US20040098965A1 - Microturbine direct fired absorption chiller - Google Patents
Microturbine direct fired absorption chiller Download PDFInfo
- Publication number
- US20040098965A1 US20040098965A1 US10/306,259 US30625902A US2004098965A1 US 20040098965 A1 US20040098965 A1 US 20040098965A1 US 30625902 A US30625902 A US 30625902A US 2004098965 A1 US2004098965 A1 US 2004098965A1
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- United States
- Prior art keywords
- recuperator
- direct fired
- absorption chiller
- exhaust
- microturbine
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- 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.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B27/00—Machines, plants or systems, using particular sources of energy
- F25B27/02—Machines, plants or systems, using particular sources of energy using waste heat, e.g. from internal-combustion engines
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- 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
- F02C6/00—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
- F02C6/18—Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2333/00—Details of boilers; Analysers; Rectifiers
- F25B2333/003—Details of boilers; Analysers; Rectifiers the generator or boiler is heated by combustion gas
-
- 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
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- 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
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Definitions
- This invention relates to chillers utilized in air conditioning systems and more particularly to direct fired absorption chillers that are used in combination with microturbine engines.
- the direct fired absorption chillers are not widely used in this country and, in fact, are not utilized with microturbine engines. While water fired absorption chillers have been known to use the waste heat generated by microturbines, these systems require the use of heat exchangers to interface with the water fired absorption chiller.
- the microturbine engine cannot effectively be utilized with the DFA is because the temperature of the exhaust gases vary depending on the load and ambient characteristics of the microturbine.
- the DFA utilizes the environmentally compatible combination of water and an absorbent and a burner to generate the heat necessary to carry out the absorption process.
- Direct fired absorption refrigeration is initiated when higher pressure liquid refrigerant solution form a condenser is discharged through an expansion device and into a lower pressure evaporator and collects therein. Expansion and “flashing” of the refrigerant solution occurs and the liquid refrigerant is collected in the sump of the evaporator. There is also the transfer of heat into the collected and cooled refrigerant solution from comparatively warm system water that is pumped through a cooling tower causing the collected refrigerant solution to evaporate, resulting in vapor that is transferred to an absorber where it is absorbed into a refrigerant solution, such as lithium bromide.
- This process creates a low pressure in the absorber that draws a continuous flow of refrigerant from the evaporator to the absorber, but also causes the vapor to condense as it releases the heat of vaporization in the evaporator.
- This heat and the heat of dilution produced as the refrigerant condensate mixes with the absorbent and is transferred into a cooling tower water and is carried out of the absorber.
- the assimilation of water refrigerant dilutes the lithium-bromide refrigerant solution and reduces its affinity for refrigerant vapor.
- the solution is then reconcentrated by continuously pumping the dilute refrigerant solution from the absorber to a generator where heat is applied to distill the water refrigerant from the absorber.
- the re-concentrated lithium-bromide solution is returned through the absorber and to the generator to resume the absorption process, while the liberated refrigerant vapor from the generator is transferred to the cooler condenser and returned to its liquid state as the cooling tower absorbs the heat of condensation carried by vapor.
- the liquid's return from the generator to the expansion device completes the cycle.
- this type of system replaces the more costly and typical fluorinated hydrocarbon compounds required by vapor compression refrigeration.
- the DFA system is considered to be stable, non-toxic and readily absorbed and easily separated in large volume during the absorption process.
- This invention is principally concerned with producing the heat that is necessary to carry out the absorption process and particularly the waste heat that is generated by a microturbine engine. Although not limited thereto to the microturbines that are utilized for generating electricity is particularly efficacious for use with the direct fired absorption chiller.
- This invention contemplates utilizing the heat discharging from the microturbine engine that is designed to power an electric generator and controlling the heat so that it is at the proper temperature to operate the chiller and that the temperature is controlled to be maintained at a consistent level, i.e. it is held at a constant temperature.
- the object of this invention is the combination of a direct fired chiller and the microturbine engine.
- a feature of this invention is the interconnection of the recuperator to the direct fired absorption chiller and a controlled by-pass valve that regulates the quantity of waste heat flowing to the chiller and the temperature thereof.
