WO2011123217A2 - Silicon-ozone cvd with reduced pattern loading using incubation period deposition - Google Patents

Silicon-ozone cvd with reduced pattern loading using incubation period deposition Download PDF

Info

Publication number
WO2011123217A2
WO2011123217A2 PCT/US2011/027246 US2011027246W WO2011123217A2 WO 2011123217 A2 WO2011123217 A2 WO 2011123217A2 US 2011027246 W US2011027246 W US 2011027246W WO 2011123217 A2 WO2011123217 A2 WO 2011123217A2
Authority
WO
WIPO (PCT)
Prior art keywords
incubation period
silicon
silicon oxide
deposition
patterned
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.)
Ceased
Application number
PCT/US2011/027246
Other languages
French (fr)
Other versions
WO2011123217A3 (en
Inventor
Sasha Kweskin
Paul Edward Gee
Shankar Venkataraman
Kedar Sapre
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Applied Materials Inc
Original Assignee
Applied Materials Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Applied Materials Inc filed Critical Applied Materials Inc
Publication of WO2011123217A2 publication Critical patent/WO2011123217A2/en
Publication of WO2011123217A3 publication Critical patent/WO2011123217A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10PGENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
    • H10P14/00Formation of materials, e.g. in the shape of layers or pillars
    • H10P14/60Formation of materials, e.g. in the shape of layers or pillars of insulating materials
    • H10P14/69Inorganic materials
    • H10P14/692Inorganic materials composed of oxides, glassy oxides or oxide-based glasses
    • H10P14/6921Inorganic materials composed of oxides, glassy oxides or oxide-based glasses containing silicon
    • H10P14/69215Inorganic materials composed of oxides, glassy oxides or oxide-based glasses containing silicon the material being a silicon oxide, e.g. SiO2
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical 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 deposition of inorganic material, other than metallic material
    • C23C16/30Deposition of compounds, mixtures or solid solutions, e.g. borides, carbides, nitrides
    • C23C16/40Oxides
    • C23C16/401Oxides containing silicon
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical 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
    • C23C16/455Chemical 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
    • C23C16/45523Pulsed gas flow or change of composition over time
    • HELECTRICITY
    • H10SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
    • H10PGENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
    • H10P14/00Formation of materials, e.g. in the shape of layers or pillars
    • H10P14/60Formation of materials, e.g. in the shape of layers or pillars of insulating materials
    • H10P14/63Formation of materials, e.g. in the shape of layers or pillars of insulating materials characterised by the formation processes
    • H10P14/6326Deposition processes
    • H10P14/6328Deposition from the gas or vapour phase
    • H10P14/6334Deposition from the gas or vapour phase using decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition
    • H10P14/6339Deposition from the gas or vapour phase using decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition deposition by cyclic CVD, e.g. ALD, ALE or pulsed CVD

