WO2017082880A1 - Procédé de production de sel cristallisé et de saumure comprenant un système reposant sur un processus d'évaporation - Google Patents

Procédé de production de sel cristallisé et de saumure comprenant un système reposant sur un processus d'évaporation Download PDF

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Publication number
WO2017082880A1
WO2017082880A1 PCT/US2015/059969 US2015059969W WO2017082880A1 WO 2017082880 A1 WO2017082880 A1 WO 2017082880A1 US 2015059969 W US2015059969 W US 2015059969W WO 2017082880 A1 WO2017082880 A1 WO 2017082880A1
Authority
WO
WIPO (PCT)
Prior art keywords
offshore
salt
floating
seawater
bittern
Prior art date
Application number
PCT/US2015/059969
Other languages
English (en)
Inventor
Jae Hyun Lim
Original Assignee
Jae Hyun Lim
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 Jae Hyun Lim filed Critical Jae Hyun Lim
Priority to PCT/US2015/059969 priority Critical patent/WO2017082880A1/fr
Publication of WO2017082880A1 publication Critical patent/WO2017082880A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D3/00—Halides of sodium, potassium or alkali metals in general
    • C01D3/04—Chlorides
    • C01D3/06—Preparation by working up brines; seawater or spent lyes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0005—Evaporating devices suitable for floating on water
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0011—Heating features
    • B01D1/0017—Use of electrical or wave energy
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/02—Evaporators with heating coils
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/047—Treatment of water, waste water, or sewage by heating by distillation or evaporation using eolic energy
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F03—MACHINES OR ENGINES FOR LIQUIDS; WIND, SPRING, OR WEIGHT MOTORS; PRODUCING MECHANICAL POWER OR A REACTIVE PROPULSIVE THRUST, NOT OTHERWISE PROVIDED FOR
    • F03G—SPRING, WEIGHT, INERTIA OR LIKE MOTORS; MECHANICAL-POWER PRODUCING DEVICES OR MECHANISMS, NOT OTHERWISE PROVIDED FOR OR USING ENERGY SOURCES NOT OTHERWISE PROVIDED FOR
    • F03G7/00—Mechanical-power-producing mechanisms, not otherwise provided for or using energy sources not otherwise provided for
    • F03G7/005—Electro-chemical actuators; Actuators having a material for absorbing or desorbing gas, e.g. a metal hydride; Actuators using the difference in osmotic pressure between fluids; Actuators with elements stretchable when contacted with liquid rich in ions, with UV light, with a salt solution
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B35/00—Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for
    • B63B35/44—Floating buildings, stores, drilling platforms, or workshops, e.g. carrying water-oil separating devices
    • B63B2035/4473—Floating structures supporting industrial plants, such as factories, refineries, or the like
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination
    • Y02A20/138—Water desalination using renewable energy
    • Y02A20/141—Wind power
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/133—Renewable energy sources, e.g. sunlight

