WO2012173931A1 - Process gas diffuser assembly for vapor deposition system - Google Patents
Process gas diffuser assembly for vapor deposition system Download PDFInfo
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- WO2012173931A1 WO2012173931A1 PCT/US2012/041913 US2012041913W WO2012173931A1 WO 2012173931 A1 WO2012173931 A1 WO 2012173931A1 US 2012041913 W US2012041913 W US 2012041913W WO 2012173931 A1 WO2012173931 A1 WO 2012173931A1
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- WIPO (PCT)
- Prior art keywords
- gas
- outlet
- diffuser assembly
- gas diffuser
- substrate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
- C23C16/45568—Porous nozzles
Definitions
- the invention relates to a gas distribution system for use in electronic device manufacturing.
- Vapor deposition processes can include chemical vapor deposition (CVD) and plasma enhanced CVD (PECVD).
- CVD chemical vapor deposition
- PECVD plasma enhanced CVD
- FEOL front-end-of-line
- low-k low dielectric constant
- BEOL back-end-of-line
- capacitor formation in advanced memory production.
- a continuous stream of film precursor vapor is introduced to a process chamber containing a substrate, wherein the composition of the film precursor has the principal atomic or molecular species found in the film to be formed on the substrate.
- the precursor vapor is chemisorbed on the surface of the substrate while it thermally decomposes and reacts with or without the presence of an additional gaseous component that assists the reduction of the chemisorbed material, thus, leaving behind the desired film.
- the CVD process further includes plasma that is utilized to alter or enhance the film deposition mechanism.
- plasma excitation can allow film-forming reactions to proceed at temperatures that are significantly lower than those typically required to produce a similar film by thermally excited CVD.
- plasma excitation may activate film-forming chemical reactions that are not energetically or kinetically favored in thermal CVD.
- ALD atomic layer deposition
- FEOL front end-of-line
- BEOL back end-of-line
- ALD atomic layer deposition
- Variations of ALD include plasma-enhanced ALD, which includes plasma formation during at least a part of the ALD cycle.
- ALD two or more process gases are introduced alternatingly and sequentially in order to form a material film one monolayer at a time.
- Such an ALD process has proven to provide improved uniformity and control in layer thickness, as well as conformality to features on which the layer is deposited.
- Various embodiments relate to a gas distribution system for use in electronic device manufacturing and, in particular to a gas distribution system for use in a vapor deposition system, such as an ALD system.
- a gas diffuser assembly is
- the gas diffuser assembly includes a gas diffuser manifold configured to be coupled to a substrate processing system and arranged to introduce a process gas from a gas outlet into the substrate processing system in a direction substantially normal to a surface of a substrate to create a stagnation flow pattern over the surface.
- the gas diffuser manifold comprises: a gas inlet for providing a flow rate of the process gas to the gas diffuser manifold, a stagnation plate located in an inlet gas plenum and configured to intersect with and force the process gas to flow radially outward, wrap around a peripheral edge of the stagnation plate, and flow radially inward, and a diffusion member located at an outlet of the inlet gas plenum and configured to diffuse the flow rate of the process gas prior to introduction into the substrate processing system, the diffusion member comprising a plurality of openings to allow the flow rate of the process gas there through.
- a vapor deposition system includes a process chamber having a vacuum pumping system configured to control and/or optimize a pressure in the process chamber; a substrate holder coupled to the process chamber and configured to support a substrate; and a gas distribution system having a gas diffuser manifold coupled to the process chamber and arranged to introduce a process gas from a gas outlet into the substrate processing system in a direction substantially normal to a surface of the substrate to create a stagnation flow pattern over the surface.
- FIGs. 1A through 1 C show schematic representations of a deposition system according to an embodiment
- FIG. 2 provides a cross-section illustration of a gas diffuser assembly according to an embodiment
- FIG. 3 provides a cross-section illustration of a gas diffuser assembly according to another embodiment
- FIG. 4 provides a graphical illustration of an assembly view of a gas diffuser assembly according to another embodiment
- FIGs. 5A and 5B provide photographs of an assembled gas diffuser assembly according to various embodiments
- FIG. 6 provides a cross-section illustration of a gas diffuser assembly according to another embodiment
- FIGs. 7A and 7B provide frontal views of a plate-like member having a plurality of openings according to various embodiments.
