Method for producing cables made of aligned carbon nanotubes

Abstract

A method for preparing a cable formed of carbon nanotubes, comprising decomposing at least one carbon precursor compound and at least one precursor compound of a catalyst on a porous substrate (43), in which method continuously: —a first gas stream comprising a precursor of a catalyst is brought into contact with a porous substrate (43); —a second gas stream comprising at least one carbon precursor is brought into contact with said porous substrate (43); —said porous substrate (43) is heated to a temperature leading to the deposition of catalyst particles and the catalytic growth of a carbon nanotube bundle, and preferably between 500° C. and 1000° C.

Claims

1. A method for preparing a cable formed of carbon nanotubes, comprising: decomposing at least one carbon precursor compound and at least one precursor compound of a catalyst on a porous substrate, wherein, continuously: a first gas stream comprising a precursor of a catalyst is brought into contact with a porous substrate; a second gas stream including at least one carbon precursor is brought into contact with the porous substrate; and the porous substrate is heated to a temperature leading to the deposition of catalyst particles and the catalytic growth of a carbon nanotube bundle, wherein the temperature is from 500° C. to 1000° C.

2. The method according to claim 1, wherein the porous substrate is passed through at least partially by the first gas stream.

3. The method according to claim 2, wherein the porous substrate is heated in a zone close to the zone through which the first gas stream leaves the substrate, or the zone on which the first gas stream is directed.

4. The method according to claim 1, wherein the first gas stream is directed on a surface zone of the porous substrate.

5. The method according to claim 1, wherein the carbon precursor is a hydrocarbon and/or carbon monoxide.

6. The method according to claim 1, wherein the localized heating is carried out by electromagnetic induction.

7. The method according to claim 6, wherein the localized heating is carried out, at least partially, by inductive heating of the catalyst particles.

8. The method according to claim 1, wherein the porous substrate is selected from the group including: a porous silicon, a porous alumina, a porous silicon carbide, a metallic foam comprising interconnected pores, a carbon foam comprising interconnected pores, vertically aligned carbon nanotubes, or a mixed substrate including a combination of any of the preceding substrates.

9. The method according to claim 1, further comprising a step wherein the bundle of nanotubes is coated over a desired length with a metal, such as copper.

10. The method according to claim 9, wherein the bundle of nanotubes is coated at an end thereof with a metal.

11. The method according to claim 9, wherein the metallic coating is brought into contact with an electrical connection element.

12. The method according to claim 1, further comprising a step of coating the bundle of nanotubes with an electrically insulating material.

13. A reactor for implementing the method according to claim 1 comprising: following the direction of the flow of the gas stream: means for supplying a first reactive gas stream comprising a precursor of a catalyst and a second stream of reactant gas comprising at least one carbon precursor, a zone for injecting a stream of reactant gas provided with a first means of heating capable of heating the gases to a second temperature, wherein the second temperature is from 250° C. to 450° C., a porous substrate travelled through by the stream of reactant gas, a zone provided with a second means of heating, wherein the second means of heating is configured to heat at least one portion of the porous substrate to a third temperature, wherein the third temperature is from 450° C. to 700° C., a tubular deployment zone configured to deploy the nanofibers or nanotubes, wherein the tubular deployment zone comprises a third means of heating, wherein the third means of heating is configured to heat the nanotubes or nanofibers to a fourth temperature,  wherein the fourth temperature is from 800° C. to 2,000° C.; means for collecting the nanofibers or nanotubes; and an outlet through which the gases can exit the reactor.

14. A reactor according to claim 13, further comprising means for confining the catalytic decomposition zone of the carbon precursor.

15. A reactor according to claim 13, wherein the second means of heating are means of localized heating.

16. A reactor according to claim 15, wherein the means of localized heating act as means for confining the catalytic decomposition zone of the carbon precursor.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

(1) FIGS. 1 to 6 show various aspects of the invention.

(2) FIGS. 1 and 2 diagrammatically show the principle of the method according to the invention.

(3) FIG. 3 diagrammatically shows two means of confinement of the heating in the vicinity of the outlet surface of the porous substrate.

(4) FIG. 4 diagrammatically shows three alternatives of the device according to the invention.

(5) FIG. 5 diagrammatically shows two alternatives of the method according to the invention.

(6) FIG. 6 diagrammatically shows three embodiments of the invention with a coaxial injection nozzle.

