Reduced pattern loading using silicon oxide multi-layers

Abstract

Aspects of the disclosure pertain to methods of depositing conformal silicon oxide multi-layers on patterned substrates. The conformal silicon oxide multi-layers are each formed by depositing multiple sub-layers. Sub-layers are deposited by flowing BIS(DIETHYLAMINO)SILANE (BDEAS) and an oxygen-containing precursor into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface. A plasma treatment may follow formation of sub-layers to further improve conformality and to decrease the wet etch rate of the conformal silicon oxide multi-layer film. The deposition of conformal silicon oxide multi-layers grown according to embodiments have a reduced dependence on pattern density while still being suitable for non-sacrificial applications.

Description

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 as the barrier layer formed over a feature may have surface defects including uneven thickness. 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. 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 more conformal methods of depositing dielectric films over features in a patterned substrate.

BRIEF SUMMARY OF THE INVENTION

Aspects of the disclosure pertain to methods of depositing conformal silicon oxide multi-layers on patterned substrates. The conformal silicon oxide multi-layers are each formed by depositing multiple sub-layers. Sub-layers are deposited by flowing BIS(DIETHYLAMINO)SILANE (BDEAS) and an oxygen-containing precursor into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface. A plasma treatment may follow formation of sub-layers to further improve conformality and to decrease the wet etch rate of the conformal silicon oxide multi-layer film. The deposition of conformal silicon oxide multi-layers grown according to embodiments have a reduced dependence on pattern density while still being suitable for non-sacrificial applications.

Embodiments of the invention include methods for forming a conformal silicon oxide multi-layer on a patterned substrate in a substrate processing region of a processing chamber. The patterned substrate has a densely patterned region and a sparsely patterned region. The method comprising the sequential steps (1) performing a first cycle of chemical vapor deposition comprising the operations: flowing BDEAS into the substrate processing region, flowing a first oxygen-containing precursor into the substrate processing region, and forming a first conformal silicon oxide sub-layer of the conformal silicon oxide multi-layer on the patterned substrate from the BDEAS and the oxygen-containing precursor by chemical vapor deposition. The method further includes (2) removing unreacted and partially-reacted precursors from the substrate processing region. The method further includes (3) performing a second cycle of chemical vapor deposition comprising the operations: flowing BDEAS into the substrate processing region, flowing a second oxygen-containing precursor into the substrate processing region, forming a second conformal silicon oxide sub-layer of the conformal silicon oxide multi-layer on the patterned substrate from the BDEAS and the oxygen-containing precursor by chemical vapor deposition. The thickness of the first conformal silicon oxide sub-layer is about 100 Å or less.

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. 1 is a flow chart of a conformal silicon oxide deposition process according to disclosed embodiments.

FIG. 2 is a chart of wet etch rate ratio (WERR) of conformal silicon oxide deposited according to disclosed embodiments.

FIG. 3 shows a substrate processing system according to embodiments of the invention.

FIG. 4A shows a simplified representation of a semiconductor processing chamber according to embodiments of the present invention;

FIG. 4B shows a simplified representation 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 multi-layers on patterned substrates. The conformal silicon oxide multi-layers are each formed by depositing multiple sub-layers. Sub-layers are deposited by flowing BIS(DIETHYLAMINO)SILANE (BDEAS) and an oxygen-containing precursor into a processing chamber such that a relatively uniform dielectric growth rate is achieved across the patterned substrate surface. A plasma treatment may follow formation of sub-layers to further improve conformality and to decrease the wet etch rate of the conformal silicon oxide multi-layer film. The deposition of conformal silicon oxide multi-layers grown according to embodiments have a reduced dependence on pattern density while still being suitable for non-sacrificial applications.

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 (O₃), oxygen (O₂) and/or oxygen radicals. The inventors have discovered that forming silicon oxide multi-layers in combination with using BDEAS as the silicon-containing precursor reduces the pattern-loading effect (PLE) of the deposited silicon oxide.