Definitions

  • This application relates to manufacturing technology solutions involving equipment, processes, and materials used in the deposition, patterning, and treatment of thin-films and coatings, with representative examples including (but not limited to) applications involving: semiconductor and dielectric materials and devices, silicon-based wafers and flat panel displays (such as TFTs).
  • Forming dielectric layers on a substrate by chemical reaction of gases is one of the primary steps in the fabrication of modern semiconductor devices. These deposition processes include chemical vapor deposition (CVD) as well as plasma enhanced chemical vapor deposition (PECVD), which uses plasma in combination with traditional CVD techniques.
  • CVD chemical vapor deposition
  • PECVD plasma enhanced chemical vapor deposition
  • CVD and PECVD dielectric layers can be used as different layers in semiconductor devices.
  • the dielectric layers may be used as intermetal dielectric layers between conductive lines or interconnects in a device.
  • the dielectric layers may be used as barrier layers, etch stops, or spacers, as well as other layers.
  • Dielectric layers that are used for applications such as barrier layers and spacers are typically deposited over features, e.g., horizontal interconnects for subsequently formed lines, vertical interconnects (vias), gate stacks, etc., in a patterned substrate.
  • the deposition provides a conformal layer.
  • the barrier layer material may overloaf, that is, deposit excess material on the shoulders of a via and deposit too little material in the base of the via, forming a shape that looks like the side of a loaf of bread.
  • the phenomena is also known as footing because the base of the via has a profile that looks like a foot.
  • the shoulders of a via may merge to form a joined, sealed surface across the top of the via.
  • the film thickness non-uniformity across the wafer can negatively impact the drive current improvement from one device to another. Modulating the process parameters alone does not significantly improve the step coverage and pattern loading problems.
  • aspects of the disclosure pertain to methods of depositing conformal silicon oxide layers on patterned substrates.
  • dielectric layers are deposited by flowing a silicon- containing precursor and ozone into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface having
  • heterogeneous materials and/or a heterogeneous pattern density distribution may have a reduced dependence on underlying material and pattern density while still being suitable for non-sacrificial applications. Reduction in dependence on pattern density is achieved by terminating deposition near the end of an incubation period. Multiple deposition cycles may be conducted in series since the beneficial nature of the incubation period may repeat after a pause in deposition.
  • Embodiments of the invention include methods for forming a conformal silicon oxide layer on a patterned substrate in a substrate processing region in a processing chamber.
  • the methods include a step of depositing a layer of silicon oxide during an incubation period.
  • the step includes initiating flows of a silicon-containing precursor and ozone (0 3 ) into the substrate processing region, and terminating the flows of the silicon-containing precursor and ozone near the end of the incubation period to avoid the formation of a nonconformal layer of silicon oxide.
  • FIG. 1A-1B are flow charts of a conformal silicon oxide deposition process according to disclosed embodiments.
  • FIG. 2 A is a graph of silicon oxide growth rates according to embodiments of the invention.
  • FIG. 2B is a graph of silicon oxide growth rate selectivity according to embodiments of the invention.
  • FIG. 3 shows a substrate processing system according to embodiments of the invention.
  • FIG. 4 A shows is a cross-sectional view of a semiconductor processing chamber according to embodiments of the present invention.
  • FIG. 4B shows a cross-sectional view of a gas panel and supply lines in relation to a processing chamber.
  • DETAILED DESCRIPTION OF THE INVENTION Aspects of the disclosure pertain to methods of depositing conformal silicon oxide layers on patterned substrates.
  • dielectric layers are deposited by flowing a silicon- containing precursor and ozone into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface having
  • heterogeneous materials and/or a heterogeneous pattern density distribution may have a reduced dependence on underlying material and pattern density while still being suitable for non-sacrificial applications. Reduction in dependence on pattern density is achieved by terminating deposition near the end of an incubation period. Multiple deposition cycles may be conducted in series since the beneficial nature of the incubation period may repeat after a pause in deposition.
  • Embodiments of the invention are directed to methods of forming silicon oxide on a patterned surface of a substrate.
  • Sub-atmospheric CVD (SACVD) and related processes involve flowing a silicon-containing precursor and an oxidizing precursor into a processing chamber to form silicon oxide on the substrate.
  • the silicon-containing precursor may include TEOS and the oxidizing precursor may include ozone (0 3 ), oxygen (0 2 ) and/or oxygen radicals.
  • TEOS TEOS
  • the oxidizing precursor may include ozone (0 3 ), oxygen (0 2 ) and/or oxygen radicals.
  • PLE pattern-loading effect
  • FIGS. 1A-1B are flow charts of a conformal silicon oxide deposition process according to disclosed embodiments.
  • FIGS. 2A-2B Properties of silicon oxide growth rates under various circumstances are shown in FIGS. 2A-2B to enhance the understanding of the silicon oxide deposition process.
  • the process 100 in FIG 1A begins when a patterned substrate is transferred into a substrate processing region (operation 110). TEOS and ozone flows are initiated into the region in operation 120 and a conformal layer of silicon oxide is formed between operation 120 and operation 130. The flows of both ozone and TEOS and ozone are terminated in operation 130.
  • FIG 2 A shows how the growth rate remains comparable during the period of deposition represented in FIG. 1 A.
  • the silicon oxide deposition growth rate accelerates after the incubation period on exposed regions of silicon compared to exposed regions of silicon oxide.
  • the vertical dashed line roughly indicates the point when the conformal deposition ends and the selective deposition begins in this exemplary embodiment.
  • the flow of TEOS is generally effected by flowing a carrier gas (e.g. N 2 ) through liquid TEOS such that the delivery rate of TEOS into the substrate processing region is above one of 1 g/min, 2 g/min or 3 g/min, in different embodiments. Both the carrier gas and the TEOS enter the substrate processing region.
  • the flow of ozone is delivered along with more stable molecular oxygen. The flow rate of the ozone portion of that flow is above one of 1 slm, 2 slm, 3 slm, 5 slm or 10 slm, in different embodiments.
  • the initiation of the TEOS and ozone flows is followed by a period of slow growth and then a period of more rapid growth as represented in FIG. 2A.
  • the process sequence shown in FIG. 1A interrupts (operation 130) the typical growth pattern near the transition from slow growth to rapid growth. If the typical growth pattern were interrupted earlier in the incubation period or too long after the transition to rapid growth, the conformality of the silicon oxide film would be reduced.
  • An average deposition rate for each region may be defined by using the slope of a line drawn between the start and finish points on a plot of the deposited thickness vs. the time since initial deposition.
  • the location of operation 130 along the time axis is somewhat flexible while still offering the benefits of conformality.
  • the period of slow growth before operation 130 will be referred to as the incubation period herein.
  • the deposition rate during the incubation period may exceed the deposition rate after the incubation period by a multiplicative factor of one of 1.3, 1.5, 1.7, 2.0, 2.5 or 3.0, in different embodiments.
  • the deposition rate of silicon oxide between operation 120 and operation 130 may be greater than 5 ⁇ , 7 ⁇ , 8 ⁇ , 9 ⁇ , ⁇ or 110 A, in different embodiments.
  • the thickness of the conformal silicon oxide layer grown over one material e.g. thermal silicon oxide
  • Flow rates are not necessarily constant during the process. Flow rates of the different precursors may be initiated and terminated in different orders and their magnitudes may be varied. Unless otherwise indicated, mass flow rate magnitudes indicated herein are given for the approximate peak flow rate used during the process. Flow rate magnitudes indicated herein are for deposition on one side of a pair of 300 mm diameter wafers (area approximately 1400 cm 2 ). Appropriate correction based on deposition area is needed for a different number of wafers, larger or smaller wafers, double sided deposition or deposition on alternative geometry substrates (e.g. rectangular substrates).
  • the pressure in the substrate processing region are typical of many SACVD and HARP processes (e.g. 600 Torr).
  • the pressure during the formation of the conformal silicon oxide film may be greater than one of 350 Torr, 400 Torr, 450 Torr, 500 Torr or 550 Torr, in different embodiments, to ensure desirable growth rates during the incubation period.
  • SACVD sub-atmospheric chemical vapor deposition
  • the substrate temperature is below a threshold value, in embodiments, also to stay within tight thermal budgets and to ensure that the deposition process possesses an incubation period.
  • the temperature of the substrate during the deposition of the conformal silicon oxide is below one of 540°C, 500°C, 450°C, 400°C and 350°C, in different embodiments.
  • No plasma is present in the substrate processing region in embodiments.
  • a small ac and/or dc voltage may be applied to the substrate processing region without detriment to the benefits of the deposition process, according to embodiments. Such an excitation should not be considered to deviate from the scope of "essentially” plasma-free or a process having "essentially” no plasma as may be recited in some claims.
  • FIG. 2B shows the dependence of silicon oxide growth selectivity as a function of silicon oxide film thickness and incubation deposition cycle.
  • the process 150 begins when a when a patterned substrate is transferred into a substrate processing region (operation 160). TEOS and ozone flows are initiated then terminated near the end of the incubation period as described previously. The initiation, film growth and termination of the flows occur within operation 170 in FIG. IB. If the target thickness has been achieved, no additional cycles are performed and the patterned substrate may be removed from the substrate processing region (operation 180). However, if a larger film thickness is desired, the flows of TEOS and ozone may be started again which will result in another incubation period.
  • the second incubation period may last for a shorter period of time than the first but will again segue into a period of more selective growth after an incubation period.
  • the flows of TEOS and ozone are terminated near the transition from slow to rapid growth on exposed silicon surfaces.
  • the process may even repeat more than two times if additional film thickness is required.
  • FIG. 2B shows that the selectivity becomes even more conformal during subsequent cycles and stays more conformal for larger film thicknesses. This provides an additional benefit when conformal deposition is desired. Deposition sequences have been explored including six incubation cycles and resulted in conformal films nearly 600A thick.
  • the flexibility provided by choosing a number for the multiple cycles in combination with adjusting the timing of the termination of one or both of the TEOS and ozone flows allows flexibility for achieving a desired silicon oxide film thickness.
  • the thickness of the secondary layers described with reference to FIG. IB may be greater than the same lower limits described with reference to the layer grown and described with reference to FIG. 1 A.
  • the pattern loading was quantified by comparing the horizontal growth of the conformal silicon oxide layer from a vertical feature in a sparsely patterned region and a densely patterned region.
  • An exemplary densely patterned region may have greater number of features than a sparsely patterned region to create the greater exposed surface area within a same area viewed from above the patterned substrate.
  • a densely patterned region may have an exposed vertical area greater than a sparsely patterned region by a factor greater than one of 2, 3, 5, 10 or 20, in different embodiments.
  • the thickness of the conformal silicon oxide layer in a densely patterned region may be within one of 30%, 25%, 20%>, 15%, 10% and 5% of the thickness of the conformal silicon oxide layer in a sparsely patterned region, in different embodiments.
  • the thickness in each region may be measured on vertical surfaces in which case the growth is in a horizontal direction. Alternatively, the thickness may be measured on a horizontal surface within each region and the growth may then be in the vertical direction.
  • the terms “vertical” and “horizontal” are used throughout to include substantially vertical and substantially horizontal directions which may or may not deviate from the theoretical vertical and horizontal by up to about 10 degrees.
  • Deposition chambers may include sub-atmospheric chemical vapor deposition (SACVD) chambers and more generally, deposition chambers which allow operation at relatively high pressures without necessarily applying plasma excitation.
  • SACVD chemical vapor deposition
  • Specific examples of CVD systems that may implement embodiments of the invention include the CENTURA ULTIMA® SACVD chambers/systems, and PRODUCER® HARP, eHARP and SACVD chambers/systems, available from Applied Materials, Inc. of Santa Clara, Calif.
  • Embodiments of the deposition systems may be incorporated into larger fabrication systems for producing integrated circuit chips.
  • FIG. 4 shows one such system 200 of deposition, baking and curing chambers according to disclosed embodiments.
  • a pair of FOUPs (front opening unified pods) 202 supply substrate substrates (e.g., 300 mm diameter wafers) that are received by robotic arms 204 and placed into a low pressure holding area 206 before being placed into one of the wafer processing chambers 208a-f.
  • a second robotic arm 210 may be used to transport the substrate wafers from the holding area 206 to the processing chambers 208a-f and back.
  • the processing chambers 208a-f may include one or more system components for depositing, annealing, curing and/or etching a flowable dielectric film on the substrate wafer.
  • two pairs of the processing chamber e.g., 208c-d and 208e-f
  • the third pair of processing chambers e.g., 208a-b
  • the same two pairs of processing chambers may be configured to both deposit and anneal a flowable dielectric film on the substrate, while the third pair of chambers (e.g., 208a-b) may be used for UV or E-beam curing of the deposited film.
  • all three pairs of chambers e.g., 208a-f may be configured to deposit and cure a flowable dielectric film on the substrate.
  • two pairs of processing chambers may be used for both deposition and UV or E-beam curing of the flowable dielectric, while a third pair of processing chambers (e.g. 208a-b) may be used for annealing the dielectric film.
  • Any one or more of the processes described may be carried out on chamber(s) separated from the fabrication system shown in different embodiments.
  • FIG. 4 A shows a simplified representation of an exemplary semiconductor processing chamber within a semiconductor processing tool 200.
  • This exemplary chamber 410 is suitable for performing a variety of semiconductor processing steps which may include CVD processes, as well as other processes, such as reflow, drive-in, cleaning, etching, and gettering processes. Multiple-step processes can also be performed on a single substrate without removing the substrate from the chamber.
  • Representative major components of the system include a chamber interior 415 that receives process and other gases from a gas delivery system 489, pumping system 488, a remote plasma system (RPS) 455, and a control system 453. These and other components are described below in order to understand the present invention.
  • RPS remote plasma system
  • the semiconductor processing chamber 410 includes an enclosure assembly 412 housing a chamber interior 415 with a gas reaction area 416.
  • a gas distribution plate 420 is provided above the gas reaction area 416 for dispersing reactive gases and other gases, such as purge gases, through perforated holes in the gas distribution plate 420 to a substrate (not shown) that rests on a vertically movable heater 425 (which may also be referred to as a substrate support pedestal).
  • the heater 425 can be controllably moved between a lower position, where a substrate can be loaded or unloaded, for example, and a processing position closely adjacent to the gas distribution plate 420, indicated by a dashed line 413, or to other positions for other purposes, such as for an etch or cleaning process.
  • a center board (not shown) includes sensors for providing information on the position of the substrate.
  • Gas distribution plate 420 may be of the variety described in U.S. Patent No. 6,793,733. These plates improve the uniformity of gas disbursement at the substrate and are particularly advantageous in deposition processes that vary gas concentration ratios.
  • the plates work in combination with the vertically movable heater 425 (or movable substrate support pedestal) such that deposition gases are released farther from the substrate when the ratio is heavily skewed in one direction (e.g., when the concentration of a silicon-containing gas is small compared to the concentration of an oxidizer-containing gas) and are released closer to the substrate as the concentration changes (e.g., when the concentration of silicon-containing gas in the mixture is higher).
  • the orifices of the gas distribution plate are designed to provide more uniform mixing of the gases.
  • the heater 425 includes an electrically resistive heating element (not shown) enclosed in a ceramic.
  • the ceramic protects the heating element from potentially corrosive chamber environments and allows the heater to attain temperatures up to about 800°C.
  • all surfaces of the heater 425 exposed within the chamber interior 415 are made of a ceramic material, such as aluminum oxide ( ⁇ 1 2 0 3 or alumina) or aluminum nitride .
  • Reactive and carrier gases are supplied through inlet tube 443 into a gas mixing box (also called a gas mixing block) 427, where they are preferably mixed together and delivered to the gas distribution plate 420.
  • the gas mixing block 427 is preferably a dual input mixing block coupled to inlet tube 443 and to a cleaning/etch gas conduit 447.
  • a valve 428 operates to admit or seal gas or plasma from conduit 447 to the gas mixing block 427.
  • Conduit 447 receives gases from an RPS 455, which has an inlet 457 for receiving input gases.
  • gas supplied to the plate 420 is vented toward the substrate surface (as indicated by arrows 421), where it may be uniformly distributed radially across the substrate surface, typically in a laminar flow.
  • Purging gas may be delivered into the chamber interior 415 through the plate 420 and/or an inlet port or tube (not shown) through a wall (preferably the bottom) of enclosure assembly 412.
  • the purging gas flows upward from the inlet port past the heater 425 and to an annular pumping channel 440 and may be useful to purge the chamber, for example, of ozone and TEOS between incubation period depositions.
  • An exhaust system then exhausts the gas (as indicated by arrow 422) into the annular pumping channel 440 and through an exhaust line 460 to a pumping system 488, which includes one or more vacuum pumps. Exhaust gases and entrained particles are drawn from the annular pumping channel 440 through the exhaust line 460 at a rate controlled by a throttle valve system 463.
  • the RPS 455 can produce a plasma for selected applications, such as chamber cleaning or etching native oxide or residue from a process substrate.
  • Plasma species produced in the remote plasma system 455 from precursors supplied via the input line 457 are sent via conduit 447 for dispersion through the plate 420 to the gas reaction area 416.
  • Precursor gases for a cleaning application may include fluorine, chlorine, and other reactive elements.
  • the RPS 455 also may be adapted to deposit plasma enhanced CVD films by selecting appropriate deposition precursor gases for use in the RPS 455.
  • the system controller 453 controls activities and operating parameters of the deposition system.
  • the processor 451 executes system control software, such as a computer program stored in a memory 452 coupled to the processor 451.
  • the memory 452 typically consists of a combination of static random access memories (cache), dynamic random access memories (DRAM) and hard disk drives but of course the memory 452 may also consist of other kinds of memory, such as solid-state memory devices.
  • the semiconductor processing chamber 410 in a preferred embodiment includes a removable storage media drive, USB ports and a card rack (not shown).
  • the processor 451 operates according to system control software programmed to operate the device according to the methods disclosed herein. For example, sets of instructions may dictate the timing, mixture of gases, chamber pressure, chamber temperature, plasma power levels, susceptor position, and other parameters for carrying out one or more incubation period depositions in a sequence.
  • the instructions are conveyed to the appropriate hardware preferably through direct cabling carrying analog or digital signals conveying signals originating from an input-output I/O module 450.
  • Other computer programs such as those stored on other memory including, for example, a USB thumb drive, a floppy disk or another computer program product inserted in a disk drive or other appropriate drive, may also be used to operate the processor 451 to configure the semiconductor processing chamber 410 for varied uses.
  • the processor 451 may have a card rack (not shown) that contains a single -board computer, analog and digital input/output boards, interface boards and stepper motor controller boards.
  • Various parts of the semiconductor processing system 200 conform to the Versa Modular European (VME) standard which defines board, card cage, and connector dimensions and types.
  • VME Versa Modular European
  • the VME standard also defines the bus structure having a 16-bit data bus and 24-bit address bus.
  • a process for depositing a conformal silicon oxide layer on a patterned substrate or a process for cleaning a chamber can be implemented using a computer program product that is executed by the system controller.
  • the computer program code can be written in any conventional computer readable programming language: for example, 68000 assembly language, C, C++, Pascal, Fortran or others. Suitable program code is entered into a single file, or multiple files, using a conventional text editor, and stored or embodied in a computer usable medium, such as a memory system of the computer. If the entered code text is in a high level language, the code is compiled, and the resultant compiler code is then linked with an object code of precompiled Microsoft Windows® library routines. To execute the linked, compiled object code the system user invokes the object code, causing the computer system to load the code in memory. The CPU then reads and executes the code to perform the tasks identified in the program.
  • the interface between a user and the controller is via a flat-panel touch-sensitive monitor.
  • two monitors are used, one mounted in the clean room wall for the operators and the other behind the wall for the service technicians.
  • the two monitors may simultaneously display the same information, in which case only one accepts input at a time.
  • the operator touches a designated area of the touch-sensitive monitor.
  • the touched area changes its highlighted color, or a new menu or screen is displayed, confirming communication between the operator and the touch- sensitive monitor.
  • Other devices such as a keyboard, mouse, or other pointing or communication device, may be used instead of or in addition to the touch-sensitive monitor to allow the user to communicate with the system controller.
  • the embodiment disclosed herein relies on direct cabling and a single processor 451.
  • Fig. 4B shows a simplified representation of a gas supply panel 480 in relation to semiconductor processing chamber 410.
  • the portion of semiconductor processing system 200 shown includes semiconductor processing chamber 410 with a heater 425, a gas mixing box 427 with inputs from inlet tube 443 and conduit 447, and RPS 455 with input line 457.
  • the gas mixing box 427 is configured for mixing and injecting deposition gas(es) and cleaning gas(es) or other gas(es) through inlet tube 443 and the input line 457 to the chamber interior 415.
  • the RPS 455 is integrally located and mounted below the processing chamber 410 with conduit 447 coming up alongside the chamber 410 to the gate valve 428 and the gas mixing box 427, located above the chamber 410.
  • Plasma power generator 411 and ozonator 459 are located remote from the clean room. Delivery lines 483 and 485 from the gas supply panel 480 provide reactive gases to inlet tube 443.
  • the gas supply panel 480 includes lines from gas or liquid sources 490 that provide the process gases for the selected application.
  • the gas supply panel 480 has mixing system 493 that mixes selected gases before flow to the gas mixing box 427.
  • mixing system 493 includes a liquid injection system for vaporizing one or more reactant liquids such as tetraethylorthosilicate ("TEOS”), triethylborate (“TEB”), and triethylphosphate (“TEPO"). Vapor from the liquids is usually combined with a carrier gas, such as helium.
  • TEOS tetraethylorthosilicate
  • TEB triethylborate
  • TEPO triethylphosphate
  • Supply lines for the process gases may include (i) shut-off valves 495 that can be used to automatically or manually shut off the flow of process gas into line 485 or line 457, and (ii) liquid flow meters (LFM) 401 or other types of controllers that measure the flow of gas or liquid through the supply lines.
  • shut-off valves 495 that can be used to automatically or manually shut off the flow of process gas into line 485 or line 457
  • liquid flow meters (LFM) 401 or other types of controllers that measure the flow of gas or liquid through the supply lines.
  • a mixture including TEOS as a silicon source may be used with mixing system 493 in a deposition process for forming a silicon oxide film during an incubation period.
  • Sources of dopants such as phosphorous and boron may include TEPO and TEB which may also be introduced to mixing system 493.
  • Precursors delivered to mixing system 493 may be liquid at room temperature and pressure and may be vaporized by conventional boiler-type or bubbler-type hot boxes.
  • a liquid injection system may be used and offers greater control of the volume of reactant liquid introduced into the gas mixing system. The liquid is typically injected as a fine spray or mist into the carrier gas flow before being delivered to a heated gas delivery line 485 to the gas mixing block and chamber.
  • Oxygen (0 2 ) and ozone (0 3 ) flow to the chamber through another gas delivery line 483, to be combined with the reactant gases from heated gas delivery line 485 near or in the chamber.
  • gas delivery line 483 may also be used.
  • line 485 may actually comprise multiple lines separated to discourage inter-precursor reactions before the precursors are flowed into chamber interior 415.
  • substrate may be a support substrate with or without layers formed thereon.
  • the support substrate may be an insulator or a semiconductor of a variety of doping concentrations and profiles and may, for example, be a semiconductor substrate of the type used in the manufacture of integrated circuits.
  • a layer of "silicon oxide” may include minority concentrations of other elemental constituents such as nitrogen, hydrogen, carbon and the like.
  • a gas may be a combination of two or more gases.
  • trench and gap are used throughout with no implication that the etched geometry necessarily has a large horizontal aspect ratio. Viewed from above the surface, gaps may appear circular, oval, polygonal, rectangular, or a variety of other shapes.
  • Gaps may also be a region between two pillars in which case the gaps are not physical separate from other gaps.
  • a conformal layer refers to a generally uniform layer of material on a surface in the same shape as the surface, i.e., the surface of the layer and the surface being covered are generally parallel. A person having ordinary skill in the art will recognize that the deposited material likely cannot be 100% conformal and thus the term "generally" allows for acceptable tolerances.

