Patent Application
20250099971
This application claims the benefit of priority under 35 U.S.C. § 119 (e) from Korean Patent Application No. 10-2023-0127699, filed on Sep. 25, 2023, which is hereby incorporated by reference as if set forth in its entirety herein.
The present disclosure relates to a jet mill capable of removing static electricity and a method of pulverizing a sulfide-based solid electrolyte using the same, and more specifically, to a jet mill capable of removing static electricity and a method of pulverizing a sulfide-based solid electrolyte using the same, which facilitates particle size control and increases pulverizing efficiency by removing static electricity inside a milling main body where pulverizing is performed.
Recently, secondary batteries have become common in electronic devices such as smartphones.
A secondary battery uses lithium as a cathode, is charged by lithium ions moving from the cathode to an anode, and is discharged while lithium moves from the anode to the cathode to generate power.
These lithium secondary batteries have the advantages of high energy density and long lifespan, and are generally used in various types of electronic devices, and recently, demand has been increasing due to rapid growth of an electric vehicle market.
However, since these lithium secondary batteries use organic solvents as electrolytes for ion movement, accidents may occur due to electrolyte leakage or volatilization, which presents safety issues.
The solid electrolytes that are being developed recently are a technology that aims to replace existing liquid electrolytes by using solid sulfide compounds, and since only lithium ions move inside the electrolyte, there are no side reactions and they have the advantages of excellent safety and durability.
Among the solid electrolytes used in lithium secondary batteries, the compound represented by Li7-XPS6-xClx has a cubic argyrodite crystal structure and is attracting attention as a mass-produced sulfide-based solid electrolyte due to high ionic conductivity and electrochemical stability over a wide temperature range.
These solid electrolytes are manufactured into particles of a certain size through a milling process after their synthesis is complete.
A milling process for existing solid electrolytes has generally used a ball mill, but in the case of this ball mill, not only does it require several tens of hours of processing time to manufacture particles of less than 10 μm required for solid electrolyte particles, but it also has problems such as the formation of carbon compounds due to solvent reaction and the resulting decrease in electrical conductivity.
Accordingly, recently, a method of dry-pulverizing particles using a jet mill has been mainly used to control the particle size of solid electrolytes.
As illustrated in
The jet mill configured in this manner pulverizes raw material through a process as illustrated in
That is, a) a raw material is fed into the hollow milling main body 20 through a predetermined raw material supply pipe 12 from the raw material supply unit 10, b) when the raw material fed into the milling main body 20 is filled to a certain height or higher, the raw materials are pulverized by collision with each other due to a strong jet air sprayed from an air nozzle 24a installed in a lower portion of the milling main body 20, c) the pulverized raw material particles are raised due to an air current, and particles having a particle size equal to or less than a certain size pass through a classifying wheel 26a, and particles having a particle size equal to or more than the certain size descend back to the lower portion of the milling main body 20 along an inner wall of the milling main body 20, and d) the particles that pass through the classifying wheel 26a move to a product collection unit.
Here, an unexplained symbol 28 is a first product transfer pipe (connecting the classifying wheel 26a and the cyclone 30), and symbol 32 is a second product transfer pipe (connecting the cyclone 30 and the bag filter 40).
In this way, the conventional jet mill can obtain particles of a desired size by injecting high-pressure air through the air nozzle 24a to cause mutual collision between pulverized particles.
The jet mill is mainly used when pulverizing sulfide-based solid electrolyte (LPSC1) and is useful for controlling the desired particle size with only air.
However, the pulverization using the conventional jet mill may generate static electricity inside the milling main body 20, and there is a problem that the particles are clumped together due to a ductile nature of the solid electrolyte and stick to the inner wall of the milling main body 20.
Accordingly, there is a problem that it is difficult to control the particle size when pulverizing the solid electrolyte, and the pulverization efficiency is reduced.
The present disclosure is intended to solve the above-mentioned various problems of the prior art, and a purpose thereof is to provide a jet mill capable of removing static electricity, which can facilitate particle size control and increase pulverizing efficiency by removing static electricity inside a milling main body where pulverization is performed, and a sulfide-based solid electrolyte pulverizing method using the same.
In order to achieve the above-described objects, according to a first aspect of the present disclosure, there is provided a jet mill in which a raw material is fed into a hollow milling main body through a predetermined raw material supply pipe from a raw material supply unit and the raw materials are pulverized by collision with each other due to a strong jet air sprayed from an air nozzle installed in the milling main body when the raw materials fed into the milling main body fill the the milling main body to a certain height or higher, in which upper and lower portions of the milling main body are grounded to remove static electricity inside the milling main body.
