Detailed Description
The following disclosure describes techniques for in-situ removal of residual high-k dielectric material from a substrate processing chamber. Certain details are set forth in the following description and figures to provide a thorough understanding of various embodiments of the disclosure. Additional details describing well-known structures and systems typically associated with plasma cleaning will not be set forth in the following disclosure to avoid unnecessarily obscuring the description of the various embodiments.
Much of the details, dimensions, angles, and other features shown in the drawings are merely illustrative of particular embodiments. Accordingly, other embodiments may have other details, components, dimensions, angles, and features without departing from the spirit or scope of the disclosure. Furthermore, further embodiments of the disclosure may be practiced without several of the details described below.
Embodiments described herein will be described below with reference to a high-k dielectric deposition process that may be performed using any suitable thin film deposition system. One example of such a system is an AKT-90K PECVD system suitable for substrates having substrate dimensions of 3000mm by 3000mm or larger, which is commercially available from Applied Materials, Inc. (Applied Materials Inc.) of Santa Clara, Calif. (Santa Clara, Calif.). Another example of such a system is an AKT-25K PECVD system or AKT-25KALD system suitable for substrates having dimensions of 1850mm by 1500mm or larger, which are commercially available from Applied Materials, Inc. of Santa Clara, California. Other tools capable of performing high-k dielectric deposition processes may also be suitable to benefit from the embodiments described herein. Additionally, any system capable of implementing the high-k dielectric deposition process described herein may be used to advantage. The device descriptions described herein are illustrative and should not be interpreted or otherwise construed as limiting the scope of the embodiments described herein.
Embodiments of the present disclosure generally relate to in-situ removal of, for example, ZrO from a processing chamber2And HfO2The high dielectric constant dielectric material of (1). Processing chambers include, but are not limited to, PECVD, ALD, or other processing chambers for fabricating high resolution display backplane TFT circuits. ZrO (ZrO)2And HfO2Are currently used in the semiconductor industry, and potentially in the flat panel display industry to enable high resolution display devices (such as Virtual Reality (VR)) Device) is formed. Such as ZrO2And HfO2Are particularly critical for achieving high resolution display devices (e.g., pixel per inch ("PPI") > 2000). Currently, as the entire pixel area is reduced to increase the resolution, the area of the storage capacitor needs to be reduced in the pixel circuit. To achieve the same capacitance, the current dielectric layer (e.g., SiN, dielectric constant (k) -7) used in the storage capacitor is being replaced by a high-dielectric constant dielectric material, such as ZrO with k > 202And HfO with k > 252. One factor for achieving high-k dielectric materials in display applications is the efficient removal of residual high-k dielectric material from the processing chamber to reduce particles and improve yield.
In general, the deposition of high dielectric constant dielectric materials is not limited to substrates and forms residual films throughout the chamber. This residual film can lead to particle formation, reduced uniformity, and plugged gas inlets, resulting in yield loss and increased cost of ownership. One way to remove unwanted residual films on the chamber walls or other chamber components is to periodically disassemble the chamber after several deposition cycles and remove the film with a solution or solvent. Disassembling the chamber, cleaning the components, and reassembling the chamber can take a significant amount of time and significantly impact the usable time of the tool. Another method is to apply plasma by applying Radio Frequency (RF) energy to promote excitation and/or dissociation of the reactive gas. The plasma includes highly reactive species that react with and etch unwanted residual materials. For example, NF3Plasma is widely used in the display industry to remove SiO from process chambersxAnd SiNxAnd (3) a membrane. However, NF3The plasma is generally unable to etch the remaining high-k dielectric material.
Embodiments of the present disclosure include both chamber cleaning processes and modifications to current hardware materials. Some embodiments of the present disclosure effectively remove residual high-permittivity dielectric material from a processing chamber by introducing reactive species formed from a halogen-containing gas mixture into the processing chamber to react with the residual high-permittivity dielectric material. The reactive species may be generated as an in-situ plasma (e.g., formed inside the processing chamber) or an ex-situ plasma (e.g., formed via a remote plasma source). The plasma may be generated by, but is not limited to, inductively-coupled plasma (ICP), capacitively-coupled plasma (CCP), Remote Plasma Source (RPS), or microwave plasma.
In some embodiments of the present disclosure, residual high-k dielectric material is removed by flowing a halogen-containing gas mixture into a processing chamber and then exciting and/or dissociating the halogen-containing gas mixture to form a plasma in the processing chamber. The excited radicals from the halogen-containing gas mixture etch residual high dielectric constant dielectric material from the chamber body. Plasma of the halogen-containing gas mixture etches the high dielectric constant dielectric material and aluminum if no additional bias is applied, but generally does not etch or minimally etches the coating material (e.g., Al)2O3). Thus, in some embodiments of the present disclosure, the thin coating material protects the aluminum chamber components during the cleaning process. The coating material may be applied using any suitable process. In some embodiments, the coating material is applied by a surface anodization process, a plasma spray process, or a thermal spray process. If the coating material must be removed, an additional bias voltage may be applied to the plasma of the halogen-containing gas mixture during the process to facilitate etching of the coating material. Thus, depending on the plasma conditions, the halogen-containing gas mixture may be used to selectively remove the high-k dielectric material relative to the coating material, or to remove both the high-k dielectric material and the coating material.
