sCO2 power conversion system
A power conversion system includes a closed first loop and a closed second loop. The first loop includes a first compressor, a first recuperator in parallel with an interloop heat exchanger, a first heater, a first turbine, and the first recuperator arranged in series. The first recuperator transfers enthalpy from an expanded portion of a first working fluid to a compressed portion of the first working fluid. The second loop includes a second compressor, a second recuperator, a second heater, a second turbine, the second recuperator, and the interloop heat exchanger, arranged in series. The second recuperator transfers enthalpy from an expanded portion of a second working fluid to a compressed portion of the second working fluid, and the interloop heat exchanger transfers enthalpy from the second working fluid to the first working fluid.
1 . A power conversion system, comprising:
a first loop having, arranged in seriatim, a first compressor, a first recuperator in parallel with an interloop heat exchanger, a first heater, a first turbine, the first recuperator, and a first cooler, the first loop being a closed loop containing a first working fluid, the first recuperator transferring enthalpy from an expanded portion of the first working fluid to a compressed portion of the first working fluid; and
a second loop having, arranged in seriatim, a second compressor, a second recuperator, a second heater, a second turbine, the second recuperator, and the interloop heat exchanger, the second loop being a closed loop containing a second working fluid, the second recuperator transferring enthalpy from an expanded portion of the second working fluid to a compressed portion of the second working fluid, the interloop heat exchanger transferring enthalpy from the second working fluid to the first working fluid.
2 . The power conversion system of claim 1 , wherein the first loop further comprises a second recuperator, the second recuperator being configured to transfer enthalpy from the expanded portion of the first working fluid located between the first recuperator and the first turbine to the compressed portion of the first working fluid located between the first recuperator and the first heater.
3 . The power conversion system of claim 1 , wherein at least one of the first and second turbines is coupled to a generator so that rotation of the turbine drives the generator to generate electrical power.
4 . The power conversion system of claim 1 , wherein the first and second turbines are coupled to a first generator and a second generator, respectively, rotation of each of the first and second turbines driving the corresponding generator of the first and second generators to generate electrical power.
5 . The power conversion system of claim 1 , wherein the first working fluid is sCO2.
6 . The power conversion system of claim 5 , wherein the second working fluid is sCO2.
7 . The power conversion system of claim 6 , wherein a temperature of the first working fluid entering the first turbine is approximately 600° C.
8 . The power conversion system of claim 7 , wherein a temperature of the second working fluid entering the second turbine is approximately 600° C.
9 . The power conversion system of claim 6 , wherein a maximum pressure of the first and second working fluids is 200 bar.
10 . The power conversion system of claim 9 , wherein a minimum pressure of the first and second working fluids is 77 bar.
11 . The power conversion system of claim 1 , wherein the first heater and the second heater are part of a closed heating loop having a third working fluid.
12 . The power conversion system of claim 11 , wherein the heating loop further includes a thermal energy source configured to provide enthalpy to the third working fluid.
13 . The power conversion system of claim 12 , wherein the thermal energy source comprises a nuclear reactor.
14 . The power conversion system of claim 11 , wherein the first and second heaters are arranged in parallel.
15 . The power conversion system of claim 11 , wherein the third working fluid is sCO2.
16 . The power conversion system of claim 1 , wherein the second loop is configured to provide power to start the first loop at startup.
17 . The power conversion system of claim 16 , wherein the second loop further includes a second cooler disposed between the interloop heat exchanger and the second compressor.
18 . The power conversion system of claim 1 , wherein the first loop is configured to provide power to start the second loop at startup.