to allow atmospheric water captured from the ambient air by the atmospheric water harvesting material to pass into the condensation chamber due to heat generated from solar energy impinging on the light admitting upper surface of the condensation chamber.
  • a method for generating water from water vapor Water vapor is absorbed by an atmospheric water harvesting material arranged on an outer surface of a cylinder.
  • the atmospheric water harvesting material includes a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent.
  • the cylinder is rotated so that a portion of the atmospheric water harvesting material that has absorbed the water vapor is facing a condensation chamber, which is arranged above the cylinder and has a light-admitting upper surface. The portion of the atmospheric water harvesting material facing the condensation chamber is exposed to solar energy passing through the light-admitting upper surface.
  • the water vapor from the portion of the atmospheric water harvesting material facing the condensation chamber is released into the condensation chamber due to the solar energy.
  • the released water vapor is condensed into water in the condensation chamber.
  • the condensed water is pure water or the water vapor is released exclusively due to the solar energy.
  • FIG. 1 is a diagram of an atmospheric water harvesting material according to embodiments
  • FIG. 2 is a flow diagram of a method for making an atmospheric water harvesting material according to embodiments
  • FIGS. 3A-3E are diagrams of the making of an atmospheric water harvesting material according to embodiments.
  • FIG. 4 is a diagram of an atmospheric water harvesting device according to embodiments.
  • FIG. 5 is a flow diagram of a method of generating water from water vapor according to embodiments.
  • FIG. 1 is a diagram illustrating an atmospheric water harvesting material 100 .
  • the atmospheric water harvesting material includes a deliquescent salt 110 , a photothermal agent 120 , and a polymeric hydrogel matrix 130 containing the deliquescent salt 110 and photothermal agent 120 .
  • the deliquescent salt 110 is in a liquid phase but is held in a solid form in the polymeric hydrogel matrix 130 .
  • the polymeric hydrogel matrix 130 comprises a cross-linked and flexible hydrogel network.
  • a photothermal agent is one that produces thermal energy in the form of heat due to photoexcitation of the agent.
  • the disclosed atmospheric water harvesting material is particularly advantageous because it is not sensitive to the ion strength of infiltrated solution, which allows it to hold more hygroscopic salt and thus exhibits a higher water capacity compared to conventional materials, such as those disclosed in Document [2]. Specifically, the disclosed atmospheric water harvesting material releases water while exhibiting a hydrophilic phase and does not require conversion to a hydrophobic phase that can exhibit salt wash out. Thus, compared to the material disclosed in Document [2], the disclosed atmospheric water harvesting material shows better durability, as well as the ability to produce pure water instead of water contaminated by salt that requires further treatment. Accordingly, the disclosed atmospheric water harvesting material can produce potable water (i.e., distilled water) from atmospheric water vapor without requiring additional, complicated post-treatment.
  • potable water i.e., distilled water
  • the inclusion of a photothermal agent in the atmospheric water harvesting material allows the atmospheric water harvesting material to generate heat under natural sunlight, which causes the atmospheric water harvesting material to heat up and evaporate out the absorbed water vapor.
  • the disclosed atmospheric water harvesting material can release water exclusively due to solar energy (i.e., it is self-heating) and does not require electricity or other heat sources that may require consumption of fossil fuels.
  • the deliquescent salt 110 is calcium chloride (CaCl 2 )).
  • the deliquescent salt 110 can be one or more of the following:
  • the photothermal agent 120 comprises carbon nanotubes (CNTs).
  • CNTs carbon nanotubes
  • the photothermal agent 120 can be one or more of the following:
  • the polymeric hydrogel matrix 130 is a poly(acrylamide) (PAM) hydrogel.
  • PAM poly(acrylamide)
  • the polymeric hydrogel matrix 130 can be comprised of one or more of the following polymers:
  • a method of making an atmospheric water harvesting material will now be described in connection with the flowchart of FIG. 2 and the diagrams of FIGS. 3A-3E .
  • this method is described with calcium chloride as the deliquescent salt, carbon nanotubes as the photothermal agent, and poly(acrylamide) (PAM) hydrogel as the hydrogel matrix, this method can employ any of the deliquescent salts, photothermal agents, and hydrogel matrices described above.
  • a polymeric hydrogel matrix comprising a photothermal agent is formed (step 210 ).
  • the carbon nanotubes are initially pretreated by dispersing, for example, 6.0 g of carbon nanotubes having a size of, for example, 6-9 nm ⁇ 5 ⁇ m, in a mixture of, for example, 70% nitric acid (60 mL) and 97% sulfuric acid (180 mL).
  • the dispersion was then refluxed for 4 hours at 70° C. followed by 2 hours of sonication.
  • the as-treated dispersion can then be filtrated and thoroughly washed by deionized water before insertion into the hydrogel matrix.
  • the hydrogel matrix is formed by dissolving, for example, 1.0 gram of acrylamide (AM) in, for example, 5 ml of the carbon nanotube dispersion with a specified amount of carbon nanotubes added (e.g., 2.5, 1.25, 0.5, 0.375, 0.25, 0.125, 0.05, 0.025 mg).
  • the acrylamide-carbon nanotube dispersion is then purged with nitrogen to eliminate dissolved oxygen.
  • FIG. 3A which illustrates acrylamide 310 and carbon nanotubes 320 suspended in deionized water 305 .
  • An initiator for example 5.00 mg of potassium peroxydisulfate (KPS), and a hydrogelling agent, for example 0.38 mg of N,N′-Methylenebis(acrylamide) (MBAA), are added into the acrylamide-carbon nanotube dispersion.
  • a hydrogelling accelerator for example, 25 ⁇ L of tetramethylethylenediamine (TEMED) is then added and the mixture is allowed to settle overnight at a temperature of, for example, 22° C.
  • TEMED tetramethylethylenediamine
  • the resulting poly(acrylamide) (PAM)-carbon nanotube hydrogel matrix 322 is illustrated in FIG. 3B , in which the hydrogel is labeled as element 325 and the poly(acrylamide) is labeled as element 330 .
  • the polymeric hydrogel matrix comprising the photothermal agent is then freeze-dried to make the hydrogel into a microporous hydrogel (step 220 ).
  • the polymeric hydrogel matrix can be freeze-dried at, for example, ⁇ 80° C.
  • the resulting microporous hydrogel is illustrated in FIG. 3C .
  • the freeze-dried polymeric hydrogel matrix comprising the photothermal agent is then immersed in a solution containing deliquescent salt to form a polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt (step 230 ).
  • the freeze-dried hydrogel can be immersed in, for example, 10 ml of a calcium chloride solution for, for example, 24 hours.
  • the drying can occur under ambient conditions, for example, 60% relative humidity and 22° C.
  • Experiments were performed using calcium chloride concentrations of 0.1, 0.2, 0.3, 0.4, 0.5, and 0.6 g/mL for 24 hours under ambient condition, for example, 60% relative humidity and 22° C.
  • the polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt is dried (step 240 ).
  • the poly(acrylamide)-carbon nanotube-calcium chloride hydrogel can be dried at 80° C. in a blast oven for three days.
  • the resulting hydrogel which is referred to herein as an atmospheric water harvesting material, is illustrated in FIG. 3E , in which the calcium chloride is labeled as element 335 .
  • the disclosed atmospheric water harvesting material can be employed in any type of water harvesting device, one example of which is illustrated in FIG. 4 .
  • the atmospheric water harvesting device 400 includes a condensation chamber 405 having a light-admitting upper surface 410 and a water outlet 415 .
  • the atmospheric water harvesting device 400 also includes an atmospheric water harvesting chamber 420 , arranged below the condensation chamber 405 , containing an atmospheric water harvesting material 425 and having a bottom surface 430 with an opening 435 to accept ambient air 440 and an upper surface 445 having an opening 450 to allow atmospheric water 455 captured from the ambient air 440 by the atmospheric water harvesting material 425 to pass into the condensation chamber 405 due to heat generated from solar energy 460 impinging on the light-admitting upper surface 410 of the condensation chamber 405 .
  • the condensation chamber 405 includes a sloped water collector 465 for moving collected water to the water outlet 415 .
  • the light-admitting surface 410 of the condensation chamber 405 should be made of a material that has minimal effect on the incoming solar energy 460 , such as, for example, quartz.
  • the atmospheric water harvesting chamber 420 comprises a cylinder 470 having an outer surface on which the atmospheric water harvesting material 425 is arranged.
  • the atmospheric water harvesting chamber 420 also includes a frame 475 surrounding the cylinder 470 .
  • the cylinder 470 includes a spindle 480 to which a motor (not illustrated) is attached. It should be recognized that the atmospheric water harvesting device 400 can include elements in addition to those that are illustrated, such as bearings on the spindle, washers, bolts, nuts, etc.
  • the cylinder 470 can be comprised of a material, such as acrylic.
  • the interior of the cylinder 470 can be empty or can be filled.
  • the side surfaces of the cylinder i.e., the surface visible in FIG. 4 ) can include holes.
  • the upper part of the cylinder 470 will be warmer than the lower part. Due to heating of the atmospheric water harvesting material 425 with the aid of the photothermal agent, water vapor is released from the cylinder 470 into the condensation chamber 405 . The water vapor will attach to the upper surface 410 and/or the side walls of the condensation chamber and water droplets will fall onto sloped water collector 465 and exit the condensation chamber 405 via the water outlet 415 .
  • the atmospheric water harvesting material 425 in the lower part of the cylinder 470 will not be heated enough to release water vapor, and thus will continue to absorb water vapor from the atmosphere.
  • the side walls of the condensation chamber 405 can be made of metal, such as copper.
  • the motor spins the cylinder 470 so that the atmospheric water harvesting material 425 in the upper part, from which water vapor has been released, is rotated to face the bottom surface 430 of the atmospheric water harvesting chamber 420 so that it can absorb water vapor from the ambient air 440 and the atmospheric water harvesting material 425 in the lower part, which has absorbed water vapor from the ambient air 440 , is rotated so that it faces the opening 450 in the atmospheric water harvesting chamber 420 so that it can be exposed to the solar energy 460 and heated to release the absorbed water vapor into the condensation chamber 405 .