Without binding the claim coverage with hypothetical mechanisms which may or may not be entirely correct, it is still beneficial to describe effects which may be occurring during the formation of the conformal silicon oxide multi-layer. BDEAS is more reactive than TEOS and other alternative silicon-containing precursors but relies more heavily on the presence of the oxygen-containing precursor due to the absence of oxygen within BDEAS. The combination of BDEAS and oxygen (O₂) preferentially reacts at or near the surface resulting in a deposition rate roughly proportional to the exposed surface area. This behavior is likely the cause of the desirable conformality reported herein. As the chemical reactions proceed, the chemical species in the near-surface area change over time. The inventors have found that the silicon oxide film becomes less conformal as the deposition proceeds. In order to regain the favorable surface-limited reaction, reacted and partially reacted chemical species may be removed from the substrate processing region and deposition may be restarted. Periodic removal of the reacted species may give rise to a growth process more uniformly dominated by surface reactions so that higher surface area regions of a patterned substrate receive additional deposition relative to lower surface area regions. The additional deposition results in a relatively constant film thickness across a patterned substrate having both high feature density areas and relatively open areas.

In order to better understand and appreciate the invention, reference is now made to FIG. 1 which is a flow chart of a conformal silicon oxide deposition process according to disclosed embodiments. The process begins when a patterned substrate is transferred into a substrate processing region (operation 110). BDEAS and an oxygen-containing precursor are flowed into the region in operation 120 and a conformal layer of silicon oxide is formed in operation 130. In some embodiments, the oxygen-containing precursor comprises molecular oxygen (O₂). In other embodiments, the oxygen-containing precursor comprises both molecular oxygen (O₂) and ozone (O₃). The flow rate of BDEAS may be less than one of 4 grams per minute (g/min), 3 g/min, 2 g/min, 1 g/min or 500 mg/min, in disclosed embodiments, to reduce the consumption of BDEAS which is not incorporated into the conformal silicon oxide film. The flow rate of BDEAS may be greater than one of 100 mg/min, 200 mg/min, 300 mg/min, 500 mg/min and 800 mg/min, in disclosed embodiments, to maintain productive growth rates of the conformal silicon oxide film. Additional embodiments result from the combination of one of the upper limits with one of the lower limits. The flow of BDEAS may be brought about by bubbling a relatively inert carrier gas like nitrogen (N₂) through a liquid supply of BDEAS and delivering a combination of nitrogen and BDEAS to the substrate processing region. The flow rate of nitrogen or a similar gas may be several tens of standard liters per minute (slms). Essentially no plasma power is applied to the substrate processing region during operation 115, in embodiments, since the precursors react in the favorable surface-limited manner without plasma excitation.

Unreacted and partially-reacted precursors are generated and linger near the patterned substrate, inhibiting highly conformal growth especially beyond a certain thickness of a deposited sub-layer of silicon oxide. Unreacted and partially-reacted precursors are removed from the substrate processing region (operation 120) to allow future deposition cycles to be more conformal. An optional plasma treatment (operation 125) may be used to densify the conformal silicon oxide layer prior to additional deposition. In some embodiments, the optional plasma treatment is not used. Once the desired thickness of silicon oxide is achieved, the patterned substrate may be removed from the substrate processing region (operation 130). The decision to terminate or continue depositing additional sub-layers is made in operation 127. If additional deposition is desired or required for a certain application, deposition begins again (operation 115). The formation of a conformal silicon oxide multi-layer may involve the deposition of two, three, four, five (or more) conformal sub-layers, in disclosed embodiments.

