Patent Application
20240096632
The present disclosure relates to methods and apparatuses for the manufacture of semiconductor devices. More particularly, the disclosure relates to methods and assemblies for depositing transition metal containing material on a substrate, and layers comprising a transition metal.
Semiconductor device fabrication processes generally use advanced deposition methods for forming metal and metal-containing layers. Transition metals, such as molybdenum, may have many of the advantages sought in the art. For example, they may be useful as a conductor in back end of line (BEOL) or mid end of line (MEOL) applications, or in buried power rail or in work function layer in logic applications and in word or bit line in advanced memory applications. However, the deposition of high quality transition metal thin films by cyclical deposition methods remains challenging due to the electropositive nature of transition metals, especially molybdenum, and its tendency to form nitride or carbide phases. Thus there is need in the art for alternative or improved methods for depositing materials comprising one or more transition metals with low amounts of carbon and/or nitrogen. Transition metal halides, such as transition metal iodides, may find use in various applications, ranging from patterning to BEOL metals.
Any discussion, including discussion of problems and solutions, set forth in this section has been included in this disclosure solely for the purpose of providing a context for the present disclosure. Such discussion should not be taken as an admission that any or all of the information was known at the time the invention was made or otherwise constitutes prior art.
This summary is provided to introduce a selection of concepts in a simplified form. These concepts are described in further detail in the detailed description of example embodiments of the disclosure below. This summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used to limit the scope of the claimed subject matter.
Various embodiments of the present disclosure relate to methods of depositing transition metal.
In the current disclosure, methods of depositing a material comprising transition metal and halogen on a substrate by a cyclical deposition process are disclosed. The methods comprise providing a substrate in a reactor chamber, providing a transition metal precursor into the reactor chamber in vapor phase, and providing a haloalkane precursor into the reactor chamber in vapor phase, to form a material comprising transition metal and halogen on the substrate.
Further, methods of depositing a material comprising transition metal on a substrate by a cyclic deposition process are disclosed. The methods comprise providing a substrate in a reactor chamber, providing a transition metal precursor into the reactor chamber in vapor phase at a temperature that is substantially equal or higher than the decomposition temperature of the transition metal precursor, and providing a haloalkane precursor into the reactor chamber in vapor phase, to form a material comprising transition metal on the substrate.
The current disclosure further relates to a transition metal layer produced by the method according to the current disclosure. Thus, a substrate is provided in a reactor chamber, a transition metal precursor is provided into the reactor chamber in vapor phase, and a haloalkane precursor is provided into the reactor chamber in vapor phase, to form a material comprising transition metal and halogen on the substrate. Further, transition metal halides according to the current disclosure may serve as intermediate compounds in processes to depose metallic transition metals.
In an additional aspect, the current disclosure relates to a semiconductor structure comprising transition metal deposited by a method according to the current disclosure. The transition metal comprised in the structure may be deposited as a layer. In other words, it may be a transition metal layer. As used herein, a “structure” can be or include a substrate as described herein. Structures can include one or more layers overlying the substrate, such as one or more layers formed by a method according to the current disclosure. The structure may be, for example, a via or a line in BEOL, or a contact or a local interconnect in MEOL. The structure may also be a work function layer in a gate electrode, or a buried power rail in logic applications, as well as a word line or a bit line in an advanced memory application.
In another aspect, a semiconductor device comprising transition metal or material comprising a transition metal and halogen deposited by a method according to the current disclosure. The device may be, for example, a logic or a memory device, or a gate electrode in device.
In a further aspect, a deposition assembly is disclosed. The deposition assembly is constructed and arranged to deposit a material comprising transition metal or metal and halogen on a substrate. The deposition assembly for depositing a material comprising transition metal on a substrate according to the current disclosure comprises one or more reaction chambers constructed and arranged to hold the substrate, a precursor injector system constructed and arranged to provide a transition metal precursor and a haloalkane precursor into the reaction chamber in a vapor phase. The deposition assembly further comprises a first precursor vessel constructed and arranged to contain and evaporate a transition metal precursor comprising a transition metal atom and a carbon-containing ligand, wherein the transition metal atom is bonded to the ligand through the carbon. The deposition assembly further comprises a second precursor vessel constructed and arranged to contain and evaporate a haloalkane precursor. The deposition assembly is constructed and arranged to provide the transition metal precursor and the haloalkane precursor via the precursor injector system to the reaction chamber to deposit material comprising transition metal and halogen on the substrate.
In this disclosure, any two numbers of a variable can constitute a workable range of the variable, and any ranges indicated may include or exclude the endpoints. Additionally, any values of variables indicated (regardless of whether they are indicated with “about” or not) may refer to precise values or approximate values and include equivalents, and may refer to average, median, representative, majority, or the like. Further, in this disclosure, the terms “including,” “constituted by” and “having” refer independently to “typically or broadly comprising,” “comprising,” “consisting essentially of,” or “consisting of” in some embodiments. In this disclosure, any defined meanings do not necessarily exclude ordinary and customary meanings in some embodiments.
The accompanying drawings, which are included to provide a further understanding of the disclosure and constitute a part of this specification, illustrate exemplary embodiment, and together with the description help explain the principles of the disclosure. In the drawings
It will be appreciated that elements in the figures are illustrated for simplicity and clarity and have not necessarily been drawn to scale. For example, the dimensions of some of the elements in the figures may be exaggerated relative to other elements to help improve understanding of illustrated embodiments of the present disclosure.
Although certain embodiments and examples are disclosed below, it will be understood by those in the art that the invention extends beyond the specifically disclosed embodiments and/or uses of the invention and obvious modifications and equivalents thereof. Thus, it is intended that the scope of the invention disclosed should not be limited by the particular disclosed embodiments described below.
The illustrations presented herein are not meant to be actual views of any particular material, structure, device or a deposition assembly, but are merely idealized representations that are used to describe embodiments of the disclosure.
The particular implementations shown and described are illustrative of the invention and are not intended to otherwise limit the scope of the aspects and implementations in any way. Indeed, for the sake of brevity, conventional manufacturing, connection, preparation, and other functional aspects of the assembly may not be described in detail. Furthermore, the connecting lines shown in the various figures are intended to represent exemplary functional relationships and/or physical couplings between the various elements. Many alternative or additional functional relationship or physical connections may be present in the practical assembly, and/or may be absent in some embodiments.