Definitions

  • a method for producing crystallized salt and bittern with a system through the evaporation process is provided.
  • a Floating Salt Farm is a system which uses extracted seawater to reliably and regularly produce substantial amounts of crystallized salt and bittern through the evaporation process, in which the produced crystallized salt and bittern are produced to have specific properties, such as specific mineral compositions.
  • a Floating Salt Farm is a system, in which its purpose is to produce crystallized salt and bittern through the evaporation process.
  • the Floating Salt Farm components can be separately installed at different offshore and/or onshore locations. In an embodiment of the Floating Salt Farm, Floating Salt Farm components are separately installed at an offshore location and at an onshore location. In an embodiment of the Floating Salt Farm, Floating Salt Farm components are separately installed at different offshore locations.
  • the Floating Salt Farm can be operated continuously at any time and at any location, in the condition that energy sources, such as electricity, gas, and fuel, are reliably and regularly supplied. These energy sources can be used in combination to supply the operating Floating Salt Farm with energy continuously.
  • energy sources such as electricity, gas, and fuel
  • the extracted seawater which is used to produce the crystallized salt and bittern with the Floating Salt Farm, can be seawater affected by volcanic activities or by spring water from thermal springs, in which the affected seawater contains substantial amounts of specific chemical elements, such as Magnesium, Aluminum, Calcium, Potassium, Bromine, Silicon, Titanium, Copper, Zinc, Selenium, Lithium, Cerium, Neodymium, Dysprosium, Lanthanum, Europium, Yttrium, and Uranium.
  • the produced crystallized salt and bittern can contain these chemical elements after the evaporation process in substantial amounts. These chemical elements can then be extracted from the produced crystallized salt and bittern.
  • Crystallized salt and bittern can also be produced with the Floating Salt Farm by using seawater extracted from specific water depths and from specific offshore locations, in which the extracted seawater contains amounts of specific chemical elements.
  • the amounts of specific chemical elements of the produced crystallized salt and bittern can be increased by placing contents, such as volcanic rocks, which can be formed from magma and are found in volcanic areas, inside the evaporator tank of the Floating Salt Farm with the seawater during the evaporation process.
  • FIG. 1 is a top view of an embodiment of a Floating Salt Farm.
  • FIG. 2A is a top view of an embodiment of a Floating Salt Farm reinforced with a combination of an offshore structure and onshore structures.
  • FIG. 2B is a side view of an embodiment of a detachable connection between an offshore structure and the buoyant foundation of a Floating Salt Farm.
  • FIG. 3 is a top view of an embodiment of a Floating Salt Farm with an installed buoyant seawall.
  • FIG. 4 is a side view of an embodiment of a Floating Salt Farm with an installed customized ceiling.
  • FIG. 5 is a side view of an embodiment of a Floating Salt Farm reinforced with offshore structures and an embodiment of a Floating Salt Farm moved by using a towboat.
  • FIG. 6 is a top view of an embodiment of a Floating Salt Farm with an installed motor propeller component.
  • FIG. 7 is a top view of an embodiment of the Floating Salt Farm components separately installed at an offshore location and an onshore location.
  • FIG. 8 is a top view of an embodiment of the Floating Salt Farm components separately installed at different offshore locations.
  • FIGS. 9 A and 9B are side views of embodiments of the evaporator plate component inside and above the evaporator tank, respectively.
  • FIGS. 10 A and 10B are side views of embodiments of heat exchangers attached to the outer surface and coiled around the inner surface of the evaporator tank, respectively.
  • FIG. 11 A is a side view of an embodiment of an offshore fixed-bottom wind turbine powering the Floating Salt Farm.
  • FIG. 1 IB is a side view of an embodiment of offshore floating wind turbines powering the Floating Salt Farm.
  • FIG. l lC is a side view of an embodiment of an electric cable supported by buoyant cable supports.
  • FIG. 12A is a side view of an embodiment of a seawater extraction vessel extracting seawater from a specific water depth and from a specific offshore location.
  • FIGS. 12B and 12C are side views of an underwater volcano and a volcano located above sea level, respectively, in which have affected the seawater to be extracted.
  • FIGS. 12D and 12E are side views of a thermal spring located above sea level and an underwater thermal spring, respectively, in which have affected the seawater to be extracted.
  • FIGS. 13A and 13B are side views of embodiments of volcanic rocks inside the evaporator tank during the evaporation process.
  • FIG. 14 is a side view of an embodiment of mud inside the evaporator tank during the evaporation process.
  • FIG. 15A is a perspective view of an evaporator basin.
  • FIG. 15B is a side view of an evaporator basin installed onto the top of the buoyant foundation.
  • FIG. 15C is a top view of evaporator basins connected to saline water storage tanks installed onto the top of buoyant foundations.
  • a Floating Salt Farm is a system, in which its purpose is to produce crystallized salt and bittern through the evaporation process using extracted seawater.
  • the buoyant foundation 101 of the Floating Salt Farm 201 must have sufficient buoyancy and must be able to support the weight of the Floating Salt Farm components 202, which lie on the buoyant foundation 101, as shown in FIG. 1.
  • the Floating Salt Farm components 202 are installed on the flooring deck 103, in which the flooring deck 103 is fixed onto the top of the buoyant foundation 101.
  • Offshore structures 104 can be used to reinforce the Floating Salt Farm 201, as shown in FIG. 5.
  • a combination of onshore structures 105 and offshore structures 104 can also be used to reinforce the Floating Salt Farm 201, as shown in FIG. 2A.
  • a breakwater 102 protects the Floating Salt Farm 201 from hitting sea waves.
  • connection between the buoyant foundation 101 of the Floating Salt Farm 201 and the offshore structure 104 can be detachable, as shown in FIG. 2B.
  • a buoyant seawall 106 can be installed to increase the buoyancy and stability of the Floating Salt Farm 201.
  • a buoyant seawall 106 is located around the perimeter of and slightly away from the buoyant foundation 101 of the Floating Salt Farm 201, as shown in FIG. 3.
  • the connection between the buoyant foundation 101 of the Floating Salt Farm 201 and the buoyant seawall 106 can be detachable.
  • the Floating Salt Farm components 202 can be further protected from weather conditions, such as rain and snow, by installing a customized ceiling 107, as shown in FIG. 4.
  • the customized ceiling 107 can have installed windows 108, which can be moveable and controlled along the surface of the customized ceiling 107 to intake sunlight for the installed photovoltaic panel components 208, in which the photovoltaic panels components 208, as shown in FIG. 6, are optional components of the Floating Salt Farm 201.
  • the Floating Salt Farm 201 is moved by using a towboat 301, as shown in FIG. 5, or is moved through an installed motor propeller component 304, as shown in FIG. 6, when transporting the Floating Salt Farm 201 to a specific offshore location to extract seawater for the evaporation process or moving the Floating Salt Farm 201 to a safe location during times of inclement weather conditions.
  • the buoyant foundation 101 of the Floating Salt Farm 201 is a barge with an installed motor propeller component 304.
  • some Floating Salt Farm components 202 can be separately installed at a safe location, such as at a harbor with breakwaters 102, as shown in FIG. 7.
  • a seawater extraction vessel 303 extracts seawater at a specific offshore location, in which the seawater extraction vessel 303 delivers the extracted seawater to some Floating Salt Farm components 202, which are installed at an offshore location, to conduct the evaporation process.
  • the transport vessel 302 delivers the produced crystallized salt and bittern to the other Floating Salt Farm components 202, which are installed at an onshore location.
  • a seawater extraction vessel 303 extracts seawater at a specific offshore location, in which the seawater extraction vessel 303 delivers the extracted seawater to some Floating Salt Farm components 202, which are installed at an offshore location, to conduct the evaporation process. After the evaporation process, the transport vessel 302 delivers the produced crystallized salt and bittern to the other Floating Salt Farm components 202, which are installed at a different offshore location.
