IP Library Granted Patent US 9,862,611
Granted Patent B1
US 9,862,611 · App. 15/666,742 · Granted Jan 9, 2018

Method for producing carbon nanotubes

Inventors: Ji-Min Kim (Daejeon, KR); Min-Ji Sung (Daejeon, KR); Yong-Tak Kwon (Daejeon, KR); Sang-Uk Kim (Daejeon, KR); Ok-Youn Kim (Daejeon, KR); Sung-Real Son (Daejeon, KR); Jung-Yul Son (Daejeon, KR)
Assignees: SK Innovation Co., Ltd.; SK Global Chemical Co., Ltd.
C01B32/162B01J8/0015B01J8/1827B01J2208/00752B82Y30/00B82Y40/00Y10S977/742Y10S977/843
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Quick Facts
Patent No.
US 9,862,611
App. No.
15/666,742
Granted
Jan 9, 2018
Kind
B1
Abstract

Disclosed is a method for producing a carbon nanotube, including supplying a carbon nanotube and a catalyst to a reactor in a predetermined order or simultaneously and fluidizing them to form a fluidized bed, wherein a difference in minimum fluidization velocities (ΔV) according to Formula 1 below is 5 cm/s or less: [Formula 1] Difference in minimum fluidization velocities (ΔV, cm/s)=|V cat −V cntproduct | wherein V cat is a minimum fluidization velocity of catalyst, and V CNTproduct is a minimum fluidization velocity of carbon nanotubes supplied to a reactor in the step of forming a fluidized bed.

Claims (13)

1. A method for producing carbon nanotubes, comprising: supplying carbon nanotubes and catalysts to a reactor in a predetermined order or simultaneously and fluidizing them to form a fluidized bed,

wherein a difference in minimum fluidization velocities (ΔV) according to the following formula 1 is not more than 5 cm/s:

Difference in minimum fluidization velocities (Δ V , cm/s)=| V cat −V CNT product |  [Formula 1]

wherein V cat is a minimum fluidization velocity of catalyst, and V CNT product is a minimum fluidization velocity of carbon nanotubes supplied to a reactor in the step of forming a fluidized bed.

2. The method of claim 1 , wherein the minimum fluidization velocity of the catalyst is 0.1 cm/s to 10 cm/s.

3. The method of claim 1 , wherein the catalyst has a particle density of 1,300 kg/cm 3 to 2,200 kg/cm 3 .

4. The method of claim 1 , wherein the catalyst has a diameter of 10 μm to 300 μm.

5. The method of claim 1 , wherein, in the step of forming the fluidized bed, when the carbon nanotubes and the catalyst are filled in the reactor to form a packed bed, the packed bed is formed to have a ratio of height to diameter (L/D) of 1 or more.

6. The method of claim 1 , wherein, in the step of forming the fluidized bed, the carbon nanotubes and the catalyst are supplied to the reactor so that a weight ratio of the carbon nanotubes to the catalyst contained in the fluidized bed is 1:0.5 to 1:1.

7. The method of claim 1 , further comprising growing carbon nanotubes on the catalyst by reacting a source gas and the catalyst.

8. The method of claim 7 , wherein, in the step of growing the carbon nanotubes, the temperature difference (ΔT) according to the following formula 2 is 20° C. or less:

Temperature difference (Δ T , ° C.)= T 1 −T 2   [Formula 2]

wherein T 1 and T 2 indicate a temperature of the fluidized bed as measured at two different heights, each being selected arbitrarily from a height ranging from the bottom to the top of the fluidized bed.

Assignments (2)
CHANGE OF NAME Recorded Sep 2, 2022
From: SK GLOBAL CHEMICAL CO., LTD
To: SK GEO CENTRIC CO., LTD.
Reel/Frame 061371/0332 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 2, 2017
From: KIM, JI-MIN; SUNG, MIN-JI; KWON, YONG-TAK; KIM, SANG-UK; KIM, OK-YOUN; SON, SUNG-REAL; SON, JUNG-YUL
To: SK INNOVATION CO., LTD.; SK GLOBAL CHEMICAL CO., LTD.
Reel/Frame 043169/0015 →
Priority Claims (1)
KR 10-2016-0099399 · Aug 4, 2016 · national