Fig. 1A illustrates a cross-sectional view of asubstrate processing chamber 100 that may benefit from a cleaning process in accordance with one or more embodiments of the present disclosure. FIG. 1B illustrates thesubstrate processing chamber 100 of FIG. 1A with residual films formed on one or more interior surfaces that may be removed using one or more embodiments of the present disclosureA cross-sectional view. Thesubstrate processing chamber 100 may be used to perform CVD, plasma enhanced CVD (PE-CVD), pulsed CVD, ALD, PE-ALD, metal-organic chemical vapor deposition (MOCVD), or combinations thereof. In some embodiments, the substrate processing chamber may be configured to deposit a high dielectric constant dielectric layer, such as ZrO2Or HfO2. In some embodiments, thesubstrate processing chamber 100 is configured to process asubstrate 102 using plasma when forming structures and devices on a large area substrate 102 (hereinafter substrate 102) for manufacturing a Liquid Crystal Display (LCD), a flat panel display, an Organic Light Emitting Diode (OLED), or a photovoltaic cell of a solar cell array.
Thesubstrate processing chamber 100 generally includessidewalls 142, abottom wall 104, and alid assembly 112, which define aprocess volume 106. In one embodiment,lid assembly 112 is generally comprised of aluminum. Thelid assembly 112 may be anodized to form Al on the surface of the lid assembly 1122O3And (3) a layer. In another embodiment, thelid assembly 112 is made of stainless steel, nickel-iron alloy (e.g., Invar, which is a nickel-iron alloy known as 64FeNi), or other material that is compatible with plasma processing. Theside wall 142 andbottom wall 104 may be made from an integral block of aluminum, stainless steel, nickel-iron alloy (e.g., invar, which is a nickel-iron alloy known as 64FeNi), or other material compatible with plasma processing. Thesidewalls 142 and thebottom wall 104 may be anodized to form a coating material on the surface of thelid assembly 112. In some embodiments, the coating material, where present, may be formed by an anodic oxidation process, a plasma spray process, or a thermal spray process. The coating material may comprise a material selected from the group consisting of alumina (Al)2O3) Yttrium-containing compounds, and combinations of the foregoing. Theside wall 142 and thebottom wall 104 may be electrically grounded.
Agas distribution plate 110 and asubstrate support assembly 130 are disposed within theprocess volume 106. Thegas distribution plate 110 and/or thesubstrate support assembly 130 may each independently be formed from aluminum, stainless steel, a nickel-iron alloy (e.g., invar, which is a nickel-iron alloy known as 64FeNi)) Or other materials compatible with plasma processing. In one embodiment, the substrate support assembly comprises stainless steel. In one embodiment, thegas distribution plate 110 comprises stainless steel and the substrate support assembly comprises aluminum oxide (Al)2O3) Yttrium-containing compounds, and combinations of the foregoing. Theprocess volume 106 is accessed through a slit valve opening 108 formed through thesidewall 142 so that thesubstrate 102 may be transferred into and out of thesubstrate processing chamber 100.
Thesubstrate support assembly 130 includes asubstrate receiving surface 132 for supporting thesubstrate 102 thereon. Thesubstrate support assembly 130 generally comprises a conductive body supported by a stem (stem)134 that extends through thebottom wall 104. Therods 134 couple thesubstrate support assembly 130 to alift system 136 that raises and lowers thesubstrate support assembly 130 between substrate transfer and processing positions. Ashadow frame 133 may be placed over the perimeter of thesubstrate 102 during processing to prevent deposition on the edge of thesubstrate 102. Lift pins 138 are movably disposed through thesubstrate support assembly 130 and are adapted to space thesubstrate 102 from thesubstrate receiving surface 132. Thesubstrate support assembly 130 may also include heating and/orcooling elements 139 for maintaining thesubstrate support assembly 130 at a selected temperature. Thesubstrate support assembly 130 may also include a ground strap (ground strap)131 to provide an rf return path around the perimeter of thesubstrate support assembly 130. In one embodiment, thesubstrate support assembly 130 has a coating disposed thereon.
Thegas distribution plate 110 is coupled at its periphery to alid assembly 112 orsidewall 142 of thesubstrate processing chamber 100 by a suspension (suspension) 114. In one embodiment, thegas distribution plate 110 is made of aluminum. The surface of thegas distribution plate 110 may be anodized to form a coating material (e.g., Al) on the surface of the gas distribution plate 1102O3). In one embodiment, the surface of thegas distribution plate 110 has a yttrium-containing coating (Y) disposed thereon2O3). The coating material may be formed on the surface of thegas distribution plate 110 by anodic oxidation, a plasma spray process, or a thermal spray process. Thegas distribution plate 110 may also pass through one or morecentral supports 116 are coupled to thelid assembly 112 to help prevent sagging of thegas distribution plate 110 and/or to control the flatness/curvature of thegas distribution plate 110. Thegas distribution plate 110 may have different configurations with different dimensions. In an exemplary embodiment, thegas distribution plate 110 has a quadrangular planar shape. Thegas distribution plate 110 has adownstream surface 150 having a plurality ofholes 111 formed through thegas distribution plate 110 and facing anupper surface 118 of thesubstrate 102 disposed on thesubstrate support assembly 130. Theholes 111 may have different shapes, numbers, densities, sizes, and distributions across thegas distribution plate 110. In one embodiment, the diameter of thebore 111 may be selected between about 0.01 inches and about 1 inch.
