Peeling device of sheet material including optimized outlet
11332375 · 2022-05-17
Assignee
Inventors
- Kwang Hyun Yoo (Daejeon, KR)
- Eun Jeong KIM (Daejeon, KR)
- In Young Kim (Daejeon, KR)
- Pum Suk Park (Daejeon, KR)
- Ye Hoon Im (Daejeon, KR)
- Won Jong Kwon (Daejeon, KR)
Cpc classification
B32B38/10
PERFORMING OPERATIONS; TRANSPORTING
Y10T156/1111
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
B32B43/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates to a peeling device of sheet material for peeling off graphite, and the peeling device of sheet material according to the present invention is characterized in that a specific microchannel is used to apply a shear force required to peel off graphite, and simultaneously, graphene itself is not ground and the discharge flow rate of the graphene dispersion increases to increase graphene preparation efficiency.
Claims
1. A method for preparing graphene using a peeling device of sheet material, comprising: supplying a solution comprising graphite to an inlet of the peeling device into which sheet material is supplied; applying pressure on the inlet, for pressurizing the sheet material, using a high pressure pump positioned at a front end of the inlet; passing the solution at a speed through a microchannel positioned at a back end of the inlet, to homogenize the sheet material; and recovering the graphene from an outlet positioned at a back end of the microchannel, wherein a distance (y) between the back end of the microchannel and an outlet wall surface where the sheet material discharged from the back end of the microchannel collides, and the speed (x) of the sheet material at the back end of the microchannel satisfy the following Equation 1:
y=≥m*x−b, [Equation 1] wherein m=2.7×10.sup.−5 s, wherein the speed (x) of the sheet material at the back end of the microchannel is 10 m/s to 600 m/s, and wherein b=4.2×10.sup.−5 m.
2. The method according to claim 1, wherein the outlet is cylindrical, and the back end of the microchannel is positioned at a lateral face of the cylindrical outlet.
3. The method according to claim 1, wherein a supply line for supplying the sheet material to the inlet is equipped.
4. The method for preparing graphene according to claim 1, wherein the step of applying pressure comprises applying a pressure between about 100 and about 3000 bar.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
DETAILED DESCRIPTION OF THE EMBODIMENTS
(4) Hereinafter, the present invention will be explained in detail.
(5) A peeling device of sheet material means a device that applies high pressure to a microchannel having a micrometer scale diameter, so as to apply a strong shear force to the material passing it through. By the shear force, the material passing through the microchannel is ground and dispersed, and thus, it is being used for preparing highly dispersed material. Thus, the peeling device of sheet material is being used for the preparation of products requiring high dispersion, for example, in various fields such as electrical/electronic material, bioengineering, pharmaceutical, food, fiber, painting, cosmetic industries, etc.
(6) Meanwhile, since the peeling device of sheet material is designed and prepared for crushing and grinding of material through a strong shear force, in general, a fluid passing through a microchannel strongly collides the wall surface of an outlet. However, the collision with the wall surface of the outlet may become a disadvantage according to the purpose of use the sheet peeling device.
(7) Particularly, the present invention is aimed at the preparation of graphene by peeling off graphite with a peeling device of sheet material, but in case a fluid passing through the microchannel strongly collides the wall surface of the outlet, peeled-off graphene itself may be ground. Thus, the size of graphene becomes small, thus lowering the preparation yield of large area graphene.
(8) Thus, the present invention provides a peeling device of sheet material that can increase preparation efficiency of large area graphene without grinding of graphene itself, within a range where a shear force required for peeling off graphite is applied.
(9) First,
(10) Thus, pressure is applied to the inlet (10) by the high pressure pump (11), and sheet material supplied in the inlet (10) passes through the microchannel (12). Since the cross sectional area of the microchannel (12) is small, if a pressure higher than the pressure applied to the inlet (10) is applied to the microchannel (12), and the sheet material receives a strong shear force and homogenized. The sheet material passing through the microchannel (12) is discharged to the outlet (13).
(11) Particularly, in the present invention, the sheet material may be graphite, and peeling may occur by the strong shear force in the microchannel (12) to prepare graphene. Here, there is a need to control the minimum distance between the back end (12-1) of the microchannel and the outlet (13) wall surface where the sheet material discharged from the back end (12-1) of the microchannel collides, so that the energy of collision of a fluid passing through the microchannel (12) with the wall surface of the outlet (13) may be reduced and graphene itself may not be ground,
(12) The minimum distance between the back end (12-1) of the microchannel and the outlet (13) wall surface where the sheet material discharged from the back end (12-1) of the microchannel collides means a distance from the back end of the microchannel to the outlet wall surface in a direction where a fluid passing through the microchannel (12) progresses. More specifically, it means a distance from the back end (12-1) of the microchannel (12) to the point where the extended line of the length direction of the microchannel (12) and the outlet (13) wall surface meet. For example, the outlet (13) may be cylindrical, and in this case, the back end (12-1) of the microchannel (12) is connected to the lateral face of the cylindrical outlet, and thus, the minimum distance from the back end (12-1) of the microchannel to the outlet (13) wall surface where sheet material discharged from the back end (12-1) of the microchannel collides means the diameter of the cylinder.
