The present invention relates to methods for preparing silicon carbide powder and single crystal silicon carbide.
Recently, rapid technological advances are taking place in the field of semiconductors. Up until now, silicon single crystal has predominantly served as a typical semiconductor device material. However, as the silicon single crystal fails to satisfy the physical properties required in the area of recent semiconductor technologies and has come to a dead end, there is a rising demand for next-generation semiconductor materials that may replace the silicon single crystal.
In particular, semiconductor materials that may significantly reduce power loss upon power conversion are at the center of attention. Among them, silicon carbide (SiC) single crystal having a large bandgap energy (˜3.2 eV) as well as characteristics of smaller size due to high dielectric breakdown, low power loss, and high temperature stability is being highlighted as a promising next-generation semiconductor material.
To make sure that silicon carbide single crystal grows, silicon carbide powder having high purity is indispensable. However, the currently available silicon carbide powder has some limitations such as low purity, an inadequate particle size for use in single crystal growth processes even with high purity, or poor productivity. As the demand for silicon carbide single crystal surges, a process for preparing silicon carbide powder having high purity is also needed.
A task to be solved by the present invention is to provide a method for preparing silicon carbide powder having high purity. Another task to be solved by the present invention is to provide a method for preparing single crystal silicon carbide, using the silicon carbide powder.
A method for preparing silicon carbide powder according to the concept of the present invention may include: providing a precursor gas onto a fibrous carbon body in a reactor to deposit silicon carbide (SiC) on the fibrous carbon body; recovering the silicon carbide deposited on the fibrous carbon body to obtain a first silicon carbide powder; and oxidizing the first silicon carbide powder, wherein the molecules of the precursor gas may include silicon atoms and carbon atoms.
A method for preparing single crystal silicon carbide according to another concept of the present invention may include: providing a precursor gas onto a fibrous carbon body in a reactor to deposit silicon carbide on the fibrous carbon body; recovering the silicon carbide deposited on the fibrous carbon body to obtain a first silicon carbide powder; providing a silicon carbide raw material including the first silicon carbide powder into a crucible; and sublimating the silicon carbide raw material to grow single crystal silicon carbide on a seed attached to an upper portion of the crucible.
The present invention provides a method for preparing silicon carbide powder having high purity. The present invention also provides a method for preparing single crystal silicon carbide having increased purity and yield by using the silicon carbide powder. However, the benefits of the present invention are not limited thereto.
Preferred embodiments of the present invention will be described with reference to the accompanying drawings so as to sufficiently understand constitutions and effects of the present invention. However, the present invention may be embodied in different forms with various changes, but not limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the present invention to a person skilled in the art to which the invention pertains.
In this specification, it will be understood that when a component is referred to as being ‘on’ another component, it can be directly on another component, or an intervening third component may also be present. Also, in the drawings, the thicknesses of the components are exaggerated for effectively describing the technical features. Like reference numerals refer to like elements throughout.
Although terms like a first, a second, and a third are used to describe various components in various embodiments of this specification, the components should not be limited to these terms. These terms are used only to tell one element from another element. Embodiments described and exemplified herein include complementary embodiments thereof.
In this specification, the terms are used only for explaining embodiments while not limiting the present invention. In this specification, the singular forms include the plural forms as well, unless the context clearly indicates otherwise. The meaning of “comprises” and/or “comprising” used herein does not exclude the presence or addition of one or more other components besides a mentioned component.
Referring to
The reactor 100 may include an inlet IL for injecting a precursor gas PG and an outlet OL for discharging the gas after reaction. The placement of the inlet IL and the outlet OL in the reactor 100 is not particularly limited, and, for example, as shown in
As the precursor gas PG, any compound containing at least one silicon atom and at least one carbon atom may be used without particular limitation. The precursor gas PG may include a compound containing at least one silicon atom and at least one carbon atom in a molecule, and may include, for example, methyltrichlorosilane (MTS). As methyltrichlorosilane herein contains silicon atoms and carbon atoms in molecules in a ratio of 1:1, the use of methyltrichlorosilane may increase yield of silicon carbide powder.
The precursor gas may be injected into the reactor 100 through the inlet IL, and deposited on a fibrous carbon body 110 in the reactor 100. A first silicon carbide powder SIC_P1 may be obtained after recovering the silicon carbide.