Agas source 120 is coupled to thelid assembly 112 to provide gases to theprocess volume 106 through thelid assembly 112 and subsequently through theapertures 111 formed in thegas distribution plate 110. Avacuum pump 109 is coupled to thesubstrate processing chamber 100 to maintain the gases in theprocess volume 106 at a selected pressure.
The firstelectrical power source 122 is coupled to thelid assembly 112 and/or thegas distribution plate 110. The firstelectric power source 122 provides power that generates an electric field between thegas distribution plate 110 and thesubstrate support assembly 130 so that a plasma may be generated from the gas present between thegas distribution plate 110 and thesubstrate support assembly 130. Thelid assembly 112 and/or thegas distribution plate 110 electrode may be coupled to the firstelectrical power source 122 through an optional filter, which may be an impedance matching circuit. The firstelectrical power source 122 may be a dc power source, a pulsed dc power source, a radio frequency bias power source, a pulsed radio frequency source, or a bias power source, or a combination thereof. In one embodiment, the firstelectrical power source 122 is a radio frequency bias power source.
In one embodiment, the first source ofelectrical power 122 is a radio frequency power source. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The firstelectrical power source 122 may generate about 10 watts to about 20,000 watts (e.g., between about 10 watts to about 5000 watts; between about 300 watts to about 1500 watts; or between about 500 watts and about 1000 watts) of radio frequency power.
Thesubstrate support assembly 130 may be grounded such that the rf power supplied by the firstelectrical power source 122 to thegas distribution plate 110 may excite gases disposed in theprocess volume 106 between thesubstrate support assembly 130 and thegas distribution plate 110. Thesubstrate support assembly 130 may be made of metal or other similar conductive material. In one embodiment, at least a portion of thesubstrate support assembly 130 may be covered with an electrically insulating coating. The coating may be a dielectric material such as an oxide, silicon nitride, silicon dioxide, aluminum oxide, aluminum dioxide, tantalum pentoxide, silicon carbide, polyimide, yttrium-containing compounds, and the like. Alternatively, thesubstrate receiving surface 132 of thesubstrate support assembly 130 may be free from coating or anodization.
Electrodes (not shown), which may be bias electrodes and/or electrostatic chucking electrodes, may be coupled to thesubstrate support assembly 130. In one embodiment, the electrodes are located in the body of thesubstrate support assembly 130. The electrodes may be coupled to the second source ofelectrical power 160 through an optional filter, which may be an impedance matching circuit. The secondelectrical power source 160 may be used to establish additional bias voltages by establishing additional potentials from the plasma to thesubstrate 102. Although there is already a built-in potential from the plasma to thesubstrate 102 even without the secondelectrical power source 160, it is believed that the secondelectrical power source 160 increases the potential to provide more ion bombardment to enhance the etching/cleaning effect. The secondelectrical power source 160 may be a dc power source, a pulsed dc power source, a radio frequency bias power source, a pulsed radio frequency source, or a bias power source, or a combination thereof.
In one embodiment, the secondelectrical power source 160 is a dc bias power source. The DC bias power supply may be supplied at a frequency of 300kHz with a power of between about 10 watts and about 3000 watts (e.g., between about 10 watts and about 1000 watts; or between about 10 watts and about 100 watts). In one embodiment, the dc bias power supply may be pulsed at a radio frequency of about 500Hz and about 10kHz with a duty cycle between about 10% to about 95%. Without being bound by theory, it is believed that the dc bias establishes a bias between the plasma and the substrate support such that ions in the plasma bombard the substrate support, thereby enhancing the etching effect.
In one embodiment, the secondelectrical power source 160 is a radio frequency bias power source. The rf bias power source may be supplied at a frequency of 300kHz with a power between about 0 watts and about 1000 watts (e.g., between about 10 watts and about 100 watts). In one embodiment, the rf bias power source may be pulsed at an rf frequency of about 500Hz and about 10kHz with a duty cycle between about 10% to about 95%.
In one embodiment, the edges of thedownstream surface 150 of thegas distribution plate 110 may be curved so as to define a spacing gradient between the edges and corners of thegas distribution plate 110 and thesubstrate receiving surface 132, and thus between thegas distribution plate 110 and theupper surface 118 of thesubstrate 102. The shape of thedownstream surface 150 may be selected to meet specific process requirements. For example, the shape ofdownstream surface 150 may be convex, planar, concave, or other suitable shape. Thus, the edge-to-corner spacing gradient can be used to adjust film property uniformity across the substrate edge, thereby correcting property non-uniformities of films disposed in the substrate corners. In addition, the edge-to-center spacing may also be controlled so that the film property distribution uniformity between the edge and the center of the substrate may be controlled. In one embodiment, a concavely curved edge of thegas distribution plate 110 may be used such that a central portion of the edge of thegas distribution plate 110 is spaced further from theupper surface 118 of thesubstrate 102 than the corners of thegas distribution plate 110. In another embodiment, a convexly curved edge of thegas distribution plate 110 may be used such that the corners of thegas distribution plate 110 are spaced further from theupper surface 118 of thesubstrate 102 than the edge of thegas distribution plate 110.
