Fabrication of advanced integrated circuits often involve patterning of 1×nm half-pitch features in high volume manufacturing of semiconductors. Multiple patterning techniques may enable feature size scaling based on lithographic techniques such as 193 nm immersion lithography. Self-aligned double patterning is an example of a multiple patterning technique. Extensions of order multiple patterning techniques to 11 nm half pitch and below present challenges.
Provided herein are methods of processing semiconductor substrates to enable deposition of high quality conformal films for use in multiple patterning integration schemes.
One aspect involves a method of processing a semiconductor substrate by depositing a nanolaminate layer on the substrate and depositing a titanium oxide layer on the nanolaminate layer. The nanolaminate layer may have a thickness between about 15 Å and about 200 Å and may have a density lower than the density of the titanium oxide layer. In various embodiments, the method also includes depositing an amorphous carbon layer. In some embodiments, the amorphous carbon layer is patterned. In various embodiments, the nanolaminate layer includes a stack that includes two or more sublayers. In some embodiments, the two or more sublayers include silicon oxide, or titanium oxide, or combinations thereof. In certain embodiments, the stack includes only two sublayers. In some embodiments, the nanolaminate layer includes a first sublayer of silicon oxide and a second sublayer of titanium oxide.
In various embodiments, the nanolaminate layer is silicon oxide or titanium oxide. In certain embodiments, the nanolaminate layer is deposited using a plasma-based process such as plasma-enhanced atomic layer deposition (PEALD) by exposing the substrate to a titanium-containing precursor or a silicon-containing precursor; exposing the substrate to an oxidant; and initiating a plasma while the substrate is exposed to the oxidant. In certain embodiments, the nanolaminate layer is deposited at a temperature between about 50° C. and about 150° C. and the plasma is initiated with a high frequency radio frequency (HFRF) power per square millimeter of substrate area between about 1.768×10−4 W per mm2 and about 1.768×10−3 W per mm2. In certain embodiments, the nanolaminate layer is deposited at a temperature less than about 100° C. An example of a titanium-containing precursor that may be used with the methods disclosed herein is tetrakis(dimethylamino)titanium (TDMAT). An example of a silicon-containing precursor is bis(tertiarybutylamino)silane (SiH2(NHC(CH3)3)2 (BTBAS).
In various embodiments, the titanium oxide layer is deposited by PEALD by exposing the substrate to a titanium-containing precursor; exposing the substrate to an oxidant; and initiating a plasma while the substrate is exposed to the oxidant at a HFRF power per square millimeter of substrate area of at least about 1.768×10−3 W per mm2. Examples of oxidants include nitrous oxide, oxygen, carbon dioxide or a combination thereof. The titanium oxide layer may be deposited at a temperature between about 50° C. and about 400° C. in some embodiments.
Another aspect involves a method of processing a semiconductor substrate by depositing a core layer; depositing a nanolaminate layer on the core layer; and depositing a metal nitride or metal oxide layer on the nanolaminate layer. In some embodiments, the core layer is patterned. In certain embodiments, the core layer may be amorphous carbon or a photoresist. In various embodiments, the nanolaminate layer may be silicon oxide or titanium oxide. In some embodiments, the thickness of the deposited nanolaminate layer is between about 15 Å and about 200 Å.
In certain embodiments, the nanolaminate layer is deposited using PEALD by exposing the substrate to a titanium-containing precursor or a silicon-containing precursor; exposing the substrate to an oxidant; and initiating a plasma while the substrate is exposed to the oxidant. In various embodiments, the nanolaminate layer is deposited at a temperature between about 50° C. and about 150° C. and the plasma is initiated with HFRF power per square millimeter of substrate area between about 1.768×10−4 W per mm2 and about 1.768×10−3 W per mm2. In some embodiments, the nanolaminate layer is deposited at a temperature less than about 100° C.
In various embodiments, the metal nitride or metal oxide layer includes titanium oxide or silicon oxide. The metal nitride or metal oxide layer may have etch selectivity to the core. In certain embodiments, the metal nitride or metal oxide layer is deposited using PEALD by exposing the substrate to a metal-containing precursor; exposing the substrate to an oxidant; and initiating a plasma while the substrate is exposed to the oxidant at a HFRF power per square millimeter of substrate area of at least about 1.768×10−3 W per mm2. Examples of oxidants include nitrous oxide, oxygen, carbon dioxide or combinations thereof. In some embodiments, the metal nitride or metal oxide layer is deposited at a temperature between about 50° C. and about 400° C.
Another aspect involves a method of processing a semiconductor substrate by (a) exposing the substrate to a first titanium-containing precursor or a silicon-containing precursor; (b) exposing the substrate to a first oxidant; (c) initiating a first plasma while the substrate is exposed to the first oxidant with a HFRF power per square millimeter of substrate area between about 1.768×10−4 W per mm2 and about 1.768×10−3 W per mm2; (d) exposing the substrate to a second titanium-containing precursor; (e) exposing the substrate to a second oxidant; and (f) initiating a second plasma while the substrate is exposed to the second oxidant with a HFRF power per square millimeter of substrate area of at least about 1.768×10−3 W per mm2.
In some embodiments, (a) through (c) are processed at temperature between about 50° C. and 150° C. In some embodiments, (d) through (f) are processed at temperature between about 50° C. and 400° C. In some embodiments, (d) through (f) are processed at a higher temperature than (a) through (c) such that transitioning from (c) to (d) includes raising the substrate temperature by at least about 50° C., at least about 100° C., at least about 150° C., or at least about 200° C.
The first titanium-containing precursor and the second titanium-containing precursor may be the same precursor, e.g., TDMAT. In some embodiments, the first oxidant may be the same as the second oxidant (e.g., nitrous oxide, oxygen, carbon dioxide or combinations thereof). In some embodiments, it may be advantageous to use a different oxidant or mixture. In some embodiments, the substrate includes amorphous carbon. In some embodiments, the amorphous carbon is patterned.
In various embodiments, the method also includes after initiating the second plasma, planarizing the substrate to expose the amorphous carbon, and selectively etching the amorphous carbon to form a mask.
Another aspect involves a method of patterning a semiconductor substrate by, prior to depositing a conformal film on a core layer, depositing a nanolaminate protective layer on a patterned core layer; depositing a conformal film on the nanolaminate protective layer; planarizing the conformal film to expose the core; and selectively etching the core to form a mask.
In certain embodiments, the core layer includes amorphous carbon. In various embodiments, the nanolaminate protective layer includes silicon oxide or titanium oxide. In certain embodiments, the thickness of the nanolaminate protective layer is between about 15 Å and about 200 Å. In many embodiments, the nanolaminate protective layer is deposited using PEALD by exposing the substrate to a titanium-containing precursor or a silicon-containing precursor; exposing the substrate to an oxidant; and initiating a first plasma while the substrate is exposed to the oxidant.
In some embodiments, the nanolaminate protective layer is deposited at a temperature less than about 100° C. In various embodiments, the nanolaminate protective layer is deposited at a temperature between about 50° C. and about 150° C. and the first plasma is initiated at a HFRF power per square millimeter of substrate area between about 1.768×10−4 W per mm2 and about 1.768×10−3 W per mm2.
In some embodiments, the titanium oxide layer is deposited using PEALD by exposing the substrate to a titanium-containing precursor; exposing the substrate to an oxidant; and initiating a second plasma while the substrate is exposed to the oxidant at a HFRF power per square millimeter of substrate area of at least about 1.768×10−3 W per mm2.
Another aspect involves an apparatus for processing a semiconductor substrate including one or more process chambers; one or more gas inlets into the process chambers and associated flow-control hardware; a HFRF generator; and a controller having at least one processor and a memory, such that the at least one processer and the memory are communicatively connected with one another, the at least one processor is at least operatively connected with the flow-control hardware and HFRF generator, and the memory stores computer-executable instructions for: exposing the substrate to a metal-containing precursor; exposing the substrate to a first oxidant; initiating a first plasma while the substrate is exposed to the first oxidant with a HFRF power of between about 12.5 W and 125 W; exposing the substrate to a titanium-containing precursor; exposing the substrate to a second oxidant; and initiating a second plasma while the substrate is exposed to the second oxidant with HFRF power of at least about 125 W.
These and other aspects are described further below with reference to the drawings.
In the following description, numerous specific details are set forth to provide a thorough understanding of the presented embodiments. The disclosed embodiments may be practiced without some or all of these specific details. In other instances, well-known process operations have not been described in detail to not unnecessarily obscure the disclosed embodiments. While the disclosed embodiments will be described in conjunction with the specific embodiments, it will be understood that it is not intended to limit the disclosed embodiments.
Fabrication of semiconductor devices typically involves depositing one or more thin films in an integrated manufacturing process and may include patterning steps. Multiple patterning techniques are used to fabricate advanced integrated circuits, such as those with smaller features or higher aspect ratios, or down to 2× or 1×nm nodes. The term “1×” node means a process node between 10 nm and 19 nm and the term “2×” node means a process node between 20 nm and 29 nm. An example of multiple patterning is self-aligned double patterning, which produces double the number of features of a pattern formed by conventional lithography. As the devices become smaller, narrower half-pitch features may be attained using advanced multiple patterning techniques, such as quadruple patterning, or “quad patterning.”
An example of a quad patterning scheme is provided in
The first core layer (and thus first cores 103) may be highly etch selective to other materials in the stack, such as silicon and/or silicon-based oxides or nitrides, for example, and may be transparent. The first core layer may be a photoresist or may be made of amorphous carbon material or amorphous silicon material. In some embodiments, the first core layer may be deposited on top of hardmask 104 by a deposition technique, such as plasma-enhanced chemical vapor deposition (PECVD), and the deposition technique may involve generating a plasma in the deposition chamber from deposition gases including a hydrocarbon precursor. The hydrocarbon precursor may be defined by the formula CxHy, where x is an integer between 2 and 10, and y is an integer between 2 and 24. Examples include methane (CH4), acetylene (C2H2), ethylene (C2H4), propylene (C3H6), butane (C4H10), cyclohexane (C6H12), benzene (C6H6), and toluene (C7H8). A dual radio frequency (RF) plasma source including a high frequency (HF) power and a low frequency (LF) power may be used. Alternatively a single RF plasma source may be used. Typically such a source will be a HFRF source.