It is to be understood that the configurations and/or approaches described herein are exemplary in nature, and that these specific embodiments or examples are not to be considered in a limiting sense, because numerous variations are possible. The specific routines or methods described herein may represent one or more of any number of processing strategies. Thus, the various acts illustrated may be performed in the sequence illustrated, in other sequences, or omitted in some cases.
The subject matter of the present disclosure includes all novel and nonobvious combinations and subcombinations of the various processes, deposition assemblies, and configurations, and other features, functions, acts, and/or properties disclosed herein, as well as any and all equivalents thereof.
The current disclosure relates to a method of depositing a material comprising transition metal and a halogen on a substrate by a cyclic deposition process. The method comprises providing a substrate in a reactor chamber, providing a transition metal precursor in the reaction chamber in vapor phase and providing a haloalkane precursor to the reaction chamber in vapor phase to form a material comprising transition metal and halogen on the substrate.
The terms “precursor” and “reactant” can refer to molecules (compounds or molecules comprising a single element) that participate in a chemical reaction that produces another compound. A precursor typically contains portions that are at least partly incorporated into the compound or element resulting from the chemical reaction in question. Such a resulting compound or element may be deposited on a substrate. A reactant may me an element or a compound that is not incorporated into the resulting compound or element to a significant extent. The terms precursor and reactant can be used interchangeably.
As used herein, “a transition metal precursor” includes a gas or a material that can become gaseous and that can be represented by a chemical formula that includes a transition metal. In some embodiments, the transition metal precursor comprises a group IV to VI transition metal. In some embodiments, the transition metal precursor comprises a group VI transition metal. In some embodiments, the transition metal is selected from the group consisting of chromium, molybdenum, tungsten, vanadium and niobium. In some embodiments, the transition metal precursor is provided in a mixture of two or more compounds. In a mixture, the other compounds in addition to the transition metal precursor is provided in a composition. Compositions suitable for use as composition can include a transition metal compound and an effective amount of one or more stabilizing agents. Compositions may be a solution or a gas in standard conditions.
As used herein, “a haloalkane precursor” includes a gas or a material that can become gaseous and that can be represented by a chemical formula that includes a halogen and an alkane. In some embodiments, the haloalkane precursor is provided in a mixture of two or more compounds. In a mixture, the other compounds in addition to the haloalkane precursor is provided in a composition. Compositions suitable for use as composition can include a haloalkane compound and an effective amount of one or more stabilizing agents. Compositions may be a solution or a gas in standard conditions.
In the methods according to the current disclosure, the transition metal precursor comprises an organometallic compound. In some embodiments, the transition metal precursor comprises an organometallic compound comprising a transition metal that is selected from the group of transition metals having an oxidation state of 0. By an organometallic compound is herein meant a transition metal atom and a hydrocarbon ligand, wherein the transition metal atom is directly bonded to a carbon atom. In embodiments in which an organometallic compound comprises two or more metal atoms, all of the metal atoms are directly bonded with a carbon atom. In some embodiments, the transition metal is selected from the group consisting of chromium, molybdenum, tungsten, vanadium, cobalt, ruthenium, nickel, copper and niobium. In some embodiments, the transition metal is selected from the group IV-VI transition metals. In some embodiments, the transition metal is selected from the group VI transition metals.
In some embodiments, the transition metal precursor comprises a transition metal atom and at least one carbon-containing ligand, wherein the transition metal atom is bonded to the ligand through the carbon. In some embodiments, the carbon-containing ligand consists of only carbon and oxygen.
In some embodiments, transition metal precursor comprises cyclic portions. For example, the transition metal precursor may comprise one or more aryl groups. In some embodiments the transition metal precursor comprises one or more benzene rings. In some embodiments, the transition metal precursor comprises two benzene rings. One or both benzene rings may comprise hydrocarbon substituents. In some embodiments, each benzene ring of the transition metal precursor comprises an alkyl substituent. An alkyl substituent may be a methyl group, an ethyl group, or a linear or branched alkyl group comprising three, four, five or six carbon atoms. For example, the alkyl substituent of the benzene ring may be an n-propyl group or an iso-propyl group. Further, the alkyl substituent may be an n-, iso-, tert- or sec-form of a butyl, pentyl or hexyl moiety.
In some embodiments, the transition metal precursor comprises a carbonyl group-containing ligand. In some embodiments, the transition metal precursor comprises at least two carbonyl group-containing ligands. In some embodiments, the transition metal precursor comprises at least four carbonyl group-containing ligands. For example, the transition metal precursor may comprise, consist essentially of, or consist of M(CO)6, M(1,3,5-cycloheptatriene)(CO)3, wherein M is the transition metal. Additionally, in some embodiments, the transition metal precursor comprises a nitrosyl group-containing ligand. For example, the transition metal precursor may comprise, consist essentially of, or consist of MCp(CO)2(NO), wherein M is the transition metal. In some embodiments, the transition metal precursor comprises a tetrakis(dimethylamido) (TMDA) group-containing ligand. In some embodiments, the transition metal precursor comprises a phosphine group-containing ligand. In some embodiments, the transition metal precursor is selected from a group consisting of Cr(CO)6, W(CO)6 and Mo(CO)6. In some embodiments, the transition metal precursor comprises, consists essentially of or consists of Mo(CO)6.
In some embodiments, the haloalkane precursor comprises a halogenated hydrocarbon comprising two or more halogen atoms. At least two halogen atoms of the haloalkane precursor are attached to different carbon atoms. The haloalkane precursor comprises a hydrocarbon containing at least two carbon atoms attached to each other. The haloalkane precursor may comprise three carbon atoms. Further, the haloalkane precursor may comprise four, five or six carbon atoms. The haloalkane precursor may comprise a linear, branched, cyclical and/or aromatic carbon chain. For example, the haloalkane precursor may comprise a halogenated ethane, propane, 2-methylpropane, 2,2-dimethylpropane (neopentane), n-butane, 2-methylbutane, 2,2-dimethylbutane, n-pentane, 2-methylpantane, 3-methylpentane or an n-hexane.
