Continuous production of carbon nanomaterials using a high temperature inductively coupled plasma
High-power inductively coupled plasma technology is used for thermal cracking and vaporization of continuously fed carbonaceous materials into elemental carbon, for reaction with separate and continuously fed metal catalysts inside a gas-phase high-temperature reactor system operating at or slightly below atmospheric pressures. In one particularly preferred embodiment, in-flight growth of carbon nanomaterials is initiated, continued, and controlled at high flow rates, enabling continuous collection and product removal via gas/solid filtration and separation methods, and/or liquid spray filtration and solid collection methods suitable for producing industrial-scale production quantities. In another embodiment, the reaction chamber and/or filtration/separation media include non-catalytic or catalytic metals to simultaneously or separately induce on-substrate synthesis and growth of carbon nanomaterials. The on-substrate grown carbon nanomaterials are produced in secondary chambers that are selectively isolated for periodic removal of the product.
1. A method for producing carbon nanomaterials (CNMs) in a reactor using an inductively coupled plasma (ICP), comprising the steps of:
(a) introducing the ICP into the reactor;
(b) introducing a carbonaceous material into the reactor, such that the ICP heats and reacts with the carbonaceous material to produce free carbon;
(c) introducing a catalyst into the reactor, the catalyst having been selected to enhance the production of CNMs from the free carbon in the reactor;
(d) providing a secondary reaction chamber, the secondary reaction chamber providing additional residence time to promote the growth of longer CNMs;
(e) using supplemental heat to maintain the temperature conditions in the secondary reaction chamber above a threshold value required to facilitate the additional growth of the CNMs; and
(f) introducing additional carbonaceous materials into the secondary reaction chamber to provide carbon to facilitate the additional growth of the CNMs.
2. The method of claim 1 , wherein:
(a) the step of introducing the ICP into the reactor comprises the step of introducing the ICP into the reactor continuously for an extended period of time;
(b) the step of introducing the carbonaceous material into the reactor comprises the step of introducing the carbonaceous material into the reactor continuously for an extended period of time; and
(c) the step of introducing the catalyst into the reactor comprises the step of introducing the catalyst into the reactor continuously for an extended period of time.
3. The method of claim 1 , wherein the step of introducing the ICP into the reactor comprises the step of establishing a gas flow within the reactor.
4. The method of claim 3 , wherein the step of introducing the carbonaceous material into the reactor comprises the step of introducing the carbonaceous material into the gas flow.
5. The method of claim 3 , wherein the step of introducing the catalyst into the reactor comprises the step of introducing the catalyst into the gas flow.
6. The method of claim 3 , wherein:
(a) the step of introducing the carbonaceous material into the reactor comprises the step of introducing the carbonaceous material into the gas flow; and
(b) the step of introducing the catalyst into the reactor comprises the step of introducing the catalyst into the gas flow, such that the catalyst stimulates the production of CNMs within the gas flow in the reactor.
7. The method of claim 1 , wherein the step of introducing the ICP into the reactor comprises the step of using an inert gas to generate the ICP.
8. The method of claim 7 , wherein the step of using an inert gas to generate the ICP comprises the step of using an inert gas that includes only traces of nitrogen, to avoid generation of cyanide species.
9. The method of claim 7 , wherein the inert gas comprises at least one of argon and helium.
10. The method of claim 9 , wherein the inert gas comprises a mixture of argon and helium.
11. The method of claim 9 , wherein the inert gas further comprises hydrogen in addition to at least one of argon and helium.
12. The method of claim 1 , wherein the step of introducing the ICP into the reactor comprises the step of using a reactive gas to generate the ICP.
13. The method of claim 12 , wherein the step of using a reactive gas to generate the ICP comprises the step of using carbon monoxide.
14. The method of claim 1 , wherein the step of introducing the catalyst into the reactor comprises the step of introducing at least one of a metal powder, a metal salt, and a metal carbonyl into the reactor.
15. The method of claim 1 , wherein the catalyst comprises at least one of: nickel, cobalt, iron, a Group III transition metal, a Group VI transition metal, a Group VII transition metal, and a Group VIII transition metal.
16. The method of claim 1 , wherein the step of introducing the catalyst into the reactor comprises the step of introducing the catalyst into the reactor such that the production of single wall carbon nanotubes is favored.
17. The method of claim 1 , wherein the step of introducing the catalyst into the reactor comprises the step of introducing the catalyst into the reactor such that the production of multi wall carbon nanotubes is favored.
18. The method of claim 1 , further comprising the step of filtering a process gas exiting the reactor to recover the catalyst.
19. The method of claim 18 , further comprising the step of recycling the catalyst by reintroducing the catalyst into the reactor.
20. The method of claim 1 , further comprising the step of filtering a process gas exiting the reactor to recover the CNMs.
21. The method of claim 20 , wherein the step of filtering the process gas exiting the reactor to recover the CNMs further comprises the step of sorting the CNMs by size.