- FIGs. 8A and 8B provide exemplary data for depositing a thin film using the gas diffuser assembly depicted in FIG. 2.
- substrate refers to the object being processed in accordance with the invention.
- the substrate may include any material portion or structure of a device, particularly a semiconductor or other electronics device, and may, for example, be a base substrate structure, such as a semiconductor wafer or a layer on or overlying a base substrate structure such as a thin film.
- substrate is not intended to be limited to any particular base structure, underlying layer or overlying layer, patterned or un-patterned, but rather, is contemplated to include any such layer or base structure, and any combination of layers and/or base structures.
- the description below may reference particular types of substrates, but this is for illustrative purposes only and not limitation.
- the inventors propose implementing a gas distribution system having high flow conductance to introduce a uniform flow of process gas over the substrate positioned in a deposition system having a reduced process volume, i.e., reduced residence time.
- FIGs. 1 A through 1 C depict a substrate processing system according to an embodiment.
- the substrate processing system may include a deposition system 100, such as a vapor deposition system.
- the deposition system 100 may include an atomic layer deposition (ALD) system.
- ALD atomic layer deposition
- deposition system 100 may include a plasma enhanced ALD (PEALD) system, a chemical vapor deposition system (CVD), a plasma enhanced CVD (PECVD) system, a filament assisted CVD
- PEALD plasma enhanced ALD
- CVD chemical vapor deposition system
- PECVD plasma enhanced CVD
- filament assisted CVD filament assisted CVD
- the substrate processing system may alternatively include an etch system, a thermal processing system, a rapid thermal processing (RTP) system, an annealing system, a rapid thermal annealing (RTA) system, a furnace, etc.
- FCVD physical vapor deposition
- PVD physical vapor deposition
- iPVD ionized PVD
- ALE atomic layer epitaxy
- MBE molecular beam epitaxy
- the substrate processing system may alternatively include an etch system, a thermal processing system, a rapid thermal processing (RTP) system, an annealing system, a rapid thermal annealing (RTA) system, a furnace, etc.
- RTP rapid thermal processing
- RTA rapid thermal annealing
- the deposition system 100 may, for example, be used to deposit metal-containing films during the metallization of inter-connect and intra- connect structures for semiconductor devices in back-end-of-line (BEOL) operations.
- the deposition system 100 may, for example, be used to deposit metal-containing films during the fabrication of gate dielectrics and/or gate electrodes in front-end-of-line (FEOL) operations.
- Deposition system 100 configured, for example, to facilitate a deposition process, comprises a process chamber 1 10 having a substrate holder 120 configured to support a substrate 125, upon which a thin film may be formed, etched, or treated.
- the process chamber 1 10 further comprises an upper assembly 1 12 through which a process material and/or a cleaning material may be introduced to the process chamber 1 10 from a material delivery system 130.
- deposition system 100 comprises a vacuum pumping system 140 coupled to the process chamber 1 10 and configured to evacuate process chamber 1 10 through one or more pumping ducts 141 .
- deposition system 100 comprises a controller 150 that can be coupled to process chamber 1 10, substrate holder 120, material delivery system 130, and vacuum pumping system 140.
- the deposition system 100 may be characterized as a stagnation flow processing system, wherein process material and/or cleaning material may be introduced through upper assembly 1 12 above substrate 125 in a direction substantially perpendicular to substrate 125 or substrate holder 120.
- process material and/or cleaning material may enter above substrate 125 through a gas distribution system 135 and flow to substrate 125 in a direction substantially perpendicular with substrate 125 or substrate holder 120.
- the deposition system 100 may be configured to process 200 mm substrates, 300 mm substrates, or larger-sized substrates.
- the substrate processing system such as deposition system 100, may be configured to process substrates, wafers, or LCD (liquid-crystal display) panels regardless of their size, as would be appreciated by those skilled in the art.
