Substrate processing method
12628581 ยท 2026-05-12
Assignee
Inventors
- SangHeon Yong (Yongin-si, KR)
- HongSuk KIM (Yongin-si, KR)
- JuHyuk Park (Hwaseong-si, KR)
- KiHun Kim (Yongin-si, KR)
- SungHa Choi (Suwon-si, KR)
Cpc classification
International classification
Abstract
A substrate processing method comprising a gap-fill process is disclosed. The method includes providing a substrate in which a gap is formed in a surface thereof to a reaction space, supplying an oligomeric silicon precursor and a nitrogen-containing gas to the reaction space, forming a silicon nitride film having flowability on the substrate to fill at least a portion of the gap of the substrate while maintaining the reaction space in a plasma state, and densifying the silicon nitride film.
Claims
1. A method of processing a substrate, the method comprising: providing the substrate in which a gap is formed in a surface thereof to a reaction space; supplying an oligomeric silicon precursor and a nitrogen-containing gas to the reaction space; forming a silicon nitride film having flowability on the substrate to fill at least a portion of the gap of the substrate while maintaining the reaction space in a plasma state; and densifying the silicon nitride film, wherein a pressure within the reaction space is in the range of about 0.5 Torr to about 10 Torr, and wherein the silicon precursor comprises a trisilylamine (TSA) having 2 to 10 repeating units.
2. The method of processing a substrate of claim 1, wherein the oligomeric silicon precursor comprises one or more of dimer-TSA, trimer-TSA, tetramer-TSA, pentamer-TSA, hexamer-TSA, heptamer-TSA, octamer-TSA.
3. The method of processing a substrate of claim 1, wherein the nitrogen-containing gas comprises at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof.
4. The method of processing a substrate of claim 1, wherein the oligomeric silicon precursor comprises trimer-trisilylamine (TSA) and the nitrogen-containing gas comprises NH.sub.3.
5. The method of processing a substrate of claim 1, wherein, in the step of forming the silicon nitride film, a temperature of the substrate is maintained between about 0 C. and about 100 C.
6. The method of processing a substrate of claim 5, wherein, in the step of forming the silicon nitride film, the temperature of the substrate is maintained between about 30 C. and about 70 C.
7. The method of processing a substrate of claim 1, wherein, in the step of supplying the oligomeric silicon precursor and the nitrogen-containing gas, the oligomeric silicon precursor and the nitrogen-containing gas are supplied so that the ratio of the Si atoms to N atoms in the silicon nitride film is 1:1 or more.
8. The method of processing a substrate of claim 1, wherein, in the step of forming the silicon nitride film, while supplying the oligomeric silicon precursor and the nitrogen-containing gas to the reaction space, RF power is applied to the reaction space to directly generate plasma over the substrate by an in-situ plasma treatment method.
9. The method of processing a substrate of claim 1, wherein the step of densifying the silicon nitride film is performed using any one selected from plasma treatment, UV treatment, or a rapid thermal process, for the silicon nitride film.
10. The method of processing a substrate of claim 9, wherein the step of densifying the silicon nitride film is performed using plasma treatment, and the plasma treatment is performed by an in-situ plasma treatment method in which plasma is directly generated over the substrate while supplying He or Ar gas.
11. The method of processing a substrate of claim 10, wherein the steps of forming the silicon nitride film and densifying the silicon nitride film are performed at the same process temperature, and in the step of densifying the silicon nitride film, second RF power that is greater than first RF power applied to the reaction space in the step of forming the silicon nitride film is applied to the reaction space.
12. The method of processing a substrate of claim 11, wherein the first RF power is in a range of about 100 W to about 500 W, and the second RF power is in the range of about 300 W to about 1,500 W.
13. The method of processing a substrate of claim 10, wherein the steps of forming the silicon nitride film and densifying the silicon nitride film are performed under RF power of the same intensity, and the step of densifying the silicon nitride film is performed at a second process temperature that is greater than a first process temperature in the step of forming the silicon nitride film.
14. The method of processing a substrate of claim 1, wherein the steps of forming the silicon nitride film and densifying the silicon nitride film are repeatedly performed a plurality of times, respectively.
15. The method of processing a substrate of claim 1, wherein the steps of forming the silicon nitride film and densifying the silicon nitride film constitute one super-cycle, and the super-cycle is performed a plurality of times according to the degree of filling of the silicon nitride film within the gap.