Landscapes

  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Formation Of Insulating Films (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

Aspects of the disclosure pertain to methods of depositing conformal silicon oxide layers on patterned substrates. In embodiments, dielectric layers are deposited by flowing a silicon-containing precursor and ozone into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface having heterogeneous materials and/or a heterogeneous pattern density distribution. The deposition of dielectric layers grown according to embodiments may have a reduced dependence on underlying material and pattern density while still being suitable for non-sacrificial applications. Reduction in dependence on pattern density is achieved by terminating deposition near the end of an incubation period. Multiple deposition cycles may be conducted in series since the beneficial nature of the incubation period may repeat after a pause in deposition.

Description

SILICON-OZONE CVD WITH REDUCED PATTERN LOADING USING INCUBATION PERIOD DEPOSITION
CROSS-REFERENCES TO RELATED APPLICATIONS This application is a PCT application of U.S. Patent Application No. 12/891,149 filed September 27, 2010, titled "SILICON-OZONE CVD WITH REDUCED PATTERN
LOADING USING INCUBATION PERIOD DEPOSITION," and claims the benefit of U.S. Provisional Application No. 61/319,970 by Kweskin et al, filed April 1, 2010 and titled "SILICON-OZONE CVD WITH REDUCED PATTERN LOADING USING
INCUBATION PERIOD DEPOSITION," which are incorporated herein in their entirety for all purposes.
FIELD
This application relates to manufacturing technology solutions involving equipment, processes, and materials used in the deposition, patterning, and treatment of thin-films and coatings, with representative examples including (but not limited to) applications involving: semiconductor and dielectric materials and devices, silicon-based wafers and flat panel displays (such as TFTs).
BACKGROUND OF THE INVENTION
Forming dielectric layers on a substrate by chemical reaction of gases is one of the primary steps in the fabrication of modern semiconductor devices. These deposition processes include chemical vapor deposition (CVD) as well as plasma enhanced chemical vapor deposition (PECVD), which uses plasma in combination with traditional CVD techniques.
CVD and PECVD dielectric layers can be used as different layers in semiconductor devices. For example, the dielectric layers may be used as intermetal dielectric layers between conductive lines or interconnects in a device. Alternatively, the dielectric layers may be used as barrier layers, etch stops, or spacers, as well as other layers.
Dielectric layers that are used for applications such as barrier layers and spacers are typically deposited over features, e.g., horizontal interconnects for subsequently formed lines, vertical interconnects (vias), gate stacks, etc., in a patterned substrate. Preferably, the deposition provides a conformal layer. However, it is often difficult to achieve conformal deposition.
For example, it is difficult to deposit a barrier layer over a feature with few or no resulting surface defects or feature deformation. During deposition, the barrier layer material may overloaf, that is, deposit excess material on the shoulders of a via and deposit too little material in the base of the via, forming a shape that looks like the side of a loaf of bread. The phenomena is also known as footing because the base of the via has a profile that looks like a foot. In extreme cases, the shoulders of a via may merge to form a joined, sealed surface across the top of the via. The film thickness non-uniformity across the wafer can negatively impact the drive current improvement from one device to another. Modulating the process parameters alone does not significantly improve the step coverage and pattern loading problems.
Deposition of conformal layers over gate stacks to provide layers that are subsequently etched to form spacers is also challenging. While methods of depositing silicon nitride and silicon oxide layers for spacers using high temperature, low pressure conventional CVD have been developed, the thermal budget for such techniques is becoming too high as semiconductor device geometry continues to shrink. PECVD processes of silicon nitride and silicon oxide deposition can be performed at lower temperatures, but the step coverage and pattern loading results are not as desirable as those obtained with high temperature, low pressure CVD.
Therefore, a need exists for method of depositing conformal films over formed features in a patterned substrate.
BRIEF SUMMARY OF THE INVENTION
Aspects of the disclosure pertain to methods of depositing conformal silicon oxide layers on patterned substrates. In embodiments, dielectric layers are deposited by flowing a silicon- containing precursor and ozone into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface having
heterogeneous materials and/or a heterogeneous pattern density distribution. The deposition of dielectric layers grown according to embodiments may have a reduced dependence on underlying material and pattern density while still being suitable for non-sacrificial applications. Reduction in dependence on pattern density is achieved by terminating deposition near the end of an incubation period. Multiple deposition cycles may be conducted in series since the beneficial nature of the incubation period may repeat after a pause in deposition.
Embodiments of the invention include methods for forming a conformal silicon oxide layer on a patterned substrate in a substrate processing region in a processing chamber. The methods include a step of depositing a layer of silicon oxide during an incubation period. The step includes initiating flows of a silicon-containing precursor and ozone (03) into the substrate processing region, and terminating the flows of the silicon-containing precursor and ozone near the end of the incubation period to avoid the formation of a nonconformal layer of silicon oxide. Additional embodiments and features are set forth in part in the description that follows, and in part will become apparent to those skilled in the art upon examination of the specification or may be learned by the practice of the disclosed embodiments. The features and advantages of the disclosed embodiments may be realized and attained by means of the instrumentalities, combinations, and methods described in the specification. BRIEF DESCRIPTION OF THE DRAWINGS
A further understanding of the nature and advantages of the disclosed embodiments may be realized by reference to the remaining portions of the specification and the drawings.
FIG. 1A-1B are flow charts of a conformal silicon oxide deposition process according to disclosed embodiments. FIG. 2 A is a graph of silicon oxide growth rates according to embodiments of the invention.
FIG. 2B is a graph of silicon oxide growth rate selectivity according to embodiments of the invention.
FIG. 3 shows a substrate processing system according to embodiments of the invention.
FIG. 4 A shows is a cross-sectional view of a semiconductor processing chamber according to embodiments of the present invention;
FIG. 4B shows a cross-sectional view of a gas panel and supply lines in relation to a processing chamber. DETAILED DESCRIPTION OF THE INVENTION Aspects of the disclosure pertain to methods of depositing conformal silicon oxide layers on patterned substrates. In embodiments, dielectric layers are deposited by flowing a silicon- containing precursor and ozone into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface having
heterogeneous materials and/or a heterogeneous pattern density distribution. The deposition of dielectric layers grown according to embodiments may have a reduced dependence on underlying material and pattern density while still being suitable for non-sacrificial applications. Reduction in dependence on pattern density is achieved by terminating deposition near the end of an incubation period. Multiple deposition cycles may be conducted in series since the beneficial nature of the incubation period may repeat after a pause in deposition.
Embodiments of the invention are directed to methods of forming silicon oxide on a patterned surface of a substrate. Sub-atmospheric CVD (SACVD) and related processes involve flowing a silicon-containing precursor and an oxidizing precursor into a processing chamber to form silicon oxide on the substrate. The silicon-containing precursor may include TEOS and the oxidizing precursor may include ozone (03), oxygen (02) and/or oxygen radicals. The inventors have discovered that growing thin films within the incubation period of the process reduces the pattern-loading effect (PLE) of the deposited silicon oxide.
Without binding the claim coverage to hypothetical mechanisms, it is believed that a non- conformal film may initially be created early during the incubation period. Later in the incubation period, the thin portions of the film are thought to experience more rapid growth rates while the thicker portions of the film support less rapid growth rates. The effect is to even out the film thickness across the wafer and between different patterned structures. The inventors have also found that the growth rates during the incubation period are less selective, meaning the film growth rate is more similar from one material to another during the period. The non-selectivity helps to further improve conformality across the wafer and between different patterned structures. In order to better understand and appreciate the invention, reference is now made to FIGS. 1A-1B which are flow charts of a conformal silicon oxide deposition process according to disclosed embodiments. Properties of silicon oxide growth rates under various circumstances are shown in FIGS. 2A-2B to enhance the understanding of the silicon oxide deposition process. The process 100 in FIG 1A begins when a patterned substrate is transferred into a substrate processing region (operation 110). TEOS and ozone flows are initiated into the region in operation 120 and a conformal layer of silicon oxide is formed between operation 120 and operation 130. The flows of both ozone and TEOS and ozone are terminated in operation 130. FIG 2 A shows how the growth rate remains comparable during the period of deposition represented in FIG. 1 A. The silicon oxide deposition growth rate accelerates after the incubation period on exposed regions of silicon compared to exposed regions of silicon oxide. The vertical dashed line roughly indicates the point when the conformal deposition ends and the selective deposition begins in this exemplary embodiment.
Generally speaking, the flows of ozone and TEOS do not need to be initiated
simultaneously nor do they have to be terminated simultaneously. The flow of TEOS is generally effected by flowing a carrier gas (e.g. N2) through liquid TEOS such that the delivery rate of TEOS into the substrate processing region is above one of 1 g/min, 2 g/min or 3 g/min, in different embodiments. Both the carrier gas and the TEOS enter the substrate processing region. The flow of ozone is delivered along with more stable molecular oxygen. The flow rate of the ozone portion of that flow is above one of 1 slm, 2 slm, 3 slm, 5 slm or 10 slm, in different embodiments. Typically, the initiation of the TEOS and ozone flows (operation 120) is followed by a period of slow growth and then a period of more rapid growth as represented in FIG. 2A. The process sequence shown in FIG. 1A interrupts (operation 130) the typical growth pattern near the transition from slow growth to rapid growth. If the typical growth pattern were interrupted earlier in the incubation period or too long after the transition to rapid growth, the conformality of the silicon oxide film would be reduced. An average deposition rate for each region may be defined by using the slope of a line drawn between the start and finish points on a plot of the deposited thickness vs. the time since initial deposition. In the case of the rapid growth, the line must be drawn between the transition start point and an extrapolated finish point to avoid underreporting the deposition rate. The location of operation 130 along the time axis is somewhat flexible while still offering the benefits of conformality. The period of slow growth before operation 130 will be referred to as the incubation period herein. One may wish to adjust the location of operation 130 in order to tune a total deposition thickness. The deposition rate during the incubation period may exceed the deposition rate after the incubation period by a multiplicative factor of one of 1.3, 1.5, 1.7, 2.0, 2.5 or 3.0, in different embodiments. The deposition rate of silicon oxide between operation 120 and operation 130 may be greater than 5θΑ, 7θΑ, 8θΑ, 9θΑ, ΙΟθΑ or 110 A, in different embodiments. The thickness of the conformal silicon oxide layer grown over one material (e.g. thermal silicon oxide) may be within one of 30%, 25%, 20%, 15%, 10% and 5% of the thickness of the conformal silicon oxide layer grown over another material (e.g. silicon), in embodiments of the invention.
Flow rates, as used herein, are not necessarily constant during the process. Flow rates of the different precursors may be initiated and terminated in different orders and their magnitudes may be varied. Unless otherwise indicated, mass flow rate magnitudes indicated herein are given for the approximate peak flow rate used during the process. Flow rate magnitudes indicated herein are for deposition on one side of a pair of 300 mm diameter wafers (area approximately 1400 cm2). Appropriate correction based on deposition area is needed for a different number of wafers, larger or smaller wafers, double sided deposition or deposition on alternative geometry substrates (e.g. rectangular substrates).
The pressure in the substrate processing region are typical of many SACVD and HARP processes (e.g. 600 Torr). The pressure during the formation of the conformal silicon oxide film may be greater than one of 350 Torr, 400 Torr, 450 Torr, 500 Torr or 550 Torr, in different embodiments, to ensure desirable growth rates during the incubation period.
Despite the name and acronym for the related process, sub-atmospheric chemical vapor deposition (SACVD), it should be noted that the processes described herein may be performed at pressures higher than atmospheric pressure (typically 760 Torr).
The substrate temperature is below a threshold value, in embodiments, also to stay within tight thermal budgets and to ensure that the deposition process possesses an incubation period. The temperature of the substrate during the deposition of the conformal silicon oxide is below one of 540°C, 500°C, 450°C, 400°C and 350°C, in different embodiments. No plasma is present in the substrate processing region in embodiments. A small ac and/or dc voltage may be applied to the substrate processing region without detriment to the benefits of the deposition process, according to embodiments. Such an excitation should not be considered to deviate from the scope of "essentially" plasma-free or a process having "essentially" no plasma as may be recited in some claims. FIG. IB shows a repeated deposition of the process sequence described with reference to FIG. 1 A. FIG. 2B shows the dependence of silicon oxide growth selectivity as a function of silicon oxide film thickness and incubation deposition cycle. The process 150 begins when a when a patterned substrate is transferred into a substrate processing region (operation 160). TEOS and ozone flows are initiated then terminated near the end of the incubation period as described previously. The initiation, film growth and termination of the flows occur within operation 170 in FIG. IB. If the target thickness has been achieved, no additional cycles are performed and the patterned substrate may be removed from the substrate processing region (operation 180). However, if a larger film thickness is desired, the flows of TEOS and ozone may be started again which will result in another incubation period. The second incubation period may last for a shorter period of time than the first but will again segue into a period of more selective growth after an incubation period. The flows of TEOS and ozone are terminated near the transition from slow to rapid growth on exposed silicon surfaces. The process may even repeat more than two times if additional film thickness is required. FIG. 2B shows that the selectivity becomes even more conformal during subsequent cycles and stays more conformal for larger film thicknesses. This provides an additional benefit when conformal deposition is desired. Deposition sequences have been explored including six incubation cycles and resulted in conformal films nearly 600A thick. The flexibility provided by choosing a number for the multiple cycles in combination with adjusting the timing of the termination of one or both of the TEOS and ozone flows allows flexibility for achieving a desired silicon oxide film thickness. The thickness of the secondary layers described with reference to FIG. IB may be greater than the same lower limits described with reference to the layer grown and described with reference to FIG. 1 A. The pattern loading was quantified by comparing the horizontal growth of the conformal silicon oxide layer from a vertical feature in a sparsely patterned region and a densely patterned region. An exemplary densely patterned region may have greater number of features than a sparsely patterned region to create the greater exposed surface area within a same area viewed from above the patterned substrate. A densely patterned region may have an exposed vertical area greater than a sparsely patterned region by a factor greater than one of 2, 3, 5, 10 or 20, in different embodiments. The thickness of the conformal silicon oxide layer in a densely patterned region may be within one of 30%, 25%, 20%>, 15%, 10% and 5% of the thickness of the conformal silicon oxide layer in a sparsely patterned region, in different embodiments. The thickness in each region may be measured on vertical surfaces in which case the growth is in a horizontal direction. Alternatively, the thickness may be measured on a horizontal surface within each region and the growth may then be in the vertical direction. The terms "vertical" and "horizontal" are used throughout to include substantially vertical and substantially horizontal directions which may or may not deviate from the theoretical vertical and horizontal by up to about 10 degrees.