Aremote plasma source 124, such as an inductively coupled remote plasma source, may also be coupled between the gas source and thegas distribution plate 110. Between processing substrates, the halogen-containing cleaning gas mixture may be energized (energized) in theremote plasma source 124 to remotely provide a plasma for cleaning chamber components. The halogen containing cleaning gas mixture entering theprocess volume 106 may be further excited by the rf power provided to thegas distribution plate 110 by the firstelectrical power source 122. Although thegas source 120 is coupled to thelid assembly 112 via theremote plasma source 124, it should be understood that in some embodiments, thegas source 120 is coupled directly to the lid assembly.
In one embodiment, asubstrate 102 that may be processed in thesubstrate processing chamber 100 may have a thickness of 10,000cm2Or larger, such as 25,000cm2Or greater, e.g. about 55,000cm2Or a larger surface area. It is understood that after processing, the substrate may be cut to form smaller other devices.
In one embodiment, the heating and/orcooling elements 139 may be configured to provide the following substrate support assembly temperatures during cleaning: about 600 degrees Celsius or less (between about 10 degrees Celsius and about 300 degrees Celsius; between about 200 degrees Celsius and about 300 degrees Celsius; between about 10 degrees Celsius and about 50 degrees Celsius; or between about 10 degrees Celsius and 30 degrees Celsius).
The nominal spacing between theupper surface 118 of thesubstrate 102 disposed on thesubstrate receiving surface 132 and thegas distribution plate 110 during cleaning may typically vary between 400 mils (mils) and about 1,200 mils, such as between 400 mils and about 800 mils, or other distances to achieve a desired deposition result. In one embodiment, in which thegas distribution plate 110 has a concave downstream surface, the spacing between the center portion of the edge of thegas distribution plate 110 and thesubstrate receiving surface 132 is between about 400 mils and about 1400 mils, and the spacing between the corners of thegas distribution plate 110 and thesubstrate receiving surface 132 is between about 300 mils and about 1,200 mils.
Fig. 1B illustrates a cross-sectional view of thesubstrate processing chamber 100 of fig. 1A with thesubstrate 102 removed. Figure 1B provides an illustration of asubstrate processing chamber 100 suitable for performing chamber cleaning using an internal energy source (such as an in-situ plasma) or an external energy source, respectively. In FIG. 1B, a halogen-containing gas mixture 170 (shown as solid arrows in FIG. 1B) is introduced into theprocess volume 106 having a residual film 180 (e.g., such as ZrO) to be removed during the cleaning process2、Y2O3Or HfO2Such as a high dielectric constant dielectric material). As shown in FIG. 1B, aresidual film 180 is deposited on at least a portion of the exposed surfaces within thesubstrate processing chamber 100, in particularAnd is deposited on thegas distribution plate 110, thesubstrate support assembly 130, theshadow frame 133, and the like. The halogen-containinggas mixture 170 is exposed to an energy source, such as the firstelectrical power source 122, the secondelectrical power source 160, or theremote plasma source 124, thus generatingreactive species 190, such as chlorine radicals, fluorine radicals, bromine radicals, hydrogen radicals, and combinations thereof. Thereactive species 190 react with theresidual film 180 and form volatile products. The volatile products are removed from thesubstrate processing chamber 100. One or more interior surfaces of the substrate processing chamber 100 (e.g., thegas distribution plate 110, thesubstrate support assembly 130, theshadow frame 133, thesidewalls 142, etc.) have at least one coating material (e.g., exposed Al) formed thereon2O3Film or exposed yttrium-containing film). The one or more interior surfaces may comprise aluminum, stainless steel, nickel-iron alloy (e.g., invar or 64FeNi), or other materials compatible with plasma processing. In an embodiment, thereactive species 190 may be delivered to theprocess volume 106 with thereactive species 190 being formed ex-situ (e.g., via a remote plasma).
Figure 2 illustrates a process flow diagram of one embodiment of amethod 200 that may be used to remove a high-k dielectric material from a substrate processing chamber. The substrate processing chamber may be similar to thesubstrate processing chamber 100 shown in fig. 1A and 1B. Atoperation 210, a high-k dielectric material is deposited over a substrate disposed in a substrate processing chamber. During deposition of the high-k dielectric material over the substrate, the high-k dielectric material may be deposited over interior surfaces of chamber components (e.g., gas distribution plates, substrate support assemblies, shadow frames, sidewalls, etc.) including the substrate processing chamber. The inner surface may comprise aluminum, stainless steel, nickel-iron alloy (e.g., invar or 64FeNi), or other materials compatible with plasma processing. Any suitable high-k dielectric material may be deposited in the substrate processing chamber. In one embodiment, the high dielectric constant dielectric material is selected from zirconium oxide (ZrO)2) Hafnium oxide (HfO)2) Alumina (Al)2O3) And combinations of the foregoing. In one embodiment, the high-k dielectric material is doped. In thatIn one embodiment, the doped high-k dielectric material is an aluminum doped zirconium oxide containing material.
