VARIABLE CONDUCTANCE GAS DISTRIBUTION APPARATUS AND METHOD
20170216762 ยท 2017-08-03
Inventors
Cpc classification
Y10T137/87265
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y10T137/87281
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
F16K1/385
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/0446
PERFORMING OPERATIONS; TRANSPORTING
F16K1/38
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F16K1/32
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
Abstract
Variable conductance gas distribution systems, reactors and systems including the variable conductance gas distribution systems, and methods of using the variable conductance gas distribution systems, reactors, and systems are disclosed. The variable conductance gas distribution systems allow rapid manipulation of gas-flow conductance through the gas distribution system.
Claims
1. A variable conductance gas distribution system comprising: a gas inlet; a first member having one or more first features; a second member having one or more second features; and a mechanism to move at least one of the first member and the second member relative to the other member to manipulate an amount of gas flow, wherein, when the gas distribution system is open, gas flows between the one or more first features and the one or more second features, wherein when the gas distribution system is closed, a seal forms between the one or more first features and the one or more second features, and wherein the first member and the second member are spaced apart a first distance to allow gas to flow at a first conductance for a first process, spaced apart a second distance to allow gas to flow at a second conductance for a second process, and wherein the first member and the second member can be moved to another position to form the seal.
2. The variable conductance gas distribution system of claim 1, wherein the one or more first features are tapered.
3. The variable conductance gas distribution system of claim 2, wherein the one or more first features are frustum shaped.
4. The variable conductance gas distribution system of claim 3, wherein the one or more second features are frustum shaped.
5. The variable conductance gas distribution system of claim 1, wherein the one or more second features are tapered.
6. The variable conductance gas distribution system of claim 1, wherein at least one of the one or more first features and at least one of the one or more second features are concentric with respect to each other.
7. The variable conductance gas distribution system of claim 1, further comprising a reactant gas source coupled to the gas inlet.
8. The variable conductance gas distribution system of claim 1, further comprising a purge gas source coupled to the gas inlet.
9. The variable conductance gas distribution system of claim 1, wherein the mechanism moves the first member and the second member together prior to the gas inlet receiving a reactant gas.
10. The variable conductance gas distribution system of claim 1, wherein the mechanism moves the first member and the second member apart prior to the gas inlet receiving a purge gas.
11. The variable conductance gas distribution system of claim 1, wherein one or more of the first features and the one or more second features comprise apertures to allow gas to flow there through when a seal is formed between the one or more first features and the one or more second features.
12. The variable conductance gas distribution system of claim 1, wherein the mechanism causes the first member to move a distance of between about 0 and about 10 mm.
13. The variable conductance gas distribution system of claim 1, further comprising a coupling element coupled to the one or more first features.
14. The variable conductance gas distribution system of claim 1, further comprising a coupling element coupled to the one or more second features.
15. The variable conductance gas distribution system of claim 1, wherein the first member comprises a plurality of first features concentrically arranged with respect to each other.
16. The variable conductance gas distribution system of claim 1, wherein the second member comprises a plurality of second features concentrically arranged with respect to each other.
Description
BRIEF DESCRIPTION OF THE DRAWING FIGURES
[0014] A more complete understanding of exemplary embodiments of the present disclosure can be derived by referring to the detailed description and claims when considered in connection with the following illustrative figures.
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[0023] 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 dimensions of some of the elements in the figures may be exaggerated relative to other elements to help to improve the understanding of illustrated embodiments of the present disclosure.
DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS OF THE DISCLOSURE
[0024] The description of exemplary embodiments provided below is merely exemplary and is intended for purposes of illustration only; the following description is not intended to limit the scope of the disclosure or the claims. Moreover, recitation of multiple embodiments having stated features is not intended to exclude other embodiments having additional features or other embodiments incorporating different combinations of the stated features.
[0025] A set forth in more detail below, various embodiments of the disclosure relate to variable conductance gas distribution systems, reactors and reactor systems that include a variable conductance gas distribution system, and to methods of using the variable conductance gas distribution systems, and reactors. The variable conductance gas distribution systems, reactors, and methods can be used for a variety of gas-phase processes, such as deposition, etch, clean, and/or treatment processes.
[0026]
[0027] Reactor 102 may be used to deposit material onto a surface of a substrate 126, etch material from a surface of substrate 126, clean a surface of substrate 126, treat a surface of substrate 126, deposit material onto a surface within reaction chamber 126, clean a surface within reaction chamber 104, etch a surface within reaction chamber 104, and/or treat a surface within reaction chamber 104. Reactor 102 can be a standalone reactor or part of a cluster tool. Further, reactor 102 can be dedicated to deposition, etch, clean, or treatment processes, or reactor 102 may be used for multiple processese.g., for any combination of deposition, etch, clean, and treatment processes. By way of examples, reactor 102 may include a reactor typically used for chemical vapor deposition (CVD) processes, such as atomic layer deposition (ALD) processes.
[0028] Substrate holder 106 is designed to hold substrate or workpiece 126 in place during processing. In accordance with some exemplary embodiments, reactor 102 includes a direct plasma apparatus; in this case substrate holder 106 can form part of a direct plasma circuit. Additionally or alternatively, substrate holder 106 can be heated, cooled, or be at ambient process temperature during processing. By way of example, substrate holder 106 can be heated during substrate 146 processing, such that reactor 102 is operated in a cold-wall, hot-substrate configuration.
