Device for drying and recovering carbon nanotube product and method for manufacturing carbon nanotube using same

Abstract

The present invention relates to a device for drying and collecting a product such as a carbon nanotube pellet or aggregate, which can accelerate solvent evaporation by inserting and dispersing high temperature gas into a drying column as well as by a heat source inside and outside of the column, and can quickly remove the evaporated solvent. Further, the device can be used for drying and collecting processes while minimizing product breakage by regulating the gas flow rate and controlling flow of the product in the column. Thus, the device can be effectively applied to mass production of a carbon nanotube pellet product.

Claims

1. A device for drying and collecting a carbon nanotube product comprising: a drying part, which receives a carbon nanotube product to be dried and dries the product; a product collecting part, which is installed at the bottom of the drying part; a gas inlet part, which is installed on top of the drying part or between the drying part and the product collecting part, for flowing gas into the drying part; and at least one valve, which is installed between the drying part and the product collecting part and has a plurality of opening parts allowing fluid communication.

2. The device for drying and collecting a carbon nanotube product according to claim 1, wherein the gas inlet part is installed between the drying part and the product collecting part, and the at least one valve comprises: a first valve installed between the drying part and the gas inlet part, and a second valve installed between the gas inlet part and the product collecting part.

3. The device for drying and collecting a carbon nanotube product according to claim 2, wherein the opening part of the first valve allows gas from the gas inlet part to flow into the drying part while preventing the product from flowing out to the collecting part during the product drying process in the drying part.

4. The device for drying and collecting a carbon nanotube product according to claim 1, wherein the carbon nanotube product is a carbon nanotube pellet or a carbon nanotube aggregate.

5. The device for drying and collecting a carbon nanotube product according to claim 1, wherein the drying part is vertical column type.

6. The device for drying and collecting a carbon nanotube product according to claim 2, wherein the first valve or the second valve is each independently a butterfly valve or a damper valve.

7. The device for drying and collecting a carbon nanotube product according to claim 6, wherein the first valve has a plurality of opening parts on the surface of a wing part of the butterfly valve or the damper valve.

8. The device for drying and collecting a carbon nanotube product according to claim 7, wherein a mesh sheet through which the carbon nanotube product cannot be communicated but only a fluid can be communicated is located over a part or a whole of the opening part.

9. The device for drying and collecting a carbon nanotube product according to claim 7, wherein a bubble cap is covered over a part or a whole of the opening part.

10. The device for drying and collecting a carbon nanotube product according to claim 1, which further comprises a preheater for preheating the gas to be flowed into the gas inlet part.

11. The device for drying and collecting a carbon nanotube product according to claim 1, which further comprises a flow rate controller for controlling the follow rate of the gas to be flowed into the gas inlet part.

12. The device for drying and collecting a carbon nanotube product according to claim 1, wherein a gas outlet is installed on top of the drying part to control pressure in the drying part.

13. The device for drying and collecting a carbon nanotube product according to claim 1, wherein a third valve is installed at the bottom of the product collecting part to discharge a product.

14. The device for drying and collecting a carbon nanotube product according to claim 13, wherein a second gas inlet part is installed at the product collecting part to introduce gas which helps discharge of a product.

15. A method for manufacturing a carbon nanotube product comprising the steps of: receiving a carbon nanotube product to be dried in a drying part; drying the carbon nanotube product while flowing gas into the drying part through a gas inlet part installed on top of the drying part or between the drying part and a product collecting part at the bottom of the drying part; controlling pressure in the drying part by discharging gas through a gas outlet installed on top of the drying part; and collecting the dried carbon nanotube product through the product collecting part installed at the bottom of the drying part, wherein a valve having a plurality of opening parts allowing fluid communication is installed between the drying part and the product collecting part, so that gas flow is allowed while preventing discharge of the product during the product drying process in the drying part.

