The embodiments described herein relate to filling gaps with flowable films.
The miniaturization of semiconductor circuit elements has reached a point where feature sizes of about 10 nm are fabricated on a commercial scale. As the dimensions continue to get smaller, new challenges arise for process steps like filling a gap between circuit elements with a dielectric material that avoids electrical cross-talk. As the width between the elements continues to shrink, the gap between them often gets taller and narrower, making the gap difficult to fill without the dielectric material getting stuck to create voids or weak seams. Conventional chemical vapor deposition (CVD) techniques often experience an overgrowth of material at the top of the gap before it has been completely filled. This can create a void or seam in the gap where the depositing dielectric material has been prematurely cut off by the overgrowth; a problem sometimes referred to as breadloafing.
One solution to the breadloafing problem has been to use liquid precursors for the dielectric starting materials that more easily flow into the gaps. A technique currently in commercial use for doing this is called spin-on-glass (SOG). More recently, techniques have been developed that impart flowable characteristics to dielectric materials deposited by CVD. These techniques can deposit flowable precursors to fill a tall, narrow gap with porous material while reducing an incidence of creating voids or weak seams. While the new flowable CVD techniques represent a significant breakthrough in filling tall, narrow (i.e., high-aspect ratio) gaps with porous materials (such as low-k dielectric materials), there is still a need to increase the density of the gapfill material.
Systems and methods for forming films on the surface of a substrate are described. The systems possess aerosol generators which form droplets from a liquid solution made from a solvent and a deposition precursor. A carrier gas may be flowed through the liquid solution and push the droplets toward a substrate placed in a substrate processing region. An inline mechanical pump connected with the aerosol generator can also be used to push the droplets towards the substrate. The droplets pass into the substrate processing region and chemically react with the substrate to form films. The temperature of the substrate may be maintained below the boiling temperature of the solvent during film formation. The solvent imparts a flowability to the forming film and enable the depositing film to flow along the surface of a patterned substrate during formation prior to solidifying. The flowable film results in bottom-up gapfill inside narrow high-aspect ratio gaps in the patterned substrate.
Methods described herein include forming a dielectric on a patterned substrate. The methods may include placing the patterned substrate into a substrate processing region of a substrate processing chamber. The patterned substrate includes a high aspect ratio gap. The methods further include dissolving a precursor into a solvent to form a precursor solution within an aerosol generator. The methods further include flowing a carrier gas into the aerosol generator to produce aerosol droplets. The aerosol droplets include the solvent and the precursor. The methods further include flowing the aerosol droplets into the substrate processing region. The methods further include adsorbing the aerosol droplets onto the patterned substrate to form adsorbed droplets outside the high aspect ratio gap. The methods further include flowing the adsorbed droplets into the high aspect ratio gap. The methods further include evaporating the solvent. The methods further include filling the high aspect ratio gap with the dielectric. The dielectric is formed from the precursor by a chemical reaction.
A temperature of the patterned substrate may be below a boiling point of the solvent during flowing the adsorbed droplets into the high aspect ratio gap. The dielectric may be one of silicon oxide, aluminum oxide, silicon nitride, hafnium oxide, zirconium oxide, tantalum oxide, titanium oxide or titanium-doped silicon oxide. An aspect ratio of the high aspect ratio gap may be greater than 10:1 height:width measured near a center between a bottom of the high aspect ratio gap and a top of the high aspect ratio gap. A width of the high aspect ratio gap may be less than 10 nm. The dielectric may fill the high aspect ratio gap without voids.
Methods described herein include forming a dielectric layer on a patterned substrate. The methods include placing the patterned substrate into a substrate processing region of a substrate processing chamber. The patterned substrate includes a high aspect ratio trench. The methods further include forming a liquid solution by combining a deposition precursor and a solvent. The methods further include placing the liquid solution into an aerosol generator. The methods further include applying ultrasonic or higher frequencies to a piezoelectric transducer submerged in the liquid solution. The methods further include forming aerosol droplets in the aerosol generator from the liquid solution. The methods further include flowing the aerosol droplets into the substrate processing region. The methods further include forming an adsorbed liquid on the patterned substrate by depositing the aerosol droplets on the patterned substrate. The adsorbed liquid includes the deposition precursor and the solvent. The methods further include flowing the adsorbed liquid along a surface of the patterned substrate into the high aspect ratio trench. The methods further include filling the high aspect ratio trench with the adsorbed liquid beginning at a bottom of the high aspect ratio trench and finishing at an opening of the high aspect ratio trench. The methods further include evaporating the solvent. The methods further include forming the dielectric layer on the patterned substrate from the deposition precursor. The dielectric layer fills the high aspect ratio trench.
