TWM539423U - Slurry dispersing system and apparatus - Google Patents

Abstract

A slurry dispersing system and apparatus are provided. The system comprises a rotating apparatus and a slurry dispersing apparatus. The slurry dispersing apparatus comprises a container and a porous dispersing structure. The container is disposed at the rotating apparatus and has a first accommodating space. The porous dispersion structure is disposed in the first accommodating space of the container, and has a second accommodating space and a plurality of dispersing holes. The first accommodation space of the container or the second accommodation space of the porous dispersion structure accommodates slurry with a plurality of particles. The rotating apparatus rotates the vessel, the porous dispersion structure and the slurry. The particles of the slurry flow through the dispersing holes to circulate between the first accommodating space of the container and the second accommodating space of the porous dispersing structure to disperse the particles of the slurry.

Description

Slurry dispersion system and device

The present disclosure relates to a slurry dispersion system and apparatus, and more particularly to a slurry dispersion system and apparatus having a porous dispersion structure.

Slurry (such as living material or carbon black) has high surface area and high structural characteristics. Whether it is a general preparation slurry or a nano-milled dispersion, it is easy to aggregate in a solution and it is difficult to prepare a uniformly dispersed slurry. . Alternatively, the slurry prepared by nanometer grinding into nanometer particle size may be re-aggregated into larger particles during storage and transportation due to internal cohesion, so that the physical properties of the slurry (such as viscosity or particle size distribution) Changes occur and deviate from the initial uniform dispersion state, so that subsequent applications produce variations.

Moreover, the structure of the general slurry dispersing device is complicated and the operation is relatively difficult. In the agitation process of the slurry dispersing device, the single particles and the aggregated particles of the slurry are easily aggregated and settled at the bottom of the container, and a dead zone is formed at the corner of the container to disperse a single particle or aggregated particles of a part of the slurry. At the same time, the slurry is also prone to agglomerated particles having a larger particle size, and the particle size of the aggregated particles of the slurry is distributed over a wider range. In addition, after the slurry is allowed to stand for a period of time, the viscosity of the slurry is greatly changed compared to the viscosity of the slurry at the initial time.

Therefore, how to overcome the problems of the prior art mentioned above has become a problem that is currently being solved.

The present disclosure provides a slurry dispersion system and a slurry dispersion device that can more uniformly disperse a slurry having a plurality of particles.

The slurry dispersion system of the present disclosure includes a rotating device and a slurry dispersion device. The slurry dispersing device comprises: a container connected to the rotating device or disposed on the rotating device, and the container has a first accommodating space; and a porous dispersing structure, which is received in the first accommodating space of the container, The porous dispersion structure has a second accommodating space and a plurality of dispersion holes, and the first accommodating space of the container or the second accommodating space of the porous dispersion structure accommodates the slurry having a plurality of particles, wherein the rotation is performed by the rotating device a container, a porous dispersion structure and a slurry therein, such that a plurality of particles of the slurry pass through a plurality of dispersion holes of the porous dispersion structure to circulate or flow in the first accommodation space of the container and the second volume of the porous dispersion structure Between the spaces, a plurality of particles of the slurry are dispersed.

The slurry dispersing device of the present disclosure comprises: a container having a first accommodating space; and a porous dispersion structure accommodated in the first accommodating space of the container, the porous dispersing structure having a second accommodating structure a space and a plurality of dispersion holes, and the first accommodation space of the container or the second accommodation space of the porous dispersion structure accommodates a slurry having a plurality of particles, wherein the container is rotated, the porous dispersion structure and the slurry therein So that a plurality of particles of the slurry pass through the plurality of dispersion holes of the porous dispersion structure to circulate or flow between the first accommodating space of the container and the second accommodating space of the porous dispersion structure, thereby dispersing the slurry Particles.

It can be seen from the above that in the slurry dispersion system and the slurry dispersion device of the present disclosure, the plurality of particles of the slurry pass through the porous dispersion structure mainly by rotating the container, the porous dispersion structure and the slurry therein. The plurality of dispersed pores circulate or flow between the container and the accommodating space of the porous dispersion structure, thereby achieving the effect of more uniformly dispersing the plurality of particles of the slurry.