Under the first core layer formed into first cores 103 is a second core layer 105. Between the first core layer and the second core layer 105 may be a hardmask 104. The hardmask 104 may have high etch selectivity relative to first core layer and second core layer 105 so as not to etch second core layer 105 while first core layer is patterned. The second core layer 105 may be made of amorphous carbon material or amorphous silicon material. Methods of deposition and deposition precursors may be any of those described above with respect to first core layer. Once patterned, the second core layer 105 is formed into second cores (also referred to as second mandrels) 105′ (shown in
Between the second core layer 105 and target layer 150 may be other layers, such as a hardmask layer 107a, or cap layer 107b, or a mask layer 107c to be used to pattern the target layer 150. The target layer 150 may be the layer ultimately to be patterned. The target layer 150 may be a semiconductor, dielectric or other layer and may be made of silicon (Si), silicon oxide (SiO2), silicon nitride (SiN), or titanium nitride (TiN), for example. The target layer 150 may be deposited by atomic layer deposition (ALD), plasma-enhanced ALD (PEALD), chemical vapor deposition (CVD), or other suitable deposition techniques.
In one example, the compositions and thicknesses of a quad patterning stack such as the one shown in
In
The conformal film 109 may be made of dielectric material, such as SiO2. The conformal film 109 may also be an oxide, such as titanium oxide (TiO2), or may be silicon nitride (SiN). In some embodiments, the conformal film 109 is made of denser material to withstand more “passes” of patterning and may be deposited by ALD, PEALD, or conformal film deposition (CFD) methods as described briefly below.
ALD processes use surface-mediated deposition reactions to deposit films on a layer-by-layer basis. In one example ALD process, a substrate surface, including a population of surface active sites, is exposed to a gas phase distribution of a first film precursor (P1). Some molecules of P1 may form a condensed phase atop the substrate surface, including chemisorbed species and physisorbed molecules of P1. The reactor is then evacuated to remove gas phase and physisorbed P1 so that only chemisorbed species remain. A second film precursor (P2) is then introduced to the reactor so that some molecules of P2 adsorb to the substrate surface. The reactor may again be evacuated, this time to remove unbound P2. Subsequently, thermal energy provided to the substrate activates surface reactions between adsorbed molecules of P1 and P2, forming a film layer. Finally, the reactor is evacuated to remove reaction by-products and possibly unreacted P1 and P2, ending the ALD cycle. Additional ALD cycles may be included to build film thickness. In an example of a PEALD process, a plasma is initiated while the second film precursor P2 is introduced to the reactor to activate the reaction between P1 and P2.
CFD may be used to deposit the conformal film 109. Generally, CFD does not rely on complete purges of one or more reactants prior to reaction to form the film. For example, there may be one or more reactants present in the vapor phase when a plasma (or other activation energy) is struck. Accordingly, one or more of the process steps described in an ALD process may be shortened or eliminated in an example CFD process. Further, in some embodiments, plasma activation of deposition reactions may result in lower deposition temperatures than thermally-activated reactions, potentially reducing the thermal budget of an integrated process. For context, a short description of CFD is provided. The concept of a CFD cycle is relevant to the discussion of various embodiments herein. As with ALD processes, generally a cycle is the minimum set of operations required to perform a surface deposition reaction one time. The result of one cycle is production of at least a partial film layer on a substrate surface. Typically, a CFD cycle will include only those steps necessary to deliver and adsorb each reactant to the substrate surface, and then react those adsorbed reactants to form the partial layer of film. The cycle may include certain ancillary steps such as sweeping one or more of the reactants or byproducts and/or treating the partial film as deposited. Generally, a cycle contains only one instance of a unique sequence of operations. As an example, a cycle may include the following operations: (i) delivery/adsorption of reactant A, (ii) delivery/adsorption of reactant B, (iii) sweep B out of the reaction chamber, and (iv) apply plasma to drive a surface reaction of A and B to form the partial film layer on the surface. As used herein, the term PEALD includes CFD processes.
The following conditions are examples of conditions suitable depositing a silicon oxide conformal film 109 by a CFD process. Deposition may occur at a temperature between about 50° C. and about 400° C., at a pressure between about 0.5 Torr and about 10 Torr, and an RF power for four stations between about 100 W and 10 kW. RF activation frequency can vary from about 13.56 MHz to 40 MHz for various embodiments. For a silicon oxide conformal film 109, process gases that may be used include, as a silicon source, a silicon amide (e.g., BTBAS, BDEAS (bis-di-ethyl aminosilane) or DIPAS (di-isopropyl aminosilane), and, as an oxygen source, oxygen or nitrous oxide or carbon dioxide, separately or together, diluted with an inert carrier gas, for example argon or nitrogen. Process gas flow rates may be as follows: for (liquid) silicon precursor (e.g., BTBAS, BDEAS, and DIPAS), between about 1 sccm and 3 sccm, for example BTBAS at about 2.5 sccm; for oxygen precursor (O2, N2O), between about 5000 sccm and 10,000 sccm, for example N2O at 5000 sccm; and for the carrier gas (Ar or N2), between about 0 sccm and 10,000 sccm, for example about 5000 sccm Ar.
In
In
If the first core layer is made of amorphous carbon material, the first cores 103 may be stripped or etched using an ashing method. An ashing method may be dependent on chemical reactions for material removal, rather than directional movement of energetic ions. For example, any surface that is exposed to the process gas used in an ashing operation may experience material removal due to the exposure, so the amorphous carbon material used in the first cores 103 may have high etch selectivity to the spacers 109′ such that the spacers 109′ are not etched while the first cores 103 are ashed. Additionally, in contrast to some chemical etching processes, ashing operations may produce a reaction product that is completely in the gas phase. Ashing operations for carbon films may, for example, utilize dissociated hydrogen (H2) or oxygen (O2) as a process gas, which may react with carbon films to form such gas-phase reaction byproducts. In some embodiments, the remaining spacers 109′ may be shaped for subsequent processing using various etch conditions.
In
In
In
In
In
In
In
Due to the nature of forming the smaller features, the material used for the second conformal film 119 may be of higher quality relative to conformal films used in spacers of wider cores so as to maintain robustness and prevent buckling when it is exposed to harsh conditions in subsequent patterning steps. Higher quality conformal film material may have near-ideal stoichiometry, such as if the conformal film is titanium oxide, the higher quality titanium oxide conformal film may have near ideal Ti:O stoichiometry, for example 1:2, and low carbon content. Higher quality conformal films may be deposited by ALD, which may perform a complete conversion from the oxidation half-reaction, thereby forming near ideal stoichiometry. Thus, higher quality conformal film material may then have a low etch rate and high etch selectivity, and also being infinitely selective against oxides and nitrides. These films may also have higher modulus, such as greater than about 150 MPa, which contributes to improved mechanical stability of the conformal film as a spacer, thereby improving critical dimension uniformity (CDU). The higher quality conformal film material disclosed herein may also be dense to withstand subsequent integration steps.
Provided herein are methods of depositing thin, conformal nanolaminate protective layers. Also provided are methods of forming high quality films that may be used as spacers, with the methods including deposition of a nanolaminate layer. The nanolaminate layers can improve spacer robustness while protecting the underlying core layer from degradation during deposition of the conformal film.
Deposition of high quality films, such as high quality titanium oxide, directly on a core layer may result in degradation or consumption of the core due to harsh conditions during deposition of the spacer, thereby harming the underlying patterned core. For example, during deposition of the high quality conformal film, a patterned core layer may be exposed to oxygen radicals, such as those produced from a N2O/O2 sequential plasma with a high HFRF power of at least about 1000 W. Due to the higher power, more oxygen radicals are formed, which increases radical bombardment on the core layer and subsequent degradation the pattern of the core. Nitrides may be able to withstand such bombardment if used as a cap over the core layer, but since nitrides are not selective to certain core materials, nitrides are not suitable. After a conformal film is deposited, the substrate may then be planarized to expose the core and remove the core, but since the core has been consumed or degraded, the resulting width between spacers may be diminished, which results in an irregular pattern in the semiconductor substrate. Rather than using lower quality conformal films to prevent degradation of the core, the methods disclosed herein enable high quality spacer materials.
Nanolaminate protective layers may be less dense than conformal film due to the lower HFRF power used during deposition. As such nanolaminate protective layers may be deposited at a minimum thickness that adequately protects the core. Minimizing the nanolaminate protective layer may facilitate subsequent integration. Nanolaminate protective layers may protect an underlying layer to the extent that a higher quality conformal film may be deposited over it. Core consumption and degradation thereby decreases and the core can withstand harsher conditions during deposition of the high quality conformal film. In subsequent patterning steps, the high quality conformal film can withstand other harsh conditions and still maintain its strong robustness as a free-standing structure. The nanolaminate protective layers may also prevent spacer leaning and enable critical dimension variability, by maintaining the integrity of the core geometry and providing mechanical support to the free-standing spacer structures, thereby enhancing the ability to form finer features at lower half-pitch in semiconductor processing.
An example of a method of using a nanolaminate protective layer may begin by providing a multi-stack semiconductor substrate with a lithographically defined or patterned first core layer, such as the one discussed above with respect to
In
In some embodiments, the nanolaminate layer 111 may include a stack, which may have two or more sublayers (not shown). For example, the stack may be a bilayer. In some embodiments the sublayers have the same composition, and in some embodiments, the sublayers have different compositions. In some embodiments, the nanolaminate layer 111 is one layer. In one example, the nanolaminate layer 111 is one layer of silicon oxide. In another example, the nanolaminate layer 111 is one layer of titanium oxide. In one example of a bilayer nanolaminate layer 111, the upper layer is silicon oxide, and the lower layer is titanium oxide. In another example of a bilayer nanolaminate layer 111, the upper layer is titanium oxide and the lower layer is silicon oxide.
The nanolaminate layer 111 may also be less dense than the material deposited in a conformal film due to the lower HFRF power which may be used to deposit the nanolaminate layer 111. In some embodiments, the nanolaminate layer 111 may be an ALD oxide, such as silicon oxide (SiO2) or titanium oxide (TiO2) and referred to as “soft” ALD oxide. The thickness of the nanolaminate layer 111 may be taken into account when configuring processing conditions for the patterning scheme and deciding the pattern to be etched. In various embodiments, the nanolaminate layer 111 is deposited by conformal film deposition (CFD) or PEALD.