DESCRIPTION

(7) The present invention has several essential characteristics, and other characteristics that are only optional.

(8) According to the invention a method of chemical vapor deposition is used from one or several hydrocarbon compounds acting as carbon precursors (also called here “source of carbon”), said chemical vapor deposition being catalyzed by catalytic particles. Said catalytic particles are deposited on the porous substrate, or formed on said porous substrate. They come from a precursor compound of a catalyst that is supplied by a first gas stream; this represents a first essential characteristic of the invention. In an advantageous embodiment said precursor compound of a catalyst is introduced into said first gas stream in the form of finely divided liquid or solid particles; in other words said first gas stream comprises at least in one portion of its travel an aerosol (also called here “catalyst aerosol”). The introduction of the catalyst precursor compound in the form of an aerosol comprising solid and/or liquid particles of said catalyst precursor compound represents a very highly preferred embodiment of the method according to the invention. In other embodiments said precursor compound of a catalyst is introduced into the first gas stream in gaseous form.

(9) According to another essential characteristic of the invention the reactive gases are brought into contact with a porous substrate. The term “reactive gas” designates here the first gas stream, i.e. on the one hand, the catalyst aerosol and the gas phase that results from the evaporation and/or decomposition, partial or total, of said particles during the conveyance thereof to said porous substrate, and, on the other hand, the source of carbon compound or compounds, possibly in the carrier gas thereof, knowing that the source of carbon compound or compounds can be part of said first gas stream, and/or can be part of a second gas stream. The bringing into contact of the reactive gases with the porous substrate can be carried out in a common stream or in separate streams, for example a first stream coming from the catalyst aerosol and a second stream that comprises the carbon source compound. It is understood that the catalyst precursor can also be a source of carbon, i.e. the organic portion of the organo-metallic molecule can be used, after decomposition of the molecule, as a source of carbon, and/or the solvent of said organo-metallic molecule, if a solvent is used, can be used as a source of carbon.

(10) In an embodiment shown diagrammatically in FIG. 1, the porous substrate is a membrane, and it is passed through by a stream of reactant gas. This results in the spatial confinement of the reactive gas stream. This membrane can in particular be microporous, meso-porous and/or nanoporous.

(11) According to another essential characteristic of the invention energy is supplied to the reactive gases so as to allow for the growth of carbon nanotubes or nanofibers. This supplying of energy can be carried out in a confined zone. In an embodiment shown diagrammatically in FIG. 1 this confinement is carried out in a zone close to the surface of the nanoporous membrane. Thus, the chemical reactions that lead to the growth of nanotubes or nanofibers take place in a confined zone.

(12) According to another essential characteristic of the invention the stream of reactive gases is supplied continuously, allowing for the uninterrupted growth of nanotubes or nanowires. In the embodiment shown diagrammatically in FIG. 1 this growth leads to a mat of VANCT of great length, forming a bundle.

(13) FIG. 2 diagrammatically shows the role of the confinement of the energy supply. FIG. 2(a) shows a porous substrate passed through by a first gas stream 21 and by a second gas stream 22; these two gas streams are mixed within a confined zone of the substrate, in a heated enclosure. The mode of heating of the substrate does not generate any confinement of the heating within the substrate. FIG. 2(b) shows a porous substrate passed through by a single gas stream with a localized thermal energy supply downstream from the porous substrate which heats the substrate only in a zone of low thickness near the outlet thereof. FIG. 2(c) shows the same configuration, but with an energy supply confined in a zone of low thickness close to the outlet of the porous substrate.

(14) FIG. 3 diagrammatically shows two embodiments for carrying out a localized heating of the substrate by induction: with a metallic foam fixed at the outlet of the porous substrate (FIG. 4(a)) and with a metallic ring at the outlet of the porous substrate (FIG. 3(b)).

(15) FIG. 4 diagrammatically shows four partial cross-section view of reactors that are suitable for implementing the invention.