16. A method of processing a substrate, the method comprising: providing the substrate to a reaction space; supplying an oligomeric silicon precursor having 2 to about 10 chain structures comprising trisilylamine and a nitrogen-containing gas to the reaction space; and forming a silicon nitride film having flowability on the substrate while maintaining the reaction space in a plasma state, wherein a pressure within the reaction space is in the range of about 0.5 Torr to about 10 Torr.
17. The method of processing a substrate of claim 16, further comprising densifying the silicon nitride film after the step of forming the silicon nitride film.
18. The method of processing a substrate of claim 16, wherein the nitrogen-containing gas comprises at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof.
19. The method of processing a substrate of claim 16, wherein, in the step of forming the silicon nitride film, the temperature of the substrate is maintained between about 30 C. and about 70 C.
20. The method of processing a substrate of claim 16, wherein, in the step of supplying the oligomeric silicon precursor and the nitrogen-containing gas, two or more kinds of oligomeric silicon precursor are supplied together to the reaction space.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) The above and other aspects, features, and advantages of certain embodiments of the disclosure will be more apparent from the following description taken in conjunction with the accompanying drawings, in which:
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DETAILED DESCRIPTION
(15) Reference will now be made in detail to embodiments, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout. In this regard, the present embodiments may have different forms and should not be construed as being limited to the descriptions set forth herein. Accordingly, the embodiments are merely described below, by referring to the figures, to explain aspects of the present description. As used herein, the term and/or includes any and all combinations of one or more of the associated listed items. Expressions such as at least one of, when preceding a list of elements, modify the entire list of elements and do not modify the individual elements of the list.
(16) Hereinafter, embodiments of the present disclosure will be described in detail with reference to the accompanying drawings.
(17) Embodiments of the present disclosure are provided to further explain the present disclosure to one of ordinary skill in the art, and the following embodiments may have different forms and the scope of the present disclosure should not be construed as being limited to the descriptions set forth herein. Rather, these embodiments are provided so that the disclosure will be thorough and complete, and will fully convey the scope of the disclosure to one of ordinary skill in the art.
(18) The terminology used herein is for describing particular embodiments and is not intended to limit the disclosure. As used herein, the singular forms a, an, and the are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms includes, comprises and/or including, comprising used herein specify the presence of stated features, integers, steps, processes, members, components, and/or groups thereof, but do not preclude the presence or addition of one or more other features, integers, steps, processes, members, components, and/or groups thereof. As used herein, the term and/or includes any and all combinations of one or more of the associated listed items.
(19) It will be understood that, although the terms first, second, etc. may be used herein to describe various members, components, regions, layers, and/or sections, these members, components, regions, layers, and/or sections should not be limited by these terms. These terms do not denote any particular order, upper and lower, or importance, but rather are only used to distinguish one member, region, layer, and/or section from another member, region, layer, and/or section. Thus, a first member, component, region, layer, or section discussed below could be termed a second member, component, region, layer, or section without departing from the teachings of embodiments.
(20) Embodiments of the disclosure will be described hereinafter with reference to the drawings in which embodiments of the disclosure are schematically illustrated. In the drawings, variations from the illustrated shapes may be expected because of, for example, manufacturing techniques and/or tolerances. Thus, the embodiments of the disclosure should not be construed as being limited to the particular shapes of regions illustrated herein but may include deviations in shapes that result, for example, from manufacturing processes.
(21) First, according to example embodiments of the present disclosure, a method of processing a substrate for forming a flowable film having flowability, for example, a silicon nitride film on a substrate will be described.
(22)
(23) Referring to
(24) As described later, the silicon nitride film formed on the substrate may have flowability, and a flow direction of the silicon nitride film may be closely related to a direction of force applied to the silicon nitride film. For example, when gravity acts on the silicon nitride film, the flow direction of the silicon nitride film may be the direction in which gravity acts on the silicon nitride film. Therefore, when the surface of the substrate is a convex surface, the silicon nitride film may be formed while flowing from a convex portion toward the periphery thereof. On the other hand, when the surface of the substrate is a concave surface recessed from the horizontal plane, the silicon nitride film having flowability may be formed while flowing toward a concave portion thereof. As examples of a case in which the surface of the substrate is concave in the semiconductor manufacturing process, there may be, for example, a gap structure, a via structure, or a stepped structure, and the like.
