Surface treatment and deposition for reduced outgassing

Information

  • Patent Grant
  • 9404178
  • Patent Number
    9,404,178
  • Date Filed
    Tuesday, June 12, 2012
    11 years ago
  • Date Issued
    Tuesday, August 2, 2016
    7 years ago
Abstract
A method of forming a dielectric layer is described. The method first deposits a silicon-nitrogen-and-hydrogen-containing (polysilazane) layer by radical-component chemical vapor deposition (CVD). The silicon-nitrogen-and-hydrogen-containing layer is formed by combining a radical precursor (excited in a remote plasma) with an unexcited carbon-free silicon precursor. A silicon oxide capping layer may be formed from a portion of the carbon-free silicon-nitrogen-and-hydrogen-containing layer to avoid time-evolution of underlying layer properties prior to conversion into silicon oxide. Alternatively, the silicon oxide capping layer is formed over the silicon-nitrogen-and-hydrogen-containing layer. Either method of formation involves the formation of a local plasma within the substrate processing region.
Description
BACKGROUND OF THE INVENTION

Semiconductor device geometries have dramatically decreased in size since their introduction several decades ago. Modern semiconductor fabrication equipment routinely produce devices with 45 nm, 32 nm, and 28 nm feature sizes, and new equipment is being developed and implemented to make devices with even smaller geometries. The decreasing feature sizes result in structural features on the device having decreased spatial dimensions. The widths of gaps and trenches on the device narrow to a point where the aspect ratio of gap depth to its width becomes high enough to make it challenging to fill the gap with dielectric material. The depositing dielectric material is prone to clog at the top before the gap completely fills, producing a void or seam in the middle of the gap.


Over the years, many techniques have been developed to avoid having dielectric material clog the top of a gap, or to “heal” the void or seam that has been formed. One approach has been to start with highly flowable precursor materials that may be applied in a liquid phase to a spinning substrate surface (e.g., SOG deposition techniques). These flowable precursors can flow into and fill very small substrate gaps without forming voids or weak seams. However, once these highly flowable materials are deposited, they have to be hardened into a solid dielectric material.


In many instances, the hardening includes a heat treatment to remove carbon and hydroxyl groups from the deposited material to leave behind a solid dielectric such as silicon oxide. Unfortunately, the departing carbon and hydroxyl species often leave behind pores in the hardened dielectic that reduce the quality of the final material. In addition, the hardening dielectric also tends to shrink in volume, which can leave cracks and spaces at the interface of the dielectric and the surrounding substrate. In some instances, the volume of the hardened dielectric can decrease by 40% or more.


Spin-on dielectrics (SOD) have also been used to flow into features on a patterned substrate. The material is generally converted to silicon oxide from a silazane-type layer which contains silicon, nitrogen and hydrogen. Silicon, nitrogen and hydrogen containing layers are typically converted to silicon oxide at high temperature in an oxygen containing environment. Oxygen from the environment displaces nitrogen and hydrogen to create the silicon oxide layer. High temperature exposure to oxygen environments can ruin underlying layers for some circuit architectures. This consideration results in the need to stay within a “thermal budget” during a manufacturing process flow. Thermal budget considerations have largely limited SOD to process flows incorporating an underlying silicon nitride layer which can protect underlying features from oxidation (e.g. DRAM applications).


Alternative methods have been developed which deposit silazane containing layers by radical-component CVD. Radical-component CVD can create a flowable layer by exciting one precursor and combining it with an unexcited silicon-containing precursor in the plasma-free substrate processing region. Layer properties, including density, may change slightly in time until the silazane containing layer is converted to silicon oxide. Controlling the evolution of the layer properties improves the manufacturability of devices using these layers. Thus, there is a need for new deposition processes and materials to form dielectric materials which do not evolve over time. This and other needs are addressed in the present application.


BRIEF SUMMARY OF THE INVENTION

A method of forming a dielectric layer is described. The method first deposits a silicon-nitrogen-and-hydrogen-containing (polysilazane) layer by radical-component chemical vapor deposition (CVD). The silicon-nitrogen-and-hydrogen-containing layer is formed by combining a radical precursor (excited in a remote plasma) with an unexcited carbon-free silicon precursor. A silicon oxide capping layer may be formed from a portion of the carbon-free silicon-nitrogen-and-hydrogen-containing layer to avoid time-evolution of underlying layer properties prior to conversion into silicon oxide. Alternatively, the silicon oxide capping layer is formed over the silicon-nitrogen-and-hydrogen-containing layer.


Either method of formation involves the formation of a local plasma within the substrate processing region.


Embodiments of the invention include methods of forming a dielectric layer on a substrate. The methods include the sequential steps of: (1) forming a carbon-free silicon-nitrogen-and-hydrogen-containing layer on the substrate in a first substrate processing region containing the substrate and (2) forming a silicon oxide capping layer on the carbon-free silicon-nitrogen-and-hydrogen-containing layer. Forming the carbon-free silicon-nitrogen-and-hydrogen-containing layer includes flowing an unexcited precursor into a remote plasma region to produce a radical-precursor, combining a carbon-free silicon-containing precursor with the radical-precursor in the first substrate processing region, and depositing a carbon-free silicon-nitrogen-and-hydrogen-containing layer over the substrate. The first substrate processing region is plasma-free during the operation of forming the carbon-free silicon-nitrogen-and-hydrogen-containing layer. The carbon-free silicon-nitrogen-and-hydrogen-containing layer is flowable during deposition. Forming the silicon oxide capping layer includes flowing an oxygen-containing precursor into a second substrate processing region containing the substrate, flowing a silicon-containing precursor into the second substrate processing region, forming a plasma from the oxygen-containing precursor and the silicon-containing precursor in the second substrate processing region, and depositing the silicon oxide capping layer over the carbon-free silicon-nitrogen-and-hydrogen-containing layer.


Embodiments of the invention include methods of forming a dielectric layer on a substrate. The method include the sequential steps of: (1) forming a carbon-free silicon-nitrogen-and-hydrogen-containing layer on the substrate in a first substrate processing region containing the substrate, and (2) treating the carbon-free silicon-nitrogen-and-hydrogen-containing layer to convert a portion of the carbon-free silicon-nitrogen-and-hydrogen-containing layer to a silicon oxide capping layer. Forming the carbon-free silicon-nitrogen-and-hydrogen-containing layer includes flowing an unexcited precursor into a remote plasma region to produce a radical-precursor, combining a carbon-free silicon-containing precursor with the radical-precursor in the first substrate processing region, and depositing a carbon-free silicon-nitrogen-and-hydrogen-containing layer over the substrate. The first substrate processing region is plasma-free during the operation of forming the carbon-free silicon-nitrogen-and-hydrogen-containing layer. The carbon-free silicon-nitrogen-and-hydrogen-containing layer is flowable during deposition. Treating the carbon-free silicon-nitrogen-and-hydrogen-containing layer includes flowing an oxygen-containing precursor into a second substrate processing region containing the substrate, forming a plasma from the oxygen-containing precursor in the second substrate processing region, and converting a portion of the carbon-free silicon-nitrogen-and-hydrogen-containing layer into the silicon oxide capping layer.


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 invention. The features and advantages of the invention may be realized and attained by means of the instrumentalities, combinations, and methods described in the specification.





BRIEF DESCRIPTION OF THE DRAWINGS

A further understanding of the nature and advantages of the present invention may be realized by reference to the remaining portions of the specification and the drawings wherein like reference numerals are used throughout the several drawings to refer to similar components. In some instances, a sublabel is associated with a reference numeral and follows a hyphen to denote one of multiple similar components. When reference is made to a reference numeral without specification to an existing sublabel, it is intended to refer to all such multiple similar components.



FIG. 1 is a flowchart illustrating selected steps for making a dielectric layer according to embodiments of the invention.



FIG. 2 is a flowchart illustrating selected steps for making a dielectric layer according to embodiments of the invention.



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



FIG. 4A shows a substrate processing chamber according to embodiments of the invention.



FIG. 4B shows a gas distribution showerhead according to embodiments of the invention.





DETAILED DESCRIPTION OF THE INVENTION

A method of forming a dielectric layer is described. The method first deposits a silicon-nitrogen-and-hydrogen-containing (polysilazane) layer by radical-component chemical vapor deposition (CVD). The silicon-nitrogen-and-hydrogen-containing layer is formed by combining a radical precursor (excited in a remote plasma) with an unexcited carbon-free silicon precursor. A silicon oxide capping layer may be formed from a portion of the carbon-free silicon-nitrogen-and-hydrogen-containing layer to avoid time-evolution of underlying layer properties prior to conversion into silicon oxide. Alternatively, the silicon oxide capping layer is formed over the silicon-nitrogen-and-hydrogen-containing layer. Either method of formation involves the formation of a local plasma within the substrate processing region.


Positioning a radical-component CVD silicon-nitrogen-and-hydrogen-containing layer beneath a silicon oxide capping layer has been found to reduce and/or eliminate outgassing and concomitant evolution of layer properties over time. Without the silicon oxide capping layer, the properties and stoichiometry of the layer may change over time. The layers evolve in time due to the outgassing of silicon-containing species, ammonia and the like. Properties may also evolve due to the absorption of water or other components present in the surrounding atmosphere within a typical fabrication facility. Changing layer properties can complicate the manufacturing process by requiring rigid control over the delay between layer formation and processing within another substrate processing system or chamber.


These complications and requirements are undesirable. The silicon-oxygen-and-carbon-containing capping layers described herein have been found to suppress outgassing but still allow conversion of the underlying silicon-nitrogen-and-hydrogen-containing layer to a silicon-and-oxygen-containing layer and to silicon oxide.


Radical-component CVD layers capped with silicon oxide capping layers according to the methods contained herein have been found to exhibit properties which do not evolve when the substrate is exposed to typical cleanroom atmospheres. Additional details about the methods and systems of forming the silicon oxide capping layer will now be described.