As the fibrous carbon body 110, any compound containing carbon may be used without any particular limitation, and therefore, activated carbon, carbon fiber, graphite fiber, or a mixture thereof may be used. For example, the fibrous carbon body 110 may include graphite fibers. The fibrous carbon body 110 may be in the form in which several graphite fibers are entangled with each other, and may include a fiber bundle 120 protruding from a surface of the fibrous carbon body. The protruding fiber bundle 120 increases surface areas on which the precursor gas PG may be deposited, and may thus increase the yield of the first silicon carbide powder SIC_P1.
Referring back to
As shown in
The method for preparing silicon carbide powder according to an embodiment of the present invention may include oxidizing the first silicon carbide powder SIC_P1 and the second silicon carbide powder SIC_P2. When the first silicon carbide powder SIC_P1 and the second silicon carbide powder SIC_P2 are oxidized, the yield and productivity of single crystal silicon carbide preparation process may increase.
The method for preparing silicon carbide powder according to an embodiment of the present invention may further include heat-treating silicon carbide powder. When the process of heat-treating is additionally performed, impurities remaining in the silicon carbide powder may be removed to increase purity. For example, the heat-treating of silicon carbide powder may be performed in air at temperatures of 700° C. to 800° C.
Referring to
The crucible 200 may include a body that includes a material having a melting point greater than or equal to the sublimation temperature of silicon carbide. The body of the crucible 200 may include a metal or an inorganic material, and may include, for example, graphite. For example, a material having a melting point greater than or equal to the sublimation temperature of silicon carbide may be applied on a surface of the crucible 200 made of graphite. As a material applied on the surface of the crucible 200, a material that is chemically inert to silicon (Si) at a temperature where the single crystal silicon carbide SIC_C is grown may be used. A material applied on the surface of the crucible 200 may be a metal carbide or a metal nitride, and for example, carbide or nitride of tungsten (W), zirconium (Zr,) tantalum (Ta), hafnium (Hf), or niobium (Nb) may be used.
The seed 210 may provide a surface on which the sublimated silicon carbide raw material may be deposited and grown. The seed holder 220 may be attached to an inner upper side of the crucible 200 in the form that the seed 210 is attached. For example, the seed holder 220 may include high-density graphite, and may be provided with a wider cross-section than the seed 210 to make sure that the seed 210 is stably fixed onto the upper portion of the crucible. For example, as the seed 210, a 4H-SiC seed or a 6H-SiC seed may be used.
As a raw material for growing the single crystal silicon carbide SIC_C, the silicon carbide raw material SIC_P may be provided into the crucible 200. For example, the silicon carbide raw material SIC_P may include the first silicon carbide powder SIC_P1, the second silicon carbide powder SIC_P2, or a mixture thereof prepared through the method for preparing silicon carbide powder, which described above. Detailed descriptions of the first silicon carbide powder SIC_P1 and the second silicon carbide powder SIC_P2 may be substantially the same as what is previously described with reference to
When the silicon carbide raw material SIC_P includes a mixture of the first silicon carbide powder SIC_P1 and the second silicon carbide powder SIC_P2, the use of the raw material in which silicon carbide powders having different average particle sizes are mixed may control the growth rate of the single crystal silicon carbide SIC_C. For example, when the weight of the first silicon carbide powder SIC_P1 having a relatively small average particle size is greater than the weight of the second silicon carbide powder SIC_P2 having a relatively large average particle size, the growth rate of the single crystal silicon carbide SIC_C may increase. When the weight of the first silicon carbide powder SIC_P1 having a relatively small average particle size is smaller than the weight of the second silicon carbide powder SIC_P2 having a relatively large average particle size, the growth rate of the single crystal silicon carbide SIC_C may decrease. As described above, when adjusting the mixing ratio (weight ratio) between the first silicon carbide powder SIC_P1 and the second silicon carbide powder SIC_P2, the growth rate of the single crystal silicon carbide SIC_C may be controlled to a desired value.
Upon the sublimation of the silicon carbide raw material SIC_P, the temperature inside the crucible may be 1,800° C. to 2,400° C. The inside of the crucible 200 may be heated through the induction coil 230 surrounding the outside of the crucible 200. The inside of the crucible 200 may be heated when high-frequency current flows in the induction coil 230.
As shown in
Although the embodiments of the present invention are described, those with ordinary skill in the technical field to which the present invention pertains will understand that the present invention can be carried out in other specific forms without changing the technical idea or essential features. Therefore, the above-described embodiments are to be considered in all aspects as illustrative and not restrictive.
Number | Date | Country | Kind |
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10-2019-0133214 | Oct 2019 | KR | national |
Filing Document | Filing Date | Country | Kind |
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PCT/KR2020/014601 | 10/23/2020 | WO |