The above described features and advantages of the present invention will be more apparent from the following description. Additional features and advantages of the present invention will be set forth in part in the description. The features and advantages of the present invention are realized and attained by the elements and combinations particularly pointed out in the appended claims. It is to be understood that both the foregoing general description and

1‧‧‧Slurry Dispersion System

2‧‧‧Rotating device

21‧‧‧First rotating module

22‧‧‧Second Rotary Module

3‧‧‧Slurry dispersing device

31‧‧‧ Container

311‧‧‧First accommodation space

32‧‧‧Porously dispersed structure

321‧‧‧Second accommodating space

322‧‧‧Distributed holes

323‧‧‧ spoiler

324‧‧‧ inside

325‧‧‧ outside

326‧‧‧Ontology

327‧‧‧ skeleton

4a, 4b‧‧‧ slurry

41a, 41b‧‧‧ particles

A1, A2‧‧‧ Location

B1, B2, B3‧‧‧ Location

C1, C2, C3‧‧‧ location points

D1‧‧‧Rotation direction

D2‧‧‧Right direction

D3‧‧‧ Flow direction

F1‧‧‧Reflow

F2‧‧‧ turbulence

H1, H2‧‧‧ strips

L‧‧‧ aperture

L1, L3‧‧‧ primary particle size

L2, L4‧‧‧ aggregate particle size

M1, M2‧‧‧ range

R‧‧‧dead zone

S1, S2‧‧‧ curve

Θ‧‧‧ tilt angle

1A and 1B are perspective views of the slurry dispersing system and the slurry dispersing device of the present disclosure, wherein FIG. 1B has an inclination angle θ compared to FIG. 1A; FIG. 2 is a first embodiment and a first embodiment of FIG. The schematic diagram of the expanded structure of the porous dispersion structure in the slurry dispersion system and the slurry dispersion device; FIG. 3A and FIG. 3B are diagrams showing a part of the porous dispersion structure of FIGS. 1A to 2, by using a plurality of dispersion holes and Schematic diagram of the spoiler dispersing slurry, wherein FIG. 3A is a perspective view, FIG. 3B is a partial cross-sectional view of FIG. 3A, and FIGS. 4A and 4B are the slurry of the first FIG. 1 to FIG. Schematic diagram of dispersed pores having different opening ratios in the porous dispersion structure of the dispersion system and the slurry dispersing device; FIG. 5A is a porous dispersion of the slurry dispersing system and the slurry dispersing device of the first to fourth drawings of the present disclosure Schematic diagram of the pore size of the dispersed pores in the structure; FIG. 5B is a schematic diagram showing the particle sizes of the single particles and the aggregated particles in the two different slurries; and FIG. 6A is a schematic diagram showing the results of dispersing the slurry without using the porous dispersed structure disclosed herein; 6B is a schematic view showing the results of dispersing the slurry using the porous dispersion structure of the present disclosure; and FIG. 7 is a comparison diagram of the results of dispersing the slurry without using the porous dispersion structure of the present disclosure and the porous dispersion structure using the present disclosure; And Figure 8 is a comparison of another result of the use of the porous dispersion structure of the present disclosure and the use of the porous dispersion structure of the present disclosure to disperse the slurry.

The embodiments of the present disclosure are described in the following specific embodiments, and those skilled in the art can easily understand other advantages and functions of the disclosure by the contents disclosed in the specification, and can also be implemented by other different embodiments. Or application.

1A and 1B are perspective views of the slurry dispersing system 1 and the slurry dispersing device 3 of the present disclosure, wherein the first drawing B has an inclination angle θ than the first embodiment AA. 2 is a developed perspective view of the porous dispersion structure 32 in the slurry dispersion system 1 and the slurry dispersion device 3 of FIGS. 1A and 1B. 3A and 3B are parts of FIG. 1A to FIG. 2 of the disclosure In the porous dispersion structure 32, a schematic diagram of dispersing a slurry (see the slurry 4a or the slurry 4b in FIG. 6B) by a plurality of dispersion holes 322 and a spoiler 323, wherein FIG. 3A is a perspective view, and FIG. 3B is a perspective view. A partial cross-sectional view of Fig. 3A.