A First Exemplary Dielectric Stack Process



FIG. 1 is a flowchart showing selected steps in a method 100 of making a dielectric stack of layers according to embodiments of the invention. The method 100 includes providing a carbon-free silicon-containing precursor to a substrate processing region 102. The carbon-free silicon-containing precursor does not pass through a plasma excitation, in embodiments, so the precursor travels into the substrate processing region intact. Excitation is then provided only by the radical precursor to be described, shortly. The carbon-free silicon-containing precursor may be, for example, a silicon-and-nitrogen-containing precursor, a silicon-and-hydrogen-containing precursor, or a silicon-nitrogen-and-hydrogen-containing precursor, among other classes of silicon precursors. The absence of carbon reduces the shrinkage of the deposited layer. The silicon-containing precursor may be oxygen-free in addition to carbon-free. The lack of oxygen results in a lower concentration of silanol (Si—OH) groups in the silicon-and-nitrogen-containing layer formed from the precursors. Excess silanol moieties in the deposited layer can cause increased porosity and shrinkage during post deposition steps that remove the hydroxyl (—OH) moieties from the deposited layer.


Specific examples of carbon-free silicon precursors may include silyl-amines such as H2N(SiH3), HN(SiH3)2, and N(SiH3)3, among other silyl-amines. The flow rates of a silyl-amine may be greater than or about 200 sccm, greater than or about 300 sccm or greater than or about 500 sccm in different embodiments. All flow rates given herein refer to a dual chamber substrate processing system. Single wafer systems would require half these flow rates and other wafer shapes/sizes would require flow rates scaled by the processed area. These silyl-amines may be mixed with additional gases that may act as carrier gases, reactive gases, or both. Additional gases may include H2, N2, NH3, He, Ne and/or Ar, among other gases. Examples of carbon-free silicon-containing precursors may also include silane (SiH4) either alone or mixed with other silicon (e.g., N(SiH3)3), hydrogen (e.g., H2), and/or nitrogen (e.g., N2, NH3) containing gases. Carbon-free silicon-containing precursors may also include disilane, trisilane, even higher-order silanes, and chlorinated silanes, alone or in combination with one another or the previously mentioned carbon-free silicon-containing precursors.


A radical precursor is also provided to the substrate processing region 104. A radical precursor describes plasma effluents produced in the plasma excitation outside the substrate processing region from any stable species (inert or reactive). The radical precursor may be a nitrogen-containing radical precursor which will be referred to herein as a radical-nitrogen precursor. The radical-nitrogen precursor is a nitrogen-radical-containing precursor that was generated outside the substrate processing region from a more stable nitrogen precursor. A stable precursor may be referred to herein as an unexcited precursor to indicate that the precursor has not yet passed through a plasma. A stable nitrogen precursor compound containing NH3, hydrazine (N2H4) and/or N2 may be activated in a chamber plasma region or another remote plasma system (RPS) outside the processing chamber to form the radical-nitrogen precursor, which is then transported into the substrate processing region to excite the silicon-containing precursor. The activation of the stable nitrogen precursor into the radical-nitrogen precursor involves dissociation which may be accomplished by means of thermal dissociation, ultraviolet light dissociation, and/or plasma dissociation, among other methods. Plasma dissociation may involve striking a plasma from helium, argon, hydrogen (H2), xenon, ammonia (NH3), etc., in a remote plasma generating chamber and introducing the stable nitrogen precursor to the plasma region to generate the radical-nitrogen precursor.


The stable nitrogen precursor may also be a mixture comprising NH3 & N2, NH3 & H2, NH3 & N2 & H2 and N2 & H2, in different embodiments. Hydrazine may also be used in place of or in combination with NH3 and in the mixtures involving N2 and H2. The flow rate of the stable nitrogen precursor may be greater than or about 300 sccm, greater than or about 500 sccm or greater than or about 700 sccm in different embodiments. The radical-nitrogen precursor produced in the chamber plasma region may be one or more of N, —NH, —NH2, etc., and may also be accompanied by ionized species formed in the plasma. Sources of oxygen may also be combined with the more stable nitrogen precursor in the remote plasma in embodiments of the invention. The addition of a source of oxygen pre-loads the layer with oxygen while decreasing flowability. Sources of oxygen may include one or more of O2, H2O, O3, H2O2, N2O, NO or NO2.


In embodiments employing a chamber plasma region, the radical-nitrogen precursor is generated in a section of the substrate processing region partitioned from a deposition region where the precursors mix and react to deposit the silicon-and-nitrogen-containing layer on a deposition substrate (e.g., a semiconductor wafer). The radical-nitrogen precursor may also be accompanied by a carrier gas such as hydrogen (H2), nitrogen (N2), helium, neon, argon etc. The substrate processing region may be described herein as “plasma-free” during the growth of the carbon-free silicon-nitrogen-and-hydrogen-containing layer and during subsequent processes. “Plasma-free” does not necessarily mean the region is devoid of plasma. The borders of the plasma in the chamber plasma region are hard to define and may encroach upon the substrate processing region through the apertures in the showerhead. In the case of an inductively-coupled plasma, e.g., a small amount of ionization may be initiated within the substrate processing region. Generally, a low intensity plasma may be created in the substrate processing region without compromising the flowable nature of the forming layer. All causes for a plasma having much lower ion density than the remote/chamber plasma region during the creation of the radical nitrogen precursor do not deviate from the scope of “plasma-free” as used herein.


In the substrate processing region, the carbon-free silicon precursor and the radical-nitrogen precursor mix and react to deposit a silicon-nitrogen-and-hydrogen-containing layer on the deposition substrate 106. In embodiments, the deposited silicon-nitrogen-and-hydrogen-containing layer has flowable characteristics unlike conventional silicon nitride (Si3N4) layer deposition techniques. The flowable nature during formation allows the layer to flow into narrow features before solidifying.


Nitrogen in the silicon-nitrogen-and-hydrogen-containing layer may originate from either (or both) of the radical precursor or the unexcited precursor. The carbon-free silicon-containing precursor may be essentially nitrogen-free, in some embodiments. However, in other embodiments, both the carbon-free silicon-containing precursor and the radical-nitrogen precursor contain nitrogen. In a third suite of embodiments, the radical precursor may be essentially nitrogen-free and the nitrogen for the carbon-free silicon-nitrogen-and-hydrogen-containing layer may be supplied by the carbon-free silicon-containing precursor. As a result, the radical precursor may be referred to herein as a “radical-nitrogen-and/or-hydrogen precursor,” which means that the precursor contains nitrogen and/or hydrogen. Analogously, the precursor flowed into the plasma region to form the radical-nitrogen-and/or-hydrogen precursor may be referred to as a nitrogen-and/or-hydrogen-containing precursor. This nomenclature may be applied to each of the embodiments disclosed herein. In embodiments, the nitrogen-and/or-hydrogen-containing precursor comprises hydrogen (H2) while the radical-nitrogen-and/or-hydrogen precursor comprises H, etc.


Returning to the specific example shown in FIG. 1, the flowability of a silicon-nitrogen-and-hydrogen-containing layer may be due to a variety of properties which result from mixing a radical-nitrogen precursors with a carbon-free silicon-containing precursor. These properties may include a significant hydrogen component in the deposited layer and/or the presence of short chained polysilazane polymers. These short chains grow and network to form more dense dielectric material during and after the formation of the layer. For example the deposited layer may have a silazane-type, Si—NH—Si backbone (i.e., a carbon-free Si—N—H layer). When both the silicon-containing precursor and the radical precursor are carbon-free, the deposited silicon-nitrogen-and-hydrogen-containing layer is also substantially carbon-free. Of course, “carbon-free” does not necessarily mean the layer lacks even trace amounts of carbon. Carbon contaminants may be present in the precursor materials that find their way into the deposited silicon-and-nitrogen-containing precursor. The amount of these carbon impurities however are much less than would be found in a silicon precursor having a carbon moiety (e.g., TEOS, TMDSO, etc.).


At this point in the process, the process effluents may be removed from the substrate processing region in embodiments of the invention. Process effluents may include any unreacted silicon-containing precursor, unreacted radical-nitrogen precursor, inert carrier gases and reaction products from the layer growth. The process effluents may be displaced by flowing inert species into the substrate processing region and/or by exhaustion through an exhaust port in disclosed embodiments.


The method 100 also includes an additional deposition of silicon oxide over the silicon-nitrogen-and-hydrogen-containing layer to avoid outgassing from the underlying layer. The layer of silicon oxide is referred to herein as a silicon oxide capping layer. The formation of the silicon oxide capping layer may occur in the same substrate processing region or the substrate may be transferred into a separate processing region. The substrate may be exposed to atmosphere during the transfer or may be kept under vacuum in embodiments of the invention. A benefit of forming the silicon oxide capping layer is to avoid the time-evolution of film properties of the silicon-nitrogen-and-hydrogen-containing layer before subsequent processing is carried out. As such, a controllable and reproducible amount of exposure of the substrate to atmosphere is desirable prior to deposition of the silicon oxide capping layer. The deposition of the silicon oxide capping layer is initiated by providing an oxygen-containing precursor to the substrate processing region 108. A silicon-containing precursor is also flowed into the substrate processing region 109 and combined with the oxygen-containing precursor in the vicinity of the substrate. A plasma is concurrently formed in the substrate processing region 110 to form the silicon oxide capping layer 112. A remote plasma (outside the substrate processing region) had been used to deposit the silicon-nitrogen-and-hydrogen-containing layer whereas a local plasma (within the substrate processing region) is used to deposit the silicon oxide capping layer.


The oxygen-containing precursor may include molecular oxygen (O2) and/or ozone (O3). The silicon-containing precursor may include tetraethyl orthosilicate (TEOS) in a preferred embodiment. Generally speaking, the silicon-containing precursor can include tetraethyl orthosilicate (TEOS), octamethyltrisiloxane (OMTS), octamethylcyclotetrasiloxane (OMCTS), methyldiethoxysilane (MDEOS), bis(tertiary-butylamino)silane (BTBAS), tridimethylaminosilane (TriDMAS), trisdimethylaminosilane (TrisDMAS), silane, disilane, dichlorosilane, trichlorosilane, dibromosilane, silicon tetrachloride, silicon tetrabromide, dimethylsilane, trimethylsilane, tetramethylsilane, diethylsilane,. tetramethylorthosilicate (TMOS), or combinations thereof. The plasma power applied to the substrate processing region may be below or about 1000 W, below or about 500 W, or below or about 300 W.