1. The Reagents

(16) The first gas stream initially comprises the catalyst aerosol, which comprises particles comprising a catalyst precursor metal compound, said particles being conveyed by a carrier gas. This carrier gas can comprise a carbon precursor hydrocarbon compound, or it can be inert in the reaction conditions chosen (it can be for example a hydrocarbon compound that does not catalytically decompose in the reaction conditions chosen, or it can be nitrogen or hydrogen). Said particles comprising a catalyst precursor metal compound can be produced from a liquid (at the temperature T1 at which said liquid is at the moment when it is conveyed into the device for forming aerosol) which is formed by said catalyst precursor metal compound, if this compound is a liquid, or by a solution of said catalyst precursor metal compound in a liquid solvent. Said liquid solvent can be a carbon precursor hydrocarbon compound, or it can be a compound that is not decomposed in the reaction conditions of catalytic decomposition on the porous substrate. Advantageously the catalyst aerosol initially comprises liquid particles. The catalyst aerosol can be formed by periodic injection of a liquid phase (being at the temperature T1) in a carrier gas. An injection pump of the current type such as is used in combustion engines can be used.

(17) During the conveyance thereof to the porous substrate these liquid particles (with the temperature in this zone of the reactor being named here T2) can evaporate partially or entirely; in particular, the solvent thereof can evaporate partially or entirely, and the particle forming the catalyst aerosol can become a solid particle formed from the precursor metal compound of a catalyst, or can evaporate. During the conveyance thereof to the porous substrate these liquid or solid particles or these gas molecules (with the temperature in this zone of the reactor being named here as T3) can be decomposed partially or entirely, in particular by pyrolysis, thus releasing the metallic catalyst that they contain. The details of the decomposition of the particles that form the catalyst aerosol or catalytic precursor gas molecules, and of the formation of catalyst particles on the porous substrate or in the porous substrate are not known by the inventors, and they do not wish to be bound by the theoretical representations that they make of this portion of the method according to the invention.

(18) Said carbon precursor hydrocarbon compound can be supplied by said first gas stream (where it can act as a carrier gas of the aerosol), and/or it can be supplied by other gas streams (for example by said second gas stream, and/or a third gas stream). Said carbon precursor hydrocarbon compound can also be introduced, in the form of an aerosol comprising finely divided liquid particles comprising a carbon precursor hydrocarbon compound (referred to here in what follows as “hydrocarbon aerosol”); in this latter case the hydrocarbon aerosol can be supplied in the same stream as the catalyst aerosol, or by another stream.

(19) In any case the carbon precursor compound can comprise a single compound or several compounds. This is preferably hydrocarbons, but it can also contain for example carbon monoxide (CO).

(20) In an embodiment, the precursor compound of a catalyst metal is ferrocene. Ferrocene having a melting point of about 172° C. and an evaporation point of about 250° C., it is suitable to dissolve it, preferably in toluene. The catalyst aerosol therefore comprises droplets of toluene in which the ferrocene is dissolved. The temperature T1 can be for example comprised between 0° C. and 50° C., and advantageously comprised between 15° C. and 30° C. When the toluene evaporates (boiling point of about 110° C.) the ferrocene remains in the catalyst aerosol in the form of solid or liquid particles, or the mixture becomes a purely gaseous mixture, according to the temperature T2 of the zone of the reactor. By way of example T2 can be comprised between 120° C. and 450° C. and preferably between 250° C. and 450° C. Other solvents can be used, such as benzene or xylene.

(21) It is known that ferrocene has a boiling (or evaporation) point of about 250° C.; the inventors do not think that the exact structure of the particles of the catalyst precursor in the catalyst aerosol is important for the present invention; according to the conducting of the method and in particular according to the temperatures T1 and T2 it is therefore possible that the catalyst aerosol changes structure between the moment when the catalyst precursor particles are injected into the carrier gas of the first gas stream and the moment when this gas stream arrives on the surface of the porous solid in the zone at the temperature T3. It is known that ferrocene decomposes around 450° C. into iron and cyclopentane, and in an advantageous embodiment the temperature T3 is at least equal to 450° C. By way of example T3 can be comprised between 450° C. and 700° C. This decomposition of the ferrocene can be carried out in the first gas stream and/or in contact with the porous substrate. According to an essential aspect of the invention the catalyst is deposited or is formed in the porous substrate or on the porous substrate in the form of nanoparticles.

(22) A carbon precursor compound that can be catalytically decomposed by the nanoparticles of iron formed from particles of ferrocene is acetylene; the question of knowing whether or not the toluene of the catalyst aerosol is also decomposed depends substantially on the temperature. Acetylene can be the carrier gas of the catalyst aerosol.

(23) Other molecules can be used as a catalyst precursor, for example cobaltocene, nickelocene, or a mixture of ferrocene and/or cobaltocene and/or nickelocene.

