US20040237526A1 - L & N cycle for hydrogen, electricity, & desalinated seawater - Google Patents
L & N cycle for hydrogen, electricity, & desalinated seawater Download PDFInfo
- Publication number
- US20040237526A1 US20040237526A1 US10/445,339 US44533903A US2004237526A1 US 20040237526 A1 US20040237526 A1 US 20040237526A1 US 44533903 A US44533903 A US 44533903A US 2004237526 A1 US2004237526 A1 US 2004237526A1
- Authority
- US
- United States
- Prior art keywords
- cycle
- hydrogen
- heat
- oxygen
- thermal
- 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.)
- Abandoned
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
- F02C1/05—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly characterised by the type or source of heat, e.g. using nuclear or solar energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
- F02C1/10—Closed cycles
-
- 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
- C02F1/06—Flash 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
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
-
- 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
- Y02A20/131—Reverse-osmosis
Definitions
- the L & N Cycle utility invention combines a single nuclear and/or solar heat source with suite of integrated state-of-the-art processes for production of hydrogen, electricity, oxygen, salt, extractible minerals, low grade process heat (warm brine at ⁇ 100 degrees F.) and desalinated seawater in a manner not considered in past designs. Hence, the invention significantly reduces the cost of producing hydrogen, electricity, and desalinated seawater.
- the L & N Cycle has application in our hydrogen economy, electricity crisis and fresh water crisis. Combining a chemo-thermal hydrogen production cycle, an electric power production cycle and a water desalination cycle into one system, sharing one heat source, will provide the economics to allow each product to be competitive in their respective markets.
- the L & N Cycle will allow recovery of the upfront capital required for implementation and the plant operating cost from three different industries oil, Power, and Water. This patent application is for the unique integration of several independent cycles into one system that maximizes the use of the thermal capability from a single heat source.
- the L & N Cycle is independent of the heat source.
- the L & N Cycle is a system that will produce hydrogen, generate electricity, provide process heat and steam, support mineral extraction via ion-exchange, desalinate seawater via reverse osmosis and/or flash distillation and produce warm brine appropriate for use in domestic heating and cooling using a single heat source coupled to an integrated thermal power/pump cycle.
- the L & N Cycle combines several different cycles into one unique system that takes maximum advantage of the heat available.
- the cycles/systems included are 1) a chemo-thermal process to convert water into oxygen and hydrogen, 2) a modified Regenerative Brayton cycle, 3) a thermal flash distillation desalination cycle 4) a reverse osmosis desalination cycle, and 5) ion-exchange mineral extraction system.
- the heat source will supply a temperature of about 900° C. to 1,000° C. to the chemo-thermal furnace for that process.
- the hot products of the chemo-thermal water conversion process (oxygen and hydrogen) pass through different heat exchangers to supply heat to the other cycles. In this manner the oxygen and hydrogen proceed through their first cooling step.
- the hot hydrogen heat exchanger supplies heat to the fluid in the Regenerative Brayton cycle to produce the electricity.
- the hot oxygen heat exchanger supplies the heat to convert the seawater to steam to extract the salt.
- the L & N Cycle combines multiple state-of-the-art cycles to employ one heat source.
- the first cycle will produce hydrogen and oxygen from a chemo-thermal reaction.
- a 600 MWt heat source heats the chemo-thermal furnace to about 900° C. to 1000°C. Water and various chemicals are introduced resulting in oxygen and hydrogen. At this point hydrogen would be cooled and transferred into the current hydrogen pipelines. The University of California, Texas A & M, and others are developing this process.
- the L & N Cycle would divert the hot hydrogen to pass through a heat exchanger to transfer its heat to the fluid in a Brayton or Regenerative cycle to produce electricity.
- the hydrogen would exit the heat exchanger cooled to the entering temperature of the Brayton or Regenerative cycle fluid.
- the hydrogen would then pass to the hydrogen pipelines.
- the heat source for the modified Brayton or Regenerative cycle is derived from the above heat exchanger.
- the electrical power cycle can be an open loop or closed loop cycle.
- the attached drawing illustrates the L & N Cycle with a closed loop Brayton cycle using an inert gas such as helium in the turbo-compressor.
- a thermal balance will determine the use of a modified Brayton cycle or a Regenerative cycle.
- the cycle consists of a turbo-compressor, alternator, and a heat exchanger.
- the electrical power cycle heat exchanger would use seawater as the cooling agent.