The plasma power applied to the substrate processing region may be above or about 50 W, above or about 100 W, or above or about 200 W in embodiments of the invention. The upper limits on the plasma power may be combined with the lower limits to form additional embodiments. The plasma power is lower than many plasma-enhanced chemical vapor deposition (PE-CVD) processes in order to essentially maintain the structure of the underlying silicon-nitrogen-and-hydrogen-containing layer. The plasma frequency may be 13.56 MHz and/or 350 KHz. Gases that are optionally introduced into the chamber at the same time as the silicon-containing precursor include helium and/or argon. Helium or other inert gases may be used as a carrier gas to deliver ordinarily liquid precursors td the substrate processing region.


The oxygen-containing precursor may be introduced into the chamber at a flow rate of between about 10 sccm and about 1000 seem. The silicon-containing precursor may be introduced into the chamber at a flow rate of between about 5 sccm and about 1000 sccm. The optional carrier gas, e.g., helium, may be introduced into the chamber at a flow rate of between about 100 sccm and about 20000 sccm. The ratio of the flow rate of the silicon-containing precursor, e.g., tetraethyl orthosilicate, to the flow rate of the carrier gas, e.g., helium, into the chamber is about 1:1 or greater, such as between about 1:1 and about 1:100. The pressure inside the substrate processing region may be greater than about 500 mTorr, such as between about 2 Torr and about 10 Torr, and the temperature of a substrate support in the chamber may be between about 100° C. and about 250° C. while the silicon-containing precursor and the oxygen-containing precursor are flowed into the chamber to deposit the silicon oxide capping layer. Preferably, the temperature is below about 250° C. or below about 200° C. in disclosed embodiments. The low substrate temperatures are also desirable in order to preserve the structure of the silicon-nitrogen-and-hydrogen-containing layer. The silicon-containing precursor and the oxygen-containing precursor may each be flowed into the chamber for a period of time sufficient to deposit a silicon oxide capping layer having a thickness of greater than or about 5 nm, greater than or about 10 nm, greater than or about 20 nm, or greater than or about 50 nm.


A Second Exemplary Dielectric Stack Process



FIG. 2 is a flowchart showing selected steps in a second method 200 of making a dielectric stack of layers according to embodiments of the invention. The method 200 includes forming a silicon-nitrogen-and-hydrogen-containing layer as described with reference to FIG. 2. Therefore, the method includes providing a carbon-free silicon-containing precursor to a substrate processing region 202 without plasma excitation and with all the embodiments described previously. The method further includes providing a radical precursor to the substrate processing region 204 as before. The radical precursor provides the dominant excitation needed to “crack” the carbon-free silicon-containing precursor in the plasma-free substrate processing region and produce a reaction which deposits the silicon-nitrogen-and-hydrogen-containing layer on the deposition substrate 206. Once again, the deposited silicon-nitrogen-and-hydrogen-containing layer may have flowable characteristics unlike conventional silicon nitride (Si3N4) layer deposition techniques. The process effluents may be removed from the substrate processing region after formation of the silicon-nitrogen-and-hydrogen-containing layer. Process effluents may include any unreacted silicon-containing precursor, unreacted radical-nitrogen precursor, inert carrier gases and reaction products from the layer growth. The process effluents may be displaced by flowing inert species into the substrate processing region and/or by exhaustion through an exhaust port in disclosed embodiments.


The method 200 further includes an additional treatment of the silicon-nitrogen-and-hydrogen-containing layer to form a silicon oxide from a portion of the silicon-nitrogen-and-hydrogen-containing layer. This silicon oxide capping layer is formed using some of the material of the silicon-nitrogen-and-hydrogen-containing layer in contrast to the method of FIG. 1. However, the purpose of the formed silicon oxide capping layer is the same as FIG. 1: to avoid outgassing from the underlying layer. The formation of the silicon oxide capping layer may occur in the same substrate processing region or the substrate may be transferred into a separate processing region. The substrate may be exposed to atmosphere during the transfer or may be kept under vacuum in embodiments of the invention. A benefit of forming the silicon oxide capping layer is to avoid the time-evolution of film properties of the silicon-nitrogen-and-hydrogen-containing layer before subsequent processing is carried out. As such, a controllable and reproducible amount of exposure of the substrate to atmosphere is desirable prior to formation of the silicon oxide capping layer. The formation of the silicon oxide capping layer is initiated by providing an oxygen-containing precursor to the substrate processing region 208. A plasma is concurrently formed in the substrate processing region 210 to form the silicon oxide capping layer 112 using material from the silicon-nitrogen-and-hydrogen-containing film and oxygen from the oxygen-containing precursor. A remote plasma (outside the substrate processing region) had been used to deposit the silicon-nitrogen-and-hydrogen-containing layer whereas a local plasma (within the substrate processing region) is used to form the silicon oxide capping layer.


The oxygen-containing precursor may include molecular oxygen (O2) and/or ozone (O3). The plasma power applied to the substrate processing region may be below or about 1000 W, below or about 500 W, or below or about 300 W. The plasma power applied to the substrate processing region may be above or about 50 W, above or about 100 W, or above or about 200 W in embodiments of the invention. The upper limits on the plasma power may be combined with the lower limits to form additional embodiments. The plasma power is lower than many plasma-enhanced chemical vapor deposition (PE-CVD) processes in order to essentially maintain the structure of the underlying silicon-nitrogen-and-hydrogen-containing layer. The plasma frequency may be 13.56 MHz and/or 350 KHz. Gases that are optionally introduced into the chamber at the same time as the silicon-containing precursor include helium and/or argon. Helium or other inert gases may be used as a carrier gas to deliver ordinarly liquid precursors to the substrate processing region.


The oxygen-containing precursor may be introduced into the chamber at a flow rate of between about 10 sccm and about 1000 sccm. The pressure inside the substrate processing region may be greater than about 500 mTorr, such as between about 2 Torr and about 10 Torr, and the temperature of a substrate support in the chamber may be between about 100° C. and about 250° C. while the oxygen-containing precursor is flowed into the chamber to form the silicon oxide capping layer. Preferably, the temperature is below about 250° C. or below about 200° C. in disclosed embodiments. The low substrate temperatures are desirable (like the low plasma powers) in order to preserve the structure of the silicon-nitrogen-and-hydrogen-containing layer so layer properties are predictable at the time further processing begins. The silicon-containing precursor and the oxygen-containing precursor may each be flowed into the chamber for a period of time sufficient to deposit a layer having a thickness of greater than or about 10 nm, greater than or about 20 nm, greater than or about 50 nm, or greater than or about 100 nm.


The layer stack is ready to be cured or annealed after either of exemplary methods 100 or 200 is complete. A curing stage may involve exposing the silicon oxide capping layer and the carbon-free silicon-nitrogen-and-hydrogen-containing layer to an oxygen-containing atmosphere. The oxygen-containing atmosphere may include ozone in embodiments of the invention. The deposition substrate may remain in the substrate processing region for curing, or the substrate may be transferred to a different chamber where the oxygen-containing atmosphere is introduced. The curing temperature of the substrate may be less than or about 300° C., less than or about 250° C., less than or about 225° C., or less than or about 200° C. in different embodiments. The temperature of the substrate may be greater than or about room temperature (25° C.), greater than or about 50° C., greater than or about 100° C., greater than or about 125° C. or greater than or about 150° C. in different embodiments. Any of the upper bounds may be combined with any of the lower bounds to form additional ranges for the substrate temperature according to additional disclosed embodiments.


The curing operation modified the carbon-free silicon-nitrogen-and-hydrogen-containing layer into a silicon-and-oxygen-containing layer. The silicon-and-oxygen-containing layer may be converted into a silicon oxide layer by annealing the substrate at relatively high temperature in an oxygen-containing environment. The deposition substrate may remain in the same substrate processing region used for curing when the oxygen-containing atmosphere is introduced, or the substrate may be transferred to a different chamber where the oxygen-containing atmosphere is introduced. The oxygen-containing atmosphere may include one or more oxygen-containing gases such as molecular oxygen (O2), ozone (O3), water vapor (H2O), hydrogen peroxide (H2O2) and nitrogen-oxides (NO, NO2, etc.), among other oxygen-containing gases. The oxygen-containing atmosphere may also include radical oxygen and hydroxyl species such as atomic oxygen (O), hydroxides (OH), etc., that may be generated remotely and transported into the substrate chamber. Ions of oxygen-containing species may also be present. The oxygen-containing atmospheres of the curing and annealing operations provide oxygen to convert the silicon-nitrogen-and-hydrogen-containing layer into a silicon oxide (SiO2) layer. The oxygen anneal temperature of the substrate may be less than or about 1100° C., less than or about 1000° C., less than or about 900° C. or less than or about 800° C. in different embodiments. The temperature of the substrate may be greater than or about 500° C., greater than or about 600° C., greater than or about 700° C. or greater than or about 800° C. in different embodiments. Once again, any of the upper bounds may be combined with any of the lower bounds to form additional ranges for the substrate temperature according to additional disclosed embodiments.


The substrate used for depositing the carbon-free silicon-nitrogen-and-hydrogen-containing layer and the capping layer may be a patterned substrate and may have a plurality of gaps for the spacing and structure of device components (e.g., transistors) formed on the substrate. The gaps may have a height and width that define an aspect ratio (AR) of the height to the width (i.e., H/W) that is significantly greater than 1:1 (e.g., 5:1 or more, 6:1 or more, 7:1 or more, 8:1 or more, 9:1 or more, 10:1 or more, 11:1 or more, 12:1 or more, etc.). In many instances the high AR is due to small gap widths of that range from about 90 nm to about 22 nm or less (e.g., less than 90 nm, 65 nm, 50 nm, 45 nm, 32 nm, 22 run, 16 nm, etc.). Because the carbon-free silicon-nitrogen-and-hydrogen-containing layer is flowable, it can fill gaps with high aspect ratios without creating voids or weak seams around the center of the filling material. For example, a depositing flowable material is less likely to prematurely clog the top of a gap before it is completely filled to leave a void in the middle of the gap.


Additional process parameters may be introduced during the description of an exemplary silicon oxide deposition system.


