The present disclosure generally relates to forming structures. More particularly, the present disclosure relates to forming structures overlaying substrates using trench bottom-up fill techniques, such as during the fabrication of semiconductor devices.
Films are commonly deposited onto substrates to form various types of structures during the fabrication of various types of semiconductors devices such as display devices, power electronics, and very large-scale integrated circuits. Deposition of such films is generally accomplished by positioning a substrate within a reactor, heating the substrate to a temperature suitable for deposition of a desired film onto the substrate, and flowing gas containing constituents of the desired film into the reactor. As the gas flows through the reactor and across the substrate the constituent forms a film on the substrate, typically at a rate and to thickness corresponding to the environmental conditions within the reactor and temperature of the substrate. The resulting film is generally conformal with the underlying substrate, the film typically depositing onto the topology of the substrate in a way that corresponds to the substrate topology.
During the fabrication of some semiconductor devices it may be necessary to deposit a film into the recess such a trench defined within the surface of the substrate. For example, during the fabrication transistor devices having two-dimensional or three-dimensional architectures, fill structures may be formed within trenches by depositing films having desired electrical properties within the trenches, such as isolation features formed to electrically separate adjacent transistors from one another. Such fill features may be formed using epitaxial techniques, the fill feature resulting from the progressive thickening of film from the bottom of the trench upwards and laterally inward from the opposing sidewalls of the trench. Film deposition typically continues until the trench closes—either by the film overlaying the trench bottom bridging the film overlying the sidewalls and overtopping the trench mouth or surfaces of the film overlaying the sidewall converging against one another within the trench.
In some fill structures, the interface (or seam) where opposing surfaces of the sidewall films and/or bottom surface film converge may influence the electrical properties of the resulting fill structure. For example, in substrates where the trench bottom presents a different crystalline structure to the trench than that presented by the trench sidewalls to the trench, film deposited on the trench bottom surface may develop with a different crystalline structure than that of film deposited onto the trench sidewalls. As a consequence, the crystalline structure within the fill structure may change at the interface of the opposing surfaces within the fill structure, locally increasing (or decreasing) electrical resistivity at the interface in relation to the remainder of the fill structure. While generally manageable, the localized variation in electrical properties at the interface can, in some semiconductor devices, influence reliability of the semiconductor device incorporating the fill structure.
Such systems and methods have generally been considered suitable for their intended purpose. However, there remains a need in the art for improved methods of forming structures using bottom-up fill techniques, semiconductor processing systems configured to form structures using bottom-up fill techniques, and semiconductor devices including structures formed using bottom-up fill techniques. The present disclosure provides a solution to this need.
A method of forming a structure is provided. The method includes supporting a substrate within a reaction chamber of a semiconductor processing system, the substrate having a recess with a bottom surface and a sidewall surface extending upwards from the bottom surface of the recess. A film is deposited within the recess and onto the bottom surface and the sidewall surface of the recess, the film having a bottom segment overlaying the bottom surface of the recess and a sidewall segment deposited onto the sidewall surface of the recess. The sidewall segment of the film is removed while at least a portion bottom segment of the film is retained within the recess, the sidewall segment of the film removed from the sidewall surface more rapidly than removing the bottom segment of the film from the bottom surface of the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the bottom segment of the film is deposited onto the bottom surface more rapidly than the sidewall segment of the film is deposited onto the sidewall surface of the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are removed at a removal rate ratio that is between about 5:1 and about 25:1.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the bottom segment and the sidewall segment of the film are deposited at a deposition rate ratio that is between about 1.1:1 and about 2:1.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are removed at a predetermined removal pressure that is between about 1 torr and about 50 torr.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are removed at a predetermined removal temperature that is between about 675° C. and about 800° C.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are deposited at a predetermined deposition pressure that is between about 1 torr and about 50 torr.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are deposited at a predetermined deposition temperature that is between about 675° C. and about 800° C.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the sidewall segment and the bottom segment of the film are deposited and removed at a common pressure, wherein the sidewall segment and the bottom segment of the film are deposited and removed at a common temperature.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include flowing dichlorosilane (DCS), hydrochloric acid (HCl), and hydrogen (H2) gas through an interior of the reaction chamber to deposit the sidewall segment and the bottom segment of the film into the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include flowing hydrochloric acid (HCl) and hydrogen (H2) gas through an interior of the reaction chamber to remove the sidewall segment and a portion of the bottom segment of the film from within the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the bottom surface of the recess has a silicon 1 0 0 crystalline structure and that the sidewall surface of the recess has a silicon 1 1 0 crystalline structure.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include that the deposition operation and the removal operation are a first deposition/removal cycle, and that the method further includes one or more second deposition/removal cycle.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include filling the recess bottom-up from the bottom surface of the recess to an opening into the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the method may include exposing the sidewall surface above a retained portion of the bottom segment of the film from within the recess.