The plasma treatment (operation 125) may follow none, some or each of the sub-layer depositions (operation 115). Each sub-layer deposition may be referred to herein as a “cycle” of chemical vapor deposition. The combined deposition of two cycles may be described as a first and second cycle of deposition. Additional cycles may be used depending on the conformality and/or thickness required for the combined deposition. Plasma treatment involves introducing a plasma treatment gas into the substrate processing region during or after the removal of the unreacted and partially-reacted precursors (operation 120). The plasma treatment gas comprises one or more of argon, helium, ozone or nitrogen (N₂), in disclosed embodiments. Other gases may also be used. The optional inclusion of plasma treatment (operation 125) serves to densify the sub-layer prior to removing the substrate or proceeding with additional deposition. The plasma treatment has been found to be more effective for thinner sub-layers. Sub-layer thicknesses are described herein following the plasma treatment, in the event that a plasma treatment is employed. Sub-layer thicknesses may be less than or about 100 Å, less than or about 50 Å or less than or about 35 Å, in embodiments of the invention. The plasma power is applied to the substrate processing region so the plasma may be described as local. For a 300 millimeter diameter circular substrate, plasma power may be greater than 300 Watts, between 300 Watts and 1500 Watts or between 400 Watts and 1000 Watts in embodiments of the invention. Appropriate correction is required for substrates having a different exposed area used for deposition. Plasma frequencies of several hundred kilohertz (e.g. 350 kHz) appear to have reduced effect than higher frequencies (13.6 MHz). The plasma excitation frequency is greater than or about 5 MHz or about 13.6 MHz, in embodiments of the invention. Microwave frequencies may also densify conformal silicon oxide sub-layers.

Characteristics of the formation of silicon oxide depend similarly on the flow rates of oxygen (O₂) and BDEAS. Increasing the flow rate of oxygen (O₂) from a small value results in an increase in deposition rate. The deposition rate plateaus after a threshold value of the oxygen flow rate is reached. The flow rate of oxygen (O₂) may be less than one of 40 standard liters per minute (slm), 30 slm, 25 slm, 20 slm or 15 slm, in disclosed embodiments, to increase the efficient use of oxygen thereby reducing the consumption of oxygen which is not incorporated into the conformal silicon oxide film. The flow rate of oxygen (O₂) may be greater than one of 5 slm, 10 slm, 15 slm, 20 slm and 25 slm, in disclosed embodiments, to maintain productive growth rates of the conformal silicon oxide film. Additional embodiments result from the combination of one of the upper limits with one of the lower limits.

The dependence on ozone (O₃) has a different character. A relatively small concentration of ozone promotes growth rate while maintaining conformality by ensuring surface resident deposition reactions. High flows of ozone undesirably increase the pattern loading effect (PLE). In some embodiments of the invention, essentially no ozone is flowed into the substrate processing region. When employed, the flow rate of ozone is accompanied by molecular oxygen, but the flow rates given here include only the ozone contribution to the total flow rate. The flow rate of ozone (O₃) may be less than one of 1 slm, 500 sccm, 300 sccm, 200 sccm, 150 sccm, 100 sccm and 70 sccm, in order to avoid a relatively high pattern loading effect. The lower the ozone flow rate, the less the pattern loading effect. The restricted flow of a precursor is sometimes referred to as a choked flow. In this case, the choked flow of ozone may substantially confine the reaction closer to or on the patterned substrate surface, thereby promoting a uniform deposition regardless of the local exposed pattern area density.

The flows of O₃, O₂ and BDEAS as described above are concurrent, in disclosed embodiments. 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. As such, concurrent does not mean that all three flows initiate and terminate together. Concurrent, as used herein, means that a period of time exists during the deposition in which all three flows are non-zero. In disclosed embodiments, all three precursor flows are non-zero for the duration of a deposition process. 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 during deposition of each silicon oxide sub-layer may be less than for many SACVD and HARP processes (e.g. 600 Torr) due to the reactivity of BDEAS. The pressure during the formation of the conformal silicon oxide sub-layers may be less than one of 350 Torr, 300 Torr, 250 Torr, 200 Torr or 150 Torr, in disclosed embodiments, to lessen the risk of uncontrolled reaction. The pressure may be greater than one of 50 Torr, 100 Torr, 150 Torr or 200 Torr, in disclosed embodiments, to maintain productive growth rates. Additional embodiments result from the combination of an upper limits with a lower limit.

The substrate temperature is below a threshold value, in embodiments, also to ensure that the reactions associated with deposition of silicon oxide sub-layers proceed near or on the surface of the patterned substrate. The temperature of the substrate during the deposition of the conformal silicon oxide is below one of 400° C., 375° C., 350° C., 325° C. and 300° C., in disclosed embodiments. No plasma is present in the substrate processing region during deposition 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.