Exemplary Silicon Oxide Deposition System


Deposition chambers that may implement embodiments of the present invention may include high-density plasma chemical vapor deposition (HDP-CVD) chambers, plasma enhanced chemical vapor deposition (PECVD) chambers, sub-atmospheric chemical vapor deposition (SACVD) chambers, and thermal chemical vapor deposition chambers, among other types of chambers. Specific examples of CVD systems that may implement embodiments of the invention include the CENTURA ULTIMA® HDP-CVD chambers/systems, and PRODUCER® PECVD chambers/systems, available from Applied Materials, Inc. of Santa Clara, Calif.


Examples of substrate processing chambers that can be used with exemplary methods of the invention may include those shown and described in co-assigned U.S. Provisional Patent App. No. 60/803,499 to Lubomirsky et al, filed May 30, 2006, and titled “PROCESS CI-IAMBER FOR DIELECTRIC GAPFILL,” the entire contents of which is herein incorporated by reference for all purposes. Additional exemplary systems may include those shown and described in U.S. Pat. Nos. 6,387,207 and 6,830,624, which are also incorporated herein by reference for all purposes.


Embodiments of the deposition systems may be incorporated into larger fabrication systems for producing integrated circuit chips. FIG. 3 shows one such system 300 of deposition, baking and curing chambers according to disclosed embodiments. In the figure, a pair of FOUPs (front opening unified pods) 302 supply substrate substrates (e.g., 300 mm diameter wafers) that are received by robotic arms 304 and placed into a low pressure holding area 306 before being placed into one of the substrate processing chambers 308a-f. A second robotic arm 310 may be used to transport the substrate wafers from the low pressure holding area 306 to the substrate processing chambers 308a-f and back.


Substrate processing chambers 308a-f may include one or more system components for depositing, annealing, curing and/or etching a flowable dielectric layer on the substrate wafer. In one configuration, two pairs of the processing chamber (e.g., 308c-d and 308e-f) may be used to deposit the flowable dielectric material on the substrate, and the third pair of processing chambers (e.g., 308a-b) may be used to anneal the deposited dielectric. In another configuration, the same two pairs of processing chambers (e.g., 308c-d and 308e-f) may be configured to both deposit and anneal a flowable dielectric layer on the substrate, while the third pair of chambers (e.g., 308a-b) may be used for UV or E-beam curing of the deposited layer. In still another configuration, all three pairs of chambers (e.g., 308a-f) may be configured to deposit and cure a flowable dielectric layer on the substrate. In yet another configuration, two pairs of processing chambers (e.g., 308c-d and 308e-f) may be used for both deposition and UV or E-beam curing of the flowable dielectric, while a third pair of processing chambers (e.g. 308a-b) may be used for annealing the dielectric layer. Any one or more of the processes described may be carried out on chamber(s) separated from the fabrication system shown in different embodiments.


In addition, one or more of the substrate processing chambers 308a-f may be configured as a wet treatment chamber. These process chambers include heating the flowable dielectric layer in an atmosphere that includes moisture. Thus, embodiments of system 300 may include wet treatment chambers and anneal processing chambers to perform both wet and dry anneals on the deposited dielectric layer.



FIG. 4A is a substrate processing chamber 400 according to disclosed embodiments. A remote plasma system (RPS) 410 may process a gas which then travels through a gas inlet assembly 411. Two distinct gas supply channels are visible within the gas inlet assembly 411. A first channel 412 carries a gas that passes through the remote plasma system (RPS) 410, while a second channel 413 bypasses the RPS 410. The first channel 412 may be used for the process gas and the second channel 413 may be used for a treatment gas in disclosed embodiments. The lid (or conductive top portion) 421 and a perforated partition or showerhead 453 are shown with an insulating ring 424 in between, which allows an AC potential to be applied to the lid 421 relative to showerhead 453: The process gas travels through first channel 412 into chamber plasma region 420 and may be excited by a plasma in chamber plasma region 420 alone or in combination with RPS 410. The combination of chamber plasma region 420 and/or RPS 410 may be referred to as a remote plasma system herein. The perforated partition (also referred to as a showerhead) 453 separates chamber plasma region 420 from a substrate processing region 470 beneath showerhead 453. Showerhead 453 allows a plasma present in chamber plasma region 420 to avoid directly exciting gases in substrate processing region 470, while still allowing excited species to travel from chamber plasma region 420 into substrate processing region 470.


Showerhead 453 is positioned between chamber plasma region 420 and substrate processing region 470 and allows plasma effluents (excited derivatives of precursors or other gases) created within chamber plasma region 420 to pass through a plurality of through-holes 456 that traverse the thickness of the plate. The showerhead 453 also has one or more hollow volumes 451 which can be filled with a precursor in the form of a vapor or gas (such as a silicon-containing precursor) and pass through small holes 455 into substrate processing region 470 but not directly into chamber plasma region 420. Showerhead 453 is thicker than the length of the smallest diameter 450 of the through-holes 456 in this disclosed embodiment. In order to maintain a significant concentration of excited species penetrating from chamber plasma region 420 to substrate processing region 470, the length 426 of the smallest diameter 450 of the through-holes may be restricted by forming larger diameter portions of through-holes 456 part way through the showerhead 453. The length of the smallest diameter 450 of the through-holes 456 may be the same order of magnitude as the smallest diameter of the through-holes 456 or less in disclosed embodiments.


In the embodiment shown, showerhead 453 may distribute (via through-holes 456) process gases which contain oxygen, hydrogen and/or nitrogen and/or plasma effluents of such process gases upon excitation by a plasma in chamber plasma region 420. In embodiments, the process gas introduced into the RPS 410 and/or chamber plasma region 420 through first channel 412 may contain one or more of oxygen (O2), ozone (O3), N2O, NO, NO2, NH3, NxHy including N2H4, silane, disilane, TSA and DSA. The process gas may also include a carrier gas such as helium, argon, nitrogen (N2), etc. The second channel 413 may also deliver a process gas and/or a carrier gas, and/or a layer-curing gas (e.g. O3) used to remove an unwanted component from the growing or as-deposited layer. Plasma effluents may include ionized or neutral derivatives of the process gas and may also be referred to herein as a radical-oxygen precursor and/or a radical-nitrogen precursor referring to the atomic constituents of the process gas introduced.


In embodiments, the number of through-holes 456 may be between about 60 and about 2000. Through-holes 456 may have a variety of shapes but are most easily made round. The smallest diameter 450 of through-holes 456 may be between about 0.5 mm and about 20 mm or between about 1 mm and about 6 mm in disclosed embodiments. There is also latitude in choosing the cross-sectional shape of through-holes, which may be made conical, cylindrical or a combination of the two shapes. The number of small holes 455 used to introduce a gas into substrate processing region 470 may be between about 100 and about 5000 or between about 500 and about 2000 in different embodiments. The diameter of the small holes 455 may be between about 0.1 mm and about 2 mm.



FIG. 4B is a bottom view of a showerhead 453 for use with a processing chamber according to disclosed embodiments. Showerhead 453 corresponds with the showerhead shown in FIG. 3A. Through-holes 456 are depicted with a larger inner-diameter (ID) on the bottom of showerhead 453 and a smaller ID at the top. Small holes 455 are distributed substantially evenly over the surface of the showerhead, even amongst the through-holes 456 which helps to provide more even mixing than other embodiments described herein.


An exemplary layer is created on a substrate supported by a pedestal (not shown) within substrate processing region 470 when plasma effluents arriving through through-holes 456 in showerhead 453 combine with a silicon-containing precursor arriving through the small holes 455 originating from hollow volumes 451. Though substrate processing region 470 may be equipped to support a plasma for other processes such as curing, no plasma is present during the growth of the exemplary layer.


A plasma may be ignited either in chamber plasma region 420 above showerhead 453 or substrate processing region 470 below showerhead 453. A plasma is present in chamber plasma region 420 to produce the radical nitrogen precursor from an inflow of a nitrogen-and-hydrogen-containing gas. An AC voltage typically in the radio frequency (RF) range is applied between the conductive top portion formed in lid 421 of the processing chamber and showerhead 453 to ignite a plasma in chamber plasma region 420 during deposition. An RF power supply generates a high RF frequency of 13.56 MHz but may also generate other frequencies alone or in combination with the 13.56 MHz frequency.


The top plasma may be left at low or no power when the bottom plasma in the substrate processing region 470 is turned on during the second curing stage or clean the interior surfaces bordering substrate processing region 470. A plasma in substrate processing region 470 is ignited by applying an AC voltage between showerhead 453 and the pedestal or bottom of the chamber. A cleaning gas may be introduced into substrate processing region 470 while the plasma is present.


The pedestal may have a heat exchange channel through which a heat exchange fluid flows to control the temperature of the substrate. This configuration allows the substrate temperature to be cooled or heated to maintain relatively low temperatures (from room temperature through about 120° C.). The heat exchange fluid may comprise ethylene glycol and water. The wafer support platter of the pedestal (preferably aluminum, ceramic, or a combination thereof) may also be resistively heated in order to achieve relatively high temperatures (from about 120° C. through about 1100° C.) using an embedded single-loop embedded heater element configured to make two full turns in the form of parallel concentric circles. An outer portion of the heater element may run adjacent to a perimeter of the support platter, while an inner portion runs on the path of a concentric circle having a smaller radius. The wiring to the heater element passes through the stem of the pedestal.


The substrate processing system is controlled by a system controller. In an exemplary embodiment, the system controller includes a hard disk drive, a floppy disk drive and a processor. The processor contains a single-board computer (SBC), analog and digital input/output boards, interface boards and stepper motor controller boards. Various parts of CVD system conform to the Versa Modular European (VME) standard which defines board, card cage, and connector dimensions and types. The VME standard also defines the bus structure as having a 16-bit data bus and a 24-bit address bus.


The system controller controls all of the activities of the deposition system. The system controller executes system control software, which is a computer program stored in a computer-readable medium. Preferably, the medium is a hard disk drive, but the medium may also be other kinds of memory. The computer program includes sets of instructions that dictate the timing, mixture of gases, chamber pressure, chamber temperature, RF power levels, susceptor position, and other parameters of a particular process. Other computer programs stored on other memory devices including, for example, a floppy disk or other another appropriate drive, may also be used to instruct the system controller.