Exemplary Substrate Processing System
Deposition chambers that may implement embodiments of the present invention may include sub-atmospheric chemical vapor deposition (SACVD) chambers and more generally, deposition chambers which allow operation at relatively high pressures without necessarily applying plasma excitation. Specific examples of CVD systems that may implement embodiments of the invention include the CENTURA ULTIMA® SACVD chambers/systems, and PRODUCER® HARP, eHARP and SACVD chambers/systems, available from Applied Materials, Inc. of Santa Clara, Calif. Embodiments of the deposition systems may be incorporated into larger fabrication systems for producing integrated circuit chips. FIG. 4 shows one such system 200 of deposition, baking and curing chambers according to disclosed embodiments. In the figure, a pair of FOUPs (front opening unified pods) 202 supply substrate substrates (e.g., 300 mm diameter wafers) that are received by robotic arms 204 and placed into a low pressure holding area 206 before being placed into one of the wafer processing chambers 208a-f. A second robotic arm 210 may be used to transport the substrate wafers from the holding area 206 to the processing chambers 208a-f and back.
The processing chambers 208a-f may include one or more system components for depositing, annealing, curing and/or etching a flowable dielectric film on the substrate wafer. In one configuration, two pairs of the processing chamber (e.g., 208c-d and 208e-f) may be used to deposit the flowable dielectric material on the substrate, and the third pair of processing chambers (e.g., 208a-b) may be used to anneal the deposited dielectic. In another configuration, the same two pairs of processing chambers (e.g., 208c-d and 208e-f) may be configured to both deposit and anneal a flowable dielectric film on the substrate, while the third pair of chambers (e.g., 208a-b) may be used for UV or E-beam curing of the deposited film. In still another configuration, all three pairs of chambers (e.g., 208a-f) may be configured to deposit and cure a flowable dielectric film on the substrate. In yet another configuration, two pairs of processing chambers (e.g., 208c-d and 208e-f) may be used for both deposition and UV or E-beam curing of the flowable dielectric, while a third pair of processing chambers (e.g. 208a-b) may be used for annealing the dielectric film. Any one or more of the processes described may be carried out on chamber(s) separated from the fabrication system shown in different embodiments.
FIG. 4 A shows a simplified representation of an exemplary semiconductor processing chamber within a semiconductor processing tool 200. This exemplary chamber 410 is suitable for performing a variety of semiconductor processing steps which may include CVD processes, as well as other processes, such as reflow, drive-in, cleaning, etching, and gettering processes. Multiple-step processes can also be performed on a single substrate without removing the substrate from the chamber. Representative major components of the system include a chamber interior 415 that receives process and other gases from a gas delivery system 489, pumping system 488, a remote plasma system (RPS) 455, and a control system 453. These and other components are described below in order to understand the present invention.
The semiconductor processing chamber 410 includes an enclosure assembly 412 housing a chamber interior 415 with a gas reaction area 416. A gas distribution plate 420 is provided above the gas reaction area 416 for dispersing reactive gases and other gases, such as purge gases, through perforated holes in the gas distribution plate 420 to a substrate (not shown) that rests on a vertically movable heater 425 (which may also be referred to as a substrate support pedestal). The heater 425 can be controllably moved between a lower position, where a substrate can be loaded or unloaded, for example, and a processing position closely adjacent to the gas distribution plate 420, indicated by a dashed line 413, or to other positions for other purposes, such as for an etch or cleaning process. A center board (not shown) includes sensors for providing information on the position of the substrate.
Gas distribution plate 420 may be of the variety described in U.S. Patent No. 6,793,733. These plates improve the uniformity of gas disbursement at the substrate and are particularly advantageous in deposition processes that vary gas concentration ratios. In some examples, the plates work in combination with the vertically movable heater 425 (or movable substrate support pedestal) such that deposition gases are released farther from the substrate when the ratio is heavily skewed in one direction (e.g., when the concentration of a silicon-containing gas is small compared to the concentration of an oxidizer-containing gas) and are released closer to the substrate as the concentration changes (e.g., when the concentration of silicon-containing gas in the mixture is higher). In other examples, the orifices of the gas distribution plate are designed to provide more uniform mixing of the gases. The heater 425 includes an electrically resistive heating element (not shown) enclosed in a ceramic. The ceramic protects the heating element from potentially corrosive chamber environments and allows the heater to attain temperatures up to about 800°C. In an exemplary embodiment, all surfaces of the heater 425 exposed within the chamber interior 415 are made of a ceramic material, such as aluminum oxide (Α1203 or alumina) or aluminum nitride .
Reactive and carrier gases are supplied through inlet tube 443 into a gas mixing box (also called a gas mixing block) 427, where they are preferably mixed together and delivered to the gas distribution plate 420. The gas mixing block 427 is preferably a dual input mixing block coupled to inlet tube 443 and to a cleaning/etch gas conduit 447. A valve 428 operates to admit or seal gas or plasma from conduit 447 to the gas mixing block 427.
Conduit 447 receives gases from an RPS 455, which has an inlet 457 for receiving input gases. During deposition processing, gas supplied to the plate 420 is vented toward the substrate surface (as indicated by arrows 421), where it may be uniformly distributed radially across the substrate surface, typically in a laminar flow. Purging gas may be delivered into the chamber interior 415 through the plate 420 and/or an inlet port or tube (not shown) through a wall (preferably the bottom) of enclosure assembly 412. The purging gas flows upward from the inlet port past the heater 425 and to an annular pumping channel 440 and may be useful to purge the chamber, for example, of ozone and TEOS between incubation period depositions. An exhaust system then exhausts the gas (as indicated by arrow 422) into the annular pumping channel 440 and through an exhaust line 460 to a pumping system 488, which includes one or more vacuum pumps. Exhaust gases and entrained particles are drawn from the annular pumping channel 440 through the exhaust line 460 at a rate controlled by a throttle valve system 463.
The RPS 455 can produce a plasma for selected applications, such as chamber cleaning or etching native oxide or residue from a process substrate. Plasma species produced in the remote plasma system 455 from precursors supplied via the input line 457 are sent via conduit 447 for dispersion through the plate 420 to the gas reaction area 416. Precursor gases for a cleaning application may include fluorine, chlorine, and other reactive elements. The RPS 455 also may be adapted to deposit plasma enhanced CVD films by selecting appropriate deposition precursor gases for use in the RPS 455.
The system controller 453 controls activities and operating parameters of the deposition system. The processor 451 executes system control software, such as a computer program stored in a memory 452 coupled to the processor 451. The memory 452 typically consists of a combination of static random access memories (cache), dynamic random access memories (DRAM) and hard disk drives but of course the memory 452 may also consist of other kinds of memory, such as solid-state memory devices. In addition to these memory means the semiconductor processing chamber 410 in a preferred embodiment includes a removable storage media drive, USB ports and a card rack (not shown).
The processor 451 operates according to system control software programmed to operate the device according to the methods disclosed herein. For example, sets of instructions may dictate the timing, mixture of gases, chamber pressure, chamber temperature, plasma power levels, susceptor position, and other parameters for carrying out one or more incubation period depositions in a sequence. The instructions are conveyed to the appropriate hardware preferably through direct cabling carrying analog or digital signals conveying signals originating from an input-output I/O module 450. Other computer programs such as those stored on other memory including, for example, a USB thumb drive, a floppy disk or another computer program product inserted in a disk drive or other appropriate drive, may also be used to operate the processor 451 to configure the semiconductor processing chamber 410 for varied uses.
The processor 451 may have a card rack (not shown) that contains a single -board computer, analog and digital input/output boards, interface boards and stepper motor controller boards. Various parts of the semiconductor processing system 200 conform to the Versa Modular European (VME) standard which defines board, card cage, and connector dimensions and types. The VME standard also defines the bus structure having a 16-bit data bus and 24-bit address bus.
A process for depositing a conformal silicon oxide layer on a patterned substrate or a process for cleaning a chamber can be implemented using a computer program product that is executed by the system controller. The computer program code can be written in any conventional computer readable programming language: for example, 68000 assembly language, C, C++, Pascal, Fortran or others. Suitable program code is entered into a single file, or multiple files, using a conventional text editor, and stored or embodied in a computer usable medium, such as a memory system of the computer. If the entered code text is in a high level language, the code is compiled, and the resultant compiler code is then linked with an object code of precompiled Microsoft Windows® library routines. To execute the linked, compiled object code the system user invokes the object code, causing the computer system to load the code in memory. The CPU then reads and executes the code to perform the tasks identified in the program.
The interface between a user and the controller is via a flat-panel touch-sensitive monitor. In the preferred embodiment two monitors are used, one mounted in the clean room wall for the operators and the other behind the wall for the service technicians. The two monitors may simultaneously display the same information, in which case only one accepts input at a time. To select a particular screen or function, the operator touches a designated area of the touch-sensitive monitor. The touched area changes its highlighted color, or a new menu or screen is displayed, confirming communication between the operator and the touch- sensitive monitor. Other devices, such as a keyboard, mouse, or other pointing or communication device, may be used instead of or in addition to the touch-sensitive monitor to allow the user to communicate with the system controller.
The embodiment disclosed herein relies on direct cabling and a single processor 451.
Alternative embodiments comprising multi-core processors, multiple processors under distributed control and wireless communication between the system controller and controlled objects are also possible.
Fig. 4B shows a simplified representation of a gas supply panel 480 in relation to semiconductor processing chamber 410. As discussed above, the portion of semiconductor processing system 200 shown includes semiconductor processing chamber 410 with a heater 425, a gas mixing box 427 with inputs from inlet tube 443 and conduit 447, and RPS 455 with input line 457. As mentioned above, the gas mixing box 427 is configured for mixing and injecting deposition gas(es) and cleaning gas(es) or other gas(es) through inlet tube 443 and the input line 457 to the chamber interior 415. The RPS 455 is integrally located and mounted below the processing chamber 410 with conduit 447 coming up alongside the chamber 410 to the gate valve 428 and the gas mixing box 427, located above the chamber 410. Plasma power generator 411 and ozonator 459 are located remote from the clean room. Delivery lines 483 and 485 from the gas supply panel 480 provide reactive gases to inlet tube 443. The gas supply panel 480 includes lines from gas or liquid sources 490 that provide the process gases for the selected application. The gas supply panel 480 has mixing system 493 that mixes selected gases before flow to the gas mixing box 427. In some embodiments, mixing system 493 includes a liquid injection system for vaporizing one or more reactant liquids such as tetraethylorthosilicate ("TEOS"), triethylborate ("TEB"), and triethylphosphate ("TEPO"). Vapor from the liquids is usually combined with a carrier gas, such as helium. Supply lines for the process gases may include (i) shut-off valves 495 that can be used to automatically or manually shut off the flow of process gas into line 485 or line 457, and (ii) liquid flow meters (LFM) 401 or other types of controllers that measure the flow of gas or liquid through the supply lines.
As an example, a mixture including TEOS as a silicon source may be used with mixing system 493 in a deposition process for forming a silicon oxide film during an incubation period. Sources of dopants such as phosphorous and boron may include TEPO and TEB which may also be introduced to mixing system 493. Precursors delivered to mixing system 493 may be liquid at room temperature and pressure and may be vaporized by conventional boiler-type or bubbler-type hot boxes. Alternatively, a liquid injection system may be used and offers greater control of the volume of reactant liquid introduced into the gas mixing system. The liquid is typically injected as a fine spray or mist into the carrier gas flow before being delivered to a heated gas delivery line 485 to the gas mixing block and chamber. Oxygen (02) and ozone (03) flow to the chamber through another gas delivery line 483, to be combined with the reactant gases from heated gas delivery line 485 near or in the chamber. Of course, it is recognized that other sources of dopants, silicon, oxygen and additive precursors may also be used. Though shown as an individual gas distribution line, line 485 may actually comprise multiple lines separated to discourage inter-precursor reactions before the precursors are flowed into chamber interior 415.
As used herein "substrate" may be a support substrate with or without layers formed thereon. The support substrate may be an insulator or a semiconductor of a variety of doping concentrations and profiles and may, for example, be a semiconductor substrate of the type used in the manufacture of integrated circuits. A layer of "silicon oxide" may include minority concentrations of other elemental constituents such as nitrogen, hydrogen, carbon and the like. A gas may be a combination of two or more gases. The terms trench and gap are used throughout with no implication that the etched geometry necessarily has a large horizontal aspect ratio. Viewed from above the surface, gaps may appear circular, oval, polygonal, rectangular, or a variety of other shapes. Gaps may also be a region between two pillars in which case the gaps are not physical separate from other gaps. As used herein, a conformal layer refers to a generally uniform layer of material on a surface in the same shape as the surface, i.e., the surface of the layer and the surface being covered are generally parallel. A person having ordinary skill in the art will recognize that the deposited material likely cannot be 100% conformal and thus the term "generally" allows for acceptable tolerances.
Having disclosed several embodiments, it will be recognized by those of skill in the art that various modifications, alternative constructions, and equivalents may be used without departing from the spirit of the disclosed embodiments. Additionally, a number of well known processes and elements have not been described in order to avoid unnecessarily obscuring the present invention. Accordingly, the above description should not be taken as limiting the scope of the invention. Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limits of that range is also specifically disclosed. Each smaller range between any stated value or intervening value in a stated range and any other stated or intervening value in that stated range is encompassed. The upper and lower limits of these smaller ranges may independently be included or excluded in the range, and each range where either, neither or both limits are included in the smaller ranges is also encompassed within the invention, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included. As used herein and in the appended claims, the singular forms "a", "an", and "the" include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to "a process" includes a plurality of such processes and reference to "the dielectric material" includes reference to one or more dielectric materials and equivalents thereof known to those skilled in the art, and so forth. Also, the words "comprise," "comprising," "include," "including," and "includes" when used in this specification and in the following claims are intended to specify the presence of stated features, integers, components, or steps, but they do not preclude the presence or addition of one or more other features, integers, components, steps, acts, or groups.

