US2005063891A1PendingUtilityA1
Method of producing carbon nanoparticles
Est. expirySep 2, 2023(expired)· nominal 20-yr term from priority
C01B 32/162C01B 2202/06D01F 9/133D01F 9/127B82Y 40/00B82Y 30/00C01B 2202/02
41
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Claims
Abstract
A method of producing carbon nanoparticles comprises the steps of: passing a gaseous carbon source through a heated reactor; and adding catalyst supported on substrate particles or thermally decomposable catalyst precursor supported on substrate particles to the heated reactor to form a fluidised bed; such that carbon nanoparticles are formed in the heated reactor.
Claims
exact text as granted — not AI-modified1 . A method of producing carbon nanoparticles, comprising the steps of:
passing a gaseous carbon source through a heated reactor; and adding catalyst supported on substrate particles or thermally decomposable catalyst precursor supported on substrate particles to the heated reactor; maintaining a fluidised bed of the substrate particles in the heated reactor; and forming carbon nanoparticles in the heated reactor.
2 . A method as claimed in claim 1 , wherein the catalyst or catalyst precursor supported on substrate particles is introduced into the heated reactor via a gravity-fed hopper.
3 . A method as claimed in claim 1 , wherein the catalyst or catalyst precursor supported on substrate particles is introduced into the heated reactor via an injection gas flow.
4 . A method as claimed in claim 3 , wherein the injection gas flow reverses the direction of gas flow through the heated reactor during injection.
5 . A method as claimed in claim 3 , wherein the injection gas is an inert gas.
6 . A method as claimed in claim 3 , wherein the injection gas is a gaseous carbon source.
7 . A method as claimed in claim 1 , wherein the reactor heated reactor is at a temperature between 500 and 1200° C.
8 . A method as claimed in claim 7 , wherein the heated reactor is at a temperature between 700 and 900° C.
9 . A method as claimed in claim 1 , wherein a catalyst precursor is present and is a metal salt, an organometallic species or a metal carbonyl.
10 . A method as claimed in claim 9 , wherein the catalyst precursor comprises one or more of nickel, iron, molybdenum, platinum and cobalt.
11 . A method as claimed in claim 9 , wherein the catalyst precursor is a metal salt and comprises a counterion consisting of nitrate, stearate, formate, oxalate, acetate or chloride.
12 . A method as claimed in claim 11 , wherein the counter ion is organic.
13 . A method as claimed in claim 12 , wherein the organic counter ion is C 2 to C 30 carboxylate.
14 . A method as claimed in claim 1 , wherein the carbon nanoparticles contain a non-carbon dopant.
15 . A method as claimed in claim 14 , wherein the non-carbon dopant is nitrogen.
16 . A method as claimed in claim 1 , wherein the gaseous carbon source is one or more of acetylene, alcohol, alkane, alkene, CO, benzene, toluene, xylene, cumene, ethylbenzene, naphthalene, phenanthrene, anthracene, formaldehyde, acetaldehyde, acetone.
17 . A method as claimed in claim 1 , wherein the gaseous carbon source is mixed with a diluent gas.
18 . A method as claimed in claim 17 , wherein the diluent gas is one or more of hydrogen, ammonia, nitrogen, helium and argon.
19 . A method as claimed in claim 17 , wherein the ratio of gaseous carbon source to diluent gas is reduced while the catalyst or catalyst precursor supported on substrate particles is introduced into the heated reactor.
20 . A method as claimed in claim 1 , in which the substrate particles comprise one or more of silica, alumina, MCM and magnesium oxide.
21 . A method as claimed in claim 1 , in which the substrate particles comprise a halide, nitrate, sulphate, carbonate, aluminate, aluminium chloride, arsenate, arsenite, borate, chromate, fluoroaluminate, silicate, sulphide, telluride, tungstate, vanadate or phosphate of a Group 1 or Group 2 metal.
22 . A method as claimed in claim 21 , wherein the Group 1 or Group 2 metal is lithium, sodium, potassium, calcium or magnesium.
23 . A method as claimed in claim 1 , wherein the average dimension of the substrate particles is between 20 microns and 1 mm.
24 . A method as claimed in claim 1 , wherein the average dimension of the substrate particles is between 40 microns and 200 microns.
25 . A method as claimed in claim 1 , further comprising the step of removing nanoparticles from the heated reactor.
26 . A method as claimed in claim 25 , wherein nanoparticles are removed from the heated reactor by under vacuum or under pressure.
27 . A method as claimed in claim 1 , wherein the process is operated continuously with simultaneous introduction of catalyst or catalyst precursor supported on substrate particles and removal of nanoparticles.
28 . A method as claimed in claim 1 , wherein the method is operated non-continuously with alternating introduction of catalyst or catalyst precursor supported on substrate particles and removal of nanoparticles.
29 . A method as claimed in claim 1 , wherein the carbon nanoparticles are nanotubes and/or nanofibres.
30 . A method as claimed in claim 29 , wherein the nanotubes are single-walled nanotubes or multi-walled nanotubes.
31 . A method of producing carbon nanoparticles, comprising the steps of:
passing a non-carbon-containing gas through a heated reactor; and adding catalyst or catalyst precursor supported on substrate particles to the heated reactor; maintaining a fluidised bed of said substrate particles in the heated reactor; passing a gaseous carbon source through the heated reactor; and forming carbon nanoparticles in the heated reactor.
32 . Carbon nanoparticles produced by a method as claimed in claim 1 or claim 31.Join the waitlist — get patent alerts
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