Adiabatic salt energy storage
Efficient energy storage is provided by using a working fluid flowing in a closed cycle including a ganged compressor and turbine, and capable of efficient heat exchange with heat storage fluids on a hot side of the system and on a cold side of the system. This system can operate as a heat engine by transferring heat from the hot side to the cold side to mechanically drive the turbine. The system can also operate as a refrigerator by mechanically driving the compressor to transfer heat from the cold side to the hot side. Heat exchange between the working fluid of the system and the heat storage fluids occurs in counter-flow heat exchangers. In a preferred approach, molten salt is the hot side heat storage fluid and water is the cold side heat storage fluid.
1. A method for storing and releasing energy, the method comprising:
(a) increasing a pressure of a working fluid operating in a closed cycle from a first pressure to a second pressure with the aid of a compressor, thereby increasing a temperature of the working fluid;
(b) using a first heat storage unit downstream of the compressor and in thermal communication with the working fluid for (i) in a storing mode, removing heat from the working fluid and decreasing the temperature of the working fluid, wherein the decrease in temperature of the working fluid by the first heat storage unit occurs at substantially the second pressure, or (ii) in a releasing mode, supplying heat to the working fluid and increasing the temperature of the working fluid, wherein the increase in temperature of the working fluid by the first heat storage unit occurs at substantially the second pressure;
(c) decreasing the pressure of the working fluid from the second pressure to the first pressure with the aid of a turbine, thereby decreasing the temperature of the working fluid;
(d) using a second heat storage unit downstream of the turbine and in thermal communication with the working fluid for (i) in the storing mode, supplying heat to the working fluid and increasing the temperature of the working fluid, wherein the increase in temperature of the working fluid by the second heat storage unit occurs at substantially the first pressure, or (ii) in the releasing mode, removing heat from the working fluid and decreasing the temperature of the working fluid, wherein the decrease in temperature of the working fluid by the second heat storage unit occurs at substantially the first pressure,
wherein the working fluid flows in a same direction in the closed cycle when in the storing mode as when in the releasing mode, and
wherein the working fluid flows through the compressor, the first heat storage unit, the turbine, and the second heat storage unit in both the storing mode and the releasing mode.
2. The method of claim 1 , wherein the second heat storage unit has a range of operating temperatures that is lower than the range of operating temperatures of the first heat storage unit.
3. The method of claim 1 , wherein the first and second heat storage units have comparable total heat capacities.
4. The method of claim 1 , wherein the first heat storage unit comprises a heat storage fluid that includes molten salt.
5. The method of claim 4 , wherein the molten salt comprises sodium nitrite and/or potassium nitrate.
6. The method of claim 1 , wherein the first and/or second heat storage unit comprises a heat storage fluid that is liquid at a range of operating temperatures of the heat storage fluid.
7. The method of claim 1 , wherein the second heat storage unit comprises a heat storage fluid that is at ambient pressure.
8. The method of claim 1 , wherein a radiator is operationally coupled to the first heat storage unit.
9. The method of claim 1 , wherein the compressor and the turbine are operably coupled such that they rotate together.
10. The method of claim 1 , wherein the working fluid is Argon.
11. A system for storing and releasing electrical energy, comprising:
a first heat exchanger;
a second heat exchanger; and
a controller programmed to regulate (i) a temperature difference between at least two thermally-coupled fluids in the heat exchangers, and/or (ii) one or more fluid properties of the fluids in the heat exchangers,
wherein the first heat exchanger and second heat exchanger each comprise a thermal storage fluid that directs thermal energy into or extracts thermal energy from a circulatory fluid flow path, wherein the circulatory fluid flow path comprises a working fluid that flows in a same direction in the circulatory fluid flow path when storing electrical energy as when releasing electrical energy, wherein the working fluid flows through a compressor, the first heat exchanger, a turbine, and the second heat exchanger in both a storing mode and a releasing mode.