Claims

WHAT IS CLAIMED IS:
1. A method for forming a conformal silicon oxide layer on a patterned substrate in a substrate processing region in a processing chamber, the method comprising:
a step of depositing a layer of silicon oxide during an incubation period comprising:
initiating flows of a silicon-containing precursor and ozone
(O3) into the substrate processing region, and
terminating the flows of the silicon-containing precursor and ozone near the end of the incubation period to avoid the formation of a
nonconformal layer of silicon oxide.
2. The method of claim 1 wherein the patterned substrate has a densely patterned region and a sparsely patterned region and the flows of the silicon-containing precursor and the ozone are terminated such that a thickness of the conformal silicon oxide layer in the densely patterned region is within a conformality percentage of a thickness in the sparsely patterned region.
3. The method of claims 2 wherein the conformality percentage is 30%.
4. The method of claim 1 wherein the patterned substrate has a first exposed material and a second exposed material and the flows of the silicon-containing precursor and the ozone are terminated such that a thickness of the conformal silicon oxide layer deposited on the first exposed material is within a conformality percentage of a thickness deposited on the second exposed material.
5. The method of claims 4 wherein the conformality percentage is 30%.
6. The method of claim 1 wherein the layer of silicon oxide is not conformal at an earlier time during the incubation period but becomes conformal near the end of the incubation period.
7. The method of claim 1 further comprising an additional step of depositing an additional layer of silicon oxide during an additional incubation period.
8. The method of claim 1 wherein a deposition rate during the incubation period is similar on any two of silicon, silicon oxide and silicon nitride.
9. The method of claim 1 wherein a deposition rate on silicon after the incubation period is greater than during the incubation period by a multiplicative factor of 1.3.
10. The method of claim 1 wherein the step of depositing a layer of silicon oxide during an incubation period further comprises flowing water vapor.
11. The method of claim 7 wherein a duration of the additional incubation period is less than a duration of the incubation period.
12. The method of claim 1 wherein terminating the flows of the silicon- containing precursor and ozone near the end of the incubation period comprising terminating the flows of the silicon-containing precursor and ozone at a time selected to achieve a predetermined thickness for the conformal silicon oxide layer.
13. The method of claim 2 wherein an average exposed substantially- vertical area in the densely patterned region exceeds that of the sparsely patterned region by a multiplicative factor of 2.
14. The method of claim 2 wherein the two thicknesses of the conformal silicon oxide layer in the densely and sparsely patterned regions are measured on a substantially- vertical surface of the patterned substrate.
15. The method of claim 2 wherein the two thicknesses of the conformal silicon oxide layer in the densely and sparsely patterned regions are measured on a substantially-horizontal surface of the patterned substrate.
16. The method of claim 1 wherein essentially no plasma is applied to the substrate processing region.
17. The method of claim 1 further comprising the operation of flowing a carrier gas which carries the silicon-containing precursor into the substrate processing region.
18. The method of claim 1 wherein the silicon-containing precursor comprises TEOS.
PCT/US2011/027246 2010-04-01 2011-03-04 Silicon-ozone cvd with reduced pattern loading using incubation period deposition Ceased WO2011123217A2 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US31997010P 2010-04-01 2010-04-01
US61/319,970 2010-04-01
US12/891,149 2010-09-27
US12/891,149 US7994019B1 (en) 2010-04-01 2010-09-27 Silicon-ozone CVD with reduced pattern loading using incubation period deposition