A semiconductor processing system is provided. The semiconductor processing system includes a reaction chamber, a gas delivery system connected to the reaction chamber, and a controller. The controller is operatively connected to the gas delivery system and the reaction chamber and is responsive to instructions recorded on a non-transitory machine-readable memory to: support a substrate within the reaction chamber, wherein the substrate has a recess with a bottom surface and a sidewall surface extending upwards from the bottom surface of the recess; deposit a film within the recess and onto the bottom surface and the sidewall surface of the recess, the film having a bottom segment overlaying the bottom surface of the recess and a sidewall segment deposited onto the sidewall surface of the recess; and remove the sidewall segment of the film while retaining at least a portion bottom segment of the film within the recess, the sidewall segment of the film is removed from the sidewall surface of the recess more rapidly than the bottom segment of the film is removed from the bottom surface of the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the system may include that the instructions further cause the controller to: flow hydrochloric acid (HCl) and hydrogen (H2) gas through an interior of the reaction chamber to remove the sidewall segment and a portion of the bottom segment of the film from within the recess; flow dichlorosilane (DCS), hydrochloric acid (HCl), and hydrogen (H2) gas through the interior of the reaction chamber to deposit the sidewall segment and the bottom segment of the film into the recess; and that the bottom segment of the film is deposited onto the bottom surface of the recess more rapidly than the sidewall segment of the film is deposited onto the sidewall surface of the recess.
In addition to one or more of the features described above, or as an alternative, further examples of the system may include that the instructions further cause the controller to: deposit the bottom segment and the sidewall segment of the film at a deposition rate ratio that is between about 1.1:1 and about 2:1; and remove the bottom segment and the sidewall segment of the film at a removal rate ratio that is between about 5:1 and about 25:1.
In addition to one or more of the features described above, or as an alternative, further examples of the system may include that the instructions further cause the controller to: deposit the sidewall segment and the bottom segment of the film at a predetermined deposition pressure that is between about 1 torr and about 50 torr; deposit the sidewall segment and the bottom segment of the film at a predetermined deposition temperature that is between about 675° C. and about 800° C.; remove the sidewall segment and a portion of the bottom segment of the film at a predetermined deposition pressure that is between about 1 torr and about 50 torr; and remove the sidewall segment and the portion of the bottom segment of the film at a predetermined deposition temperature that is between about 675° C. and about 850° C.
A semiconductor device structure is provided. The semiconductor device structure includes a finFET or gate-all-around transistor having a structure formed using the method as described above.
This summary is provided to introduce a selection of concepts in a simplified form. These concepts are described in further detail in the detailed description of examples of the disclosure below. This summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used to limit the scope of the claimed subject matter.
These and other features, aspects, and advantages of the invention disclosed herein are described below with reference to the drawings of certain embodiments, which are intended to illustrate and not to limit the invention.
It will be appreciated that elements in the figures are illustrated for simplicity and clarity and have not necessarily been drawn to scale. For example, the relative size of some of the elements in the figures may be exaggerated relative to other elements to help improve understanding of illustrated embodiments of the present disclosure.
Reference will now be made to the drawings wherein like reference numerals identify similar structural features or aspects of the subject disclosure. For purposes of explanation and illustration, and not limitation, a partial view of an example of semiconductor processing system in accordance with the present disclosure is shown in
Referring to
The reaction chamber 102 has a hollow interior 130 that extends between an injection end 132 and an exhaust end 134 of the reaction chamber 102, and is formed from a transmissive material 136. The transmissive material 136 may include a glass material, such as quartz. One or more heater elements 138 may be arranged outside of the reaction chamber 102. The one or more heater elements 138 may be configured to communicate heat H into the interior 130 of the reaction chamber 102 through the transmissive material 136 forming the reaction chamber 102, the transparent material 136 radiantly coupling the one or more heater elements 138 the interior 130 of the reaction chamber 102 in such examples. The one or more heater element 138 is in turn operably associated with the controller 128.