In some embodiments the haloalkane precursor two or more halogen atoms, and at least two halogen atoms are attached to different carbon atoms. The halogen atoms may be the same halogen, for example bromine, iodine, fluorine or chlorine. Alternatively, the halogens may be different halogens, such as iodine and bromine, bromine and chlorine, chlorine and iodine. The haloalkane precursor may comprise two halogen atoms attached to different carbon atoms. The haloalkane precursor may comprise three halogen atoms, each attached to a different carbon atom. The haloalkane precursor may comprise four halogen atoms, each attached to a different carbon atom. Alternatively, in embodiments where the haloalkane precursor comprises three, four or more halogen atoms, some carbon atoms may be attached to two or three halogen atoms.
In some embodiments, the two halogen atoms in the haloalkane precursor are attached to adjacent carbon atoms of the hydrocarbon. Thus, the haloalkane precursor may comprise two adjacent carbon atoms, each having at least one halogen substituent. In some embodiments, each of the adjacent carbon atoms has only one halogen substituent. Alternatively, one or both of the carbon atoms being attached to a halogen, may have two halogen atoms attached to it. Embodiments may be envisaged in which one or both of the carbon atoms being attached to a halogen, have three halogen atoms attached to it. The location of said two carbon atoms in a carbon chain may vary. In some embodiments, they are at the end of a carbon chain, but in some embodiments, they are located away from the end of a carbon chain. As is evident to those skilled in the art, the position of a given carbon atom in a carbon chain limits the number of potential substituents available.
For example, in embodiments, where the haloalkane precursor comprises two carbon atoms, at least one halogen atom is attached to each carbon. If a two-carbon haloalkane precursor comprises two halogen atoms, then each of them is attached to a different carbon atom. In embodiments where the haloalkane precursor comprises two carbon atoms and three halogens, one of the carbon atoms is doubly substituted with a halogen. In embodiments where the haloalkane precursor comprises two carbon atoms and four halogens, both of the carbon atoms may be doubly substituted with a halogen. Alternatively, one carbon atom may have one halogen substituent, whereas the second may have three.
Similarly, in embodiments where the haloalkane precursor comprises three carbon atoms and two halogen atoms, each halogen atom is attached to a different carbon atom. Thus one carbon atom does not have a halogen atom attached to it. Two halogen atoms may be attached to neighboring carbon atoms (i.e. carbon atoms adjacent to each other in a carbon chain). Alternatively, there may be one carbon atom between the halogenated carbon atoms. For example, haloalkane precursor may comprise, consist essentially of, or consist of 1,2-dihalopropane or 1,3-dihalopropane, such as 1,2-dichloropropane, 1,3-dichloropropane, 1,2-diiodopropane or 1,3-diiodopropane, 1,2-difluoropropane or 1,3-difluoropropane.
In embodiments where the haloalkane precursor comprises three carbon atoms and three halogen atoms, each carbon atom may have a halogen atom attached to it. Alternatively, any one of the three carbon atoms may have two halogen atoms attached to it, and one carbon atom—either at the end of the carbon chain or in the middle of it—may be without a halogen. The doubly substituted carbon atom may be at the end of the carbon chain or in the middle of it. As a further alternative, in some embodiments, a three-carbon haloalkane precursor may contain four halogen atoms. In such embodiments, each carbon may have a halogen atom attached to it, and one carbon—either at the end of the carbon chain or in the middle of it—may have an additional halogen atom attached to it. As a still further alternative, two of the carbons may have two halogen atoms attached to it, whereas one carbon atom—either at the end of the carbon chain or in the middle of it—may be without a halogen. In some embodiments, the haloalkane precursor comprises 1,2-dihaloalkane or 1,2-dihaloalkene or 1,2-dihaloalkyne or 1,2-dihaloarene, where the halogens are attached to adjacent carbon atoms.
In some embodiments, a haloalkane precursor has a general formula XaRbC—(CXcR″d)n—CXaR′b, wherein X is halogen, R, R′ and R″ are independently H or an alkyl group, a and b are independently 1 or 2, so that for each carbon atom a+b=3, n is 0, 1, 2, 3, 4 or 5, and wherein c and d are independently 0, 1 or 2, so that for each carbon atom c+d=2.
In some embodiments, a haloalkane precursor has a general formula XaRbC—CXaR′b, wherein X is halogen, R and R′ are independently H or an alkyl group, a and b are independently 1, 2 or 3 so that for each carbon atom a+b=3.
In embodiments in which the haloalkane precursor comprises four carbon, there may be two, three, four, five or six halogen substituents attached to the carbons. For example, the haloalkane precursor may have a formula CH3—CXH—CH2—CXH2, CH3—CH2—CXH—CXH2, CH3—CXH—CXH—CH3 or H2CX—CH2—CH2—CXH2. In embodiments where the four-carbon halogen comprises three carbons, the haloalkane precursor may have a formula such as H2CX—CXH—CH2—CXH2, H2CX—OCH—OCH—CHs, HCX2—CXH—CH2—CH3, HCX2—CH2—OCH—CH3 or HCX2—CH2—CH2—CXH2 or CH3—CXH—CX2—CH3. In the formulas, X represents a halogen. Examples of such haloalkane precursor are 1,2-dihalobutane, 1,3-dihalobutane and 1,4-dihalobutane.
A cyclic or an aromatic haloalkane precursor may be used on some embodiments. In some embodiments, haloalkane precursor comprises a cyclic or an aromatic compound. A haloalkane precursor may comprise a di-halogenated benzene ring. The benzene ring may comprise two or more halogens. The benzene ring may contain additional substituents, such as one or more alkyl groups as described above. A haloalkane precursor may comprise, consist essentially of, or consist of a di-halogenated benzene, such as 1,2-dibromobenzene, 1,2-diiodobenzene or 1,2-dichloroobenzene. The di-halogenated benzene, may also be a 1,3-dihalogenated or a 1,4-dihalogenated benzene. Further, a tri-halogenated benzene, such as 1,2,3- or 1,2,4-halogenated benzene is possible. An aromatic haloalkane precursor may comprise four, five or six halogens. Cyclical haloalkane precursor may comprise a cyclopentane or a cyclohexane, for example. A cyclical haloalkane precursor may comprise two or more halogens. For example, a cyclohexane may contain up to twelve halogens, which may be the same or different. The halogens may be situated in cis- or trans-configuration. The halogens in a cyclohexane may be located in carbon positions 1 and 2, 1 and 3, 1 and 4, or 1,2,3 or 1,2,4. Examples of cyclic haloalkane precursors are 1,2-diiodocyclohexane, 1,3-diiodocyclohexane, 1,4-diiodocyclohexane, 1,2-dibromocyclohexane, 1,3-dibromocyclohexane, 1,4-dibromocyclohexane, 1,2-difluorocyclohexane, 1,3-difluorocyclohexane, 1,4-difluorocyclohexane
In some embodiments, the haloalkane precursor has a general formula XaRbC—CXaR′b, wherein X is halogen, R and R′ are independently H or an alkyl group, a and b are independently 1 or 2, so that for each carbon atom a+b=3. In some embodiments, X is iodine. In some embodiments, X is bromine. In some embodiments, X is chlorine. In some embodiments, a is 1 for both carbon atoms. In some embodiments a is 1 for one carbon atom, and 2 for the other carbon atom. In some embodiments, R and R′ are both H.
