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Which, using a heat transfer fluid in any thermodynamic cycle or system for using process heat, comprises: two-dimensional solar concentrator means for heating the heat transfer fluid from a temperature T1 to a temperature T2; three-dimensional solar concentrator means for overheating the heat trans

Which, using a heat transfer fluid in any thermodynamic cycle or system for using process heat, comprises: two-dimensional solar concentrator means for heating the heat transfer fluid from a temperature T1 to a temperature T2; three-dimensional solar concentrator means for overheating the heat transfer fluid from a temperature T2 to a temperature T3; such that the advantages of working at high-temperatures of the three-dimensional solar concentrator means are taken advantage of with overall costs similar to those of two-dimensional solar concentrator means. In a specific application for generating electric power, the two-dimensional solar concentrator means consist of a parabolic trough collector (1), while the three-dimensional solar concentrator means consist of a heliostat field and central tower (2) for generating overheated steam that expands in a turbine (6) coupled to an electric generator (7).

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1. A method of generating electricity under a Rankine thermodynamic cycle, the method comprising: a) providing a solar concentrator electric plant;b) generating saturated water vapor at a pressure of at least 96 bar utilizing a two-dimensional solar concentrator from water;c) subsequent to step b) g

1. A method of generating electricity under a Rankine thermodynamic cycle, the method comprising: a) providing a solar concentrator electric plant;b) generating saturated water vapor at a pressure of at least 96 bar utilizing a two-dimensional solar concentrator from water;c) subsequent to step b) generating overheated water vapor utilizing a three-dimensional concentrator from the saturated water vapor;d) subsequent to step c) generating electricity using a steam turbine from the overheated water vapor;e) in a first operating condition, flowing the water in a continuous cycle through a piping system so as to flow in sequence through the two-dimensional solar concentrator, the three-dimensional solar concentrator, the turbine and back to the two-dimensional solar concentrator; andf) in a second operating condition, flowing the water in a continuous cycle through a piping system so as to flow in sequence through the two-dimensional solar concentrator, through a back up fossil fuel generator adapted to provide backup heat to the water, through the turbine, and back to the two-dimensional solar concentrator, bypassing the three-dimensional solar collector. 2. The method according to claim 1, wherein the step of generating saturated water vapor includes heating the water to at least 310° C. 3. The method according to claim 1, wherein the step of generating overheated water vapor includes heating the saturated water vapor to at least 520° C. and at least 18% of solar energy used to heat the fluid is produced in the three-dimensional solar concentrator. 4. The method according to claim 1, further comprising, in a third operating condition: flowing the water in a continuous cycle through a piping system so as to flow in sequence through a back up fossil fuel generator adapted to provide backup heat to the water, through the turbine, and back to the back up fossil fuel generator, bypassing both the two-dimensional solar collector and the three-dimensional solar collector. 5. A solar concentrator plant utilizing water as a working fluid in a Rankine cycle for creating a thermal power supply, the plant comprising: a) a two-dimensional solar concentrator assembly adapted to provide about 82% of the thermal power supply and to convert the water to saturated water vapor, wherein the water is heated in the two-dimensional solar concentrator assembly to at least 310° C.; andb) a three dimensional solar concentrator assembly comprising a heliostat field and a central receiver tower, the assembly being adapted to provide no less than 18% of the thermal power supply and to convert the saturated water vapor to overheated water vapor, wherein the saturated water vapor is heated to at least 520° C.;c) a turbine for utilizing the overheated water vapor to produce electricity; and including piping wherein the water flows in a loop from the two-dimensional solar concentrator assembly, then to the three dimensional solar concentrator assembly, then to the turbine and then back to the two-dimensional solar concentrator assembly;d) a backup fossil fuel generator; ande) a bypass of the three-dimensional solar concentrator, so as to operably provide flow of the working fluid in a continuous cycle first through the two-dimensional solar concentrator, then through the back up fossil fuel generator, then through the turbine after which the fluid is returned to the two-dimensional concentrator. 6. The solar concentrator plant according to claim 5, further comprising a second bypass of both the two-dimensional concentrator and the three-dimensional concentrator, so as to operably provide flow of the working fluid in a continuous cycle first through the back up fossil fuel generator, then through the turbine after which the fluid is returned to the back up fossil fuel generator. 7. A method of creating a supply of thermal power, comprising: a) providing a solar concentrator plant with water as a working fluid including a two-dimensional solar concentrator assembly and a three-dimensional solar concentrator assembly;b) flowing the water through the two-dimensional solar concentrator and converting the water therein to saturated water vapor at a pressure of at least 96 bar, so that about 82% of a total supply of thermal power is generated in the two dimensional solar concentrator;c) after step b) flowing the water through the three-dimensional solar concentrator and converting the saturated water vapor therein to overheated water vapor, such that no less than 18% of the total supply of thermal power is generated in the three dimensional solar concentrator;d) after step c flowing the water through a turbine and generating electricity therein;e) during the method, in a first operating condition, flowing the water sequentially through the two-dimensional solar concentrator, the three-dimensional solar concentrator, the turbine and back to the two-dimensional solar concentrator in a continuous loop wherein the water does not utilize a heat exchanger heat transfer interface with flows from other process equipment while circulating in the loop; andf) in a second operating condition, flowing the working fluid in a continuous cycle through a piping system so as to flow in sequence through the two-dimensional solar concentrator, through a back up fossil fuel generator adapted to provide backup heat to the working fluid, through the turbine, and back to the two-dimensional solar concentrator, bypassing the three-dimensional solar collector. 8. A method according to claim 7, wherein the step of converting water to saturated water vapor includes heating the water to at least 310° C. 9. A method according to claim 7, wherein the step of converting saturated water vapor to overheated water vapor includes heating the saturated water vapor to at least 520° C. 10. The method according to claim 7, further comprising, in a third operating condition: flowing the working fluid in a continuous cycle through a piping system so as to flow in sequence through a back up fossil fuel generator adapted to provide backup heat to the working fluid, through the turbine, and back to the back up fossil fuel generator, bypassing both the two-dimensional solar collector and the three-dimensional solar collector. 11. A solar concentrator plant for producing electricity from sunlight and utilizing a single working fluid in a flow path; the plant comprising: a) a solar two dimensional concentrator for heating the fluid to at least 310° C. and producing saturated water vapor;b) a solar three dimensional concentrator for heating the saturated water to at least 520° C. and producing overheated water vapor;c) a steam turbine receiving the overheated water vapor to generate electricity;d) a piping system operably providing flow of the working fluid in a continuous cycle first through the two-dimensional concentrator, then through the three-dimensional concentrator, then through the turbine after which the fluid is returned to the two-dimensional concentrator; ande) a backup fossil fuel generator adapted to provide backup heat to a side stream of the water through a heat exchanger;wherein the piping system comprises a bypass of the three-dimensional concentrator, so as to operably provide flow of the working fluid in a continuous cycle first through the two-dimensional concentrator, then through the back up fossil fuel generator, then through the turbine after which the fluid is returned to the two-dimensional concentrator. 12. The plant according to claim 11, wherein the piping system further comprises a second bypass of both the two-dimensional concentrator and the three-dimensional concentrator, so as to operably provide flow of the working fluid in a continuous cycle first through the back up fossil fuel generator, then through the turbine after which the fluid is returned to the back up fossil fuel generator. 13. A method of generating electricity, comprising: a) providing a solar concentrator plant as recited in claim 11; andb) generating electricity, wherein no less than 18% of the thermal power for generating the electricity originates from the overheated water vapor and a remainder of the thermal power for generating the electricity originates from the saturated water vapor.