- Substrates can be introduced to process chamber 1 10 through a passage (not shown), and they may be lifted to and from an upper surface of substrate holder 120 via a substrate lift system 126.
- the substrate lift system 126 may, for example, include an array of lift pins that extend through the substrate holder 120 to the backside of substrate 125, thus, enabling vertical translation of substrate 125 between a substrate process position 170 (see FIGs. 1A and 1 B) on an upper surface 128 of the substrate holder 120 and a substrate exchange position 172 (see FIG. 1 C) located above the upper surface 128 of the substrate holder 120.
- the substrate holder When processing substrate 125, the substrate holder may be positioned at a process location 180 (see FIG. 1A). Alternatively, when loading or unloading substrate 125, the substrate holder may be positioned at a transfer location 182 (see FIGs. 1 B and 1 C).
- the material delivery system 130 may include a process material supply system 132 for introducing process material to process chamber 1 10, and a cleaning material supply system 134 for introducing cleaning material to process chamber 1 10.
- the process material supply system 132 may be configured to provide a continuous flow, a cyclical flow, or an acyclical flow of process material to process chamber 1 10.
- the cleaning material supply system 134 may be configured to provide a continuous flow, a cyclical flow, or an acyclical flow of cleaning material to process chamber 1 10.
- the process material can, for example, comprise a film forming composition, such as a composition having the principal atomic or molecular species found in the film formed on substrate 125, or the process material can, for example, comprise an etchant or other treating agent.
- the process material may be prepared and supplied to the process chamber 1 10 through the upper assembly 1 12 using the material delivery system 130.
- the process material can originate as a solid phase, a liquid phase, or a gaseous phase, and it may be delivered to process chamber 1 10 in a gaseous phase with or without the use of an additive gas and/or a carrier gas.
- the process material may include one or more gases, or one or more vapors formed in one or more gases, or a mixture of two or more thereof.
- the process material supply system 132 can include one or more gas sources, or one or more vaporization sources, or a combination thereof.
- vaporization refers to the transformation of a material (normally stored in a state other than a gaseous state) from a non-gaseous state to a gaseous state. Therefore, the terms "vaporization,” “sublimation” and “evaporation” are used interchangeably herein to refer to the general formation of a vapor (gas) from a solid or liquid material, regardless of whether the transformation is, for example, from solid to liquid to gas, solid to gas, or liquid to gas.
- the process material may, for example, include a purge gas.
- the purge gas may comprise an inert gas, such as a noble gas (i.e., helium, neon, argon, xenon, krypton), or other gas, such as an oxygen- containing gas, a nitrogen-containing gas, and/or a hydrogen-containing gas.
- the cleaning material can, for example, comprise ozone. As shown in FIG. 1A, ozone may be created using an ozone gas generator and supplied to the process chamber 1 10 through the upper assembly 1 12 using the material delivery system 130.
- the ozone gas generator may include an H-series, P-series, C-series, or N-series ozone gas generating system commercially available from TMEIC (Toshiba Mitsubishi-Electric Industrial Systems Corporation, Tokyo, Japan).
- An oxygen-containing gas is supplied to the ozone gas generator, and optionally a nitrogen-containing gas is supplied to act as a catalyst.
- the oxygen-containing gas may include O2, NO, NO2, N 2 O, CO, or CO2, or any combination of two or more thereof.
- the nitrogen-containing gas may include N 2 , NO, NO 2 , N 2 O, or NH 3 , or any combination of two or more thereof.
- O2 and, optionally, N 2 may be supplied to the ozone gas generator to form ozone.
- the cleaning material may, for example, include a purge gas.
- the purge gas may comprise an inert gas, such as a Noble gas (i.e., helium, neon, argon, xenon, krypton), or other gas, such as an oxygen- containing gas, a nitrogen-containing gas, and/or hydrogen-containing gas.
- the material delivery system 130 can include one or more material sources, one or more pressure control devices, one or more flow control devices, one or more filters, one or more valves, or one or more flow sensors.
- the material delivery system 130 may be configured to alternatingly introduce one or more process materials, one or more cleaning materials, or one or more purge gases, or any combination of two or more thereof to process chamber 1 10.
