METHOD OF PROCESSING A SUBSTRATE

Embodiments of the present disclosure generally relate to a method of processing a substrate. The method includes exposing the substrate positioned in a processing volume of a processing chamber to a hydrocarbon-containing gas mixture, exposing the substrate to a boron-containing gas mixture, and generating a radio frequency (RF) plasma in the processing volume to deposit a boron-carbon film on the substrate. The hydrocarbon-containing gas mixture and the boron-containing gas mixture are flowed into the processing volume at a precursor ratio of (boron-containing gas mixture/((boron-containing gas mixture)+hydrocarbon-containing gas mixture) of about 0.38 to about 0.85. The boron-carbon hardmask film provides high modulus, etch selectivity, and stress for high aspect-ratio features (e.g., 10:1 or above) and smaller dimension devices (e.g., 7 nm node or below).

FIELD

Embodiments of the present disclosure generally relate a method and, more specifically, to a method of processing a substrate.

BACKGROUND

The demands for greater integrated circuit densities impose demands on the process sequences used in the manufacture of integrated circuit components. For example, in process sequences that use conventional photolithographic techniques, a layer of energy sensitive resist is formed over a stack of material layers disposed on a substrate. The energy sensitive resist layer is exposed to an image of a pattern to form a photoresist mask. Thereafter, the mask pattern is transferred to one or more of the material layers of the stack using an etch process. The chemical etchant used in the etch process is selected to have a greater etch selectivity for the material layers of the stack than for the mask of energy sensitive resist. The etch selectivity to the one or more material layers of the stack over the resist layer prevents the energy sensitive resist layer from being consumed prior to completion of the pattern transfer.

As the pattern dimensions are reduced, the thickness of the energy sensitive resist is correspondingly reduced in order to control pattern resolution. Such thin resist layers can be insufficient to mask underlying material layers during the pattern transfer operation due to attack by the chemical etchant. An intermediate layer, called a hardmask, is often used between the energy sensitive resist layer and the underlying material layers to facilitate pattern transfer because of greater resistance of the hardmask to the chemical etchant. As critical dimensions (CD) decrease, current hardmask materials lack the desired etch selectivity relative to underlying materials.

Therefore there is a need for methods for depositing hardmask films with improved etch selectivity.

SUMMARY

Embodiments included herein include methods of processing a substrate. The methods include depositing a boron-carbon film, and the boron-carbon film exhibits improved etch selectivity.

In one embodiment, a method of processing a substrate is provided. The method includes exposing the substrate positioned in a processing volume of a processing chamber to a hydrocarbon-containing gas mixture, exposing the substrate to a boron-containing gas mixture, and generating a radio frequency (RF) plasma in the processing volume to deposit a boron-carbon film on the substrate. The hydrocarbon-containing gas mixture and the boron-containing gas mixture are flowed into the processing volume at a precursor ratio of (boron-containing gas mixture/((boron-containing gas mixture)+hydrocarbon-containing gas mixture) of about 0.38 to about 0.85. The boron-carbon film has about 55 atomic percentage to about 95 atomic percentage of boron.

In another embodiment, a method of processing a substrate is provided. The method includes exposing the substrate positioned in a processing volume of a processing chamber to a hydrocarbon-containing gas mixture, exposing the substrate to a boron-containing gas mixture, and generating a radio frequency (RF) plasma in the processing volume to deposit a boron-carbon film on the substrate. The hydrocarbon-containing gas mixture and the boron-containing gas mixture are flowed into the processing volume at a precursor ratio of (boron-containing gas mixture/((boron-containing gas mixture)+hydrocarbon-containing gas mixture) of about 0.38 to about 0.85. The boron-carbon film has about 35 atomic percentage to about 55 atomic percentage of boron.