In some embodiments, the haloalkane precursor comprises an allyl halide. The haloalkane precursor may comprise one or more halogen atoms attached to the corresponding amount of allylic carbons in an allyl halide.
In some embodiments, the haloalkane precursor comprises a vinyl halide. The haloalkane precursor may comprise one or more halogen atoms attached to the corresponding amount of vinylic carbons in a vinyl halide.
In some embodiments, the transition metal precursor is provided to the reactor chamber at a temperature from about 150° C. to about 400° C. For example, transition metal may be deposited at a temperature from about 200° C. to about 400° C., or at a temperature from about 250° C. to about 350° C. In some embodiments of the current disclosure, transition metal may be deposited at a temperature from about 260° C. to about 330° C., or at a temperature from about 270° C. to about 330° C. In some embodiments, transition metal may be deposited at a temperature from about 150° C. to about 200° C., or at a temperature from about 300° C. to about 400° C., or at a temperature from about 280° C. to about 320° C. For example, transition metal may be deposited at a temperature of about 210° C. or about 225° C. or about 285° C., or about 290° C., or about 310° C., or about 315° C. or about 325° C., or about 375° C., or about 380° C., or about 385° C., or about 390° C.
In some embodiments, the haloalkane precursor is provided to the reactor chamber at a temperature from about 200° C. to about 400° C. For example, haloalkane precursor may be deposited at a temperature from about 250° C. to about 350° C. In some embodiments of the current disclosure, haloalkane precursor may be deposited at a temperature from about 260° C. to about 330° C., or at a temperature from about 270° C. to about 330° C. In some embodiments, haloalkane precursor may be deposited at a temperature from about 150° C. to about 200° C., or at a temperature from about 300° C. to about 400° C., or at a temperature from about 280° C. to about 320° C. For example, haloalkane precursor may be deposited at a temperature of about 210° C. or about 225° C. or about 285° C., or about 290° C., or about 310° C., or about 315° C. or about 325° C., or about 375° C., or about 380° C., or about 385° C., or about 390° C.
A pressure in a reaction chamber may be selected independently for different process steps. In some embodiments, a first pressure may be used during transition metal precursor pulse, and a second pressure may be used during haloalkane precursor pulse. A third or a further pressure may be used during purging or other process steps. In some embodiments, a pressure within the reaction chamber during the deposition process is less than 760 Torr, or wherein a pressure within the reaction chamber during the deposition process is between 0.2 Torr and 760 Torr, or between 1 Torr and 100 Torr, or between 1 Torr and 10 Torr. In some embodiments, a pressure within the reaction chamber during the deposition process is less than about 0.001 Torr, less than 0.01 Torr, less than 0.1 Torr, less than 1 Torr, less than 10 Torr, less than 50 Torr, less than 100 Torr or less than 300 Torr. In some embodiments, a pressure within the reaction chamber during at least a part of the method according to the current disclosure is less than about 0.001 Torr, less than 0.01 Torr, less than 0.1 Torr, less than 1 Torr, less than 10 Torr or less than 50 Torr, less than 100 Torr or less than 300 Torr. For example, in some embodiments, a first pressure may be about 0.1 Torr, about 0.5 Torr, about 1 Torr, about 5 Torr, about 10 Torr, about 20 Torr or about 50 Torr. In some embodiments, a second pressure is about 0.1 Torr, about 0.5 Torr, about 1 Torr, about 5 Torr, about 10 Torr, about 20 Torr or about 50 Torr.
In some embodiments, the transition metal precursor and haloalkane precursors are supplied in pulses, haloalkane precursor is supplied in pulses and the reaction chamber is purged between consecutive pulses of transition metal precursors and haloalkane precursors. The length of a transition metal precursor pulse or a haloalkane precursor pulse may be, for example, from about 0.01 s to about 60 s, for example from about 0.01 s to about 5 s, or from about 1 s to about 20 s, or from about 0.5 s to about 10 s, or from about 5 s to about 15 s, or from about 10 s to about 30 s, or from about 10 s to about 60 s, or from about 20 s to about 60 s. The length of a transition metal precursor or a haloalkane precursor pulse may be, for example 0.03 s, 0.1 s, 0.5 s, 1 s, 1.5 s, 2 s, 2.5 s, 3 s, 4 s, 5 s, 8 s, 10 s, 12 s, 15 s, 25 s, 30 s, 40 s, 50 s or 60 s. In some embodiments, transition metal precursor pulse time may be at least 5 seconds, or at least 10 seconds, or at least 20 seconds, or at least 30 seconds. In some embodiments, transition metal precursor pulse time may be at most 5 seconds, or at most 10 seconds or at most 20 seconds, or at most 30 seconds. In some embodiments, haloalkane precursor pulse time may be at least 15 seconds, or at least 30 seconds, or at least 45 seconds, or at least 60 seconds. In some embodiments, haloalkane precursor pulse time may be at most 15 seconds, or at most 30 seconds or at most 45 seconds, or at most 60 seconds.