- the material delivery system 130 may be configured to alternatingly introduce one or more process materials, one or more cleaning materials, or one or more purge gases, or any combination of two or more thereof through the gas distribution system 135 to the process chamber 1 10.
- the gas distribution system 135 may include a gas diffuser assembly 200 configured to introduce a process gas
- the gas diffuser assembly 200 includes a gas diffuser manifold 210 arranged to introduce a process gas from a gas outlet 214 into a process space 215 of a substrate processing system, such as deposition system 100, in a direction
- the gas diffuser manifold 210 comprises a gas inlet 212 for providing a flow rate of the process gas 213 to the gas diffuser manifold 210, a stagnation plate 220 located in an inlet gas plenum 230 and configured to intersect with and force the process gas 213 to flow radially outward, wrap around a peripheral edge of the stagnation plate 220, and flow radially inward, and a diffusion member 240 located at an outlet of the inlet gas plenum and configured to diffuse the flow rate of the process gas 213 prior to introduction into the process space 215, wherein the diffusion member 240 comprises a plurality of openings to allow the flow rate of the process gas 213 there through.
- the diffusion member 240 may include a porous foam member, a perforated member, a plate-like member, a mesh-like member, or a screenlike member, or any combination of two or more thereof.
- the diffusion member 240 may include a porous foam member having a porosity ranging from about 5 pores per inch to about 200 pores per inch.
- the diffusion member 240 may include a porous foam member having a porosity ranging from about 10 pores per inch to about 100 pores per inch. Additionally yet, for example, the diffusion member 240 may include a porous foam member having a porosity ranging from about 10 pores per inch to about 60 pores per inch. [0039] As shown in FIG. 2, the stagnation plate 220 and the diffusion member 240 are centered on an axis of the gas inlet 212. Further, a first lateral dimension 222 of the stagnation plate 220 may exceed a second lateral dimension 242 of the diffusion member 240.
- the stagnation plate 220 and the diffusion member 240 may each include a circular plate or disc, wherein a first diameter of the stagnation plate 220 exceeds a second diameter of the diffusion member 240.
- the flow of the process gas 213 is forced to flow radially outward, wrap around a peripheral edge of the stagnation plate 220, and flow radially inward.
- the second diameter of the diffusion member 240 through which the flow of the process gas 213 passes to substrate 225, may range from about 5% to about 50% the diameter of substrate 225 being processed. Additionally, for example, the second diameter of the diffusion member 240 may range from about 10% to about 30% the diameter of substrate 225 being processed. Additionally yet, for example, the second diameter of the diffusion member 240 may range from about 15% to about 20% the diameter of substrate 225 being processed.
- the flow of the process gas 213, when flowing radially inward may flow substantially parallel to a front surface of the diffusion member 240 facing the inlet gas plenum 230 before turning to flow through the diffusion member 240.
- the exterior portion of the inlet gas plenum 230 and/or the peripheral edge of the stagnation plate 220 may be shaped, e.g., may be designed to possess smooth, round surfaces, to allow the flow of process gas 213 to flow around the stagnation plate 220 without substantial loss or separation.
- the gas diffuser assembly 200 may also include an outlet gas plenum 250 located at an outlet of the diffusion member 240.
- the outlet gas plenum 250 may include a cylindncally shaped plenum, a conically shaped plenum, or a plenum of arbitrary shape.
- a gas diffuser assembly 300 may include an outlet gas plenum 350 located at an outlet of the diffusion member 240, and an outlet gas distribution plate 360 located at an outlet of the outlet gas plenum 350.
- the outlet gas plenum 350 may include a cylindncally shaped plenum, a conically shaped plenum, or a plenum of arbitrary shape.
- the outlet gas distribution plate 360 may include a porous foam member, a perforated member, a plate-like member, a mesh-like member, or a screen-like member, or any combination of two or more thereof.
- the gas diffuser assembly (200, 300) may be designed to have a flow conductance from the gas inlet 212 to the gas outlet 214 that exceeds 10 liters per second.