In yet another embodiment, a method of processing a substrate is provided. The method includes exposing the substrate positioned in a processing volume of a processing chamber to a hydrocarbon-containing gas mixture, exposing the substrate to a boron-containing gas mixture, and generating a radio frequency (RF) plasma in the processing volume to deposit a boron-carbon film on the substrate. The hydrocarbon-containing gas mixture and the boron-containing gas mixture are flowed into the processing volume at a precursor ratio of (boron-containing gas mixture/((boron-containing gas mixture)+hydrocarbon-containing gas mixture) of about 0.38 to about 0.85. The hydrocarbon-containing gas mixture includes propylene (C3H6). The boron-carbon film has about 55 atomic percentage to about 95 atomic percentage of boron.

DETAILED DESCRIPTION

Embodiments of the present disclosure generally relate to a method of processing a substrate. The present disclosure describes techniques for deposition of hardmasks (e.g., boron-carbon films) with high modulus and etch selectivity on a substrate. The method includes the fabrication of high-density boron-carbon hardmask films with increased concentration of boron and lower incorporated hydrogen. Decreasing a flow rate of a hydrocarbon-containing gas source increases the percentage of boron (B %) in the boron-carbon hardmask films. The boron-carbon hardmask films provide high modulus, etch selectivity, and stress for high aspect-ratio features (e.g., 10:1 or above) and smaller dimension devices (e.g., 7 nm node or below). Embodiments described herein are compatible with current carbon hard mask process integration schemes. Thus, introduction of the methods into existing device manufacturing lines will not require substantial changes in upstream or downstream processing methods or equipment related thereto. Embodiments disclosed herein may be useful for, but are not limited to, deposition of boron-carbon hardmasks.

As used herein, the term “about” refers to a +/−10% variation from the nominal value. It is to be understood that such a variation can be included in any value provided herein.

Embodiments described herein will be described below in reference to a plasma enhanced chemical vapor deposition (PECVD) process that can be carried out using any suitable thin film deposition system. Examples of suitable systems include the CENTURA® systems which can use a DxZ™ processing chamber, PRECISION 5000® systems, PRODUCER™ systems, PRODUCER GT™ and the PRODUCERSE™ processing chambers which are commercially available from Applied Materials, Inc., of Santa Clara, Calif. Other tools capable of performing PECVD processes can also be adapted to benefit from the embodiments described herein. In addition, any system enabling the PECVD processes described herein can be used to advantage. The apparatus description described herein is illustrative and should not be construed or interpreted as limiting the scope of the embodiments described herein.

FIG. 1illustrates a schematic view of a substrate processing system132, according to one embodiment. The substrate processing system132is configured to perform hardmask layer deposition. As shown, the substrate processing system132includes a processing chamber100coupled to a gas panel130and a controller110.

The processing chamber100is configured to perform a variety of processing methods on a substrate190disposed within. For example, the processing chamber100is configured to deposit a hardmask on the substrate190. As shown, the processing chamber100includes a top wall124, one or more side walls101, and a bottom wall122that define an interior processing volume126. A support pedestal150, for supporting the substrate190, is positioned in the interior processing volume126of the processing chamber100. The support pedestal150is supported by a stem160, and the support pedestal150and/or stem160can include aluminum, ceramic, and any other suitable materials, such as stainless steel. The support pedestal150can be moved in a vertical direction inside the processing chamber100using a displacement mechanism (not shown) (e.g., an actuator that raises and lowers the support pedestal). In some embodiments, the support pedestal150includes an electrostatic chuck (ESC). The ESC secures the substrate190during processing.

The support pedestal150can include an heater element170embedded in the support pedestal150. The heater element170is configured to control the temperature of the substrate190supported on a surface192of the support pedestal150. The support pedestal150can be resistively heated by applying an electric current from a power supply106to the heater element170. The electric current supplied from the power supply106is regulated by the controller110to control the heat generated by the heater element170, thus maintaining the substrate190and the support pedestal150at a substantially constant temperature during film deposition. The supplied electric current is adjusted to selectively control the temperature of the support pedestal150between about 400° C. and about 700° C.