A process for depositing a layer stack (e.g. sequential deposition of a carbon-free silicon-nitrogen-and-hydrogen-containing layer and then a silicon oxide capping layer) on a substrate, converting a layer to silicon oxide or a process for cleaning a chamber can be implemented using a computer program product that is executed by the system controller. The computer program code can be written in any conventional computer readable programming language: for example, 68000 assembly language, C, C++, Pascal, Fortran or others. Suitable program code is entered into a single file, or multiple files, using a conventional text editor, and stored or embodied in a computer usable medium, such as a memory system of the computer. If the entered code text is in a high level language, the code is compiled, and the resultant compiler code is then linked with an object code of precompiled Microsoft Windows® library routines. To execute the linked, compiled object code the system user invokes the object code, causing the computer system to load the code in memory. The CPU then reads and executes the code to perform the tasks identified in the program.


The interface between a user and the controller is via a flat-panel touch-sensitive monitor. In the preferred embodiment two monitors are used, one mounted in the clean room wall for the operators and the other behind the wall for the service technicians. The two monitors may simultaneously display the same information, in which case only one accepts input at a time. To select a particular screen or function, the operator touches a designated area of the touch-sensitive monitor. The touched area changes its highlighted color, or a new menu or screen is displayed, confirming communication between the operator and the touch-sensitive monitor. Other devices, such as a keyboard, mouse, or other pointing or communication device, may be used instead of or in addition to the touch-sensitive monitor to allow the user to communicate with the system controller.


As used herein “substrate” may be a support substrate with or without layers formed thereon. The support substrate may be an insulator or a semiconductor of a variety of doping concentrations and profiles and may, for example, be a semiconductor substrate of the type used in the manufacture of integrated circuits. A layer of “silicon oxide” may include minority concentrations of other elemental constituents such as nitrogen, hydrogen, carbon and the like. In some embodiments, silicon oxide consists essentially of silicon and oxygen. The term “precursor” is used to refer to any process gas which takes part in a reaction to either remove material from or deposit material onto a surface. A gas in an “excited state” describes a gas wherein at least some of the gas molecules are in vibrationally-excited, dissociated and/or ionized states. A gas (or precursor) may be a combination of two or more gases (or precursors). A “radical precursor” is used to describe plasma effluents (a gas in an excited state which is exiting a plasma) which participate in a reaction to either remove material from or deposit material on a surface. A “radical-nitrogen precursor” is a radical precursor which contains nitrogen and a “radical-hydrogen precursor” is a radical precursor which contains hydrogen. The phrase “inert gas” refers to any gas which does not form chemical bonds when etching or 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.


The term “trench” is used throughout with no implication that the etched geometry has a large horizontal aspect ratio. Viewed from above the surface, trenches may appear circular, oval, polygonal, rectangular, or a variety of other shapes. The term “via” is used to refer to a low aspect ratio trench which may or may not be filled with metal to form a vertical electrical connection. As used herein, a conformal layer refers to a generally uniform layer of material on a surface in the same shape as the surface, i.e., the surface of the layer and the surface being covered are generally parallel. A person having ordinary skill in the art will recognize that the deposited material likely cannot be 100% conformal and thus the term “generally” allows for acceptable tolerances.


Having described 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 invention. Additionally, a number of well-known processes and elements have not been described in order to avoid unnecessarily obscuring the present invention. Accordingly, the above description should not be taken as limiting the scope of the invention.


Where a range of values is provided, it is understood that each intervening value, to the tenth of the unit of the lower limit unless the context clearly dictates otherwise, between the upper and lower limits of that range is also specifically disclosed. Each smaller range between any stated value or intervening value in a stated range and any other stated or intervening value in that stated range is encompassed. The upper and lower limits of these smaller ranges may independently be included or excluded in the range, and each range where either, neither or both limits are included in the smaller ranges is also encompassed within the invention, subject to any specifically excluded limit in the stated range. Where the stated range includes one or both of the limits, ranges excluding either or both of those included limits are also included.


As used herein and in the appended claims, the singular forms “a”, “an”, and “the” include plural referents unless the context clearly dictates otherwise. Thus, for example, reference to “a process” includes a plurality of such processes and reference to “the precursor” includes reference to one or more precursor and equivalents thereof known to those skilled in the art, and so forth.


Also, the words “comprise,” “comprising,” “include,” “including,” and “includes” when used in this specification and in the following claims are-intended to specify the presence of stated features, integers, components, or steps, but they do not preclude the presence or addition of one or more other features, integers, components, steps, acts, or groups.

Claims
  • 1. A method of forming a dielectric layer on a substrate, the method comprising the sequential steps of: forming a carbon-free silicon-nitrogen-and-hydrogen-containing layer on the substrate in a first substrate processing region containing the substrate by: flowing an unexcited precursor into a remote plasma region to produce a radical-precursor,combining a carbon-free silicon-containing precursor with the radical-precursor in the first substrate processing region, wherein the first substrate processing region is devoid of plasma during the forming the carbon-free silicon-nitrogen-and-hydrogen-containing layer, anddepositing a carbon-free silicon-nitrogen-and-hydrogen-containing layer over the substrate, wherein the carbon-free silicon-nitrogen-and-hydrogen-containing layer is flowable during deposition and flows into a trench on a deposition surface of the substrate as the carbon-free silicon-nitrogen-and hydrogen-containing layer deposits; andforming a silicon oxide capping layer on the carbon-free silicon-nitrogen-and-hydrogen-containing layer by: flowing an oxygen-containing precursor into a second substrate processing region containing the substrate,flowing a silicon-containing precursor into the second substrate processing region,forming a plasma from the oxygen-containing precursor and the silicon-containing precursor in the second substrate processing region, anddepositing the silicon oxide capping layer over the carbon-free silicon-nitrogen-and-hydrogen-containing layerwherein the dielectric layer comprises the carbon-free silicon-nitrogen-and-hydrogen-containing layer and the silicon oxide capping layer; andconverting the underlying carbon-free silicon-nitrogen-and-hydrogen-containing layer to silicon oxide despite an intervening presence of the silicon oxide capping layer.
  • 2. The method of claim 1 wherein a temperature of the substrate is greater than or about 25° C. and less than or about 125° C. during formation of the carbon-free silicon-nitrogen-and-hydrogen-containing layer.
  • 3. The method of claim 1 wherein the substrate temperature is less than or about 200° C. during formation of the silicon oxide capping layer.
  • 4. The method of claim 1 wherein a thickness of the silicon oxide capping layer is about 10 nm or more.
  • 5. The method of claim 1 wherein the unexcited precursor comprises nitrogen and the radical precursor is a radical-nitrogen precursor.
  • 6. The method of claim 1 wherein the unexcited precursor comprises at least one of N2H2, NH3, N2 and H2 and the carbon-free silicon-containing precursor comprises one of H2N(SiH3), HN(SiH3)2 or N(SiH3)3.
  • 7. The method of claim 1 wherein the first substrate processing region is the second substrate processing region.
  • 8. The method of claim 1 wherein forming a plasma from the oxygen-containing precursor and the silicon-containing precursor in the second substrate processing region comprises applying a plasma power of below or about 1000 W.
  • 9. The method of claim 1 wherein a thickness of the silicon oxide capping layer is greater than or about 50 nm.
CROSS-REFERENCES TO RELATED APPLICATIONS

This application claims the benefit of U.S. Prov. Pat. App. No. 61/508,355 filed Jul. 15, 2011, and titled “SURFACE TREATMENT AND DEPOSITION FOR REDUCED OUTGASSING,” which is entirely incorporated herein by reference for all purposes.