- the gas diffuser assembly (200, 300) may be designed to have a flow conductance from the gas inlet 212 to the gas outlet 214 that exceeds 20 liters per second.
- the gas diffuser assembly 400 includes a gas diffuser manifold 410 having a gas inlet (not shown) and an inlet gas plenum 430.
- the gas diffuser manifold 410 may be attached to a substrate processing system, such as deposition system 100 in FIGs. 1 A through 1 C, using fasteners 434.
- the gas diffuser assembly 400 further includes a stagnation plate 420 configured to be positioned within the inlet gas plenum 430, an inlet gas plenum ring 426 configured to attach to the gas diffuser manifold 410 and further define inlet gas plenum 430, a gas diffusion member 440, and a clamp ring 442 configured to couple with the inlet gas plenum ring 426 and securely affix the diffusion member 440 there between.
- the stagnation plate 420 is attached to the gas diffuser manifold 410 using fasteners 424 and spaced away from the gas inlet using spacers 422. Additionally, the clamp ring 442 is attached to the inlet gas plenum ring 426 using fasteners 444.
- the gas diffuser assembly 400 may include an outlet gas distribution plate 460 that may be attached to the gas diffuser manifold 410 using plate ring 462 and fasteners 464.
- a bottom photograph of the gas diffuser assembly 400 without the outlet gas distribution plate 460 is provided in FIG. 5A, and a bottom photograph of the gas diffuser assembly 400 with the outlet gas distribution plate 460 is provided in FIG. 5B.
- a gas diffuser assembly 600 may include a diffusion member 640 that includes a plate-like member having a plurality of openings 642. At least one of the plurality of openings 642 may include an outlet chamfer 644 machined into an outlet side of the plate-like member. Additionally, at least one of the plurality of openings 642 may include an inlet chamfer (not shown) machined into an inlet side of the plate-like member. Furthermore, as shown in FIG.
- each of the plurality of openings 642 in the diffusion member 640 may include an outlet chamfer 644 machined into an outlet side of the plate-like member, wherein the outlet chamfer 644 for each of the plurality of openings 640 collectively merge to reduce flow recirculation zones by producing minimal surface area on the outlet side of the plate-like member that is parallel with substrate 225.
- the plurality of openings 642 may vary in size, or density, or both size and density across the diffusion member 640.
- a diffusion member 640A, 640B includes a plurality of openings 642A, 642B.
- at least one of the plurality of openings 642A, 642B in the plate-like member is centrally located and at least another of the plurality of openings 642A, 642B in the plate-like member is located off-center.
- the diameter of the centrally located opening is greater than the diameter of each opening located off-center.
- the size of the openings varies from center-to-edge.
- the substrate holder 120 comprises one or more temperature control elements 124 that may be configured for heating, or cooling, or both heating and cooling. Further, the one or more temperature control elements 124 may be arranged in more than one separately controlled temperature zones.
- the substrate holder 120 may have two thermal zones, including an inner zone and an outer zone. The temperatures of the zones may be controlled by heating or cooling the substrate holder thermal zones separately.
- the one or more temperature control elements 124 may include a substrate cooling element embedded beneath the surface of or within the substrate holder 120.
- the substrate cooling element may include a re-circulating fluid flow that receives heat from substrate holder 120 and transfers heat to a heat exchanger system.
- the one or more temperature control elements 124 may include one or more thermo-electric devices.
- the substrate holder 120 may optionally comprise a substrate clamping system (e.g., electrical or mechanical clamping system) to clamp the substrate 125 to the upper surface of substrate holder 120.
- substrate holder 120 may include an electrostatic chuck (ESC).
- ESC electrostatic chuck
- the substrate holder 120 may optionally facilitate the delivery of heat transfer gas to the back-side of substrate 125 via a backside gas supply system to improve the gas-gap thermal conductance between substrate 125 and substrate holder 120.
- a backside gas supply system can be utilized when temperature control of the substrate is required at elevated or reduced temperatures.
- the backside gas system can comprise a two- zone gas distribution system, wherein the backside gas (e.g., helium) pressure can be independently varied between the center and the edge of substrate 125.