As shown in FIGS. 1A to 3B, the slurry dispersion system 1 may include a rotating device 2 (such as a rotating platform) and at least one (eg, one or two) slurry dispersing device 3. If it is a slurry dispersing device 3, it can be placed on the rotating device 2 (such as a central position). In the case of the two rotating devices 2, they can be respectively disposed at opposite ends of the rotating device 2. The following is described in a slurry dispersing device 3.

The slurry dispersion device 3 includes a container 31 and a porous dispersion structure 32. The container 31 can be connected to the rotating device 2 or disposed on the rotating device 2, and the container 31 has a first receiving space 311. The porous dispersion structure 32 is received in the first accommodating space 311 of the container 31, and the porous dispersion structure 32 has a second accommodating space 321 and a plurality of dispersion holes 322. At least one of the first accommodating space 311 of the container 31 and the second accommodating space 321 of the porous dispersion structure 32 can accommodate a slurry having a plurality of particles (see the slurry 4a or the slurry 4b of Fig. 6B).

Therefore, by rotating the container 31, the porous dispersion structure 32, and the slurry therein by the rotating device 2, and by the centrifugal force action, the gravity action, the shaking oscillating force, and the restraint of the container 31, the particles of the slurry can be worn. The plurality of dispersion holes 322 of the porous dispersion structure 32 are continuously circulated or flowed between the first accommodating space 311 of the container 31 and the second accommodating space 321 of the porous dispersion structure 32, thereby uniformly dispersing the slurry. Multiple particles.

The above rotating device 2 can be a rotating mechanism, a rotating platform, and a rotating machine Taiwan, revolution machine, self-rotation transfer machine, planetary rotary machine, agitated rotary machine or rotor rotary machine. The porous dispersion structure 32 may be a microporous dispersion structure, a porous (or microporous) dispersion network, a porous (or microporous) dispersion layer, a porous (or microporous) dispersion plate, or the like. The dispersion holes 322 may be openings or holes, and the shape of each of the dispersion holes 322 may be square, rectangular, circular, trapezoidal or triangular. The slurry in the container 31 and the porous dispersion structure 32 may be one or more, and the slurry may be a living material, carbon black, a solute, a metal slurry, a ceramic slurry, a carbon slurry, a carbon dispersion or a slurry. A dispersion or the like, for example, a slurry 4a (such as a living matter) having a plurality of particles 41a in Fig. 6B, or a slurry 4b (e.g., carbon black) having a plurality of particles 41b. However, this disclosure is not limited to this.

As shown in FIGS. 1A and 1B, the rotating device 2 can have a first rotating module 21. The container 31 is connected to the first rotating module 21 or disposed on the first rotating module 21, and the first rotating module 21 can rotate the container 31, the porous dispersion structure 32 and the same according to the rotation direction D1 (such as the counterclockwise direction). The slurry is such that the container 31, the porous dispersion structure 32, and the slurry therein are centrifugally generated to disperse the slurry.

The rotating device 2 can also have a second rotating module 22. The first rotating module 21 is connected to the second rotating module 22 or disposed on the second rotating module 22, and the second rotating module 22 can rotate the first rotating module 21 according to the revolution direction D2 (such as a clockwise direction). The container 31, the porous dispersion structure 32, and the slurry therein are such that the first rotating module 21, the container 31, the porous dispersion structure 32, and the slurry therein are subjected to centrifugal force and gravity to disperse the slurry. The aforementioned revolution direction D2 may be opposite or the same as the rotation direction D1.

The porous dispersion structure 32 can be a body 326 and a skeleton 327 The skeleton 327 supports the body 326, and the body 326 and the skeleton 327 are fixed to each other or may be separated from each other.

As shown in Fig. 1A, the container 31 and the porous dispersion structure 32 may not have the inclination angle θ as shown in Fig. 1B. Alternatively, as shown in FIG. 1B, both the container 31 and the porous dispersion structure 32 may have an inclination angle θ of 30 to 60 degrees, thereby providing a three-dimensional force of gravity to enhance the slurry dispersion system 1 and slurry dispersion. The effectiveness of the device 3 to disperse the slurry. The inclination angle θ may be 30, 40, 45, 50 or 60 degrees, but is not limited thereto.

As shown in FIGS. 1A to 3B, the porous dispersion structure 32 may have a plurality of spoilers 323. A plurality of spoilers 323 are formed at the plurality of dispersion holes 322, respectively, and are located inside the inner 324 of the porous dispersion structure 32 (body 326), or the inner side 324 plus the outer side 325. The spoiler 323 may be a baffle or a fin or the like, and the dimension of the spoiler 323 may be two-dimensional (planar) or three-dimensional (stereo).