- FIG. 1 is a schematic illustration of a prior art system utilizing a microturbine powering an electrical generating system and a water fired absorption chiller illustrating a comparison with this invention
- FIG. 2 is a schematic illustration of this invention where a microturbine powering an electrical system as disclosed in FIG. 1 but modified to power a direct fired absorption chiller in accordance with this invention.
- microturbine powering an electrical generator
- the microturbine engine has become popular in the last several years and essentially is a jet engine that includes a turbine, compressor, combustor and recuperator.
- the microturbine is essentially a miniaturized gas turbine engine typically utilized for powering electrical generators. In certain configurations, the turbine and compressor are attached back-to-back on one end of a shaft that is common to the shaft connecting the armature of the electrical generator.
- Fuel and relatively hot pressurized air discharging from the compressor and recuperator are fed to an annular combustor where they are combined and combusted to further heat and accelerate the engine's working medium for powering the turbine.
- the engine working medium is adiabatically expanded in the turbine for extracting energy which, in turn, is utilized for rotating the compressor and armature.
- the working medium after leaving the turbine is directed to the recuperator where it is placed in indirect heat exchange with the compressor discharge air prior to being admitted into the combustor.
- the turbine exhaust is ultimately discharged from the recuperator.
- FIG. 1 is included to illustrate the microturbine engine utilized in a heretofore prior art system where the exhaust gases are utilized to power a water fired absorption chiller system by directing the exhaust gases to be placed in indirect heat exchange with the water of the chiller.
- the microturbine is generally illustrated by reference numeral 10 and includes a compressor 12 for compressing the air admitted therein which is preheated by being placed in indirect heat exchange with the turbine discharged gases in the reucperator 14 .
- the preheated compressor combustor 16 where it forms a gases engine working medium for powering the turbine 18 .
- the turbine 18 drives the compressor 12 and the turbine exhaust gases are routed to the recuperator 14 where it serves to preheat the compressor discharge air.
- the power generated by the microturbine 10 serves to power the alternator 20 which through an inverter and associated electronic circuitry 22 produces the desired electrical output.
- a well known prior art water fired absorption chiller 21 is powered by the heat generated by the heat exchanger 24 which heats the water feeding the chiller 21 .
- the exhaust gases from the heat exchanger 24 is discharged into ambient.
- the system described in connection with the microturbine depicted in FIG. 1 requires a heat exchanger and the temperature and quantity of the gases utilized as the heat source is predicated on the exhaust discharging from the recuperator of the microturbine engine.
- the invention to be described immediately hereinbelow places the exhaust directly into the chiller and hence, eliminates the necessity of a heat exchanger to heat the water of the chiller. By eliminating the heat exchanger it is contemplated that there will be substantially a 30% increase in cooling capacity of the overall system with substantially a 25% reduction in the cooling system costs.
- the microturbine 10 (all like or substantially like elements bear the same reference numerals in all of the Figs.) includes the compressor 12 , turbine 18 , combustor 16 and recuperator 14 and like the system in FIG. 1, the microturbine powers an electrical generating system.
- the microturbine powers an electrical generating system.
- a by-pass valve 30 is connected between the recuperator discharge and the exhaust discharge so that opening valve 30 will dump turbine exhaust gases directly in the chiller 32 .
- the waste heat from the turbine can be utilized directly in the chiller 32 , can be combined with waste heat discharging from the recuperator 14 or can be disconnected so that the total heat emanate from the recuperator 14 .
- a well known and commercially available temperature sensor 36 senses the heat in the chiller 32 and through a suitable control 37 operates the opening and closing of the by-pass valve 30 by virtue of a suitable commercially available actuator 34 to assure that the desired heat in the chiller is maintained.
- the control 37 which may be a suitable digital comparator, serves to compare the input i.e. the desired temperature and the actual temperature sensed by the sensor 37 . Obviously, sensor 37 measures the temperature of the chiller and by virtue of this system assures that the temperature remains constant.
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Sorption Type Refrigeration Machines (AREA)
Abstract
Description
- This invention relates to chillers utilized in air conditioning systems and more particularly to direct fired absorption chillers that are used in combination with microturbine engines.