2. The Porous Substrate

(24) Said catalyst precursor, preferably the catalyst aerosol, is conveyed by a carrier gas and forms the first gas stream; this stream is brought into contact with a porous substrate. This is a second essential characteristic of the method according to the invention. The substrate has to have the following characteristics: good resistance at a high temperature, a porosity that is open to reactive gases, good chemical inertia regarding reagents, good surface chemical affinity with the catalyst (in order to provide an adhesion that promotes the growth regime of carbon nanotubes or nanofibers by the base thereof, with this growth mechanism being known under the term “base growth mechanism”, discussed hereinabove), and a low solubility of the catalyst in volume in order to limit the diffusion and deactivation of the catalytic particle.

(25) The porous substrate must have in particular an open porosity that is sufficient to be able to be passed through by a gas stream. Said porous substrate can be a porous membrane.

(26) The following substrates are suitable in particular, with the condition of having interconnected pores (in opposition to closed porosities): porous silicon (which can be obtained by chemical etching of monocrystalline silicon using a suitable microlithographic mask; a membrane is thus obtained that has through-pores of a diameter of about a micrometer (typically between 0.7 μm and 3 μm, called “macroporous silicon”); if the chemical nature of the silicon is not suitable a thin layer of another material can be deposited, for example by electroplating); porous alumina (which can be obtained by anodization of a sheet of aluminum then detaching of the layer of oxide from the substrate thereof; the anodic layer has columnar pores, parallel between them and perpendicular with respect to the substrate, of a diameter that is typically between 10 nm and 100 nm); porous silicon carbide, in particular β silicon carbide and preferably in the form of foam; metallic foams (for example aluminum foams); carbon foams; the VACNT (either self-borne or deposited onto a porous substrate; or hollow of which the central channel is filled with metal or metallic carbide); mixed substrates (for example a nickel foam supported by a membrane of alumina).

(27) As shall be explained in more detail hereinbelow, the non-metallic substrates that do not conduct electricity can be coated at least partially (and preferably in the zone close to the outlet surface thereof) with a metallic film in order to reinforce the effect of the localized heating by induction.

(28) The bringing into contact of the catalyst or catalyst precursor with the porous substrate can be carried out in several ways.

(29) In a first embodiment the first gas stream (comprising the catalyst precursor compound with the carrier gas thereof) is injected into said porous substrate that it passes through at least partially. In a second embodiment it is injected in the vicinity of said porous substrate, in particular in the vicinity of the outer surface thereof, through the exterior.

(30) It is preferred that said first gas stream be injected into the porous substrate. Alternatively it can be injected into the reactor in the vicinity of the substrate, in particular over the outer surface thereof.

(31) The method according to the invention has the particularity of simultaneously supplying all throughout the growth of the nanotubes the reaction medium with catalytic nanoparticles and with carbon precursor. In the methods according to prior art, the supplying of the catalyst and the supplying with carbon precursor are usually separated into two separate steps: in a first step catalytic particles are deposited onto the substrate or in the substrate, then in a second step the carbon nanotubes are made to grow by the supply of carbon precursor.

(32) The inventors have discovered that the method according to the invention actually makes it possible to overcome the limitation of the length of the CNT by disappearance of the catalyst or loss of the catalytic activity thereof: this method makes it possible to constantly replace the catalyst that has become in active or that has disappeared by disaggregation (i.e. progressively driven in the body of the nanotubes during the growth thereof). Indeed, the method according to the invention leads to carbon nanotubes that contain, spaced apart but present over the entire length of the tubes, nanoparticles of metallic catalyst (for example: iron) imprisoned in the central channel of the nanotube during the growth thereof: this is the signature of this method, stemming from the constant supply of catalyst in the form of an aerosol, that it shares with the method described in EP 1 515 911 B1 (see FIG. III-5 (a) of the thesis, mentioned hereinabove, of Sebastien Lagoutte, pages 117/118) which proves the constant supply of catalyst and the progressive disappearance thereof by incorporation into the nanotubes.

(33) Without wanting to be bound by this theory, the inventors believe that the method according to the invention resolves a reaction mechanism problem that limits the potential of the methods according to prior art: when the length of the VACNT becomes greater than a certain limit (typically a few hundred micrometers or a few millimeters) the low diffusion of the precursors and of the by-products (of which the streams are opposed) blocks the access of the precursors to the catalytic sites and the access of the by-products to the surface of the mat of VACNT. In the method according to the invention the catalyst is renewed regularly, and the access of the reactive gases is spatially separated from the clearance of the by-products.