- the seawater will exit the electric power cycle heat exchanger in five forms. These would be desalinated steam, which will be sent through a condenser to yield desalinated water, warm brine, warm desalinated (reverse osmosis) water, salt, and extractable minerals (ionexchange) such as uranium, manganese, and gold.
- Another product of the chemo-thermal process is very hot oxygen.
- the L & N Cycle proposes to use the hot oxygen to pass through a second heat exchanger to transfer heat to seawater to turn the seawater into steam to remove the salt.
- the steam would pass into a container to be mixed/sprayed with the oxygen exiting the heat exchanger for purification.
- the mixture would then proceed to a condenser to yield water.
- the L & N cycle uses heat normally wasted from the chemo-thermo process for cycles that can produce electrical power and desalinated water.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- High Energy & Nuclear Physics (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The L & N Cyde combines a single heat source with several different cycles into one unique system that takes maximum advantage of the heat available. The cycles/systems included are 1) a chemo-thermal process to convert water into oxygen and hydrogen, 2) a modified Regenerative Brayton cycle to produce electricity, 3) a thermal flash distillation desalination cycle 4) a reverse osmosis desalination cycle, and 5) ion-exchange mineral extraction system. The heat source will supply a temperature of about 900° C. to 1,000° C. to the chemo-thermal furnace for that process. The hot products of the chemo-thermal water conversion process (oxygen and hydrogen) pass through different heat exchangers to supply heat to the other cycles. In this manner the oxygen and hydrogen proceed through their first cooling step. The hot hydrogen heat exchanger supplies heat to the fluid in the Regenerative Brayton cycle to produce the electricity. The hot oxygen heat exchanger supplies the heat to convert the seawater to steam to extract the salt. The L & N Cycle provides the United States with the economics to allow the success of a hydrogen economy, provide independence from foreign oil, and advert our electricity and fresh water crisis.
Description
- The Federal government did not directly sponsor any research or development for the invention of the L & N Cycle. However, most of the elements of the L & N Cycle have had research or development sponsored by different agencies of the Federal Government. The L & N Cycle utility invention combines a single nuclear and/or solar heat source with suite of integrated state-of-the-art processes for production of hydrogen, electricity, oxygen, salt, extractible minerals, low grade process heat (warm brine at −100 degrees F.) and desalinated seawater in a manner not considered in past designs. Hence, the invention significantly reduces the cost of producing hydrogen, electricity, and desalinated seawater.
- Our country is facing three separate crisis situations with oil, power, and water resources. The current electrical power crisis in California has stirred interest in new ways to produce and distribute electricity. Solar power is a clean method to produce electricity but independently it cannot compete with natural gas and coal power plants. Nuclear reactor power plants can compete with natural gas and coal, but if the cost of disposing nuclear waste is included, they may not be competitive. The L & N Cycle will improve economics of these processes and aid in reducing dependence on natural gas.
- Moving in the direction of a hydrogen economy will reduce our dependence on foreign oil. Hydrogen is required by 1) the oil industry to improve extraction of clean gasoline from heavy crude oil, 2) the automobile industry for fuel cells, 3) making fertilizer, and 4) many chemical processes. Oil refineries use hydrogen to make gasoline. Crude oil requires hydrogen to refine it into gasoline. Using very heavy crude oil with more hydrogen can provide clean gasoline. Low cost non-fossil hydrogen will also reduce the price of gasoline to the public. Today the majority of hydrogen is produced from natural gas, and therefore is dependent on natural gas prices. Since a majority of the electrical power plants in California use natural gas, their electrical power crisis caused a significant increase in natural gas prices and hence an increase in the cost of hydrogen. The higher cost of hydrogen was passed on to the public through higher gasoline prices. Developing a non-fossil method to produce hydrogen will reduce our dependence on foreign oil and gas. The L & N Cycle will improve the economics of these processes and aid in reducing dependence on foreign oil and natural gas.
- Our country is also facing a fresh water crisis. Texas water conservationists predict that Texas will run out of fresh water in10 years. California is already in a water conservation mode. The population of California is predicted to double in the next 50 years and will need an alternate source for water. Just as the renewable electrical power and non-fossil hydrogen production processes independently are expensive, so is desalination of water. If we can devise an economical method to desalinate seawater we could advert the fresh water crisis. The L & N Cycle will improve the economics of desalination of seawater.