The high-k dielectric material may be deposited using, for example, a Chemical Vapor Deposition (CVD) process, a Plasma Enhanced Chemical Vapor Deposition (PECVD) process, an Atomic Layer Deposition (ALD) process, a Metal Organic Chemical Vapor Deposition (MOCVD) process, and a Physical Vapor Deposition (PVD) process. In some embodiments, at least some portions of the chamber component are comprised of aluminum. In some embodiments, at least some portions of the chamber component have a coating disposed thereon. In some embodiments, the coating comprises a material selected from the group consisting of alumina (Al)2O3) Yttrium-containing compounds, and combinations of the foregoing. In one embodiment, the yttrium-containing compound is selected from yttrium oxide (Y)2O3) Yttrium Oxide Fluoride (YOF), yttrium chlorate (Y (ClO)3)3) Yttrium (III) fluoride (YF)3) Yttrium (III) chloride (YCl)3) Yttria-stabilized zirconia (YSZ), and combinations thereof. In some embodiments, the chamber component does not have a coating disposed thereon and is thus "uncoated".
Atoperation 220, the substrate is transferred out of the substrate processing chamber. In some embodiments, the substrate remains in the substrate processing chamber during the cleaning process.
Atoperation 230, reactive species are introduced into the substrate processing chamber. The reactive species may be generated using a plasma. The plasma may be generated in situ or the plasma may be generated ex situ (e.g., remotely). Suitable plasma generation techniques and sources, such as Inductively Coupled Plasma (ICP), Capacitively Coupled Plasma (CCP), Remote Plasma Source (RPS), or microwave plasma generation techniques, may be used to form the reactive species. In some embodiments, the reactive species are formed in situ via an in situ plasma process. In some embodiments, the reactive species are formed ex situ via a remote plasma source and introduced into the substrate processing chamber.
In one embodiment, the reactive species may be generated by flowing a halogen-containing cleaning gas mixture into the process volume 106And (4) generating. In one embodiment, the halogen containing cleaning gas mixture comprises a halogen containing gas. In one embodiment, the halogen-containing gas is selected from the group consisting of chlorine-containing gas, hydrogen bromide (HBr) gas, and combinations thereof. In one embodiment, the chlorine-containing gas is selected from BCl3And Cl2. In one embodiment, the halogen-containing gas is selected from BCl3、Cl2、HBr、NF3And combinations of the foregoing gases. In one embodiment, the halogen containing cleaning gas mixture includes BCl3And NF3. In one embodiment, the halogen containing cleaning gas mixture includes BCl3And Cl2. In one embodiment, the halogen-containing gas mixture further comprises a carbon-containing gas. In one embodiment, the carbon-containing gas is selected from CO2、CH4、CHF3、CH2F2、CH3F、CF4And combinations of the foregoing gases. In one embodiment, the halogen-containing gas mixture further comprises a diluent gas. The diluent gas may be selected from helium, argon, and combinations of the foregoing. In some embodiments, the halogen-containing gas and the carbon-containing gas are introduced separately into theprocess volume 106.
In one embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3F、CF4And BCl and at least one of the above gases in combination3. In another embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3F、CF4And Cl and at least one of the above gases in combination2. In yet another embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3HBr and at least one of F and combinations of the foregoing gases. In another embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3F、CF4NF and at least one of the above gases in combination3. In yet another embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3F、CF4And BCl and at least one of the above gases in combination3、NF3. In another embodiment, the halogen containing cleaning gas mixture includes CO2、CH4、CHF3、CH2F2、CH3F、CF4And BCl and at least one of the above gases in combination3、Cl2。
In one embodiment, the halogen containing cleaning gas mixture is exposed to an rf source and/or a bias power source. The rf source and/or the bias power source energizes the halogen containing cleaning gas mixture within theprocess volume 106 so that a plasma may be sustained. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The firstelectrical power source 122 may generate about 10 watts to about 5000 watts (e.g., between about 300 watts and about 1500 watts; between about 500 watts and about 1000 watts) of radio frequency power.
In some embodiments, in addition to the rf source power, an rf bias power supply may also be utilized during the cleaning process to help dissociate the cleaning gas mixture forming the plasma. The radio frequency bias may be provided by a secondelectrical power source 160. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The rf bias power source may be supplied at a frequency of 300kHz with a power between about 0 watts and about 1000 watts (e.g., between about 10 watts and about 100 watts). In one embodiment, the rf bias power source may be pulsed at an rf frequency of about 500Hz and about 10kHz with a duty cycle between about 10% to about 95%. In some embodiments, the coating material (e.g., Al) is applied with an additional bias voltage2O3) Along with the remaining high-k dielectric material. Without being bound by theory, it is believed that the DC bias creates a potential difference between the plasma and the substrate to enhance etching.