(34) According to a particular embodiment, a mat of VACNT is used as a porous substrate; in an alternative a mat of VACNT is used of which the central channel comprises metallic particles (for example Fe or Ni or Co) or metallic carbide (for example Fe, Ni or Co carbide) coming from the catalyst produced with a continuous supply of catalyst by the periodic injection of a catalyst aerosol, knowing that the metallic particles or carbide that are inclusions in the central channel of the nanotubes make it possible to heat this substrate locally by induction.

3. The Localized Heating

(35) A third essential characteristic is that the chemical vapor deposition is carried out in a localized zone of the porous substrate, which is preferably located at the downstream periphery thereof (with respect to the direction of the stream of carrier gas). The location of this zone can be defined by the effect of a localized heating at a temperature referred to as T3. It is in the heated zone that the catalyst precursor is decomposed in order to form nanoparticles of catalyst, and it is in this zone where the catalytic decomposition of the carbon precursor will take place. According to the value of the temperature T3 the decomposition of the catalyst precursor can begin upstream from this zone.

(36) If the first gas stream does not comprise a carbon precursor compound, or if it is desired to supply another carbon precursor compound (or an additional quantity of said compound), a second gas stream comprising the carbon precursor compound must be injected as close as possible to this localized zone, and preferably in this localized zone. The injection of said second gas stream against the current of said first gas stream is to be avoided because it does not allow the secondary reaction products to be removed easily.

(37) The confinement of the zone catalytic decomposition of the carbon precursor compound is an essential aspect of the method according to the invention. This confinement can be carried out by two means, which can be combined: by the localized heating of porous substrate to a temperature at least equal to T3, and by the localized injection of the stream of carbon precursor compound on or in the substrate (or a zone of said substrate) that is at a temperature at least equal to T3. In the two embodiments the confinement defines the heterogeneous catalyst zone from which the continuous growth of the carbon nanotubes or nanofibers is carried out, through the base thereof.

(38) In a first embodiment it is the location of the energy supply that defines the heterogeneous catalyst zone. Several means of localized heating can be used. It is possible for example to selectively heat certain parts of the reaction zone and/or the porous substrate can participate in the heating (by itself becoming a heated part). This can for example be carried out by inductive heating, using a coil that surrounds at least partially the substrate and by judiciously choosing the materials that form the environment of the reaction zone. This is the preferred embodiment.

(39) In induction heating, the zone to be heated is bathed in the oscillating magnetic field generated by a coil that surrounds said zone. In an embodiment a metallic part is positioned in the vicinity of the reaction (for example close to the outlet surface of the porous substrate), all of the other parts located in the zone of influence of the magnetic field applied being either non-metallic or made of an electrically-conductive material that has a lower resistivity than said metallic part. By way of example, the porous substrate can be made from a non-metallic material (for example of porous alumina), and a metallic foam that has open macropores can be affixed on the outlet surface of the non-metallic porous substrate (or positioned very close to this outlet surface). This is diagrammatically shown in FIG. 3(a), where the mark 31 designates said non-metallic porous substrate and the mark 32 said metallic foam. As shown in FIG. 3(b) it is also possible to use a metal ring 33 instead of the metallic foam, or in addition to the metallic foam (alternative not shown in the figures).

(40) The localized energy supply can also be carried out by any suitable means, and in particular by resistive heating (Joule effect) of a resistance or of the porous substrate itself, even if these solutions are not the preferred solutions (the confinement of the heating is more difficult to control, and the connections become difficult to manage). The energy supply can also be carried out by laser irradiation, but this also is not the preferred solution (because the absorption coefficient of the surfaces can change during the synthesis due to surface deposition, and because space constraints for the optical path of the laser beam have to be taken into consideration).

(41) The porous substrate can also be formed of carbon nanotubes, preferably aligned. When the porous substrate is formed of VACNT, the localized energy supply can also be carried out by inductive heating of the VACNT of which the central channel can possibly and advantageously comprise metallic particles or carbides of a metal, as was explained hereinabove.

(42) The localized energy supply can also be carried out by inductive heating directly of the active catalytic particles for the synthesis of the carbon nanotubes. This solution is the one that allows for the most localized heating. It can be used alone, or preferably as a supplement to another means of heating, in particular in the case where it alone does not make it possible to form all of the energy supply required for the growth of the CNT.