Publications (2)

Publication Number Publication Date
WO2011123217A2 true WO2011123217A2 (en) 2011-10-06
WO2011123217A3 WO2011123217A3 (en) 2011-11-24

Family

ID=44350741

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2011/027246 Ceased WO2011123217A2 (en) 2010-04-01 2011-03-04 Silicon-ozone cvd with reduced pattern loading using incubation period deposition

Country Status (3)

Country Link
US (1) US7994019B1 (en)
TW (1) TWI368669B (en)
WO (1) WO2011123217A2 (en)

Families Citing this family (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8232176B2 (en) 2006-06-22 2012-07-31 Applied Materials, Inc. Dielectric deposition and etch back processes for bottom up gapfill
US7867923B2 (en) * 2007-10-22 2011-01-11 Applied Materials, Inc. High quality silicon oxide films by remote plasma CVD from disilane precursors
US8357435B2 (en) 2008-05-09 2013-01-22 Applied Materials, Inc. Flowable dielectric equipment and processes
US8980382B2 (en) 2009-12-02 2015-03-17 Applied Materials, Inc. Oxygen-doping for non-carbon radical-component CVD films
US8741788B2 (en) 2009-08-06 2014-06-03 Applied Materials, Inc. Formation of silicon oxide using non-carbon flowable CVD processes
US8449942B2 (en) 2009-11-12 2013-05-28 Applied Materials, Inc. Methods of curing non-carbon flowable CVD films
CN102687252A (en) 2009-12-30 2012-09-19 应用材料公司 Method for growing dielectric thin films with free radicals produced by variable nitrogen/hydrogen ratios
US8329262B2 (en) 2010-01-05 2012-12-11 Applied Materials, Inc. Dielectric film formation using inert gas excitation
JP2013517616A (en) 2010-01-06 2013-05-16 アプライド マテリアルズ インコーポレイテッド Flowable dielectrics using oxide liners
SG182333A1 (en) 2010-01-07 2012-08-30 Applied Materials Inc In-situ ozone cure for radical-component cvd
CN102844848A (en) 2010-03-05 2012-12-26 应用材料公司 Conformal layers deposited by chemical vapor deposition of radical components
US8236708B2 (en) * 2010-03-09 2012-08-07 Applied Materials, Inc. Reduced pattern loading using bis(diethylamino)silane (C8H22N2Si) as silicon precursor
JP5052638B2 (en) * 2010-03-17 2012-10-17 Sppテクノロジーズ株式会社 Deposition method
US8476142B2 (en) 2010-04-12 2013-07-02 Applied Materials, Inc. Preferential dielectric gapfill
US8524004B2 (en) 2010-06-16 2013-09-03 Applied Materials, Inc. Loadlock batch ozone cure
US8318584B2 (en) 2010-07-30 2012-11-27 Applied Materials, Inc. Oxide-rich liner layer for flowable CVD gapfill
US9285168B2 (en) 2010-10-05 2016-03-15 Applied Materials, Inc. Module for ozone cure and post-cure moisture treatment
US8664127B2 (en) 2010-10-15 2014-03-04 Applied Materials, Inc. Two silicon-containing precursors for gapfill enhancing dielectric liner
US10283321B2 (en) 2011-01-18 2019-05-07 Applied Materials, Inc. Semiconductor processing system and methods using capacitively coupled plasma
US8450191B2 (en) 2011-01-24 2013-05-28 Applied Materials, Inc. Polysilicon films by HDP-CVD
US8716154B2 (en) 2011-03-04 2014-05-06 Applied Materials, Inc. Reduced pattern loading using silicon oxide multi-layers
US8445078B2 (en) 2011-04-20 2013-05-21 Applied Materials, Inc. Low temperature silicon oxide conversion
US8466073B2 (en) 2011-06-03 2013-06-18 Applied Materials, Inc. Capping layer for reduced outgassing
US9404178B2 (en) 2011-07-15 2016-08-02 Applied Materials, Inc. Surface treatment and deposition for reduced outgassing
US8617989B2 (en) 2011-09-26 2013-12-31 Applied Materials, Inc. Liner property improvement
US8551891B2 (en) 2011-10-04 2013-10-08 Applied Materials, Inc. Remote plasma burn-in
US8889566B2 (en) 2012-09-11 2014-11-18 Applied Materials, Inc. Low cost flowable dielectric films
US9018108B2 (en) 2013-01-25 2015-04-28 Applied Materials, Inc. Low shrinkage dielectric films
JP6336719B2 (en) * 2013-07-16 2018-06-06 株式会社ディスコ Plasma etching equipment
US9412581B2 (en) 2014-07-16 2016-08-09 Applied Materials, Inc. Low-K dielectric gapfill by flowable deposition
US20160225652A1 (en) 2015-02-03 2016-08-04 Applied Materials, Inc. Low temperature chuck for plasma processing systems
US10647578B2 (en) 2016-12-11 2020-05-12 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude N—H free and SI-rich per-hydridopolysilzane compositions, their synthesis, and applications
JP7033667B2 (en) 2018-02-21 2022-03-10 レール・リキード-ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Perhydropolysilazane composition and method for forming an oxide film using it
CN113529057B (en) * 2020-04-13 2023-02-28 长鑫存储技术有限公司 Semiconductor manufacturing method and multi-sheet type deposition apparatus
US20250201548A1 (en) * 2023-12-15 2025-06-19 Applied Materials, Inc. Methods of depositing silicon-containing dielectric layers for semiconductor devices

