CNT and method for manufacturing thereof

Patent metadata

Field	Value
Publication number	US-9399578-B2
Application number	US-201314348833-A
Country	US
Kind code	B2
Filing date	Jan 9, 2013
Priority date	Jan 11, 2012
Publication date	Jul 26, 2016
Grant date	Jul 26, 2016

Abstract

Disclosed are carbon nanotubes and a method for manufacturing the same wherein the carbon nanotubes (CNTs) which comprise a three-component carbon nanotube catalyst containing a catalytic component and an active component and have a potato or spherical shape with a particle diameter distribution (Dcnt) of 0.5 to 1.0 can be manufactured at a high yield using an impregnated supported catalyst by simultaneously removing activity and a fine powder of the impregnated supported catalyst in an attempt to solve a drawback of conventional impregnation methods for producing CNTs, namely, the difficulty in improving a yield of CNTs.

First claim

What is claimed is:

1. Particles comprising:
an alumina support;
a three-component catalyst that comprises a catalytic component, a multicarboxylic acid and an active component coated on a surface of the alumina support; and
carbon nanotubes on a surface of the three-component catalyst,
wherein the catalytic component comprises a first catalytic component and a second catalytic component,
wherein a number of moles (x) of the first catalytic component, a number of moles (y) of the second catalytic component and a number of moles (z) of the active component satisfy ranges of 30≦x+y≦53, 0.1≦y/[x+y]≦0.95 and 3≦z≦13, based on 100 moles of the alumina support,
wherein the each of the particles has a spherical shape having a particle diameter distribution (Dcnt) of 0.5 to 1.0,
wherein the particle diameter distribution (Dcnt) is defined by Equation 1:
Dcnt=[Dn 90− Dn 10]/ Dn 50  [Equation 1]

wherein Dn90 is a number average particle diameter which is measured based on 90% in an absorption mode using Microtrac particle diameter analyzer after the particles are immersed in distilled water and then allowed to stand for 3 hours, Dn10 is a number average particle diameter measured based on 10% under the same condition as Dn90, and Dn50 is a number average particle diameter measured based on 50% under the same condition as Dn90, and
wherein a molar ratio of the multicarboxylic acid to the active component is in a range of 0.34616 to 0.36665.

2. The particles according to claim 1 , wherein the particles are a non-bundle type having an ellipticity of 0.9 to 1.0.

3. The particles according to claim 1 , wherein the particles have a bulk density of 80 to 250 kg/m 3 , a particle diameter or an average particle diameter of 300 to 800 μm, and
wherein a diameter of each of the carbon nanotubes is 10 to 50 nm.

4. The particles according to claim 1 , wherein the three-component catalyst provides a carbon nanotube yield of 2,000% or higher.

5. The particles according to claim 1 , wherein the three-component catalyst has a structure in which the first catalytic component comprising at least one selected from Fe and Ni, the second catalytic component comprising Co, and the active component comprising Mo are coated as one-layer or a multi-layer on the surface or pores of the alumina support,
wherein the particles comprise an ultrasonic fine powder of 10% or less, and
wherein the ultrasonic fine powder is the particles having a number average particle diameter of 32 μm or less, measured after ultrasonic-shaking for one minute by an ultrasonicator, which is set to 40 watts.

6. The carbon nanotube particles according to claim 5 , wherein the carbon nanotube particles comprise the ultrasonic fine powder of 5% or less.

7. The particles according to claim 1 ,
wherein the three-component catalyst is obtained from a mixture solution obtained by sequentially adding the multicarboxylic acid, the first catalytic component and the second catalytic component to the active component to prepare a clear aqueous metal solution and then adding the clear aqueous metal solution to the alumina support.

8. The particles according to claim 7 , wherein the mixture solution is obtained as a supported catalyst in which the first catalytic component, the second catalytic component and the active component are impregnated in and coated on the surface and pores of the alumina support through vacuum-drying and then baking.

9. The particles according to claim 7 , wherein the clear aqueous metal solution has a concentration of 0.1 to 0.4 g/ml.

10. The particles according to claim 1 , wherein the multicarboxylic acid comprises at least one selected from the group consisting of dicarboxylic acid, tricarboxylic acid and tetracarboxylic acid.

11. A method for manufacturing carbon nanotubes comprising:
sequentially mixing an active component precursor aqueous solution with a multicarboxylic acid component and a catalytic component precursor aqueous solution to prepare a clear aqueous metal solution and mixing the clear aqueous metal solution with an alumina support;
vacuum-drying the resulting mixture at 40 to 80° C. and then baking the mixture at 650 to 800° C. to obtain a carbon nanotube catalyst in which a catalytic component and an active component are impregnated in and coated on the surface and pores of the alumina support;
loading the carbon nanotube catalyst into a fluidized bed reactor and injecting at least one carbon source selected from C1-C4 saturated or unsaturated hydrocarbons, or the selected carbon source and a mixed gas of hydrogen and nitrogen into the reactor at 500 to 900° C.; and
growing the carbon nanotubes of claim 1 on the surface of the catalyst by chemical vapor synthesis using decomposition of the carbon source,
wherein the catalytic component precursor aqueous solution comprises a first catalytic component precursor aqueous solution and a second catalytic component precursor aqueous solution, a number of moles (x) of the first catalytic component precursor aqueous solution, a number of moles (y) of the second catalytic component precursor aqueous solution and a number of moles (z) of the active component precursor aqueous solution satisfy ranges of 30≦x+y≦53, 0.1≦y/[x+y]≦0.95 and 3≦z≦13, based on 100 moles of the alumina support, and
wherein a molar ratio of the multicarboxylic acid to the active component is in the range of 0.34616 to 0.36665.

12. The method according to claim 11 , further comprising aging the mixture 45 to 80° C. before the vacuum drying.

13. The method according to claim 11 , further comprising pre-baking the mixture at 250 to 400° C. after the vacuum-drying and before the baking.

14. The method according to claim 13 , wherein a portion of the total amount of the aqueous metal solution is impregnated in the alumina support immediately before the pre-baking and the residue of the aqueous metal solution is impregnated in the alumina support immediately before the baking.

Assignees

• Lg Chemical Ltd

Inventors

• Kang Kyung Yeon
• Kim Jin Do
• Kim Sung Jin
• Yoon Jae Keun

Classifications

• B82Y40/00

  Manufacture or treatment of nanostructures · CPC title

• B82Y30/00

  Nanotechnology for materials or surface science, e.g. nanocomposites · CPC title

• B01J37/0203

  the impregnation liquid containing organic compounds · CPC title

• B01J37/0236

  Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title

• B01J37/0234

  Impregnation and coating simultaneously · CPC title