An aspect ratio of the high aspect ratio trench may be greater than 10:1 height:width measured near a center between the bottom of the high aspect ratio trench and the opening of the high aspect ratio trench. A width of the high aspect ratio trench may be less than 10 nm. The dielectric layer may fill the high aspect ratio trench without voids.
Substrate processing chambers described herein include a carrier gas supply. The substrate processing chambers include an aerosol generator configured to receive a carrier gas from the carrier gas supply. The aerosol generator includes a piezoelectric transducer configured to produce aerosol droplets from a liquid solution. The liquid solution is formed from a solvent and a precursor dissolved in the solvent. The substrate processing chambers further include a substrate processing region. The substrate processing chambers further include a precursor conduit configured to receive the aerosol droplets and pass the aerosol droplets into the substrate processing region. The substrate processing chambers further include a substrate pedestal disposed within the substrate processing region within the substrate processing chamber. The substrate pedestal is configured to support the substrate during formation of the film.
The precursor conduit may be configured to pass the aerosol droplets into the substrate processing region through a top of the substrate processing region. The piezoelectric transducer may be in direct contact with the liquid solution. The substrate processing chambers may further include a remote plasma system configured to receive a gas, to form remote plasma effluents, and to flow the remote plasma effluents into the substrate processing region. The substrate processing chambers may further include a local excitation source configured to receive and excite the aerosol droplets within the substrate processing region.
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.
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.
In the appended figures, similar components and/or features may have the same reference label. Further, various components of the same type may be distinguished by following the reference label by a dash and a second label that distinguishes among the similar components. If only the first reference label is used in the specification, the description is applicable to any one of the similar components having the same first reference label irrespective of the second reference label.
Systems and methods for forming films on the surface of a substrate are described. The systems possess aerosol generators which form droplets from a liquid solution made from a solvent and a deposition precursor. A carrier gas may be flowed through the liquid solution and push the droplets toward a substrate placed in a substrate processing region. An inline mechanical pump connected with the aerosol generator can also be used to push the droplets towards the substrate. The droplets pass into the substrate processing region and chemically react with the substrate to form films. The temperature of the substrate may be maintained below the boiling temperature of the solvent during film formation. The solvent imparts a flowability to the forming film and enable the depositing film to flow along the surface of a patterned substrate during formation prior to solidifying. The flowable film results in bottom-up gapfill inside narrow high-aspect ratio gaps in the patterned substrate.
The size reduction of integrated circuit (IC) features has enabled increases in performance while reducing costs. Each size reduction (referred to as a node) involves overcoming a suite of technological hurdles. Exemplary hurdles involve crosstalk, line shorting, and mechanical failure after chemical mechanical polishing (CMP). To overcome these challenges, dielectric materials have been used for shallow trench isolation of IC chips. Gapfill low dielectric constant materials, for example, can isolate circuits disposed on either side of the gap. Circuit isolation may improve device performance. Filling high aspect ratio structures without voids or seams would improve device performance. Existing methods and systems are available to fill low-k materials like SiO2, but there are no analogous techniques or methods available for high k materials deposition like TiOx, HfOx, SiN etc. The methods and systems described herein involve depositing a variety of materials onto a patterned substrate at low temperature while material flows after adsorption onto the patterned substrate before solidifying. The flowing of the material after adsorption enables a desirable bottom up gapfill without the formation of seams, voids and other defects inside the gap. The methods disclosed also improve the quality of materials (e.g. SiO2) for which flowable deposition techniques already existed. However, the techniques described herein may also be used to flowably deposit materials which had no prior solution.
