US2011121241A1PendingUtilityA1

Process for Producing Carbon Nanotubes from Renewable Raw Materials

Assignee: BORDERE SERGEPriority: Apr 6, 2007Filed: Jan 31, 2011Published: May 26, 2011
Est. expiryApr 6, 2027(~0.7 yrs left)· nominal 20-yr term from priority
C01B 32/162B82Y 40/00B82B 3/0009B82Y 30/00
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Claims

Abstract

A subject of the present invention is a process for producing carbon nanotubes, the process comprising: a) the synthesis of alcohol(s) by fermentation of at least one vegetable matter and optionally the purification of the product obtained; b) the dehydration of the alcohol or alcohols obtained in a) in order to produce, in a first reactor, a mixture of alkene(s) and water and optionally the purification of the product obtained; c) the introduction, in particular the introduction into a fluidized bed, in a second reactor, of a powdery catalyst at a temperature ranging from 450 to 850° C., this catalyst comprising at least one catalytic metal supported by an inert solid substrate, the grains of catalyst having a d50 of less than 300 μm; d) bringing the alkene produced in b) into contact with the powdery catalyst of stage c), optionally in a fluidized bed, in order to form carbon nanotubes and hydrogen on the surface of said catalyst by catalytic decomposition of said alkene; e) the recovery of the carbon nanotubes produced in d). The invention also relates to nanotubes capable of being obtained according to the abovementioned process, which can be advantageously used in all the known fields of application of carbon nanotubes.

Claims

exact text as granted — not AI-modified
1 . Carbon nanotubes according to  claim 24 , which are capable of being obtained by a process comprising
 a) synthesizing alcohol(s) by fermentation of at least one vegetable matter and optionally purifying the product obtained;   b) dehydrating the alcohol or alcohols obtained in a) to produce, in a first reactor, a mixture of alkene(s) and water and optionally purifying the product obtained;   c) introducing, in a second reactor, a powdery catalyst at a temperature ranging from 450 to 850° C., the catalyst comprising at least one catalytic metal supported by an inert solid substrate, the grains of catalyst having a d50 of less than 300 μm;   d) bringing the alkene produced in b) into contact with the powdery catalyst of c), optionally in a fluidized bed, to form carbon nanotubes and hydrogen on the surface of said catalyst by catalytic decomposition of said alkene;   e) recovering the carbon nanotubes produced in d).   
     
     
         2 . Carbon nanotubes according to  claim 1 , wherein c), d) and e) are implemented continuously and simultaneously in the second reactor. 
     
     
         3 . Carbon nanotubes according to  claim 1 , wherein the vegetable matter is selected from beet; sugar cane; cereals such as corn, wheat, barley and sorghum; potatoes; biomass; and a of cellulose. 
     
     
         4 . (canceled) 
     
     
         5 . Carbon nanotubes according to  claim 1 , wherein the alcohol is ethanol. 
     
     
         6 . Carbon nanotubes according to  claim 1 , wherein b) is carried out by means of a catalyst based on γ-alumina. 
     
     
         7 . Carbon nanotubes according to  claim 1 , wherein c) is carried out at a temperature of 500° C. to 700° C. 
     
     
         8 . Carbon nanotubes according to  claim 1 , wherein the alkene is mixed in d) with a flow of hydrogen and/or at least part of the water produced during the dehydrating of the alcohol in b). 
     
     
         9 . Carbon nanotubes according to  claim 1 , wherein the hydrogen produced in d) is recycled at least in part into the second reactor. 
     
     
         10 . Carbon nanotubes according to  claim 1 , wherein the catalytic metal is iron. 
     
     
         11 . Carbon nanotubes according to  claim 1 , wherein the powdery catalyst is produced by impregnating the solid substrate with an aqueous solution of said catalytic metal then calcination of the solid substrate thus impregnated. 
     
     
         12 . Carbon nanotubes according to  claim 11 , wherein the calcination is carried out at a temperature of 200° C. to 400° C. 
     
     
         13 . Carbon nanotubes according to  claim 1 , wherein the d50 of the grains of powdery catalyst is less than 200 μm and preferably greater than 100 μm. 
     
     
         14 .- 16 . (canceled) 
     
     
         17 . A method for manufacturing composite materials having improved electrical and/or thermal conduction properties and/or improved mechanical properties, in particular elongation resistance, comprising the step of introducing the carbon nanotubes according to  claim 24  in a macromolecular composition. 
     
     
         18 . Macromolecular compositions intended for the packaging of electronic components or the production of fuel lines or antistatic coatings, or in thermistors or electrodes for supercapacitors, comprising carbon nanotubes according to  claim 24 . 
     
     
         19 .- 23 . (canceled) 
     
     
         24 . Carbon nanotubes which contain at least 20% by mass, of carbon of renewable origin relative to the total mass of carbon. 
     
     
         25 . Carbon nanotubes according to  claim 24 , which contain at least 0.2×10 −10 % by mass of  14 C. 
     
     
         26 . Carbon nanotubes according to  claim 24 , which contain at least 0.6×10 −10 % by mass of  14 C 
     
     
         27 . Carbon nanotubes according to  claim 24 , wherein the source of cellulose is corn. 
     
     
         28 . Carbon nanotubes which contain at least 50% by mass, of carbon of renewable origin relative to the total mass of carbon.

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