METHOD AND APPARATUS FOR DEPOSITING AMORPHOUS SILICON FILM
20170256410 ยท 2017-09-07
Assignee
Inventors
- Seung-Woo Shin (Hwaseong-si, KR)
- Hai-Won Kim (Icheon-si, KR)
- Woo-Duck Jung (Suwon-si, KR)
- Sung-Kil Cho (Yongin-si, KR)
- Wan-Suk Oh (Icheon-si, KR)
- Ho-Min Choi (Yongin-si, KR)
- Koon-Woo Lee (Yongin-si, KR)
Cpc classification
H01L21/32055
ELECTRICITY
H01L21/28525
ELECTRICITY
C23C16/4405
CHEMISTRY; METALLURGY
H01L21/28556
ELECTRICITY
H01L21/76877
ELECTRICITY
International classification
H01L21/3205
ELECTRICITY
H01L21/02
ELECTRICITY
C23C16/455
CHEMISTRY; METALLURGY
Abstract
Provided is a method and apparatus for depositing an amorphous silicon film. The method includes supplying a source gas and an atmospheric gas onto a substrate in a state where the substrate is loaded in a chamber to deposit the amorphous silicon film on the substrate. The atmospheric gas includes at least one of hydrogen and helium. The source gas includes at least one of silane (SiH.sub.2), disilane (Si.sub.2H.sub.6), and dichlorosilane (SiCl.sub.2H.sub.2).
Claims
1. A method for depositing an amorphous silicon film, the method comprising: supplying a source gas and an atmospheric gas onto a substrate in a state where the substrate is loaded in a chamber; and depositing the amorphous silicon film on the substrate at a process temperature under a process pressure, wherein the source gas comprises at least one of silane (SiH.sub.2), disilane (Si.sub.2H.sub.6), and dichlorosilane (SiCl.sub.2H.sub.2), wherein the process temperature is adjusted to be in a range of about 540 C. to about 580 C. and the process pressure is adjusted to be in a range of about 8 Torr to about 300 Torr, so that the source gas is pyrolyzed to deposit the amorphous silicon film on the substrate, and wherein the atmospheric gas comprises at least one of hydrogen and helium.
2. The method of claim 1, wherein the source gas has a flow rate of about 0.5 sccm to about 300 sccm, and the atmospheric gas has a flow rate of about 100 sccm to about 25000 sccm.
3. The method of claim 1, wherein the amorphous silicon film is deposited to have a thickness of about 1000 or more.
4. The method of claim 3, wherein the amorphous silicon film is deposited to have a surface roughness of about 1 nm or less.
5. The method of claim 1, wherein the substrate is placed on a heater, and the substrate is heated by the heater to the process temperature.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0014] The accompanying drawings are included to provide a further understanding of the present invention, and are incorporated in and constitute a part of this specification. The drawings illustrate exemplary embodiments of the present invention and, together with the description, serve to explain principles of the present invention. In the drawings:
[0015]
[0016]
[0017]
[0018]
[0019]
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0020] Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to
[0021] Hereinafter, the term amorphous silicon does not merely represent only the amorphous silicon. For example, the amorphous silicon includes amorphous silicon, nano-crystalline silicon formed by combining crystal grains each of which has an amorphous nano size to achieve precision in surface roughness that will be described below, and silicon in which the amorphous silicon is mixed with the nano-crystalline silicon.
[0022]
[0023] Referring to
[0024] Also, a first flow controller 18b and a first valve 18c are disposed in the first supply line 18a, and a second flow controller 19b and a second valve 19c are disposed in the second supply line 19a. Here, the gas introduced through the introduction unit 12 may be injected into the chamber 11 through a showerhead 13 disposed in the chamber 11.
[0025] Also, a wafer 15 that is a target object to be deposited may be placed on a heater 14. The heater 14 may heat the wafer 15 to a process temperature in a state where the heater 14 is supported by a heater support 16. When the deposition is completed, a non-reaction gas and by-products within the chamber 11 may be exhausted through a vacuum port 17. An exhaust line 17a and a vacuum pump 17b may be connected to the vacuum port 17 to forcibly exhaust the non-reaction gas and the by-products within the chamber 11. Also, a process pressure within the chamber 11 may be adjusted by using the exhaust line 17a and the vacuum pump 17b.