Dielectric material may be formed in gaps and trenches using the techniques presented herein. Dielectric material may be formed in high aspect ratio structures without voids or seams according to embodiments. The gapfill processes involve atomization of the source precursor in the solvent with an atomizer and the precursor mist is delivered into the chamber through without or with a carrier gas (an inert gas, e.g. N2 or Ar). The precursor and the solvent may be in a gas-liquid combined phase in the form of droplets. The solvent is selected to have a low viscosity which enables the droplets to adsorb onto the surface of the patterned substrate and flow on the surface before forming the solid gapfill dielectric in a gap on the patterned substrate. The gapfill dielectric preferentially flows into gaps and fills the gap from the bottom first before filling progressively higher in the gap until the gap is filled all the way to the opening in embodiments. Conventional chemical vapor deposition (CVD) systems may expose the patterned substrate to precursors alone (without the solvent) which limits the flow of adsorbates across the surface of the patterned substrate. The techniques presented herein result in flowably deposited films at low substrate temperatures (e.g. room temperature up to the boiling point of the solvent). The techniques described herein can fill high aspect ratio gaps with dielectric material having a wide range of dielectric constants (low dielectric constant <3.5 through high dielectric constant >7). The techniques offer greater flexibility on the selection of the precursors since flowability is supplied by the solvent droplets rather than the precursor or a combination of precursors as with conventional flowable CVD. The precursor need not to be volatile and there are no constraints on the vapor pressure of the precursors. The precursor may be selected to be soluble in a selected solvent. The solvent may be an organic solvent according to embodiments. After the precursor is dissolved in the solvent the mist or aerosol is generated using an aerosol generator. The mist contains solvent along with the precursor and the mist is delivered into the CVD chamber to react with the patterned substrate supported on a pedestal. Following adsorption and redistribution (flow) on the surface of the patterned substrate, the solvent evaporates leaving behind the source precursor.
The embodiments described herein may involve a precursor in combination with a solvent to form a liquid solution. A liquid may be referred to as a condensed matter which consists of atoms/molecules which are constantly under the influence of the forces imparted by neighboring atoms/molecules and may be defined as matter having essentially no or no mean free path according to embodiments. An aerosol is formed from the condensed matter and may be formed using an atomizer (other terms include vaporizer, volatizer, nebulizer or humidifier) formed from a transducer. The atomizer may have a piezoelectric transducer that can be operated at one or more frequencies (e.g. ultrasonic, megasonic and gigasonic frequencies). The atomizer may generate aerosol droplets which are, optionally, carried into the reaction chamber (substrate processing region) using a carrier gas such as nitrogen (N2) or argon (Ar). The carrier gas may be inert and not form covalent chemical bonds with the condensed matter nor with the substrate. An inline mechanical pump connected with the aerosol generator can also (alone or in combination with the carrier gas) be used to push the droplets towards the substrate.
The aerosol droplets may pass through conduit(s) which are heated to prevent condensation. The temperatures of all conduit(s) or other contact surfaces may be kept below the boiling point of the solvent in the aerosol droplets. The substrate processing region resides within a substrate processing chamber. The substrate processing region may be in a vacuum chamber which is evacuated of atmospheric gases prior to delivery of precursors. The substrate processing region is sealed from the external atmosphere and may be operated at much lower than atmospheric pressure to evacuate the atmospheric gases in embodiments. The precursor may be soluble in a solvent or mixture of solvents from which aerosol droplets are generated.
To better understand and appreciate the embodiments described herein, reference is now made to
A precursor is dissolved in a solvent in operation 120 and placed in an aerosol generator 1003-1 with a piezoelectric transducer 1004-1. A carrier gas is heated in heated carrier gas supply 1002 and flowed into aerosol generator 1003-1 in operation 130. Piezoelectric transducer 1004-1 is vibrated by applying an oscillating voltage to the top and bottom of the transducer and aerosol droplets are generated from the precursor solution in aerosol generator 1003-1 (operation 140). Also in operation 140, the aerosol droplets flow through the precursor conduit 1015-1 and enter substrate processing chamber 1001 through top lid 1005. The aerosol droplets are adsorbed onto the patterned substrate 1013 but remain in a liquid and flowable form facilitating the flow into a gap in the patterned substrate. Some aerosol droplets deposit initially outside the gap and flow on the surface into the gap to fill the gap (operation 150). The solvent is removed (desorbed) from the liquid in operation 160. Operation 160 takes place predominantly after the beneficial flow into the gap has occurred. The substrate is optionally removed from the substrate processing region in operation 170.