In
In
In
In
In
Examples of a titanium-containing precursor include tetrakis(dimethylamino)titanium (TDMAT), tetraethoxytitanium, tetrakis-dimethyl-amido titanium, titanium isopropoxide, titanium tetraisopropoxide, and titanium tetrachloride. A silicon-containing precursor may be, for example, a silane, a halosilane or an aminosilane. A silane contains hydrogen and/or carbon groups, but does not contain a halogen. Examples of silanes are silane (SiH4), disilane (Si2H6), and organo silanes such as methylsilane, ethylsilane, isopropylsilane, t-butylsilane, dimethylsilane, diethylsilane, di-t-butylsilane, allylsilane, sec-butylsilane, thexylsilane, isoamylsilane, t-butyldisilane, di-t-butyldisilane, tetra-ethyl-ortho-silicate (also known as tetra-ethoxy-silane or TEOS) and the like. A halosilane contains at least one halogen group and may or may not contain hydrogens and/or carbon groups. Examples of halosilanes are iodosilanes, bromosilanes, chlorosilanes and fluorosilanes. Although halosilanes, particularly fluorosilanes, may form reactive halide species that can etch silicon materials, in certain embodiments described herein, the silicon-containing reactant is not present when a plasma is struck. Specific chlorosilanes are tetrachlorosilane (SiCl4), trichlorosilane (HSiCl3), dichlorosilane (H2SiCl2), monochlorosilane (ClSiH3), chloroallylsilane, chloromethylsilane, dichloromethylsilane, chlorodimethylsilane, chloroethylsilane, t-butylchlorosilane, di-t-butylchlorosilane, chloroisopropylsilane, chloro-sec-butylsilane, t-butyldimethylchlorosilane, thexyldimethylchlorosilane, and the like. An aminosilane includes at least one nitrogen atom bonded to a silicon atom, but may also contain hydrogens, oxygens, halogens and carbons. Examples of aminosilanes are mono-, di-, tri- and tetra-aminosilane (H3Si(NH2)4, H2Si(NH2)2, HSi(NH2)3 and Si(NH2)4, respectively), as well as substituted mono-, di-, tri- and tetra-aminosilanes, for example, t-butylaminosilane, methylaminosilane, tert-butylsilanamine, bis(tertiarybutylamino)silane (SiH2(NHC(CH3)3)2 (BTBAS), tert-butyl silylcarbamate, SiH(CH3)—(N(CH3)2)2, SiHCl—(N(CH3)2)2, (Si(CH3)2NH)3 and the like. A further example of an aminosilane is trisilylamine (N(SiH3)3).
After operation 1901, the deposition chamber may be purged in a sweep phase with an injector purge or a pump away step. Generally, a sweep phase removes or purges one of the vapor phase reactant from a reaction chamber and typically occurs only after delivery of such reactant is completed. In other words, that reactant is no longer delivered to the reaction chamber during the sweep phase. However, the reactant remains adsorbed on the substrate surface during the sweep phase. Typically, the sweep serves to remove any residual vapor phase reactant in the chamber after the reactant is adsorbed on the substrate surface to the desired level. A sweep phase may also remove weakly adsorbed species (e.g., certain precursor ligands or reaction by-products) from the substrate surface. In ALD, the sweep phase has been viewed as necessary to prevent gas phase interaction of two reactants or interaction of one reactant with a thermal, plasma or other driving force for the surface reaction. In general, and unless otherwise specified herein, a sweep/purge phase may be accomplished by (i) evacuating a reaction chamber, and/or (ii) flowing gas not containing the species to be swept out through the reaction chamber. In the case of (ii), such gas may be, for example, an inert gas.
In operation 1903, the substrate may be exposed to a second precursor or an oxidant. In some embodiments, the oxidant is nitrous oxide (N2O) or oxygen (O2) or carbon dioxide (CO2) or a mixture or combinations thereof. In some embodiments, the oxidizer may be a mixture of oxygen (O2) and a weak oxidizer such as N2O, CO, CO2, NO, NO2, SO, SO2, CxHyOz and/or H2O. In other implementations, the oxidation reactant may be entirely a weak oxidizer. Alternatively, the oxidation reactant may include O3. In some embodiments, the oxidation reactant is about 0-50% O2 and about 50-100% weak oxidizer.
In some cases, one of the reactants may be delivered continuously (e.g., even during delivery of other reactants and/or during plasma exposure). For example, an oxidizing reactant may be delivered continuously. The continuously flowing reactant may be delivered to the reaction chamber in conjunction with a carrier gas such as argon. In some cases, the delivery of the continuously flowing reactants to reaction chamber is controlled by using divert valve/inlet valve toggling. Gas flow changes may be diverted or co-flowed. In one example, a continuously flowing reactant is periodically diverted from the reaction chamber such that it is only delivered to the reaction chamber at certain periods. The continuously flowing gas may be diverted to an outlet/dump using appropriate valves. For instance, an oxidizing reactant may flow continuously, but only be delivered to the reaction chamber periodically. When the oxidizing reactant is not being delivered to the reaction chamber, it may be diverted to an outlet, recycle system, etc.
In operation 1905, a plasma may be initiated with a low HFRF power while the substrate is exposed to the oxidant. In some embodiments, the low HFRF power per area of the wafer may be between about 1.768×10−4 W per mm2 and about 1.768×10−3 W per mm2 where mm2 represents the unit for surface area of the wafer. Plasma power may be scaled linearly with wafer surface area. For example, a low HFRF power may be between about 12.5 W to about 125 W per station for a 300 mm wafer, or between about 28 W and about 280 W for a 450 mm wafer. The deposition temperature may be between about 50° C. and about 150° C. After operation 1905, the deposition chamber may be purged again. These steps may be repeated until the desired thickness of the film is deposited.
In some embodiments, operation 1905 may occur at a low temperature, such as a temperature less than about 100° C. with an HFRF power while exposing a 300 mm substrate to the oxidant between about 50 W and about 500 W in a four-station tool, the power being the total power applied to the four-station tool.
In operation 1907, the substrate may be exposed to a titanium-containing precursor. Examples of titanium-containing precursors may be any of those described with respect to operation 1901. As an example, the substrate may be exposed to TDMAT for about 2 seconds, which may be described as a “dose.” After operation 1907, the deposition chamber may be purged with an injector purge or pump away step. As an example, the purge may last about 10 seconds.
In operation 1909, the substrate may be exposed to another precursor or an oxidant. In many embodiments, the oxidant is nitrous oxide (N2O) or oxygen (O2) or carbon dioxide (CO2) or a mixture thereof. As an example, operation 1909 may be about 30 seconds, such that for the first 25 seconds, no oxidant is flowed and only a carrier gas or inert gas is flowed, and an oxidant is flowed starting after the 25 seconds and is kept on through the next operation. Examples of carrier gases include argon (Ar) and nitrogen (N2). The flow rate of these carrier gases may be between about 0 sccm and about 10,000 sccm.
In operation 1911, a plasma may be initiated with high HFRF power while the substrate is exposed to the oxidant. In many embodiments, the HFRF power may be between about 125 W and about 1500 W per station for 300 mm wafers. As an example, HFRF power may be about 625 W per station. The plasma may be initiated for a time between about 0.25 seconds and about 3 seconds, or about 0.5 seconds. Operations 1907 through 1911 may occur at a temperature between about 50° C. and about 400° C., or between about 50° C. and 200° C., or about 150° C. and at a pressure between about 3 Torr and about 3.5 Torr. After operation 1911, the plasma may be turned off and the chamber may be purged or pumped to base. Example purge gases for use after operations 1901, 1903, 1905, 1907, 1909, and 1911 may be argon (Ar) or nitrogen (N2) or any other suitable purge gas. In some embodiments, the density of the film deposited in operations 1901 through 1905 may be less dense than the film deposited in operations 1907 through 1911.
According to various embodiments, operations 1901 through 1905 may be performed at a lower temperature, and/or lower RF power, and/or shorter RF time, and/or lower pressure, and/or with a weaker oxidant than operations 1907 through 1911. These deposition conditions may help prevent damage to the underlying substrate while producing an operable device.
Apparatus
Deposition techniques provided herein may be implemented in a plasma enhanced chemical vapor deposition (PECVD) reactor or a conformal film deposition (CFD) reactor. Such a reactor may take many forms, and may be part of an apparatus that includes one or more chambers or “reactors” (sometimes including multiple stations) that may each house one or more wafers and may be configured to perform various wafer processing operations. The one or more chambers may maintain the wafer in a defined position or positions (with or without motion within that position, e.g., rotation, vibration, or other agitation). In one implementation, a wafer undergoing film deposition may be transferred from one station to another within a reactor chamber during the process. In other implementations, the wafer may be transferred from chamber to chamber within the apparatus to perform different operations, such as etching operations or lithography operations. The full film deposition may occur entirely at a single station or any fraction of the total film thickness for any deposition step. While in process, each wafer may be held in place by a pedestal, wafer chuck, and/or other wafer-holding apparatus. For certain operations in which the wafer is to be heated, the apparatus may include a heater, such as a heating plate. A Vector™ (e.g., C3 Vector) or Sequel™ (e.g., C2 Sequel) reactor, produced by Lam Research Corp. of Fremont, Calif., are both examples of suitable reactors that may be used to implement the techniques described herein.
Within the reactor, a wafer pedestal 2118 may support a substrate 2116. The wafer pedestal 2118 may include a chuck, a fork, or lift pins (not shown) to hold and transfer the substrate during and between the deposition and/or plasma treatment reactions. The chuck may be an electrostatic chuck, a mechanical chuck, or various other types of chuck as are available for use in the industry and/or for research.
Various process gases may be introduced via inlet 2112. Multiple source gas lines 2110 are connected to manifold 2108. The gases may be premixed or not. Appropriate valving and mass flow control mechanisms may be employed to ensure that the correct process gases are delivered during the deposition and plasma treatment phases of the process. In the case where a chemical precursor(s) is delivered in liquid form, liquid flow control mechanisms may be employed. Such liquids may then be vaporized and mixed with process gases during transportation in a manifold heated above the vaporization point of the chemical precursor supplied in liquid form before reaching the deposition chamber.
Process gases may exit chamber 2124 via an outlet 2122. A vacuum pump, e.g., a one or two stage mechanical dry pump and/or turbomolecular pump 2140, may be used to draw process gases out of the process chamber 2124 and to maintain a suitably low pressure within the process chamber 2124 by using a closed-loop-controlled flow restriction device, such as a throttle valve or a pendulum valve.
As discussed above, the techniques for deposition discussed herein may be implemented on a multi-station or single station tool. In specific implementations, a 300 mm Lam Vector™ tool having a 4-station deposition scheme or a 200 mm Sequel™ tool having a 6-station deposition scheme may be used. In some implementations, tools for processing 450 mm wafers may be used. In various implementations, the wafers may be indexed after every deposition and/or post-deposition plasma treatment, or may be indexed after etching steps if the etching chambers or stations are also part of the same tool, or multiple depositions and treatments may be conducted at a single station before indexing the wafer.