(43) To these means of localized heating can be added a preheating of said first and/or second gas streams.

(44) The porous substrate (non metallic and insulating) can also be provided with a metallic coating so that only the surface thereof is heated by induction (for example an aluminum coating on a porous alumina).

(45) The confinement of the energy supply can also be supplemented by the insertion of thermal barriers, for example comprised of layers with low heat conductivity close to the reactive zone (outlet surface of the porous substrate).

4. The Reactor

(46) The heated substrate is in an enclosure, here called a “reactor”, and the method advantageously takes place at a pressure close to the atmospheric pressure. This enclosure can be closed or partially closed but rendered sealed to the gas exchanges between the inside and the outside of the reactor. It comprises means for collecting the nanotubes formed. The enclosure can comprise means for heating the walls thereof, so as to prevent excessively high thermal gradients within the reactor. The reactor also comprises means for pumping, knowing that the gases entering into the reactor as well as the gases resulting from the method must be removed continuously. The reactor also comprises means for purging; purging can be carried out by rinsing using a neutral gas, whether or not associated with a steaming of the reactor prior to the starting of the method.

(47) FIG. 4 diagrammatically shows three partial cross-section views of reactors that are suitable for the implementing of the method according to the invention. FIG. 4(a) shows the supply duct 41 with gas mixture 40 (with this gas mixture comprising the catalyst precursor and the carbon precursor) with the means of heating 42 that make it possible to reach a temperature T2 (defined hereinabove, for example a heating resistance that surrounds the supply duct), as well as the porous substrate 43 passed through by this gas stream. The means of localized heating 45 (for example a metal ring heated by an induction coil) that make it possible to reach a temperature T3 that is sufficient to allow for the catalytic growth of carbon nanotubes or nanofibers are located very close to the outlet surface 44 of the porous substrate 43. Downstream from the porous substrate 43 is located, optionally, a heating zone provided with means of heating 55 that make it possible to heat the nanotubes or nanofibers to a temperature T4 that makes it possible to improve the crystallinity thereof. The condition T2<T3 must be satisfied.

(48) FIG. 4(b) shows the growth of the carbon nanotubes or nanofibers 46 that is deployed in a tubular deployment zone 49 located downstream from the porous substrate 43. If the reactor comprises the means for heating 55 that make it possible to heat the nanotubes or nanofibers to a temperature T4, these means are advantageously located around this tubular deployment zone 49.

(49) FIG. 4(c) shows a means 47 that make it possible to wind the nanotubes or nanofibers. Any reaction gases that have not reacted, the carrier gases and the gaseous reaction products can exit the reactor through a discharge orifice 48. The pressure is advantageously close to the ambient pressure.

(50) FIG. 4(d) shows an alternative of the reactor according to FIG. 4(c) wherein the reactor has means for continuously exiting the nanotubes produced. Note that the means 47 for winding the nanotubes or nanofibers can be an endless screw able to displace the nanotubes or nanofibers laterally in the direction of the arrow. The reactor is not entirely closed: a slot 52 is provided in order to allow for the exiting of the means 47 for winding the nanotubes or nanofibers. A nitrogen knife 50 with its means of aspiration 51 is provided to isolate the inside of the reactor from the ambient atmosphere.

5. Alternatives Relating to the Injection of Reagents

(51) In order to be able to precisely confine the reaction zone, it is desirable that the mixing of the gaseous chemical species and/or particles of the aerosol can be carried out locally, as close as possible to the targeted heterogeneous catalyst zone (reaction zone), i.e. as close as possible to the outlet surface of the porous substrate. Indeed, if the decomposition of the molecules of the reaction mixture takes place inside the porous substrate and if the temperature is not sufficiently confined (typically a temperature greater than 450° C.), the growth of the CNT will take place far from the surface of the porous substrate, which will inevitably result in a clogging of the pores and the stopping of the growth of the CNT.

(52) The inventors found that it is possible to use coaxial injection heads, such as they are used in the field of the synthesis of fibers by electro-spinning: these coaxial injection heads make it possible in particular to confine the reactive gases without mixing them on a scale of a few millimeters; the outlet of the injection head can correspond to the inlet surface of the porous substrate.