(25) Referring back to
(26) In some embodiments, the oligomeric silicon source may be supplied alone to the reaction space, respectively, and for example, dimer-TSA as the silicon source may be supplied alone to the reactive space, and in other embodiments, trimer-TSA as the silicon source may be supplied alone to the reactive space. In addition, in some embodiments, two or more kinds of oligomeric silicon precursor sources may be supplied together to the reaction space. For example, in some embodiments, dimer-TSA and trimmer-TSA may be simultaneously supplied as the silicon precursor source, in some other embodiments, trimmer-TSA and tetramer-TSA may be simultaneously supplied as the silicon precursor source, and in yet other embodiments, dimer-TSA, trimmer-TSA, and tetramer-TSA may be simultaneously supplied to the reaction space.
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(28) On the other hand, the nitrogen-containing gas to be used in the example embodiments of the present disclosure may include at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof. In some embodiments, NH.sub.3 may be used as the nitrogen-containing gas. The nitrogen-containing gas may promote condensation reaction and crosslinking in the process of oligomerization of the oligomeric silicon precursor.
(29) Referring back to
(30) The oligomeric silicon precursor supplied to the reaction space together with the nitrogen-containing gas may flow with flowability on the substrate by thermal energy supplied to the substrate in the reaction space under the plasma state, and thus, the silicon nitride film having flowability may be formed on the substrate. At this time, the temperature of the substrate may be maintained at a relatively low temperature, for example, about 100 C. or less, preferably between about 30 C. to about 70 C., so that the substrate has appropriate flowability. As described above, when the silicon precursor source of the monomer or the single molecule is supplied to the substrate maintained in such a temperature range, the silicon precursor source may easily be volatilized, and thus lose flowability. Conversely, when the polymer having the complicated molecular structure is supplied, the silicon precursor may not have significant flowability. Therefore, in such a temperature range of the substrate, to ensure that the silicon source has flowability on the substrate to be significant and suitable for the semiconductor manufacturing process, the oligomeric silicon source having the molecular structure that is not excessively simple and not excessively complicated, for example, having a chain structure of 2 to about 10 chains, may be used.
(31) The oligomeric silicon precursor source supplied to the substrate may flow on the substrate, and when flowing, bonds may occur between the oligomer precursor source molecules to form a structure that has at least about 10 chain structures. This is called oligomerization. The oligomerization may be facilitated through the condensation reaction between the oligomeric source molecules. In the condensation reaction, hydrogen may be removed as a reaction by-product in a SiH bond of the silicon precursor source. The oligomers bonded through the condensation reaction may form a cross-linking structure through cross-linking while flowing within the silicon nitride film having flowability.
(32) Subsequently, although not shown, after forming the silicon nitride film having flowability on the substrate, the surface of the silicon nitride film may be densified to prevent external impurities, such as oxygen or carbon, from penetrating into the silicon nitride film. The densification of the silicon nitride film will be described later.
(33)
(34) Referring to
(35) Referring back to
(36) Referring back to
(37) The oligomeric silicon precursor supplied to the reaction space together with the nitrogen-containing gas may flow with flowability on the substrate by thermal energy supplied to the substrate in the reaction space under the plasma state, so that, due to the flowability itself, the silicon nitride film having flowability may fill the gap concentrically that is formed on the surface of the substrate. As described above, when the silicon precursor source comprising of monomer or single molecule is supplied to the substrate maintained in such a temperature range, the silicon precursor source may be easily volatilized, and thus lose flowability. Conversely, when the silicon precursor source comprising of polymer having the complicated molecular structure is supplied, the flow of the silicon precursor source may be too slow, so that the silicon nitride film may be first formed in the inlet region of the gap before reaching the lower region thereof, thereby closing the inlet region of the gap.