A temperature sensor172, such as a thermocouple, can be embedded in the support pedestal150to monitor the temperature of the support pedestal150. The measured temperature is used by the controller110to control the power supplied to the embedded heater element170to maintain the substrate190at a desired temperature.

A vacuum pump102is coupled to a port formed in the bottom wall122of the processing chamber100. The vacuum pump102is used to maintain a desired gas pressure in the processing chamber100. The vacuum pump102also evacuates post-processing gases and by-products of the process from the processing chamber100.

A gas distribution assembly120having a plurality of apertures128is disposed on the top of the processing chamber100above the support pedestal150. The gas distribution assembly120is configured to flow one or more process gases into the processing chamber100. The apertures128can have different sizes, number, distributions, shape, design, and diameters to facilitate the flow of the various process gases into the processing chamber100. The gas distribution assembly120is connected to the gas panel130that supplies various gases to the interior processing volume126during substrate processing. Plasma can be formed from the process gas mixture exiting the gas distribution assembly120to enhance thermal decomposition of the process gases, resulting in the deposition of material on a surface191of the substrate190.

The gas distribution assembly120and the support pedestal150can form a pair of spaced electrodes in the interior processing volume126. One or more radio frequency (RF) power sources140provides a bias potential through a matching network138to the gas distribution assembly120to facilitate generation of plasma between the gas distribution assembly120and the support pedestal150. Alternatively, the RF power sources140and matching network138are coupled to the gas distribution assembly120, the support pedestal150, or coupled to both the gas distribution assembly120and the support pedestal150, or coupled to an antenna (not shown) disposed exterior to the processing chamber100. In one embodiment, the RF power sources140provide between about 100 W and about 3,000 W at a frequency of about 50 kHz to about 13.6 MHz. In another embodiment, the RF power sources140provide between about 500 W and about 1,800 W at a frequency of about 50 kHz to about 13.6 MHz.

As shown, the controller110includes a central processing unit (CPU)112, a memory116, and a support circuit114configured to control the process sequence and regulate the gas flows from the gas panel130. The CPU112is any form of a general-purpose computer processor that is used in an industrial setting. The software routines can be stored in the memory116, such as random access memory, read only memory, floppy, or hard disk drive, or other form of digital storage. The support circuit114is conventionally coupled to the CPU112and can include cache, clock circuits, input/output systems, power supplies, and the like. Bi-directional communications between the controller110and the various components of the substrate processing system132are handled through numerous signal cables collectively referred to as signal buses118.

FIG. 2is a flow diagram of method200operations for depositing a boron-carbon film, according to one embodiment. Although the method200operations are described in conjunction withFIGS. 2 and 3, persons skilled in the art will understand that any system configured to perform the method operations, in any order, falls within the scope of the embodiments described herein. The method200can be stored or accessible to the controller110as computer readable media containing instructions, that when executed by the CPU112of the controller, cause the system132and/or processing chamber100to perform the method200.

The method200begins at operation210, where a substrate disposed in a processing volume of a processing chamber is exposed to a hydrocarbon-containing gas. The processing chamber can be the processing chamber100depicted inFIG. 1.FIG. 3illustrates a schematic cross-sectional view of a substrate structure300, according to one embodiment. As shown, the substrate structure300includes the substrate190. The substrate190can have a substantially planar surface191having a structure formed thereon or therein at a desired elevation. Alternatively, the substrate190can have patterned structures, for example, a surface having trenches, holes, or vias formed therein. While the substrate190is illustrated as a single body inFIG. 3, it is understood that the substrate190can contain one or more materials used in forming semiconductor devices, such as metal contacts, trench isolations, gates, bitlines, or any other interconnect features. The substrate190can include any number or combination of metallic, semiconducting, and/or insulating layers thereon.