(53) In the case of the separate injection (for example coaxial) of the two gas streams, there are two extreme cases: (i) in a substrate with random porosity, the reactive gases will mix together progressively during the passing through of the porous substrate; if the temperature is not sufficiently confined near the outlet surface of the porous substrate, there is a risk of clogging of (some) pores; (ii) in a substrate with compartmentalized porosity (sealed channels), the reactive gases are mixed only at the outlet of the porous substrate, the pores do not clog but the reaction cannot take place on the surface of the substrate if the mixture is carried out only after having completely passed through the porous substrate.

(54) Other intermediate cases can be considered, in particular the one of a forced stream on the surface of the porous substrate: a channel is dedicated to the pumping (extraction) of the reaction mixture, and the one where the reaction gases are mixed very close to the outlet surface but “below” the latter (multiple injector with intertwined channels, possibly associated with a porous substrate). Two of these embodiments are shown in FIG. 6. FIG. 6(a) shows an embodiment with a coaxial injection (shown as a longitudinal cross-section): a first gas stream 21 is injected into the porous substrate 64 reactor through a first peripheral tube 61, at the center of which there is a second tube 62 which injects the second gas stream 22. The two gas streams are mixed together in the porous substrate 64, and the growth of the carbon nanotubes 66 takes place on the surface of the substrate. FIG. 6(a) does not show the means for the confined heating that provides the temperature T4 required for the growth of carbon nanotubes.

(55) FIG. 6(b) shows a more complex mode of injection derived from the one of FIG. 6(a) with a coaxial outer 61 and inner 62 tube and a coaxial peripheral tube 63 dedicated to the aspiration of the reaction mixture; the gas streams mix together when they are deviated in the aspiration tube 63. If no porous substrate is provided, the growth of the carbon nanotubes takes place on the edges (the section) of the tube 62 injecting the second gas stream 22; the coaxial tubes play in the case the role of a porous substrate with compartmentalized porosity. If a porous substrate is provided, the growth of the carbon nanotubes takes place on or in the vicinity of the outlet surface of the latter; in this embodiment the porous substrate is advantageously very thin (porous membrane).

6. General Characteristics of the Method, Advantages

(56) FIG. 5 diagrammatically shows two embodiments of the method according to the invention.

(57) FIG. 5(a) shows an embodiment with localized heating to the temperature of catalytic decomposition of the carbon precursor, by one of the methods presented hereinabove in section 3. The precursor of the catalyst is dissolved in a liquid solvent. This can be for example ferrocene dissolved in toluene. An aerosol is formed that comprises particles (droplets) of this solution and a has phase as a carrier, said gas phase comprising the carbon precursor gas, which is a hydrocarbon, and said gas phase able to comprise other gases. This aerosol is heated to a first temperature T1, that is sufficient to allow for the evaporation of the solvent and of the catalyst precursor. This gas phase is heated to a second temperature T2, that is sufficient to allow for the decomposition of the precursor of the catalyst. This decomposition probably forms atoms of a suitable metal element, then metallic aggregates. By way of example, if the precursor of the catalyst is ferrocene atoms of iron are formed. These atoms aggregate and form metal nanoparticles on the surface of the porous substrate. (Note that in the framework of the present invention it is not important to know if the aggregation takes place in the gas phase or on the surface of the substrate). By the localized heating of a zone close to the outlet surface of the substrate to a third temperature T3 that is sufficient to allow for the catalytic growth of carbon nanotubes or nanofibers, the carbon precursor is allowed the catalytic decomposition on the surface of the catalytic nanoparticles. This decomposition leads to the formation of carbon nanotubes through the base-growth mechanism, provided that there is a continuous supply of carbon freshly generated the decomposition of the carbon precursor, with this supply being carried out through the porous substrate. Fresh catalyst nanoparticles are formed practically continuously, or at least periodically, by the continuous supply of atoms of metal that agglomerate to form new nanoparticles or that are added to the existing nanoparticles, with this supply being carried out through the porous substrate. Thus the growth of the carbon nanotubes is normally not interrupted, except for an accidental event of instability in the reaction conditions. In this embodiment the condition T1<T2<T3 must be satisfied.