  • the atmospheric water harvesting device 400 can be continuously operated so that it can continuously absorb water vapor from the ambient air 440 and discharge water vapor into the condensation chamber 405 .
  • the cylinder 470 can be rotated at a speed of, for example, 00.5, 0.75, 1.5, or 4 revolutions per hour. This is particularly advantageous because water vapor can be continuously absorbed and desorbed without further human intervention, thus making it practical for a number of implementations outside of a pure industrial implementation, such as in residential use.
  • a method for generating water from water vapor using the atmospheric water harvesting device 400 illustrated in FIG. 4 will now be described in connection with the flow diagram of FIG. 5 .
  • water vapor is absorbed by the atmospheric water harvesting material 425 arranged on an outer surface of a cylinder 470 (step 510 ).
  • the atmospheric water harvesting material 425 comprises a deliquescent salt 110 , a photothermal agent 120 , and a polymeric hydrogel matrix 130 containing the deliquescent salt 110 and photothermal agent 120 .
  • the cylinder 470 is rotated so that a portion of the atmospheric water harvesting material 425 that has absorbed the water vapor is facing a condensation chamber 405 , which is arranged above the cylinder 470 and has a light-admitting upper surface 410 (step 520 ).
  • the portion of the atmospheric water harvesting material 425 facing the condensation chamber 405 is exposed to solar energy passing through the light-admitting upper surface 410 (step 530 ).
  • the solar energy causes the water vapor to be released from the portion of the atmospheric water harvesting material 425 facing the condensation chamber 405 into the condensation chamber 405 (step 540 ).
  • the released water vapor is condensed into water in the condensation chamber 405 (step 550 ).
  • the condensed water is pure water or the water vapor is released exclusively due to the solar energy.
  • the atmospheric water harvesting device 400 can be continuously operated so that it can continuously absorb water vapor from the ambient air 440 and discharge water vapor into the condensation chamber 405 . Further, the atmospheric water harvesting material does not change phase from hydrophilic to hydrophobic while releasing the water vapor.
  • PAM-CNT-CaCl 2 poly(acrylamide)-carbon nanotube-calcium chloride hydrogel
  • PAM hydrogel poly(acrylamide)-carbon nanotube hydrogel
  • PAM-CaCl 2 hydrogel poly(acrylamide)-calcium chloride hydrogel
  • PAM hydrogel poly(acrylamide) hydrogel
  • composition of the atmospheric water harvesting material experiments were conducted with different concentrations of carbon nanotubes (i.e., with 2.5, 1.25, 0.5, 0.375, 0.25, 0.125, 0.05, and 0.025 mg) and with different concentrations of calcium chloride (i.e., 0.1, 0.2, 0.3, 0.4, 0.5, and 0.6 g/mL).
  • the amount of the acrylamide monomer precursor was optimized to be 20 wt % based on the following facts and the cost consideration.
  • the acrylamide monomer of 20 wt % is the threshold at which the PAM hydrogel exhibits a standalone solid form and has a sufficient structural stability. If the acrylamide monomer concentration is lower than 20%, the product is sticky and thick liquid-like. Second, increasing acrylamide monomer concentration to above 20 wt % does not lead to any noticeable benefit of enhanced water sorption and release.
  • the atmospheric water harvesting material is designed to release water by being exposed to solar energy
  • the light absorbance of the PAM hydrogel without carbon nanotubes and with carbon nanotubes were evaluated.
  • the PAM hydrogel without carbon nanotubes strongly absorbs near-infrared light at wavelength above 1400 nm, which is due to the light absorption by the water molecules inside the hydrogel. Adding the carbon nanotubes increased the light absorption from 240 to 1400 nm.
  • a small amount of carbon nanotubes in the hydrogel i.e., at a ppm level
  • leads to a large increase in light absorbance
  • 99% of the incident light was absorbed when the carbon nanotube loading amount was only 0.083 wt ⁇ .
  • the carbon nanotube loading in the PAM hydrogel can be set to be 0.42 ⁇ , where almost 100% of the incident light will be absorbed.
  • the water vapor sorption behavior of the calcium chloride was evaluated both by itself and when incorporated into the PAM-CNT hydrogel.
  • the water sorption behaviors of the PAM-CNT-CaCl 2 hydrogel was investigated and compared under dynamic and static humidity scenarios.
  • a constant temperature of 25° C. was set and kept throughout the water sorption process for all samples.
  • a temperature of 25° C. was selected because it is a typical in arid areas at night when water vapor sorption takes place. All samples for water sorption assessment were first dried prior testing.
  • the hydrogels were kept in a flow with a step-wise increasing humidity for certain period of time and in the static scenario the relative humidity was unchanged throughout the water sorption process.
  • the dynamic relative humidity test was first applied to PAM hydrogels and PAM-CNT hydrogels. Both exhibited a similar water sorption characteristic, with the water vapor sorption slightly higher for the dried PAM hydrogel than for the dried PAM-CNT hydrogel in the low humidity range ( ⁇ 40%) and no obvious difference in high relative humidity range. However, there was no significant difference in high humidity range.
  • the static relative humidity test indicated that the PAM hydrogel and the PAM-CNT hydrogel both gradually approached water uptake value near to its saturation capacity within 400 min, and the final weight change due to water sorption are 32 wt % and 38 wt % water in 80% relative humidity, respectively.
  • the water sorption property of the hydrogels with calcium chloride loading is very similar to that of pure calcium chloride crystal, with only slight difference in specific sorption amount, indicating that calcium chloride is primarily responsible for the water sorption of PAM-CNT-CaCl 2 ) hydrogel. Because the phase diagram of water-calcium chloride has been well studied and can be easily found in literature, it is believed that this can be used to explain the water sorption behavior of the disclosed PAM-CNT-CaCl 2 ) hydrogel.
  • the calcium chloride contains two primary stages in connection with the water sorption process. In the first stage, anhydrous calcium chloride crystal captures water molecules through hydration reaction and forms hydrates.
  • the vapor pressure of a saturated calcium chloride aqueous solution at 25° C. is 0.9 kPa, equivalent to a humidity of 26%.
  • the water sorption by calcium chloride at a relative humidity less than 26% is attributed to its increase of the hydration water, and that occurring at a relative humidity greater than 26% leads to a dilution of the calcium chloride aqueous solution, i.e., deliquescence.
  • the value 26% relative humidity value as a critical point can be varied with the ambient temperature.
  • the water sorption amount in the first stage for pure anhydrous calcium chloride is 97% ending as CaCl 2 .6H 2 O.
  • the last two water crystals are difficult to remove at a temperature lower than 160° C.
  • the samples were pre-dried at 80° C. because this is a reasonable temperature that can be achieved by photothermal heating under regular and non-concentrated sunlight. Consequently, after drying process at 80° C., the calcium chloride in the disclosed PAM-CNT-CaCl 2 hydrogel was mainly a mixture of CaCl 2 .4H 2 O and CaCl 2 .2H 2 O, which was confirmed by x-ray diffraction analysis and phase diagram.
  • PAM-CaCl 2 ) hydrogel and a PAM-CNT-CaCl 2 ) hydrogel share similar sorption trends to that of calcium chloride, but with much higher sorption rates, which might be due to the porous structure of the hydrogels.
  • the PAM-CaCl 2 ) hydrogel and the PAM-CNT-CaCl 2 ) hydrogel reached their saturation states at the definite relative humidity of 10, 35 and 60%, indicated by their sorption rate at the end of the test being quite close to zero.
  • the water evaporation rate then gradually decreases because the salt concentration in the residual water inside the hydrogel keeps increasing during this process due to the loss of water. As a result, the heat consumption by the water evaporation decreases, moving the balance to a higher equilibrium temperature.
  • the temperature of the PAM-CaCl 2 hydrogel reached 42° C. and 25% of the total weight of the hydrogel was lost to the released water. This suggests that only less than half of the water inside the PAM-CaCl 2 hydrogel was able to be released.
  • the temperature and weight variation time course of the PAM-CNT-CaCl 2 hydrogel irradiated with simulated sunlight with varied light intensity was also evaluated.
  • the temperature observed at 270 min under 0.6, 0.8 and 1.0 kW/m2 sunlight illumination was 55, 66 and 75° C., respectively.
  • the corresponding weight change of the samples was 44, 49 and 53%, respectively, corresponding to 80, 89 and 97% release of the sorbed water. This demonstrates that most of the sorbed water can still be efficiently released under weakened sunlight.
  • a cycling test was performed to evaluate the stability of the disclosed PAM-CNT-CaCl 2 hydrogel.
  • Water sorption was conducted by letting 2.5 g of the dried hydrogel sit in an open air with a relative humidity of 60% at 22° C. for 36 hours in the dark, followed by one sun irradiation for 5 hours. The whole cycle was repeated for 10 times. This experiment showed that the water sorption and release performances of the PAM-CNT-CaCl 2 hydrogel exhibited no degradation after 10 cycles, indicating its long-term operational stability.
  • the disclosed PAM-CNT-CaCl 2 hydrogel possesses outstanding water sorption capability, which is similar to calcium chloride, and its flexible solid form makes it an effective atmospheric water harvesting device. Due to the fact that the working relative humidity range of the disclosed PAM-CNT-CaCl 2 ) hydrogel covers most of arid deserts, almost all islands, and inland remote regions, the atmospheric water harvesting device based on the hydrogel are low cost, versatile, deployable, and thus suitable for delivering much needed fresh water therein. Additionally, the disclosed PAM-CNT-CaCl 2 ) hydrogel only requires solar energy to release the captured water vapor and the released water is pure water that does not contain hygroscopic or other impurities.
  • the disclosed embodiments provide an atmospheric water harvesting material, method of producing an atmospheric water harvesting material, and an atmospheric water harvesting device. It should be understood that this description is not intended to limit the invention. On the contrary, the exemplary embodiments are intended to cover alternatives, modifications and equivalents, which are included in the spirit and scope of the invention as defined by the appended claims. Further, in the detailed description of the exemplary embodiments, numerous specific details are set forth in order to provide a comprehensive understanding of the claimed invention. However, one skilled in the art would understand that various embodiments may be practiced without such specific details.