The substrate190can include one or more metal layers, one or more dielectric materials, semiconductor material, and combinations thereof utilized to fabricate semiconductor devices. For example, the substrate190includes an oxide material, a nitride material, a polysilicon material, or the like, depending upon application. In one embodiment where a memory application is desired, the substrate190includes the silicon substrate material, an oxide material, and a nitride material, with or without polysilicon sandwiched in between.

In another embodiment, the substrate190includes a plurality of alternating oxide and nitride materials (i.e., oxide-nitride-oxide (ONO)) deposited on the surface191of the substrate190. In various embodiments, the substrate190includes a plurality of alternating oxide and nitride materials, one or more oxide or nitride materials, polysilicon or amorphous silicon materials, oxides alternating with amorphous silicon, oxides alternating with polysilicon, undoped silicon alternating with doped silicon, undoped polysilicon alternating with doped polysilicon, or undoped amorphous silicon alternating with doped amorphous silicon. The substrate190can be any substrate or material surface upon which film processing is performed. For example, the substrate190can include crystalline silicon, silicon oxide, silicon oxynitride, silicon nitride, strained silicon, silicon germanium, tungsten, titanium nitride, doped or undoped polysilicon, doped or undoped silicon wafers and patterned or non-patterned wafers, silicon on insulator (SOI), carbon doped silicon oxides, silicon nitrides, doped silicon, germanium, gallium arsenide, glass, sapphire, low-k dielectrics, and combinations thereof.

The hydrocarbon-containing gas mixture is flowed from the gas panel130into the interior processing volume126through the gas distribution assembly120. The gas mixture includes at least one hydrocarbon compound. The gas mixture can further include an inert gas, a dilution gas, or combinations thereof. The hydrocarbon can be any gas or liquid that can be vaporized to simplify the hardware needed for material metering, control and delivery to the chamber. In one embodiment, the hydrocarbon source is a gaseous hydrocarbon, such as a linear hydrocarbon. In one embodiment, the hydrocarbon compound has a general formula CxHy, where x has a range of between 1 and 20 and y has a range of between 1 and 20. In one embodiment, the hydrocarbon compound is an alkane. Suitable hydrocarbon compounds include, for example, alkanes such as methane (CH4), ethane (C2H6), propylene (C3H6), propane (C3H8), butane (C4H10) and its isomer isobutane, pentane (C5H12), hexane (C6H14) and its isomers isopentane and neopentane, hexane (C6H14) and its isomers 2-methylpentane, 3-methylpentane, 2,3-dimethylbutane, and 2,2-dimethyl butane, or combinations thereof. Additional suitable hydrocarbons include, for example, alkenes, such as acetylene, ethylene, propylene, butylene and its isomers, pentene and its isomers, and the like, dienes such as butadiene, isoprene, pentadiene, hexadiene, or combinations thereof.

The flow rate of the hydrocarbon-containing gas mixture can be from about 2,000 sccm to about 4,500 sccm, for example, about 2,200 sccm to about 4,000 sccm. In one embodiment where C3H6is used as the hydrocarbon-containing gas source, the flow rate of the hydrocarbon-containing gas mixture is from about 2,250 sccm to about 3,000 sccm, such as from about 2,300 sccm to about 2,800 sccm.

Suitable dilution gases such as helium (He), argon (Ar), hydrogen gas (H2), nitrogen gas (N2), ammonia (NH3), or combinations thereof, among others, can be added to the gas mixture, if desired. Ar, He, and N2are used to control the density and deposition rate of the amorphous carbon layer. Alternatively, dilution gases are not used during the deposition.

In some cases, a nitrogen-containing gas is supplied with the hydrocarbon-containing gas mixture into the processing chamber100to control the hydrogen ratio of the amorphous carbon layer. Suitable nitrogen-containing compounds include, for example, nitrogen gas, ammonia, pyridine, aliphatic amine, amines, nitriles, and similar compounds.