The exhaust header 106 is connected to the exhaust end 134 of the reaction chamber 102 and is configured to connect the interior 130 of the reaction to an exhaust source such as a scrubber. In certain examples, the exhaust end 134 of the reaction chamber 102 may have an exhaust flange extending thereabout, the exhaust header 106 in such examples connected to the exhaust flange. The injection header 104 is connected to the injection end 132 of the reaction chamber 102. It is contemplated that the injection header 104 connect the gas delivery arrangement 118 to the reaction chamber 102. In this respect the injection header 104 connects each of the first precursor source 120, the second precursor source 122, the halide source 124, and the purge/carrier gas source 126 to the reaction chamber 102 in the illustrated examples. In certain examples, the injection end 132 of the reaction chamber 102 may have an injection flange extending thereabout, and the injection header 104 may be connected to the injection flange. The reaction chamber 102 may be as shown and described in U.S. Patent Application Publication No. 2018/0363139 A1 to Rajavelu et al., filed Apr. 25, 2018, the contents of which are incorporated herein by reference in their entirety.
The first precursor source 120 is connected to the injection header 104 by a precursor conduit 140 and is configured to provide a first precursor 142 to the reaction chamber 102. In certain examples, the first precursor 142 may include a silicon-containing precursor, such as a hydrogenated silicon-containing precursor and/or a chlorinated silicon-containing precursor. Examples of suitable chlorinated silicon-containing precursors include monochlorosilane (MCS), dichlorosilane (DCS), trichlorosilane (TCS), hexachlorodisilane (HCDS), octachlorotrislane (OCS), and silicon tetrachloride (STC). Examples of suitable hydrogenated silicon-containing precursors include silane (SiH4), disilane (Si2H6), trisilane (Si3H8), and tetrasilane (Si4H10). It is contemplated that a first precursor mass flow controller (MFC) 144 connect the first precursor source 120 to the precursor conduit 140. The first precursor MFC 144 may be operatively associated with the controller 128 to flow the first precursor 142 to the injection header 104, and therethrough into the interior 130 of the reaction chamber 102.
The second precursor source 122 is also connected to the injection header 104 by the precursor conduit 140 and is configured to provide a second precursor 146 to the reaction chamber 102. In certain examples, the second precursor 146 may include a germanium-containing precursor. Examples of suitable germanium-containing precursors include germane (GeH4), digermane (Ge2H6), trigermane (Ge3H8), and germylsilane (GeH6Si). In accordance with certain examples, the second precursor 146 may include an n-type or a p-type dopant. Examples of suitable n-type dopants include phosphorus (P) and arsenic (As). Examples suitable p-type dopants include boron (B), gallium (Ga) and indium (In). It is contemplated that a second precursor MFC 148 connect the second precursor source 122 to the precursor conduit 140. The second precursor MFC 148 may be operatively associated with the controller 128 to control flow of the second precursor 146 to the injection header 104, and therethrough into the interior 130 of the reaction chamber 102.
In the illustrated example, the halide source 124 is connected to the injection header 104 by both the precursor conduit 140 and a halide conduit 150 and is configured to provide a halide 152 to the reaction chamber 102. The halide 152 may include fluorine (F) or chlorine (Cl), for example by providing a flow of hydrochloric acid (HCl) to the reaction chamber 102. It is contemplated that a first halide MFC 154 connect the halide source 124 to the precursor conduit 140 and therethrough to the reaction chamber 102 through the injection header 104, and that a second halide MFC 156 also connect the halide source 124 to the halide conduit 150 and therethrough to the reaction chamber 102 through the injection header 104. The first halide MFC 154 and the second halide MFC 156 are in turn operatively associated with the controller 128 to control flow of the halide 152 through either (or both) the precursor conduit 140 and the halide conduit 150, respectively. As will be appreciated by those of skill in the art in view of the present disclosure, this allows the halide source 124 to flow the halide 152 into the reaction chamber 102 with the first precursor 142 and/or the second precursor 146 and/or independently of first precursor 142 and/or the second precursor 146.