Abstract

An atmospheric water harvesting material includes a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • This application claims priority to U.S. Provisional Patent Application No. 62/672,865, filed on May 17, 2018, entitled “MATERIALS FOR SOLAR-ASSISTED ATMOSPHERIC WATER HARVESTING FOR FRESH WATER PRODUCTION,” and U.S. Provisional Patent Application No. 62/795,691, filed on Jan. 23, 2019, entitled “A SORPTION-BASED CONTINUOUS ATMOSPHERIC WATER GENERATOR (AWG) DEVICE,” the disclosures of which are incorporated herein by reference in their entirety.
  • BACKGROUND Technical Field
  • Embodiments of the subject matter disclosed herein generally relate to a device, materials, and method for harvesting atmospheric water vapor using a polymeric hydrogel that includes a deliquescent salt and a photothermal agent.
  • Discussion of the Background
  • Water is essential for life on this planet. Many regions of the world, however, do not have ready access to water. Further, even regions that have access to water, the available water may not be suitable for human consumption. For example, the available water may be salinated water from the ocean, which contains too much sodium for consumption in the amounts required to sustain human life.
  • One readily-available source of water is the Earth's atmosphere, which is accessible almost anywhere on Earth and holds approximately 12,900 billion tons of fresh water. Thus, there has been considerable research into capturing atmospheric water vapor to provide clean water for arid regions, land-locked regions, and remote communities. The most promising conventional atmospheric water harvesting devices employ a water sorbent to capture atmospheric water vapor and solar energy to release the captured atmospheric water vapor for consumption. The use of solar energy to release the captured atmospheric water is advantageous because the device does not require an external power source to desorb the captured atmospheric water from the water sorbent.
  • In order to be cost-effective and encourage wide-spread adoption, an atmospheric water harvesting device should include a water sorbent capable of adsorbing large amounts of water from the air, even in relatively low humidity conditions, and capable of releasing the adsorbed water under relatively low temperatures. Conventional desiccants, such as silica gel, zeolite, activated alumina, typically have wide water vapor sorption window, but to efficiently release the captured water, they require high temperatures (>160° C.), which are typically beyond what simple solar photothermal based heating devices are capable of offering.
  • Document [1] discloses solid super desiccants formed from a sodium polyacrylate powder with a lithium chloride solution. The desiccants can be regenerated, i.e., the absorbed water can be released, at temperatures less than 80° C. Although Document [1] does not disclose how much lower than 80° C. the desiccants can be regenerated, heating the super desiccants to approximately 80° C. using solar radiation would require very strong sun rays. Thus, the solution disclosed in Document [1] can produce water only under limited environmental conditions.
  • Document [2] discloses a hydrogel composite desiccant composed of porous Poly(N-isopropylacrylamide) impregnated by hygroscopic salt in the form of calcium chloride (CaCl2). Specifically, the calcium chloride is impregnated in a thermo-responsive polymer matrix-double network Al-alginate/PNIPPAm hydrogel. The hydrogel composite desiccant is a thermo-responsive polymer, which is a temperature-induced phase transfer material. When the temperature is low, the polymer exhibits hydrophilic wetting behavior in which water can be absorbed into the crosslink structure. When the temperature is higher than certain value (known as the lower critical solution temperature, LOST), the polymer converts into hydrophobic wetting behavior in which the polymer chain will shrink and extrude water.
  • Because PNIPAAm is an electrostatically crosslinked hydrogel, the ion strength (i.e., concentration of salt solution) of infiltrated solution will significantly influence its phase-conversion property, which appears to be the reason why Document [2] discloses that very limited salt can be loaded into the hydrogel.
  • One problem with the hydrogel disclosed in Document [2] is that it requires a heat source that is sufficient to raise the temperature of the hydrogel so that it converts to a hydrophobic phase. This typically involves a heat source that burns fossil fuels, thus requiring additional fossil fuel energy input to convert water vapor into water.
  • Another problem with the hydrogel disclosed in Document [2] relates to its water release process. When the temperature is higher than LOST, the polymer chain/crosslink will shrink due to the conversion of hydrophilicity to hydrophobicity. Thus, water is “left behind” at its original position. This process will lead to a serious salt wash out and the hygroscopic, as well as other impurities precipitated from the hydrogel, will contaminate the collected water. Further, the wash out of salt will lead to a decrease of water sorption property of sorbent, and accordingly, requires occasional addition of salt to the hydrogel to maintain its water absorption properties.
  • Thus, there is a need for an atmospheric water harvesting material that is able to absorb large amounts of atmospheric water vapor and to safely desorb the atmospheric water vapor under relatively low temperatures without requiring a fossil fuel heating source and/or that can produce pure water instead of salt contaminated water.
  • SUMMARY
  • According to an embodiment, there is an atmospheric water harvesting material, which includes a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent.
  • According to another embodiment, there is a method for forming an atmospheric water harvesting material. A polymeric hydrogel matrix comprising a photothermal agent is formed. The polymeric hydrogel matrix comprising the photothermal agent is then freeze-dried. The freeze-dried polymeric hydrogel matrix comprising the photothermal agent is immersed in a solution containing deliquescent salt to form a polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt. The polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt is then dried.
  • According to a further embodiment, there is an atmospheric water harvesting device, which includes a condensation chamber having a light admitting upper surface and a water outlet. The device also includes an atmospheric water harvesting chamber, arranged below the condensation chamber, containing an atmospheric water harvesting material and having a bottom surface with an opening to accept ambient air and an upper surface having an opening to allow atmospheric water captured from the ambient air by the atmospheric water harvesting material to pass into the condensation chamber due to heat generated from solar energy impinging on the light admitting upper surface of the condensation chamber.
  • According to another embodiment, there is a method for generating water from water vapor. Water vapor is absorbed by an atmospheric water harvesting material arranged on an outer surface of a cylinder. The atmospheric water harvesting material includes a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent. The cylinder is rotated so that a portion of the atmospheric water harvesting material that has absorbed the water vapor is facing a condensation chamber, which is arranged above the cylinder and has a light-admitting upper surface. The portion of the atmospheric water harvesting material facing the condensation chamber is exposed to solar energy passing through the light-admitting upper surface. The water vapor from the portion of the atmospheric water harvesting material facing the condensation chamber is released into the condensation chamber due to the solar energy. The released water vapor is condensed into water in the condensation chamber. The condensed water is pure water or the water vapor is released exclusively due to the solar energy.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate one or more embodiments and, together with the description, explain these embodiments. In the drawings:
  • FIG. 1 is a diagram of an atmospheric water harvesting material according to embodiments;
  • FIG. 2 is a flow diagram of a method for making an atmospheric water harvesting material according to embodiments;
  • FIGS. 3A-3E are diagrams of the making of an atmospheric water harvesting material according to embodiments;
  • FIG. 4 is a diagram of an atmospheric water harvesting device according to embodiments; and
  • FIG. 5 is a flow diagram of a method of generating water from water vapor according to embodiments.
  • DETAILED DESCRIPTION
  • The following description of the exemplary embodiments refers to the accompanying drawings. The same reference numbers in different drawings identify the same or similar elements. The following detailed description does not limit the invention. Instead, the scope of the invention is defined by the appended claims. The following embodiments are discussed, for simplicity, with regard to the terminology and structure of atmospheric water harvesting for production of water. It should be recognized, however, that the embodiments can also be employed in connection other uses of atmospheric water harvesting, including dehumidification, desiccant-assisted cooling, etc.
  • Reference throughout the specification to “one embodiment” or “an embodiment” means that a particular feature, structure or characteristic described in connection with an embodiment is included in at least one embodiment of the subject matter disclosed. Thus, the appearance of the phrases “in one embodiment” or “in an embodiment” in various places throughout the specification is not necessarily referring to the same embodiment. Further, the particular features, structures or characteristics may be combined in any suitable manner in one or more embodiments.