- The L & N Cycle has application in our hydrogen economy, electricity crisis and fresh water crisis. Combining a chemo-thermal hydrogen production cycle, an electric power production cycle and a water desalination cycle into one system, sharing one heat source, will provide the economics to allow each product to be competitive in their respective markets. The L & N Cycle will allow recovery of the upfront capital required for implementation and the plant operating cost from three different industries oil, Power, and Water. This patent application is for the unique integration of several independent cycles into one system that maximizes the use of the thermal capability from a single heat source. The L & N Cycle is independent of the heat source.
- The L & N Cycle is a system that will produce hydrogen, generate electricity, provide process heat and steam, support mineral extraction via ion-exchange, desalinate seawater via reverse osmosis and/or flash distillation and produce warm brine appropriate for use in domestic heating and cooling using a single heat source coupled to an integrated thermal power/pump cycle. The L & N Cycle combines several different cycles into one unique system that takes maximum advantage of the heat available. The cycles/systems included are 1) a chemo-thermal process to convert water into oxygen and hydrogen, 2) a modified Regenerative Brayton cycle, 3) a thermal flash distillation desalination cycle 4) a reverse osmosis desalination cycle, and 5) ion-exchange mineral extraction system. The heat source will supply a temperature of about 900° C. to 1,000° C. to the chemo-thermal furnace for that process. The hot products of the chemo-thermal water conversion process (oxygen and hydrogen) pass through different heat exchangers to supply heat to the other cycles. In this manner the oxygen and hydrogen proceed through their first cooling step. The hot hydrogen heat exchanger supplies heat to the fluid in the Regenerative Brayton cycle to produce the electricity. The hot oxygen heat exchanger supplies the heat to convert the seawater to steam to extract the salt.
- The L & N Cycle combines multiple state-of-the-art cycles to employ one heat source. The first cycle will produce hydrogen and oxygen from a chemo-thermal reaction. There are a few different chemo-thermal processes to produce hydrogen. A 600 MWt heat source heats the chemo-thermal furnace to about 900° C. to 1000°C. Water and various chemicals are introduced resulting in oxygen and hydrogen. At this point hydrogen would be cooled and transferred into the current hydrogen pipelines. The University of California, Texas A & M, and others are developing this process. Instead of going directly to the hydrogen pipeline, the L & N Cycle would divert the hot hydrogen to pass through a heat exchanger to transfer its heat to the fluid in a Brayton or Regenerative cycle to produce electricity. The hydrogen would exit the heat exchanger cooled to the entering temperature of the Brayton or Regenerative cycle fluid. The hydrogen would then pass to the hydrogen pipelines. The heat source for the modified Brayton or Regenerative cycle is derived from the above heat exchanger. The electrical power cycle can be an open loop or closed loop cycle. The attached drawing illustrates the L & N Cycle with a closed loop Brayton cycle using an inert gas such as helium in the turbo-compressor. A thermal balance will determine the use of a modified Brayton cycle or a Regenerative cycle. The cycle consists of a turbo-compressor, alternator, and a heat exchanger. With a 600 MWt heat source for the chemo-thermal process, the hydrogen will have a high enough temperature to heat the fluid in the turbo-compressor cycle. With an overall efficiency of 25% the system could produce 150 MWe of electricity. The electrical power cycle heat exchanger would use seawater as the cooling agent. The seawater will exit the electric power cycle heat exchanger in five forms. These would be desalinated steam, which will be sent through a condenser to yield desalinated water, warm brine, warm desalinated (reverse osmosis) water, salt, and extractable minerals (ionexchange) such as uranium, manganese, and gold.
- Another product of the chemo-thermal process is very hot oxygen. The L & N Cycle proposes to use the hot oxygen to pass through a second heat exchanger to transfer heat to seawater to turn the seawater into steam to remove the salt. The steam would pass into a container to be mixed/sprayed with the oxygen exiting the heat exchanger for purification. The mixture would then proceed to a condenser to yield water. The L & N cycle uses heat normally wasted from the chemo-thermo process for cycles that can produce electrical power and desalinated water.
Claims (3)
1. The L & N cycle files a claim as a system that applies a single heat source to state-of-the-art processes to produce a) hydrogen and oxygen from water through a chemo-thermal reaction, b) electricity with a modified regenerative brayton cycle, c) desalinate seawater through a thermal flash distillation desalination cycle and/or a reverse osmosis desalination cycle, and d) ion-exchange mineral extraction system.
2. The L & N Cycle files a claim as a system that applies a single heat source to state-of-the-art processes to produce a) hydrogen and oxygen from water through a chemo-thermal reaction and b) electricity with a modified Regenerative Brayton cycle.