Aerosol generators 1003 may be positioned close to substrate processing chamber 1001 to maintain small aerosol droplet sizes. The volume within Aerosol generators 1003 may be roughly proportional to the area of the substrate to be processed. For example, a one liter aerosol generator 1003 may be used to create aerosol droplets for a 300 mm substrate. A mass flow controller may be used to control flow rate of aerosol droplets within the precursor conduit 1015-1 towards substrate processing chamber 1001. The precursor conduit 1015-1 may contain heated activated charcoal to maintain elevated temperature (above room temperature) of the aerosol droplets which also helps to maintain small aerosol droplet sizes.
Reference is now made to
In all embodiments described herein, the precursor and the solvent are in a liquid solution. The vapor pressure of the liquid solution may be greater than 1 mTorr, greater than 10 mTorr, greater than 0.1 Torr, greater than 1 Torr, greater than 10 Torr, greater than 30 Torr or greater than 50 Torr, according to embodiments. The pressure in the substrate processing region may be greater than 10 Torr, greater than 30 Torr, greater than 50 Torr, or greater than 100 Torr. The pressure in the substrate processing may be increased by using the optional carrier gas to assist in the delivery of the aerosol droplets from the liquid solution into the substrate processing region. Higher pressure during deposition has been correlated with improved gapfill.
Deep gaps, trenches or vias often exhibit a higher deposition rate near their opening relative to portions deep within a trench especially when droplet sizes are large compared to the feature sizes or linewidths. The methods described herein may be used to fill gaps or trenches having a width (in the narrower dimension) less than having a width less than 10 nm, less than 8 nm or less than 7 nm, according to embodiments, as measured halfway between the bottom and the top (opening) of the gap. The depths of a via or trench may be greater than 70 nm, greater than 80 nm or greater than 100 nm in embodiments. Depths are measured herein from the top (the opening) to the bottom of a trench. The aspect ratio (height:width) may be greater than 7:1, greater than 10:1, greater than 15:1 or greater than 20:1 according to embodiments. “Top”, “above” and “up” will be used herein to describe portions/directions perpendicularly distal from the substrate plane and further away from the major plane of the substrate in the perpendicular direction. “Vertical” will be used to describe items aligned in the “up” direction towards the “top”. Other similar terms may be used whose meanings will now be clear.
The gapfill dielectric may be one of silicon oxide (e.g. SiOX), titanium oxide (TiOX), Ti doped SiOX, tantalum oxide (TaOX), hafnium oxide (e.g. HfOx), zirconium oxide (e.g. ZrOX), aluminum oxide (e.g. Al2O3) or silicon nitride (SiN) in embodiments.
The solvent may be an organic solvent and may be one of ethanol, methanol isopropanol, butanol or pentanol according to embodiments. The solvent may also be a higher-order solvent which has six or more carbon atoms. The solvent may be a combination of ethanol and methanol (e.g. 50:50 ethanol/methanol, 75:25 ethanol/methanol or 90:10 ethanol methanol) in embodiments. The solvent may be one of xylene, benzene, toluene, hexane, cyclohexane, tetrahydrofuran, dimethyl sulfoxide, dimethylformamide, acetonitrile, dichloromethane, ethyl acetate, dimethyl sulfoxide, or chloroform according to embodiments. The solvent may comprise an aromatic hydrocarbon, may comprise or consist of carbon and hydrogen, or may comprise or consist of carbon, hydrogen and oxygen in embodiments.