In some embodiments, an apparatus may be provided that is configured to perform the techniques described herein. A suitable apparatus may include hardware for performing various process operations as well as a system controller 2130 having instructions for controlling process operations in accordance with the disclosed embodiments. The system controller 2130 will typically include one or more memory devices and one or more processors communicatively connected with various process control equipment, e.g., valves, RF generators, wafer handling systems, etc., and configured to execute the instructions so that the apparatus will perform a technique in accordance with the disclosed embodiments, e.g., a technique such as that provided in the deposition steps of
In some embodiments, a system controller 2130 may control all of the activities of the reactor 2100. The system controller 2130 may execute system control software stored in a mass storage device, loaded into a memory device, and executed on a processor. The system control software may include instructions for controlling the timing of gas flows, wafer movement, RF generator activation, etc., as well as instructions for controlling the mixture of gases, the chamber and/or station pressure, the chamber and/or station temperature, the wafer temperature, the target power levels, the RF power levels, the substrate pedestal, chuck, and/or susceptor position, and other parameters of a particular process performed by the reactor apparatus 2100. The system control software may be configured in any suitable way. For example, various process tool component subroutines or control objects may be written to control operation of the process tool components necessary to carry out various process tool processes. The system control software may be coded in any suitable computer readable programming language.
The system controller 2130 may typically include one or more memory devices and one or more processors configured to execute the instructions so that the apparatus will perform a technique in accordance with the present disclosure. Machine-readable media containing instructions for controlling process operations in accordance with disclosed embodiments may be coupled to the system controller 2130.
The method and apparatus described herein may be used in conjunction with lithographic patterning tools or processes such as those described below for fabrication or manufacture of semiconductor devices, displays, LEDs, photovoltaic panels, and the like. Typically, though not necessarily, such tools/processes will be used or conducted together in a common fabrication facility. Lithographic patterning of a film typically includes some or all of the following steps, each step performed with a number of possible tools: (1) application of photoresist on a workpiece, i.e., substrate or multi-layer stack as provided in disclosed embodiments, using a spin-on or spray-on tool; (2) curing a photoresist using a hot plate or furnace or UV curing tool; (3) exposing the photoresist to visible or UV or x-ray light with a tool such as a wafer stepper; (4) developing the resist so as to selectively remove resist and thereby pattern it using a tool such as a wet bench; (5) transferred the resist pattern into an underlying film or workpiece, such as an amorphous carbon layer, by using a dry or plasma-assisted etching tool such as those described below; and (6) removing the resist using a tool such as an RF or microwave plasma resist stripper. In one implementation, one or more gap features on a wafer are filled with a carbon film using a technique as described herein. The carbon film may then be used, for example, for one of the purposes described herein. Further the implementation may include one or more of steps (1) through (6) described above.
One or more process stations may be included in a multi-station processing tool.
The depicted processing chamber 2214 includes four process stations, numbered from 1 to 4 in the embodiment shown in
In some embodiments, system controller 2250 controls all of the activities of process tool 2200. System controller 2250 executes system control software 2258 stored in mass storage device 2254, loaded into memory device 2256, and executed on processor 2252. Alternatively, the control logic may be hard coded in the controller 2250. Applications Specific Integrated Circuits, Programmable Logic Devices (e.g., field-programmable gate arrays, or FPGAs) and the like may be used for these purposes. In the following discussion, wherever “software” or “code” is used, functionally comparable hard coded logic may be used in its place. System control software 2258 may include instructions for controlling the timing, mixture of gases, chamber and/or station pressure, chamber and/or station temperature, wafer temperature, target power levels, RF power levels, RF exposure time, substrate pedestal, chuck and/or susceptor position, and other parameters of a particular process performed by process tool 2200. System control software 2258 may be configured in any suitable way. For example, various process tool component subroutines or control objects may be written to control operation of the process tool components necessary to carry out various process tool processes. System control software 2258 may be coded in any suitable computer readable programming language.
In some embodiments, system control software 2258 may include input/output control (IOC) sequencing instructions for controlling the various parameters described above. For example, each phase of a CFD process may include one or more instructions for execution by system controller 2250. The instructions for setting process conditions for a CFD process phase may be included in a corresponding CFD recipe phase. In some embodiments, the CFD recipe phases may be sequentially arranged, so that all instructions for a CFD process phase are executed concurrently with that process phase.
Other computer software and/or programs stored on mass storage device 2254 and/or memory device 2256 associated with system controller 2250 may be employed in some embodiments. Examples of programs or sections of programs for this purpose include a substrate positioning program, a process gas control program, a pressure control program, a heater control program, and a plasma control program.
A substrate positioning program may include program code for process tool components that are used to load the substrate onto pedestal 2218 and to control the spacing between the substrate and other parts of process tool 2200.
A process gas control program may include code for controlling gas composition and flow rates and optionally for flowing gas into one or more process stations prior to deposition in order to stabilize the pressure in the process station. In some embodiments, the controller includes instructions for depositing a nanolaminate protective layer on a core layer, and depositing a conformal layer over the protective layer.
A pressure control program may include code for controlling the pressure in the process station by regulating, for example, a throttle valve in the exhaust system of the process station, a gas flow into the process station, etc. In some embodiments, the controller includes instructions for depositing a nanolaminate protective layer on a core layer, and depositing a conformal layer over the protective layer.
A heater control program may include code for controlling the current to a heating unit that is used to heat the substrate. Alternatively, the heater control program may control delivery of a heat transfer gas (such as helium) to the substrate. In certain implementations, the controller includes instructions for depositing a nanolaminate protective layer at a first temperature, and a conformal layer over the protective layer at a second temperature, where the second temperature is higher than the first temperature.
A plasma control program may include code for setting RF power levels and exposure times in one or more process stations in accordance with the embodiments herein. In some embodiments, the controller includes instructions for depositing a nanolaminate protective layer at a first RF power level and RF duration, and depositing a conformal layer over the protective layer at a second RF power level and RF duration. The second RF power level and/or the second RF duration may be higher/longer than the first RF power level/duration.
In some embodiments, there may be a user interface associated with system controller 2250. The user interface may include a display screen, graphical software displays of the apparatus and/or process conditions, and user input devices such as pointing devices, keyboards, touch screens, microphones, etc.
In some embodiments, parameters adjusted by system controller 2250 may relate to process conditions. Non-limiting examples include process gas composition and flow rates, temperature, pressure, plasma conditions (such as RF bias power levels and exposure times), etc. These parameters may be provided to the user in the form of a recipe, which may be entered utilizing the user interface.
Signals for monitoring the process may be provided by analog and/or digital input connections of system controller 2250 from various process tool sensors. The signals for controlling the process may be output on the analog and digital output connections of process tool 2200. Non-limiting examples of process tool sensors that may be monitored include mass flow controllers, pressure sensors (such as manometers), thermocouples, etc. Appropriately programmed feedback and control algorithms may be used with data from these sensors to maintain process conditions.
System controller 2250 may provide program instructions for implementing the above-described deposition processes. The program instructions may control a variety of process parameters, such as DC power level, RF bias power level, pressure, temperature, etc. The instructions may control the parameters to operate in-situ deposition of film stacks according to various embodiments described herein.
The system controller will typically include one or more memory devices and one or more processors configured to execute the instructions so that the apparatus will perform a method in accordance with the disclosed embodiments. Machine-readable, non-transitory media containing instructions for controlling process operations in accordance with the disclosed embodiments may be coupled to the system controller.
Experiments were conducted to compare deposited spacer or conformal films on unprotected cores and those deposited on cores protected by a nanolaminate protective layer. In the first trial, a substrate with a patterned core layer made of amorphous carbon was provided. High quality titanium oxide was deposited directly on the core layer by a plasma enhanced atomic layer deposition (PEALD) or conformal film deposition (CFD) method. The chamber pressure was about 3 Torr and at a temperature about 150° C. The substrate was exposed to the first precursor, TDMAT, for 2 seconds, followed by a 10 second purge. The substrate was then exposed to a mixture of oxidants N2O/O2 in a 30 second exposure where the first 25 seconds involved flowing only the carrier gas N2 (at a flow rate of up to 9500 sccm) and in the last five seconds, the N2O/O2 flow was turned on and stayed on until the plasma was initiated for 0.5 seconds. The plasma was initiated with a high frequency radio frequency (HFRF) power of 625 W per station, or 2500 W for four stations. The N2O/O2 flow and plasma were turned off at the same time after the 0.5 second plasma exposure, and lastly the chamber was pumped to base to purge the chamber. An image of the deposited conformal film and the underlying core layer is shown in
In the second trial, a substrate with a patterned core layer made of amorphous carbon was also provided. A silicon oxide (SiO2) nanolaminate protective layer was deposited on the core layer by PEALD. Deposition chamber temperature was 50° C. and pressure of the chamber was 1.8 Torr. The substrate was exposed to a silicon-containing precursor 0.2 seconds, followed by a 0.2 second purge. The substrate was then exposed to a mixture of oxidants N2O/O2 in a 0.3 second exposure. A plasma was initiated for the four-station chamber at 1000 W, or about 500 W per station. The N2O/O2 flow and plasma were turned off and the chamber was purged. Subsequently, the substrate was exposed to TDMAT for 2 seconds, followed by a 10 second purge. Following the purge, the substrate was exposed to oxidants N2O/O2 in a 30 second exposure such that the mixture flowed only in the last 5 seconds and after the 30 seconds, continued to flow for 0.5 seconds while plasma was initiated for the 0.5 seconds at 625 W per station, or 2500 W for four stations. After both the plasma and the oxidants N2O/O2 flow were turned off, the chamber was again purged. An image of the deposited conformal film, nanolaminate layer, and underlying core layer is shown in
In the third trial, a substrate with a patterned core layer made of amorphous carbon was also provided. A titanium oxide (TiO2) nanolaminate protective layer was deposited on the core layer by PEALD. Deposition chamber temperature was 150° C. and pressure of the chamber was 3.0 Torr. The substrate was exposed to TDMAT for 2 seconds, followed by a 10 second purge. The substrate was then exposed to a mixture of oxidants N2O/O2 in a 30 second exposure such that the mixture flowed only in the last 5 seconds and after the 30 seconds, continued to flow for 0.5 seconds while a plasma was initiated for the four-station chamber at 1000 W, or about 500 W per station. The N2O/O2 flow and plasma were turned off and the chamber was purged. Subsequently, the substrate was exposed to TDMAT for 2 seconds, followed by a 10 second purge. Following the purge, the substrate was exposed to oxidants N2O/O2 in a 30 second exposure such that the mixture flowed only in the last 5 seconds and after the 30 seconds, continued to flow for 0.5 seconds while plasma was initiated for the 0.5 seconds at 625 W per station, or 2500 W for four stations. After both the plasma and the oxidants N2O/O2 flow were turned off, the chamber was again purged. An image of the deposited conformal film, nanolaminate layer, and underlying core layer is shown in
Another series of experiments were conducted using the same conditions as those described with respect to the three trials above, but for blanket substrates with no features. In each trial, the thickness of the amorphous carbon layer was measured, then the spacer was deposited and the spacer thickness was measured, and lastly the thickness of the remaining amorphous carbon layer after spacer deposition was measured. The carbon consumption was calculated by subtracting the thickness after spacer deposition from the thickness before spacer deposition. The results of this series of experiments are shown in Table 1.