The pulse times for transition metal precursor and haloalkane precursor vary independently according to process in question. The selection of an appropriate pulse time may depend on the substrate topology. For higher aspect ratio structures, longer pulse times may be needed to obtain sufficient surface saturation in different areas of a high aspect ratio structure. Also the selected transition metal precursor and haloalkane precursor chemistries may influence suitable pulsing times. For process optimization purposes, shorter pulse times might be preferred as long as appropriate layer properties can be achieved. In some embodiments, transition metal precursor pulse time is longer than haloalkane precursor pulse time. In some embodiments, haloalkane precursor pulse time is longer than transition metal precursor pulse time. In some embodiments, transition metal precursor pulse time is same as haloalkane precursor pulse time.
In some embodiments, transition metal precursor may be pulsed more than one time, for example two, three or four times, before a haloalkane is pulsed to the reaction chamber. Similarly, there may be more than one pulse, such as two, three or four pulses, of a haloalkane precursor before transition metal precursor is pulsed (i.e. provided) to the reaction chamber.
In some embodiments, the method comprises removing excess transition metal precursor from the reaction chamber by an inert gas prior to providing the haloalkane precursor in the reaction chamber. In some embodiments, the reaction chamber is purged between providing a transition metal precursor in a reaction chamber and providing a haloalkane precursor in the reaction chamber. In some embodiments, there is a purge step between every pulse. Thus, the reaction chamber may be purged also between two pulses of the same chemistry, such as a transition metal precursor or a haloalkane precursor.
As used herein, the term “purge” may refer to a procedure in which vapor phase precursors and/or vapor phase byproducts are removed from the substrate surface for example by evacuating the reaction chamber with a vacuum pump and/or by replacing the gas inside a reaction chamber with an inert or substantially inert gas such as argon or nitrogen. Purging may be effected between two pulses of gases which react with each other. However, purging may be effected between two pulses of gases that do not react with each other. For example, a purge, or purging may be provided between pulses of two precursors. Purging may avoid or at least reduce gas-phase interactions between the two gases reacting with each other. It shall be understood that a purge can be effected either in time or in space, or both. For example in the case of temporal purges, a purge step can be used e.g. in the temporal sequence of providing a first precursor to a reactor chamber, providing a purge gas to the reactor chamber, and providing a second precursor to the reactor chamber, wherein the substrate on which a layer is deposited does not move. For example in the case of spatial purges, a purge step can take the following form: moving a substrate from a first location to which a first precursor is continually supplied, through a purge gas curtain, to a second location to which a second precursor is continually supplied. Purging times may be, for example, from about 0.01 seconds to about 20 seconds, from about 1 s to about 20 s, or from about 0.5 s to about 10 s, or between about 1 s and about 7 seconds, such as 5 s, 6 s or 8 s. However, other purge times can be utilized if necessary, such as where highly conformal step coverage over extremely high aspect ratio structures or other structures with complex surface morphology is needed, or in specific reactor types, such as a batch reactor, may be used.
In some embodiments, the material comprising transition metal is deposited on the substrate as a layer. In such embodiments, transition metal forms a transition metal layer. As used herein, a “transition metal layer” can be a material layer that contains transition metal. As used herein, the term “layer” and/or “film” can refer to any continuous or non-continuous structure and material, such as material deposited by the methods disclosed herein. For example, layer and/or film can include two-dimensional materials, three-dimensional materials, nanoparticles or even partial or full molecular layers or partial or full atomic layers or clusters of atoms and/or molecules. A film or layer may comprise material or a layer with pinholes, which may be at least partially continuous. A seed layer may be a non-continuous layer serving to increase the rate of nucleation of another material. However, the seed layer may also be substantially or completely continuous.
In some embodiments, the material is deposited as a layer. In some embodiments the layer has a thickness of 1 nm to 30 nm, for example 1 to 20 nm, such as 1 to 10 nm.
The substrate in the current disclosure may be any underlying material or materials that can be used to form, or upon which, a structure, a device, a circuit, or a layer can be formed. A substrate can include a bulk material, such as silicon (e.g., single-crystal silicon), other Group IV materials, such as germanium, or other semiconductor materials, such as a Group II-VI or Group III-V semiconductor materials, and can include one or more layers overlying or underlying the bulk material. Further, the substrate can include various features, such as recesses, protrusions, and the like formed within or on at least a portion of a layer of the substrate. For example, a substrate can include bulk semiconductor material and an insulating or dielectric material layer overlying at least a portion of the bulk semiconductor material. Substrate may include nitrides, for example TiN, oxides, insulating materials, dielectric materials, conductive materials, metals, such as such as tungsten, ruthenium, molybdenum, cobalt, aluminum or copper, or metallic materials, crystalline materials, epitaxial, heteroepitaxial, and/or single crystal materials. In some embodiments of the current disclosure, the substrate comprises silicon. The substrate may comprise other materials, as described above, in addition to silicon. The other materials may form layers.
The method of depositing transition metal according to the current disclosure comprises providing a substrate in a reaction chamber. In other words, a substrate is brought into space where the deposition conditions can be controlled. The reaction chamber may be part of a cluster tool in which different processes are performed to form an integrated circuit. In some embodiments, the reaction chamber may be a flow-type reactor, such as a cross-flow reactor. In some embodiments, the reaction chamber may be a showerhead reactor. In some embodiments, the reaction chamber may be a space-divided reactor. In some embodiments, the reaction chamber may be single wafer ALD reactor. In some embodiments, the reaction chamber may be a high-volume manufacturing single wafer ALD reactor. In some embodiments, the reaction chamber may be a batch reactor for manufacturing multiple substrates simultaneously.
In the method according to the current disclosure, the transition metal precursor and haloalkane precursor may be in vapor phase when it is in a reaction chamber. The transition metal precursor and haloalkane precursor may be partially gaseous or liquid, or even solid at some points in time prior to being provided in the reaction chamber. In other words, a transition metal precursor and haloalkane precursor may be solid, liquid or gaseous, for example, in a precursor vessel or other receptacle before delivery in a reaction chamber. Various means of bringing the precursor in to gas phase can be applied when delivery into the reaction chamber is performed. Such means may include, for example, heaters, vaporizers, gas flow or applying lowered pressure, or any combination thereof. Thus, the method according to the current disclosure may comprise heating the transition metal precursor and haloalkane precursor prior to providing it to the reaction chamber. In some embodiments, transition metal precursor and haloalkane precursor is heated to at least 100° C., or to at least 110° C., or to at least 120° C. or to at least 130° C. or to at least 140° C. in the vessel. Also the injector system may be heated to improve the vapor phase delivery of the transition metal precursor and haloalkane precursor to the reaction chamber.