An inert gas, such as argon (Ar) and/or helium (He) can be supplied with the hydrocarbon-containing gas mixture into the processing chamber100. Other inert gases, such as nitrogen gas (N2), can also be used to control the density and deposition rate of the amorphous carbon layer. Additionally, a variety of other processing gases can be added to the gas mixture to modify properties of the amorphous carbon material. In one embodiment, the processing gases include reactive gases, such as hydrogen gas (H2), ammonia (NH3), a mixture of hydrogen gas (H2) and nitrogen gas (N2) (also known as forming gas), or combinations thereof. The addition of H2and/or NH3is used to control the hydrogen ratio (e.g., carbon to hydrogen ratio) of the deposited amorphous carbon layer. The hydrogen ratio present in the amorphous carbon film provides control over layer properties, such as reflectivity.

At operation220, the substrate190is exposed to a boron-containing gas mixture. The boron-containing gas mixture is flowed from the gas panel130into the interior processing volume126through the gas distribution assembly120. In one embodiment, the boron-containing gas mixture includes a boron-containing compound and a dilution gas. Examples of boron-containing compounds include diborane (B2H6), trimethyl boronane [TMB] (B(CH3)3), triethylborane [TEB] (B(C2H5)3), methyl borane, dimethyl borane, ethyl borane, diethyl borane, ortho-carborane (C2B10H12), and similar compounds. Suitable dilution gases such as hydrogen gas (H2), helium (He), argon (Ar), nitrogen gas (N2), ammonia (NH3), or combinations thereof, among others, can be included. In one example, the boron-containing gas mixture includes B2H6and H2.

In various embodiments where C3H6is used as the hydrocarbon-containing gas source and 9 wt. % B2H6diluted in H2is used as the boron-containing gas source, a ratio of the flowrate (hereafter ratio) of the hydrocarbon-containing gas source to the boron-containing gas source can be in a range between about 0.05:1 and about 0.13:1, such as between about 0.07:1 and about 0.12:1, for example about 0.9:1 to about 0.11:1.

In one embodiment where 9 wt. % diborane diluted in H2is used as the boron-containing gas source, the flow rate of the boron-containing gas mixture varies from about 1,000 sccm to about 10,000 sccm, such as about 1,800 sccm to about 3,500 sccm, for example, about 2,300 sccm. In another embodiment where 6% diborane diluted in H2is used as the boron-containing gas source, the flow rate of the boron-containing gas mixture is from about 5,000 sccm to about 15,000 sccm, for example, about 13,000 sccm. In yet another embodiment where 12% diborane diluted in H2is used as the boron-containing gas source, the flow rate of the boron-containing gas mixture is from about 2,000 sccm to about 8,000 sccm, for example about 2,200 sccm to about 7,500 sccm.

The hydrocarbon-containing gas mixture can be introduced into the interior processing volume126for about 3 seconds to about 30 seconds, for example, about 15 seconds, which varies depending upon the size of the substrate. The flowing of the hydrocarbon-containing gas mixture prior to the introduction of the boron-containing gas can provide continuous thermal and pressure stabilization of the interior processing volume126. The boron-containing gas mixture is then flowed into the interior processing volume126for about 0.5 seconds to about 5 seconds, for example, about 1 seconds to about 2 seconds (the flowing time can vary as long as the flow is long enough for the boron-containing gas mixture to start reaching the interior processing volume126), prior to striking the RF plasma. It is contemplated that operation210can be performed simultaneously with, prior to, after, or partially overlapping with the processes of operation220.

At operation230, RF plasma is generated in the interior processing volume126to deposit a boron-carbon film304on the substrate190. The plasma can be formed by capacitive or inductive means, and can be energized by coupling RF power into the precursor gas mixture. The RF power can be a dual-frequency RF power using a frequency in a range from about 0.4 MHz to about 300 MHz. For example, the RF power is a dual-frequency RF power that has a high frequency component and a low frequency component. The RF power is typically applied at a power level between about 50 W and about 2,500 W, which can be all high-frequency RF power, for example at a frequency of about 13.56 MHz, or can be a mixture of high-frequency power and low frequency power, for example, at a high frequency of about 13.56 MHz and a low frequency of about 0.35 kHz.