As shown in the table, presence of the nanolaminate layer reduced carbon consumption substantially. Without the nanolaminate layer, carbon consumption was 15.4 nm, whereas for both the SiO2 and TiO2 nanolaminate layers, carbon consumption was only about 8 nm. Thus, depositing a nanolaminate layer over an amorphous carbon layer, particularly patterned amorphous carbon layer, protects the amorphous carbon layer when the spacer is deposited and higher quality films may be deposited for spacer deposition as a result.
Although the foregoing embodiments have been described in some detail for purposes of clarity of understanding, it will be apparent that certain changes and modifications may be practiced within the scope of the appended claims. It should be noted that there are many alternative ways of implementing the processes, systems and apparatus of the present embodiments. Accordingly, the present embodiments are to be considered as illustrative and not restrictive, and the embodiments are not to be limited to the details given herein.
This application is a continuation-in-part of U.S. patent application Ser. No. 14/074,617, filed Nov. 7, 2013, and titled “METHODS FOR DEPOSITING FILMS ON SENSITIVE SUBSTRATES,” which is incorporated by reference herein in its entirety and for all purposes.
Number | Name | Date | Kind |
---|---|---|---|
4492620 | Matsuo et al. | Jan 1985 | A |
4500563 | Ellenberger et al. | Feb 1985 | A |
4609903 | Toyokura et al. | Sep 1986 | A |
5139825 | Gordon et al. | Aug 1992 | A |
5194398 | Miyachi et al. | Mar 1993 | A |
5223443 | Chinn et al. | Jun 1993 | A |
5496608 | Matsuda et al. | Mar 1996 | A |
5593914 | Evans, Jr. et al. | Jan 1997 | A |
5670432 | Tsai | Sep 1997 | A |
5700519 | Lam | Dec 1997 | A |
5856003 | Chiu | Jan 1999 | A |
5874368 | Laxman et al. | Feb 1999 | A |
5932286 | Beinglass et al. | Aug 1999 | A |
5961791 | Frisa et al. | Oct 1999 | A |
5962923 | Xu et al. | Oct 1999 | A |
6045666 | Satitpunwaycha et al. | Apr 2000 | A |
6054382 | Hsu et al. | Apr 2000 | A |
6090709 | Kaloyeros et al. | Jul 2000 | A |
6093966 | Venkatraman et al. | Jul 2000 | A |
6140223 | Kim et al. | Oct 2000 | A |
6191033 | Liao et al. | Feb 2001 | B1 |
6217721 | Xu et al. | Apr 2001 | B1 |
6235163 | Angelo et al. | May 2001 | B1 |
6270572 | Kim et al. | Aug 2001 | B1 |
6271591 | Dubin et al. | Aug 2001 | B1 |
6333547 | Tanaka et al. | Dec 2001 | B1 |
6337151 | Uzoh et al. | Jan 2002 | B1 |
6342448 | Lin et al. | Jan 2002 | B1 |
6346741 | Van Buskirk et al. | Feb 2002 | B1 |
6350688 | Liu et al. | Feb 2002 | B1 |
6391803 | Kim et al. | May 2002 | B1 |
6416822 | Chiang et al. | Jul 2002 | B1 |
6428859 | Chiang et al. | Aug 2002 | B1 |
6468924 | Lee et al. | Oct 2002 | B2 |
6509601 | Lee et al. | Jan 2003 | B1 |
6528430 | Kwan et al. | Mar 2003 | B2 |
6541374 | de Felipe et al. | Apr 2003 | B1 |
6551893 | Zheng et al. | Apr 2003 | B1 |
6566246 | de Felipe et al. | May 2003 | B1 |
6569783 | Uzoh et al. | May 2003 | B2 |
6576053 | Kim et al. | Jun 2003 | B1 |
6632478 | Gaillard et al. | Oct 2003 | B2 |
6645574 | Lee et al. | Nov 2003 | B1 |
6689220 | Nguyen | Feb 2004 | B1 |
6723595 | Park | Apr 2004 | B2 |
6730614 | Lim et al. | May 2004 | B1 |
6743738 | Todd | Jun 2004 | B2 |
6756318 | Nguyen et al. | Jun 2004 | B2 |
6809421 | Hayasaka et al. | Oct 2004 | B1 |
6828218 | Kim et al. | Dec 2004 | B2 |
6835417 | Saenger et al. | Dec 2004 | B2 |
6841044 | Ruzic | Jan 2005 | B1 |
6861356 | Matsuse et al. | Mar 2005 | B2 |
6884466 | Kaloyeros et al. | Apr 2005 | B2 |
6930058 | Hill et al. | Aug 2005 | B2 |
6930060 | Chou et al. | Aug 2005 | B2 |
6943092 | Kim et al. | Sep 2005 | B2 |
6962876 | Ahn et al. | Nov 2005 | B2 |
6967154 | Meng et al. | Nov 2005 | B2 |
6987240 | Jennings et al. | Jan 2006 | B2 |
6995471 | Shue et al. | Feb 2006 | B2 |
7001844 | Chakravarti et al. | Feb 2006 | B2 |
7041335 | Chung | May 2006 | B2 |
7041595 | Chopra | May 2006 | B2 |
7077904 | Cho et al. | Jul 2006 | B2 |
7081271 | Chung et al. | Jul 2006 | B2 |
7109129 | Papasouliotis | Sep 2006 | B1 |
7115528 | Vaarstra et al. | Oct 2006 | B2 |
7122222 | Xiao et al. | Oct 2006 | B2 |
7122464 | Vaartstra | Oct 2006 | B2 |
7125815 | Vaartstra | Oct 2006 | B2 |
7132353 | Xia et al. | Nov 2006 | B1 |
7141278 | Koh et al. | Nov 2006 | B2 |
7148155 | Tarafdar et al. | Dec 2006 | B1 |
7151039 | Lee et al. | Dec 2006 | B2 |
7172792 | Wang et al. | Feb 2007 | B2 |
7176084 | Lee et al. | Feb 2007 | B2 |
7205187 | Leith et al. | Apr 2007 | B2 |
7223649 | Oh et al. | May 2007 | B2 |
7241686 | Marcadal et al. | Jul 2007 | B2 |
7244668 | Kim | Jul 2007 | B2 |
7250083 | Sneh | Jul 2007 | B2 |
7259050 | Chen et al. | Aug 2007 | B2 |
7261919 | Mehregany et al. | Aug 2007 | B2 |
7294582 | Haverkort et al. | Nov 2007 | B2 |
7297641 | Todd et al. | Nov 2007 | B2 |
7300885 | Hasebe et al. | Nov 2007 | B2 |
7314835 | Ishizaka et al. | Jan 2008 | B2 |
7341959 | Brcka | Mar 2008 | B2 |
7351668 | Chou et al. | Apr 2008 | B2 |
7361538 | Luan et al. | Apr 2008 | B2 |
7361611 | Chakravarti et al. | Apr 2008 | B2 |
7390743 | Shin | Jun 2008 | B2 |
7393561 | Paranjpe | Jul 2008 | B2 |
7399388 | Moghadam et al. | Jul 2008 | B2 |
7419888 | Yang et al. | Sep 2008 | B2 |
7435454 | Brcka | Oct 2008 | B2 |
7435684 | Lang et al. | Oct 2008 | B1 |
7462571 | Hasebe et al. | Dec 2008 | B2 |
7482247 | Papasouliotis et al. | Jan 2009 | B1 |
7488694 | Kim et al. | Feb 2009 | B2 |
7507676 | Chou et al. | Mar 2009 | B2 |
7510984 | Saito et al. | Mar 2009 | B2 |
7521331 | Park et al. | Apr 2009 | B2 |
7524762 | Marcadal et al. | Apr 2009 | B2 |
7544615 | Vaartstra | Jun 2009 | B2 |
7572052 | Ravi et al. | Aug 2009 | B2 |
7592231 | Cheng et al. | Sep 2009 | B2 |
7595010 | Chakravarti et al. | Sep 2009 | B2 |
7601648 | Chua et al. | Oct 2009 | B2 |
7615438 | Ahn et al. | Nov 2009 | B2 |
7615449 | Chung et al. | Nov 2009 | B2 |
7622369 | Lee et al. | Nov 2009 | B1 |
7622383 | Kim et al. | Nov 2009 | B2 |
7629267 | Wan et al. | Dec 2009 | B2 |
7632757 | Matsuura | Dec 2009 | B2 |
7633125 | Lu et al. | Dec 2009 | B2 |
7638170 | Li | Dec 2009 | B2 |
7645484 | Ishizaka | Jan 2010 | B2 |
7651729 | Kim et al. | Jan 2010 | B2 |
7651730 | Hasebe | Jan 2010 | B2 |
7651953 | Todd et al. | Jan 2010 | B2 |
7651959 | Fukazawa et al. | Jan 2010 | B2 |
7670646 | Ahn et al. | Mar 2010 | B2 |
7682657 | Sherman | Mar 2010 | B2 |
7687409 | Ahn et al. | Mar 2010 | B2 |
7713592 | Nguyen et al. | May 2010 | B2 |
7727882 | Wu et al. | Jun 2010 | B1 |
7758920 | Hasebe et al. | Jul 2010 | B2 |
7776733 | Hasegawa | Aug 2010 | B2 |
7825039 | Takahashi et al. | Nov 2010 | B2 |
7906168 | Hasebe et al. | Mar 2011 | B2 |
7919416 | Lee et al. | Apr 2011 | B2 |
7923068 | Dickey et al. | Apr 2011 | B2 |
7923378 | Hasebe et al. | Apr 2011 | B2 |
7959985 | Ishizaka et al. | Jun 2011 | B2 |
7964241 | Hasebe et al. | Jun 2011 | B2 |
7964513 | Todd et al. | Jun 2011 | B2 |
7981473 | Kim et al. | Jul 2011 | B2 |
7989365 | Park et al. | Aug 2011 | B2 |
8034673 | Kadonaga et al. | Oct 2011 | B2 |
8080290 | Hasebe et al. | Dec 2011 | B2 |
8101531 | Li et al. | Jan 2012 | B1 |
8119424 | Mather et al. | Feb 2012 | B2 |
8119544 | Hasebe et al. | Feb 2012 | B2 |
8133797 | van Schravendijk et al. | Mar 2012 | B2 |
8178448 | Nodera et al. | May 2012 | B2 |
8227032 | Dussarrat et al. | Jul 2012 | B2 |
8257789 | Matsunaga et al. | Sep 2012 | B2 |
8278224 | Mui et al. | Oct 2012 | B1 |
8334218 | Van Nooten et al. | Dec 2012 | B2 |
8357619 | Hasebe et al. | Jan 2013 | B2 |
8366953 | Kohno et al. | Feb 2013 | B2 |
8383525 | Raisanen et al. | Feb 2013 | B2 |
8394466 | Hong et al. | Mar 2013 | B2 |
8456007 | Sandhu et al. | Jun 2013 | B2 |
8524612 | Li et al. | Sep 2013 | B2 |
8592328 | Hausmann et al. | Nov 2013 | B2 |