In this disclosure, “gas” can include material that is a gas at normal temperature and pressure (NTP), a vaporized solid and/or a vaporized liquid, and can be constituted by a single gas or a mixture of gases, depending on the context. Transition metal precursor and haloalkane precursor may be provided to the reaction chamber in gas phase. The term “inert gas” can refer to a gas that does not take part in a chemical reaction and/or does not become a part of a layer to an appreciable extent. Exemplary inert gases include He and Ar and any combination thereof. In some cases, molecular nitrogen and/or hydrogen can be an inert gas. A gas other than a process gas, i.e., a gas introduced without passing through a precursor injector system, other gas distribution device, or the like, can be used for, e.g., sealing the reaction space, and can include a seal gas.
In the current disclosure, the deposition process may comprise a cyclical deposition process, such as an atomic layer deposition (ALD) process or a cyclical chemical vapor deposition (CVD) process. The term “cyclical deposition process” can refer to the sequential introduction of transition metal precursors, haloalkane precursors and possible reactants into a reaction chamber to deposit material, such as transition metal, on a substrate. Cyclic deposition includes processing techniques such as atomic layer deposition (ALD), cyclical chemical vapor deposition (cyclical CVD), and hybrid cyclical deposition processes that include an ALD component and a cyclical CVD component. The process may comprise a purge step between providing precursors or between providing a transition metal precursor and a haloalkane precursor in the reaction chamber.
The process may comprise one or more cyclical phases. In some embodiments, the process comprises or one or more cyclical phases. In some embodiments, the deposition process comprises the continuous flow of at least one precursor. In some embodiments, a haloalkane precursor may be continuously provided in the reaction chamber. In such an embodiment, the process comprises a continuous flow of a haloalkane precursor.
The term “atomic layer deposition” (ALD) can refer to a vapor deposition process in which deposition cycles, such as a plurality of consecutive deposition cycles, are conducted in a reaction chamber. The term atomic layer deposition, as used herein, is also meant to include processes designated by related terms, such as chemical vapor atomic layer deposition, when performed with alternating pulses of precursor(s)/reactant(s), and optional purge gas(es). Generally, for ALD processes, during each cycle, a first precursor, such as a transition metal precursor, is introduced to a reaction chamber and is chemisorbed to a deposition surface (e.g., a substrate surface that may include a previously deposited material from a previous ALD cycle or other material), forming about a monolayer or sub-monolayer of material that does not readily react with additional precursor (i.e., a self-limiting reaction). Thereafter, in some cases, a second precursor (e.g., another precursor or a reaction gas), such as a haloalkane precursor, may subsequently be introduced into the process chamber for use in converting the chemisorbed precursor to the desired material on the deposition surface. The second precursor can be capable of further reaction with the first precursor. Purging steps may be utilized during one or more cycles, e.g., during each step of each cycle, to remove any excess first precursor, such as transition metal precursor, from the process chamber and/or remove any excess second precursor, such as haloalkane precursor, and/or reaction byproducts from the reaction chamber.
CVD-type processes may be characterized by vapor deposition which is not self-limiting. They typically involve gas phase reactions between two or more precursors and/or reactants. The precursor(s) and reactant(s) can be provided simultaneously to the reaction space or substrate, or in partially or completely separated pulses. However, CVD may be performed with a single precursor, or two or more precursors that do not react with each other. The single precursor may decompose into reactive components that are deposited on the substrate surface. The decomposition may be brought about by plasma or thermal means, for example. The substrate and/or reaction space can be heated to promote the reaction between the gaseous precursor and/or reactants. In some embodiments the precursor(s) and reactant(s) are provided until a layer having a desired thickness is deposited. In some embodiments, cyclic CVD processes can be used with multiple cycles to deposit a thin film having a desired thickness. In cyclic CVD processes, the precursors and/or reactants may be provided to the reaction chamber in pulses that do not overlap, or that partially or completely overlap.
According to an aspect, there is provided a transition metal layer produced according to the method of the current disclosure. In some embodiments, the layer is continuous or pinhole-free.
In some embodiments, the method depositing a transition metal layer further comprises providing a reactant into the reaction chamber. The reactant may decrease unwanted impurities of the deposited material. In other words, by adding a reactant the transition metal layer may have a high purity of transition metal in the layer. In some embodiments, a transition metal layer may comprise, for example, about 60 to about 99 atomic percentage (at. %) transition metal, or about 75 to about 99 at. % transition metal, or about 75 to about 95 at. % transition metal, or about 80 to about 95 at. % transition metal. A transition metal layer deposited by a method according to the current disclosure may comprise, for example about 80 at. %, about 83 at. %, about 85 at. %, about 87 at. %, about 90 at. %, about 95 at. %, about 97 at. % or about 99 at. % transition metal. In some embodiments, a transition metal layer may consist essentially of, or consist of transition metal. In some embodiments, transition metal layer may consist essentially of, or consist of transition metal. Layer consisting of transition metal may include an acceptable amount of impurities, such as oxygen, carbon, chlorine or other halogen, and/or hydrogen that may originate from one or more precursors used to deposit the transition metal layer.
In some embodiments, the reactant comprises H2 or NH3. The reactant is provided into the reactor chamber under similar pressure and temperature as the precursors listed above. The reactant may be provided into the reactor chamber either before, between or after the precursors. In some embodiments, the reactant is provided to the reaction chamber as least partially simultaneously with providing the transition metal precursor and/or the haloalkane precursor.
According to another aspect of the current disclosure, a method of depositing a material comprising transition metal on a substrate by a cyclic deposition process is disclosed. The method comprises providing a substrate in a reactor chamber, providing a transition metal precursor into the reactor chamber in vapor phase at a temperature that is substantially equal or higher than the decomposition temperature of the transition metal precursor, and providing a haloalkane precursor into the reactor chamber in vapor phase to form a material comprising transition metal on the substrate.
In some embodiments, the transition metal precursor comprises a transition metal and a carbonyl ligand. In some embodiments, the transition metal precursor comprises, consist of, or consists essentially of Mo(CO)6.