In some embodiments, the plasma may be formed capacitively or inductively and may be energized by coupling rf power to the halogen containing cleaning gas mixture. The radio frequency power may be dual frequency radio frequency power having a high frequency component and a low frequency component. The radio frequency power is typically applied at a power level of between about 50W and about 2500W, which may all be high frequency radio frequency power, for example at a frequency of about 13.56 Mhz; or may be a mixture of high frequency power and low frequency power, for example at a frequency of about 300 kHz.
In some embodiments in which the reactive species are formed ex-situ, the halogen containing cleaning gas mixture is flowed into a remote plasma source fluidly coupled to the substrate processing chamber. The halogen containing cleaning gas mixture comprises a halogen containing gas, optionally a carbon containing gas, and optionally a diluent gas. In some embodiments, an optional diluent gas may serve as a carrier gas. In some embodiments, the optional diluent gas may extend the lifetime of the radical species and increase the density of the radical species. In some embodiments, a halogen-containing gas is flowed into a remote plasma source and other process gases (e.g., carbon-containing gases) are delivered into the chamber, respectively.
The remote plasma source may be an inductively coupled plasma source. The remote plasma source receives the halogen containing cleaning gas mixture and forms a plasma in the halogen containing cleaning gas mixture, which causes the halogen containing cleaning gas mixture to dissociate to form reactive species. The reactive species may include chlorine radicals, bromine radicals, fluorine radicals, and combinations thereof. The remote plasma source provides efficient dissociation of the halogen-containing cleaning gas mixture.
In some embodiments, the remote plasma is initiated with an initial flow of argon or similar inert gas prior to introducing the halogen-containing cleaning gas mixture into the remote plasma chamber.
The halogen containing cleaning gas mixture may be flowed into the substrate processing chamber at a flow rate of about 100sccm to about 20,000 sccm. In some embodiments, the halogen containing cleaning gas mixture may be flowed into the substrate processing chamber at a flow rate of about 500sccm to about 4,000 sccm. In some embodiments, the halogen containing cleaning gas mixture may be flowed into the substrate processing chamber at a flow rate of about 1,000 sccm.
In one embodiment, the pressure within the substrate processing chamber is between about 10 mtorr and about 300 torr. In one embodiment, the pressure within the substrate processing chamber is between about 10 mtorr and about 5 torr, such as about 20 mtorr.
In some embodiments, the remote plasma is initiated with an initial flow of argon or similar inert gas prior to introducing the halogen-containing gas mixture into the remote plasma source. Subsequently, the flow of argon is reduced as the halogen containing gas mixture is introduced into the remote plasma chamber. As an example, the remote plasma may be initiated with argon at a flow rate of 3,000sccm, with the flow rate of argon being gradually reduced to 1,000sccm and then to 500sccm as the halogen containing gas mixture is introduced into the remote plasma chamber at an initial flow rate of 1,000sccm and then increased to 1,500 sccm.
In some embodiments, the cleaning process is performed at room temperature. In some embodiments, the substrate support pedestal is heated to a temperature of about 600 degrees celsius or less, for example between about 10 degrees celsius and about 200 degrees celsius, or between about 10 degrees celsius and about 50 degrees celsius, such as a temperature between about 10 degrees celsius and about 30 degrees celsius. Controlling the temperature can be used to control the removal/etch rate of deposits containing high dielectric constant dielectric materials. The removal rate may increase as the chamber temperature increases.
Reactive species formed from the halogen containing cleaning gas mixture are delivered to the substrate processing chamber. In one embodiment, the reactive species comprises a halogen radical. In one embodiment, the reactive species comprises chlorine radicals. In one embodiment, the reactive species comprises chlorine radicals and fluorine radicals. In one embodiment, the reactive species comprises a bromine radical. In one embodiment, the reactive species comprises bromine radicals and hydrogen radicals.
At
operation 240, the reactive species react with the deposit containing the high-k dielectric material to form a dielectric layerVolatile products are formed in the gaseous state. In some embodiments, the removal rate of the residual high dielectric constant dielectric material-containing deposit is greater than the removal rate of a coating material that coats at least a portion of the chamber component. In some embodiments, the removal rate of the residual high-k dielectric-containing deposition is greater than
(e.g., from about
To about
From about
To about
Or from about
To about
). In some embodiments, reacting the residual high dielectric constant dielectric-containing deposit with a reactive species to form a volatile product is a bias-free process. In some embodiments in which no additional bias is applied, the removal rate of the coating material is less than
(e.g., from about
To about
From about
To about
Or
). In some embodiments in which no additional bias is applied, the removal rate of the coating material is a minimum or very slow removal rate (e.g., lower than
Is lower than
Is lower than
Is lower than
Is lower than
Is lower than
Or below
)。
Optionally, atoperation 250, the volatile products in a gaseous state are purged from the substrate processing chamber. The substrate processing chamber may be efficiently purged by flowing a purge gas into the substrate processing chamber. Alternatively, or in addition to introducing the purge gas, the substrate processing chamber may be depressurized to remove any residual cleaning gas and any byproducts from the substrate processing chamber. The substrate processing chamber may be purged by evacuating the substrate processing chamber. The time period for the purging process should generally be long enough to remove volatile products from the substrate processing chamber. The period of time during which the purge gas is flowed should generally be long enough to remove volatile products from the interior surfaces of the chamber including the chamber components.