Supplying a choked flow of ozone along with TEOS also forms a conformal layer of silicon oxide. However, the film formed thereby possesses greater porosity and a high wet etch rate. Conformal silicon oxide multi-layers formed using BDEAS have greater density and comparatively lower wet etch rate. The wet etch rate of silicon oxide multi-layers formed according to disclosed embodiments possess wet etch rates (using a 1% HF solution) of less than one of 6, 5, 4, 3 or 2.5 times the wet etch rate of a thermally grown silicon oxide layer, in disclosed embodiments. The greater density and lower wet etch rate of conformal silicon oxide films grown in disclosed embodiments presented herein enables the conformal silicon oxide films (or portions thereof) to be incorporated into finished devices. More porous films, such as those grown with choked ozone and TEOS at low substrate temperature, must generally be removed due to the less resilient structure. As such, material grown using BDEAS and ozone may be left on the patterned substrate during subsequent processing.

During the removal of unreacted and partially-reacted precursors (operation 120) the flow of BDEAS may be terminated to allow deposition reaction by-products to be removed from the processing region. The pressure in the chamber is reduced during or following the removal of the unreacted and partially-reacted precursors (operation 120) in embodiments of the invention. The reduced pressures ensure that the by-product concentration is reduced sufficiently to restore the conformality of subsequently deposited sub-layers. Alternatively, the plasma treatment gas may be flowed into the substrate processing region to displace the unreacted and partially-reacted precursors. Regardless of the method of removal, the partial pressure of BDEAS within the substrate processing region may be reduced to below or about 10%, below or about 5% or below or about 3% of the partial pressure of BDEAS during the operation of flowing BDEAS and the oxygen-containing precursor, in embodiments of the invention. The partial pressure of BDEAS present in the substrate processing region is an indicator of the concentration of the concentration of unreacted and partially-reacted precursors residing in the near surface region.

The pressure in the substrate processing region during the plasma treatment (operation 125) of one, some or each silicon oxide sub-layer may be less than 50 Torr, 20 Torr, 10 Torr, or 8 Torr, in disclosed embodiments. The pressure may be greater than one of 1 Torr, 2 Torr, 3 Torr or 4 Torr, in disclosed embodiments. Additional embodiments of the invention result from the combination of an upper limits with a lower limit.

FIG. 2 is a chart of wet etch rate ratio (WERR) of conformal silicon oxide deposited according to disclosed embodiments. Conformal silicon oxide multi-layers were formed without an intervening plasma treatment (operation 125) with each sub-layer measuring about 35 Å. The wet etch rate ratio was measured to be 14.30. The wet etch rate ratio in each of the measurements was determined by comparing the etch rate of the conformal silicon oxide multi-layer and dividing by the wet etch rate of thermally grown silicon oxide. Thermally grown silicon oxide is a very high density form of silicon oxide having the lowest known etch rate in a hydrofluoric acid solution. In these experiments a 1% hydrofluoric acid solution in water was used to etch the silicon oxide multi-layers.

A conformal silicon oxide multi-layer was also grown with an intervening plasma treatment formed from nitrogen (N₂) and sub-layers of 35 Å thickness. The WERR was measured to be 4.41. A similarly prepared conformal silicon oxide multi-layer film having sub-layers (each 75 Å thick) was found to have a larger WERR of 5.72. This establishes that plasma treatment has a limit on the depth of treatment penetration. Thinner sub-layers are densified more completely than thicker sub-layers. Three more pairs of conformal silicon oxide multi-layers were formed with plasma treatment gases of ozone, helium and argon. The two pairs of multi-layers processed with ozone and helium plasmas were similar in WERR to one another. Argon plasmas produced lower WERR films and the nitrogen plasma, for comparison, resulted in higher WERR films. In a preferred embodiment, the plasma treatment gas comprises argon. Generally speaking, the plasma treatment gas may comprise a combination of these exemplary gases but may also comprise other gases since the chemical reactivity does not appear to play a central role.