[0029] Although gas inlet 124 is illustrated in block form, gas inlet 124 may be relatively complex and be designed to mix gas (e.g., vapor) from reactant sources 112, 114 and/or carrier/purge gases from one or more sources 116 prior to distributing the gas mixture to reaction chamber 104. Further, gas inlet 124 can be configured to provide vertical (as illustrated) or horizontal flow of gases to chamber 104. An exemplary gas distribution system is described in U.S. Pat. No. 8,152,922 to Schmidt et al., issued Apr. 10, 2012, entitled Gas Mixer and Manifold Assembly for ALD Reactor, the contents of which are hereby incorporated herein by reference, to the extent the contents do not conflict with the present disclosure. Gas inlet can optionally include an integrated manifold block designed to receive and distribute one or more gases to reaction chamber 104. An exemplary integrated inlet manifold block is disclosed in U.S. Pat. No. 7,918,938 to Provencher et al., issued Apr. 5, 2011, entitled High Temperature ALD Inlet Manifold, the contents of which are hereby incorporated herein by reference, to the extent the contents do not conflict with the present disclosure.
[0030] Remote plasma unit 128 can be an inductively coupled plasma unit or a microwave remote plasma unit. In the illustrated example remote plasma unit 128 can be used to create reactive or excited species for use in reaction chamber 104. Although system 100 is illustrated with remote plasma unit 128, systems in accordance with other exemplary embodiments of the disclosure do not include a remote plasma unit. In addition to or as an alternative to using remote plasma unit 128 to form excited species, system 100 can include another excitation source, such as a thermal or hot filament source, a microwave source, or the like.
[0031] Vacuum source 110 can include any suitable vacuum source capable of providing a desired pressure in reaction chamber 104. Vacuum source 110 may include, for example, a dry vacuum pump alone or in combination with a turbo molecular pump.
[0032] Reactant gas sources or precursors 112 and 114 can each include one or more gases, or materials that become gaseous, that are used in deposition, etch, clean, or treatment processes. Exemplary gas sources include noble gases liquid vapors and vaporized solid sources. Although illustrated with two reactant gas sources 112, 114, systems in accordance with the disclosure can include any suitable number of reactant sources.
[0033] Purge gas source 116 includes one or more gases, or materials that become gaseous, that are relatively unreactive in reactor 102. Exemplary purge gases include nitrogen, argon, helium, and any combinations thereof. Although illustrated with one purge gas source, systems in accordance with the present disclosure can include any suitable number of purge gas sources. Further one or more purge gas sources can provide one or more carrier gases and/or system 100 can include additional carrier gas sources to provide a carrier gas to be mixed with one or more gases from a reactant source, such as sources 112, 114.
[0034] Flow controllers 118-122 can include any suitable device for controlling gas flow. For example, flow controllers 118-122 can be mass flow controllers. In addition, system 100 can include valves 130-134 to further control or shut off a gas source.
[0035] Variable conductance gas distribution system 108 is configured to manipulate a gas flow rate of a gas flowing between gas inlet 124 toward substrate 126 and vacuum source 110. In the illustrated example, variable conductance gas distribution system 108 includes a first member 136 and a second member 138. First member 136 includes one or more features 140-142 and a coupling element 158. Second member 138 includes one or more second features 148-158 and a coupling element 160. A mechanism 162 can cause first member 136 and second member 138 to move relative each other to increase or decrease a conductance of gas flowing between features 140-142 and features 148-152. By way of examples, mechanism 162 can cause first member 136 and second member 130 to move from a closed or 0 position to a distance of about 10 mm, or from about 0 to about 6 mm.
[0036] A material used to form first member 136, second member 138, and components thereof can vary according to application. By way of examples, first member 136 and second member 138 are formed of nickel, nickel-plated aluminum, a high-nickel stainless steel material, such as Hastalloy alloy (e.g., c22), or the like.
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[0039] With reference again to
[0040] Features 140-142, 148-152 are illustrated as tapered, generally having frustum shaped (e.g., frusto-triangular shape in cross section). However, the features 140-152 can have any suitable shape. However, to facilitate control of gas conductance, features 140-152 can desirably include a slanted surface. For example, an angle of a sidewall between a base of a feature and the top of the feature can range from about 10 to about 80 degrees or about 30 to about 60 degrees.
[0041] Variable conductance gas distribution system 108 can include any suitable number of features. By way of examples, first member 136 can include 1-10 or more features, and second member 138 can include 1-10 or more features, with the features associated (e.g., attached to) first member 136 generally alternating with the features of second member 138. Further, although features 140-142, 148-152 are illustrated as concentric circles or hollow circles in cross-section as viewed from the top or bottom of variable conductance gas distribution system 108 (see
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[0044] Turning now to
[0045] Although exemplary embodiments of the present disclosure are set forth herein, it should be appreciated that the disclosure is not so limited. For example, although the methods and reactor systems are described in connection with various specific configurations, the disclosure is not necessarily limited to these examples. Various modifications, variations, and enhancements of the exemplary systems and methods set forth herein may be made without departing from the spirit and scope of the present disclosure.
[0046] The subject matter of the present disclosure includes all novel and nonobvious combinations and subcombinations of the various systems, components, and configurations, and other features, functions, acts, and/or properties disclosed herein, as well as any and all equivalents thereof.