  • some Floating Salt Farm components 202 are located at a specific offshore location to extract seawater for the evaporation process. After the evaporation process, the transport vessel 302 delivers the produced crystallized salt and bittern to the other Floating Salt Farm components 202, which are installed at a different offshore location.
  • the evaporator plate component 204 is placed inside the evaporator tank 203 and the water vapor produced is released to the atmosphere. After the evaporation process, the produced crystallized salt lies at the surface of the evaporator plate component 204 and the produced bittern is located below the evaporator plate component 204, as shown in FIG. 9A.
  • the produced crystallized salt at the surface of the evaporator plate component 204 is extracted using a crystallized salt extraction tube 211. After extracting the produced crystallized salt, the evaporator plate component 204 is lifted above the top of the evaporator tank 203, as shown in FIG. 9B, and the produced bittern is extracted using a bittern extraction tube 212.
  • the heating used for the evaporation process is provided through heat exchangers 207, which are connected to the heating tank 206.
  • heating for the evaporation process is supplied through heat exchangers 207 attached to the outer surface of the evaporator tank 203.
  • heating for the evaporation process is supplied through a heat exchanger 207 coiled around the inner surface of the evaporator tank 203.
  • the Floating Salt Farm 201 can be operated continuously at any time and at any location, in the condition that energy sources, such as electricity, gas, and fuel, are reliably and regularly supplied. These energy sources can be used in combination to supply the operating Floating Salt Farm 201 with energy continuously.
  • energy sources such as electricity, gas, and fuel
  • Offshore fixed-bottom wind turbines 501 and offshore floating wind turbines 502 can be used to supply electricity to power the Floating Salt Farm 201, as shown in FIGS. 11A and 11B.
  • the electricity generated from the offshore fixed-bottom wind turbines 501 and offshore floating wind turbines 502 is supplied to the Floating Salt Farm 201 through electric cables 503.
  • an offshore fixed-bottom wind turbine 501 supplies electricity to power the Floating Salt Farm 201.
  • offshore floating wind turbines 502 which can be moved through an installed motor propeller component 304, supply electricity to power the Floating Salt Farm 201.
  • the electric cable 503 connecting the Floating Salt Farm 201 and the offshore fixed-bottom wind turbine 501 or the offshore floating wind turbine 502, can be supported by a buoyant cable support 504 to keep the electric cable 503 above the water level, as shown in FIG. 11C.
  • the seawater to be used for the evaporation process of the Floating Salt Farm 201 can be extracted from specific water depths and from specific offshore locations by using the seawater extraction tube 210 of the seawater extraction vessel 303, as shown in FIG. 12A, to extract seawater containing amounts of specific chemical elements.
  • the extracted seawater to be used for the evaporation process of the Floating Salt Farm 201 can be seawater which has been affected by volcanic activities and can contain substantial amounts of specific chemical elements.
  • the volcanic activities, which have affected the seawater to be used for the evaporation process of the Floating Salt Farm 201 originate from underwater volcanoes 401, as shown in FIG. 12B, or from volcanoes located above sea level 402, as shown in FIG. 12C.
  • the extracted seawater to be used for the evaporation process of the Floating Salt Farm 201 can also be seawater which has been affected by spring water from thermal springs and can contain substantial amounts of specific chemical elements.
  • the spring water, which has affected the seawater to be used for the evaporation process originate from thermal springs located above sea level 403, as shown in FIG. 12D, or from underwater thermal springs 404, as shown in FIG. 12E.
  • the produced crystallized salt and bittern can contain substantial amounts of specific chemical elements, such as Magnesium, Aluminum, Calcium, Potassium, Bromine, Silicon, Titanium, Copper, Zinc, Selenium, Lithium, Cerium, Neodymium, Dysprosium, Lanthanum, Europium, Yttrium, and Uranium.
  • specific chemical elements such as Magnesium, Aluminum, Calcium, Potassium, Bromine, Silicon, Titanium, Copper, Zinc, Selenium, Lithium, Cerium, Neodymium, Dysprosium, Lanthanum, Europium, Yttrium, and Uranium.
  • the crystallized salt and bittern can also be produced to contain substantial amounts of specific chemical elements by placing contents such as volcanic rocks, which can be formed from magma and are found in volcanic areas, inside the evaporator tank 203, with the seawater during the evaporation process.
  • contents such as volcanic rocks, which can be formed from magma and are found in volcanic areas, inside the evaporator tank 203, with the seawater during the evaporation process.
  • FIG. 13 A An embodiment of the evaporator tank 203 is shown in FIG. 13 A, in which the evaporator tank 203 has an evaporator plate component 204 and volcanic rocks are placed below the evaporator plate component 204 with the seawater during the evaporation process to produce crystallized salt and bittern containing substantial amounts of specific chemical elements.
  • FIG. 13B An embodiment of the evaporator tank 203 is shown in FIG. 13B, in which the evaporator tank 203 has an evaporator bin component 205 linked to the bottom of the evaporator plate component 204.
  • the evaporator bin component 205 holds volcanic rocks and is located inside the evaporator tank 203 with the seawater during the evaporation process to produce crystallized salt and bittern containing substantial amounts of specific chemical elements.
  • the amount of specific chemical elements in the crystallized salt and bittern produced with the Floating Salt Farm 201 can be modified by adjusting the heating temperature and the heating time of the evaporation process accordingly.
  • the amount of specific chemical elements in the produced crystallized salt and bittern can be increased by reusing the produced bittern for other additional and multiple evaporation process cycles. After each evaporation process cycle, additional extracted seawater and/or other previously produced bittern can be added to the evaporator tank 203 and mixed with the produced bittern for the following evaporation process cycles. By running the evaporation process multiple cycles, the amount of specific chemical elements in the produced crystallized salt and bittern can be produced to be higher.
  • FIG. 14 An embodiment of the evaporator tank 203 is shown in FIG. 14, in which the evaporator tank 203 has an evaporator bin component 205 holding mud to produce crystallized salt and bittern of similar quality as the conventional sun-dried salt and bittern produced in conventional salt ponds.
  • the mud placed inside the evaporator bin component 205 can be mud conventionally used to produce conventional sun-dried salt and bittern at conventional salt ponds or can be suitable mud or clay found at other locations.
  • the wind propeller components 209 in this embodiment are installed to be inside the evaporator tank 203 and are used to emulate the sea breeze used for the evaporation process.
  • Conventional sun-dried salt can be produced at offshore locations by using an evaporator basin 213, as shown in FIG. 15 A.
  • the evaporator basin 213 is installed onto the top of the buoyant foundation 101, in which the buoyant foundation 101 can be reinforced with offshore structures 104.
  • the connection between the buoyant foundation 101 and the offshore structure 104 can be detachable.
  • a buoyant seawall 106 can be installed to increase the buoyancy and the stability of the buoyant foundation 101, which is located around the perimeter of and slightly away from the buoyant foundation 101, as shown in FIG. 3.
  • the connection between the buoyant foundation 101 and the buoyant seawall 106 can be detachable.
  • the evaporator basin 213 has different dimensions than the evaporator tank 203, in which the evaporator basin 213 has dimensions which span most of the buoyant foundation 101 surface and has a lower height than the evaporator tank 203.
  • seawater is first extracted into the evaporator basin 213 and is then harvested through solar evaporation.
  • the harvested seawater in the evaporator basin 213 is transferred to the saline water storage tank 214, in which the saline water storage tank 214 is installed onto the top of the buoyant foundation 101 and can be protected with an installed customized ceiling 107, as shown in FIGS. 15B and 15C.
  • the produced crystallized salt is delivered to the other Floating Salt Farm components 202 by using a transport vessel 302, as shown in FIG. 15C.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Combustion & Propulsion (AREA)
  • Analytical Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