- As one skilled in this technology knows, the direct fired absorption chillers (DFA) are not widely used in this country and, in fact, are not utilized with microturbine engines. While water fired absorption chillers have been known to use the waste heat generated by microturbines, these systems require the use of heat exchangers to interface with the water fired absorption chiller. One of the main reasons that the microturbine engine cannot effectively be utilized with the DFA is because the temperature of the exhaust gases vary depending on the load and ambient characteristics of the microturbine. As is well known, the DFA utilizes the environmentally compatible combination of water and an absorbent and a burner to generate the heat necessary to carry out the absorption process. Direct fired absorption refrigeration is initiated when higher pressure liquid refrigerant solution form a condenser is discharged through an expansion device and into a lower pressure evaporator and collects therein. Expansion and “flashing” of the refrigerant solution occurs and the liquid refrigerant is collected in the sump of the evaporator. There is also the transfer of heat into the collected and cooled refrigerant solution from comparatively warm system water that is pumped through a cooling tower causing the collected refrigerant solution to evaporate, resulting in vapor that is transferred to an absorber where it is absorbed into a refrigerant solution, such as lithium bromide. This process creates a low pressure in the absorber that draws a continuous flow of refrigerant from the evaporator to the absorber, but also causes the vapor to condense as it releases the heat of vaporization in the evaporator. This heat and the heat of dilution produced as the refrigerant condensate mixes with the absorbent and is transferred into a cooling tower water and is carried out of the absorber. The assimilation of water refrigerant dilutes the lithium-bromide refrigerant solution and reduces its affinity for refrigerant vapor. In order to sustain the refrigeration cycle the solution is then reconcentrated by continuously pumping the dilute refrigerant solution from the absorber to a generator where heat is applied to distill the water refrigerant from the absorber. As the water refrigerant is removed by distillation, the re-concentrated lithium-bromide solution is returned through the absorber and to the generator to resume the absorption process, while the liberated refrigerant vapor from the generator is transferred to the cooler condenser and returned to its liquid state as the cooling tower absorbs the heat of condensation carried by vapor. The liquid's return from the generator to the expansion device completes the cycle. Of course, this type of system replaces the more costly and typical fluorinated hydrocarbon compounds required by vapor compression refrigeration. The DFA system is considered to be stable, non-toxic and readily absorbed and easily separated in large volume during the absorption process.
- This invention is principally concerned with producing the heat that is necessary to carry out the absorption process and particularly the waste heat that is generated by a microturbine engine. Although not limited thereto to the microturbines that are utilized for generating electricity is particularly efficacious for use with the direct fired absorption chiller.
- As one skilled in this art will appreciate, it is abundantly important that the amount of heat and consistency of the heat source is required to operate the direct fired absorption chiller efficiently. This invention contemplates utilizing the heat discharging from the microturbine engine that is designed to power an electric generator and controlling the heat so that it is at the proper temperature to operate the chiller and that the temperature is controlled to be maintained at a consistent level, i.e. it is held at a constant temperature.
- The object of this invention is the combination of a direct fired chiller and the microturbine engine.
- A feature of this invention is the interconnection of the recuperator to the direct fired absorption chiller and a controlled by-pass valve that regulates the quantity of waste heat flowing to the chiller and the temperature thereof.
- The foregoing and other features of the present invention win become more apparent from the following description and accompanying drawings.
- FIG. 1 is a schematic illustration of a prior art system utilizing a microturbine powering an electrical generating system and a water fired absorption chiller illustrating a comparison with this invention;
- FIG. 2 is a schematic illustration of this invention where a microturbine powering an electrical system as disclosed in FIG. 1 but modified to power a direct fired absorption chiller in accordance with this invention. These figures merely serve to further clarify and illustrate the present invention and are not intended to limit the scope thereof.
