Apparatus and method for plasma synthesis of graphitic products including graphene

1. A method of synthesizing graphitic products including graphene, the method comprising:

supplying a process gas to a plasma nozzle that is coupled to a reaction chamber, the process gas comprising a carbon-containing species;

supplying radio frequency radiation to the process gas within the plasma nozzle, so as to produce a non-equilibrium plasma within the plasma nozzle, and passing the process gas through a radio frequency radiation field within the plasma nozzle, to thereby cause cracking of the carbon-containing species within the plasma nozzle, wherein the radio frequency radiation comprises microwave radiation;

forming multiple vortices in the process gas within the plasma nozzle and subjecting the multiple vortices to the microwave radiation;

wherein the plasma nozzle is arranged such that an afterglow of the plasma extends into the reaction chamber, the cracked carbon-containing species also passes into the reaction chamber, and the cracked carbon-containing species recombines within the afterglow, so as to form the graphitic products including the graphene;

applying cooling to the afterglow on exiting the plasma nozzle, wherein the cooling comprises one of water cooling or gas cooling;

subjecting the reaction chamber to gas filtration to collect solid carbon from the gas phase, wherein the gas filtration is performed using a gas filtration system that is attached above the reaction chamber and comprises an elongate chamber comprising one or more filter candles; and

blowing gas through the elongate chamber to dislodge the graphitic products collected by the one or more filter candles as a result of the gas filtration, to cause the graphitic products collected by the one or more filter candles to fall down, through the reaction chamber, for extraction through an exit at the bottom of the reaction chamber.

2. The method according to claim 1 , further comprising generating the plasma at substantially atmospheric pressure.

3. The method according to claim 1 , wherein the carbon-containing species comprises one of natural gas, CH 4 , C 2 H 6 , C 2 H 4 , C 3 H 8 or C 4 H 10 .

4. The method according to claim 1 , wherein the process gas further comprises a buffer gas, the buffer gas comprising one of argon, nitrogen, or helium; and

wherein the ratio of carbon-containing species to buffer gas in the process gas is 50:50 or less; or around 20:80.

5. The method according to claim 1 , wherein the process gas further comprises a buffer gas, the buffer gas comprising carbon dioxide.

6. The method according to claim 1 , wherein the afterglow within the reaction chamber has an operating temperature of lower than 3500° C., lower than 1000° C., or around 300° C.; and

wherein the temperature outside the plasma nozzle, at the carbon formation point within the afterglow, is in the range of 800° C. to 1200° C.

7. The method according to claim 1 , further comprising delivering gas around an interface between the plasma nozzle and the reaction chamber.

8. The method according to claim 1 , further comprising extracting the graphitic products using a continuous extraction process.

9. The method according to claim 1 , wherein the carbon-containing species is cracked without the process gas being introduced into a thermal zone;

wherein no catalyst is used in forming the graphitic products; and

wherein no external heating is applied during the formation of the graphitic products.