System and method for small, clean, steady-state fusion reactors
According to some embodiments, a system for widening and densifying a scrape-off layer (SOL) in a field reversed configuration (FRC) fusion reactor is disclosed. The system includes a gas box at one end of the reactor including a gas inlet system and walls of suitable heat bearing materials. The system further includes an exit orifice adjoining the gas box, wherein the exit orifice has a controllable radius and length to allow plasma to flow out from the gas box to populate the SOL with the plasma. The system may also include fusion products, which decrease in speed in the plasma in the SOL, allowing energy to be extracted and converted into thrust or electrical power and further allowing ash to be extracted to reduce neutron emissions and maintain high, steady-state fusion power.
1. A method for increasing 3 He supply for use in field reversed configuration (FRC) fusion reactors, comprising:
burning deuterium (D) with D in a first FRC reactor to breed first helium-3 ( 3 He) and tritium (T);
separating the first 3 He from the T through a permeable membrane in the first FRC reactor;
producing power in the first FRC reactor by burning the first 3 He with the D in the first FRC reactor;
storing the T for a predetermined period of time such that the T transmutes to second 3 He; and
producing power in a second FRC reactor by burning the second 3 He with D in the second FRC reactor.
2. The method of claim 1 , wherein breeding first 3 He and T comprises exhausting ash that includes the first 3 He and T through an exhaust plume in the first FRC reactor.
3. The method of claim 2 , wherein the ash is exhausted before it can fuse.
4. The method of claim 1 , wherein breeding first 3 He and T comprises exhausting ash that includes the first 3 He and T through a gas box in the first FRC reactor.
5. The method of claim 1 , wherein separating the first 3 He from the T comprises separating via superpermeation.
6. The method of claim 1 , wherein separating the first 3 He from the T comprises separating via at least one of a thermal, chemical, and centrifugal process.
7. The method of claim 1 , further comprising separating the first 3 He from 4 He via a gas centrifuge system in the first FRC reactor.
8. The method of claim 1 , wherein the first 3 He and the D-D are burned at a ratio of 1:10 in the first FRC reactor.
9. The method of claim 1 , wherein the predetermined period of time comprises 10 to 20 years.
10. The method of claim 1 , wherein producing power in a second FRC reactor further comprises burning D.
11. The method of claim 10 , wherein the second 3 He and D are burned at a ratio of 3:1 in the second FRC reactor.