In some embodiments, the temperature of providing the transition metal precursor into the reaction chamber is between about 150° C. and about 400° C. For example, transition metal may be deposited at a temperature from about 200° C. to about 400° C., or at a temperature from about 250° C. to about 350° C. In some embodiments of the current disclosure, transition metal may be deposited at a temperature from about 260° C. to about 330° C., or at a temperature from about 270° C. to about 330° C. In some embodiments, transition metal may be deposited at a temperature from about 150° C. to about 200° C., or at a temperature from about 300° C. to about 400° C., or at a temperature from about 280° C. to about 320° C. For example, transition metal may be deposited at a temperature of about 210° C. or about 225° C. or about 285° C., or about 290° C., or about 310° C., or about 315° C. or about 325° C., or about 375° C., or about 380° C., or about 385° C., or about 390° C.
In some embodiments, the method of depositing a material on a substrate is performed in an oxygen-free environment. The oxygen-free environment prevents the material from unwanted oxidation.
According to one aspect of the current disclosure, there is provided a semiconductor structure comprising transition metal deposited according to a method of depositing a material comprising transition metal and a halogen on a substrate by a cyclic deposition process. The method comprises providing a substrate in a reactor chamber, providing a transition metal precursor in the reaction chamber in vapor phase and providing a haloalkane precursor to the reaction chamber in vapor phase to form a semiconductor structure.
According to one aspect of the current disclosure, there is provided a semiconductor device comprising transition metal deposited according to a method of depositing a material comprising transition metal and a halogen on a substrate by a cyclic deposition process. The method comprises providing a substrate in a reactor chamber, providing a transition metal precursor in the reaction chamber in vapor phase and providing a haloalkane precursor to the reaction chamber in vapor phase to form a semiconductor device.
According to another aspect of the current disclosure, there is provided a deposition assembly for depositing transition metal on a substrate. The assembly comprises one or more reaction chambers constructed and arranged to hold the substrate, a precursor injector system constructed and arranged to provide a transition metal precursor and a haloalkane precursor into the reaction chamber in a vapor phase. The deposition assembly further comprises a first precursor vessel constructed and arranged to contain and evaporate a transition metal precursor comprising a transition metal atom and a carbon-containing ligand, wherein the transition metal atom is bonded to the ligand through the carbon. The deposition assembly further comprises a second precursor vessel constructed and arranged to contain and evaporate a haloalkane precursor. The deposition assembly is constructed and arranged to provide the transition metal precursor and the haloalkane precursor via the precursor injector system to the reaction chamber to deposit material comprising transition metal and halogen on the substrate.
In some embodiments, the assembly further comprises a reactant vessel constructed and arranged to contain and evaporate a reactant comprising H2 or NH3, a reactant injector system constructed and arranged to provide the reactant into the reaction chamber in vapor phase, and the assembly is constructed and arranged to provide the reactant via the reactant injector system to the reaction chamber.
In some embodiments, the assembly further comprises a temperature controller for controlling the temperature of the reaction chamber. The temperature in the reaction chamber can be set to be between 150° C. and 400° C. as described in the above disclosure.
The process according to the disclosure was tested. According to tests transition a metal precursor, for example Mo(CO)6, and a haloalkane precursor, for example 1,2-diiodoethane, are provided into the reaction chamber at a temperature of 180° C., 190° C., 205° C., 200° C., 250° C., 300° C., 325° or 350° C. The pulse time for the transition metal precursor is 1 second or 3 seconds. The pulse time for the haloalkane precursor is 0.1 seconds, 0.5 seconds, 3 seconds or seconds. The flow rate at which the precursors are fed into the reaction chamber is 500 sccm or 800 sccm. The purge time after each precursor is 3 seconds. This cycle is repeated 500 times. The formed material layer comprises about 55 to 65% of transition metal and 17 to 27% of halogen.
According to other tests a transition metal precursor, for example Mo(CO)6, a haloalkane precursor, for example 1,2-diiodoethane, and a reactant, for example H2, are provided into the reaction chamber at a temperature of 180° C., 190° C., 205° C., 300° C., 325° C. or 350° C. The pulse time for the transition metal precursor is 1 second or 3 seconds. The pulse time for the haloalkane precursor is 0.1 seconds or 0.5 seconds. The pulse time for the reactant is 15 seconds. The flow rate at which the precursors are fed into the reaction chamber is 500 sccm. The purge time after each precursor is 3 seconds. This cycle is repeated 500 times. The formed material layer comprises over 82% transition metal in metallic form and only minimal amounts of carbon, oxygen and halogen.
The disclosure is further explained by the following exemplary embodiments depicted in the drawings. The illustrations presented herein are not meant to be actual views of any particular material, structure, or device, but are merely schematic representations to describe embodiments of the current disclosure. It will be appreciated that elements in the figures are illustrated for simplicity and clarity and have not necessarily been drawn to scale. For example, the dimensions of some of the elements in the figures may be exaggerated relative to other elements to help improve the understanding of illustrated embodiments of the present disclosure. The structures and devices depicted in the drawings may contain additional elements and details, which may be omitted for clarity.
During step 102, a substrate is provided into a reaction chamber of a reactor. The reaction chamber can form part of an atomic layer deposition (ALD) reactor. The reactor may be a single wafer reactor. Alternatively, the reactor may be a batch reactor. Various phases of method 100 can be performed within a single reaction chamber or they can be performed in multiple reactor chambers, such as reaction chambers of a cluster tool. In some embodiments, the method 100 is performed in a single reaction chamber of a cluster tool, but other, preceding or subsequent, manufacturing steps of the structure or device are performed in additional reaction chambers of the same cluster tool. Optionally, a reactor including the reaction chamber can be provided with a heater to activate the reactions by elevating the temperature of one or more of the substrate and/or the reactants and/or precursors.
During step 102, the substrate can be brought to a desired temperature and pressure for providing transition metal precursor in the reaction chamber 104 and/or for providing haloalkane precursor in the reaction chamber 106. A temperature (e.g. of a substrate or a substrate support) within a reaction chamber can be, for example, from about 150° C. to about 400° C., or from about 250° C. to about 350° C. As a further example, a temperature within a reaction chamber can be from about 275° C. to about 325° C., or from about 280° C. to about 320° C. Exemplary temperatures within the reaction chamber may be 225° C., 250° C., 275° C., 285° C., 300° C., 310° C., 320° C., and 330° C.