3. The L & N Cycle files a claim as a system that applies a single heat source to state-of-the-art processes to produce a) hydrogen and oxygen from water through a chemo-thermal reaction, b) desalinate seawater through a thermal flash distillation desalination cycle and/or reverse osmosis desalination cycle, and c) ion-exchange mineral extraction system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/445,339 US20040237526A1 (en) | 2003-05-27 | 2003-05-27 | L & N cycle for hydrogen, electricity, & desalinated seawater |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/445,339 US20040237526A1 (en) | 2003-05-27 | 2003-05-27 | L & N cycle for hydrogen, electricity, & desalinated seawater |
Publications (1)
Publication Number | Publication Date |
---|---|
US20040237526A1 true US20040237526A1 (en) | 2004-12-02 |
Family
ID=33450840
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/445,339 Abandoned US20040237526A1 (en) | 2003-05-27 | 2003-05-27 | L & N cycle for hydrogen, electricity, & desalinated seawater |
Country Status (1)
Country | Link |
---|---|
US (1) | US20040237526A1 (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100455520C (en) * | 2007-05-18 | 2009-01-28 | 中核能源科技有限公司 | Coupling devices of using nuclear energy for sea water desalination, and method |
CN102040258A (en) * | 2010-10-29 | 2011-05-04 | 国家海洋局天津海水淡化与综合利用研究所 | Coproduction method and equipment for thermal power generation and distillation sea water desalinization |
US20110100006A1 (en) * | 2009-11-03 | 2011-05-05 | Korea Advanced Institute Of Science And Technology | Integrated process for water-hydrogen-electricity nuclear gas-cooled reactor |
CN102358633A (en) * | 2011-06-21 | 2012-02-22 | 中国神华能源股份有限公司 | Seawater desalination system used in water-electricity cogeneration and method for desalinating seawater |
US20130287162A1 (en) * | 2009-11-03 | 2013-10-31 | Korea Advanced Institute Of Science And Technology | Integrated process for water-hydrogen-electricity nuclear gas-cooled reactor |
CN104089277A (en) * | 2014-06-25 | 2014-10-08 | 中国石油大学(北京) | Novel energy supply electricity and heat cogeneration system for substituting oil and gas gathering and transporting production process transfer station |
CN112562879A (en) * | 2020-12-03 | 2021-03-26 | 东北大学 | Energy cascade utilization multi-element energy supply system based on nuclear energy |
CN112576328A (en) * | 2020-12-28 | 2021-03-30 | 西安交通大学 | Power cycle water and electricity cogeneration system and method thereof |
CN113417703A (en) * | 2021-05-31 | 2021-09-21 | 南京航空航天大学 | Solar wet helium turbine circulation electricity-water-salt three-coproduction zero-emission system and method |
US11311818B1 (en) * | 2021-09-28 | 2022-04-26 | King Abdulaziz University | Brayton cycle adsorption desalination system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4161657A (en) * | 1975-02-21 | 1979-07-17 | Shaffer Marlin R Jr | Hydrogen supply and utility systems and components thereof |
US4841731A (en) * | 1988-01-06 | 1989-06-27 | Electrical Generation Technology, Inc. | Electrical energy production apparatus |
US6289666B1 (en) * | 1992-10-27 | 2001-09-18 | Ginter Vast Corporation | High efficiency low pollution hybrid Brayton cycle combustor |
US6470683B1 (en) * | 1999-08-30 | 2002-10-29 | Science Applications International Corporation | Controlled direct drive engine system |
US20040219400A1 (en) * | 2003-01-22 | 2004-11-04 | Said Al-Hallaj | Hybrid fuel cell/desalination systems and method for use |
-
2003
- 2003-05-27 US US10/445,339 patent/US20040237526A1/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4161657A (en) * | 1975-02-21 | 1979-07-17 | Shaffer Marlin R Jr | Hydrogen supply and utility systems and components thereof |
US4841731A (en) * | 1988-01-06 | 1989-06-27 | Electrical Generation Technology, Inc. | Electrical energy production apparatus |
US6289666B1 (en) * | 1992-10-27 | 2001-09-18 | Ginter Vast Corporation | High efficiency low pollution hybrid Brayton cycle combustor |
US6470683B1 (en) * | 1999-08-30 | 2002-10-29 | Science Applications International Corporation | Controlled direct drive engine system |
US20040219400A1 (en) * | 2003-01-22 | 2004-11-04 | Said Al-Hallaj | Hybrid fuel cell/desalination systems and method for use |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100455520C (en) * | 2007-05-18 | 2009-01-28 | 中核能源科技有限公司 | Coupling devices of using nuclear energy for sea water desalination, and method |
US20110100006A1 (en) * | 2009-11-03 | 2011-05-05 | Korea Advanced Institute Of Science And Technology | Integrated process for water-hydrogen-electricity nuclear gas-cooled reactor |