Exemplary precursors include tetraethylorthosilicate and titanium isopropoxide, according to embodiments, used to form silicon nitride and titanium oxide. Exemplary precursors further include organometallic precursors in embodiments. The precursors combined with the solvent to form the liquid solution may consist of a single metal element in covalent combination with a hydrocarbon ligand (e.g. methyl, ethyl ispropyl or a higher order hydrocarbon ligand) according to embodiments. A metal element is defined as an element which forms a metal if condensed matter consists only of the metal element. Precursors combined with the solvent may comprise or consist of a metal element and carbonyl, 3-aminopropyl in embodiments. Precursors may comprise or consist of a metal element and a hydrocarbon having a ring structure according to embodiments. For example, precursors may comprise or consist of a metal element and one of cyclopentadienyl, methylcyclopentadienyl, pentamethylcyclopentadienyl, ethylcyclopentadienyl, isopropylcyclopentadienyl, tri-isopropyl-cyclopentadienyl, tris(tert-butyl)cyclopentadienyl, n-propyltetramethyl-cyclopentadienyl, or trimethylsilyl-cyclopentadienyl in embodiments. Precursors may comprise or consist of a metal element and an oxygen atom bonding to a hydrocarbon ligand according to embodiments. For example, precursors may comprise or consist of a metal element and one of methoxy, ethoxy, n-propoxy, isopropoxy, n-butoxy, isobutoxy, tert-butoxy, or tertpentoxy in embodiments. The metal atoms may be one of zirconium, hafnium, titanium, aluminum, or cobalt according to embodiments. All ligands just described may be covalently combined with silicon, in embodiments, which is generally considered a semiconductor rather than a metal. Precursors may comprise or consist of a semiconducting element (e.g. silicon or germanium) and any of the ligands described herein in combination with the metal elements. All precursors described herein may be partially or fully substituted with halogens in place of hydrogens in embodiments. For example, hydrocarbon ligands may have some or all hydrogens replaced by fluorine, chlorine or bromine according to embodiments.
The pressure in the substrate processing region during the deposition processes described herein may be greater than 10 Torr, greater than 30 Torr or greater than 100 Torr in embodiments. The reactions may proceed thermally, excited only by the temperature of the patterned substrate itself, according to embodiments. In embodiments which rely on the temperature of the substrate to effect the deposition reaction, the term “plasma-free” may be used herein to describe the substrate processing region during application using no or essentially no plasma power. Lack of plasma in the substrate processing region will be quantified in several complementary ways which may be used separately or in combination. The plasma power may also be kept below small threshold amounts to enable the appropriate reactions to proceed. The plasma power applied to the substrate processing region may be less than 100 watts, less than 50 watts, less than 30 watts, less than 10 watts and may be 0 watts in embodiments.
Absence (or reduction in magnitude) of any local plasma is desirable to make deposition processes more conformal and less likely to deform features. The term “plasma-free” will be used herein to describe the substrate processing region during application of no or essentially no plasma power to the substrate processing region. Stated another way, the electron temperature in the substrate processing region may be less than 0.5 eV, less than 0.45 eV, less than 0.4 eV, or less than 0.35 eV according to embodiments. The low vapor pressure precursor is not excited in any remote plasma prior to entering the substrate processing region in embodiments. For example, if a remote plasma region or a separate chamber region is present and used to conduct the aerosol droplets toward the substrate processing region and any remote region(s) may be plasma-free as defined herein.
Additional benefits of the hardware and processes described herein can now be described. Prior art aerosol droplets have had diameters between about 0.5 μm and several μms. Several problems arise from having large diameter droplets delivering the precursors to the patterned substrate. The aerosol droplets formed herein may have a diameter between 3 nm and 75 nm, between 5 nm and 50 nm or between 10 nm and 25 nm according to embodiments. Small aerosol droplet dimensions facilitate penetration of the precursor sources into smaller features on a patterned substrate. The smaller sizes may result in enhanced material gapfill and fewer trapped voids within gaps. Some elements are not desirable in the deposited film. The smaller droplet sizes described herein enable undesirable elements (e.g. carbon or hydrogen) to form volatile species which readily leave the surface during the deposition reaction. Small aerosol droplets may be formed using ultrasonic agitation in aerosol generators 1003. The small aerosol droplets flow through the precursor conduits 1015 and then into the substrate processing region. Sizes of the aerosol droplets may be measured using an in-situ particle size analyzers (such as a condensation particle counter or detector).
The substrate processing region within substrate processing chamber 1001 may be evacuated using the vacuum pump 1017 prior to introducing aerosol droplets into the substrate processing region during all deposition operations described herein. Some chemicals may require further processing after passing through the vacuum pump 1017 prior to being released into the atmosphere. A scrubber 1018 may be placed downstream from the vacuum pump 1017 to modify or remove chemical constituents of the process effluents before releasing the process effluents. A closed-loop exhaust feedback system may be used to maintain a desired pressure within the substrate processing region. In the event a pressure within the substrate processing region rises above a set point pressure (an overpressure situation), an automatic valve (not shown) may release the pressure inside substrate processing chamber 1001 opening the substrate processing region to the vacuum pump 1017 and the scrubber 1018.