US Referenced Citations (457)
Number Name Date Kind
4147571 Stringfellow et al. Apr 1979 A
4200666 Reinberg Apr 1980 A
4816098 Davis et al. Mar 1989 A
4818326 Liu et al. Apr 1989 A
4910043 Freeman et al. Mar 1990 A
4931354 Wakino et al. Jun 1990 A
4946593 Pinigis Aug 1990 A
5016332 Reichelderfer et al. May 1991 A
5110407 Ono et al. May 1992 A
5212119 Hah et al. May 1993 A
5271972 Kwok et al. Dec 1993 A
5279784 Bender et al. Jan 1994 A
5364488 Minato et al. Nov 1994 A
5393708 Hsia et al. Feb 1995 A
5426076 Moghadam Jun 1995 A
5434109 Geissler et al. Jul 1995 A
5468687 Carl et al. Nov 1995 A
5485420 Lage et al. Jan 1996 A
5530293 Cohen et al. Jun 1996 A
5547703 Camilletti et al. Aug 1996 A
5558717 Zhao et al. Sep 1996 A
5578532 van de Ven et al. Nov 1996 A
5587014 Lyechika et al. Dec 1996 A
5593741 Ikeda Jan 1997 A
5620525 van de Ven et al. Apr 1997 A
5622784 Okaue et al. Apr 1997 A
5635409 Moslehi Jun 1997 A
5665643 Shin Sep 1997 A
5691009 Sandhu Nov 1997 A
5769951 van de Ven et al. Jun 1998 A
5786263 Perera Jul 1998 A
5811325 Lin et al. Sep 1998 A
5843233 van de Ven et al. Dec 1998 A
5853607 Zhao et al. Dec 1998 A
5882417 van de Ven et al. Mar 1999 A
5925411 van de Ven et al. Jul 1999 A
5926737 Ameen et al. Jul 1999 A
5935340 Xia et al. Aug 1999 A
5937308 Gardner et al. Aug 1999 A
5937323 Orczyk et al. Aug 1999 A
5961850 Satou et al. Oct 1999 A
5966595 Thakur et al. Oct 1999 A
6008515 Hsia et al. Dec 1999 A
6009830 Li et al. Jan 2000 A
6014979 Van Autryve et al. Jan 2000 A
6017791 Wang et al. Jan 2000 A
6024044 Law et al. Feb 2000 A
6087243 Wang Jul 2000 A
6090442 Klaus et al. Jul 2000 A
6090723 Thakur et al. Jul 2000 A
6110838 Loewenstein Aug 2000 A
6114219 Spikes et al. Sep 2000 A
6121130 Chua et al. Sep 2000 A
6140242 Oh et al. Oct 2000 A
6146970 Witek et al. Nov 2000 A
6150286 Sun et al. Nov 2000 A
6156394 Yamasaki et al. Dec 2000 A
6156581 Vaudo et al. Dec 2000 A
6165834 Agarwal et al. Dec 2000 A
6180490 Vassiliev et al. Jan 2001 B1
6187682 Denning et al. Feb 2001 B1
6191004 Hsiao Feb 2001 B1
6207587 Li et al. Mar 2001 B1
6211040 Liu et al. Apr 2001 B1
6258690 Zenke Jul 2001 B1
6287962 Lin Sep 2001 B1
6296255 Hashimoto Oct 2001 B1
6302964 Umotoy et al. Oct 2001 B1
6339997 Nakagawa et al. Jan 2002 B1
6355581 Vassiliev et al. Mar 2002 B1
6383954 Wang et al. May 2002 B1
6387207 Janakiraman et al. May 2002 B1
6406677 Carter et al. Jun 2002 B1
6413583 Moghadam et al. Jul 2002 B1
6448187 Yau et al. Sep 2002 B2
6469283 Burkhart et al. Oct 2002 B1
6503557 Joret Jan 2003 B1
6506253 Sakuma Jan 2003 B2
6508879 Hashimoto Jan 2003 B1
6509283 Thomas Jan 2003 B1
6524931 Perera Feb 2003 B1
6528332 Mahanpour et al. Mar 2003 B2
6544900 Raaijmakers et al. Apr 2003 B2
6548416 Han et al. Apr 2003 B2
6548899 Ross Apr 2003 B2
6559026 Rossman et al. May 2003 B1
6566278 Harvey et al. May 2003 B1
6583063 Khan et al. Jun 2003 B1
6583069 Vassiliev et al. Jun 2003 B1
6589868 Rossman Jul 2003 B2
6596654 Bayman et al. Jul 2003 B1
6599839 Gabriel et al. Jul 2003 B1
6602806 Xia et al. Aug 2003 B1
6614181 Harvey et al. Sep 2003 B1
6624064 Sahin et al. Sep 2003 B1
6630413 Todd Oct 2003 B2
6645303 Frankel et al. Nov 2003 B2
6656804 Tsujikawa et al. Dec 2003 B2
6660391 Rose et al. Dec 2003 B1
6667553 Cerny et al. Dec 2003 B2
6670284 Yin Dec 2003 B2
6676751 Solomon et al. Jan 2004 B2
6682659 Cho et al. Jan 2004 B1
6682969 Basceri et al. Jan 2004 B1
6683364 Oh et al. Jan 2004 B2
6706634 Seitz et al. Mar 2004 B1
6716770 O'Neill et al. Apr 2004 B2
6756085 Waldfried et al. Jun 2004 B2
6762126 Cho et al. Jul 2004 B2
6787191 Hanahata et al. Sep 2004 B2
6794290 Papasouliotis et al. Sep 2004 B1
6800571 Cheung et al. Oct 2004 B2
6818517 Maes Nov 2004 B1
6819886 Runkowske et al. Nov 2004 B2
6830624 Janakiraman et al. Dec 2004 B2
6833052 Li et al. Dec 2004 B2
6833322 Anderson et al. Dec 2004 B2
6833578 Tu et al. Dec 2004 B1
6835278 Selbrede et al. Dec 2004 B2
6849520 Kim et al. Feb 2005 B2
6858523 Deboer et al. Feb 2005 B2
6858533 Chu et al. Feb 2005 B2
6867086 Chen et al. Mar 2005 B1
6872323 Entley et al. Mar 2005 B1
6875687 Weidman et al. Apr 2005 B1
6890403 Cheung May 2005 B2
6900067 Kobayashi et al. May 2005 B2
6955836 Kumagai et al. Oct 2005 B2
6958112 Karim et al. Oct 2005 B2
7018902 Visokay et al. Mar 2006 B2
7077904 Cho et al. Jul 2006 B2
7084076 Park et al. Aug 2006 B2
7087497 Yuan et al. Aug 2006 B2
7109114 Chen et al. Sep 2006 B2
7115419 Suzuki Oct 2006 B2
7122222 Xiao et al. Oct 2006 B2
7129185 Aoyama et al. Oct 2006 B2
7148155 Tarafdar et al. Dec 2006 B1
7176144 Wang et al. Feb 2007 B1
7183177 Al-Bayati et al. Feb 2007 B2
7192626 Dussarrat et al. Mar 2007 B2
7205248 Li et al. Apr 2007 B2
7220461 Hasebe et al. May 2007 B2
7297608 Papasouliotis et al. Nov 2007 B1
7335609 Ingle et al. Feb 2008 B2
7399388 Moghadam et al. Jul 2008 B2
7419903 Haukka et al. Sep 2008 B2
7435661 Miller et al. Oct 2008 B2
7456116 Ingle et al. Nov 2008 B2
7498273 Mallick et al. Mar 2009 B2
7514375 Shanker et al. Apr 2009 B1
7521378 Fucsko et al. Apr 2009 B2
7524735 Gauri et al. Apr 2009 B1
7524750 Nemani et al. Apr 2009 B2
7541297 Mallick et al. Jun 2009 B2
7622369 Lee et al. Nov 2009 B1
7745352 Mallick et al. Jun 2010 B2
7749574 Mahajani et al. Jul 2010 B2
7790634 Munro et al. Sep 2010 B2
7803722 Liang Sep 2010 B2
7825038 Ingle et al. Nov 2010 B2
7825044 Mallick et al. Nov 2010 B2
7867923 Mallick et al. Jan 2011 B2
7902080 Chen et al. Mar 2011 B2
7915139 Lang et al. Mar 2011 B1
7935643 Liang et al. May 2011 B2
7943514 West May 2011 B2
7943531 Nemani et al. May 2011 B2
7989365 Park et al. Aug 2011 B2
7994019 Kweskin et al. Aug 2011 B1
8119544 Hasebe et al. Feb 2012 B2
8129555 Cheng et al. Mar 2012 B2
8232176 Lubomirsky et al. Jul 2012 B2
8236708 Kweskin et al. Aug 2012 B2
8242031 Mallick et al. Aug 2012 B2
8264066 Lo et al. Sep 2012 B2
8304351 Wang et al. Nov 2012 B2
8318584 Li et al. Nov 2012 B2
8329587 Liang et al. Dec 2012 B2
8445078 Liang et al. May 2013 B2
8449942 Liang et al. May 2013 B2
8466067 Liang et al. Jun 2013 B2
8466073 Wang et al. Jun 2013 B2
8551891 Liang et al. Oct 2013 B2
8563445 Liang et al. Oct 2013 B2
8741788 Liang et al. Jun 2014 B2
8975152 Hong et al. Mar 2015 B2
8980382 Ingle et al. Mar 2015 B2
8986557 Underwood et al. Mar 2015 B2
9018108 Hong et al. Apr 2015 B2
9136273 Purayath Sep 2015 B1
20010021595 Jang et al. Sep 2001 A1
20010029114 Vulpio et al. Oct 2001 A1
20010038919 Berry et al. Nov 2001 A1
20010042511 Liu et al. Nov 2001 A1
20010048980 Kishimoto et al. Dec 2001 A1
20010054387 Frankel et al. Dec 2001 A1
20010055889 Iyer Dec 2001 A1
20020027286 Sundararajan et al. Mar 2002 A1
20020048969 Suzuki et al. Apr 2002 A1
20020068416 Hsieh et al. Jun 2002 A1
20020068466 Lee et al. Jun 2002 A1
20020079523 Zheng et al. Jun 2002 A1
20020081817 Bhakta et al. Jun 2002 A1
20020081842 Sambucetti et al. Jun 2002 A1
20020086166 Hendricks et al. Jul 2002 A1
20020119607 Miyasaka et al. Aug 2002 A1
20020127350 Ishikawa et al. Sep 2002 A1
20020129769 Kim et al. Sep 2002 A1
20020142585 Mandal Oct 2002 A1
20020146879 Fu et al. Oct 2002 A1
20020160585 Park Oct 2002 A1
20020164421 Chiang et al. Nov 2002 A1
20020164429 Gaillard et al. Nov 2002 A1
20020164891 Gates et al. Nov 2002 A1
20020177298 Konishi et al. Nov 2002 A1
20020182893 Ballantine et al. Dec 2002 A1
20030001201 Yuzuriha et al. Jan 2003 A1
20030023113 Druzkowski et al. Jan 2003 A1
20030040199 Agarwal Feb 2003 A1
20030064154 Laxman et al. Apr 2003 A1
20030077918 Wu et al. Apr 2003 A1
20030113992 Yau et al. Jun 2003 A1
20030118748 Kumagai et al. Jun 2003 A1
20030124873 Xing et al. Jul 2003 A1
20030143841 Yang et al. Jul 2003 A1
20030159656 Tan et al. Aug 2003 A1
20030172872 Thakur et al. Sep 2003 A1
20030194881 Totsuka et al. Oct 2003 A1
20030199151 Ho et al. Oct 2003 A1
20030203653 Buchanan et al. Oct 2003 A1
20030207561 Dubin et al. Nov 2003 A1
20030232495 Moghadam et al. Dec 2003 A1
20040008334 Sreenivasan et al. Jan 2004 A1
20040020601 Zhao et al. Feb 2004 A1