The purge/carrier gas source 126 is connected to the injection header 104 by the precursor conduit 140 and the halide conduit 150 and is configured to provide a purge/carrier gas 158 to the reaction chamber 102. Examples of suitable purge/carrier gases include hydrogen (H2), nitrogen (N2), helium (He), krypton (Kr), argon (Ar), and mixtures thereof. It is contemplated that a first purge/carrier gas MFC 160 connect the purge/carrier gas source 126 to the precursor conduit 140 and therethrough the reaction chamber 102 through the injection header 104, and that a second purge/carrier gas MFC 162 further connect the purge/carrier gas source 126 to the halide conduit 150 and therethrough to the reaction chamber 102 through the injection header 104. The first purge/carrier gas MFC 160 and the second purge/carrier gas MFC 162 are in turn operatively associated with the controller 128 to control flow the purge/carrier gas 158 into the reaction chamber 102. As will be appreciated by those of skill in the art in view of the present disclosure, this allows the purge/carrier gas 158 to be provided to the reaction chamber 102 through either (or both) the precursor conduit 140 and the halide conduit 150. In certain examples, the gas delivery arrangement 118 may be as shown and described in U.S. Patent Application Publication No. 2020/00404458 A1 to Ma et al., filed Aug. 6, 2018, the contents of which is incorporated herein by reference in its entirely. However, as will be appreciated by those of skill in the art in view of the present disclosure, gas delivery arrangements employing one or more manual flow control valve may also be employed and remain within the scope of the present disclosure.
The outer ring 110 is fixed within the interior 130 of the reaction chamber 102. The outer ring 110 may be formed from an opaque material 164 to receive heat H from one or more heater element 138. Examples of suitable opaque materials include silicon carbide coated graphite. It is contemplated that the outer ring 110 have an aperture therein arranged to receive therein the susceptor 112, the susceptor 112 circumferentially separated from the outer ring 110 by a gap.
The susceptor 112 is arranged within the interior 130 of the reaction chamber 102 and within the outer ring 110 and is configured to support thereon a substrate 302 during the forming of a structure 300 within a recess 308 (shown in
The controller 128 includes a processor 170, a device interface 172, a user interface 174, and a memory 176. The device interface 172 operably associates the controller 128 with the semiconductor processing system 100, e.g., via a wired or wireless link to one or more of the one or more heater element 138; one or more of the MFCs of the semiconductor processing system 100, e.g., the first precursor MFC 144, the second precursor MFC 148, the first halide MFC 154 and the second halide MFC 156, and the first purge/carrier gas MFC 160 and the second purge/carrier gas MFC 162; and the drive module 168. The processor 170 is in turn operably connected to the user interface 174, which may include a display and/or a user input device and is disposed in communication with the memory 176. The memory 176 has a plurality of program modules 178 recorded thereon that, when read by the processor 170, cause the processor 170 to execute certain operations. Among the operations are operations of a method 200 (shown in
With reference to
As shown with box 220, a film, e.g., a film 328 (shown in
With reference to
As shown with box 223, depositing 220 the film may include flowing dichlorosilane (DCS), hydrochloric acid (HCl), and hydrogen (H2) gas into the interior of the reaction chamber, e.g., using the gas delivery arrangement 118 (shown in
As shown with box 227, a predetermined deposition temperature may be maintained within the interior of the reaction chamber during the deposition 220 operation. The predetermined deposition temperature may be between about 675° C. and about 850° C. during the depositing 220 operation, as also shown with box 227. For example, the predetermined deposition temperature may be less than about 850° C., or less than 800° C., or less than about 750° C., or even less than about 675° C. during the depositing 220 operation, as also shown with box 227. Advantageously, flowing dichlorosilane (DCS), hydrochloric acid (HCl), and hydrogen (H2) gas within these pressure and temperature ranges allows the bottom segment of the film to be deposited onto the bottom surface of the recess more rapidly than the sidewall segment of the film is deposited onto the sidewall surface of the recess in examples where the bottom surface of the recess has a silicon 1 0 0 crystalline structure and the lower surface of the recess has a silicon 1 1 0 crystalline structure, as shown with chart A in
With continuing reference to
With reference to