It has been observed that increasing boron doping in boron-carbon films can increase etch selectivity and film transparency while reducing stress of boron-carbon films. While the amount of boron in the boron-carbon films can be increased by increasing the flow of the boron-containing gas mixture (e.g., B2H6) during the deposition, the hydrogen content in the resulting boron-carbon films will also be increased inevitably. The mechanical strength and etch selectivity of the film can be affected due to the presence of a large amount of hydrogen in the boron-carbon films. However, it has been surprisingly discovered that decreasing the hydrocarbon-containing gas mixture during the deposition can result in increased boron content and reduced hydrogen content in the boron-carbon film304, when compared to conventionally deposited amorphous carbon layers (e.g., APF™ hardmasks).

Table 1 below depicts various flow combinations of a hydrocarbon-containing gas source and a boron-containing gas source used for forming an amorphous carbon film reference (baseline) and boron-carbon films (cases 1-4). Case 1 is an example where only the hydrocarbon-containing gas source is decreased when compared to the baseline. Case 2 is an example where the hydrocarbon-containing gas source is decreased and the boron-containing gas source is increased when compared to the baseline. Case 3 is an example where only the boron-containing gas source is increased when compared to the baseline. Case 4 is an example where the hydrocarbon-containing gas source is decreased and the boron-containing gas source is increased when compared to the baseline. Table 2 below depicts boron-carbon film properties for the amorphous carbon film reference and boron-carbon films (cases 1-4) formed according to flow combinations shown in Table 1. The percentage of boron incorporation in the boron-carbon films is calculated as follows: ((B/(B+C) %).

As can be seen in Table 2, the boron incorporation was increased through three different conditions: (a) C3H6reduction only (e.g., case 1); (b) B2H6/H2increase only (e.g., case 3); and (c) combination of (1) and (2) (e.g., cases 2 and 4). When the flow rate of the hydrocarbon-containing gas source decreases further (e.g., case 2), the boron content in the final boron-carbon film increases accordingly. However, when the flow rate of the boron-containing gas source greatly increases (e.g., case 3), the boron content in the final boron-carbon film decreases instead. Particularly, the decreased refractive index and the increased film stress suggest that higher content of hydrogen can etch or consume boron, resulting in inefficient boron increase in the final boron-carbon film.

FIG. 4is a plot400illustrating boron (B) percentage with respect to precursor ratio (PR). The plot400is based on an example where C3H6is used as the hydrocarbon-containing gas source and 9 wt. % B2H6diluted in H2is used as the boron-containing gas source. The PR inFIG. 4is calculated as follows: PR=(9 wt. % B2H6in H2/((9 wt. % B2H6in H2)+C3H6). As can be seen, PR increases as the flow rate of the hydrocarbon-containing gas source decreases (e.g., cases 1 and 2), which in turn results in increased boron doping (B %) in a boron-carbon film. It is contemplated that the precursor ratio discussed herein are equally applicable to other hydrocarbon-containing gas mixtures and boron-containing gas mixtures mentioned in this disclosure. In addition, while the PR is shown varying from 0.3 to 0.55, lower or higher PR is contemplated, depending on the desired boron content in the final boron-carbon films. In various examples, the PR can be in a range from 0.38 to 0.85, for example from about 0.45 to about 0.75. It is proposed that the generated RF plasma is more uniform when the PR of the plasma is increased. The uniformity of the RF plasma corresponds to uniformity of the deposited film. Thus, unexpectedly, increasing the B % of the RF plasma results in a more uniform deposited film.