A recessed lower plate may be horizontally positioned on a lower side inside the milling main body, a plurality of air nozzles may be installed spaced apart along an edge of the lower plate, and the air nozzles may be arranged to face a center of the lower plate.
The lower plate may be formed of ceramic.
A cover may be installed on an open upper end of the milling main body, and a classifying wheel may be provided inside the cover.
An upper plate may be horizontally arranged on an inner upper portion of the milling main body, one or more raw material input holes may be formed vertically through the upper plate along a circumferential direction, and the raw materials supplied from the raw material supply pipe may be fed into the raw material input holes.
The upper plate may be formed of ceramic.
A predetermined ionizer may be installed in the raw material supply pipe to supply the raw material to the raw material input holes of the upper plate and supply ionized air together, thereby preventing raw materials from accumulating on the upper plate.
According to a second aspect of the present disclosure, there is provided a method of pulverizing a sulfide-based solid electrolyte using a jet mill in which a sulfide-based solid electrolyte is fed into a hollow milling main body through a predetermined raw material supply pipe from a raw material supply unit and the sulfide-based solid electrolytes are pulverized by collision with each other due to a strong jet air sprayed from an air nozzle installed in an inner lower portion of the milling main body when the sulfide-based solid electrolyte fed into the milling main body fill the milling main body to a certain height or higher, the method includes removing static electricity inside the milling main body by grounding upper and lower portions of the milling main body.
The method may further include installing a predetermined ionizer in the raw material supply pipe to supply the sulfide-based solid electrolyte inside the milling main body and supply ionized air together.
Specific details of other embodiments are included in the “DETAILED DESCRIPTION” and the attached “DRAWINGS”.
The advantages and/or features of the present disclosure and the methods for achieving them will become clear with reference to the various embodiments described in detail below together with the attached drawings.
However, the present disclosure is not limited to the configuration of each embodiment disclosed below and may also be implemented in various different forms, and it should be noted that each embodiment disclosed in the present specification is provided only to ensure that the disclosure of the present disclosure is complete and to fully inform a person having ordinary skill in the art to which the present disclosure belongs of the scope of the present disclosure, and the present disclosure is defined only by the scope of each claim of the claims.
According to the means for solving the above-described problem, the present disclosure has the following effects.
The present disclosure has the effect of preventing agglomeration of raw material particles such as sulfide-based solid electrolytes and preventing the raw material particles from sticking to an inner wall of the milling main body by grounding the upper and lower portions of the milling main body and removing the static electricity inside the milling main body.
Accordingly, the static electricity inside the milling main body where pulverization is performed can be removed, facilitating particle size control.
In addition, the present disclosure has the effect of increasing pulverization efficiency and productivity by installing a predetermined ionizer in the raw material supply pipe to supply raw material to the raw material input hole of the upper plate located inside the milling main body and simultaneously supplying the ionized air together, thereby preventing raw material such as sulfide-based solid electrolytes from accumulating on the upper plate due to static electricity.
Hereinafter, a preferred embodiment of a jet mill capable of removing static electricity according to the present disclosure and a method of pulverizing a sulfide-based solid electrolyte using the same will be described in detail with reference to the attached drawings. For reference, the terms and words used in this specification and claims should not be interpreted as limited to their usual or dictionary meanings, and should be interpreted as meanings and concepts that conform to the technical idea of the present disclosure based on the principle that the inventor can appropriately define the concept of the term in order to explain his or her own invention in the best possible way. In addition, the embodiments described in this specification and the configurations illustrated in the drawings are only the most preferred embodiments of the present disclosure and do not represent all of the technical ideas of the present disclosure, so it should be understood that there may be various equivalents and modified examples that can replace them at the time of filing this application.
The jet mill capable of removing static electricity according to the present disclosure is configured such that raw materials are fed into a hollow milling main body 20 through a predetermined raw material supply pipe 12 from a raw material supply unit, and when the raw materials fed into the milling main body 20 fill the milling main body 20 to a certain height or higher, the raw materials are pulverized by collision with each other due to a strong jet air sprayed from an air nozzle 24a installed at a lower portion of the milling main body 20.
In this case, the raw material may be a sulfide-based solid electrolyte.
Such a sulfide-based solid electrolyte is a type of inorganic solid electrolyte.
The inorganic solid electrolytes are generally classified into oxide-based and sulfide-based.
The sulfide-based solid electrolyte is widely studied as a promising material in the field of next-generation all-solid-state battery development, and has the advantages of high ionic conductivity, low mechanical deformability, and low weight density, similar to a liquid electrolyte.