8637411 | Swaminathan et al. | Jan 2014 | B2 |
8647993 | Lavoie et al. | Feb 2014 | B2 |
8669185 | Onizawa et al. | Mar 2014 | B2 |
8728956 | LaVoie et al. | May 2014 | B2 |
8956983 | Swaminathan et al. | Feb 2015 | B2 |
8999859 | Swaminathan et al. | Apr 2015 | B2 |
9076646 | Sims et al. | Jul 2015 | B2 |
20010039113 | Blalock et al. | Nov 2001 | A1 |
20010054769 | Raajimakers et al. | Dec 2001 | A1 |
20020076507 | Chiang et al. | Jun 2002 | A1 |
20030008070 | Seutter et al. | Jan 2003 | A1 |
20030024477 | Okuda et al. | Feb 2003 | A1 |
20030200917 | Vaartstra | Oct 2003 | A1 |
20040033698 | Lee et al. | Feb 2004 | A1 |
20040043633 | Vaartstra | Mar 2004 | A1 |
20040053515 | Comita et al. | Mar 2004 | A1 |
20040121164 | Iacovangelo et al. | Jun 2004 | A1 |
20040219746 | Vaartstra et al. | Nov 2004 | A1 |
20040231799 | Lee et al. | Nov 2004 | A1 |
20050042865 | Cabral et al. | Feb 2005 | A1 |
20050085070 | Park | Apr 2005 | A1 |
20050109276 | Iyer et al. | May 2005 | A1 |
20050118837 | Todd et al. | Jun 2005 | A1 |
20050159017 | Kim et al. | Jul 2005 | A1 |
20050181535 | Yun et al. | Aug 2005 | A1 |
20050186793 | Omoto et al. | Aug 2005 | A1 |
20050196977 | Saito et al. | Sep 2005 | A1 |
20050233553 | Kountz et al. | Oct 2005 | A1 |
20050255700 | Gopalraja et al. | Nov 2005 | A1 |
20050260347 | Narwankar et al. | Nov 2005 | A1 |
20050276099 | Horng et al. | Dec 2005 | A1 |
20050287775 | Hasebe et al. | Dec 2005 | A1 |
20060030148 | Seutter et al. | Feb 2006 | A1 |
20060084283 | Paranjpe et al. | Apr 2006 | A1 |
20060088985 | Haverkort et al. | Apr 2006 | A1 |
20060165890 | Kaushal et al. | Jul 2006 | A1 |
20060199357 | Wan et al. | Sep 2006 | A1 |
20060228868 | Ahn et al. | Oct 2006 | A1 |
20060286774 | Singh et al. | Dec 2006 | A1 |
20060286776 | Ranish et al. | Dec 2006 | A1 |
20060286818 | Wang et al. | Dec 2006 | A1 |
20070010071 | Matsuura | Jan 2007 | A1 |
20070018214 | Ahn | Jan 2007 | A1 |
20070020922 | Chiang et al. | Jan 2007 | A1 |
20070065576 | Singh et al. | Mar 2007 | A1 |
20070134942 | Ahn et al. | Jun 2007 | A1 |
20070137572 | Matsuura et al. | Jun 2007 | A1 |
20070167028 | Chou et al. | Jul 2007 | A1 |
20070193982 | Brown et al. | Aug 2007 | A1 |
20070200243 | Kraus et al. | Aug 2007 | A1 |
20070215036 | Park et al. | Sep 2007 | A1 |
20070218701 | Shimizu et al. | Sep 2007 | A1 |
20070232082 | Balseanu et al. | Oct 2007 | A1 |
20070251444 | Gros et al. | Nov 2007 | A1 |
20070259110 | Mahajani et al. | Nov 2007 | A1 |
20080038936 | Todd et al. | Feb 2008 | A1 |
20080063791 | Hasebe et al. | Mar 2008 | A1 |
20080075881 | Won et al. | Mar 2008 | A1 |
20080087890 | Ahn et al. | Apr 2008 | A1 |
20080123394 | Lee et al. | May 2008 | A1 |
20080131601 | Kim et al. | Jun 2008 | A1 |
20080139003 | Pirzada et al. | Jun 2008 | A1 |
20080213479 | Chou et al. | Sep 2008 | A1 |
20080242116 | Clark | Oct 2008 | A1 |
20080274299 | Chen et al. | Nov 2008 | A1 |
20080274302 | Hasebe et al. | Nov 2008 | A1 |
20080299765 | Besling | Dec 2008 | A1 |
20080311760 | Nodera et al. | Dec 2008 | A1 |
20080317972 | Hendriks et al. | Dec 2008 | A1 |
20090018668 | Galbraith | Jan 2009 | A1 |
20090039349 | Honda | Feb 2009 | A1 |
20090041952 | Yoon et al. | Feb 2009 | A1 |
20090065896 | Hwang et al. | Mar 2009 | A1 |
20090075490 | Dussarrat | Mar 2009 | A1 |
20090148625 | Yeom et al. | Jun 2009 | A1 |
20090155606 | Yoon et al. | Jun 2009 | A1 |
20090163012 | Clark et al. | Jun 2009 | A1 |
20090191722 | Hasebe et al. | Jul 2009 | A1 |
20090203197 | Hanawa et al. | Aug 2009 | A1 |
20090208880 | Nemani et al. | Aug 2009 | A1 |
20090278224 | Kim et al. | Nov 2009 | A1 |
20100022099 | Van Nooten et al. | Jan 2010 | A1 |
20100025824 | Chen et al. | Feb 2010 | A1 |
20100096688 | Balseanu et al. | Apr 2010 | A1 |
20100099236 | Kwon et al. | Apr 2010 | A1 |
20100102417 | Ganguli et al. | Apr 2010 | A1 |
20100124621 | Kobayashi et al. | May 2010 | A1 |
20100136260 | Matsunaga et al. | Jun 2010 | A1 |
20100136313 | Shimizu et al. | Jun 2010 | A1 |
20100167555 | Maula et al. | Jul 2010 | A1 |
20100221925 | Lee et al. | Sep 2010 | A1 |
20100304574 | Nodera et al. | Dec 2010 | A1 |
20100310791 | Shimazu et al. | Dec 2010 | A1 |
20110003445 | Murata et al. | Jan 2011 | A1 |
20110014795 | Lee et al. | Jan 2011 | A1 |
20110014796 | Hayashi | Jan 2011 | A1 |
20110014798 | Mallick et al. | Jan 2011 | A1 |
20110064969 | Chen et al. | Mar 2011 | A1 |
20110086516 | Lee et al. | Apr 2011 | A1 |
20110120943 | Johansson et al. | May 2011 | A1 |
20110139176 | Cheung et al. | Jun 2011 | A1 |
20110143548 | Cheung et al. | Jun 2011 | A1 |
20110151142 | Seamons et al. | Jun 2011 | A1 |
20110151246 | Ramon Moreno et al. | Jun 2011 | A1 |
20110151674 | Tang et al. | Jun 2011 | A1 |
20110151678 | Ashtiani et al. | Jun 2011 | A1 |
20110159202 | Matsushita et al. | Jun 2011 | A1 |
20110198756 | Thenappan et al. | Aug 2011 | A1 |
20110201210 | Sato et al. | Aug 2011 | A1 |
20110215445 | Yang et al. | Sep 2011 | A1 |
20110256726 | LaVoie et al. | Oct 2011 | A1 |
20110256734 | Hausmann et al. | Oct 2011 | A1 |
20110298099 | Lee et al. | Dec 2011 | A1 |
20110309475 | Lee | Dec 2011 | A1 |
20120009802 | LaVoie et al. | Jan 2012 | A1 |
20120009803 | Jung et al. | Jan 2012 | A1 |
20120028454 | Swaminathan et al. | Feb 2012 | A1 |
20120028469 | Onizawa et al. | Feb 2012 | A1 |
20120058282 | Hong et al. | Mar 2012 | A1 |
20120077349 | Li et al. | Mar 2012 | A1 |
20120108079 | Mahajani | May 2012 | A1 |
20120113672 | Dubrow et al. | May 2012 | A1 |
20120164846 | Ha et al. | Jun 2012 | A1 |
20120193693 | Kanaya | Aug 2012 | A1 |
20120213940 | Mallick | Aug 2012 | A1 |
20120280200 | Tada et al. | Nov 2012 | A1 |
20120282418 | Chou et al. | Nov 2012 | A1 |
20120315394 | Ito | Dec 2012 | A1 |
20130040447 | Swaminathan et al. | Feb 2013 | A1 |
20130058161 | Yamanaka et al. | Mar 2013 | A1 |
20130058162 | Yamanaka et al. | Mar 2013 | A1 |
20130071580 | Weidman et al. | Mar 2013 | A1 |
20130115783 | Kim et al. | May 2013 | A1 |
20130189854 | Hausmann et al. | Jul 2013 | A1 |
20130196516 | Lavoie et al. | Aug 2013 | A1 |
20130309415 | Swaminathan et al. | Nov 2013 | A1 |
20130319329 | Li et al. | Dec 2013 | A1 |
20140030444 | Swaminathan et al. | Jan 2014 | A1 |
20140051262 | Lavoie et al. | Feb 2014 | A9 |
20140106574 | Kang et al. | Apr 2014 | A1 |
20140113457 | Sims et al. | Apr 2014 | A1 |
20140120737 | Swaminathan et al. | May 2014 | A1 |
20140134827 | Swaminathan et al. | May 2014 | A1 |
20140141542 | Kang et al. | May 2014 | A1 |
20140141626 | Hausmann et al. | May 2014 | A1 |
20140182619 | Goto et al. | Jul 2014 | A1 |
20140209562 | LaVoie et al. | Jul 2014 | A1 |
20140216337 | Swaminathan et al. | Aug 2014 | A1 |
20140264555 | Ahn et al. | Sep 2014 | A1 |
20140302686 | Pan et al. | Oct 2014 | A1 |
20150109814 | Chen et al. | Apr 2015 | A1 |
20150147483 | Fukazawa | May 2015 | A1 |
20150159271 | Lee et al. | Jun 2015 | A1 |
20150170900 | LaVoie | Jun 2015 | A1 |
Number | Date | Country |
---|---|---|
0 277 766 | Aug 1988 | EP |
0 541 212 | May 1993 | EP |
2 278 046 | Jan 2011 | EP |
4364320 | Aug 2009 | JP |
2010-10497 | Jan 2010 | JP |
10-2001-0111448 | Dec 2001 | KR |
10-2004-0001036 | Jan 2004 | KR |
10-2009-0057665 | Jun 2009 | KR |
10-2009-0080019 | Jul 2009 | KR |
10-2009-0081396 | Jul 2009 | KR |
WO 2006026350 | Mar 2006 | WO |
WO 2006104741 | Oct 2006 | WO |
WO 2007118026 | Oct 2007 | WO |
WO 2011130326 | Oct 2011 | WO |
WO 2011130397 | Oct 2011 | WO |
WO 2012040317 | Mar 2012 | WO |
WO 2012048094 | Apr 2012 | WO |
WO 2012087737 | Jun 2012 | WO |
WO 2013032786 | Mar 2013 | WO |
WO 2013043330 | Mar 2013 | WO |
WO 2013112727 | Aug 2013 | WO |
Entry |
---|
U.S. Appl. No. 13/963,212, filed Aug. 9, 2013, entitled “Plasma-Activated Deposition of Conformal Films”. |