Since the boron content is directly related to PR, any quantity/percentage of boron in the as-deposited boron-carbon film304can be achieved by tuning the PR. In any case, the atomic percentage of boron incorporation in the film can be calculated as follows: ((B/(B+C) %). In various embodiments of the present disclosure, the boron-carbon film304contains at least 50, 55, 60, 65, 70, 75, 80, 85, or 90 atomic percentage of boron. In one embodiment, the boron-carbon film304contains from about 45 to about 95 atomic percentage of boron. In another embodiment, the boron-carbon film contains from about 55 to about 90 atomic percentage of boron. In yet another embodiment, the boron-carbon film contains from about 60 to about 85 atomic percentage of boron. Likewise, the atomic percentage of carbon incorporation in the film can be calculated as follows: ((C/(B+C) %). In various embodiments of the present disclosure, the boron-carbon film304contains at least 10, 15, 20, 25, 30, 35, 40, 45, or 50, atomic percentage of carbon. In one embodiment, the boron-carbon film304contains from about 15 to about 55 atomic percentage of carbon. In another embodiment, the boron-carbon film304contains from about 25 to about 45 atomic percentage of carbon. In various embodiments, the boron-carbon film304contains less than about 10, 15, or 20 atomic percentage of hydrogen. The boron-carbon film304can be crystalline or amorphous.

At operation240, a decision is made as to determine whether the deposited boron-carbon film304has reached a target thickness. The boron-carbon film304can have a target thickness corresponding to the subsequent etching requirements of the substrate190. The flowing the hydrocarbon-containing gas mixture into the processing volume (operation210), the flowing a boron-containing gas mixture into the processing volume (operation220), and the generating the RF plasma in the processing volume to deposit the boron-carbon film (operation230) can be repeated until a target thickness is achieved. In one embodiment, the boron-carbon film is deposited to a thickness between about 100 Å and about 30,000 Å (e.g., from about 1,000 Å to about 18,000 Å; from about 100 Å to about 20,000 Å; from about 300 Å to about 5,000 Å; or from about 1,000 Å to about 2,000 Å.)

At optional operation250, additional processing is performed on the substrate structure300. For example, a patterned photoresist (not shown) is formed over the boron-carbon film304. The boron-carbon film304can be etched in a pattern corresponding with the patterned photoresist layer followed by etching the pattern into the substrate190. Material can be deposited into the etched portions of the boron-carbon film304. The boron-carbon film304can be removed using a solution including hydrogen peroxide and sulfuric acid, or any etch chemistries containing oxygen and halogens (e.g. fluorine or chlorine). The boron-carbon film304can be removed by a chemical mechanical polishing (CMP) process.

B doping generally reduces sp3carbon-hydrogen (C—H) bonding in the boron-carbon films. B dopants form at interstitial sites. Neighboring H atoms combine to make hydrogen gas (H2), leaving the film. The remaining C and B atoms then form C—B bonds. It is theorized that sp3C—H bonds leads to lattice relaxation, resulting in tensile stress. B doping generally increases C═C and C≡C bonding in the boron-carbon films, increasing the C/H ratio. sp3C—H bonds are also reduced, resulting in compressive stress. Increasing B2H6flow can include greater amount of sp3C—H bonds, leading to higher H content. Shorter chained C molecules are preferred, in order to prevent formation of C—C polymer chains in the film.

Current low temperature boron-containing carbon hardmasks achieve good etch selectivity, mechanical strength, and transparency compared to previous amorphous carbon hardmask films. However, the amorphous nature, higher incorporated hydrogen and lower modulus (˜100 GPa) of low temperature boron-containing hardmask films limit fabrication of high aspect-ratio features and smaller dimension devices. To enable next-generation integrated circuit chipsets, embodiments of the present disclosure provide for the fabrication of high-density boron-carbon hardmask films at higher temperatures (e.g., ≥400° Celsius), with increased concentration of boron and lower incorporated hydrogen.