20040029352 Beyer et al. Feb 2004 A1
20040029353 Zheng et al. Feb 2004 A1
20040048492 Ishikawa et al. Mar 2004 A1
20040065253 Tois et al. Apr 2004 A1
20040079118 M'Saad et al. Apr 2004 A1
20040082131 Tsujikawa et al. Apr 2004 A1
20040084680 Ruelke et al. May 2004 A1
20040110354 Natzle et al. Jun 2004 A1
20040139983 Lakshmanan et al. Jul 2004 A1
20040146661 Kapoor et al. Jul 2004 A1
20040152342 Li et al. Aug 2004 A1
20040161899 Luo et al. Aug 2004 A1
20040166680 Miyajima et al. Aug 2004 A1
20040175501 Lukas et al. Sep 2004 A1
20040180557 Park et al. Sep 2004 A1
20040183202 Usami Sep 2004 A1
20040185641 Tanabe et al. Sep 2004 A1
20040194706 Wang et al. Oct 2004 A1
20040197843 Chou et al. Oct 2004 A1
20040216844 Janakiraman et al. Nov 2004 A1
20040219780 Ohuchi Nov 2004 A1
20040224534 Beulens et al. Nov 2004 A1
20040231590 Ovshinksy Nov 2004 A1
20040241342 Karim et al. Dec 2004 A1
20040253826 Ivanov et al. Dec 2004 A1
20050001556 Hoffman et al. Jan 2005 A1
20050014354 Ozawa et al. Jan 2005 A1
20050019494 Moghadam et al. Jan 2005 A1
20050026443 Goo et al. Feb 2005 A1
20050042889 Lee et al. Feb 2005 A1
20050062165 Saenger et al. Mar 2005 A1
20050087140 Yuda et al. Apr 2005 A1
20050112901 Ji et al. May 2005 A1
20050118794 Babayan et al. Jun 2005 A1
20050121145 Du Bois et al. Jun 2005 A1
20050142895 Ingle et al. Jun 2005 A1
20050153574 Mandal Jul 2005 A1
20050160974 Ivanov et al. Jul 2005 A1
20050181555 Haukka et al. Aug 2005 A1
20050186731 Derderian et al. Aug 2005 A1
20050186789 Agarwal Aug 2005 A1
20050196533 Hasebe et al. Sep 2005 A1
20050196935 Ishitsuka et al. Sep 2005 A1
20050196977 Saito et al. Sep 2005 A1
20050224866 Higashi et al. Oct 2005 A1
20050227017 Senzaki et al. Oct 2005 A1
20050227499 Park et al. Oct 2005 A1
20050230350 Kao et al. Oct 2005 A1
20050233595 Choi et al. Oct 2005 A1
20050250340 Chen et al. Nov 2005 A1
20050257890 Park et al. Nov 2005 A1
20050260347 Narwankar et al. Nov 2005 A1
20050287775 Hasebe et al. Dec 2005 A1
20060011984 Curie Jan 2006 A1
20060014399 Joe Jan 2006 A1
20060030151 Ding et al. Feb 2006 A1
20060030165 Ingle et al. Feb 2006 A1
20060046427 Ingle et al. Mar 2006 A1
20060046506 Fukiage Mar 2006 A1
20060055004 Gates et al. Mar 2006 A1
20060068599 Baek et al. Mar 2006 A1
20060075966 Chen et al. Apr 2006 A1
20060088985 Haverkort et al. Apr 2006 A1
20060090694 Cho et al. May 2006 A1
20060091104 Takeshita et al. May 2006 A1
20060096540 Choi May 2006 A1
20060102977 Fucsko et al. May 2006 A1
20060105106 Balseanu et al. May 2006 A1
20060110939 Joshi et al. May 2006 A1
20060110943 Swerts et al. May 2006 A1
20060121394 Chi Jun 2006 A1
20060158101 Camilletti et al. Jul 2006 A1
20060159847 Porter et al. Jul 2006 A1
20060160372 Dorfman Jul 2006 A1
20060162661 Jung et al. Jul 2006 A1
20060178018 Olsen Aug 2006 A1
20060211265 Trott Sep 2006 A1
20060223315 Yokota et al. Oct 2006 A1
20060228903 McSwiney et al. Oct 2006 A1
20060252240 Gschwandtner et al. Nov 2006 A1
20060263522 Byun Nov 2006 A1
20060281496 Cedraeus Dec 2006 A1
20060286774 Singh et al. Dec 2006 A1
20060286776 Ranish et al. Dec 2006 A1
20070004170 Kawasaki et al. Jan 2007 A1
20070010072 Bailey et al. Jan 2007 A1
20070020392 Kobrin et al. Jan 2007 A1
20070026689 Nakata et al. Feb 2007 A1
20070031598 Okuyama et al. Feb 2007 A1
20070031609 Kumar et al. Feb 2007 A1
20070032054 Ramaswamy et al. Feb 2007 A1
20070049044 Marsh Mar 2007 A1
20070065578 McDougall Mar 2007 A1
20070066022 Chen et al. Mar 2007 A1
20070077777 Gumpher Apr 2007 A1
20070092661 Ryuzaki et al. Apr 2007 A1
20070099438 Ye et al. May 2007 A1
20070108404 Stewart et al. May 2007 A1
20070111546 Iyer et al. May 2007 A1
20070128864 Ma et al. Jun 2007 A1
20070134433 Dussarrat et al. Jun 2007 A1
20070166892 Hori Jul 2007 A1
20070173073 Weber Jul 2007 A1
20070181966 Watatani et al. Aug 2007 A1
20070232071 Balseanu et al. Oct 2007 A1
20070232082 Balseanu et al. Oct 2007 A1
20070275569 Moghadam et al. Nov 2007 A1
20070281106 Lubomirsky et al. Dec 2007 A1
20070281448 Chen et al. Dec 2007 A1
20070281495 Mallick et al. Dec 2007 A1
20070281496 Ingle et al. Dec 2007 A1
20070289534 Lubomirsky et al. Dec 2007 A1
20070298585 Lubomirsky et al. Dec 2007 A1
20080000423 Fukiage Jan 2008 A1
20080014711 Choi et al. Jan 2008 A1
20080014759 Chua et al. Jan 2008 A1
20080020591 Balseanu et al. Jan 2008 A1
20080026597 Munro et al. Jan 2008 A1
20080038486 Treichel et al. Feb 2008 A1
20080063809 Lee et al. Mar 2008 A1
20080070409 Park et al. Mar 2008 A1
20080081104 Hasebe et al. Apr 2008 A1
20080085607 Yu et al. Apr 2008 A1
20080096364 Wilson et al. Apr 2008 A1
20080099431 Kumar et al. May 2008 A1
20080102223 Wagner et al. May 2008 A1
20080102650 Adams et al. May 2008 A1
20080182382 Ingle et al. Jul 2008 A1
20080188087 Chen et al. Aug 2008 A1
20080206954 Choi et al. Aug 2008 A1
20080241358 Joe et al. Oct 2008 A1
20080260969 Dussarrat et al. Oct 2008 A1
20080305648 Fukazawa et al. Dec 2008 A1
20080318429 Ozawa et al. Dec 2008 A1
20090031953 Ingle et al. Feb 2009 A1
20090035917 Ahn et al. Feb 2009 A1
20090053901 Goto et al. Feb 2009 A1
20090054674 Lukas et al. Feb 2009 A1
20090061647 Mallick et al. Mar 2009 A1
20090075490 Dussarrat et al. Mar 2009 A1
20090093132 Xu et al. Apr 2009 A1
20090095714 Chen et al. Apr 2009 A1
20090104755 Mallick et al. Apr 2009 A1
20090104789 Mallick et al. Apr 2009 A1
20090104790 Liang Apr 2009 A1
20090104791 Nemani et al. Apr 2009 A1
20090104798 Hirano Apr 2009 A1
20090142935 Fukuzawa et al. Jun 2009 A1
20090170282 Dong Jul 2009 A1
20090181550 Hasebe et al. Jul 2009 A1
20090194809 Cho Aug 2009 A1
20090203225 Gates et al. Aug 2009 A1
20090206409 Arisumi et al. Aug 2009 A1
20090209081 Matero et al. Aug 2009 A1
20090215251 Vellaikal et al. Aug 2009 A1
20090224374 Bhatia et al. Sep 2009 A1
20090232985 Dussarrat et al. Sep 2009 A1
20090242957 Ma et al. Oct 2009 A1
20090277587 Lubomirsky et al. Nov 2009 A1
20090280650 Lubomirsky et al. Nov 2009 A1
20090289284 Goh et al. Nov 2009 A1
20090294925 Lin et al. Dec 2009 A1
20090298257 Lee et al. Dec 2009 A1
20090325391 De Vusser et al. Dec 2009 A1
20100052066 Yu et al. Mar 2010 A1
20100059889 Gosset et al. Mar 2010 A1
20100081094 Hasebe et al. Apr 2010 A1
20100081293 Mallick et al. Apr 2010 A1
20100099236 Kwon et al. Apr 2010 A1
20100136313 Shimizu et al. Jun 2010 A1
20100140756 Kozasa et al. Jun 2010 A1
20100143609 Fukazawa et al. Jun 2010 A1
20100184302 Lee et al. Jul 2010 A1
20100190317 Iwasawa et al. Jul 2010 A1
20100190348 Akae et al. Jul 2010 A1
20100221428 Dussarrat Sep 2010 A1
20100221925 Lee et al. Sep 2010 A1
20100227276 Mizuno Sep 2010 A1
20100255655 Mallick et al. Oct 2010 A1
20100261318 Feng et al. Oct 2010 A1
20100283097 Endoh et al. Nov 2010 A1
20110014798 Mallick et al. Jan 2011 A1
20110034035 Liang et al. Feb 2011 A1
20110034039 Liang et al. Feb 2011 A1
20110045676 Park et al. Feb 2011 A1
20110111137 Liang et al. May 2011 A1
20110129616 Ingle et al. Jun 2011 A1
20110136347 Kovarsky et al. Jun 2011 A1
20110159213 Cai et al. Jun 2011 A1
20110159703 Liang et al. Jun 2011 A1
20110165347 Miller et al. Jul 2011 A1
20110165781 Liang et al. Jul 2011 A1
20110186990 Mawatari et al. Aug 2011 A1
20110187000 West Aug 2011 A1
20110217851 Liang et al. Sep 2011 A1
20110223774 Kweskin et al. Sep 2011 A1
20120003840 Wang et al. Jan 2012 A1
20120009802 LaVoie et al. Jan 2012 A1
20120074387 King Mar 2012 A1
20120079982 Lubomirsky et al. Apr 2012 A1
20120083133 Solis et al. Apr 2012 A1
20120094468 Bhatia et al. Apr 2012 A1
20120094476 Tanaka et al. Apr 2012 A1
20120111831 Ha May 2012 A1
20120122302 Weidman et al. May 2012 A1
20120142192 Li et al. Jun 2012 A1
20120145079 Lubomirsky et al. Jun 2012 A1
20120161405 Mohn et al. Jun 2012 A1
20120177846 Li et al. Jul 2012 A1
20120190178 Wang et al. Jul 2012 A1
20120193778 Mawatari Aug 2012 A1
20120213940 Mallick Aug 2012 A1
20120225565 Bhatia et al. Sep 2012 A1
20120238108 Chen et al. Sep 2012 A1
20120269989 Liang et al. Oct 2012 A1
20120292720 Chen et al. Nov 2012 A1