As shown in FIGS. 1A to 3B, the plurality of spoilers 323 of the porous dispersion structure 32 may face the flow direction D3 of the plurality of particles of the slurry (see the slurry 4a or the slurry 4b of FIG. 6B), and The plurality of spoilers 323 can provide a shear force to the flow of the plurality of particles of the slurry, so that the flow of the plurality of particles of the slurry produces the reflux F1 and the turbulent flow F2, and the plurality of particles of the slurry Continuously repetitively circulating or circulating between the first accommodating space 311 of the container 31, the plurality of dispersion holes 322 of the porous dispersion structure 32, and the second accommodating space 321, thereby dispersing a plurality of particles of the slurry and homogenizing the slurry. The particle size of the plurality of particles.

4A and 4B are schematic views of the dispersion hole 322 having different opening ratios in the porous dispersion structure 32 of the slurry dispersion system 1 and the slurry dispersing device 3 of FIGS. 1A to 2, wherein Opening ratio is equal to The area of the discrete holes 322 is divided by the area of the body 326.

As shown in FIG. 4A, the opening ratio of the plurality of dispersion holes 322 may be greater than or equal to 50%, such as 50%, 60%, 70%, or 80%. Alternatively, as shown in FIG. 4B, the opening ratio of the plurality of dispersion holes 322 may be less than 50%, such as 40%, 30%, or 20%. Accordingly, the present disclosure can adjust the opening ratio of the plurality of dispersion holes 322 according to actual needs to preferably disperse a plurality of particles of the slurry or to homogenize the particle diameters of the plurality of particles.

FIG. 5A is a schematic view showing the pore diameter L of the dispersion hole 322 in the porous dispersion structure 32 of the slurry dispersion system 1 and the slurry dispersing device 3 of FIGS. 1A to 2 . Fig. 5B is a view showing the particle diameters of the single particles 41a (41b) and the aggregated particles in the two different slurries 4a and 4b, wherein the aggregated particles are obtained by agglomerating at least two particles 41a (41b).

As shown in Fig. 5A, the pore diameter L of the single dispersion hole 322 of the porous dispersion structure 32 may be, for example, about 300 μm (micrometer). As shown in Fig. 5B, the primary particle diameter L1 of the single particle 41a of the slurry 4a (e.g., living matter) may be, for example, about 10 μm (micrometer), and the aggregated particle diameter L2 of the aggregated particle of the slurry 4a may be, for example, about 30 μm. (micron). While the primary particle diameter L3 of the single particle 41b of the slurry 4b (e.g., carbon black) may be, for example, about 0.1 μm (micrometer), and the aggregated particle diameter L4 of the aggregated particle of the slurry 4b may be, for example, about 0.3 μm (micrometer).

Therefore, the pore diameter L of the single dispersion hole 322 in the porous dispersion structure 32 of the present disclosure may be larger than the primary particle diameter L1 (L3) of the single particle 41a (41b) of the slurry 4a (4b), and larger than the slurry 4a (4b). The aggregated particle size L2 (L4) of the aggregated particles is supplied to the single particles 41a (41b) of the slurry 4a (4b) and the aggregated particles. The pores 322 pass through the porous dispersion structure 32.

Fig. 6A is a view showing the result of dispersing the slurry 4a (4b) without using the porous dispersion structure 32 of the present disclosure. Fig. 6B is a view showing the result of dispersing the slurry 4a (4b) using the porous dispersion structure 32 of the present disclosure.

As shown in FIG. 6A, when the slurry 4a (4b) is dispersed without using the porous dispersion structure 32 of the present disclosure, the single particles 41a (41b) of the slurry 4a (4b) and the aggregated particles are easily aggregated and settled in the container 31. At the bottom, a dead zone R is generated at the corner of the container 31 to disperse the single particles 41a (41b) of the partial slurry 4a (4b) and the aggregated particles. On the other hand, as shown in Fig. 6B, when the porous dispersion structure 32 of the present disclosure is used to disperse the slurry 4a (4b), the porous dispersion structure 32 can eliminate the dead zone R as in Fig. 6A and disperse the slurry more uniformly. The single particles 41a (41b) of the material 4a (4b) are aggregated with the particles throughout the container 31.