  • FIG. 1 is a diagram illustrating an atmospheric water harvesting material 100. The atmospheric water harvesting material includes a deliquescent salt 110, a photothermal agent 120, and a polymeric hydrogel matrix 130 containing the deliquescent salt 110 and photothermal agent 120. The deliquescent salt 110 is in a liquid phase but is held in a solid form in the polymeric hydrogel matrix 130. The polymeric hydrogel matrix 130 comprises a cross-linked and flexible hydrogel network. Those skilled in the art will appreciate that a photothermal agent is one that produces thermal energy in the form of heat due to photoexcitation of the agent.
  • The disclosed atmospheric water harvesting material is particularly advantageous because it is not sensitive to the ion strength of infiltrated solution, which allows it to hold more hygroscopic salt and thus exhibits a higher water capacity compared to conventional materials, such as those disclosed in Document [2]. Specifically, the disclosed atmospheric water harvesting material releases water while exhibiting a hydrophilic phase and does not require conversion to a hydrophobic phase that can exhibit salt wash out. Thus, compared to the material disclosed in Document [2], the disclosed atmospheric water harvesting material shows better durability, as well as the ability to produce pure water instead of water contaminated by salt that requires further treatment. Accordingly, the disclosed atmospheric water harvesting material can produce potable water (i.e., distilled water) from atmospheric water vapor without requiring additional, complicated post-treatment.
  • The inclusion of a photothermal agent in the atmospheric water harvesting material allows the atmospheric water harvesting material to generate heat under natural sunlight, which causes the atmospheric water harvesting material to heat up and evaporate out the absorbed water vapor. Thus, the disclosed atmospheric water harvesting material can release water exclusively due to solar energy (i.e., it is self-heating) and does not require electricity or other heat sources that may require consumption of fossil fuels.
  • In the illustrated embodiment, the deliquescent salt 110 is calcium chloride (CaCl2)). However, the deliquescent salt 110 can be one or more of the following:
  • Chemical formula IUPAC Name
    Chloride salt LiCl Lithium chloride
    MgCl2 Magnesium chloride
    ZnCl2 Zinc chloride
    FeCl3 Iron (III) chloride
    Nitrate salt Zn(NO3)2 Zinc nitrate
    Cu(NO3)2 Copper (II) nitrate
    Ni(NO3)2 Nickel (II) nitrate
    Mn(NO3)2 Manganese (II) nitrate
  • In the illustrated embodiment, the photothermal agent 120 comprises carbon nanotubes (CNTs). However, the photothermal agent 120 can be one or more of the following:
  • Material Composition
    Carbon black Carbon material
    Graphite
    Graphene
    Graphene oxide (GO)
    Reduced Graphene oxide (rGO)
    MXene (i.e., Ti3C2, Ti3CN, Ti4N3, 2-D structured Metal carbide,
    Mo2TiC2, etc.) metal nitride
    Black phosphorous Phosphorous
    Black titanium oxide Titanium oxide
    Nanorods Metal (i.e., Al, Ag, Au, etc.)
    Nanoparticles Metal (i.e., Al, Ag, Au, etc.)
    Nanowire Metal (i.e., Al, Ag, Au, etc.)
    Ferrous ferric oxide Iron oxide
    polypyrrole polymer
    dopamine polymer
    Metal oxides CuO, MnO2, CuCr2O4, Fe2O3,
    Fe3O4, etc.
  • In the illustrated embodiment, the polymeric hydrogel matrix 130 is a poly(acrylamide) (PAM) hydrogel. However, the polymeric hydrogel matrix 130 can be comprised of one or more of the following polymers:
  • Polymer Abbreviation
    Poly(acrylic acid) PAA
    Poly(vinyl pyrrolidone) PVP
    Poly(acrylamide) PAM
    Poly(ethylene oxide) PEO
    Poly(vinyl methyl ether) PVME
    Poly(vinyl alcohol) PVA
    Hydroxypropylcellulose HPC
    Hydroxyethylcellulose HEC
    Poly(2-hydroxyethyl vinyl ether) PHEVE
    Poly(N-isopropylacrylamide) PNIPAM
  • A method of making an atmospheric water harvesting material will now be described in connection with the flowchart of FIG. 2 and the diagrams of FIGS. 3A-3E. Although this method is described with calcium chloride as the deliquescent salt, carbon nanotubes as the photothermal agent, and poly(acrylamide) (PAM) hydrogel as the hydrogel matrix, this method can employ any of the deliquescent salts, photothermal agents, and hydrogel matrices described above.
  • Initially, a polymeric hydrogel matrix comprising a photothermal agent is formed (step 210). Specifically, the carbon nanotubes are initially pretreated by dispersing, for example, 6.0 g of carbon nanotubes having a size of, for example, 6-9 nm×5 μm, in a mixture of, for example, 70% nitric acid (60 mL) and 97% sulfuric acid (180 mL). The dispersion was then refluxed for 4 hours at 70° C. followed by 2 hours of sonication. The as-treated dispersion can then be filtrated and thoroughly washed by deionized water before insertion into the hydrogel matrix. The hydrogel matrix is formed by dissolving, for example, 1.0 gram of acrylamide (AM) in, for example, 5 ml of the carbon nanotube dispersion with a specified amount of carbon nanotubes added (e.g., 2.5, 1.25, 0.5, 0.375, 0.25, 0.125, 0.05, 0.025 mg). The acrylamide-carbon nanotube dispersion is then purged with nitrogen to eliminate dissolved oxygen. The results of this is illustrated in FIG. 3A, which illustrates acrylamide 310 and carbon nanotubes 320 suspended in deionized water 305.
  • An initiator, for example 5.00 mg of potassium peroxydisulfate (KPS), and a hydrogelling agent, for example 0.38 mg of N,N′-Methylenebis(acrylamide) (MBAA), are added into the acrylamide-carbon nanotube dispersion. A hydrogelling accelerator, for example, 25 μL of tetramethylethylenediamine (TEMED) is then added and the mixture is allowed to settle overnight at a temperature of, for example, 22° C. The resulting poly(acrylamide) (PAM)-carbon nanotube hydrogel matrix 322 is illustrated in FIG. 3B, in which the hydrogel is labeled as element 325 and the poly(acrylamide) is labeled as element 330.
  • The polymeric hydrogel matrix comprising the photothermal agent is then freeze-dried to make the hydrogel into a microporous hydrogel (step 220). The polymeric hydrogel matrix can be freeze-dried at, for example, −80° C. The resulting microporous hydrogel is illustrated in FIG. 3C.
  • The freeze-dried polymeric hydrogel matrix comprising the photothermal agent is then immersed in a solution containing deliquescent salt to form a polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt (step 230). For example, the freeze-dried hydrogel can be immersed in, for example, 10 ml of a calcium chloride solution for, for example, 24 hours. The drying can occur under ambient conditions, for example, 60% relative humidity and 22° C. Experiments were performed using calcium chloride concentrations of 0.1, 0.2, 0.3, 0.4, 0.5, and 0.6 g/mL for 24 hours under ambient condition, for example, 60% relative humidity and 22° C. Based on experimentation, the highest loading of calcium chloride and the highest water vapor sorption capacity occurred with a calcium chloride concentration of 0.4 g/mL. The resulting hydrogel is illustrated in FIG. 3D, in which the calcium chloride is not visible because it is suspended in the solution.
  • Finally, the polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt is dried (step 240). For example, the poly(acrylamide)-carbon nanotube-calcium chloride hydrogel can be dried at 80° C. in a blast oven for three days. The resulting hydrogel, which is referred to herein as an atmospheric water harvesting material, is illustrated in FIG. 3E, in which the calcium chloride is labeled as element 335.
  • The disclosed atmospheric water harvesting material can be employed in any type of water harvesting device, one example of which is illustrated in FIG. 4. The atmospheric water harvesting device 400 includes a condensation chamber 405 having a light-admitting upper surface 410 and a water outlet 415. The atmospheric water harvesting device 400 also includes an atmospheric water harvesting chamber 420, arranged below the condensation chamber 405, containing an atmospheric water harvesting material 425 and having a bottom surface 430 with an opening 435 to accept ambient air 440 and an upper surface 445 having an opening 450 to allow atmospheric water 455 captured from the ambient air 440 by the atmospheric water harvesting material 425 to pass into the condensation chamber 405 due to heat generated from solar energy 460 impinging on the light-admitting upper surface 410 of the condensation chamber 405. As illustrated, the condensation chamber 405 includes a sloped water collector 465 for moving collected water to the water outlet 415. Further, the light-admitting surface 410 of the condensation chamber 405 should be made of a material that has minimal effect on the incoming solar energy 460, such as, for example, quartz.
  • The atmospheric water harvesting chamber 420 comprises a cylinder 470 having an outer surface on which the atmospheric water harvesting material 425 is arranged. The atmospheric water harvesting chamber 420 also includes a frame 475 surrounding the cylinder 470. The cylinder 470 includes a spindle 480 to which a motor (not illustrated) is attached. It should be recognized that the atmospheric water harvesting device 400 can include elements in addition to those that are illustrated, such as bearings on the spindle, washers, bolts, nuts, etc.
  • The cylinder 470 can be comprised of a material, such as acrylic. The interior of the cylinder 470 can be empty or can be filled. The side surfaces of the cylinder (i.e., the surface visible in FIG. 4) can include holes. Thus, when there is solar energy 460 impinging upon the cylinder 470, the upper part of the cylinder 470 will be warmer than the lower part. Due to heating of the atmospheric water harvesting material 425 with the aid of the photothermal agent, water vapor is released from the cylinder 470 into the condensation chamber 405. The water vapor will attach to the upper surface 410 and/or the side walls of the condensation chamber and water droplets will fall onto sloped water collector 465 and exit the condensation chamber 405 via the water outlet 415. At the same time, the atmospheric water harvesting material 425 in the lower part of the cylinder 470 will not be heated enough to release water vapor, and thus will continue to absorb water vapor from the atmosphere. In order to assist with the condensation of the water vapor, the side walls of the condensation chamber 405 can be made of metal, such as copper.