[0026] According to the above-described method, the source gas and the atmospheric gas may be supplied onto the wafer 15 within the chamber 11. Then, an amorphous silicon film may be deposited on the wafer 15 using a source gas pyrolyzed by the heater 14. Here, a control unit 20 may control the heater 14 for adjusting the process temperature, the vacuum pump 17b for adjusting the process pressure, and the first and second flow controllers 18b and 19b for respectively adjusting supply flow rates of the source gas and the atmospheric gas. The controller 20 may adjust the process temperature in the chamber 11 to a temperature of about 200 C. to about 800 C. and the process pressure in the chamber 11 to a pressure of about 1 Torr to about 200 Torr. Also, the control unit 20 may adjust the supply flow rate of the source gas to a flow rate of about 0.5 sccm to about 300 sccm and the supply flow rate of the atmospheric gas to a flow rate of about 100 sccm to about 25,000 sccm.
[0027] As described above, the wafer 15 may be loaded into the chamber 11, and then the source gas and the atmospheric gas may be supplied onto the wafer 15 at nearly the same time to deposit the amorphous silicon film on the wafer 15. The source gas may be a silane-based gas such as a silane (SiH.sub.2), disilane (Si.sub.2H.sub.6), and dichlorosilane (SiCl.sub.2H.sub.2, DCS). Also, the wafer 15 may be loaded into the chamber 11 in a state where a seed layer is formed on a top surface of the wafer 15. Here, the amorphous silicon film may be formed on the seed layer.
[0028]
[0029] Referring to
[0030] In general, in a batch type deposition apparatus, the thin film has an improved surface roughness when compared to that in a single type deposition apparatus illustrated in
[0031] Here, the surface roughness gradually increases as a thin film increases in thickness. However, as illustrated in
[0032]
[0033] Resultantly, if the helium gas is used as the atmospheric gas, when the thin film increases in thickness (for example, a thickness of about 7500 ), the increase of the surface roughness may be prevented. Also, the amorphous silicon film in the single type deposition apparatus may have the same surface roughness as that in the batch type deposition apparatus. In particular, the deposition rate at a high temperature (for example, a temperature of about 540 C. or more) may be significantly improved.
[0034]
TABLE-US-00001 TABLE 1 Atmospheric Process Disilane Atmospheric Deposition Thickness gas temperature ( C.) (sccm) gas (sccm) Pressure rate (/sec) () Nitrogen (N) 530 30 20000 30 0.7 50 Argon (Ar) 18000 0.79 Helium (He) 12000 0.72 Hydrogen (H) 8000 0.76
[0035] As a result, it was seen that, when helium (He) is supplied, the surface roughness of the amorphous silicon film was improved in comparison to that of the amorphous silicon film when nitrogen (N) and argon (Ar) are supplied. That is, when each of nitrogen (N) and argon (Ar) are supplied onto the amorphous silicon film, a surface roughness of the amorphous silicon film is greater than about 0.3 nm. However, when helium (He) is supplied, a surface roughness of the amorphous silicon film is less than about 0.3 nm. That is, it was seen that, when helium (He) is supplied, the amorphous silicon film has surface roughness improved by about 15% or more. Also, when hydrogen (H) is supplied, a surface roughness of the amorphous silicon film was improved in comparison to that when helium (He) is supplied. Also, when hydrogen (H) is supplied, the amorphous silicon film has a deposition rate of about 0.76 /sec which is greater than that of about 0.72 /sec when helium (He) is supplied.
[0036] The above-described amorphous silicon film is useful to fill a contact hole defined in an interlayer dielectric such as a silicon oxide film or a silicon nitride film or to fill a line defined in the interlayer dielectric, e.g., a groove for an inner wire. Particularly, if the amorphous silicon film has great surface roughness, a large void may be generated when the contact hole is filled with the amorphous silicon film. On the other hand, if the amorphous silicon film has low surface roughness, a small void may be generated to prevent a resistance of the amorphous silicon film filled in the contact hole from increasing.
[0037] According to the embodiments of the present invention, the surface roughness may be more improved in precision. Also, the method and apparatus according to the present invention may respond to the miniaturization of the contact hole or line.
[0038] Although the present invention is described in detail with reference to the exemplary embodiments, the invention may be embodied in many different forms. Thus, technical idea and scope of claims set forth below are not limited to the preferred embodiments.
[0039] The above-disclosed subject matter is to be considered illustrative, and not restrictive, and the appended claims are intended to cover all such modifications, enhancements, and other embodiments, which fall within the true spirit and scope of the present invention. Thus, to the maximum extent allowed by law, the scope of the present invention is to be determined by the broadest permissible interpretation of the following claims and their equivalents, and shall not be restricted or limited by the foregoing detailed description.