(38) Therefore, a void similar to that shown in
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(40) On the other hand, as described above, the nitrogen-containing gas to be used in the example embodiments of the present disclosure may include at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof. The nitrogen-containing gas may facilitate the cross-linking in the oligomerization process. More specifically, when the gap is filled with only the oligomeric silicon precursor source molecule, NH pores may occur in the gap, and due to the NH pores, a bonding structure of the formed silicon nitride film may be incomplete. With respect to the silicon nitride film with the cross-linking structure shown on the right side of
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(42) On the other hand, when a ratio of Si atoms to N atoms in the silicon nitride film is about 1:1 or less (i.e., about 1:1, for example, 1:0.5), that is, when the number of nitrogen atoms in the silicon nitride film is less than the number of silicon atoms therein, the formation of the cross-linking may be not smooth, and incomplete oligomerization may proceed. When the oligomerization incompletely proceeds, mechanical properties, such as strength of the formed silicon nitride film, may be deteriorated, and the silicon nitride film may also shrink in a post-treatment step to be described later. Therefore, by supplying the nitrogen-containing gas together with the silicon precursor source to solve the lack of nitrogen atoms in the silicon nitride film, nitrogen atoms may be additionally supplied in the silicon nitride film. On the other hand, when the ratio of Si atoms to N atoms in the silicon nitride film is about 1:1 or more (i.e., about 1:1, for example, 1:1.5), that is, when the number of nitrogen atoms in the silicon nitride film is greater than the number of silicon atoms therein, the formation of the cross-linking may be facilitated, which may facilitate the oligomerization, and thus may inhibit the formation of NH pores in the silicon nitride film.
(43) Therefore, in order to facilitate the oligomerization of the silicon nitride film and to inhibit the formation of the NH pores in the silicon nitride film, it may be necessary to supply the nitrogen-containing gas with the silicon precursor source, and further to sufficiently provide the supply amount of nitrogen-containing gas relative to the silicon precursor source. For example, the silicon precursor and the nitrogen-containing gas may be supplied so that the ratio of the Si atoms to N atoms in the silicon nitride film becomes about 1:1 or more (i.e., about 1:1). In some embodiments, when NH.sub.3 is used as the nitrogen-containing gas, the supply amount of NH.sub.3 may be in the range of, for example, greater than 0 sccm to about 2,500 sccm, preferably about 200 sccm to about 2,000 sccm.
(44) Referring back to
(45) Hereinafter, according to example embodiments of the present disclosure, the method of processing the substrate for filling the gap with the silicon nitride film having flowability, specifically the gap-fill process, will be described.
(46)
(47) Referring to
(48) The gap 34 may be an STI generally used to define an active region of a semiconductor device in the semiconductor manufacturing process, and may be various types of recess regions formed on the surface of the substrate 30. In addition, the gap 34 may also be in a form of a via that penetrates a conductive layer between an insulating layer and another insulating layer, or penetrates an insulating layer between a conductive layer and another conductive layer. The gap 34 in
(49) Although the layer 32 is shown as a single layer, the layer 32 may be a multilayer. Furthermore, the gap 34 may have a cylindrical shape, but the cross-sectional shape of the surface of the gap 34 may be various polygonal shapes, such as an ellipse, a triangle, a rectangle, or a pentagon, and the like. In addition, the gap 34 may have an island shape having various cross-sectional shapes of surface, but in some embodiments, the gap 34 may have a line shape on the substrate 30. Furthermore, the gap 34 may have a vertical profile having substantially the same width from the upper region of the gap 34, which is the inlet region of the gap 34, to the lower region thereof. In some embodiments, the gap 34 may have a non-vertical profile in which the width of the gap 34 decreases or increases linearly or stepwise from the upper region of the gap to the lower region thereof.
(50) On the other hand, although
(51) Referring to
(52) In some embodiments, the oligomeric silicon source may be supplied alone to the reaction space, respectively, and for example, dimer-TSA as the silicon source may be supplied alone to the reactive space, and in other embodiments, trimer-TSA as the silicon source may be supplied alone to the reactive space. In addition, in some embodiments, two or more kinds of silicon precursor sources may be supplied together to the reaction space. In some embodiments, dimer-TSA and trimmer-TSA may be simultaneously supplied as the silicon precursor source, in some other embodiments, trimmer-TSA and tetramer-TSA may be simultaneously supplied as the silicon precursor source, and in some other embodiments, dimer-TSA, trimmer-TSA, and tetramer-TSA may be simultaneously supplied to the reaction space.
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(54) On the other hand, the nitrogen-containing gas to be used in example embodiments of the present disclosure may include at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof. In one embodiment, NH.sub.3 may be used as the nitrogen-containing gas.