Family Cites Families (176)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4147571A (en) 1977-07-11 1979-04-03 Hewlett-Packard Company Method for vapor epitaxial deposition of III/V materials utilizing organometallic compounds and a halogen or halide in a hot wall system
FR2598520B1 (en) 1986-01-21 1994-01-28 Seiko Epson Corp MINERAL PROTECTIVE FILM
US4818326A (en) 1987-07-16 1989-04-04 Texas Instruments Incorporated Processing apparatus
US4816098A (en) 1987-07-16 1989-03-28 Texas Instruments Incorporated Apparatus for transferring workpieces
US4931354A (en) 1987-11-02 1990-06-05 Murata Manufacturing Co., Ltd. Multilayer printed circuit board
JPH03257182A (en) 1990-03-07 1991-11-15 Hitachi Ltd Surface processing device
US5016332A (en) 1990-04-13 1991-05-21 Branson International Plasma Corporation Plasma reactor and process with wafer temperature control
US5436172A (en) 1991-05-20 1995-07-25 Texas Instruments Incorporated Real-time multi-zone semiconductor wafer temperature and process uniformity control system
US5426076A (en) 1991-07-16 1995-06-20 Intel Corporation Dielectric deposition and cleaning process for improved gap filling and device planarization
US5393708A (en) 1992-10-08 1995-02-28 Industrial Technology Research Institute Inter-metal-dielectric planarization process
US5587014A (en) 1993-12-22 1996-12-24 Sumitomo Chemical Company, Limited Method for manufacturing group III-V compound semiconductor crystals
US5679152A (en) 1994-01-27 1997-10-21 Advanced Technology Materials, Inc. Method of making a single crystals Ga*N article
US5576071A (en) 1994-11-08 1996-11-19 Micron Technology, Inc. Method of reducing carbon incorporation into films produced by chemical vapor deposition involving organic precursor compounds
US5558717A (en) 1994-11-30 1996-09-24 Applied Materials CVD Processing chamber
JPH08236518A (en) * 1995-02-28 1996-09-13 Hitachi Ltd Method for forming silicon oxide film
US5786263A (en) 1995-04-04 1998-07-28 Motorola, Inc. Method for forming a trench isolation structure in an integrated circuit
JPH08288286A (en) * 1995-04-19 1996-11-01 Sharp Corp Method for forming silicon oxide film
JPH09237785A (en) 1995-12-28 1997-09-09 Toshiba Corp Semiconductor device and manufacturing method thereof
US6070551A (en) 1996-05-13 2000-06-06 Applied Materials, Inc. Deposition chamber and method for depositing low dielectric constant films
US5827783A (en) 1996-08-23 1998-10-27 Mosel Vitelic, Inc. Stacked capacitor having improved charge storage capacity
US5873781A (en) 1996-11-14 1999-02-23 Bally Gaming International, Inc. Gaming machine having truly random results
US6090723A (en) 1997-02-10 2000-07-18 Micron Technology, Inc. Conditioning of dielectric materials
FR2759362B1 (en) 1997-02-10 1999-03-12 Saint Gobain Vitrage TRANSPARENT SUBSTRATE EQUIPPED WITH AT LEAST ONE THIN LAYER BASED ON SILICON NITRIDE OR OXYNITRIDE AND ITS PROCESS FOR OBTAINING IT
US5937308A (en) 1997-03-26 1999-08-10 Advanced Micro Devices, Inc. Semiconductor trench isolation structure formed substantially within a single chamber
US5937323A (en) 1997-06-03 1999-08-10 Applied Materials, Inc. Sequencing of the recipe steps for the optimal low-k HDP-CVD processing
US6207587B1 (en) 1997-06-24 2001-03-27 Micron Technology, Inc. Method for forming a dielectric
TW416100B (en) 1997-07-02 2000-12-21 Applied Materials Inc Control of oxygen to silane ratio in a seasoning process to improve particle performance in an HDP-CVD system
US6024044A (en) 1997-10-09 2000-02-15 Applied Komatsu Technology, Inc. Dual frequency excitation of plasma for film deposition
US6624064B1 (en) 1997-10-10 2003-09-23 Applied Materials, Inc. Chamber seasoning method to improve adhesion of F-containing dielectric film to metal for VLSI application
US6087243A (en) 1997-10-21 2000-07-11 Advanced Micro Devices, Inc. Method of forming trench isolation with high integrity, ultra thin gate oxide
US6009830A (en) 1997-11-21 2000-01-04 Applied Materials Inc. Independent gas feeds in a plasma reactor
KR100253079B1 (en) 1997-12-01 2000-04-15 윤종용 Semiconductor element trench isolation method
US6068884A (en) 1998-04-28 2000-05-30 Silcon Valley Group Thermal Systems, Llc Method of making low κ dielectric inorganic/organic hybrid films
US6165834A (en) 1998-05-07 2000-12-26 Micron Technology, Inc. Method of forming capacitors, method of processing dielectric layers, method of forming a DRAM cell
US6509283B1 (en) 1998-05-13 2003-01-21 National Semiconductor Corporation Thermal oxidation method utilizing atomic oxygen to reduce dangling bonds in silicon dioxide grown on silicon
US6146970A (en) 1998-05-26 2000-11-14 Motorola Inc. Capped shallow trench isolation and method of formation
US6302964B1 (en) 1998-06-16 2001-10-16 Applied Materials, Inc. One-piece dual gas faceplate for a showerhead in a semiconductor wafer processing system
US6406677B1 (en) 1998-07-22 2002-06-18 Eltron Research, Inc. Methods for low and ambient temperature preparation of precursors of compounds of group III metals and group V elements
US6197658B1 (en) 1998-10-30 2001-03-06 Taiwan Semiconductor Manufacturing Company Sub-atmospheric pressure thermal chemical vapor deposition (SACVD) trench isolation method with attenuated surface sensitivity
US6245690B1 (en) 1998-11-04 2001-06-12 Applied Materials, Inc. Method of improving moisture resistance of low dielectric constant films
US6290774B1 (en) 1999-05-07 2001-09-18 Cbl Technology, Inc. Sequential hydride vapor phase epitaxy
US6180490B1 (en) 1999-05-25 2001-01-30 Chartered Semiconductor Manufacturing Ltd. Method of filling shallow trenches
US6204201B1 (en) 1999-06-11 2001-03-20 Electron Vision Corporation Method of processing films prior to chemical vapor deposition using electron beam processing
US6524931B1 (en) 1999-07-20 2003-02-25 Motorola, Inc. Method for forming a trench isolation structure in an integrated circuit
US6383954B1 (en) 1999-07-27 2002-05-07 Applied Materials, Inc. Process gas distribution for forming stable fluorine-doped silicate glass and other films
US6602806B1 (en) * 1999-08-17 2003-08-05 Applied Materials, Inc. Thermal CVD process for depositing a low dielectric constant carbon-doped silicon oxide film
JP2001144325A (en) 1999-11-12 2001-05-25 Sony Corp Method for manufacturing nitride III-V compound semiconductor and method for manufacturing semiconductor device
FI118804B (en) 1999-12-03 2008-03-31 Asm Int Process for making oxide films
US6348420B1 (en) 1999-12-23 2002-02-19 Asm America, Inc. Situ dielectric stacks
US6541367B1 (en) 2000-01-18 2003-04-01 Applied Materials, Inc. Very low dielectric constant plasma-enhanced CVD films
US6440860B1 (en) 2000-01-18 2002-08-27 Micron Technology, Inc. Semiconductor processing methods of transferring patterns from patterned photoresists to materials, and structures comprising silicon nitride
US6461980B1 (en) 2000-01-28 2002-10-08 Applied Materials, Inc. Apparatus and process for controlling the temperature of a substrate in a plasma reactor chamber
EP1124252A2 (en) 2000-02-10 2001-08-16 Applied Materials, Inc. Apparatus and process for processing substrates
EP1130633A1 (en) 2000-02-29 2001-09-05 STMicroelectronics S.r.l. A method of depositing silicon oxynitride polimer layers
US7419903B2 (en) 2000-03-07 2008-09-02 Asm International N.V. Thin films
US6558755B2 (en) 2000-03-20 2003-05-06 Dow Corning Corporation Plasma curing process for porous silica thin film
DE10196026B4 (en) 2000-04-04 2011-02-10 Asahi Kasei Kabushiki Kaisha Coating composition, thin film, thin film use, and method of producing a thin porous silica film
US6630413B2 (en) 2000-04-28 2003-10-07 Asm Japan K.K. CVD syntheses of silicon nitride materials
US6387207B1 (en) 2000-04-28 2002-05-14 Applied Materials, Inc. Integration of remote plasma generator with semiconductor processing chamber
US6559026B1 (en) 2000-05-25 2003-05-06 Applied Materials, Inc Trench fill with HDP-CVD process including coupled high power density plasma deposition
JP4371543B2 (en) 2000-06-29 2009-11-25 日本電気株式会社 Remote plasma CVD apparatus and film forming method
US6835278B2 (en) 2000-07-07 2004-12-28 Mattson Technology Inc. Systems and methods for remote plasma clean
US7183177B2 (en) 2000-08-11 2007-02-27 Applied Materials, Inc. Silicon-on-insulator wafer transfer method using surface activation plasma immersion ion implantation for wafer-to-wafer adhesion enhancement
US6614181B1 (en) 2000-08-23 2003-09-02 Applied Materials, Inc. UV radiation source for densification of CVD carbon-doped silicon oxide films
US6566278B1 (en) 2000-08-24 2003-05-20 Applied Materials Inc. Method for densification of CVD carbon-doped silicon oxide films through UV irradiation
JP4232330B2 (en) 2000-09-22 2009-03-04 東京エレクトロン株式会社 Excited gas forming apparatus, processing apparatus and processing method
JP3712356B2 (en) 2000-10-23 2005-11-02 アプライド マテリアルズ インコーポレイテッド Film-forming method and semiconductor device manufacturing method
US20020060322A1 (en) 2000-11-20 2002-05-23 Hiroshi Tanabe Thin film transistor having high mobility and high on-current and method for manufacturing the same
US6287962B1 (en) 2000-11-30 2001-09-11 Taiwan Semiconductor Manufacturing Company Method for making a novel graded silicon nitride/silicon oxide (SNO) hard mask for improved deep sub-micrometer semiconductor processing
US6930041B2 (en) 2000-12-07 2005-08-16 Micron Technology, Inc. Photo-assisted method for semiconductor fabrication
US6576564B2 (en) 2000-12-07 2003-06-10 Micron Technology, Inc. Photo-assisted remote plasma apparatus and method
US20020081817A1 (en) 2000-12-22 2002-06-27 Jayendra Bhakta Void reduction and increased throughput in trench fill processes
US6660662B2 (en) 2001-01-26 2003-12-09 Applied Materials, Inc. Method of reducing plasma charge damage for plasma processes
US6589868B2 (en) 2001-02-08 2003-07-08 Applied Materials, Inc. Si seasoning to reduce particles, extend clean frequency, block mobile ions and increase chamber throughput
US6447651B1 (en) 2001-03-07 2002-09-10 Applied Materials, Inc. High-permeability magnetic shield for improved process uniformity in nonmagnetized plasma process chambers
WO2002077320A1 (en) 2001-03-23 2002-10-03 Dow Corning Corporation Method for producing hydrogenated silicon oxycarbide films
US6596576B2 (en) 2001-04-10 2003-07-22 Applied Materials, Inc. Limiting hydrogen ion diffusion using multiple layers of SiO2 and Si3N4
US6528332B2 (en) 2001-04-27 2003-03-04 Advanced Micro Devices, Inc. Method and system for reducing polymer build up during plasma etch of an intermetal dielectric
US6780499B2 (en) 2001-05-03 2004-08-24 International Business Machines Corporation Ordered two-phase dielectric film, and semiconductor device containing the same
US6596653B2 (en) 2001-05-11 2003-07-22 Applied Materials, Inc. Hydrogen assisted undoped silicon oxide deposition process for HDP-CVD
US6716770B2 (en) 2001-05-23 2004-04-06 Air Products And Chemicals, Inc. Low dielectric constant material and method of processing by CVD
KR100421046B1 (en) 2001-07-13 2004-03-04 삼성전자주식회사 Semiconductor device and method for manufacturing the same
US6548416B2 (en) 2001-07-24 2003-04-15 Axcelis Technolgoies, Inc. Plasma ashing process
US6596654B1 (en) 2001-08-24 2003-07-22 Novellus Systems, Inc. Gap fill for high aspect ratio structures
US20030064154A1 (en) 2001-08-06 2003-04-03 Laxman Ravi K. Low-K dielectric thin films and chemical vapor deposition method of making same
US6756085B2 (en) 2001-09-14 2004-06-29 Axcelis Technologies, Inc. Ultraviolet curing processes for advanced low-k materials
US6872323B1 (en) 2001-11-01 2005-03-29 Novellus Systems, Inc. In situ plasma process to remove fluorine residues from the interior surfaces of a CVD reactor
US6770521B2 (en) 2001-11-30 2004-08-03 Texas Instruments Incorporated Method of making multiple work function gates by implanting metals with metallic alloying additives
US6794290B1 (en) 2001-12-03 2004-09-21 Novellus Systems, Inc. Method of chemical modification of structure topography
JP3891267B2 (en) 2001-12-25 2007-03-14 キヤノンアネルバ株式会社 Silicon oxide film manufacturing method
US20030124873A1 (en) 2001-12-28 2003-07-03 Guangcai Xing Method of annealing an oxide film
WO2003065424A2 (en) 2002-01-25 2003-08-07 Applied Materials, Inc. Apparatus for cyclical deposition of thin films
US6911391B2 (en) 2002-01-26 2005-06-28 Applied Materials, Inc. Integration of titanium and titanium nitride layers
US6998014B2 (en) 2002-01-26 2006-02-14 Applied Materials, Inc. Apparatus and method for plasma assisted deposition
TW536775B (en) 2002-04-18 2003-06-11 Nanya Technology Corp Manufacturing method of shallow trench isolation structure
WO2003090268A1 (en) 2002-04-19 2003-10-30 Tokyo Electron Limited Method of treating substrate and process for producing semiconductor device
US6936551B2 (en) 2002-05-08 2005-08-30 Applied Materials Inc. Methods and apparatus for E-beam treatment used to fabricate integrated circuit devices
US7307273B2 (en) 2002-06-07 2007-12-11 Amberwave Systems Corporation Control of strain in device layers by selective relaxation
TWI283899B (en) 2002-07-09 2007-07-11 Applied Materials Inc Capacitively coupled plasma reactor with magnetic plasma control
US6900881B2 (en) 2002-07-11 2005-05-31 Molecular Imprints, Inc. Step and repeat imprint lithography systems
US7456116B2 (en) 2002-09-19 2008-11-25 Applied Materials, Inc. Gap-fill depositions in the formation of silicon containing dielectric materials
US7335609B2 (en) * 2004-08-27 2008-02-26 Applied Materials, Inc. Gap-fill depositions introducing hydroxyl-containing precursors in the formation of silicon containing dielectric materials
JP4358492B2 (en) 2002-09-25 2009-11-04 レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Method for producing silicon nitride film or silicon oxynitride film by thermal chemical vapor deposition
US6828211B2 (en) 2002-10-01 2004-12-07 Taiwan Semiconductor Manufacturing Co., Ltd. Shallow trench filled with two or more dielectrics for isolation and coupling or for stress control
US6833322B2 (en) 2002-10-17 2004-12-21 Applied Materials, Inc. Apparatuses and methods for depositing an oxide film
US6819886B2 (en) 2002-10-23 2004-11-16 Nex Press Solutions Llc Gloss/density measurement device with feedback to control gloss and density of images produced by an electrographic reproduction apparatus
US7080528B2 (en) 2002-10-23 2006-07-25 Applied Materials, Inc. Method of forming a phosphorus doped optical core using a PECVD process
US6900067B2 (en) 2002-12-11 2005-05-31 Lumileds Lighting U.S., Llc Growth of III-nitride films on mismatched substrates without conventional low temperature nucleation layers
US6808748B2 (en) 2003-01-23 2004-10-26 Applied Materials, Inc. Hydrogen assisted HDP-CVD deposition process for aggressive gap-fill technology
US7122222B2 (en) 2003-01-23 2006-10-17 Air Products And Chemicals, Inc. Precursors for depositing silicon containing films and processes thereof
US7205248B2 (en) 2003-02-04 2007-04-17 Micron Technology, Inc. Method of eliminating residual carbon from flowable oxide fill
US6884685B2 (en) 2003-02-14 2005-04-26 Freescale Semiconductors, Inc. Radical oxidation and/or nitridation during metal oxide layer deposition process
US7084076B2 (en) 2003-02-27 2006-08-01 Samsung Electronics, Co., Ltd. Method for forming silicon dioxide film using siloxane
US7098149B2 (en) 2003-03-04 2006-08-29 Air Products And Chemicals, Inc. Mechanical enhancement of dense and porous organosilicate materials by UV exposure
US7429540B2 (en) 2003-03-07 2008-09-30 Applied Materials, Inc. Silicon oxynitride gate dielectric formation using multiple annealing steps
US6867086B1 (en) 2003-03-13 2005-03-15 Novellus Systems, Inc. Multi-step deposition and etch back gap fill process
JP2004283065A (en) 2003-03-20 2004-10-14 Ushio Inc Method for producing chemotactic function-controlling film, artificial material, and method for producing artificial material
JP3976703B2 (en) 2003-04-30 2007-09-19 エルピーダメモリ株式会社 Manufacturing method of semiconductor device
US6830624B2 (en) 2003-05-02 2004-12-14 Applied Materials, Inc. Blocker plate by-pass for remote plasma clean
US6958112B2 (en) 2003-05-27 2005-10-25 Applied Materials, Inc. Methods and systems for high-aspect-ratio gapfill using atomic-oxygen generation
JP2005033173A (en) 2003-06-16 2005-02-03 Renesas Technology Corp Manufacturing method of semiconductor integrated circuit device
US7399388B2 (en) 2003-07-25 2008-07-15 Applied Materials, Inc. Sequential gas flow oxide deposition technique
US7192891B2 (en) 2003-08-01 2007-03-20 Samsung Electronics, Co., Ltd. Method for forming a silicon oxide layer using spin-on glass
US6818517B1 (en) 2003-08-29 2004-11-16 Asm International N.V. Methods of depositing two or more layers on a substrate in situ
US7361991B2 (en) 2003-09-19 2008-04-22 International Business Machines Corporation Closed air gap interconnect structure
JP4285184B2 (en) 2003-10-14 2009-06-24 東京エレクトロン株式会社 Film forming method and film forming apparatus
AU2004313262B2 (en) 2003-12-17 2009-06-04 Cedraeus Inc. Method for a random-based decision-making process
US7030468B2 (en) 2004-01-16 2006-04-18 International Business Machines Corporation Low k and ultra low k SiCOH dielectric films and methods to form the same
US7067438B2 (en) 2004-02-19 2006-06-27 Micron Technology, Inc. Atomic layer deposition method of forming an oxide comprising layer on a substrate
US7524735B1 (en) 2004-03-25 2009-04-28 Novellus Systems, Inc Flowable film dielectric gap fill process
US20050221020A1 (en) 2004-03-30 2005-10-06 Tokyo Electron Limited Method of improving the wafer to wafer uniformity and defectivity of a deposited dielectric film
US7115508B2 (en) 2004-04-02 2006-10-03 Applied-Materials, Inc. Oxide-like seasoning for dielectric low k films
US7109114B2 (en) 2004-05-07 2006-09-19 Applied Materials, Inc. HDP-CVD seasoning process for high power HDP-CVD gapfil to improve particle performance
WO2005121397A2 (en) 2004-06-04 2005-12-22 Applied Microstructures, Inc. Controlled vapor deposition of multilayered coatings adhered by an oxide layer
US7297608B1 (en) 2004-06-22 2007-11-20 Novellus Systems, Inc. Method for controlling properties of conformal silica nanolaminates formed by rapid vapor deposition
US7129187B2 (en) 2004-07-14 2006-10-31 Tokyo Electron Limited Low-temperature plasma-enhanced chemical vapor deposition of silicon-nitrogen-containing films
US7642171B2 (en) 2004-08-04 2010-01-05 Applied Materials, Inc. Multi-step anneal of thin films for film densification and improved gap-fill
US7629270B2 (en) 2004-08-27 2009-12-08 Asm America, Inc. Remote plasma activated nitridation
KR100550351B1 (en) 2004-09-07 2006-02-08 삼성전자주식회사 A film forming method of a semiconductor device and a film forming device of a semiconductor device for performing the same
US7148155B1 (en) 2004-10-26 2006-12-12 Novellus Systems, Inc. Sequential deposition/anneal film densification method
KR100782369B1 (en) 2004-11-11 2007-12-07 삼성전자주식회사 Semiconductor manufacturing device
US20060162661A1 (en) 2005-01-22 2006-07-27 Applied Materials, Inc. Mixing energized and non-energized gases for silicon nitride deposition
US20060228903A1 (en) 2005-03-30 2006-10-12 Mcswiney Michael L Precursors for the deposition of carbon-doped silicon nitride or silicon oxynitride films
US7972441B2 (en) 2005-04-05 2011-07-05 Applied Materials, Inc. Thermal oxidation of silicon using ozone
US7651955B2 (en) 2005-06-21 2010-01-26 Applied Materials, Inc. Method for forming silicon-containing materials during a photoexcitation deposition process
JP4860953B2 (en) 2005-07-08 2012-01-25 富士通株式会社 Silica-based film forming material, silica-based film and manufacturing method thereof, multilayer wiring and manufacturing method thereof, and semiconductor device and manufacturing method thereof
US7427570B2 (en) 2005-09-01 2008-09-23 Micron Technology, Inc. Porous organosilicate layers, and vapor deposition systems and methods for preparing same
US7498270B2 (en) 2005-09-30 2009-03-03 Tokyo Electron Limited Method of forming a silicon oxynitride film with tensile stress
US7901743B2 (en) 2005-09-30 2011-03-08 Tokyo Electron Limited Plasma-assisted vapor phase treatment of low dielectric constant films using a batch processing system
JP5154009B2 (en) 2005-10-21 2013-02-27 株式会社ジャパンディスプレイイースト Manufacturing method of organic siloxane insulating film, and manufacturing method of liquid crystal display device using organic siloxane insulating film manufactured by this manufacturing method as interlayer insulation
KR101019293B1 (en) 2005-11-04 2011-03-07 어플라이드 머티어리얼스, 인코포레이티드 Plasma-Enhanced Atomic Layer Deposition Apparatus and Method
US7972954B2 (en) 2006-01-24 2011-07-05 Infineon Technologies Ag Porous silicon dielectric
US7435661B2 (en) 2006-01-27 2008-10-14 Atmel Corporation Polish stop and sealing layer for manufacture of semiconductor devices with deep trench isolation
JP4984558B2 (en) 2006-02-08 2012-07-25 富士通セミコンダクター株式会社 Manufacturing method of semiconductor device
US7601651B2 (en) 2006-03-31 2009-10-13 Applied Materials, Inc. Method to improve the step coverage and pattern loading for dielectric films
US7780865B2 (en) 2006-03-31 2010-08-24 Applied Materials, Inc. Method to improve the step coverage and pattern loading for dielectric films
US7524750B2 (en) 2006-04-17 2009-04-28 Applied Materials, Inc. Integrated process modulation (IPM) a novel solution for gapfill with HDP-CVD
US7825038B2 (en) 2006-05-30 2010-11-02 Applied Materials, Inc. Chemical vapor deposition of high quality flow-like silicon dioxide using a silicon containing precursor and atomic oxygen
US7498273B2 (en) 2006-05-30 2009-03-03 Applied Materials, Inc. Formation of high quality dielectric films of silicon dioxide for STI: usage of different siloxane-based precursors for harp II—remote plasma enhanced deposition processes
US7902080B2 (en) 2006-05-30 2011-03-08 Applied Materials, Inc. Deposition-plasma cure cycle process to enhance film quality of silicon dioxide
US7790634B2 (en) 2006-05-30 2010-09-07 Applied Materials, Inc Method for depositing and curing low-k films for gapfill and conformal film applications
US7629273B2 (en) 2006-09-19 2009-12-08 Taiwan Semiconductor Manufacturing Company, Ltd. Method for modulating stresses of a contact etch stop layer
US7737050B2 (en) 2006-10-30 2010-06-15 International Business Machines Corporation Method of fabricating a nitrided silicon oxide gate dielectric layer
US20080102223A1 (en) 2006-11-01 2008-05-01 Sigurd Wagner Hybrid layers for use in coatings on electronic devices or other articles
US7572647B2 (en) 2007-02-02 2009-08-11 Applied Materials, Inc. Internal balanced coil for inductively coupled high density plasma processing chamber
US7745352B2 (en) 2007-08-27 2010-06-29 Applied Materials, Inc. Curing methods for silicon dioxide thin films deposited from alkoxysilane precursor with harp II process
US7943531B2 (en) 2007-10-22 2011-05-17 Applied Materials, Inc. Methods for forming a silicon oxide layer over a substrate
US7541297B2 (en) 2007-10-22 2009-06-02 Applied Materials, Inc. Method and system for improving dielectric film quality for void free gap fill
US7867923B2 (en) 2007-10-22 2011-01-11 Applied Materials, Inc. High quality silicon oxide films by remote plasma CVD from disilane precursors
US7803722B2 (en) 2007-10-22 2010-09-28 Applied Materials, Inc Methods for forming a dielectric layer within trenches
US20090325391A1 (en) * 2008-06-30 2009-12-31 Asm International Nv Ozone and teos process for silicon oxide deposition
US7972980B2 (en) 2009-01-21 2011-07-05 Asm Japan K.K. Method of forming conformal dielectric film having Si-N bonds by PECVD
US7935643B2 (en) 2009-08-06 2011-05-03 Applied Materials, Inc. Stress management for tensile films
US8741788B2 (en) 2009-08-06 2014-06-03 Applied Materials, Inc. Formation of silicon oxide using non-carbon flowable CVD processes
US7989365B2 (en) 2009-08-18 2011-08-02 Applied Materials, Inc. Remote plasma source seasoning
US8449942B2 (en) 2009-11-12 2013-05-28 Applied Materials, Inc. Methods of curing non-carbon flowable CVD films