Atoperation 260, at least one ofoperations 230, 240, and 250 is repeated until the selected cleaning endpoint is achieved. It should be understood that several cleaning cycles may be applied, with an optional purging process being performed between cleaning cycles.
In some embodiments, themethod 200 further comprises removing the coating material (if present) from the substrate processing chamber. The coating material is removed by applying an additional bias while forming the reactive species and/or while reacting the coating material with the reactive species to form the second volatile product. The second volatile product may be removed from the substrate processing chamber.
Figure 3 illustrates a process flow diagram of one embodiment of amethod 200 that may be used to remove a high dielectric constant material from a substrate processing chamber. The substrate processing chamber may be similar to thesubstrate processing chamber 100 shown in fig. 1A and 1B. Atoperation 310, zirconium oxide (ZrO) is included2) The layer is deposited over a substrate disposed in a substrate processing chamber. During deposition of the zirconium oxide-containing layer over the substrate, zirconium oxide and/or zirconium oxide-containing compounds may be deposited over interior surfaces of chamber components (e.g., gas distribution plates, substrate support assemblies, shadow frames, sidewalls, etc.) including the substrate processing chamber. The zirconia-containing layer can be an aluminum-doped zirconia-containing layer. The zirconia-containing layer can be deposited using, for example, a Chemical Vapor Deposition (CVD) process, a Plasma Enhanced Chemical Vapor Deposition (PECVD) process, a chamber, an Atomic Layer Deposition (ALD) process, a Metal Organic Chemical Vapor Deposition (MOCVD), and a Physical Vapor Deposition (PVD) process. One or more of the interior surfaces/chamber components may comprise aluminum, stainless steel, nickel-iron alloy (e.g., invar or 64FeNi), or other materials compatible with plasma processing. In some casesIn an embodiment, at least a portion of the chamber component is comprised of aluminum. In some embodiments, at least a portion of the chamber component has aluminum oxide (Al) disposed thereon2O3) And (3) a layer. In some embodiments, at least a portion of the chamber component is comprised of stainless steel.
Atoperation 320, the substrate is transferred out of the substrate processing chamber. In some embodiments, the substrate remains in the substrate processing chamber during the cleaning process.
Atoperation 330, reactive species are introduced into the substrate processing chamber. The reactive species may be generated using an in situ generated plasma or the plasma may be generated ex situ (e.g., remotely). Suitable plasma generation techniques, such as Inductively Coupled Plasma (ICP), Capacitively Coupled Plasma (CCP), Remote Plasma Source (RPS), or microwave plasma generation techniques, may be used to form the reactive species. In some embodiments, the reactive species are formed in situ via an in situ plasma process. In some embodiments, the reactive species are formed ex situ via a remote plasma source.
In one embodiment, the reactive species may be generated by flowing a cleaning gas mixture into theprocess volume 106. In one embodiment, the cleaning gas mixture comprises BCl3And optionally a diluent gas. The diluent gas may be an inert gas selected from helium, argon, or a combination thereof. The cleaning gas mixture is exposed to a radio frequency source and/or a bias power source. The rf source and/or the bias power source energizes the cleaning gas mixture within theprocess volume 106 so that a plasma may be sustained. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The firstelectrical power source 122 may generate about 10 watts to about 5000 watts (e.g., between about 300 watts and about 1500 watts; between about 500 watts and about 1000 watts) of radio frequency power.
In some embodiments, in addition to the rf source power, an rf bias power supply may also be utilized during the cleaning process to help dissociate the cleaning gas mixture forming the plasma. The RF bias may be provided byA second source ofelectrical power 160. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The rf bias power source may be supplied at a frequency of 300kHz with a power between about 0 watts and about 1000 watts (e.g., between about 10 watts and about 100 watts). In one embodiment, the rf bias power source may be pulsed at a duty cycle between about 10% to about 95% at an rf frequency between about 500Hz and about 10 kHz. In some embodiments in which this additional bias is applied, Al2O3With residual ZrO-containing2The films are removed together.
In some embodiments, in addition to the rf source power, a dc bias power supply may also be utilized during the cleaning process to help dissociate the cleaning gas mixture forming the plasma. The dc bias may be provided by the secondelectrical power source 160. In one embodiment, the first source ofelectrical power 122 is operable to provide radio frequency power at a frequency between 0.3MHz and about 14MHz, such as about 13.56 MHz. The secondelectrical power source 160 is operable to provide a dc bias power source at a frequency of 300kHz at a power of between about 10 watts and about 3000 watts (e.g., between about 10 watts and about 1000 watts; or between about 10 watts and about 100 watts). In one embodiment, the dc bias power supply may be pulsed at a frequency between about 500Hz and about 10kHz with a duty cycle between about 10% to about 95%. Without being bound by theory, it is believed that the DC bias creates a potential difference between the plasma and the substrate to enhance etching.