22. The method of claim 21 , wherein the step of sorting the CNMs by size comprises the step of using a differential mobility analyzer to sort the CNMs by size.
23. The method of claim 20 , further comprising the step of incorporating the CNMs that are recovered into a product.
24. The method of claim 20 , further comprising the step of purifying the CNMs that are recovered.
25. The method of claim 24 , wherein the step of purifying the CNMs that are recovered comprises the step of separating the CNMs from the catalyst.
26. The method of claim 24 , wherein the step of purifying the CNMs that are recovered comprises the step of separating the CNMs from less valuable carbon materials produced in the reactor.
27. The method of claim 1 , further comprising the step of directing a process gas exiting the reactor into a secondary reactor.
28. The method of claim 1 , further comprising the step of directing the gas flow over a substrate, such that CNMs are formed on the substrate.
29. The method of claim 1 , wherein the reactor that does not include structures that would inhibit a free flow of gas within the reactor.
30. The method of claim 1 , wherein internal surfaces of the reactor are substantially non metallic, such that a deposition of CNMs on the internal surfaces of the reactor is minimized.
31. The method of claim 1 , wherein internal surfaces of the reactor are smooth.
32. The method of claim 1 , wherein internal surfaces of the reactor comprise at least one of a glass, a ceramic, and quartz.
33. The method of claim 1 , further comprising the step of establishing a negative pressure condition within the reactor, such that the gas flow is pulled through the reactor.
34. The method of claim 1 , wherein the step of introducing the carbonaceous material into the reactor comprises the step of introducing the carbonaceous material into the reactor at more than one location, in order to prevent carbon concentrations in any one part of the reactor to favor the formation of soot.
35. A method for producing carbon nanomaterials (CNMs) using an inductively coupled plasma (ICP), comprising the steps of:
(a)using an inert gas to generate the ICP;
(b)using the ICP to establish a gas flow;
(c) introducing a carbonaceous material into the gas flow, such that the ICP reacts with the carbonaceous material to produce free carbon;
(d) introducing a catalyst into the gas flow, such that the catalyst stimulates the combination of free carbon to form CNMs within the gas flow; and
(e) filtering the gas flow to remove CNMs entrained therein.
36. The method of claim 35 , wherein the step of using an inert gas to generate the ICP comprises at least one of the steps of:
(a) using an inert gas that includes only traces of nitrogen, to avoid generation of cyanide species;
(b) using at least one of argon and helium for the inert gas;
(c) using a mixture of argon and helium for the inert gas; and
(d) using a mixture of at least one inert gas and hydrogen.
37. The method of claim 35 , wherein the step of introducing the catalyst into the gas flow comprises the step of introducing at least one of: nickel, cobalt, iron, a Group III transition metal, a Group VI transition metal, a Group VII transition metal, and a Group VIII transition metal into the gas flow.
38. The method of claim 35 , further comprising the step of filtering the gas flow to recover the catalyst.
39. The method of claim 35 , wherein the step of filtering the gas flow to remove the CNMs further comprises the step of sorting the CNMs by size.
40. The method of claim 35 , further comprising the step of purifying the CNMs using at least one of the steps of:
(a) separating the CNMs from the catalyst; and
(b) separating the CNMs from less valuable carbon materials produced in the gas flow.
41. The method of claim 35 , further comprising the step of directing the gas flow over a substrate, such that CNMs are formed on the substrate.
42. The method of claim 35 , wherein the step of introducing the catalyst into the gas flow comprises the step of introducing the catalyst into the gas flow such that the production of single wall carbon nanotubes is favored.
43. The method of claim 35 , wherein the step of introducing the catalyst into the gas flow comprises the step of introducing the catalyst into the gas flow such that the production of multi wall carbon nanotubes is favored.
44. The method of claim 35 , wherein the step of introducing the carbonaceous material into the gas flow comprises the step of introducing the carbonaceous material into the gas flow at more than one location, in order to prevent carbon concentrations in any one part of the gas flow to favor the formation of soot.
45. A method for producing carbon nanomaterials (CNMs) in a reactor using an inductively coupled plasma (ICP), comprising the steps of:
(a) introducing the ICP into the reactor;
(b) introducing a carbonaceous material into the reactor, such that the ICP heats and reacts with the carbonaceous material to produce free carbon;
(c) introducing a catalyst into the reactor, the catalyst having been selected to enhance the production of CNMs from the free carbon in the reactor;
(d) filtering a process gas exiting the reactor to recover the catalyst; and
(e) recycling the catalyst by reintroducing the catalyst into the reactor.
46. A method for producing carbon nanomaterials (CNMs) in a reactor using an inductively coupled plasma (ICP), comprising the steps of:
(a) using an inert gas to generate the ICP;
(b) introducing the ICP into the reactor;
(c) introducing a carbonaceous material into the reactor, such that the ICP heats and reacts with the carbonaceous material to produce free carbon; and
(d) introducing a catalyst into the reactor, the catalyst having been selected to enhance the production of CNMs from the free carbon in the reactor.