Also Published As

Publication number Publication date
TWI368669B (en) 2012-07-21
TW201137165A (en) 2011-11-01
WO2011123217A3 (en) 2011-11-24
US7994019B1 (en) 2011-08-09

Similar Documents

Publication Publication Date Title
US7994019B1 (en) Silicon-ozone CVD with reduced pattern loading using incubation period deposition
US8236708B2 (en) Reduced pattern loading using bis(diethylamino)silane (C8H22N2Si) as silicon precursor
US8716154B2 (en) Reduced pattern loading using silicon oxide multi-layers
US10903071B2 (en) Selective deposition of silicon oxide
US12451346B2 (en) Modulated atomic layer deposition
US10804144B2 (en) Deposition of aluminum oxide etch stop layers
US8012887B2 (en) Precursor addition to silicon oxide CVD for improved low temperature gapfill
US8664127B2 (en) Two silicon-containing precursors for gapfill enhancing dielectric liner
US10804099B2 (en) Selective inhibition in atomic layer deposition of silicon-containing films
US12157945B2 (en) Thermal atomic layer deposition of silicon-containing films
US10037884B2 (en) Selective atomic layer deposition for gapfill using sacrificial underlayer
US20130217239A1 (en) Flowable silicon-and-carbon-containing layers for semiconductor processing
KR20090019865A (en) New Deposition-Plasma Curing Cycle Process Enhances Film Quality of Silicon Dioxide
US8476142B2 (en) Preferential dielectric gapfill
US20230220544A1 (en) In-feature wet etch rate ratio reduction
TW202409322A (en) Lateral gap fill

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11763199

Country of ref document: EP

Kind code of ref document: A2

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11763199

Country of ref document: EP

Kind code of ref document: A2