The boron-carbon films, as deposited, have heavily linked boron-carbon (B—C) networks, which protects the boron-carbide film from etchants. Thus, the boron-carbide films exhibit high selectivity with respect to the substrate for further etching processes (either oxide or nitride substrates). The B—C bonds are shorter than carbon-carbon (C—C) bonds, which shifts the boron-carbon film stress towards tensile stress. The boron-carbon films have low stress, resulting in less substrate bowing. The boron-carbon films have high modulus and hardness, making the boron-carbon films mechanically robust. In addition, the B—C bonds increase the band gap of the film. Thus, the boron-carbon films are transparent to at least some of the frequencies of light used in photolithography. Also, reduction of the boron-containing gas mixture leads to lower cost of ownership, as less of the boron-containing gas (e.g., diborane) is needed without reducing desired properties of the films.

In general, the following exemplary deposition process parameters are used to form the boron-containing amorphous carbon layer. The process parameters can range from a substrate temperature of about 400° C. to about 700° C. (e.g., between about 450° C. to about 650° C.). The chamber pressure can range from a chamber pressure of about 1 Torr to about 20 Torr (e.g., between about 2 Torr and about 10 Torr). The flow rate of the hydrocarbon-containing gas (e.g., C3H6) can be from about 150 sccm to about 400 sccm, for example, about 160 sccm to about 260 sccm. The flow rate of a dilution gas (e.g., He) can individually range from about 0 sccm to about 3,000 sccm (e.g., from about 1,200 sccm to about 2,000 sccm). The flow rate of an inert gas (e.g., Ar) can individually range from about 0 sccm to about 10,000 sccm (e.g., from about 2,500 sccm to about 4,000 sccm). The flow rate of the boron-containing gas mixture (e.g., from about 6 wt. % to about 10 wt. % B2H6diluted in H2) can be from about 1,000 sccm to about 3,500 sccm, for example, about 1500 sccm to about 2300 sccm. The high-frequency RF power can be between 1,000 W and 3,000 W, for example, about 2,000 W. The low-frequency RF power can be between about 0 W and about 1,500 W, for example, about 800 W. The spacing between the surface191of the substrate190(e.g., the top surface) and the gas distribution assembly120can be between about 100 mm to about 600 mm (e.g., between about 150 mm to about 400 mm). The power voltage for the ESC can be between about 0 V and about 1000 V, for example, about 600 V to about 750 V. The boron-carbon film can be deposited to a thickness between about 100 Å and about 30,000 Å, for example, about 1,000 Å to about 18,000 Å. The above process parameters provide a typical deposition rate for the boron-containing amorphous carbon layer in the range of about 100 Å/min to about 10,000 Å/min and can be implemented on a 300 mm substrate in a deposition chamber available from Applied Materials, Inc. of Santa Clara, Calif.

The as-deposited boron-carbon film304can have a refractive index (n) at a 633 nm wavelength of greater than about 2, for example, about 2.34. The as-deposited boron-carbon film304can have an extinction coefficient (k) at a 633 nm wavelength of less than about 0.1, for example, 0.04 or less. The as-deposited boron-carbon film304can have an elastic modulus of about 150 MPa to about 400 MPa. The as-deposited boron-carbon film304can have a stress of about −200 MPa to about 200 MPa (e.g., about −50 MPa to about 100 MPa). The as-deposited boron-carbon film304can have a density of greater than 1.5 g/cc, for example, about 1.85 g/cc.

As described above, a method for processing a substrate is provided. The method includes the fabrication of high-density boron-carbon hardmask films with increased concentration of boron and lower incorporated hydrogen. Decreasing the flow rate of the hydrocarbon-containing gas source increases the B % in the boron-carbon hardmask film.

The boron-carbon hardmask films provide high modulus, etch selectivity, and stress for high aspect-ratio features (e.g., 10:1 or above) and smaller dimension devices (e.g., 7 nm node or below). Embodiments described herein are compatible with current carbon hard mask process integration schemes. Thus, introduction of the methods into existing device manufacturing lines will not require substantial changes in upstream or downstream processing methods or equipment related thereto.