US20130287162A1 (en) * | 2009-11-03 | 2013-10-31 | Korea Advanced Institute Of Science And Technology | Integrated process for water-hydrogen-electricity nuclear gas-cooled reactor |
CN102040258A (en) * | 2010-10-29 | 2011-05-04 | 国家海洋局天津海水淡化与综合利用研究所 | Coproduction method and equipment for thermal power generation and distillation sea water desalinization |
CN102358633A (en) * | 2011-06-21 | 2012-02-22 | 中国神华能源股份有限公司 | Seawater desalination system used in water-electricity cogeneration and method for desalinating seawater |
CN104089277A (en) * | 2014-06-25 | 2014-10-08 | 中国石油大学(北京) | Novel energy supply electricity and heat cogeneration system for substituting oil and gas gathering and transporting production process transfer station |
CN112562879A (en) * | 2020-12-03 | 2021-03-26 | 东北大学 | Energy cascade utilization multi-element energy supply system based on nuclear energy |
CN112576328A (en) * | 2020-12-28 | 2021-03-30 | 西安交通大学 | Power cycle water and electricity cogeneration system and method thereof |
CN113417703A (en) * | 2021-05-31 | 2021-09-21 | 南京航空航天大学 | Solar wet helium turbine circulation electricity-water-salt three-coproduction zero-emission system and method |
US11311818B1 (en) * | 2021-09-28 | 2022-04-26 | King Abdulaziz University | Brayton cycle adsorption desalination system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Kianfard et al. | Exergy and exergoeconomic evaluation of hydrogen and distilled water production via combination of PEM electrolyzer, RO desalination unit and geothermal driven dual fluid ORC | |
Yadav et al. | Membrane distillation using low-grade energy for desalination: A review | |
Luqman et al. | Thermodynamic analysis of an oxy-hydrogen combustor supported solar and wind energy-based sustainable polygeneration system for remote locations | |
Ozturk et al. | An integrated system for ammonia production from renewable hydrogen: a case study | |
McMillan et al. | Generation and use of thermal energy in the US industrial sector and opportunities to reduce its carbon emissions | |
US10208665B2 (en) | Methods and systems for energy conversion and generation | |
Rosen | Advances in hydrogen production by thermochemical water decomposition: a review | |
Delgado-Torres et al. | Design recommendations for solar organic Rankine cycle (ORC)–powered reverse osmosis (RO) desalination | |
Wang et al. | Low grade heat driven multi-effect distillation technology | |
Alarcón-Padilla et al. | Design recommendations for a multi-effect distillation plant connected to a double-effect absorption heat pump: A solar desalination case study | |
Palenzuela et al. | Concentrating solar power and desalination plants | |
Orhan et al. | Coupling of copper–chloride hybrid thermochemical water splitting cycle with a desalination plant for hydrogen production from nuclear energy | |
US20040237526A1 (en) | L & N cycle for hydrogen, electricity, & desalinated seawater | |
Hasan et al. | An ocean thermal energy conversion based system for district cooling, ammonia and power production | |
Ghorbani et al. | An integrated structure of bio-methane/bio-methanol cogeneration composed of biogas upgrading process and alkaline electrolysis unit coupled with parabolic trough solar collectors system | |
Baniasadi | Concurrent hydrogen and water production from brine water based on solar spectrum splitting: process design and thermoeconomic analysis | |
Manwell et al. | Recent renewable energy driven desalination system research and development in North America | |
Ismail et al. | Thermo-economic and design analysis of a solar thermal power combined with anaerobic biogas for the air gap membrane distillation process | |
Chen et al. | A spray-assisted multi-effect distillation system driven by ocean thermocline energy | |
Chen et al. | An ocean thermocline desalination system using the direct spray method | |
Alshebli et al. | Energy and exergy analysis of a renewable energy-driven ion recovery system for hydroponic greenhouses | |
Sankar et al. | Solar power and desalination plant for carbon black industry: Improvised techniques | |
Rújula et al. | Application of a multi-criteria analysis for the selection of the most suitable energy source and water desalination system in Mauritania | |
Motieshirazi et al. | Application of membranes in district energy systems | |
CN112939124A (en) | Novel low-temperature exhaust-heat seawater desalination system and method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |