A solar powered cooling system that obtains a plurality of cooling temperatures in a simultaneous fashion. The system includes a heliostat field, a steam-Rankine cycle (SRC), absorption-refrigeration cycle (ARC), an ejector-refrigeration cycle (ERC) and a cascaded-refrigeration cycle (CRC). The heli
A solar powered cooling system that obtains a plurality of cooling temperatures in a simultaneous fashion. The system includes a heliostat field, a steam-Rankine cycle (SRC), absorption-refrigeration cycle (ARC), an ejector-refrigeration cycle (ERC) and a cascaded-refrigeration cycle (CRC). The heliostat field directs solar energy to a receiver included in the SRC to heat molten-salt. The heated molten salt transfers heat energy to form vapors of a first refrigerant. A steam turbine transfer the power to drive the vapor compression system (CRC) system and vapor at the turbine exit is fed to the ERC cooling system. The ERC achieves a first cooling temperature range by driving an ejector-nozzle by the vapors of the first refrigerant. The steam turbine drives a first compressor and a second compressor included in the CRC to obtain a second cooling temperature range. A condenser included in the ARC portion condenses the vapors of the first refrigerant to obtain a third cooling temperature range.
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1. A method of simultaneously obtaining a plurality of cooling-temperature ranges by a solar powered cooling system, the method comprising: directing, by a heliostat field, solar energy to a receiver included in a first portion of the cooling system, the receiver heating molten-salt that flows in th
1. A method of simultaneously obtaining a plurality of cooling-temperature ranges by a solar powered cooling system, the method comprising: directing, by a heliostat field, solar energy to a receiver included in a first portion of the cooling system, the receiver heating molten-salt that flows in the first portion of the cooling system;transferring heat energy from the heated molten salt to a first refrigerant, in a first generator and a second generator, the transferred heat energy forming vapors of the first refrigerant;distributing, by a steam turbine, vapors of the first refrigerant obtained by the first generator, to drive a second portion and a third portion of the cooling system;driving an ejector nozzle included in the second portion of the cooling system by the vapors of the first refrigerant to obtain a first cooling temperature range;compressing a second refrigerant, by a first compressor and a second compressor included in a third portion of the cooling system to obtain a second cooling temperature range; andcondensing, by a condenser included in a fourth portion of the cooling system, vapors of the first refrigerant obtained by the second generator, to obtain a third cooling temperature range. 2. The method of claim 1, wherein the first portion of the cooling system is a steam Rankine cycle, the second portion of the cooling system is an ejector refrigeration cycle, the third portion of the cooling system is a cascaded refrigeration cycle, and the fourth portion of the cooling system is an absorption refrigeration cycle. 3. The method of claim 1, wherein the first cooling temperature range is from 0° C. to 5° C., the second cooling temperature range is from −50° C. to −80° C., and the third cooling temperature range is from 10° C. to 18° C. 4. The method of claim 1, wherein the first refrigerant is water (H2O) and the second refrigerant is nitrous oxide (N2O). 5. The method of claim 1, wherein the molten salt is selected from a group consisting of lithium fluoride (LiF), sodium chloride (NaCl), sodium tetra-fluoroborate (NaBF4), a mixture of NaCl and potassium chloride (KCl), a mixture of lithium fluoride (LiF) and Beryllium fluoride (LiF—BeF2), a mixture of LiF, sodium fluoride (NaF), and potassium fluoride (KF) and a mixture of potassium chloride and magnesium chloride. 6. The method of claim 1, further comprising: detecting via flow sensors, a flow rate of the first refrigerant and the second refrigerant in the first portion, second portion, third portion and the fourth portion of the cooling system, respectively; andtransmitting, the detected flow rates to circuitry that is configured to control the flow rates of the first refrigerant and the second refrigerant. 7. The solar powered cooling system of claim 1, wherein the molten salt is selected from a group consisting of lithium fluoride (LiF), sodium chloride (NaCl), sodium tetra-fluoroborate (NaBF4), a mixture of NaCl and potassium chloride (KCl), a mixture of lithium fluoride (LiF) and Beryllium fluoride (LiF—BeF2), a mixture of LiF, sodium fluoride (NaF), and potassium fluoride (KF) and a mixture of potassium chloride and magnesium chloride. 8. The non-transitory computer readable of claim 1, wherein the molten salt is selected from a group consisting of lithium fluoride (LiF), sodium chloride (NaCl), sodium tetra-fluoroborate (NaBF4), a mixture of NaCl and potassium chloride (KCl), a mixture of lithium fluoride (LiF) and Beryllium fluoride (LiF—BeF2), a mixture of LiF, sodium fluoride (NaF), and potassium fluoride (KF) and a mixture of potassium chloride and magnesium chloride. 