  • Thus, as will be appreciated, the motor spins the cylinder 470 so that the atmospheric water harvesting material 425 in the upper part, from which water vapor has been released, is rotated to face the bottom surface 430 of the atmospheric water harvesting chamber 420 so that it can absorb water vapor from the ambient air 440 and the atmospheric water harvesting material 425 in the lower part, which has absorbed water vapor from the ambient air 440, is rotated so that it faces the opening 450 in the atmospheric water harvesting chamber 420 so that it can be exposed to the solar energy 460 and heated to release the absorbed water vapor into the condensation chamber 405.
  • By attached a motor to the cylinder 470, the atmospheric water harvesting device 400 can be continuously operated so that it can continuously absorb water vapor from the ambient air 440 and discharge water vapor into the condensation chamber 405. The cylinder 470 can be rotated at a speed of, for example, 00.5, 0.75, 1.5, or 4 revolutions per hour. This is particularly advantageous because water vapor can be continuously absorbed and desorbed without further human intervention, thus making it practical for a number of implementations outside of a pure industrial implementation, such as in residential use.
  • A method for generating water from water vapor using the atmospheric water harvesting device 400 illustrated in FIG. 4 will now be described in connection with the flow diagram of FIG. 5. Initially, water vapor is absorbed by the atmospheric water harvesting material 425 arranged on an outer surface of a cylinder 470 (step 510). The atmospheric water harvesting material 425 comprises a deliquescent salt 110, a photothermal agent 120, and a polymeric hydrogel matrix 130 containing the deliquescent salt 110 and photothermal agent 120. The cylinder 470 is rotated so that a portion of the atmospheric water harvesting material 425 that has absorbed the water vapor is facing a condensation chamber 405, which is arranged above the cylinder 470 and has a light-admitting upper surface 410 (step 520). The portion of the atmospheric water harvesting material 425 facing the condensation chamber 405 is exposed to solar energy passing through the light-admitting upper surface 410 (step 530). The solar energy causes the water vapor to be released from the portion of the atmospheric water harvesting material 425 facing the condensation chamber 405 into the condensation chamber 405 (step 540). The released water vapor is condensed into water in the condensation chamber 405 (step 550). The condensed water is pure water or the water vapor is released exclusively due to the solar energy.
  • When the portion of the atmospheric water harvesting material 425 is facing a condensation chamber 405 a second portion of the atmospheric water harvesting material 425 is not directly exposed to the solar energy and the second portion of the atmospheric water harvesting material absorbs water vapor. Accordingly, the atmospheric water harvesting device 400 can be continuously operated so that it can continuously absorb water vapor from the ambient air 440 and discharge water vapor into the condensation chamber 405. Further, the atmospheric water harvesting material does not change phase from hydrophilic to hydrophobic while releasing the water vapor.
  • A number of experiments were conducted on the atmospheric water harvesting material comprising the poly(acrylamide)-carbon nanotube-calcium chloride hydrogel (hereinafter “PAM-CNT-CaCl2) hydrogel”), as well as a poly(acrylamide)-carbon nanotube hydrogel (hereinafter “PAM-CNT hydrogel”), poly(acrylamide)-calcium chloride hydrogel (hereinafter “PAM-CaCl2) hydrogel”), and a poly(acrylamide) hydrogel (hereinafter “PAM hydrogel”).
  • With regard to composition of the atmospheric water harvesting material, experiments were conducted with different concentrations of carbon nanotubes (i.e., with 2.5, 1.25, 0.5, 0.375, 0.25, 0.125, 0.05, and 0.025 mg) and with different concentrations of calcium chloride (i.e., 0.1, 0.2, 0.3, 0.4, 0.5, and 0.6 g/mL). The experiments demonstrated that the structure rigidity of the hydrogel is strongly dependent on the amount of the polymer in the hydrogel, which can be modulated by changing the amount of acrylamide monomer in the synthesis process. The amount of the acrylamide monomer precursor was optimized to be 20 wt % based on the following facts and the cost consideration. First, the acrylamide monomer of 20 wt % is the threshold at which the PAM hydrogel exhibits a standalone solid form and has a sufficient structural stability. If the acrylamide monomer concentration is lower than 20%, the product is sticky and thick liquid-like. Second, increasing acrylamide monomer concentration to above 20 wt % does not lead to any noticeable benefit of enhanced water sorption and release.
  • Because the atmospheric water harvesting material is designed to release water by being exposed to solar energy, the light absorbance of the PAM hydrogel without carbon nanotubes and with carbon nanotubes were evaluated. The PAM hydrogel without carbon nanotubes strongly absorbs near-infrared light at wavelength above 1400 nm, which is due to the light absorption by the water molecules inside the hydrogel. Adding the carbon nanotubes increased the light absorption from 240 to 1400 nm. Experiments demonstrated that a small amount of carbon nanotubes in the hydrogel (i.e., at a ppm level) leads to a large increase in light absorbance. Experiments demonstrated that 99% of the incident light was absorbed when the carbon nanotube loading amount was only 0.083 wt ‰. In one embodiment, the carbon nanotube loading in the PAM hydrogel can be set to be 0.42‰, where almost 100% of the incident light will be absorbed.
  • The water vapor sorption behavior of the calcium chloride was evaluated both by itself and when incorporated into the PAM-CNT hydrogel. The experiments demonstrated that the white solid salt was fully liquidized to a colorless transparent solution after the calcium chloride salt was exposed in 60% relative humidity conditions and that after water sorption, the PAM-CNT-CaCl2 hydrogel significantly expanded but still in a solid form like a soft rubber.
  • The water sorption behaviors of the PAM-CNT-CaCl2 hydrogel was investigated and compared under dynamic and static humidity scenarios. A constant temperature of 25° C. was set and kept throughout the water sorption process for all samples. A temperature of 25° C. was selected because it is a typical in arid areas at night when water vapor sorption takes place. All samples for water sorption assessment were first dried prior testing. In the dynamic scenario, the hydrogels were kept in a flow with a step-wise increasing humidity for certain period of time and in the static scenario the relative humidity was unchanged throughout the water sorption process.
  • The dynamic relative humidity test was first applied to PAM hydrogels and PAM-CNT hydrogels. Both exhibited a similar water sorption characteristic, with the water vapor sorption slightly higher for the dried PAM hydrogel than for the dried PAM-CNT hydrogel in the low humidity range (<40%) and no obvious difference in high relative humidity range. However, there was no significant difference in high humidity range. The static relative humidity test indicated that the PAM hydrogel and the PAM-CNT hydrogel both gradually approached water uptake value near to its saturation capacity within 400 min, and the final weight change due to water sorption are 32 wt % and 38 wt % water in 80% relative humidity, respectively.
  • Further relative humidity experiments were performed using a PAM-CaCl2) hydrogel and a PAM-CNT-CaCl2) hydrogel. Both of these exhibited a similar relative humidity-dependent water vapor sorption trend in dynamic water sorption measurement. Specifically, for both, the water sorption started at a very low humidity of 5%, and then gradually increased with the increase of humidity, with much higher water sorption amounts than the hydrogels without calcium chloride loading under otherwise the same condition. With a relative humidity of 10, 35, 60 and 80%, the water sorption amounts at the end of the experiment were respectively 6, 72, 116, 203% for the PAM-CaCl2) hydrogel, and were respectively 5, 69, 110, 173% for the PAM-CNT-CaCl2) hydrogel. The amount of water sorbed by the PAM-CaCl2) hydrogel and the PAM-CNT-CaCl2) hydrogel at 80% humidity were 6.3 and 4.5 times the weight of the respective hydrogels before loading with calcium chloride, which clearly demonstrates the effectiveness of calcium chloride in water sorption.
  • The water sorption property of the hydrogels with calcium chloride loading is very similar to that of pure calcium chloride crystal, with only slight difference in specific sorption amount, indicating that calcium chloride is primarily responsible for the water sorption of PAM-CNT-CaCl2) hydrogel. Because the phase diagram of water-calcium chloride has been well studied and can be easily found in literature, it is believed that this can be used to explain the water sorption behavior of the disclosed PAM-CNT-CaCl2) hydrogel. The calcium chloride contains two primary stages in connection with the water sorption process. In the first stage, anhydrous calcium chloride crystal captures water molecules through hydration reaction and forms hydrates. After the calcium chloride sorbs enough water and forms CaCl2.6H2O, it is then dissolved in the sorbed water as more water is sorbed. The vapor pressure of a saturated calcium chloride aqueous solution at 25° C. is 0.9 kPa, equivalent to a humidity of 26%. In other words, the water sorption by calcium chloride at a relative humidity less than 26% is attributed to its increase of the hydration water, and that occurring at a relative humidity greater than 26% leads to a dilution of the calcium chloride aqueous solution, i.e., deliquescence. It should be noted that the value 26% relative humidity value as a critical point can be varied with the ambient temperature.