Figure 7 is a graph comparing the results of the use of the porous dispersion structure 32 of the present disclosure and the use of the porous dispersion structure 32 of the present disclosure to disperse the slurry. As shown by the strip H1 and the strip H2 in Fig. 7, this example is the experimental result of the slurry 4b (such as carbon black) of Fig. 5B, and the strength of the slurry 4b (unit is au, that is, no The relationship between the limited unit and the particle size (in nm) is taken as an example.

When the porous dispersion structure 32 of the present disclosure is used to disperse the slurry 4b, the aggregated particles of the slurry 4b have a broader particle size distribution and are more unevenly distributed in the range of about 80 to 1000 nm (nano), and have a slurry. The particle size of the larger aggregated particles of the material 4b (see strip H1) is distributed in the range M1 of 300 to 1000 nm (nano). On the contrary, when the porous dispersion structure 32 of the present disclosure is used to disperse the slurry 4b (such as carbon black), the aggregated particles of the slurry 4b have a narrow particle size distribution and are more evenly distributed at about 80 to 300 nm (nano). Range and slurry The particle size of the smaller aggregated particles of 4b (see strip H2) is distributed over the range M2 of 70 to 90 nm (nano). Therefore, when the porous dispersion structure 32 of the present disclosure is used, the porous dispersion structure 32 can eliminate the aggregated particles having a larger particle diameter, and reduce the particle diameter of the aggregated particles of the slurry 4b, and can also uniformly disperse the slurry 4b. Aggregated particles.

Further, as shown by the curve S1 and the curve S2 in Fig. 7, the present embodiment is an experimental result of the slurry 4b (e.g., carbon black) of Fig. 5B, and the cumulative percentage of the particles 41b of the slurry 4b (in units %) is related to the relationship of the particle diameter (in nm).

When the slurry 4b is dispersed without using the porous dispersion structure 32 disclosed herein, on the curve S1, the particle diameter of the aggregated particles of the slurry 4b is distributed from 80 nm (nano), and the point A1 from the position of the curve S1 can be It is seen that the cumulative percentage of aggregated particles having a particle size of less than 100 nm (nano) is only about 28%. On the other hand, when the porous dispersion structure 32 of the present disclosure is used to disperse the slurry 4b (such as carbon black), on the curve S2, the particle diameter of the aggregated particles of the slurry 4b is distributed from 60 nm (nano), and As can be seen from the position A2 of the curve S2, the cumulative percentage of aggregated particles having a particle diameter of 100 nm (nano) or less is about 68%. Therefore, when the porous dispersion structure 32 of the present disclosure is used, the particle size of the aggregated particles of the slurry 4b is mostly distributed below 100 nm (nano), so that the porous dispersion structure 32 can disperse and homogenize the aggregated particles of the slurry 4b. Particle size.

Figure 8 is a graph comparing another result of the use of the porous dispersion structure 32 of the present disclosure and the use of the porous dispersion structure 32 of the present disclosure to disperse the slurry. As shown, this embodiment is a plurality of discrete pores 322 in the porous dispersion structure 32. The experimental results of the slurry 4b (e.g., carbon black) of Fig. 5B under the condition that the plurality of spoilers 323 have a shear force of 100 (1/sec).

When the slurry 4b is dispersed without using the porous dispersion structure 32 of the present disclosure, the viscosity of the slurry 4b is higher than 48 cPs (centipoise) on the curve S3, for example, at the point of initial time B1, 1 month. The position of the time point B2 and the position of the 2 month rest time point B3 are 48, 64 and 86 cPs (centipoise), respectively, and the viscosity (86cPs) phase of the slurry 4b after 2 months of standing time. The viscosity of the slurry 4b (48 cPs) was approximately 2 times higher than the initial time. On the other hand, when the porous dispersion structure 32 of the present disclosure is used to disperse the slurry 4b, the viscosity of the slurry 4b is lower than 27 cPs (centipoise) on the curve S4, for example, at the initial time point C1, 1 month. The viscosity at the position C2 of the rest time and the position C3 of the 2 month rest time are 25, 22 and 27 cPs (centipoise), respectively, and the viscosity of the slurry 4b after 2 months of standing time (25 cPs) There is almost no variation in the viscosity (27 cPs) of the slurry 4b compared to the initial time. Therefore, when the porous dispersion structure 32 of the present disclosure is used, the porous dispersion structure 32 can lower the viscosity of the slurry 4b, and the slurry 4b hardly mutates after standing for a while.