Several additional examples will be presented which show additional elements and configurations which may be added to any other embodiments discussed herein.
Remote plasma powers can be of a variety of frequencies or a combination of multiple frequencies. The remote plasma may be provided by RF power delivered to the remote plasma system 1012 by capacitive or inductive means. The RF power may alternatively or in combination be applied within the substrate processing region to form a local plasma. The RF power applied to the remote plasma system may be between 100 watts and 10,000 watts, between 200 watts and 15,000 watts, preferably between 500 watts and 10,000 watts or more preferably between 2,000 watts and 7,500 watts in embodiments. The RF power applied to the substrate processing region to form the local plasma may be between 10 watts and 10,000 watts, between 10 watts and 5,000 watts, preferably between 25 watts and 2000 watts or more preferably between 50 watts and 1500 watts in embodiments. The RF frequency applied to form either the local plasma or the remote plasma may be low RF frequencies less than 200 kHz, higher RF frequencies between 10 MHz and 15 MHz, or microwave frequencies greater than or about 1 GHz in embodiments. The remote plasma and the local plasma may be used separately or in combination. The local plasma may be used to excite the aerosol droplets and any secondary gas in embodiments. The remote plasma may excite only the secondary gas but not the aerosol droplets according to embodiments.
The susceptor 1114 is parallel to the top plate 1112 and the vaporized precursor or aerosol droplets are delivered into the substrate processing region from between the susceptor 114 and the top plate 1112.
A heater coil 1116 may be disposed on the top plate 1112 and/or on the susceptor 1114. Heating the top plate 1112 and/or the susceptor 1114 discourages condensation of the vaporized precursor and decreases aerosol droplet size. The substrate temperature may be elevated above room temperature during deposition depending on the type of film grown and precursors and solvents used. The dry or liquid-gaseous processes introduced herein enable the processes to be performed at higher temperatures than prior art wholly liquid processes. The vaporized precursor makes contact with patterned substrate 1113 while the patterned substrate is maintained at a temperature between 0° C. and 300° C. according to embodiments. Process pressures were also given previously and will not be repeated here for the sake of brevity. The reactions may proceed thermally, excited only by the temperature of the patterned substrate itself, according to embodiments. The substrate processing region may be described as plasma-free whose definition was previously presented.
The entry plate 1212 is parallel to the exit plate 1220 and the vaporized precursor or aerosol droplets are delivered through the entry plate 1212 into the substrate processing region between the plates. The entry plate 1212 and the exit plate 1220 are planar, in embodiments, and each are perpendicular to the major plane of the patterned substrate 1215. A film is deposited on the patterned substrate 1215 from the aerosol droplets. Unreacted precursor or other process effluents may be pumped out through the exit plate 1220 according embodiments. The process effluents may be pumped out through the vacuum pump 1222. Substrate temperatures, process pressures, droplet sizes and process benefits were presented previously.
In all embodiments described herein, the precursor may be supplied at a flow rate of between 5 mgm (milligrams per minute) and 500 mgm, between 10 mgm and 300 mgm or between 25 mgm and 200 mgm. Two or more low vapor pressure condensed matter precursors may be used in which case each one may have a flow rate between the ranges given above. Film growth rates using the aerosol droplet generation methods and hardware described herein may exceed 300 Å/min, may exceed 500 Å/min or may exceed 1,000 Å/min, in embodiments.
Embodiments of the substrate processing chambers may be incorporated into larger fabrication systems for producing integrated circuit chips.
As used herein “patterned substrate” may be a support substrate with or without layers formed thereon. The patterned 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. Exposed “metal” of the patterned substrate is predominantly a metal element but may include minority concentrations of other elemental constituents such as nitrogen, oxygen, hydrogen, silicon and carbon. Exposed “metal” may consist of or consist essentially of a metal element. A metal may comprise or consist of a “metal element” which forms a conducting material in a solid consisting only of that metal element. The conducting material consisting only of the one metal element (or the metal in relatively pure form) may have a conductivity less than 10-5 Ω-m at 20° C. in embodiments. Exposed “metal nitride” of the patterned substrate is predominantly nitrogen and a metal element but may include minority concentrations of other elemental constituents such as oxygen, hydrogen, silicon and carbon. Exposed “metal nitride” may consist of or consist essentially of nitrogen and a metal element.
