Compressed gas energy storage system
A compressed air energy storage system may have an accumulator and a thermal storage subsystem having a cold storage chamber for containing a supply of granular heat transfer, a hot storage chamber and at least a first mixing chamber in the gas flow path and having an interior in which the compressed gas contacts the granular heat transfer particles at a mixing pressure that is greater than the cold storage pressure and the hot storage pressure and a conveying system operable to selectably move the granular heat transfer particles from the cold storage chamber, through the first mixing chamber and into the hot storage chamber, and vice versa.
1. A compressed air energy storage system comprising:
a) a container configured to contain compressed gas at a storage pressure;
b) a gas compressor/expander subsystem comprising at least a first compression stage having a first gas inlet and a gas outlet in fluid communication with the container via a gas flow path for conveying compressed gas at the storage pressure to the container when in a charging mode and from the container when in a discharging mode;
c) a thermal storage subsystem comprising:
i) a cold storage chamber for containing a supply of granular heat transfer particles at a cold temperature and cold storage pressure;
ii) a hot storage chamber for containing the supply of granular heat transfer particles at a hot temperature and hot storage pressure;
iii) at least a first mixing chamber in the gas flow path and having an interior in which the compressed gas contacts the granular heat transfer particles at a mixing pressure that is greater than the cold storage pressure and the hot storage pressure;
iv) a conveying system operable to selectably move the granular heat transfer particles from the cold storage chamber, through the first mixing chamber and into the hot storage chamber, and vice versa;
wherein:
when the compressed air energy storage system is in the charging mode i) granular heat transfer particles are conveyed from the cold storage chamber into the first mixing chamber, ii) thermal energy is transferred to the granular heat transfer particles within the first mixing chamber from the compressed gas stream being conveyed into the container via the first mixing chamber thereby heating the granular heat transfer particles and cooling the compressed gas, and iii) the heated granular heat transfer particles are conveyed from the first mixing chamber toward the hot storage chamber for storage and the cooled compressed stream is conveyed from the first mixing chamber toward the container for storage; and
when the compressed gas energy storage system is in the discharging mode i) granular heat transfer particles are conveyed from the hot storage chamber into the first mixing chamber, ii) thermal energy is transferred from the granular heat transfer particles within the first mixing chamber to the compressed gas stream being conveyed out of the container via the first mixing chamber thereby cooling the granular heat transfer particles and heating the compressed gas and iii) the cooled granular heat transfer particles are conveyed from the first mixing chamber toward the cold storage chamber for storage and the heated compressed stream is conveyed from the first mixing chamber toward the compressor/expander subsystem for expansion.
2. The compressed air energy storage system of claim 1 , wherein the mixing pressure is substantially the same as the storage pressure and wherein the hot storage chamber is spaced apart from and fluidly isolated from the cold storage chamber.
3. The compressed air energy storage system of claim 1 , wherein the first mixing chamber has
d) a gas inlet by which compressed gas can enter the first mixing chamber,
e) a gas outlet by which compressed gas can exit the first mixing chamber,
f) a particle inlet by which the granular heat transfer particles can enter the first mixing chamber;
g) a particle outlet by which the granular heat transfer particles can exit the first mixing chamber and
wherein the conveying system comprises an inlet airlock at the particle inlet that is operable to permit passage of the granular heat transfer particles at the cold or hot storage temperature into the first mixing chamber interior while substantially maintaining the interior at the mixing pressure.
4. The compressed air energy storage system of claim 3 , wherein the conveying system comprises an outlet airlock at the particle outlet that is operable to permit passage of the granular heat transfer particles at the cold or hot storage temperature out of the first mixing chamber interior while substantially maintaining the interior at the mixing pressure and wherein the mixing chamber is configured in a counter-flow arrangement in which the granular heat transfer particles move from the particle inlet to the particle outlet in a first flow direction and the compressed gas moves from the gas inlet to the gas outlet in a generally opposing, second flow direction.
5. The compressed air energy storage system of claim 1 , wherein the granular heat transfer particles are conveyed in a generally continuous flow manner between the cold storage tank and hot storage tank when the system is the charging or discharging mode (as compared to a batch process).
6. The compressed air energy storage system of claim 1 , wherein the granular heat transfer particles are conveyed in a generally batch process between the cold storage tank and hot storage tank when the system is the charging or discharging mode.
7. The compressed air energy storage system of claim 1 , wherein the mixing pressure is greater than atmospheric pressure and is substantially equal to the storage pressure.
8. The compressed air energy storage system of claim 1 , wherein the hot storage chamber is at a lower pressure than the first mixing chamber.
9. The compressed air energy storage system of claim 1 , wherein the hot storage pressure is less than about 10% of the storage pressure.
10. The compressed air energy storage system of claim 1 , wherein the hot storage chamber is at substantially atmospheric pressure.
11. The compressed air energy storage system of claim 1 , wherein the cold storage chamber is at a lower pressure than the mixing chamber.
12. The compressed air energy storage system of claim 1 , wherein the cold storage pressure is less than about 10% of the storage pressure.
13. The compressed air energy storage system of claim 1 , wherein the cold storage chamber is at substantially the same pressure as the hot storage chamber.
14. The compressed air energy storage system of claim 1 , wherein a capacity of the cold storage chamber is greater than a capacity of the first mixing chamber.
15. A method of temporarily storing thermal energy via a thermal storage subsystem in a compressed air energy storage system comprising a container configured to contain compressed gas at a storage pressure and a gas compressor/expander subsystem comprising at least a first compression stage having a first gas inlet and a gas outlet in fluid communication with the container via a gas flow path for conveying compressed gas to the container when in a charging mode and from the container when in a discharging mode, the method comprising:
h) during the charging mode:
i) conveying a first portion of cold granular heat transfer particles from a cold storage chamber into an interior of a mixing chamber;
ii) contacting the first portion of cold granular heat transfer particles in the interior with the compressed gas traveling from the gas compressor/expander subsystem into the container, thereby transferring thermal energy from the compressed gas to the first portion of cold granular heat transfer particles thereby providing a first portion of warmed granular heat transfer particles;
iii) conveying the first portion of warmed granular heat transfer particles from the interior of the mixing chamber into a hot storage chamber;
iv) conveying a second portion of cold granular heat transfer particles from the cold storage chamber into the interior of the mixing chamber;
v) contacting the second portion of cold granular heat transfer particles in the interior with the compressed gas traveling from the gas compressor/expander subsystem into the container, thereby transferring thermal energy from the compressed gas to the second portion of cold granular heat transfer particles and providing a second portion of warmed granular heat transfer particles;
vi) conveying the second portion of warmed granular heat transfer particles from the interior of the mixing chamber into a hot storage chamber.
16. The method of claim 15 , wherein the first portion of cold granular heat transfer particles comprises only a portion of the total quantity of cold granular heat transfer particles contained in the cold storage chamber.
17. The method of claim 15 , wherein steps i) to vi) are conducted in a generally continuous manner whereby at least some of the first portion of cold granular heat transfer particles is in the mixing chamber at the same time as the second portion of cold granular heat transfer particles is introduced into the mixing chamber.
18. The method of claim 15 , further comprising only partially charging the container wherein the first portion of warmed granular heat transfer particles and second portion of warmed granular heat transfer particles are stored within the hot storage chamber and wherein a third portion of cold granular heat transfer particles remains within the cold storage chamber and does not enter the mixing chamber.
19. The method of claim 15 , wherein after steps i) to vi) have been completed a third portion of cold granular heat transfer particles remains within the cold storage chamber.
20. The method of claim 15 , wherein at least some of the first portion of warmed granular heat transfer particles.