16. The method for manufacturing a carbon nanotube product according to claim 15, wherein the gas inlet part is installed between the drying part and the product collecting part, and the valve having a plurality of opening parts comprises a first valve installed between the drying part and the gas inlet part and a second valve installed between the gas inlet part and the product collecting part, wherein when proceeding a drying process, the gas flows in with the first valve closed to proceed the drying process, and when collecting the dried product, the first valve is opened to introduce the product into the gas inlet part, and then the first valve is closed and the second valve is opened to introduce the product into the collecting part.

17. The method for manufacturing a carbon nanotube product according to claim 15, wherein a second gas inlet part is installed at the product collecting part to introduce gas which helps discharge of a product.

18. The method for manufacturing a carbon nanotube product according to claim 15, which further comprises the steps of: pyrolyzing an organic compound with a transition metal or its compound as a catalyst in a pyrolysis furnace to obtain carbon nanotubes to be introduced into the drying part; separating reactive exhaust gas generated at the pyrolysis process from the carbon nanotubes; and incinerating the reactive exhaust gas separated from the carbon nanotubes.

19. The method for manufacturing a carbon nanotube product according to claim 15, wherein the exhaust gas discharged from the gas outlet is incinerated.

20. The method for manufacturing a carbon nanotube product according to claim 19, wherein the reactive exhaust gas generated at a pyrolysis process for manufacturing a carbon nanotube product is also incinerated when incinerating the exhaust gas.

Description

DESCRIPTION OF DRAWINGS

(1) FIG. 1 is a schematic diagram of a device for drying and collecting a carbon nanotube product according to one embodiment of the present invention.

(2) FIG. 2 is a schematic diagram partially magnifying the device of FIG. 1.

(3) FIG. 3 is a diagram schematically illustrating shape of the spray nozzle illustrated in FIG. 2.

(4) FIG. 4 and FIG. 5 are plane figures schematically illustrating an embodiment of a first valve.

(5) FIG. 6 and FIG. 7 are graphs showing the results of the tests according to the present invention.

MODE FOR INVENTION

(6) Prior to a detailed description of the present invention, the present invention may be variously modified and altered and have several exemplary embodiments. Examples described below and illustrated in the drawings are not to limit the present invention to specific exemplary embodiments. In addition, various modifications, alterations, and amendments may be made in the scope of the following claims, and it may be understood that these modifications, alterations, and amendments fall within the scope of the present invention. When it is decided that a detailed description for the known art related to the present invention may unnecessarily obscure the gist of the present invention, the detailed description will be omitted.

(7) It is to be understood that when one element is referred to as being connected to or coupled to another element, it may be connected directly to or coupled directly to another element with the other element intervening therebetween.

(8) Singular forms include plural forms unless the context clearly indicates otherwise.

(9) It will be further understood that terms include, have, or the like, used in the present specification are to specify the presence of features, numerals, steps, operations, components, parts mentioned in the present specification, or a combination thereof, but do not preclude the presence or addition of one or more other features, numerals, steps, operations, components, parts, or a combination thereof.

(10) The term carbon nanotube used in the present specification may refer to a singular or plural carbon nanotube, and the term may include a fiber form formed by a plurality of carbon nanotubes.

(11) Hereinafter, with reference to drawings, embodiments of the present invention are described in detail in a manner that one of ordinary skill in the art may perform the embodiments without undue difficulty. The present invention may be embodied in various forms, and the scope of the present invention is not limited to examples provided herein.

BEST MODE CARRYING OUT THE INVENTION

(12) The device according to the present invention comprises:

(13) a drying part, which receives a carbon nanotube product to be dried and dries the product;

(14) a product collecting part, which is installed at the bottom of the drying part;

(15) a gas inlet part, which is installed on top of the drying part or between the drying part and the product collecting part, for flowing gas into the drying part; and

(16) a valve, which is installed between the drying part and the product collecting part and has a plurality of opening parts allowing fluid communication.