(55) On the other hand, the temperature of the substrate in the reaction space may be maintained, for example, about 100 C. or less, preferably about 30 C. to about 70 C. The process temperature in the reaction space or the temperature of the vessel containing the silicon source may be maintained, for example, about 100 C. or less, preferably about 30 C. to about 70 C. Then, RF power of about 100 W to about 500 W, preferably about 200 W to about 400 W, may be applied to the reaction space to generate a plasma state in the reaction space. In this case, RF frequency used may be in the range of 13 MHz to 60 MHz, preferably about 20 MHz to about 30 MHz. In order to generate a plasma state in the reaction space, in the example embodiments of the present disclosure, the in-situ plasma treatment may be used, in which RF power is directly applied to the reaction space while supplying the silicon precursor source and the nitrogen-containing gas together to the reaction space, to generate plasma directly over the substrate.
(56) Referring to
(57) Referring to
(58) Referring to
(59) Referring to
(60) Referring to
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(62) Referring to
(63) Referring to
(64) On the other hand, although not specifically shown, a purge step may be provided between the film forming step and the post-treatment step, or between the post-treatment step and the film forming step, and in the purge step, the excess silicon precursor source or the nitrogen-containing gas, or reaction by-products may be removed. On the other hand, in the film forming step, the silicon precursor source or the nitrogen-containing gas may be continuously supplied, but may be supplied intermittently and sequentially. In this case, the purge may be performed during a step in which the silicon precursor source or the nitrogen-containing gas is not supplied.
(65) As described above, as the silicon precursor source used in example embodiments of the present disclosure, for example, the oligomeric silicon precursor source having two to about 10 chain structures, may be used. The nitrogen-containing gas to be used in example embodiments of the present disclosure may include at least one selected from N.sub.2, N.sub.2O, NO.sub.2, NH.sub.3, N.sub.2H.sub.2, N.sub.2H.sub.4, at least one of radicals thereof, and mixtures thereof.
(66) In the film forming step, the temperature of the substrate in the reaction space may be maintained, for example, about 100 C. or less, preferably about 30 C. to about 70 C. The temperature of the substrate in the reaction space described above may be maintained by maintaining the process temperature in the reaction space or the temperature of vessel containing the silicon precursor source, for example, at about 100 C. or less, preferably at about 100 C. to about 70 C. In addition, a relatively low RF power, for example, about 100 W to about 500 W, preferably about 200 W to about 400 W, may be applied to generate a plasma state in the reaction space. The pressure in the reaction space during the film forming step may be maintained in the range of about 0.5 Torr to about 10 Torr, preferably about 2 Torr to about 6 Torr.
(67) Referring back to
(68) On the other hand, the film forming step and the post-treatment step may be performed at the same process temperature, and by increasing second RF power applied to the reaction space in the post-treatment step greater than first RF power applied to the reaction space in the film forming step, the surface of the film to be formed may be easily densified.
(69) Alternatively, the film forming step and the post-treatment step may be performed in the plasma state to which RF power of the same intensity is applied, and by increasing a second temperature applied to the reaction space in the post-treatment step higher than a first temperature applied to the reaction space in the film forming step, the surface of the film to be formed may be easily densified.
(70) On the other hand, as shown in
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(72) First, in step S310, the substrate having a gap structure may be provided to the reaction space. Step S310 may correspond to a process step of
(73) In step S320, the flowable film may be formed in the gap. Step S320 may correspond to processes step of
(74) In step S330, whether the first sub-cycle is terminated may be determined. Whether the first sub-cycle is terminated may be determined in a variety of ways. After setting the number of repetitions of the first sub-cycle to a program in advance, whether the first sub-cycle is terminated may be determined by whether the number of repetitions set in the program is reached. Alternatively, after setting a process time to the program in advance, whether the first sub-cycle is terminated may be determined by whether the process time set in the program is reached. In addition, after identifying the height and width of the gap 34 in advance, whether the first sub-cycle is terminated may be determined by whether the thickness of the flowable film formed in the gap 34 after the first sub-cycle is reached to a certain thickness set in advance. When it is determined as NO in step S330, step S320 may be repeated, and when it is determined as YES in step S330, it may proceed to step S340.