(13) Meanwhile, in commonly used sheet peeling devices, due to the limitation in the mechanical strength of the material used in a microchannel, the operating pressure in the microchannel is about 100 bar to about 3000 bar. Further, for homogenization in the microchannel, the cross sectional area of the microchannel is controlled within a range of about 1.00×10.sup.2 um.sup.2 to 1.44×10.sup.8 um.sup.2, and according to the operating pressure and the cross sectional area, the speed of the sheet material at the back end of the microchannel, i.e., discharge speed is determined.
(14) Thus, as the discharge speed is higher, the minimum distance between the back end of the microchannel and the outlet wall surface where sheet material discharged from the back end of the microchannel collides should be long. Meanwhile, in case a collision pressure at the time of collision of graphene with the outlet wall surface is 40 bar or less, grinding of graphene does not occur, and thus, the discharge speed and the minimum distance between the back end of the microchannel and the outlet wall surface where sheet material discharged from the back end of the microchannel collides should be controlled so that a collision pressure may become 40 bar or less.
(15) In the present invention, while the minimum distance between the back end of the microchannel and the outlet wall surface where sheet material discharged from the back end of the microchannel collides is designated as a variable y (unit m), and the speed of the sheet material at the back end of the microchannel is designated as a variable x (unit m/s), a collision pressure according to the control of each variable was measured, and the results are shown in
(16) As shown in
(17) Preferably, the minimum distance(y) is 0.001 m to 0.050 m. More preferably, the minimum distance(y) is 0.005 m or more, 0.006 m or more, 0.007 m or more, 0.008 m or more, 0.009 m or more, 0.010 m or more, 0.011 m or more, 0.012 m or more, 0.013 m or more, 0.014 m or more, or 0.015 m or more.
(18) Preferably, the speed (x) of the sheet material at the back end of the microchannel is 10 m/s to 600 m/s. As explained above, the speed of the sheet material at the back end of the microchannel may be controlled by the operating pressure in the microchannel and the cross sectional area of the microchannel.
(19) Further, the peeling device of sheet material according to the present invention may be equipped with a supply line for supplying sheet material to the inlet (10). Through the supply line, the input of sheet material, etc. can be controlled.
(20) Further, the present invention also provides a method for preparing graphene using the above sheet peeling device, said method comprising the steps of:
(21) 1) supplying a solution comprising graphite to the inlet (10);
(22) 2) putting pressure on the inlet (10) with a high pressure pump (11) to pass the solution comprising graphite through the microchannel (12); and
(23) 3) recovering a graphene dispersion from the outlet (13).
(24) As explained above, the method for preparing graphene is conducted so as to fulfill the requirement of the above Equation 1, thereby preventing graphene from colliding the wall surface of the outlet and being ground.
(25) The pressure of the step 2 is preferably 100 to 3000 bar. Further, after recovering a graphene dispersion from the outlet (13), it may be reintroduced into the inlet (10). The reintroduction process may be conducted 2 to 30 times repeatedly. The reintroduction process may be conducted using the sheet peeling device used, or using plural sheet peeling devices. Further, the reintroduction process may be conducted dividedly according to the process, or may be continuously conducted.
(26) Meanwhile, the method for preparing graphene may further comprise the steps of recovering graphene from the recovered graphene dispersion and drying it. The recovery step may be progressed by centrifugation, vacuum filtration or pressure filtration. Further, the drying step may be conducted by vacuum drying or general drying at a temperature of about 30 to 200° C.
(27) Further, the size of graphene prepared according to the present invention is large and uniform, and thus, favorable for the realization of the unique properties of graphene. The prepared graphene may be redispersed in various solvents and utilized as various uses such as a conductive paste composition, a conductive ink composition, a composition for forming a heat radiating substrate, an electroconductive complex, a thermally conductive complex, a complex for shielding EMI, or conductor or slurry for batteries, etc.
(28) Hereinafter, preferable examples are presented for better understanding of the present invention. However, these examples are presented only as the illustrations of the present invention, and the present invention is not limited thereby.
Example 1
(29) 1) A Peeling Device of Sheet Material
(30) A microchannel as shown in
(31) 2) Peeling of Graphite
(32) 2.5 g of graphite (BNB90) and 1 g of PVP58k (polyvinylpyrrolidone, weight average molecular weight: 58 k) as a dispersant were mixed with 500 g of distilled water to prepare a feed solution. The feed solution was supplied while applying a high pressure of 730 bar through the inlet (10), and the feed solution was recovered from the outlet (13).
Example 2
(33) Graphene was prepared using the same device as Example 1, except that an outlet (13) with an increased diameter of 15 mm was used.
Experimental Example 1
(34) The size of graphene in the sample obtained in each Example was measured. Specifically, the lateral size distribution of dispersed graphene was measured with LA-960 Laser Particle Size Analyzer, and the results are shown in
Experimental Example 2
(35) The peeling device of sheet material used in Example 1 was used, except that a device capable of measuring a collision pressure that can control the distance from the back end of the microchannel was used instead of the outlet. The speed of the sheet material discharged from the back end of the microchannel was controlled to specific values, and the distances from the back end of the microchannel where a collision pressure at each discharge rate became 40 bar were measured, and the results are shown in
(36) In
EXPLANATION OF SIGN
(37) 1: peeling device of sheet material 10: inlet 11: high pressure pump 12: microchannel 12-1: back end of microchannel 13: outlet