- While this invention pertains to a microturbine system powering an electrical generator it is to be understood that the microturbine can be utilized for other types of systems and hence, is not limited to an electrical generating system. The microturbine engine has become popular in the last several years and essentially is a jet engine that includes a turbine, compressor, combustor and recuperator. The microturbine is essentially a miniaturized gas turbine engine typically utilized for powering electrical generators. In certain configurations, the turbine and compressor are attached back-to-back on one end of a shaft that is common to the shaft connecting the armature of the electrical generator. Fuel and relatively hot pressurized air discharging from the compressor and recuperator are fed to an annular combustor where they are combined and combusted to further heat and accelerate the engine's working medium for powering the turbine. The engine working medium is adiabatically expanded in the turbine for extracting energy which, in turn, is utilized for rotating the compressor and armature. The working medium after leaving the turbine is directed to the recuperator where it is placed in indirect heat exchange with the compressor discharge air prior to being admitted into the combustor. The turbine exhaust is ultimately discharged from the recuperator. For further details of the microturbine reference should be made to co-pending patent application Ser. No. 09/934,640 filed on Aug. 22, 2001 by William R. Ryan entitled RECUPERATOR FOR USE WITH TURBINE/TURBO-ALTERNATOR, published and U.S. Pat. No. 6,314,717 granted to Teets et al on Nov. 13, 2001 entitled ELECTRICITY GENERATING SYSTEM HAVING AN ANNULAR COMBUSTOR both of which are commonly assigned to the assignee of this patent application, and both being incorporated by reference herein. Also, for more details of this invention reference should also be made to the microturbines manufactured by the assignee, Elliott Energy Systems, Inc., of Stuart, Fla. and, particularly of the types exemplified by Model Number TA-80.
- To better understand this invention, FIG. 1 is included to illustrate the microturbine engine utilized in a heretofore prior art system where the exhaust gases are utilized to power a water fired absorption chiller system by directing the exhaust gases to be placed in indirect heat exchange with the water of the chiller. As shown therein the microturbine is generally illustrated by
reference numeral 10 and includes acompressor 12 for compressing the air admitted therein which is preheated by being placed in indirect heat exchange with the turbine discharged gases in thereucperator 14. The preheatedcompressor combustor 16 where it forms a gases engine working medium for powering theturbine 18. Theturbine 18 drives thecompressor 12 and the turbine exhaust gases are routed to therecuperator 14 where it serves to preheat the compressor discharge air. The power generated by themicroturbine 10 serves to power thealternator 20 which through an inverter and associatedelectronic circuitry 22 produces the desired electrical output. - As noted in FIG. 1, a well known prior art water fired
absorption chiller 21 is powered by the heat generated by theheat exchanger 24 which heats the water feeding thechiller 21. The exhaust gases from theheat exchanger 24 is discharged into ambient. - As is apparent from the foregoing, the system described in connection with the microturbine depicted in FIG. 1 requires a heat exchanger and the temperature and quantity of the gases utilized as the heat source is predicated on the exhaust discharging from the recuperator of the microturbine engine. The invention to be described immediately hereinbelow, places the exhaust directly into the chiller and hence, eliminates the necessity of a heat exchanger to heat the water of the chiller. By eliminating the heat exchanger it is contemplated that there will be substantially a 30% increase in cooling capacity of the overall system with substantially a 25% reduction in the cooling system costs.
- According to this invention and as depicted in FIG. 2, the microturbine 10 (all like or substantially like elements bear the same reference numerals in all of the Figs.) includes the
compressor 12,turbine 18,combustor 16 andrecuperator 14 and like the system in FIG. 1, the microturbine powers an electrical generating system. However, in this embodiment and inaccordance recuperator 14 and like the system in FIG. 1, the microturbine powers an electrical generating system. However, in this embodiment and in accordance with this invention a by-pass valve 30 is connected between the recuperator discharge and the exhaust discharge so that opening valve 30 will dump turbine exhaust gases directly in thechiller 32. Hence, the waste heat from the turbine can be utilized directly in thechiller 32, can be combined with waste heat discharging from therecuperator 14 or can be disconnected so that the total heat emanate from therecuperator 14. In order to assure that a constant heat is applied to the chiller 32 a well known and commerciallyavailable temperature sensor 36 senses the heat in thechiller 32 and through asuitable control 37 operates the opening and closing of the by-pass valve 30 by virtue of a suitable commerciallyavailable actuator 34 to assure that the desired heat in the chiller is maintained. Thecontrol 37, which may be a suitable digital comparator, serves to compare the input i.e. the desired temperature and the actual temperature sensed by thesensor 37. Obviously,sensor 37 measures the temperature of the chiller and by virtue of this system assures that the temperature remains constant. - What has been shown by this invention is a method and system that allows the microturbine engine to be utilized to power the direct fired absorption chiller without the necessity of a water to exhaust gas heat exchanger. This system not only improves on the efficiency of the chiller, it also reduces the overall cost of the system.