- process chamber 1 10 may also include one or more temperature control elements that may be configured for heating, or cooling, or both heating and cooling.
- the one or more temperature control elements may be configured for heating, or cooling, or both heating and cooling.
- temperature control elements may include a wall heating element configured to elevate the temperature of the process chamber 1 10 in order to reduce condensation, which may or may not cause film formation on surfaces of the process chamber 1 10, and the accumulation of residue.
- the upper assembly 1 12 of process chamber 1 10 may also include one or more temperature control elements that may be configured for heating, or cooling, or both heating and cooling.
- the one or more temperature control elements may include a gas/vapor delivery heating element
- process chamber 1 configured to elevate the temperature of the surfaces in contact with process material, cleaning material, or purge gases, or a combination thereof introduced to process chamber 1 10.
- a temperature control system, or controller 150 may be configured to monitor, adjust, and/or control the temperature of substrate holder 120.
- the substrate holder 120 may be operated at a temperature ranging up to approximately 600 degrees C.
- the substrate holder 120 may be operated at a temperature ranging up to approximately 500 degrees C.
- the substrate holder 120 may be operated at a temperature ranging from approximately 200 degrees C to approximately 400 degrees C.
- a temperature control system, or controller 150 may be configured to monitor, adjust, and/or control the temperature of process chamber 1 10.
- the process chamber 1 10 may be operated at a temperature ranging up to approximately 400 degrees C.
- the process chamber 1 10 may be operated at a temperature ranging up to approximately 300 degrees C.
- the process chamber 1 10 may be operated at a temperature ranging from approximately 50 degrees C to approximately 200 degrees C.
- the temperature control system, or controller 150, or both may use one or more temperature measuring devices to monitor one or more temperatures, such as a temperature of substrate 125, a temperature of substrate holder 120, a temperature of process chamber 1 10, etc.
- the temperature measuring device may include an optical fiber thermometer, an optical pyrometer, a band-edge temperature measurement system as described in pending U.S. Patent Application 10/168,544, filed on July 2, 2002 and now issued as U.S. Patent No.
- thermocouple such as a K-type thermocouple.
- optical thermometers include: an optical fiber thermometer commercially available from Advanced Energys, Inc., Model No. OR2000F; an optical fiber thermometer commercially available from Luxtron Corporation, Model No. M600; or an optical fiber thermometer commercially available from Takaoka Electric Mfg., Model No. FT-1420.
- the vacuum pumping system 140 may include a dry vacuum pump, such as a turbo-molecular vacuum pump (TMP) or a cryogenic pump capable of a pumping speed up to about 5000 liters per second (and greater), coupled to process chamber 1 10 and configured to control and/or optimize a pressure in process chamber 1 10 via pumping through one or more pumping ducts 141 .
- the vacuum pumping system 140 may comprise one or more vacuum valves 142 to control the pumping speed delivered to process chamber 1 10.
- the vacuum pumping system 140 may comprise a pressure control system for monitoring, adjusting, optimizing, and/or controlling a pressure in process chamber 1 10.
- controller 150 can comprise a microprocessor, memory, and a digital I/O port capable of generating control voltages sufficient to communicate and activate inputs to the substrate processing system, such as deposition system 100, as well as monitor outputs from the substrate processing system, such as deposition system 100.
- the controller 150 may be coupled to and may exchange information with the process chamber 1 10, substrate holder 120, material delivery system 130, and vacuum pumping system 140.
- a program stored in the memory may be utilized to activate the inputs to the aforementioned components of the substrate processing system, such as deposition system 100, according to a process recipe in order to perform a deposition process, an etching process, a treatment process, and/or a cleaning process.
- controller 150 may be configured for any number of processing elements (1 10, 120, 130, 140), and the controller 150 can collect, provide, process, store, and display data from processing elements.
- Controller 150 can comprise a number of applications for controlling one or more of the processing elements.
- controller 150 may include a graphic user interface (GUI) component (not shown) that can provide easy to use interfaces that enable a user to monitor and/or control one or more processing elements.