(58) FIG. 5(b) shows another embodiment with the localized supply of the carbon precursor in the reaction zone heated to a temperature T3 that is sufficient to allow for the growth of carbon nanotubes or nanofibers. A first gas stream 21 is formed by the catalytic aerosol in a carrier gas (which can be a carbon source gas or, as indicated on the diagram, another gas). A second gas stream 22 is formed by a carbon precursor, possibly diluted in another gas. The precursor of the catalyst dissolved in the liquid solvent is mixed with another gas in order to form an aerosol, as in the embodiment of FIG. 5(a), which is heated to a first temperature T1 in order to evaporate the solvent and the catalyst precursor. This gas stream is heated to a second temperature T2, that is sufficient to allow for the decomposition of the precursor of the catalyst; the atoms of the metal of said precursor of the catalyst aggregate and form nanoparticles of metal on the surface of the porous substrate. As in the preceding embodiment, the substrate is heated to a third temperature T3 that is sufficient to allow for the growth of carbon nanotubes or nanofibers. The second gas stream 22 which comprises a carbon precursor gas, possibly mixed with another gas, is brought into contact with the catalyst located on the outlet surface of the porous substrate through a localized supply in the zone heated to said third temperature T3, in such a way that the catalytic decomposition of said carbon precursor in this zone leads to the formation of carbon nanotubes through the base-growth mechanism, provided that there is a continuous supply of carbon freshly generated the decomposition of the carbon precursor, with this supply being carried out locally. Fresh catalyst nanoparticles are formed practically continuously, or at least periodically, by the continuous supply of atoms of metal that agglomerate to form new nanoparticles or that are added to the existing nanoparticles, with this supply being carried out through the porous substrate. Thus the growth of the carbon nanotubes is normally not interrupted, except for an accidental event of instability in the reaction conditions. In this embodiment also the condition T1<T2<T3 must be satisfied.

(59) In the two embodiments that have just been described, i.e. with localized heating to the temperature T3 or with localized supply of the carbon precursor in the zone heated to the temperature T3, a fourth heating zone to a fourth temperature T4 can be provided downstream from the growth zone of the nanotubes, in order to improve the crystallinity (i.e. the order on the atomic and nanometric scale) of the carbon nanotubes or nanofibers formed.

(60) Without wanting to be bound by this theory, the inventors believe that the method according to the invention makes it possible to form in situ (i.e. on the porous surface of the substrate, and in the reaction zone) catalytic particles from the particles of the catalyst aerosol; indeed, these particles of a precursor compound of a catalyst are decomposed by pyrolysis in the heated localized zone of the porous substrate, and form metallic particles of nanometric size. In this same reaction zone the carbon precursor component conveyed, either in gas form or in the form of liquid particles, with the carrier gas or injected independently, is broken down under the catalytic effect of catalyst particles.

(61) The method according to the invention would therefore be characterized by the fact that the supply with reagents is localized directly in the vicinity of the catalytic particles, and in the reaction zone. For this purpose a porous substrate is used that can play the role at the same time of mechanical support, catalyst regenerator and source of carbon precursor. In this preferred configuration the stream of reactant reagents (catalyst and carbon precursor) is no longer opposed to the stream of by-products and a permanent supply-removal system can be established, independent of the length of the carbon nanotubes. This configuration is compatible with a growth of CNT that persists as long as the conditions for the supply with reagents and the removal of by-products are maintained in a stable manner, i.e. quasi-infinitely.

(62) The method according to the invention allows for the growth of nanotubes and nanofibers of great length, with this growth taking place in the form of a bundle of parallel nanotubes or nanofibers; this facilitates the handling of the nanotubes or nanofibers obtained. By way of example, during the growth thereof they can be conveyed into a tube by directing the gas stream exiting from the reaction zone to this tube. By way of example, this tube can be made of metal or of quartz, and the end thereof can be located in the vicinity of the substrate (which can be a collection surface, for example the surface of a rotating roller), which makes it possible to receive, to direct and to protect the bundle of nanotubes or nanofibers obtained.

(63) These nanotubes and nanofibers show a very low number of interfaces or crystal boundaries over the length thereof, or are even exempt from such interfaces or boundaries; these interfaces and boundaries can be highlighted by different analysis techniques known to those skilled in the art, and in any case by par transmission electron microscopy.

(64) Said nanotubes and nanofibers of great length according to the invention can be used as electrical conductors, or in the production of electrical conductors. They can also be used, possible after coating, as mechanical cables and/or as thermal energy transport elements. In these three applications, the thermal and/or electrical conductivity thereof is improved by the uninterrupted nature of said nanotubes and nanofibers, and by the excellent crystallographic quality thereof.