L'invention concerne un parc à sel flottant qui utilise de l'eau de mer extraite pour produire de manière fiable et régulière des quantités importantes de sel cristallisé et de saumure par le biais d'un processus d'évaporation. L'eau de mer utilisée pour le processus d'évaporation du parc à sel flottant peut être 1) de l'eau de mer affectée par des activités volcaniques, 2) de l'eau de mer affectée par de l'eau de source provenant de sources thermales et 3) de l'eau de mer extraite de profondeurs d'eau spécifiques et provenant de localisations offshore spécifiques. Le sel cristallisé et la saumure devant être produits sont affectés par le placement de produits, tels que des roches volcaniques, à l'intérieur de la cuve d'évaporateur avec l'eau de mer pendant le processus d'évaporation.
PCT/US2015/059969 2015-11-10 2015-11-10 Procédé de production de sel cristallisé et de saumure comprenant un système reposant sur un processus d'évaporation WO2017082880A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/US2015/059969 WO2017082880A1 (fr) 2015-11-10 2015-11-10 Procédé de production de sel cristallisé et de saumure comprenant un système reposant sur un processus d'évaporation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2015/059969 WO2017082880A1 (fr) 2015-11-10 2015-11-10 Procédé de production de sel cristallisé et de saumure comprenant un système reposant sur un processus d'évaporation