20120309205 Wang et al. Dec 2012 A1
20130062736 Brighton et al. Mar 2013 A1
20130084711 Liang et al. Apr 2013 A1
20130149462 Liang et al. Jun 2013 A1
20130193578 Yu et al. Aug 2013 A1
20160064233 Wang Mar 2016 A1
Foreign Referenced Citations (58)
Number Date Country
19654737 Jul 1997 DE
0892083 Jan 1999 EP
1095958 May 2001 EP
1717848 Nov 2006 EP
61-234534 Oct 1986 JP
64-048425 Feb 1989 JP
1-198033 Aug 1989 JP
01-235259 Sep 1989 JP
01241826 Sep 1989 JP
03-197684 Aug 1991 JP
03-286531 Dec 1991 JP
04-328825 Nov 1992 JP
05-259156 Oct 1993 JP
05-304147 Nov 1993 JP
06-077150 Mar 1994 JP
6-168930 Jun 1994 JP
07-014826 Jan 1995 JP
07-169762 Jul 1995 JP
07-316823 Dec 1995 JP
08-236518 Sep 1996 JP
08-288286 Nov 1996 JP
09-237785 Sep 1997 JP
10-163183 Jun 1998 JP
11-274285 Oct 1999 JP
2001-148382 May 2001 JP
2002-370059 Dec 2002 JP
2003-179054 Jun 2003 JP
2004-012315 Jan 2004 JP
2004-327639 Nov 2004 JP
2005-142448 Jun 2005 JP
2005-268396 Sep 2005 JP
2005-302848 Oct 2005 JP
2008-159824 Jul 2008 JP
2008218684 Sep 2008 JP
2011-220127 Nov 2011 JP
10-2004-0091978 Nov 2004 KR
1020040104533 Dec 2004 KR
10-2005-0003758 Jan 2005 KR
10-2005-0072332 Jul 2005 KR
10-2005-0085838 Aug 2005 KR
10-2005-0094183 Sep 2005 KR
1020060081350 Jul 2006 KR
10-2009-0011765 Feb 2009 KR
10-2009-0121361 Nov 2009 KR
10-2009-0122860 Dec 2009 KR
200514163 Apr 2005 TW
200707582 Feb 2007 TW
02077320 Oct 2002 WO
03066933 Aug 2003 WO
2005078784 Aug 2005 WO
2007040856 Apr 2007 WO
2007140376 Dec 2007 WO
2007140424 Dec 2007 WO
2009055340 Apr 2009 WO
2010080216 Jul 2010 WO
WO 2011059675 May 2011 WO
2012145148 Oct 2012 WO
2013025336 Feb 2013 WO
Non-Patent Literature Citations (37)
Entry
Franz, et al., “Conversion of silicon nitride into silicon dioxide through the influence of oxygen,” Solid-State Electronics, Jun. 1971, pp. 449-505, vol. 14, Issue 6, West Germany. Abstract Only.
International Search Report and Written Opinion of PCT/US2011/066275, mailed Sep. 24, 2012, 9 pages.
International Search Report and Written Opinion of PCT/US2012/026786, mailed Jan. 2, 2013, 7 pages.
International Search Report and Written Opinion of PCT/US2012/031640 mailed Oct. 18, 2012, 10 pages.
International Search Report and Written Opinion of PCT/US2012/039629, mailed Dec. 26, 2012, 6 pages.
Tripp, et al., “The Anodic Oxidation of Silicon Nitride Films on Silicon,” Journal of the Electrochemical Society, Feb. 1970, pp. 157-159, vol. 117 (No. 2).
Usenko, et al., “Silicon Nitride Surface Conversion into Oxide to Enable Hydrophilic Bonding,” ECS Meeting Abstracts, 2010, 1 page, Abstract #1716, 218th ECS Meeting.
International Search Report and Written Opinion of PCT/US2012/053999, mailed Feb. 27, 2013, 12 pages.
International Search Report and Written Opinion of PCT/US2012/065086, mailed Mar. 25, 2013, 10 pages.
International Search Report and Written Opinion of PCT/US2012/059400, mailed Mar. 26, 2013, 11 pages.
Wang Li et al., “Properties of Hydrogenated Amorphous Silicon Caarbide Films Irradiated by Excimer Pulse Laser,” 1998, Abstract Only, Acta Physica Sinca (overseas edition), vol. 7, No. 12.
Ying-Yu Xu et al., “Preparation of SiC Thin Film Using Organosilicon by Remote Plasma CVD Method,” Abstract Only, MRS Proceedings; vol. 544; Materials Research Society; 1998.
International Search Report and Written Opinion of PCT/US2011/054635, mailed Jul. 9, 2012, 11 pages.
International Search Report and Written Opinion of PCT/US2011/066601, mailed Jul. 20, 2012, 10 pages.
Alexandrov, Sergei E., et al., “Formation of Silicon Nitride Films by Remote Plasma-enhanced Chemical Vapour Deposition”. Advanced Materials for Optics and Electronics, vol. 2, 301-312 (1993).
Aylett, B. J. et al., “Silicon-Nitrogen Compounds. Part V. Diphenylamino-derivatives of Silane,” J. Chem. Soc. (A), Apr. 1969, pp. 636-638, Inorganic Physical Theory.
Aylett, B. J. et al., “Silicon-Nitrogen Compounds. Part VI. The Preparation and Properties of Disilazane,” J. Chem. Soc. (A), Apr. 1969, pp. 639-642, Inorganic Physical Theory.
Aylett, B. J. et al., “The Preparation and Some Properties of Disilylamine-Correspondence”, p. 167.
Beach, David B., “Infrared and Mass Spectroscopic Study of the Reaction of Silyl Iodide and Ammonia. Infrared Spectrum to Silylamine,” Inorganic Chemistry, Sep. 1992, pp. 4174-4177, vol. 31 No. 20.
Bowen, C., et al., “New Processing Techniques: Sweeping of Quartz Wafers and A Practical Method for Processing Quartz Resonators Under Controlled Conditions,” Proceedings of the 1992 IEEE Frequency Control Symposium, pp. 648-656.
Burg, Anton B. et al., “Silyl-Amino Boron Compounds,” J. Amer. Chem. Soc., Jul. 1950, pp. 3103-3107, vol. 72.
Coltrin, M.E., et al., “Chemistry of AlGaN Particulate Formation,” pp. 42-43, Wide Bandgap Semiconductor Material & Devices.
Davison, A et al., “The Raman Spectra of Manganese and Rhenium Carbonyl Hydrides and Some Related Species,” Inorganic Chemistry, Apr. 1967, pp. 845-847, vol. 6 No. 4.
Dussarrat, C. et al., “Low Pressure Chemical Vapor Deposition of Silicon Nitride Using Mono- and Disilylamine,” Chemical Vapor Deposition XVI and EUROCVD 14 vol. 2 Proceedings of the International Symposium, Part of the 203rd Electrochemical Society Meeting in Paris France, Apr. 27-May 2, 2003, 11 pages, p. 1372-1379; Proceedings vol. 2003-08; Allendorf et al., editors.
Gulleri, G. et al., “Deposition Temperature Determination of HDPCVD Silicon Dioxide Films,” 2005, Microelectronic Engineering, vol. 82, pp. 236-241.
International Search Report and Written Opinion of PCT/US2011/054981, mailed May 9, 2012, 10 pages.
International Search Report and Written Opinion of PCT/US2011/054984, mailed May 11, 2012, 10 pages.
Kang, Hun, “A Study of the Nucleation and Formation of Multi-functional Nanostructures using GaN-Based Materials for Device Applications,” Georgia Institute of Technology, Doctor of Philosophy in the School of Electrical & Computer Engineering Dissertation, Dec. 2006, p. 14, entire dissertation submitted, 187 pages.
Lee, Eun Gu, et al., “Effects of Wet Oxidation on the Electrical Properties of sub-10 nm thick silicon nitride films” Thin Solid Films, Elsevier-Sequoia S.A. Lausanne, CH. vol. 205, No. 2, Dec. 1, 1991, pp. 246-251.
Loboda, M.J., et al., “Chemical influence of inert gas on the thin film stress in plasma-enhanced chemical vapor deposited a-SiN:H films”. Journal of Materials Research, vol. 11, No. 2, Feb. 1996, pp. 391-398.
Lucovsky, G. et al., “Deposition of silicon dioxide and silicon nitride by remote plasma enhanced chemical vapor deposition,” Journal of Vacuum Science & Technology A, vol. 4, No. 3, May-Jun. 1986, pp. 681-688.
Norman, Arlan D. et al., “Reaction of Silylphosphine with Ammonia,” Inoragnic Chemistry, Jun. 1979, pp. 1594-1597, vol. 18 No. 6.
Sujishi, Sei et al., “Effect of Replacement of Carbon by Silicon in Trimethylamine on the Stabilities of the Trimethylboron Addition Compounds. Estimation of the Resonance Energy for Silicon-Nitrogen Partial Double Bond,” Amer. Chem. Soc., Sep. 20, 1954, pp. 4631-4636, vol. 76.
Tsu, D. V. et al., “Silicon Nitride and Silicon Diimide Grown by Remote Plasma Enhanced Chemical Vapor Deposition”, Journal of Vacuum Science and Technology: Part A, AVS/AIP, Melville, NY, US, vol. 4, No. 3, Part 01, May 1, 1986, pp. 480-485.
Ward, L. G. L. et al., “The Preparation and Properties of Bis-Disilanyl Sulphide and Tris-Disilanylamine,” J. Inorg. Nucl. Chem., Dec. 1961, pp. 287-293, vol. 21, Pergamon Press Ltd., Northern Ireland.
Ward, Laird G. L., “Bromosilane, Iodosilane, and Trisilylamine,” Inorganic Syntheses, 1968, pp. 159-170, vol. 11.
Zuckerman, J.J., “Inorganic Reactions and Methods,” Formation of Bonds to N, P, As, Sb, Bi (Part 1), ISBN-0-89573-250-5, 5 pages, vol. 7, VCH Publishers, Inc., New York, excerpt of pp. 76-78, plus title and publishing pages, showing 1988.
Related Publications (1)
Number Date Country
20130149462 A1 Jun 2013 US
Provisional Applications (1)
Number Date Country
61508355 Jul 2011 US