- Although this invention has been shown and described with respect to detailed embodiments thereof, it will be appreciated and understood by those skilled in the art that various changes in form and detail thereof may be made without departing from the spirit and scope of the claimed invention.
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Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/306,259 US6745574B1 (en) | 2002-11-27 | 2002-11-27 | Microturbine direct fired absorption chiller |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/306,259 US6745574B1 (en) | 2002-11-27 | 2002-11-27 | Microturbine direct fired absorption chiller |
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| US20040098965A1 true US20040098965A1 (en) | 2004-05-27 |
| US6745574B1 US6745574B1 (en) | 2004-06-08 |
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| US10/306,259 Expired - Lifetime US6745574B1 (en) | 2002-11-27 | 2002-11-27 | Microturbine direct fired absorption chiller |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20060059919A1 (en) * | 2004-09-07 | 2006-03-23 | Leachman David P | System and method for improving thermal efficiency of dry low emissions combustor assemblies |
| US7185495B2 (en) * | 2004-09-07 | 2007-03-06 | General Electric Company | System and method for improving thermal efficiency of dry low emissions combustor assemblies |
| WO2007023326A1 (en) * | 2005-08-23 | 2007-03-01 | Shap Spa Solar Heat And Power | Cogeneration plant |
| WO2007054507A1 (en) * | 2005-11-08 | 2007-05-18 | Officine Termotecniche Fraccaro - O.T.F. S.R.L. | Device for heating, generating electric power, and cooling enclosed spaces |
| US8132738B2 (en) | 2005-11-08 | 2012-03-13 | Officine Termotecniche Fraccaro -O.T.F. S.R.L. | Device for heating, generating electric power, and cooling enclosed spaces |
| WO2012039611A1 (en) * | 2010-09-21 | 2012-03-29 | Micro Turbine Technology Bv | Combustor with a single limited fuel-air mixing burner and recuperated micro gas turbine |
| NL2005381C2 (en) * | 2010-09-21 | 2012-03-28 | Micro Turbine Technology B V | Combustor with a single limited fuel-air mixing burner and recuperated micro gas turbine. |
| GB2498540A (en) * | 2012-01-18 | 2013-07-24 | Samad Power Ltd | A gas turbine heat and electricity generating apparatus |
| US20130255268A1 (en) * | 2012-03-30 | 2013-10-03 | Pratt & Whitney Canada Corp. | Turbine engine heat recuperator system |
| US9068506B2 (en) * | 2012-03-30 | 2015-06-30 | Pratt & Whitney Canada Corp. | Turbine engine heat recuperator system |
| WO2015011645A1 (en) * | 2013-07-23 | 2015-01-29 | Samad Power Limited | Apparatus for generating heat and electricity |
| US20160138431A1 (en) * | 2014-11-14 | 2016-05-19 | University Of Florida Research Foundation, Inc. | Humid Air Turbine Power, Water Extraction, and Refrigeration Cycle |
| US10247408B2 (en) * | 2014-11-14 | 2019-04-02 | University Of Florida Research Foundation, Inc. | Humid air turbine power, water extraction, and refrigeration cycle |
| US11105498B2 (en) | 2014-11-14 | 2021-08-31 | University Of Florida Research Foundation, Inc. | Humid air turbine power, water extraction, and refrigeration cycle |
| US10731554B2 (en) | 2017-09-12 | 2020-08-04 | University Of Florida Research Foundation, Inc. | Humid air turbine power, water extraction, and refrigeration cycle |
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| US6745574B1 (en) | 2004-06-08 |
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