In certain examples, removing 230 the sidewall segment of the film while retaining at least a portion of the bottom segment of the film may include maintaining a predetermined removal pressure within the interior of the reaction chamber, as shown with box 233. Pressure may be maintained within the interior of the reaction chamber between about 1 torr and about 50 torr during the removing operation, as also shown with box 233. For example, pressure within the interior of the reaction chamber may be maintained at less than about 50 torr, or less than about 40 torr, or less than about 30 torr, or less than about 20 torr, or even less than about 10 torr, as shown with box 235. Advantageously, pressures within this range allows the sidewall segment of the film to be removed more rapidly than the bottom segment of the film, as shown with chart C in
In certain examples, removing the sidewall segment of the film while retaining at least a portion of the bottom segment of the film may include maintaining a predetermined removal temperature within the interior of the reaction chamber, as shown with box 239. For example, temperature within the interior of the reaction chamber may be maintained at less than about 850° C., or less than about 800° C., or less than about 750° C., or even less than about 675° C., as also shown with box 239. Temperature within the interior of the reaction chamber may be maintained between about 850° C. and about 675° C. during the removing operation, as further shown with box 239. Advantageously, temperatures within this range may further increase the removal rate ratio during the removing operation, as shown with chart D in
With continuing reference to
As shown with box 250, the method 200 may include filling the recess. In this respect the recess may be bottom-up filled, i.e., without incorporating film deposited onto the sidewall of the recess into the retained portions forming the structure, as shown with box 252. Completion of the fill may be accomplished in a topping operation during which a topping film is deposited onto the at least one second retained portion, as shown with box 254. It is contemplated that each of the retained portions have a homogenous 1 0 0 crystalline structure, the structure having a homogenous 1 0 0 crystalline structure throughout, i.e. without internal converging surfaces and/or portions formed with 1 1 0 crystalline structure, as shown with box 256. As will be appreciated by those of skill in the art in view of the present disclosure, the homogenous 1 0 0 crystalline structure limits variation of the electrical properties of the structure, improving reliability of semiconductor devices including structures formed using the method.
In certain examples, a semiconductor device, e.g., a semiconductor device 400 (shown in
With reference to
The recess 308 has a width 324 and a depth 326. In certain examples, the recess 308 may be a high aspect ratio recess. For example, an aspect ratio defined by the depth 326 and the width 324 may be greater than about 3:1, or greater than about 10:1, or greater than about 50:1, or even greater than about 100:1. The aspect ratio may be between about 3:1 and about 100:1. In accordance with certain examples, the recess may be a trench. It is also contemplated that the recess 308 may be a via, a contact, or any other recess suitable for forming the structure 300 (shown in
As shown in
The film 328 may be deposited within the recess 308 by flowing dichlorosilane (DCS), hydrochloric acid (HCl), and hydrogen (H2) gas through the interior 130 of the reaction chamber 102. The film 328 may be deposited within the recess 308 by maintaining at least one of a predetermined deposition pressure and a predetermined deposition temperature within the interior 130 of the reaction chamber 102 (shown in
As shown in
The sidewall segment 332 (shown in
As shown in
As shown in
As shown in
Although this disclosure has been provided in the context of certain embodiments and examples, it will be understood by those skilled in the art that the disclosure extends beyond the specifically described embodiments to other alternative embodiments and/or uses of the embodiments and obvious modifications and equivalents thereof. In addition, while several variations of the embodiments of the disclosure have been shown and described in detail, other modifications, which are within the scope of this disclosure, will be readily apparent to those of skill in the art based upon this disclosure. It is also contemplated that various combinations or sub-combinations of the specific features and aspects of the embodiments may be made and still fall within the scope of the disclosure. It should be understood that various features and aspects of the disclosed embodiments can be combined with, or substituted for, one another in order to form varying modes of the embodiments of the disclosure. Thus, it is intended that the scope of the disclosure should not be limited by the particular embodiments described above.
The headings provided herein, if any, are for convenience only and do not necessarily affect the scope or meaning of the devices and methods disclosed herein.
This application is a non-provisional of, and claims priority to and the benefit of, U.S. Provisional Patent Application No. 63/216,811, filed Jun. 30, 2021 and entitled “FORMING STRUCTURES WITH BOTTOM-UP FILL TECHNIQUES,” which is hereby incorporated by reference herein.
Number | Date | Country | |
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63216811 | Jun 2021 | US |