Exposed “silicon” or “polysilicon” of the patterned substrate is predominantly Si but may include minority concentrations of other elemental constituents such as nitrogen, oxygen, hydrogen and carbon. Exposed “silicon” or “polysilicon” may consist of or consist essentially of silicon. Exposed “silicon nitride” of the patterned substrate is predominantly silicon and nitrogen but may include minority concentrations of other elemental constituents such as oxygen, hydrogen and carbon. “Exposed silicon nitride” may consist essentially of or consist of silicon and nitrogen. Exposed “silicon oxide” of the patterned substrate is predominantly SiO2 but may include minority concentrations of other elemental constituents (e.g. nitrogen, hydrogen, carbon). In some embodiments, silicon oxide regions formed using the methods disclosed herein consist essentially of silicon and oxygen.
The carrier gases described herein may be inert gases. The phrase “inert gas” refers to any gas which does not form chemical bonds when being incorporated into a layer. Exemplary inert gases include noble gases but may include other gases so long as no chemical bonds are formed when (typically) trace amounts are trapped in a layer.
A gap is an etched geometry having any horizontal aspect ratio. Viewed from above the surface, gaps may appear circular, oval, polygonal, rectangular, or a variety of other shapes. A “trench” is a long gap. A trench may be in the shape of a moat around an island of material whose aspect ratio is the length or circumference of the moat divided by the width of the moat. A “via” is a short gap with horizontal aspect ratio, as viewed from above, near unity. A via may appear circular, slightly oval, polygonal or slightly rectangular. A via may or may not be filled with metal to form a vertical electrical connection.
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 to avoid unnecessarily obscuring the disclosed embodiments. Accordingly, the above description should not be taken as limiting the scope of the claims.
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 disclosed embodiments, 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.
The application is a divisional of U.S. patent application Ser. No. 15/489,242, filed Apr. 17, 2017. The disclosure of Ser. No. 15/489,242 is hereby incorporated by reference in its entirety for all purposes.
Number | Name | Date | Kind |
---|---|---|---|
7074690 | Gauri et al. | Jul 2006 | B1 |
7524735 | Gauri et al. | Apr 2009 | B1 |
7582555 | Lang et al. | Sep 2009 | B1 |
7629227 | Wang et al. | Dec 2009 | B1 |
7867923 | Mallick et al. | Jan 2011 | B2 |
7915139 | Lang et al. | Mar 2011 | B1 |
7935643 | Liang et al. | May 2011 | B2 |
7954730 | Ng | Jun 2011 | B2 |
10017856 | Arnepalli et al. | Jul 2018 | B1 |
20040209190 | Mori | Oct 2004 | A1 |
20060124057 | Sasaki | Jun 2006 | A1 |
20070032097 | Chen | Feb 2007 | A1 |
20110015167 | Miehe et al. | Jan 2011 | A1 |
20110034039 | Liang et al. | Feb 2011 | A1 |
20110111137 | Liang et al. | May 2011 | A1 |
20110217851 | Liang et al. | Sep 2011 | A1 |
20130115781 | Matsumoto | May 2013 | A1 |
20140017904 | Gauri et al. | Jan 2014 | A1 |
20140302689 | Ashtiani et al. | Oct 2014 | A1 |
20150118863 | Rathod et al. | Apr 2015 | A1 |
20170140920 | Arnepalli et al. | May 2017 | A1 |
Number | Date | Country |
---|---|---|
4254238 | Apr 2009 | JP |
2014187187 | Oct 2014 | JP |
3208344 | Dec 2016 | JP |
Entry |
---|
U.S. Appl. No. 15/489,242, “Notice of Allowance”, dated Mar. 27, 2018, 11 pages. |
PCT/US2018/027789, “International Search Report and Written Opinion”, dated Aug. 2, 2018, 5 pages. |
Number | Date | Country | |
---|---|---|---|
20180298492 A1 | Oct 2018 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 15489242 | Apr 2017 | US |
Child | 15978930 | US |