Process for making single-wall carbon nanotubes utilizing refractory particles

• US 20030147802A1
• Filed: 11/20/2002
• Published: 08/07/2003
• Est. Priority Date: 11/21/2001
• Status: Active Grant

• Current Assignee: Rice University
• Original Assignee: Rice University
• Inventors: Smalley, Richard E., Hauge, Robert H.
• Granted Patent: US 7,138,100 B2
• Time in Patent Office: Days
• US Class Current: 423/447.3
• CPC Class Codes: B82Y 30/00 Nanotechnology for materials or surface science, e.g. nanocomposites
• CPC Class Codes: D01F 9/1278 Carbon monoxide
• CPC Class Codes: Y10S 977/842 for carbon nanotubes or fullerenes

Abstract

A continuous gas-phase method for producing single-wall carbon nanotubes at high catalyst productivity and high yield is disclosed. The method involves the use of a novel in-situ formed catalyst to initiate and grow single-wall carbon nanotubes using a carbon-containing feedstock in a high temperature and pressure process. The catalyst comprises in-situ-generated transition metal particles in contact with in-situ-generated refractory particles. The population of nucleating sites for single-wall carbon nanotubes is enhanced due to the ease of formation of a population of refractory particles. These, in turn, improve the nucleation and stability of the transition metal particles that grow on them. The larger number of transition metal particles translate into a larger number of sites for single-wall carbon nanotube production. The higher catalyst yields provide a means for obtaining higher purity single-wall carbon nanotubes.

Claims

1. A method for producing single-wall carbon nanotubes comprising:

(a) providing a transition metal catalyst precursor stream comprising a carrier gas and a transition metal catalyst precursor comprising at least one atom of at least one transition metal selected from the group consisting of Group VIb elements, Group VIIIb elements and combinations thereof, wherein the transition metal catalyst precursor stream is at a temperature below the decomposition temperature of the transition metal catalyst precursor;

(b) providing a refractory precursor stream comprising a carrier gas and a refractory precursor, wherein the refractory precursor is at a temperature below the thermolysis temperature of the refractory precursor;

(c) providing a carbon-containing feedstock gas stream at a temperature above the minimum single-wall carbon nanotube formation initiation temperature; and

(d) mixing the carbon-containing feedstock gas stream with the transition metal catalyst precursor stream and the refractory precursor stream to form a mixed gas stream, wherein

(i) the transition metal catalyst precursor reaches a temperature above the decomposition temperature of the transition metal catalyst precursor,

(ii) the refractory precursor reaches a temperature above which the thermolysis temperature of the refractory precursor and forms refractory particles,

(iii) the temperature is sufficient to promote the initiation and growth of metal catalyst clusters on the refractory particles, and

(iv) the temperature is sufficient to promote the initiation and growth of single-wall carbon nanotubes on the metal catalyst clusters and to form the single-wall carbon nanotubes in the mixed gas stream.

2. The method of claim 1, wherein the carrier gas comprises a compound selected from the group consisting of CO, nitrogen, inert gases and mixtures thereof.

3. The method of claim 1, wherein the carrier gas comprises CO.

4. The method of claim 1 wherein the transition metal catalyst precursor comprises an element selected from the group consisting of chromium, molybdenum, tungsten, iron, nickel, cobalt, ruthenium, rhenium, palladium, osmium, iridium, platinum, and combinations thereof.

5. The method of claim 1 wherein the transition metal catalyst precursor comprises a carbonyl.

6. The method of claim 5 wherein the carbonyl is selected from the group consisting of Fe(CO)₅, Ni(CO)₄, and combinations thereof.

7. The method of claim 1 wherein the refractory precursor comprises a metal element selected from the group consisting of aluminum, magnesium, silicon, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, rhenium, uranium, rare earth elements and mixtures thereof.

8. The method of claim 1 wherein the refractory precursor comprises a compound selected from the group consisting of tetramethoxysilane, trimethoxymethyl-silane, hexamethylsilicane, titanium isopropoxide, trimethylaluminum, aluminum isopropylate, titanium tetrachloride, silicon tetrachloride, niobium pentachloride, niobium pentafluoride, tantalum pentachloride, tantalum pentafluoride, tungsten hexafluoride, uranium hexafluoride and combinations thereof.