- GUI graphic user interface
- controller 150 may be coupled to one or more additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain setup and/or configuration information from an additional controllers/computers (not shown), and controller 150 may obtain
- Controller 150 or portions of controller 150 may be locally located relative to the substrate processing system, such as deposition system 100, and/or may be remotely located relative to the substrate processing system, such as deposition system 100.
- the controller 150 may exchange data with the substrate processing system, such as deposition system 100, using at least one of a direct connection, an intranet, the Internet and a wireless connection.
- the controller 150 may be coupled to an intranet at, for example, a customer site (i.e., a device maker, etc.), or it may be coupled to an intranet at, for example, a vendor site (i.e., an equipment manufacturer). Additionally, for example, the controller 150 may be coupled to the Internet.
- controller 150 may access, for example, the controller 150 to exchange data via at least one of a direct connection, an intranet, and the Internet.
- controller 150 may exchange data with the substrate processing system, such as deposition system 100, via a wireless connection.
- hafnium oxide (HfO 2 ) films have been deposited using a deposition system, such as deposition system 100 depicted in FIGs. 1 A through 1 C, using a gas diffuser assembly such as the one depicted in FIG. 2.
- the deposition process is an ALD process having 35 cycles, wherein each cycle includes: (1 ) an introduction of Hf-containing precursor; (2) a first gas purge; (3) an introduction of an oxidizer; and (4) a second gas purge.
- FIG. 8A provides the thickness of the thin film (Angstrom, A) (solid line, solid diamonds) and the standard deviation ( ⁇ , %) (dashed line, solid squares) as a function of substrate count.
- FIG. 8B provides the particle delta ( ⁇ ) for 0.06 micron particles and larger added to each substrate as a result of the deposition process, i.e., difference in particle count between immediately following the deposition process and immediately preceding the deposition process.
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Abstract
Description
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Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014515901A JP2014518452A (en) | 2011-06-11 | 2012-06-11 | Process gas diffuser assembly for vapor deposition systems. |
| KR1020147000708A KR20140043781A (en) | 2011-06-11 | 2012-06-11 | Process gas diffuser assembly for vapor deposition system |
| US14/125,465 US20140116339A1 (en) | 2011-06-11 | 2012-06-11 | Process gas diffuser assembly for vapor deposition system |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/158,394 | 2011-06-11 | ||
| US13/158,394 US20120312234A1 (en) | 2011-06-11 | 2011-06-11 | Process gas diffuser assembly for vapor deposition system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2012173931A1 true WO2012173931A1 (en) | 2012-12-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2012/041913 Ceased WO2012173931A1 (en) | 2011-06-11 | 2012-06-11 | Process gas diffuser assembly for vapor deposition system |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20120312234A1 (en) |
| JP (1) | JP2014518452A (en) |
| KR (1) | KR20140043781A (en) |
| TW (1) | TW201303973A (en) |
| WO (1) | WO2012173931A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015046588A (en) * | 2013-07-31 | 2015-03-12 | 京セラ株式会社 | Thin film formation method and manufacturing method for solar battery element |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2937890B1 (en) * | 2014-04-22 | 2020-06-03 | Europlasma nv | Plasma coating apparatus with a plasma diffuser and method preventing discolouration of a substrate |
| US11802340B2 (en) | 2016-12-12 | 2023-10-31 | Applied Materials, Inc. | UHV in-situ cryo-cool chamber |
| JP2019019391A (en) * | 2017-07-19 | 2019-02-07 | 株式会社アルバック | Film deposition apparatus |