The pattern loading was quantified by comparing the horizontal growth of the conformal silicon oxide multi-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 multiplicative factor greater than one of 2, 3, 5, 10 or 20, in disclosed embodiments. The thickness of the conformal silicon oxide multi-layer in a densely patterned region may be within one of 20%, 15%, 10%, 5% and 3% of the thickness of the conformal silicon oxide multi-layer in a sparsely patterned region, in embodiments of the invention. 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. 3 shows one such system 300 of deposition, baking and curing chambers according to disclosed embodiments. In the figure, a pair of FOUPs (front opening unified pods) 302 supply substrate substrates (e.g., 300 mm diameter wafers) that are received by robotic arms 304 and placed into a low pressure holding area 306 before being placed into one of the substrate processing chambers 308a-f. A second robotic arm 310 may be used to transport the substrate wafers from the holding area 306 to substrate processing chambers 308a-f and back.

Substrate processing chambers 308a-f may include one or more system components for depositing, annealing, curing and/or etching a dielectric film on the substrate wafer. In one configuration, two pairs of the processing chamber (e.g., 308c-d and 308e-f) may be used to deposit the dielectric material on the substrate, and the third pair of processing chambers (e.g., 308a-b) may be used to treat the deposited dielectic with a plasma. In another configuration, the same two pairs of processing chambers (e.g., 308c-d and 308e-f) may be configured to both deposit and plasma treat a deposited dielectric film on the substrate, while the third pair of chambers (e.g., 308a-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., 308a-f) may be configured to deposit and cure a dielectric film on the substrate. In yet another configuration, two pairs of processing chambers (e.g., 308c-d and 308e-f) may be used for both deposition and UV or E-beam curing of the dielectric, while a third pair of processing chambers (e.g. 308a-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 disclosed embodiments.

FIG. 4A shows a simplified representation of an exemplary substrate processing chamber within a substrate processing system 300. This exemplary substrate processing 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 system controller 453. These and other components are described below in order to understand the present invention.

Substrate 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). Vertically movable 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. Pat. 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.

Vertically movable 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 vertically movable heater 425 exposed within the chamber interior 415 are made of a ceramic material, such as aluminum oxide (Al₂O₃ or alumina) or aluminum nitride.

Reactive and carrier gases are supplied through process gas supply line 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 a process gas supply line 443 and to a cleaning/etch gas conduit 447. A gate valve 428 operates to admit or seal gas or plasma from cleaning/etch gas conduit 447 to the gas mixing block 427. The cleaning/etch gas conduit 447 receives gases from a remote plasma system (RPS 455), which has an input line 457 for receiving input gases. During deposition processing, gas supplied to gas distribution 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 gas distribution 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 vertically movable heater 425 and to an annular pumping channel 440. 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 RPS 455 from precursors supplied via the input line 457 are sent via cleaning/etch gas conduit 447 for dispersion through the gas distribution 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 substrate 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 of a particular process. 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 substrate 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 300 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 multi-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 substrate processing chamber 410. As discussed above, the portion of semiconductor processing system 300 shown includes substrate processing chamber 410 with vertically movable heater 425, a gas mixing block 427 with inputs from process gas supply line 443 and cleaning/etch gas conduit 447, and RPS 455 with input line 457. As mentioned above, the gas mixing block 427 is configured for mixing and injecting deposition gas(es) and cleaning gas(es) or other gas(es) through the process gas supply line 443 and the input line 457 to the chamber interior 415.

The RPS 455 is integrally located and mounted below the substrate processing chamber 410 with cleaning/etch gas conduit 447 coming up alongside substrate processing chamber 410 to the gate valve 428 and the gas mixing block 427, located above substrate processing chamber 410. Plasma power generator 411 and ozonator 459 are located remote from the clean room. Supply lines 483 and 485 from the gas supply panel 480 provide reactive gases to process gas supply line 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 a gas mixing system 493 that mixes selected gases before flow to the gas mixing block 427. In some embodiments, gas mixing system 493 includes a liquid injection system for vaporizing one or more reactant liquids such as BDEAS, 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 supply line 485 or input 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 BDEAS as a silicon source may be used with gas mixing system 493 in a deposition process for forming a silicon oxide film. Sources of dopants such as phosphorous and boron may include TEPO and TEB which may also be introduced to gas mixing system 493. Precursors delivered to gas 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 supply line 485 to the gas mixing block and chamber. Oxygen (O₂) flows to the chamber through supply line 483, to be combined with the reactant gases from heated gas supply 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 supply line, supply 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