Publications (1)

Publication Number Publication Date
WO2017082880A1 true WO2017082880A1 (fr) 2017-05-18

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4219387A (en) * 1977-12-19 1980-08-26 Gruntman Leonard R Solar still
US20040065614A1 (en) * 2002-10-08 2004-04-08 Gordon Andrew W. Mobile desalination plants and systems, and methods for producing desalinated water
US20130048226A1 (en) * 2012-10-28 2013-02-28 Jae Hyun Lim Floating salt farm
US20130318870A1 (en) * 2013-08-15 2013-12-05 Jae Hyun Lim Applications of the bittern produced using the evaporation process of the floating salt farm
US20140020850A1 (en) * 2012-10-28 2014-01-23 Jae Hyun Lim Method for producing crystallized salt and bittern with a system through the evaporation process.

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4219387A (en) * 1977-12-19 1980-08-26 Gruntman Leonard R Solar still
US20040065614A1 (en) * 2002-10-08 2004-04-08 Gordon Andrew W. Mobile desalination plants and systems, and methods for producing desalinated water
US20130048226A1 (en) * 2012-10-28 2013-02-28 Jae Hyun Lim Floating salt farm
US20140020850A1 (en) * 2012-10-28 2014-01-23 Jae Hyun Lim Method for producing crystallized salt and bittern with a system through the evaporation process.
US20130318870A1 (en) * 2013-08-15 2013-12-05 Jae Hyun Lim Applications of the bittern produced using the evaporation process of the floating salt farm

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