9. A solar powered cooling system comprising: a heliostat field configured to direct received solar energy to a receiver included in a first portion of the cooling system, the receiver heating molten-salt that flows in the first portion of the cooling system;a first steam-generator and a second steam generator configured to form vapors of a first refrigerant by transferring heat energy from the molten-salt to the first refrigerant;a steam turbine configured to distribute vapors of the first refrigerant obtained by the first steam-generator, to drive a second portion and a third portion of the cooling system;an ejector nozzle included in the second portion of the cooling system, and driven by vapors of the first refrigerant, being configured to obtain a first cooling-temperature range;a first compressor and a second compressor included in a third portion of the cooling system and configured to compress a second refrigerant to obtain a second cooling-temperature range; anda condenser included in a fourth portion of the cooling system and configured to condense vapors of the first refrigerant obtained by the second generator, to obtain a third cooling temperature range. 10. The solar powered cooling system of claim 9, wherein the first portion of the cooling system is a steam Rankine cycle, the second portion of the cooling system is an ejector refrigeration cycle, the third portion of the cooling system is a cascaded refrigeration cycle, and the fourth portion of the cooling system is an absorption refrigeration cycle. 11. The solar powered cooling system of claim 9, wherein the first cooling temperature range is from 0° C. to 5° C., the second cooling temperature range is from −50° C. to −80° C., and the third cooling temperature range is from 10° C. to 18° C. 12. The solar powered cooling system of claim 9, wherein the first refrigerant is water (H2O) and the second refrigerant is nitrous oxide (N2O). 13. The solar powered cooling system of claim 9, further comprising: flow sensors configured to detect a flow rate of the first refrigerant and the second refrigerant in the first portion, second portion, third portion and the fourth portion of the cooling system, respectively; andtransmit, the detected flow rates to circuitry that is configured to control the flow rates of the first refrigerant and the second refrigerant. 14. A non-transitory computer readable medium having stored thereon a program that when executed by a computer causes the computer to execute a method of simultaneously obtaining a plurality of cooling-temperature ranges by a solar powered cooling system, the method comprising: directing, by a heliostat field, solar energy to a receiver included in a first portion of the cooling system, the receiver heating molten-salt that flows in the first portion of the cooling system;transferring heat energy from the heated molten salt to a first refrigerant, in a first generator and a second generator, the transferred heat energy forming vapors of the first refrigerant;distributing, by a steam turbine, vapors of the first refrigerant obtained by the first generator, to drive a second portion and a third portion of the cooling system;driving an ejector nozzle included in the second portion of the cooling system by the vapors of the first refrigerant to obtain a first cooling temperature range;compressing a second refrigerant, by a first compressor and a second compressor included in a third portion of the cooling system to obtain a second cooling temperature range; andcondensing, by a condenser included in a fourth portion of the cooling system, vapors of the first refrigerant obtained by the second generator, to obtain a third cooling temperature range. 15. The non-transitory computer readable of claim 14, wherein the first portion of the cooling system is a steam Rankine cycle, the second portion of the cooling system is an ejector refrigeration cycle, the third portion of the cooling system is a cascaded refrigeration cycle, and the fourth portion of the cooling system is an absorption refrigeration cycle. 16. The non-transitory computer readable of claim 14, wherein the first cooling temperature range is from 0° C. to 5° C., the second cooling temperature range is from −50° C. to −80° C., and the third cooling temperature range is from 10° C. to 18° C. 17. The non-transitory computer readable of claim 14, wherein the first refrigerant is water (H2O) and the second refrigerant is nitrous oxide (N2O). 18. The non-transitory computer readable of claim 14, the method further comprising: detecting via flow sensors, a flow rate of the first refrigerant and the second refrigerant in the first portion, second portion, third portion and the fourth portion of the cooling system, respectively; andreceiving the detected flow rates to control the flow rates of the first refrigerant and the second refrigerant.
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이 특허에 인용된 특허 (4)
Newton Alwin B. (York PA), Control of absorption systems energized from plural storage tanks maintained at different temperatures.
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