1. A method for forming a conformal silicon oxide multi-layer on a patterned substrate in a substrate processing region of a processing chamber, wherein the patterned substrate has a densely patterned region and a sparsely patterned region, the method comprising sequential steps of: performing a first cycle of chemical vapor deposition comprising the operations: flowing BDEAS into the substrate processing region,flowing a first oxygen-containing precursor into the substrate processing region, wherein the operations of flowing the BDEAS and flowing the first oxygen-containing precursor are concurrent, andforming a first conformal silicon oxide sub-layer of the conformal silicon oxide multi-layer on the patterned substrate from the BDEAS and the first oxygen-containing precursor by chemical vapor deposition;removing unreacted and partially-reacted precursors from the substrate processing region; andperforming a second cycle of chemical vapor deposition comprising the operations: flowing BDEAS into the substrate processing region,flowing a second oxygen-containing precursor into the substrate processing region, andforming a second conformal silicon oxide sub-layer of the conformal silicon oxide multi-layer on the patterned substrate from the BDEAS and the second oxygen-containing precursor by chemical vapor deposition,wherein a thickness of the first conformal silicon oxide sub-layer is about 100 Å or less.

2. The method of claim 1 wherein flowing the first and second oxygen-containing precursors into the substrate processing region comprises flowing molecular oxygen into the substrate processing region.

3. The method of claim 2 wherein the first and second oxygen-containing precursors consists essentially of molecular oxygen (O2).

4. The method of claim 2 wherein the first and second oxygen-containing precursors contains essentially no ozone (O3).

5. The method of claim 1 wherein flowing the first and second oxygen-containing precursors comprise flowing molecular oxygen and ozone into the substrate processing region.

6. The method of claim 5 wherein a flow rate of the ozone is less than about 300 sccm.

7. The method of claim 1 wherein a first thickness of the conformal silicon oxide multi-layer in the densely patterned region is within 10% of a second thickness in the sparsely patterned region.

8. The method of claim 7 wherein the first and second thicknesses are measured on a substantially-vertical surface of the patterned substrate, wherein the substantially-vertical surface is substantially perpendicular to the patterned substrate.

9. The method of claim 7 wherein the two thicknesses of the conformal silicon oxide multi-layer in the densely and sparsely patterned regions are measured on a substantially-horizontal surface of the patterned substrate.

10. The method of claim 1 wherein a first thickness of the conformal silicon oxide multi-layer in the densely patterned region is within 3% of a second thickness in the sparsely patterned region.

11. The method of claim 1 wherein the operation of flowing BDEAS comprises flowing BDEAS at a rate greater than or about 100 mg/min.

12. The method of claim 1 further comprising treating the first conformal silicon oxide sub-layer with a plasma after performing the first cycle and before performing the second cycle of chemical vapor deposition.

13. The method of claim 12 wherein the plasma is formed from at least one of argon, helium, ozone or nitrogen (N2).

14. The method of claim 12 wherein the plasma is formed using a frequency greater than or about 5 MHz and a power greater than or about 300 Watts.

15. The method of claim 1 wherein a pressure in the substrate processing region during formation of the first conformal silicon oxide sub-layer is below or about 350 Torr.

16. The method of claim 1 wherein a temperature of the patterned substrate during formation of the first conformal silicon oxide sub-layer is below or about 400° C.

17. The method of claim 1 wherein the thickness of the first conformal silicon oxide sub-layer is about 50 Å or less.

18. The method of claim 1 wherein an average exposed substantially-vertical area prior to deposition in the densely patterned region exceeds that of the sparsely patterned region by a multiplicative factor of about 2.

19. The method of claim 1 further comprising an operation of flowing a carrier gas which carries the BDEAS into the substrate processing region during the first cycle of chemical vapor deposition.