9. The method of claim 1 wherein the refractory precursor is volatile.

10. The method of claim 1 wherein the refractory precursor is sublimable.

11. The method of claim 1 wherein the refractory particles comprise compounds selected from the group consisting of metal oxides, carbides, oxycarbides, carbonitrides, nitrides, sulfides, borides and combinations thereof.

12. The method of claim 1 wherein the refractory particles comprise a refractory material selected from the group consisting of comprising ceramic, zeolite, mullite, alumina, silica, aluminosilicate, titania, zirconia, magnesia, rare earth oxides, cerium oxide, lanthanum oxide and combinations thereof.

13. The method of claim 1 wherein the refractory precursor is present in a greater concentration than the transition metal catalyst precursor.

14. The method of claim 1, wherein the carbon-containing feedstock gas comprises a gas selected from the group consisting of CO, hydrocarbons, and mixtures thereof.

15. The method of claim 1, wherein the carbon-containing feedstock gas comprises CO.

16. The method of claim 1, wherein the pressure of the mixed gas stream is between about 3 atm and about 1000 atm.

17. The method of claim 1, wherein the temperature of the mixed gas stream is in a range of about 850°

C. and about 1500°

C.

18. The method of claim 1, wherein the temperature of the mixed gas stream is in a range of about 900°

C. and about 1100°

C.

19. The method of claim 1 further comprising recovering a single-wall carbon nanotube product from the mixed gas stream.

20. The method of claim 19, wherein the recovering step comprises passing the mixed gas stream through a gas-permeable filter.

21. A method for producing single-wall carbon nanotubes comprising:

(a) providing a transition metal catalyst precursor stream comprising a carrier gas and a transition metal catalyst precursor comprising at least one atom of at least one transition metal selected from the group consisting of Group VIb elements, Group VIIIb elements and combinations thereof, wherein the transition metal catalyst precursor stream is at a temperature below the decomposition temperature of the transition metal catalyst precursor;

(b) providing a refractory precursor stream, comprising a carrier gas and a refractory precursor,

(c) providing a refractory reactant stream comprising a refractory reactant compound capable of reacting with the refractory precursor to form a refractory material;

(d) providing a carbon-containing feedstock gas stream at a temperature above the minimum single-wall carbon nanotube formation initiation temperature; and

(e) mixing the carbon-containing feedstock gas stream with refractory precursor stream, the refractory reactant stream, and the transition catalyst precursor stream to form a mixed gas stream, wherein

(i) the transition metal catalyst precursor reaches a temperature above the decomposition temperature of the transition metal catalyst precursor,

(ii) the refractory precursor reacts with the refractory reactant to form refractory particles,

(iii) the temperature is sufficient to promote the initiation and growth of metal catalyst clusters on the refractory particles, and

(iv) the temperature is sufficient to promote the initiation and growth of single-wall carbon nanotubes on the metal catalyst clusters and to form the single-wall carbon nanotubes in the mixed gas stream.

22. The method of claim 21, wherein the carrier gas comprises a compound selected from the group consisting of CO, nitrogen, inert gases and mixtures thereof.

23. The method of claim 21, wherein the carrier gas comprises CO.

24. The method of claim 21, wherein the transition metal catalyst precursor comprises an element selected from the group consisting of chromium, molybdenum, tungsten, iron, nickel, cobalt, ruthenium, rhenium, palladium, osmium, iridium, platinum, and combinations thereof.

25. The method of claim 21, wherein the transition metal catalyst precursor comprises a carbonyl.

26. The method of claim 25, wherein the carbonyl is selected from the group consisting of Fe(CO)₅, Ni(CO)₄, and combinations thereof.

27. The method of claim 21 wherein the refractory precursor comprises a metal element selected from the group consisting of aluminum, magnesium, silicon, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, rhenium, uranium, rare earth elements and mixtures thereof.

28. The method of claim 21 wherein the refractory precursor comprises a compound selected from the group consisting of tetramethoxysilane, trimethoxymethylsilane, hexamethylsilicane, titanium isopropoxide, trimethylaluminum, aluminum isopropylate, titanium tetrachloride, silicon tetrachloride, niobium pentachloride, niobium pentafluoride, tantalum pentachloride, tantalum pentafluoride, tungsten hexafluoride, uranium hexafluoride and combinations thereof.