(17) In the present invention, the carbon nanotube product may refer to a carbon nanotube pellet or a carbon nanotube aggregate.

(18) FIG. 1 schematically illustrates a device for drying and collecting a carbon nanotube product, wherein a gas inlet part is installed between the drying part and the product collecting part, according to one embodiment of the present invention. Namely, FIG. 1 illustrates a structure designed to make gas flow from bottom to top of the drying part. However, the present invention is not limited thereto and also contains a structure wherein the gas flows from top to bottom of the drying part. When the gas flow from top to bottom of the drying part, the heat transferred from the furnace wrapping the heating part can be directly transferred to the gas, and therefore drying can be conducted with the gas of higher temperature.

(19) FIG. 1 illustrates a device for drying and collecting a carbon nanotube product 100 comprises:

(20) a drying part 10, which receives a carbon nanotube product to be dried and dries the product;

(21) a product collecting part 20, which is installed at the bottom of the drying part;

(22) a gas inlet part 30, which is installed between the drying part 10 and the product collecting part 20, for flowing gas into the drying part;

(23) a first valve 50 installed between the drying part 10 and the gas inlet part 30 and has a plurality of opening parts allowing fluid communication; and

(24) a second valve 60 installed between the gas inlet part and the product collecting part.

(25) The drying part 10 may be vertical column type, and equipped with a heating means 12 for heating the drying part. As illustrated in FIG. 1, the heating means 12 may be a furnace wrapping the drying part 10, but not limited thereto.

(26) The device illustrated in FIG. 1 preferably further comprises a preheater 32 for preheating the gas to be flowed into the gas inlet part 30, and a flow rate controller 33 for controlling the follow rate of the gas to be flowed into the gas inlet part 30. The gas introduced in to the gas inlet part 30 is used to prevent agglomeration of a product in the drying part 10 and to promote drying the product in the drying part 10 by adding additional heat. Accordingly, the gas may preferably be inert gas which does not react with the product. Nitrogen gas is most preferred, but not limited thereto.

(27) Further, a gas outlet 13 may be installed on top of the drying part 10 to control pressure in the drying part 10 by controlling the amount of the discharged gas 14.

(28) On the other hand, whether the product in the drying part 10 reaches a predetermined dried state or not can be checked by a method of measuring the temperature change in the drying part 10 (i.e., check whether there is little temperature change) or a method of measuring moisture in the exhaust gas discharged from the outlet 13 (e.g., using a hygrometer) to check whether the moisture content is within a certain level or not, but not limited thereto. The exhaust gas discharged from the gas outlet 13 may mainly contain nitrogen or water, but if an organic solvent is used instead of water when preparing a CNT pellet, the gas may contain a large quantity of the solvent evaporated during the product drying process. The gas may be evaporated or incinerated. However, if the gas is unreactive or flame retardant, the incineration efficiency may be deteriorated. It is also possible to incinerate this unreactive and flame retardant exhaust gas together with the exhaust gas discharged from the carbon nanotube synthesis process, i.e., the flammable reactive exhaust gas containing hydrogen, hydrocarbon and the like. Namely, when the reaction of the carbon nanotube synthesis process is finished, the reactive exhaust gas remained in a reaction system or a reactive exhaust gas feeding line can be incinerated by purging the gas with the unreactive and flame retardant gas discharged from the process according to the present invention, and therefore, backfiring into the reactive exhaust gas feeding line can be prevented and also the combustion efficiency can be increased.

(29) FIG. 2 is a schematic diagram for describing constitution of the gas inlet part 30 and the product collecting part 20 in more detail.

(30) The gas inlet part 30 is equipped with a nozzle 34 for spraying the introduced gas upward toward the drying part 10 thereby feeding the gas through the opening part of the first valve 50, preferably. The shape of the nozzle 34 may refer to FIG. 3.