It can be seen from the above that in the slurry dispersion system and the slurry dispersion device of the present disclosure, the plurality of particles of the slurry pass through the porous dispersion structure mainly by rotating the container, the porous dispersion structure and the slurry therein. The plurality of dispersed pores circulate or flow between the container and the accommodating space of the porous dispersion structure, thereby achieving the effect of more uniformly dispersing the plurality of particles of the slurry.

At the same time, the slurry dispersion system and the slurry dispersion device of the present disclosure are simple in structure and simple in operation. The container and the porous dispersion structure of the present disclosure may have The angle of inclination, thereby providing a three-dimensional force of gravity, thereby enhancing the effectiveness of the slurry dispersion system and the slurry dispersion device to disperse the slurry. Moreover, the plurality of spoilers of the porous dispersion structure of the present disclosure can provide high shear forces to disperse a plurality of particles of the slurry and to homogenize the particle size of the plurality of particles of the slurry.

In addition, the slurry dispersing system and the slurry dispersing device of the present disclosure can eliminate the dead zone to uniformly disperse the single particles and the aggregated particles of the slurry in the entire container, and can eliminate the aggregated particles having a larger particle size. The particle size of the aggregated particles of the slurry is reduced. Moreover, the slurry dispersing system and the slurry dispersing device of the present disclosure can reduce the viscosity of the slurry, and can also make the slurry hardly mutate after standing for a period of time, thereby improving the stability of the slurry and the stability of long-term storage.

The above-described embodiments are merely illustrative of the principles, features, and functions of the present disclosure, and are not intended to limit the scope of the present disclosure. Any person skilled in the art can practice the above without departing from the spirit and scope of the disclosure. The embodiment is modified and changed. Any equivalent changes and modifications made by the disclosure of this disclosure should still be covered by the scope of the patent application. Therefore, the scope of protection of this disclosure should be as set forth in the scope of the patent application.

1‧‧‧Slurry Dispersion System

2‧‧‧Rotating device

21‧‧‧First rotating module

22‧‧‧Second Rotary Module

3‧‧‧Slurry dispersing device

31‧‧‧ Container

311‧‧‧First accommodation space

32‧‧‧Porously dispersed structure

321‧‧‧Second accommodating space

322‧‧‧Distributed holes

323‧‧‧ spoiler

324‧‧‧ inside

325‧‧‧ outside

326‧‧‧Ontology

327‧‧‧ skeleton

D1‧‧‧Rotation direction

D2‧‧‧Right direction

F1‧‧‧Reflow

F2‧‧‧ turbulence

Θ‧‧‧ tilt angle

Claims (21)

