Catalyst composition for the synthesis of thin multi-walled carbon nanotube and its manufacturing method
The present invention relates to a catalyst composition for the synthesis of thin multi-walled carbon nanotube (MWCNT) and a method for manufacturing a catalyst composition. More particularly, this invention relates to a multi-component metal catalyst composition comprising i) main catalyst of Fe and Al, ii) inactive support of Mg and iii) optional co-catalyst at least one selected from Co, Ni, Cr, Mn, Mo, W, V, Sn, or Cu. Further, the present invention affords thin multi-walled carbon nanotube having 5˜20 nm of diameter and 100˜10,000 of aspect ratio in a high yield.
1. A catalyst composition for producing carbon nanotube represented by following formula
[Fe a :Al b ] x :M y :Mg z
wherein
Fe represents catalytic metal of iron, its oxide; Al represents catalytic metal of aluminum, its oxide;
Mg represents inactive support of magnesium, its oxide;
M represents at least one transition metal selected from Co, Ni, Cr, Mn, Mo, W, V, Sn, or Cu, its oxide;
x, y, and z represent molar fraction of [the sum of Fe and Al], M, and Mg,
x+y+z=10, 2.0≦x≦8.0, 0.0≦y≦2.5, 0.5≦z≦8.0
a and b represent molar fraction of Fe and Al,
a+b=10, 2.0≦a≦5.5, 4.5≦b≦8.0.
2. The catalyst composition for preparing carbon nanotube according to claim 1 , wherein the molar fraction of [the sum of Fe and Al], M, and Mg is x+y+z=10, 3.0≦x≦7.0, 0.0≦y≦2.0, 1.0≦z≦7.0, and the molar fraction of Fe and Al is a+b=10, 2.4≦a≦4.2, 5.8≦b≦7.6.
3. A process for preparing carbon nanotube comprising
i) preparing a catalyst composition for the synthesis of carbon nanotube of claim 1 ;
ii) supplying mixed gas of hydrogen and at least one carbon source selected from saturated or unsaturated hydrocarbon having 1˜4 carbon atoms to the reactor at 500˜900° C.; and
iii) growing and synthesizing carbon nanotube by decomposition of supplied carbon source on the surface of a catalyst composition according to a thermal chemical vapor deposition method.
4. The process for preparing carbon nanotube according to claim 3 , wherein vertical fixed-bed reactor, horizontal fixed-bed reactor, rotary kiln reactor, mobile bed reactor, or fluidized bed reactor can be used as reactor.