29. The method of claim 21 wherein the refractory precursor is volatile.

30. The method of claim 21 wherein the refractory precursor is sublimable.

31. The method of claim 21 wherein the refractory precursor is present in a greater concentration than the transition metal catalyst precursor.

32. The method of claim 21 wherein the refractory precursor comprises trimethylaluminum.

33. The method of claim 21 wherein the refractory reactant comprises water.

34. The method of claim 21 wherein the refractory precursor comprises trimethylaluminum and the refractory reactant comprises water.

35. The method of claim 34 wherein the trimethylaluminum and the water are in a ratio of at least about 1 part TMA to 3 parts water.

36. The method of claim 34 wherein the trimethylaluminum and the water are in a ratio of at least about 2 parts TMA to 3 parts water.

37. The method of claim 34 wherein the trimethylaluminum and the water are in a ratio of at least about 6 parts TMA to 1 part water.

38. The method of claim 21 wherein the refractory particles comprise compounds selected from the group consisting of metal oxides, carbides, oxycarbides, carbonitrides, nitrides, sulfides, borides and combinations thereof.

39. The method of claim 21 wherein the refractory particles comprise refractory material selected from the group comprising ceramic, zeolite, mullite, alumina, silica, aluminosilicate, titania, zirconia, magnesia, rare earth oxides, cerium oxide, lanthanum oxide and combinations thereof.

40. The method of claim 21 wherein the refractory particles comprise alumina.

41. The method of claim 21, wherein the carbon-containing feedstock gas comprises a gas selected from the group consisting of CO, hydrocarbons, and mixtures thereof.

42. The method of claim 21, wherein the carbon-containing feedstock gas comprises CO.

43. The method of claim 21, wherein the pressure of the mixed gas stream is in a range of about 3 atm and about 1000 atm.

44. The method of claim 21, wherein the temperature of the mixed gas stream is in a range of about 850°

C. and about 1500°

C.

45. The method of claim 21, wherein the temperature of the mixed gas stream is in a range of about 900°

C. and about 1100°

C.

46. The method of claim 21 further comprising recovering a single-wall carbon nanotube product from the mixed gas stream.

47. The method of claim 46, wherein the recovering step comprises passing the mixed gas stream through a gas-permeable filter.

48. A method for producing single-wall carbon nanotubes comprising:

(a) providing a transition metal catalyst precursor stream comprising a carrier gas and a transition metal catalyst precursor, wherein the transition metal catalyst precursor stream is at a temperature below the transition metal catalyst precursor'"'"'s decomposition temperature;

(b) providing a refractory precursor stream comprising a carrier gas and a refractory precursor;

(c) providing a carbon-containing feedstock gas stream at a temperature above which formation of single-wall carbon nanotube formation can be initiated;

(d) mixing the carbon-containing feedstock gas stream with the transition metal catalyst precursor stream and the refractory precursor stream to form a mixed gas stream; and

(e) growing single-wall carbon nanotubes in the mixed stream.

49. The method of claim 48, wherein metal from the transition metal catalyst precursor and the refractory precursor are present in the mixed stream in a metal/refractory precursor molar ratio (moles of the metal to moles of the refractory precursor) between about 20:

1 to about 1;

10.

50. The method of claim 48 further comprising

(a) providing a refractory reactant stream comprising a refractory reactant compound capable of reacting with the refractory precursor to form a refractory material;

and

(b) mixing the refractory reactant stream in the mixed gas stream.

51. The method of claim 50, wherein metal from the transition metal catalyst precursor and the refractory precursor are present in the mixed stream in a metal/refractory precursor molar ratio (moles of the metal to moles of the refractory precursor) between about 20:

1 and about 1;

10.

52. The method of claim 51, wherein the refractory precursor and the refractory reactant compound are present in the mixed stream in a refractory precursor/refractory reactant compound ratio (moles of the refractory precursor to moles of the refractory reactant compound) between about 10:

1 and about 1;

3.