  • Theoretically, the water sorption amount in the first stage for pure anhydrous calcium chloride is 97% ending as CaCl2.6H2O. However, the last two water crystals are difficult to remove at a temperature lower than 160° C. In the experiments, the samples were pre-dried at 80° C. because this is a reasonable temperature that can be achieved by photothermal heating under regular and non-concentrated sunlight. Consequently, after drying process at 80° C., the calcium chloride in the disclosed PAM-CNT-CaCl2 hydrogel was mainly a mixture of CaCl2.4H2O and CaCl2.2H2O, which was confirmed by x-ray diffraction analysis and phase diagram. Because, in the experiments, 4 grams of calcium chloride was loaded into 1 gram of PAM-CNT hydrogel (⅘ of overall weight), the loading ratio of calcium chloride was 80%. The overall weight change contributed by hydration reaction should be insignificant during water sorption process, i.e., less than 30%, which is small portion of the final water sorption amount. This analysis indicates that most of the water sorption for the hydrogel material is contributed by deliquesce of the calcium chloride aqueous solution. The amount of water sorbed during deliquescent stage is highly dependent on humidity of the surroundings. Therefore, the sorption continuously increases with the increase of humidity, which gives calcium chloride a broad sorption window.
  • Derivative weight change based on the results obtained from the static relative humidity test was employed to investigate the water sorption kinetics of calcium chloride, PAM-CaCl2) hydrogel, and PAM-CNT-CaCl2) hydrogel. All three samples exhibited a small sorption rate at a relative humidity of 10% in the first 200 mins, and the sorption rate quickly decreases to near zero after 200 min, implying a quick but small water uptake at a relative humidity of 10%. When the relative humidity was less than 10%, PAM-CaCl2) hydrogel and a PAM-CNT-CaCl2) hydrogel share similar sorption trends to that of calcium chloride, but with much higher sorption rates, which might be due to the porous structure of the hydrogels. During the period of the static relative humidity test (i.e., 1,000 min), the PAM-CaCl2) hydrogel and the PAM-CNT-CaCl2) hydrogel reached their saturation states at the definite relative humidity of 10, 35 and 60%, indicated by their sorption rate at the end of the test being quite close to zero. However, at a relative humidity of 35, 60 and 80%, pristine calcium chloride salt failed to reach its saturation state within 1,000 min, which might be attributed to its liquid characteristic after deliquescence. Presumably, water sorption only occurs and is controlled by boundary layer at the air on the calcium chloride solution interface.
  • By comparing the results of three batches of the samples all together, the following conclusions can be made: (1) the water sorption performance of PAM-CaCl2) hydrogel and PAM-CNT-CaCl2) hydrogel are mainly contributed by calcium chloride; (2) the hydrogel substrate does not suppress the overall water sorption performance; and (3) the hydrogel platform not only provides physical stability of the atmospheric water harvesting device but also enhances the water sorption kinetics, leading to a faster vapor sorption rate than pristine calcium chloride salt.
  • In an atmospheric water harvesting device, water is released under the help of sunlight via photothermal effect to increase the temperature of the sorbent. Accordingly, the water release performance of the hydrogels was investigated using a simulated sunlight source in lab. PAM-CaCl2) hydrogel and PAM-CNT-CaCl2) hydrogel samples were first stored at room temperature in air with a relative humidity of 60% for 36 hours to ensure a full water sorption. The water content of these two water-saturated hydrogels was 53.7% for the PAM-CaCl2) hydrogel and 54.5% for the PAM-CNT-CaCl2) hydrogel. 5.0 g of the water-saturated hydrogels were exposed under a simulated sunlight with an intensity of 1 kW/m2 for water releasing. The surface temperature of the PAM-CaCl2) hydrogel only increased to 35° C. under the light illumination for 50 mins, and then slowly increased to approximately 42° C. after 275 mins. The temperature increase is mainly attributed to the light sorption by water in this case, as discussed above. The surface temperature of the hydrogel is determined by its energy balance. In the initial stage of 50 mins light illumination, there was a relatively fast water release, which takes away a large amount of heat and thus leads to a low temperature of the hydrogel. The water evaporation rate then gradually decreases because the salt concentration in the residual water inside the hydrogel keeps increasing during this process due to the loss of water. As a result, the heat consumption by the water evaporation decreases, moving the balance to a higher equilibrium temperature. At the end of the experiment, the temperature of the PAM-CaCl2 hydrogel reached 42° C. and 25% of the total weight of the hydrogel was lost to the released water. This suggests that only less than half of the water inside the PAM-CaCl2 hydrogel was able to be released.
  • Regarding the disclosed PAM-CNT-CaCl2 hydrogel, its surface temperature jumped to 50° C. initially at 25 mins, which is 15° C. higher than that of the PAM-CaCl2 hydrogel. This comparison convincingly demonstrates the great photothermal effect of the carbon nanotubes in the hydrogel. It should be noted that, due to its higher temperature, the PAM-CNT-CaCl2 hydrogel had a much higher evaporation rate than the PAM-CaCl2 hydrogel. The water evaporation rate then gradually decreased along with the increase of the surface temperature. The temperature recorded in the end was 75° C. and the weight change % was −53% at the end of 270 min for the PAM-CNT-CaCl2 hydrogel, indicating almost all (>97%) sorbed water inside the PAM-CNT-CaCl2 hydrogel was released. With most of the available water being released from the hydrogel, the heat loss via convection, radiation, and conduction are the major energy consumption to balance the constant solar input, and therefore the hydrogel temperature profile exhibits a plateau in the last stage from 180 min to 270 min.
  • The temperature and weight variation time course of the PAM-CNT-CaCl2 hydrogel irradiated with simulated sunlight with varied light intensity was also evaluated. The temperature observed at 270 min under 0.6, 0.8 and 1.0 kW/m2 sunlight illumination was 55, 66 and 75° C., respectively. The corresponding weight change of the samples was 44, 49 and 53%, respectively, corresponding to 80, 89 and 97% release of the sorbed water. This demonstrates that most of the sorbed water can still be efficiently released under weakened sunlight. These photothermal-assisted water release experiments indicate that the disclosed PAM-CNT-CaCl2 hydrogel has a great potential as an efficient atmospheric water harvesting device working within a wide range of relative humidity and sunlight conditions.
  • A cycling test was performed to evaluate the stability of the disclosed PAM-CNT-CaCl2 hydrogel. Water sorption was conducted by letting 2.5 g of the dried hydrogel sit in an open air with a relative humidity of 60% at 22° C. for 36 hours in the dark, followed by one sun irradiation for 5 hours. The whole cycle was repeated for 10 times. This experiment showed that the water sorption and release performances of the PAM-CNT-CaCl2 hydrogel exhibited no degradation after 10 cycles, indicating its long-term operational stability.
  • In conclusion, the disclosed PAM-CNT-CaCl2 hydrogel possesses outstanding water sorption capability, which is similar to calcium chloride, and its flexible solid form makes it an effective atmospheric water harvesting device. Due to the fact that the working relative humidity range of the disclosed PAM-CNT-CaCl2) hydrogel covers most of arid deserts, almost all islands, and inland remote regions, the atmospheric water harvesting device based on the hydrogel are low cost, versatile, deployable, and thus suitable for delivering much needed fresh water therein. Additionally, the disclosed PAM-CNT-CaCl2) hydrogel only requires solar energy to release the captured water vapor and the released water is pure water that does not contain hygroscopic or other impurities.
  • The disclosed embodiments provide an atmospheric water harvesting material, method of producing an atmospheric water harvesting material, and an atmospheric water harvesting device. It should be understood that this description is not intended to limit the invention. On the contrary, the exemplary embodiments are intended to cover alternatives, modifications and equivalents, which are included in the spirit and scope of the invention as defined by the appended claims. Further, in the detailed description of the exemplary embodiments, numerous specific details are set forth in order to provide a comprehensive understanding of the claimed invention. However, one skilled in the art would understand that various embodiments may be practiced without such specific details.
  • Although the features and elements of the present exemplary embodiments are described in the embodiments in particular combinations, each feature or element can be used alone without the other features and elements of the embodiments or in various combinations with or without other features and elements disclosed herein.
  • This written description uses examples of the subject matter disclosed to enable any person skilled in the art to practice the same, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the subject matter is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims.
  • CITED DOCUMENTS
    • [1] Yang et al., Development of Solid Super Desiccants Based on a Polymeric Superabsorbent Hydrogel Composite, RSC Adv., 2015, 5, 59583-59590.
    • [2] Cui et al., Fast Superabsorbent Thermo-Responsive Hydrogel Composite Desiccant with Low Regeneration Temperature (2018).