In some embodiments, the plasma may be formed capacitively or inductively and may be energized by coupling rf power to the cleaning gas mixture. The radio frequency power may be dual frequency radio frequency power having a high frequency component and a low frequency component. The rf power is typically applied at a power level of between about 50W and about 2,500W, which may all be high frequency rf power, for example at a frequency of about 13.56 MHz; or may be a mixture of high frequency power and low frequency power, for example at a frequency of about 300 kHz.
In some embodiments in which the reactive species are formed ex situ, the BCl will be contained3The gas mixture flows into a remote plasma source fluidly coupled to the substrate processing chamber. Containing BCl3The gas mixture of (A) comprises BCl3And optionally an inert gas. In some embodiments, an optional inert gas may serve as a carrier gas. In some embodiments, the optional inert gas may extend the lifetime of the radical species and increase the density of the radical species. In some embodiments, BCl is included, respectively3The gas mixture flows into a remote plasma source and other process gases are delivered into the chamber. The optional inert gas may be selected from the group consisting of helium, argon, or combinations thereof.
The remote plasma source may be an inductively coupled plasma source. Remote plasma source receiving BCl-containing plasma3Gas mixture and in the presence of BCl3Plasma formation in the gas mixture, which results in BCl-containing3The gas mixture dissociates to form reactive species. The reactive species may include chlorine radicals. Remote plasma source providing BCl-containing plasma3Efficient dissociation of gas mixtures.
In some embodiments, the remote plasma is to contain BCl3The gas mixture is initiated with an initial flow of argon or similar inert gas prior to introduction into the remote plasma chamber.
Containing BCl3The gas mixture may be flowed into the substrate processing chamber at a flow rate of about 100sccm to about 10,000 sccm. In some embodiments, the BCl is included3The gas mixture is flowed into the substrate processing chamber at a flow rate from about 500sccm to about 4,000 sccm. In some embodiments, the BCl is included3The gas mixture is flowed into the substrate processing chamber at a flow rate of about 1,000 sccm.
The pressure within the substrate processing chamber may be between about 10 mtorr and about 300 torr. The pressure within the substrate processing chamber may be between 10 mtorr and about 5 mtorr, such as about 20 mtorr.
In some embodiments, the remote plasma is in the presence of BCl3Initiation with an initial flow of argon or similar inert gas is used prior to introduction into the remote plasma source. Then, following BCl3Introducing remote plasmaIn the daughter chamber, the flow of argon is reduced. As an example, the remote plasma may be initiated with 3,000sccm of argon gas, followed by BCl3An initial flow of 1,000sccm and then increasing to 1,500sccm was introduced into the remote plasma chamber, and the flow of argon was gradually decreased to 1,000sccm and then to 500 sccm.
In some embodiments, the cleaning process is performed at room temperature. In some embodiments, the substrate support pedestal is heated to a temperature of about 600 degrees celsius or less, for example between about 10 degrees celsius and about 200 degrees celsius, or between about 10 degrees celsius and about 50 degrees celsius, such as a temperature between about 10 degrees celsius and 30 degrees celsius. Controlling the temperature can be used to control the removal/etch rate of high-k dielectric material deposits. The removal rate may increase as the chamber temperature increases.
From BCl3Reactive species formed from the gas mixture are transported to the substrate processing chamber. The reactive species comprise chlorine radicals.
At
operation 340, the reactive species react with the zirconia-containing deposits to form gaseous volatile products. The volatile product comprises zirconium tetrachloride (ZrCl)
4). In some embodiments, residual ZrO-containing
2The film removal rate is greater than Al
2O
3Removal rate of (a), the Al
2O
3At least a portion of the aluminum chamber component is coated. In some embodiments, residual ZrO-containing
2The removal rate of the film is greater than
(e.g., from about
To about
From about
To about
Or from about
To about
). In some embodiments, the residual ZrO-containing is reacted
2The reaction of the film with the reactive species to form volatile products is a bias-free process. In some embodiments, where no additional bias is applied, Al
2O
3Has a removal rate less than
(e.g., from about
To about
From about
To about
Or
)。
Optionally, atoperation 350, the volatile products in a gaseous state are purged from the substrate processing chamber. The substrate processing chamber may be efficiently purged by flowing a purge gas into the substrate processing chamber. Alternatively, or in addition to introducing the purge gas, the substrate processing chamber may be depressurized to remove any residual cleaning gas and any byproducts from the substrate processing chamber. The substrate processing chamber may be purged by evacuating the substrate processing chamber. The time period for the purging process should generally be long enough to remove volatile products from the substrate processing chamber. The period of time during which the purge gas is flowed should generally be long enough to remove volatile products from the interior surfaces of the chamber including the chamber components.
Atoperation 360, at least one ofoperations 330, 340, and 350 is repeated until the selected cleaning endpoint is achieved. It should be understood that several cleaning cycles may be applied, with an optional purging process being performed between cleaning cycles.
In some embodiments, themethod 300 further comprises removing Al-containing from the substrate processing chamber2O3The membrane (if present). Al (Al)2O3By simultaneous and/or simultaneous formation of reactive species and/or by incorporation of Al2O3The film is removed with the application of an additional bias while reacting with the reactive species to form a second volatile product. The second volatile product may be removed from the substrate processing chamber.