(75) In step S340, the post-treatment on the flowable film formed in the gap may be performed. Step S340 may correspond to a process step of
(76) In step S350, whether the second sub-cycle is terminated may be determined. Whether the second sub-cycle is terminated may be determined in a variety of ways. For example, after setting the number of repetitions of the second sub-cycle to the program in advance, whether the second sub-cycle is terminated may be determined by whether the number of repetitions set in the program is reached. Alternatively, after setting the process time to the program in advance, whether the second sub-cycle is terminated may be determined by whether the process time set in the program is reached. When it is determined as NO in step S350, step S340 may be repeated, and when it is determined as YES' in step S350, it may proceed to step S360.
(77) In step S360, whether a super-cycle is terminated may be determined. The super-cycle may include the first sub-cycle and the second sub-cycle. In some embodiments, one super-cycle may include one first sub-cycle and one second sub-cycle, but in other embodiments, one super-cycle may include a plurality of times of the first sub-cycles (e.g., N times in
(78) Whether the super-cycle is terminated may be determined in a variety of ways. After setting the number of repetitions of the first sub-cycle and the number of repetitions of the second sub-cycle (for example, N times and M times, respectively) to the program in advance, whether the super-cycle is terminated may be determined by whether the numbers of repetitions set in the program is reached. Alternatively, after setting the process times of the first and second sub-cycles to the program in advance, whether the super-cycle is terminated may be determined by whether the process times set in the program is reached. Alternatively, after setting the thickness of the flowable film to fill the gap 34 in advance, whether the super-cycle is terminated may be determined by whether the thickness of the flowable film formed in the gap 34 is reached to the thickness set in advance. Alternatively, whether the super-cycle is terminated may be determined by whether the flowable film fully fills the gap 34.
(79) On the other hand, the super-cycle may be terminated even before the flowable film fully fills in the gap 34. For example, when the aspect ratio of the gap 34 is sufficiently small before the flowable film fully fills the gap 34 so that there is no risk of the occurrence of voids in the gap 34 in a subsequent gap-fill process, the super-cycle may be terminated and a remaining unfilled portion of the gap 34 may be filled through a conventional plasma enhanced chemical vapor deposition method. In step S360, when it is determined as NO, the process may return to step S320 to continue the first sub-cycle forming the flowable film in the gap 34 and the second sub-cycle performing the post-treatment on the flowable film. In step S360, when it is determined as YES, it may proceed to step S370.
(80) In step S370, when it is determined that the super-cycle is terminated, the surface of the gap structure may be planarized. Step S370 may correspond to a process step of
Embodiments
(81) Hereinafter, a substrate processing process according to example embodiments of the present disclosure was performed. Trimer-TSA was used as the silicon precursor source and NH.sub.3 gas was used as the nitrogen-containing gas. The film forming step and the post-treatment step of
(82) TABLE-US-00001 TABLE 1 Time Step Conditions (sec) Film Gas Ar 0 to 3000 (preferably 500 to 2000) <600 forming (sccm) NH.sub.3 0 to 2500 (preferably 500 to 2000) step Carrier Ar 0 to 3000 (preferably 500 to 2000) Plasma RF Power (W) 100 to 500 (preferably 200 to 400) condition RF frequency (MHz) 13 to 60 (preferably 20 to 30) Process pressure (Torr) 0.5 to 10 (preferably 2 to 6) Process Temperature ( C.) 0 to 100 (preferably 30 to 70) Si source Trimer-TSA Si source vessel 70 temperature ( C.) Post Gas Ar (or He) 0 to 3000 (preferably 200 to 2000) <1800 treatment (sccm) step Plasma RF Power (W) 300 to 1500 (preferably 500 to 1000) condition RF frequency (MHz) 13 to 60 (preferably 20 to 30) Process pressure (Torr) 0.5 to 10 (preferably 2 to 6) Process Temperature ( C.) 0 to 100 (preferably 30 to 70)
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(84) Referring to
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(86) Referring to
(87) It should be understood that embodiments described herein should be considered in a descriptive sense only and not for purposes of limitation. Descriptions of features or aspects within each embodiment should typically be considered as available for other similar features or aspects in other embodiments. While one or more embodiments have been described with reference to the figures, it will be understood by those of ordinary skill in the art that various changes in form and details may be made therein without departing from the spirit and scope of the disclosure as defined by the following claims.