Claims (20)

1. An atmospheric water harvesting material, comprising:
a deliquescent salt;
a photothermal agent; and
a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent.
2. The atmospheric water harvesting material of claim 1, wherein deliquescent salt is in a liquid phase but held in a solid form in the polymeric hydrogel matrix.
3. The atmospheric water harvesting material of claim 1, wherein the deliquescent salt is a chloride salt or a nitrate salt.
4. The atmospheric water harvesting material of claim 3, wherein the deliquescent salt is a chloride salt comprising lithium chloride, LiCl, calcium chloride, CaCl2), magnesium chloride, MgCl2, zinc chloride, iron (III) chloride, FeCl3, or zinc nitrate, Zn(NO3)2.
5. The atmospheric water harvesting material of claim 3, wherein the deliquescent salt is a nitrate salt comprising copper (II) nitrate, Cu(NO3)2, nickel (II) nitrate, Ni(NO3)2, or manganese (II) nitrate, Mn(NO3)2.
6. The atmospheric water harvesting material of claim 1, wherein the polymeric hydrogel matrix comprises at least one of the following polymers:
poly(acrylic acid), PAA;
poly(vinyl pyrrolidone), PVP;
poly(acrylamide), PAM;
poly(ethylene oxide), PEO;
poly(vinyl methyl ether), PVME;
poly(vinyl alcohol), PVA;
hydroxypropylcellulose, HPC;
hydroxyethylcellulose, HEC;
poly(2-hydroxyethyl vinyl ether), PHEVE; and
poly(N-isopropylacrylamide) PNIPAM.
7. The atmospheric water harvesting material of claim 1, wherein the photothermal agent comprises one or more of the following:
a carbon material;
a two-dimensional metal carbide;
a two-dimensional metal nitride;
phosphorus;
titanium oxide;
metal nanomaterial;
iron oxide;
a polymer; and
a metal oxide.
8. The atmospheric water harvesting material of claim 1, wherein the photothermal agent comprises one or more of the following:
carbon black;
graphite;
graphene;
graphene oxide, GO;
carbon nanotubes, CNTs;
an MXene;
black phosphorous;
black titanium oxide;
metal nanorods;
metal nanoparticles;
metal nanowire;
ferrous ferric oxide;
polypyrrole;
dopamine; and
a metal oxide.
9. The atmospheric water harvesting material of claim 1, wherein the atmospheric water harvesting material captures atmospheric water having a relative humidity in a range of 15%-100%.
10. The atmospheric water harvesting material of claim 1, wherein the polymeric hydrogel matrix comprises a cross-linked and flexible hydrogel network.
11. A method for forming an atmospheric water harvesting material, the method comprising:
forming polymeric hydrogel matrix comprising a photothermal agent;
freeze-drying the polymeric hydrogel matrix comprising the photothermal agent; and
immersing the freeze-dried polymeric hydrogel matrix comprising the photothermal agent in a solution containing deliquescent salt to form a polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt; and
drying the polymeric hydrogel matrix comprising the photothermal agent and the deliquescent salt.
12. The method of claim 11, wherein the formation of the polymeric hydrogel matrix comprising the photothermal agent comprises:
dissolving a polymer precursor in a dispersion of the photothermal agent to form a dispersion of the polymer precursor and the photothermal agent;
eliminating dissolved oxygen in the dispersion of the polymer precursor and the photothermal agent; and
adding a hydrogelling initiator and a hydrogelling agent to the dispersion of the polymer precursor and the photothermal agent.
13. The method of claim 12, further comprising:
adding a hydrogelling accelerator to the composition of the polymer precursor, photothermal agent, hydrogelling initiator, and hydrogelling agent.
14. The method of claim 12, wherein the elimination of dissolved oxygen comprises:
purging the dispersion of the polymer precursor and the photothermal agent with nitrogen.
15-20. (canceled)
21. A method for generating water from water vapor, the method comprising:
absorbing water vapor by an atmospheric water harvesting material arranged on an outer surface of a cylinder, wherein the atmospheric water harvesting material comprises a deliquescent salt, a photothermal agent, and a polymeric hydrogel matrix containing the deliquescent salt and photothermal agent;
rotating the cylinder so that a portion of the atmospheric water harvesting material that has absorbed the water vapor is facing a condensation chamber, which is arranged above the cylinder and has a light-admitting upper surface;
exposing the portion of the atmospheric water harvesting material facing the condensation chamber to solar energy passing through the light-admitting upper surface;
releasing, due to the solar energy, the water vapor from the portion of the atmospheric water harvesting material facing the condensation chamber into the condensation chamber; and
condensing in the condensation chamber, the released water vapor into water,
wherein the condensed water is pure water or the water vapor is released exclusively due to the solar energy.
22. The method of claim 21, wherein when the portion of the atmospheric water harvesting material is facing a condensation chamber, a second portion of the atmospheric water harvesting material is not directly exposed to the solar energy, the method further comprising:
absorbing water vapor by the second portion of the atmospheric water harvesting material.
23. The method of claim 21, wherein the atmospheric water harvesting material does not change phase from hydrophilic to hydrophobic while releasing the water vapor.
24. The method of claim 21, wherein the condensed water is pure water.
25. The method of claim 21, wherein the water vapor is released exclusively due to the solar energy.
US17/049,421 2018-05-17 2019-04-03 Water vapor harvesting materials and devices Active US10960347B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US17/049,421 US10960347B1 (en) 2018-05-17 2019-04-03 Water vapor harvesting materials and devices

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US201862672865P 2018-05-17 2018-05-17
US201962795691P 2019-01-23 2019-01-23
PCT/IB2019/052726 WO2019220225A1 (en) 2018-05-17 2019-04-03 Water vapor harvesting materials and devices
US17/049,421 US10960347B1 (en) 2018-05-17 2019-04-03 Water vapor harvesting materials and devices

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2019/052726 A-371-Of-International WO2019220225A1 (en) 2018-05-17 2019-04-03 Water vapor harvesting materials and devices

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US17/181,532 Division US20210178321A1 (en) 2018-05-17 2021-02-22 Water vapor harvesting materials and devices

Publications (2)

Publication Number Publication Date
US20210069639A1 true US20210069639A1 (en) 2021-03-11
US10960347B1 US10960347B1 (en) 2021-03-30

Family

ID=66397370

Family Applications (3)

Application Number Title Priority Date Filing Date
US17/049,421 Active US10960347B1 (en) 2018-05-17 2019-04-03 Water vapor harvesting materials and devices
US17/181,532 Abandoned US20210178321A1 (en) 2018-05-17 2021-02-22 Water vapor harvesting materials and devices
US18/210,181 Pending US20230321595A1 (en) 2018-05-17 2023-06-15 Water vapor harvesting materials and devices

Family Applications After (2)

Application Number Title Priority Date Filing Date
US17/181,532 Abandoned US20210178321A1 (en) 2018-05-17 2021-02-22 Water vapor harvesting materials and devices
US18/210,181 Pending US20230321595A1 (en) 2018-05-17 2023-06-15 Water vapor harvesting materials and devices

Country Status (3)

Country Link
US (3) US10960347B1 (en)
CN (2) CN112135676B (en)
WO (1) WO2019220225A1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20210299607A1 (en) * 2020-03-24 2021-09-30 The Johns Hopkins University Water harvesting device
CN113956531A (en) * 2021-09-24 2022-01-21 桂林电子科技大学 Polymer-based composite material with water storage and photo-thermal water purification functions and preparation method thereof
CN114452954A (en) * 2022-02-14 2022-05-10 北京大学 Heat-conducting water vapor adsorbent and preparation method and application thereof
US20220219116A1 (en) * 2019-05-28 2022-07-14 W. L. Gore & Associates, Inc. Apparatus comprising a contaminant-resistant and non-corrosive desiccant composite with high moisture capacity
CN114940799A (en) * 2022-06-14 2022-08-26 天津工业大学 Preparation method of core-shell structure PAA-PNIPAAm hydrogel material for collecting environmental water
CN115232331A (en) * 2022-08-22 2022-10-25 兰州理工大学 MPAE conductive composite hydrogel and preparation method and application thereof
CN116001368A (en) * 2023-01-30 2023-04-25 上海交通大学 Adsorption type passive cooling composite backboard for photovoltaic module and photovoltaic module
CN116180446A (en) * 2023-03-10 2023-05-30 天津工业大学 Preparation method of PNIPAAm hydrogel-based raised fabric with super-strong moisture absorption and water release

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112135676B (en) * 2018-05-17 2022-06-03 阿卜杜拉国王科技大学 Material and device for collecting water vapor
CN112107547A (en) * 2020-10-16 2020-12-22 温州医科大学附属第二医院(温州医科大学附属育英儿童医院) Hydrogel microsphere with photo-thermal responsiveness and preparation method and application thereof
CN112902315B (en) * 2021-01-13 2022-02-11 常州大学 Circulation dehumidification cooling system
CN113083213B (en) * 2021-04-07 2022-08-09 西南科技大学 Single-layer MXene colloid and preparation method and application thereof
CN113456837B (en) * 2021-07-14 2022-12-02 山西医科大学 MXene @ BSA nano diagnosis and treatment agent with controllable size and preparation and application thereof
GB202113190D0 (en) * 2021-09-15 2021-10-27 Ahbstra Eng Ltd Atmospheric water harvesting device and method
CN113789025B (en) * 2021-09-30 2022-11-11 华东理工大学 Xerogel for removing organic solvent micro-water and preparation method and application thereof
CN113816455B (en) * 2021-10-19 2022-12-20 华东理工大学 Two-dimensional tricotitanium carbide/titanium dioxide heterojunction-based film and preparation method and application thereof
CN113929826B (en) * 2021-11-17 2023-12-05 浙江理工大学 Neuron-like composite conductive hydrogel and multifunctional flexible sensor
CN114259953B (en) * 2021-12-31 2023-01-31 杭州电子科技大学 P-CaCl 2 -Cr-MOF aerogel material, and preparation method and application thereof
CN114316750B (en) * 2022-01-05 2022-06-07 方亨 Method for improving corrosion resistance of vinyl resin
WO2023214221A1 (en) * 2022-05-05 2023-11-09 Chiaphua Industries Ltd Composition and making of self-forming, continuous-release antimicrobial air gel
CN115975262A (en) * 2022-12-13 2023-04-18 成都理工大学 Solar-driven high-strength atmospheric water-collecting composite material, and preparation method and application thereof
CN116159546A (en) * 2023-02-14 2023-05-26 干霸干燥剂(深圳)有限公司 High-moisture-absorption resin desiccant and preparation method thereof
CN116371379A (en) * 2023-04-13 2023-07-04 陕西科技大学 rGO@PPy adsorption-photo-thermal composite material and preparation method and application thereof