(31) Further, as illustrated in FIG. 2, the first valve 50 is installed at to bottom of the drying part 10, whereunder the gas inlet part 30 and the second valve 60 are installed.

(32) The product collecting part 20 may be located below the second valve 60, and for easier product collecting, the second gas inlet 25 and the third valve 27 may be installed at the bottom of the product collecting part 20. The gas introduced through the second gas inlet 25 is sprayed through the spray nozzle 24 to prevent agglomeration of the product during the product discharging process. The shape of the spray nozzle 24 may be the same as illustrated in FIG. 3, but not limited thereto. The gas to be introduced may preferably be inert gas and there is no need to preheat the gas.

(33) FIG. 4 to FIG. 5 illustrate an example of the first valve 50. The valve may be a butterfly valve or a damper valve. The first valve has a central axis 51. Accordingly, the valve is rotatable and foldable on the axis and therefore, the valve is openable.

(34) In order to prevent the product flowing out during product drying, the butterfly valve or the damper valve is used. However, the valve blocks the gas flow when the valve is closed, and therefore hot air flow of the upper part of the valve (drying part) is reduced. Thus, it causes reduction of the drying efficiency. According to the present invention, the opening part 53 of the first valve 50 may improve the drying efficiency by allowing hot air flow through introduction of the gas from the gas inlet part 20 to the drying part 10, while preventing the product from discharging to the collecting part 20 during the product drying process in the drying part 10.

(35) For the second valve 60 or the third valve 27, a butterfly valve or a damper valve without an opening part can be used. Namely, as illustrated in FIG. 4 to FIG. 6, the first valve may have a plurality of opening parts 53 on the surface of a wing part 52 of the butterfly valve or the damper valve.

(36) Further, not illustrated herein, a mesh sheet through which the carbon nanotube product can't be communicated but only flow can be communicated may be put over a part or a whole of the opening part 53.

(37) According to another embodiment, as illustrate in FIG. 5, a bubble cap 55 may be covered over a part or a whole of the opening part 53.

(38) According to the present invention, by placing the first valve 50 and the second valve 60 at the bottom of the drying part 10, it is possible to feed hot air into the drying part by using the high temperature gas while first valve 50 is closed. Thus, the drying process can be proceeded efficiently. Further, during the collecting process of the dried product, it is possible to open the first valve 50 to introduce the product into the gas inlet 30, and then to close the first valve 50 and to open the second valve 60 to introduce the product into the collecting part 20. Thus, without stopping the drying process or lowering the temperature, it is possible to proceed the drying process and the product collecting process continuously.

(39) The device illustrated in FIG. 1 was assembled by using a lab-scale cylinder-type high temperature dryer (Internal diameter 50 mm quartz tube), and FIG. 6 and FIG. 7 show the results of tests performed with the device. Test conditions are as listed in the following Table 1.

(40) TABLE-US-00001 TABLE 1 Test 1 Test 2 Input of CNT pellet 300 g 300 g Drying time 90 min 180 min Nitrogen gas flow rate 2.7 cm/s 2.7 cm/s Furnace temperature 300 C. 300 C.

(41) Namely, the tests were performed at the same conditions except for changing the drying time, and the drying rate, the percentage of water content and the bed temperature change were observed.

(42) FIG. 6 shows the drying rate and the bed temperature according to the drying time, and FIG. 7 shows the percentage of water content according to the drying time.

(43) According to the above results, in spite of short drying time of 90 min, the final percentage of water content is acceptable to 1% or less, and the damage rate was just less than 5%. Accordingly, it can be found that the drying efficiency of the compressed pellet difficult to be dried can be also enhanced, and the drying rate and the water content can be easily controlled.

(44) Although the present invention has been described in detail with reference to the specific features, it will be apparent to those skilled in the art that this description is only for a preferred embodiment and does not limit the scope of the present invention. Thus, the substantial scope of the present invention will be defined by the appended claims and equivalents thereof.