A slurry dispersion system comprising: a rotating device; and a slurry dispersing device comprising: a container connected to the rotating device or disposed on the rotating device, the container having a first receiving space; and a a porous dispersion structure, which is disposed in a first accommodating space of the container, the porous dispersion structure has a second accommodating space and a plurality of dispersion holes, and the first accommodating space or the porous dispersion structure of the container The second accommodating space accommodates a slurry having a plurality of particles, wherein the container, the porous dispersion structure and the slurry therein are rotated by the rotating device to pass a plurality of particles of the slurry through the porous dispersion A plurality of dispersed pores of the structure circulate or flow between the first accommodating space of the container and the second accommodating space of the porous dispersion structure, thereby dispersing a plurality of particles of the slurry. The slurry dispersion system according to claim 1, wherein the rotating device is a rotating mechanism, a rotating platform, a rotating machine, a revolution machine, a rotation and a revolution machine, a planetary rotary machine, and a stirring rotation. Machine or rotor type rotating machine. The slurry dispersing system of claim 1, wherein the rotating device has a first rotating module, the container is connected to the first rotating module or disposed on the first rotating module, and the The first rotating module rotates the container, the porous dispersion structure and the rotating body according to the rotation direction The slurry inside. The slurry dispersing system of claim 3, wherein the rotating device further has a second rotating module, the first rotating module is connected to the second rotating module or disposed on the second rotating die And the second rotating module rotates the first rotating module, the container, the porous dispersion structure and the slurry therein according to the revolution direction. The slurry dispersion system of claim 1, wherein the container and the porous dispersion structure each have an inclination angle of 30 to 60 degrees. The slurry dispersion system according to claim 1, wherein the porous dispersion structure is a porous dispersion network, a porous dispersion layer or a porous dispersion plate. The slurry dispersion system of claim 1, wherein the porous dispersion structure is a body and a skeleton, the skeleton supports the body, and the body and the skeleton are fixed to each other or can be separated from each other. The slurry dispersion system of claim 1, wherein the porous dispersion structure further has a plurality of spoiler plates respectively formed at the plurality of dispersion holes and located at least inside the porous dispersion structure, and The dimensions of each of the spoilers are two-dimensional or three-dimensional. The slurry dispersion system of claim 8, wherein the plurality of spoilers of the porous dispersion structure face a flow direction of the plurality of particles of the slurry, and the plurality of spoilers provide shearing force The particle size of the plurality of particles of the slurry is homogenized by causing the flow of the plurality of particles of the slurry to cause reflux and turbulence. The slurry dispersion system according to claim 1, wherein each of the dispersion holes of the porous dispersion structure has a square shape, a rectangular shape, a circular shape, a trapezoidal shape or a triangular shape. The slurry dispersion system according to claim 1, wherein the plurality of dispersion holes of the porous dispersion structure have an opening ratio of more than 50% or less than 50%. The slurry dispersion system of claim 1, wherein the pore size of the single dispersion pore of the porous dispersion structure is larger than the primary particle diameter of the single particle of the slurry, and is larger than the formation of at least two particles of the slurry. The aggregated particle size of the aggregated particles is such that the single particles and aggregated particles of the slurry pass through the dispersed pores of the porous dispersed structure. A slurry dispersing device comprising: a container having a first accommodating space; and a porous dispersing structure housed in the first accommodating space of the container, the porous dispersing structure having a second volume a space and a plurality of dispersion holes, and the first accommodation space of the container or the second accommodation space of the porous dispersion structure accommodates a slurry having a plurality of particles, wherein by rotating the container, the porous dispersion structure and The slurry therein, wherein a plurality of particles of the slurry pass through a plurality of dispersion holes of the porous dispersion structure to circulate or flow in a first accommodation space of the container and a second accommodation of the porous dispersion structure Between the spaces, a plurality of particles of the slurry are further dispersed. The slurry dispersing device of claim 13, wherein the container and the porous dispersion structure each have a slope of 30 to 60 degrees. angle. The slurry dispersing device according to claim 13, wherein the porous dispersion structure is a porous dispersion network, a porous dispersion layer or a porous dispersion plate. The slurry dispersion device of claim 13, wherein the porous dispersion structure is a body and a skeleton, the skeleton supports the body, and the body and the skeleton are fixed to each other or can be separated from each other. The slurry dispersion device of claim 13, wherein the porous dispersion structure further has a plurality of spoiler plates respectively formed at the plurality of dispersion holes and located at least inside the porous dispersion structure, and The dimensions of each of the spoilers are two-dimensional or three-dimensional. The slurry dispersing device of claim 17, wherein the plurality of spoilers of the porous dispersion structure face a flow direction of the plurality of particles of the slurry, and the plurality of spoilers provide shearing force The particle size of the plurality of particles of the slurry is homogenized by causing the flow of the plurality of particles of the slurry to cause reflux and turbulence. The slurry dispersing device according to claim 13, wherein each of the dispersed pores of the porous dispersion structure has a square shape, a rectangular shape, a circular shape, a trapezoidal shape or a triangular shape. The slurry dispersing device according to claim 13, wherein the plurality of dispersion holes of the porous dispersion structure have an opening ratio of more than 50% or less than 50%. The slurry dispersing device according to claim 13, wherein a pore diameter of the single dispersed pore of the porous dispersed structure is larger than a single of the slurry The primary particle size of a particle is greater than the aggregate particle size of the aggregated particles formed by at least two particles of the slurry, such that the single particle and the aggregated particle of the slurry pass through the dispersed pore of the porous dispersion structure.