| JP7680361B2 (en) | 2019-03-08 | 2025-05-20 | アプライド マテリアルズ インコーポレイテッド | Porous showerhead for processing chamber - Patents.com |
| CN112853316B (en) * | 2020-12-31 | 2023-03-14 | 拓荆科技股份有限公司 | Coating device and bearing seat thereof |
| US11742185B2 (en) * | 2021-03-26 | 2023-08-29 | Applied Materials, Inc. | Uniform in situ cleaning and deposition |
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| US5105761A (en) * | 1989-10-19 | 1992-04-21 | Commissariat A L'energie Atomique | Diffusion plasma-assisted chemical treatment apparatus |
| US20020179248A1 (en) * | 2000-12-22 | 2002-12-05 | Alex Kabansky | Integrated circuit fabrication dual plasma process with separate introduction of different gases into gas flow |
| US20060060138A1 (en) * | 2004-09-20 | 2006-03-23 | Applied Materials, Inc. | Diffuser gravity support |
| US20090226614A1 (en) * | 2008-03-04 | 2009-09-10 | Tokyo Electron Limited | Porous gas heating device for a vapor deposition system |
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| EP0462730A1 (en) * | 1990-06-18 | 1991-12-27 | AT&T Corp. | Method and apparatus for forming planar integrated circuit layers |
| JPH05267176A (en) * | 1991-06-25 | 1993-10-15 | Lsi Logic Corp | Fluid diffusion head and manufacture therefor |
| US5441568A (en) * | 1994-07-15 | 1995-08-15 | Applied Materials, Inc. | Exhaust baffle for uniform gas flow pattern |
| JP2726005B2 (en) * | 1994-07-20 | 1998-03-11 | 株式会社ジーティシー | Film forming apparatus and film forming method |
| JPH11279778A (en) * | 1998-03-30 | 1999-10-12 | Seiko Epson Corp | Etching apparatus and method for manufacturing semiconductor device |
| JP2000173927A (en) * | 1998-12-02 | 2000-06-23 | Sony Corp | Parallel plate type CVD film forming apparatus and film forming method |
| JP2004047631A (en) * | 2002-07-10 | 2004-02-12 | Shibaura Mechatronics Corp | Plasma processing equipment |
| JP4352783B2 (en) * | 2002-08-23 | 2009-10-28 | 東京エレクトロン株式会社 | Gas supply system and processing system |
| US7273526B2 (en) * | 2004-04-15 | 2007-09-25 | Asm Japan K.K. | Thin-film deposition apparatus |
| TWI287279B (en) * | 2004-09-20 | 2007-09-21 | Applied Materials Inc | Diffuser gravity support |
| US7708835B2 (en) * | 2004-11-29 | 2010-05-04 | Tokyo Electron Limited | Film precursor tray for use in a film precursor evaporation system and method of using |
| US8034176B2 (en) * | 2006-03-28 | 2011-10-11 | Tokyo Electron Limited | Gas distribution system for a post-etch treatment system |
| US7476291B2 (en) * | 2006-09-28 | 2009-01-13 | Lam Research Corporation | High chamber temperature process and chamber design for photo-resist stripping and post-metal etch passivation |
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-
2011
- 2011-06-11 US US13/158,394 patent/US20120312234A1/en not_active Abandoned
-
2012
- 2012-05-21 TW TW101118046A patent/TW201303973A/en unknown
- 2012-06-11 KR KR1020147000708A patent/KR20140043781A/en not_active Withdrawn
- 2012-06-11 WO PCT/US2012/041913 patent/WO2012173931A1/en not_active Ceased
- 2012-06-11 JP JP2014515901A patent/JP2014518452A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5105761A (en) * | 1989-10-19 | 1992-04-21 | Commissariat A L'energie Atomique | Diffusion plasma-assisted chemical treatment apparatus |
| US20020179248A1 (en) * | 2000-12-22 | 2002-12-05 | Alex Kabansky | Integrated circuit fabrication dual plasma process with separate introduction of different gases into gas flow |
| US20060060138A1 (en) * | 2004-09-20 | 2006-03-23 | Applied Materials, Inc. | Diffuser gravity support |
| US20090226614A1 (en) * | 2008-03-04 | 2009-09-10 | Tokyo Electron Limited | Porous gas heating device for a vapor deposition system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015046588A (en) * | 2013-07-31 | 2015-03-12 | 京セラ株式会社 | Thin film formation method and manufacturing method for solar battery element |
Also Published As
| Publication number | Publication date |
|---|---|
| TW201303973A (en) | 2013-01-16 |
| KR20140043781A (en) | 2014-04-10 |
| JP2014518452A (en) | 2014-07-28 |
| US20120312234A1 (en) | 2012-12-13 |
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