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2810269A1 (en) * 1978-03-09 1979-09-20 Mittex Ag PLANT FOR RECOVERING WATER FROM THE AIR AND PROCESSES FOR ITS OPERATION
DE2935697C2 (en) * 1979-09-04 1983-03-17 Mittex AG, 9490 Vaduz Method and device for obtaining water from air
JPS5726331A (en) * 1980-07-24 1982-02-12 Toyobo Co Ltd Air cooling system and air conditioning system using activated carbon fiber
NO943534L (en) * 1994-09-23 1996-03-25 Krupec V Per Kaare Krumsvik Method of collecting water from humidity
RU2131000C1 (en) * 1998-02-25 1999-05-27 Алексеев Вячеслав Викторович Installation for fresh water condensation from atmospheric air
IL124978A (en) * 1998-06-17 2003-01-12 Watertech M A S Ltd Method and apparatus for extracting water from atmospheric air
US6574979B2 (en) * 2000-07-27 2003-06-10 Fakieh Research & Development Production of potable water and freshwater needs for human, animal and plants from hot and humid air
CN1124386C (en) * 2001-02-13 2003-10-15 大连冰山集团有限公司 Adsorption-type solar water generator with air as raw material
WO2003025295A1 (en) * 2001-09-20 2003-03-27 Norman Arrison Method and apparatus for producing potable drinking water from air
AU2004243388B2 (en) * 2003-05-26 2010-09-16 Logos-Innovationen Gmbh Device for the extraction of water from atmospheric air
US7467523B2 (en) * 2003-08-26 2008-12-23 Aqwest, Llc Autonomous water source
WO2009153634A1 (en) * 2008-06-19 2009-12-23 University Of Witwatersrand, Johannesburg A transmucosal delivery system
DE102010047788B4 (en) * 2010-10-08 2017-04-27 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. System for obtaining water by absorbing atmospheric moisture from the environment
MX340967B (en) * 2010-11-25 2016-08-01 Monique Lehky Hagen Extraction of water from air.
US9433682B2 (en) * 2012-02-23 2016-09-06 University South Florida Graphene hydrogel and method for using the same
US9382401B2 (en) * 2012-07-05 2016-07-05 Dic Corporation Nondrying polymer hydrogel
US9440187B2 (en) * 2013-07-21 2016-09-13 The Petroleum Institute Device for water collection from atmospheric moisture
AU2015327786B2 (en) * 2014-10-03 2021-01-21 William Marsh Rice University Use of surface modified porous membranes for fluid distillation
US11185792B2 (en) * 2014-11-22 2021-11-30 J. Glenn Turner, Jr. System, and associated method, for recovering water from air
WO2016187709A1 (en) * 2015-05-22 2016-12-01 Simon Fraser University Hybrid atmospheric water generator
CN106809897B (en) * 2015-11-30 2020-03-20 中国科学院金属研究所 Preparation method of graphene photothermal conversion material for seawater desalination and water purification treatment
WO2018118377A1 (en) * 2016-12-20 2018-06-28 Massachusetts Institute Of Technology Sorption-based atmospheric water harvesting device
CN107879405B (en) * 2017-10-26 2021-06-11 西安交通大学 Solar water evaporation purification and decomposition device
FR3077068B1 (en) * 2018-01-22 2019-12-27 Philippe Dekoninck APPARATUS FOR PRODUCING LIQUID WATER BY ADSORPTION AT NIGHT AND DESORPTION BY DAY FROM ATMOSPHERIC AIR
CN112135676B (en) * 2018-05-17 2022-06-03 阿卜杜拉国王科技大学 Material and device for collecting water vapor

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220219116A1 (en) * 2019-05-28 2022-07-14 W. L. Gore & Associates, Inc. Apparatus comprising a contaminant-resistant and non-corrosive desiccant composite with high moisture capacity
US20210299607A1 (en) * 2020-03-24 2021-09-30 The Johns Hopkins University Water harvesting device
US11638899B2 (en) * 2020-03-24 2023-05-02 The Johns Hopkins University Water harvesting device
CN113956531A (en) * 2021-09-24 2022-01-21 桂林电子科技大学 Polymer-based composite material with water storage and photo-thermal water purification functions and preparation method thereof
CN114452954A (en) * 2022-02-14 2022-05-10 北京大学 Heat-conducting water vapor adsorbent and preparation method and application thereof
CN114940799A (en) * 2022-06-14 2022-08-26 天津工业大学 Preparation method of core-shell structure PAA-PNIPAAm hydrogel material for collecting environmental water
CN115232331A (en) * 2022-08-22 2022-10-25 兰州理工大学 MPAE conductive composite hydrogel and preparation method and application thereof
CN116001368A (en) * 2023-01-30 2023-04-25 上海交通大学 Adsorption type passive cooling composite backboard for photovoltaic module and photovoltaic module
CN116180446A (en) * 2023-03-10 2023-05-30 天津工业大学 Preparation method of PNIPAAm hydrogel-based raised fabric with super-strong moisture absorption and water release

Also Published As

Publication number Publication date
CN112135676B (en) 2022-06-03
US20230321595A1 (en) 2023-10-12
CN112135676A (en) 2020-12-25
US20210178321A1 (en) 2021-06-17
CN114809190A (en) 2022-07-29
WO2019220225A1 (en) 2019-11-21
US10960347B1 (en) 2021-03-30

Similar Documents

Publication Publication Date Title
US10960347B1 (en) Water vapor harvesting materials and devices
Shan et al. High-yield solar-driven atmospheric water harvesting with ultra-high salt content composites encapsulated in porous membrane
Li et al. Improving atmospheric water production yield: Enabling multiple water harvesting cycles with nano sorbent
Zhao et al. Super moisture‐absorbent gels for all‐weather atmospheric water harvesting
Yang et al. Magnetic prussian blue/graphene oxide nanocomposites caged in calcium alginate microbeads for elimination of cesium ions from water and soil
Entezari et al. Modifying water sorption properties with polymer additives for atmospheric water harvesting applications
Kim et al. Solar-assisted smart nanofibrous membranes for atmospheric water harvesting
Wang et al. Heterogeneous wettability and radiative cooling for efficient deliquescent sorbents-based atmospheric water harvesting
Wang et al. High-yield and scalable water harvesting of honeycomb hygroscopic polymer driven by natural sunlight
Tzu et al. Sorption of Pb (II), Cd (II), and Ni (II) toxic metal ions by alginate-bentonite
Ablouh et al. Uptake of Pb (II) onto nanochitosan/sodium alginate hybrid beads: mechanism and kinetics study
Li et al. Hybrid water vapor sorbent design with pollution shielding properties: extracting clean water from polluted bulk water sources
Gaikwad et al. Electrospun fiber mats with multistep seeded growth of UTSA-16 metal organic frameworks by microwave reaction with excellent CO2 capture performance
Zheng et al. Humidity capture and solar-driven water collection behaviors of alginate-g-PNIPAm-based hydrogel
Mohapatra et al. Salt in matrix for thermochemical energy storage-A review
Liao et al. Impact of key geochemical parameters on the highly efficient sequestration of Pb (II) and Cd (II) in water using g-C3N4 nanosheets
He et al. Fluorescent hydrogels based on oxidized carboxymethyl cellulose with excellent adsorption and sensing abilities for Ag+
Li et al. Preparation of high-performance chitosan adsorbent by cross-linking for adsorption of Reactive Red 2 (RR2) dye wastewater
Meng et al. Materials and devices for atmospheric water harvesting
Zhou et al. Solar-driven MXene aerogels with high water vapor harvesting capacity for atmospheric water harvesting
Maity et al. Hydratable Core–Shell Polymer Networks for Atmospheric Water Harvesting Powered by Sunlight
Yunyun et al. Investigation of the adsorption properties of U (VI) by sulfonic acid-functionalized carbon materials
Jiang et al. Polyamide 6-LiCl nanofibrous membrane as low-temperature regenerative desiccant with improved stability
Han et al. Facile and efficient chitosan-based hygroscopic aerogel for air dehumidification
Hayashi et al. The first application of fullerene polymer-like materials, C 60 Pd n, as gas adsorbents

Legal Events

Date Code Title Description
FEPP Fee payment procedure

Free format text: ENTITY STATUS SET TO UNDISCOUNTED (ORIGINAL EVENT CODE: BIG.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

AS Assignment

Owner name: KING ABDULLAH UNIVERSITY OF SCIENCE AND TECHNOLOGY, SAUDI ARABIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:WANG, PENG;LI, RENYUAN;SHI, YIFENG;AND OTHERS;REEL/FRAME:054652/0806

Effective date: 20201026

STCF Information on status: patent grant

Free format text: PATENTED CASE