Continuous manufacturing apparatus and method for carbon nanotubes having gas separation units

Patent metadata

Field	Value
Publication number	US-10081002-B2
Application number	US-201514665774-A
Country	US
Kind code	B2
Filing date	Mar 23, 2015
Priority date	Apr 5, 2011
Publication date	Sep 25, 2018
Grant date	Sep 25, 2018

Abstract

The present invention relates to a continuous manufacturing apparatus for a carbon nanotube having gas separation units and a continuous manufacturing method for a carbon nanotube using the same. According to the present invention, the present invention has an effect to provide the continuous manufacturing apparatus of the carbon nanotube and continuous manufacturing method using the same, in which it makes possible to perform a rapid processing; has excellent productivity and excellent conversion rate of carbon source; can significantly reduce the cost of production; can reduce energy consumption because a reactor size can be decreased as compared with capacity; and a gas separation unit that not generate a waste gas.

First claim

The invention claimed is:

1. A continuous carbon nanotube manufacturing apparatus, comprising:
i) a reactor for synthesizing the carbon nanotube;
ii) a separator for separating a mixed gas and the carbon nanotube transferred from the reactor;
iii) a heat exchanger between the reactor i) and the separator ii);
iv) a gas separation unit for removing, in part or in whole, a component gas from the mixed gas, the gas separation unit comprising one or more hollow tubular polymer membranes constructed to separate hydrogen from the mixed gas at a temperature of 50° C. or below; and
v) a re-circulation pipe for recirculating the mixed gas, without the component gas separated by the gas separation unit, to the reactor;
vi) a catalyst supplier connected to an upper part of the reactor, the catalyst supplier comprising a hopper; and
vii) a reaction gas supplier connected to a bottom part of the reactor,
wherein the apparatus comprises a sole product discharging pipe for discharging the product produced by the reactor i), and wherein the heat exchanger is in direct communication with the sole product discharging pipe.

2. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the one or more polymer membranes are produced with more than one polymer selected from the group consisting of polysulfone, polycarbonate, polyimide, and polystyrene.

3. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein reactor i) is a chemical vapor deposition reactor.

4. The continuous carbon nanotube manufacturing apparatus according to claim 3 , wherein the chemical vapor deposition reactor is a rotary kiln reactor or a fluidized bed reactor.

5. The continuous carbon nanotube manufacturing apparatus according to claim 4 , wherein the rotary kiln reactor or the fluidized bed reactor are connected with a catalyst supply pipe for supplying a catalyst; a reaction gas supply pipe for supplying a carbon source, a reducing gas, and an inert gas.

6. The continuous carbon nanotube manufacturing apparatus according to claim 5 , further comprising a preheater for preheating the reaction gas to a temperature of 200 to 500° C.

7. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the separator of ii) is a cyclone.

8. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the heat exchanger is constructed to cool the mixed gas and the carbon nanotube transferred from the reactor to a temperature of 40 to 50° C.

9. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the continuous manufacturing apparatus of the carbon nanotube further includes a flow controlling device constructed to control the amount of a reaction gas supplied to the reactor and the amount of component gas removed from the gas separation unit.

10. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the continuous manufacturing apparatus of the carbon nanotube further includes a flow controlling device constructed to control the amount of a reducing gas supplied to the reactor and the amount of the reducing gas passed through the gas separation unit.

11. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the continuous manufacturing apparatus does not comprise any apparatus for incinerating waste gas.

12. The continuous carbon nanotube manufacturing apparatus according to claim 1 , wherein the reactor is a vertical fluidized bed reactor constructed to provide a fluidization velocity of 0.03 to 30 cm/s.

13. The continuous carbon nanotube manufacturing apparatus according to claim 1 , further comprising a filter arranged in an expander part of the reactor.

Assignees

• Lg Chemical Ltd

Inventors

• Chang Kwang-Hyun
• Kim Jin-Do
• Yoon Kwang-Woo

Classifications

• B01J8/10

  moved by stirrers or by rotary drums or rotary receptacles {or endless belts} · CPC title

• B01J8/24 Primary

  according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title

• B82Y40/00

  Manufacture or treatment of nanostructures · CPC title

• Y10S977/843

  Gas phase catalytic growth, i.e. chemical vapor deposition · CPC title

• B01J2208/00548

  Flow · CPC title