U.S. Appl. No. 14/133,239, filed Dec. 18, 2013, entitled “Plasma Activated Conformal Dielectric Film Deposition”. |
U.S. Appl. No. 14/065,334, filed Oct. 28, 2013, entitled “Method for Depositing a Cholrine-Free Conformal Sin Film”. |
U.S. Appl. No. 14/074,596, filed Nov. 7, 2013, entitled “Conformal Film Deposition for Gapfill”. |
U.S. Appl. No. 14/074,617, filed Nov. 7, 2013, entitled “Methods for Depositing Filsms on Sensitive Substrates”. |
U.S. Appl. No. 14/061,587, filed Oct. 23, 2013, entitled “Sub-Saturated Atomic Layer Deposition and Conformal Film Deposition”. |
U.S. Appl. No. 14/137,860, filed Dec. 20, 2013, entitled “Gapfill of Variable Aspect Ratio Features with a Composite Peald and Pecvd Method”. |
U.S. Appl. No. 14/144,107, filed Dec. 30, 2013, entitled “Plasma Enhanced Atomic Layer Deposition with Pulsed Plasma Exposure”. |
U.S. Appl. No. 14/183,287, filed Feb. 18, 2014, entitled “High Growth Rate Process for Conformal Aluminum Nitride.” |
U.S. Appl. No. 14/187,145 , filed Feb. 21, 2014, entitled “Plasma Assisted Atomic Layer Deposition Titanium Oxide for Conformal Encapsulation and Gap Fill Applications.” |
US Office Action dated Mar. 15, 2013 issued in U.S. Appl. No. 13/084,399. |
US Final Office Action dated Sep. 13, 2013 issued in U.S. Appl. No. 13/084,399. |
US Notice of Allowance dated Jan. 15, 2014 issued in U.S. Appl. No. 13/084,399. |
US Office Action dated Sep. 14, 2012 issued in U.S. Appl. No. 13/084,305. |
US Final Office Action dated Apr. 25, 2013 issued in U.S. Appl. No. 13/084,305. |
US Office Action dated Apr. 13, 2011 issued in U.S. Appl. No. 12/889,132. |
US Notice of Allowance dated Sep. 30, 2011 issued in U.S. Appl. No. 12/889,132. |
US Office Action dated Aug. 1, 2012 issued in U.S. Appl. No. 13/011,569. |
US Final Office Action dated Feb. 26, 2013 issued in U.S. Appl. No. 13/011,569. |
US Notice of Allowance dated May 6, 2013 issued in U.S. Appl. No. 13/011,569. |
US Office Action dated Apr. 4, 2013 issued U.S. Appl. No. 13/242,084. |
US Notice of Allowance dated Jun. 19, 2013 issued U.S. Appl. No. 13/242,084. |
US Notice of Allowance dated Sep. 19, 2013 issued U.S. Appl. No. 13/242,084. |
US Office Action dated Apr. 29, 2013 issued U.S. Appl. No. 13/224,240. |
US Final Office Action dated Nov. 22, 2013 issued U.S. Appl. No. 13/224,240. |
US Office Action dated Jun. 7, 2013 issued U.S. Appl. No. 13/414,619. |
US Notice of Allowance dated Jul. 26, 2013, issued U.S. Appl. No. 13/414,619. |
US Office Action dated May 24, 2013 issued U.S. Appl. No. 13/472,282. |
US Notice of Allowance dated Oct. 4, 2013 issued U.S. Appl. No. 13/472,282. |
PCT International Search Report and Written Opinion, dated Oct. 20, 2011, issued in PCT/US2011/032186. |
PCT International Preliminary Report on Patentability, dated Oct. 26, 2012, issued in PCT/US2011/032186. |
PCT Invitation to Pay Additional Fees; Communication Re Partial International Search, dated Dec. 16, 2011, issued in PCT/US2011/032303. |
PCT International Search Report and Written Opinion, dated Feb. 20, 2012, issued in PCT/US2011/032303. |
PCT International Preliminary Report on Patentability and Written Opinion, dated Oct. 26, 2012, issued in PCT/US2011/032303. |
PCT International Search Report and Written Opinion dated May 2, 2012 issued in Application No. PCT/US2011/052537. |
PCT International Preliminary Report on Patentability and Written Opinion dated Apr. 4, 2013 issued in Application No. PCT/US2011/052537. |
PCT International Search Report and Written Opinion dated Dec. 18, 2012, issued in Application No. PCT/US2012/052769. |
PCT International Search Report and Written Opinion dated Feb. 28, 2013, issued in Application No. PCT/US2012/051740. |
Korean Notice of Provisional Rejection dated Dec. 6, 2013 issued in KR 10-2012-0043797. |
PCT International Search Report and Written Opinion dated May 27, 2013, issued in Application No. PCT/US2013/022977. |
Cecchi et al., (2007) “Ultra-thin conformal pore-sealing of low-k materials by plasma-assisted ALD,” University of New Mexico, Albuquerque, NM, Sandia National Labs, Albuquerque, NM, 1 page. |
Choi, Gyu-Jin et al., (2009) “Plasma-enhanced atomic layer deposition of TiO2 and Al-doped TiO2 films using N2O and O2 reactants,” Journal of the Electrochemical Society, 156(9):G138-G143. |
Hausmann et al. (2002) “Atomic Layer Deposition of Hafnium and Zirconium Oxides Using Metal Amide Precursors,” Chem. Mater. 14(10):4350-4358. |
King, Sean W., (Jul./Aug. 2011) “Plasma enhanced atomic layer deposition of SiNx:H and SiO2,” J. Vac. Sci. Technol. A29(4):9 pages. |
Lee et al., (2005) “Chemically conformal deposition of SrTiO3 thin films by Atomic Layer Deposition using conventional metal organic precursors and remote-plasma activated H2O,” School of Materials Science and Engineering, and Inter-university Semiconductor Research Center, Seoul National University, Microelectronic Engineering 80:158-161. |
Lee, Jong Ju, (2005) “Low-impurity, highly conformal atomic layer deposition of titanium nitride using NH3-Ar-H2 plasma treatment for capacitor electrodes,” Materials Letters, 59:615-617. |
Man P.F. et al., (Feb. 11-15, 1996) “Elimination of Post-Release Adhesion in Microstructures Using Conformal Fluorocarbon Coatings,” MEMS '96 Proceedings, IEEE, pp. 55-60. |
Nguyen, S.V. et al., (Jan./Mar. 1999) “Plasma-assist chemical vapor deposition of dielectric thin films for ULSI semiconductor circuits,” IBM J.Res.Develop. 43(1.2):5-38. |
Plasma Enhanced Atomic Layer Deposition (PEALD), Website: http://www.asm.com/index.php?option=com—content&task=view&id=19&Itemid=161 (2010), 1 page. |
PlasmaPro™, NGP® 80 Range, Next Generation Plasma Systems, Oxford Instruments (2010), 8 pages. |
van der Straten et al. (2004) “Atomic layer deposition of tantalum nitride for ultrathin liner applications in advanced copper metallization schemes,” Journal of Materials Research, 19(2):447-453. |
U.S. Appl. No. 14/194,549, filed Feb. 28, 2014, entitled “Capped ALD Films for Doping FIN-Shaped Channel Regions of 3-D IC Transistors.” |
U.S. Appl. No. 14/195,653, filed Mar. 3, 2014, entitled “RF Cycle Purging to Reduce Surface Roughness in Metal Oxide and Metal Nitride Films.” |
U.S. Appl. No. 14/464,462, filed Aug. 20, 2014, entitled “Method and Apparatus to Deposit Pure Titanium Thin Film at Low Temperature Using Titanium Tetraiodide Precursor.” |
U.S. Appl. No. 14/464,475, filed Aug. 20, 2014, entitled “Method to Tune Tiox Stoichiometry Using Atomic Layer Deposited TI Film to Minimize Contact Resistance for TIOX/TI Based MIS Contact Scheme for CMOS.” |
U.S. Appl. No. 14/335,785, filed Jul. 18, 2014, entitled “Methods for Depositing Silicon Oxide.” |
U.S. Appl. No. 14/552,011, filed Nov. 24, 2014, entitled “Selective Inhibition in Atomic Layer Deposition of Silicon-Containing Films.” |
U.S. Appl. No. 14/678,736, filed Apr. 3, 2015, entitled “Deposition of Conformal Films by Atomic Layer Deposition and Atomic Layer Etch.” |
U.S. Appl. No. 12/154,984, filed May 28, 2008, entitled “Methods and Apparatus for Depositing Titanium Based Diffusion Barrier Films.” |
U.S. Appl. No. 14/607,997, filed Jan. 28, 2015, entitled “Plasma Activated Conformal Dielectric Film Deposition”. |
US Notice of Allowance, dated Jul. 31, 2002, issued in U.S. Appl. No. 09/862,539. |
US Office Action, dated Jun. 15, 2004, issued in U.S. Appl. No. 10/289,237. |
US Notice of Allowance, dated Sep. 3, 2004, issued in U.S. Appl. No. 10/289,237. |
US Office Action, dated Sep. 2, 2009, issued in U.S. Appl. No. 12/002,780. |
US Notice of Allowance, dated Jan. 27, 2010, issued in U.S. Appl. No. 12/002,780. |
US Office Action, dated Oct. 6, 2009, issued in U.S. Appl. No. 12/154,984. |
US Final Office Action, dated Apr. 15, 2010, issued in U.S. Appl. No. 12/154,984. |