When raw materials such as sulfide-based solid electrolytes are fed into the milling main body 20, static electricity may be generated, and due to ductile nature of the solid electrolytes, agglomeration occurs between particles and the particles stick to the inner wall of the milling main body 20.
Accordingly, an objective of the present disclosure is to facilitate particle size control and increase pulverization efficiency by grounding the upper and lower portions of the milling main body 20 to remove the static electricity inside the milling main body 20.
The milling main body 20 is formed in a hollow cylindrical shape, and one end of the raw material supply pipe 12 is connected to one side of the milling main body 20 so as to communicate with the inside of the milling main body 20.
In addition, an upper plate 22 is horizontally arranged on the inner upper portion of the milling main body 20, a lower plate 24 is horizontally arranged on the inner lower side of the milling main body 20, and a cover 26 is arranged on the open upper end of the milling main body 20 to seal the upper portion of the milling main body 20.
In addition, a predetermined ionizer 14 is installed in the raw material supply pipe 12 to supply raw material to the raw material input hole of the upper plate 22 arranged in the inner upper portion of the milling main body 20 and supply ionized air together, thereby preventing raw material clumped between particles by static electricity from accumulating on the upper portion of the upper plate 22.
The upper plate 22 is horizontally arranged on the inner upper portion of the milling main body 20.
In this case, the outer surface of the upper plate 22 is formed in a shape corresponding to the inner surface of the milling main body 20, so that when the upper plate 22 is placed inside the milling main body 20, an airtight state can be maintained between the outer surface of the upper plate 22 and the inner surface of the milling main body 20.
For example, the upper plate 22 can be formed in a disk shape, and the inner surface of the milling main body 20 can be formed in a cylindrical shape.
In such an upper plate 22, one or more raw material input holes 22a are formed to penetrate upward and downward along the circumferential direction, and the raw material supplied from the raw material supply pipe 12 is fed into the raw material input hole 22a and fills the milling main body 20 to a certain height.
When the raw material fills the milling main body 20 to a certain height or more, the raw materials are pulverized by collision with each other due to the strong jet air sprayed from the air nozzle 24a.
This upper plate 22 may be formed of ceramic.
The lower plate 24 having a recessed shape (a shape that slopes downward from an edge to the inside) is horizontally positioned at the lower side inside the milling main body 20.
The plurality of air nozzles 24a are installed radially spaced apart along the edge of the lower plate 24, and the air outlets of the air nozzles 24a may be arranged to face the center of the lower plate 24.
The raw material input into the milling main body 20 through the raw material input hole 22a formed in the upper plate 22 descends to the lower plate 24 and fills the inside of the milling main body (20) to a certain height. When the raw material is filled to a certain height or higher, the raw material particles are pulverized due to the strong jet air sprayed from the air nozzle 24a.
In this case, the lower plate 24 may be formed of ceramic.
The cover 26 is installed on the open upper end of the milling main body 20 to seal the upper portion of the milling main body 20.
The classifying wheel 26a may be provided on the inner side (the side facing the inside of the milling main body 20 when the cover 26 seals the milling main body 20) of the cover 26.
The raw material particles pulverized by the strong jet air sprayed from the air nozzle 24a inside the milling main body 20 are raised by the air current, and when the particle size is smaller than a certain size, the raw material particles pass through the classifying wheel 26a and then move to the product collecting section.
In addition, when the raw material particles are larger than a certain size, the raw material particles descend to the inside of the milling main body 20 again along the inner wall surface of the milling main body 20 and are pulverized by the jet air.
The ionizer 14 installed in the raw material supply pipe 12 removes static electricity of the supplied air. That is, the ionizer 14 prevents agglomeration of the raw material particles caused by static electricity of the raw material fed into the milling main body 20 and prevents the raw material particles from blocking the raw material input hole 22a of the upper plate 22, thereby preventing such clumped particles from accumulating on the upper plate 22.
When ionized air is supplied by the ionizer 14, the accumulation of raw material on the upper part of the upper plate 22 can be improved, and as illustrated in the upper end photograph (Example) on the right side of
The upper end photograph (Comparative Example) on the left side of
When the raw material is not accumulated on the upper portion of the upper plate 22, the raw material pulverized at the lower portion of the milling main body 20 can smoothly move (be classified) through the classifying wheel 26a located at the upper portion along the rising air current, thereby increasing the pulverization efficiency and productivity.
In addition, as illustrated in the Particle Size Analyzer (PSA) results described at the bottom of
The present disclosure described above is not limited to the aforementioned examples and the attached drawings, and it will be apparent to those skilled in the art that various substitutions, modifications, and changes are possible within the scope that does not depart from the technical idea of the present disclosure.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10-2023-0127699 | Sep 2023 | KR | national |