US Office Action dated Jan. 2, 2015 issued in U.S. Appl. No. 14/231,554. |
US Final Office Action dated Jun. 10, 2015 issued in U.S. Appl. No. 14/231,554. |
US Notice of Allowance dated Aug. 7, 2014 issued U.S. Appl. No. 14/133,239. |
US Notice of Allowance dated Nov. 26, 2014 issued U.S. Appl. No. 14/133,239. |
US Examiner's Answer to Appeal Brief (filed May 22, 2014) Before the Patent Trial and Appeal Board dated Aug. 14, 2014 issued U.S. Appl. No. 13/224,240. |
US Office Action dated May 21, 2014 issued in U.S. Appl. No. 13/607,386. |
US Notice of Allowance dated Oct. 8, 2014 issued in U.S. Appl. No. 13/607,386. |
US Notice of Allowance dated Nov. 19, 2014 issued in U.S. Appl. No. 13/607,386. |
US Office Action dated Jun. 13, 2014 issued in U.S. Appl. No. 13/953,616. |
US Final Office Action dated Nov. 24, 2014 issued in U.S. Appl. No. 13/953,616. |
US Office Action dated Dec. 11, 2014 issued in U.S. Appl. No. 14/074,596. |
US Office Action dated May 15, 2015 issued in U.S. Appl. No. 14/074,617. |
US Office Action dated Mar. 2, 2015 issued in U.S. Appl. No. 14/137,860. |
US Office Action dated Jul. 10, 2014 issued in U.S. Appl. No. 14/144,107. |
US Final Office Action dated Jan. 15, 2015 issued in U.S. Appl. No. 14/144,107. |
US Notice of Allowance dated Mar. 19, 2015 issued in U.S. Appl. No. 14/144,107. |
US Office Action dated Jul. 2, 2015 issued in U.S. Appl. No. 14/187,145. |
US Office Action dated Jul. 16, 2015 issued in U.S. Appl. No. 14/464,462. |
US Office Action dated Apr. 13, 2015 issued in U.S. Appl. No. 14/335,785. |
Chinese First Office Action [no translation] dated Jun. 2, 2015 issued in CN 201180045808.6. |
PCT International Preliminary Report on Patentability and Written Opinion dated Apr. 3, 2014, issued in Application No. PCT/US2012/052769. |
PCT International Preliminary Report on Patentability and Written Opinion dated Mar. 13, 2014, issued in Application No. PCT/US2012/051740. |
European Extended Search Report dated Apr. 14, 2014 issued in EP 13 15 2046. |
Korean Final Office Action dated Aug. 18, 2014 issued in KR 10-2012-0043797. |
Korean Trial Decision (English description) dated May 25, 2015 issued in KR 10-2012-0043797. |
PCT International Preliminary Report on Patentability and Written Opinion dated Aug. 7, 2014, issued in Application No. PCT/US2013/022977. |
Abe et al. (2000) “Effect of Ti insertion between Cu and TiN Layers on electromigration reliability in Cu/(Ti)/TiN/Ti layered damascene interconnects”, IEEE 00CH37059. 38th Annual International Reliability Physics Symposium, San Jose, California, pp. 333-338. |
Chen et al. (Jan./Feb. 1999) “Low Temperature Plasma-Assisted Chemical Vapor Deposition of Tantalum Nitride form Tantalum Pentabromide for Copper Metallization,” J. Vac. Sci. Technol., B 17(1):182-185. |
Cheng et al. (Mar./Apr. 1995) “Directional Deposition of Cu into Semiconductor Trench Structures Using Ionized Magnetron Sputtering,” J. Vac. Sci. Technol., B 13(2):203-208. |
Cho et al. (Dec.1998) “Remote Plasma-Assisted Metal Organic Chemical Vapor Deposition of Tantalum Nitride Thin Films with Different Radicals,” Japanese Journal of Appl. Phys., 37(Part 1)(12A):6502-6505. |
D'Couto et al. (2001) “In situ physical vapor deposition of ionized Ti and TiN thin films using hollow cathode magnetron plasma source,” J. Vac. Sci. Technol. B. 19(1):244-249. |
Elam, J.W. (2003) Surface chemistry and film growth TiN atomic layer deposition using TDMAT and NH3, Elsevier Science B.V., 436:145-156. |
Endle et al. (May/Jun. 1998) “X-Ray Photoelectron Spectroscopy Study on TiN Films Produced with Tetrakis (dimethylamido)Titanium and Selected N-Containing Precusors on SiO.sub.2,” J. Vac. Sci. Technol., A 16(3):1262-1267. |
Green et al. (Dec. 1997) “Determination of Flux Ionization Fraction Using a Quartz Crystal Microbalance and a Gridded Energy Analyzer in an Ionized Magnetron Sputtering System,” Rev. Sci. Instrum., 68(12):4555-4560. |
Han et al. (May 1998) “Barrier Metal Properties of Amorphous Tantalum Nitride Thin Films Between Platnium and Silicon Deposited Using Remote Plasma Metal Organic Chemical Vapor Method,” Jpn. J. Appl. Phys., 37 Part 1(5A):2646-2651. |
Hayden et al. (1999) “Helion Plasma Source for Ionized Physical Vapor Deposition,” 1999, Surface and Coatings Technology, pp. 120-121, pp. 401-404. |
Hayden et al. (Mar./Apr. 1998) “Characterization of Magnetron-Sputtered Partially Ionized Aluminum Deposition,” J. Vac. Sci. Technol., A 16(2):624-627. |
Kim, H., et al., (2002) “The Growth of Tantalum Thin Films by Plasma-Enhanced Atomic Layer Deposition and Diffusion Barrier Properties,” Mat. Res. Soc. Symp. Proc. 716:B8.5.1-B8.5.6. |
Klawuhn et al. (Jul./Aug. 2000) “Ionized Physical-vapor deposition Using a Hollow-Cathode Magnetron Source for Advanced Metallization,” J. Vac, Sci, Technol. A, 18(4):1546-1549. |
Ko, Myoung-Gyun, et al., “Characterization of ruthenium thin film deposited by rf-direct plasma atomic layer deposition,” 209th ECS Meeting, Abstract #50, p. 1 [Downloaded on Jun. 9, 2014]. |
Ko, Myoung-Gyun, et al., (Oct. 2008) “Correlation of Carbon Content with the Thermal Stability of Ruthenium Deposited by Using RF-Direct Plasma-Enhanced Atomic-Layer Deposition,” Journal of the Korean Physical Society, 53(4):2123-2128. |
Lee et al. (1996) “The Failure Mechanism of MOCVD TiN Diffusion Barrier at High Temperature,” Mat. Res. Soc. Symp. Proc., 324:279-284. |
Li, Xingcun et al., (2011) “Atomic Layer Deposition A1203 Thin Films in Magnetized Radio Frequency Plasma Source,” Physics Procedia 18:100-106. |
Lucovsky, Gerald et al. (1990) “Formation of Thin Films by Remote Plasma Enhanced Chemical Vapor Deposition (Remote PECVD),” in Handbook of Plasma Processing Technology, eds. Rossnagel, Cuomo and Westwood, Noyes Publications, pp. 387-408. |
Musher et al. (Feb. 1996) “Atmospheric Pressure Chemical Vapor Deposition of Titanium Nitride from Tetrakis (diethylamido) Titanium and Ammonia,” J. Electochem. Soc., 143(2):736-744. |
Peng et al. (Jul./Aug. 1998) “Structural and Electrical Properties of Chemical Vapor Deposition Tungsten Overgrowth on Physical Vapor Deposited and Metalorganic Chemical Vapor Deposited TiNAdhesion Layers,” J. Vac. Sci. Technol., B 16(4):2013-2018. |
Puurunen, Riikka L. (2005) “Surface chemistry of atomic layer deposition: A case study for the trimethylaluminum/water process,” Journal of Applied Physics, 97:121301-1-121301-52. |
Reif et al. (Feb. 1990) “Plasma Enhanced Chemical Vapor Deposition of Thin Films for Microelectronics,” Handbook of Plasma Processing Technology, eds: Rossnagel, Cuomo and Westwood, Noyes Publications, pp. 260-284. |
Schumacher Products, TDEAT (Tetrakis-diethylamino Titanium), Electronic Grade, www.schumacher.com/tdeat.html, printed Jun. 5, 2001, 1 page. |
Truong et al. (1995) “Low-Pressure Deposition of TiN Thin Films from a Tetrakis (diethylamido) Titanium Precursor,” J. Phys. Chem, 99:8831-8842. |
Tsai et al. (May 1996) “Comparison of the Diffusion Barrier Properties of Chemical-Vapor-Deposited TaN and Sputtered TaN Between Cu and Si,” J. Appl. Phys., 79(9):6932-6938. |
Ueki et al. (2004) “Effects of Ti Addition on Via Reliability in Cu Dual Damascene Interconnects,” IEEE Translations on Electron Devices, 51(11):1883-1891. |
Wu et al. (2008) “Ti-based Barrier for Cu Interconnect Applications”, International Interconnect Technology Conference paper on Jun. 1, 3 pp. |
Zhong et al. (Mar./Apr. 1999) “Ionized Titanium Deposition into High tAspect Ratio Vias and Trenches”, American Vacuum Society, J. Vac. Sci. Technol. B 17(2):405-409. |
Number | Date | Country | |
---|---|---|---|
20150126042 A1 | May 2015 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 14074617 | Nov 2013 | US |
Child | 14194324 | US |