A pressure within the reaction chamber can be less than 760 Torr, for example 400 Torr, 100 Torr, 50 Torr or 20 Torr, 5 Torr, Torr or 0.1 Torr. Different pressure may be used for different process steps.
Transition metal precursor is provided in the reaction chamber containing the substrate 104. Without limiting the current disclosure to any specific theory, transition metal precursor may chemisorb on the substrate during providing transition metal precursor in the reaction chamber. The duration of providing transition metal precursor in the reaction chamber (transition metal precursor pulse time) may be, for example, 0.01 s, 0.5 s, 1 s, 1.5 s, 2 s, 2.5 s, 3 s, 3.5 s, 4 s, 4.5 s or 5 s. In some embodiments, the duration of providing transition metal precursor in the reaction chamber (transition metal precursor pulse time) is may be more than 5 s or more than 10 s or about 20 s.
When haloalkane precursor is provided in the reaction chamber 106, it may react with the chemisorbed transition metal precursor, or its derivate species, to form a material comprising transition metal and haloalkane. The duration of providing haloalkane precursor in the reaction chamber (haloalkane precursor pulse time) may be, for example 0.5 s, 1 s, 2 s, 3 s, 3.5 s, 4 s, 5 s, 6 s, 7 s, 8 s, 10 s, 12 s, 15 s, 30 s, 40 s, 50 s or 60 s. In some embodiments, the duration of providing haloalkane precursor in the reaction chamber is be less than 15 s or less than 10 s or about 3 s.
In some embodiments, transition metal precursor may be heated before providing it into the reaction chamber. In some embodiments, the haloalkane precursor may be heated before providing it to the reaction chamber. In some embodiments, the haloalkane precursor may kept in ambient temperature before providing it to the reaction chamber.
Steps 104 and 106, performed in any order, may form a deposition cycle, resulting in the deposition of a material comprising transition metal and halogen. In some embodiments, the two steps of the deposition, namely providing the transition metal precursor and the haloalkane precursor in the reaction chamber (104 and 106), may be repeated (loop 108). Such embodiments contain several deposition cycles. The thickness of the deposited material may be regulating by adjusting the number of deposition cycles. The deposition cycle (loop 108) may be repeated until a desired material thickness is achieved. For example about 50, 100, 150, 200, 250, 300, 400, 500, 600, 700, 800, 1,200 or 1,500 deposition cycles may be performed.
The amount of transition metal deposited during one cycle (growth per cycle) varies depending on the process conditions, and may be, for example, from about 0.3 Å/cycle to about 4.5 Å/cycle, such as from about 0.5 Å/cycle to about 3.5 Å/cycle or from about 1.2 Å/cycle to about 3.0 Å/cycle. For example, the growth rate may be about 1.0 Å/cycle, 1.2 Å/cycle, 1.4. Å/cycle, 1.6 Å/cycle, 1.8 Å/cycle, 2 Å/cycle, 2.2 Å/cycle, 2.4 Å/cycle. Depending on the deposition conditions, deposition cycle numbers etc., material of variable thickness may be deposited. For example, a material may have a thickness between approximately 0.2 nm and 60 nm, or between about 1 nm and 50 nm, or between about 0.5 nm and 25 nm, or between about 1 nm and 50 nm, or between about 10 nm and 60 nm. A material may have a thickness of, for example, approximately 0.2 nm, 0.3 nm, 0.5 nm, 1 nm, 1.5 nm, 2 nm, 2.5 nm, 3 nm, 3.5 nm, 4 nm, 4.5 nm, 5 nm, 6 nm, 8 nm, 10 nm, 15 nm, 20 nm, 25 nm, 30 nm, 35 nm, 40 nm, 50 nm, 70 nm, 85 nm or 100 nm. The desired thickness may be selected according to the application in question.
Transition metal precursor and haloalkane precursor may be provided in the reaction chamber in separate steps (104 and 106).
Purging the reaction chamber 103, 105 may prevent or mitigate gas-phase reactions between a transition metal precursor and a haloalkane precursor, and enable possible self-saturating surface reactions. Surplus chemicals and reaction byproducts, if any, may be removed from the substrate surface, such as by purging the reaction chamber or by moving the substrate, before the substrate is contacted with the next reactive chemical. In some embodiments, however, the substrate may be moved to separately contact a transition metal precursor and a haloalkane precursor. Because in some embodiments, the reactions may self-saturate, strict temperature control of the substrates and precise dosage control of the precursors may not be required. However, the substrate temperature is preferably such that an incident gas species does not condense into monolayers or multimonolayers nor thermally decompose on the surface.
When performing the method 100, a material comprising transition metal and halogen is deposited onto the substrate. The deposition process may be a cyclical deposition process, and may include cyclical CVD, ALD, or a hybrid cyclical CVD/ALD process. For example, in some embodiments, the growth rate of a particular ALD process may be low compared with a CVD process. One approach to increase the growth rate may be that of operating at a higher deposition temperature than that typically employed in an ALD process, resulting in some portion of a chemical vapor deposition process, but still taking advantage of the sequential introduction of a transition metal precursor and a haloalkane precursor. Such a process may be referred to as cyclical CVD. In some embodiments, a cyclical CVD process may comprise the introduction of two or more precursors into the reaction chamber, wherein there may be a time period of overlap between the two or more precursors in the reaction chamber resulting in both an ALD component of the deposition and a CVD component of the deposition. This is referred to as a hybrid process. In accordance with further examples, a cyclical deposition process may comprise the continuous flow of one reactant or precursor and the periodic pulsing of the other chemical component into the reaction chamber. The temperature and/or pressure within a reaction chamber during step 104 can be the same or similar to any of the pressures and temperatures noted above in connection with step 102.
In some embodiments, the transition metal precursor is brought into contact with a substrate surface 104, excess transition metal precursor is partially or substantially completely removed by an inert gas or vacuum 105, and haloalkane precursor is brought into contact with the substrate surface comprising transition metal precursor. Transition metal precursor may be brought in to contact with the substrate surface in one or more pulses 104. In other words, pulsing of the transition metal precursor 104 may be repeated. The transition metal precursor on the substrate surface may react with the haloalkane precursor to form a material comprising transition metal and halogen on the substrate surface. Also pulsing of the haloalkane precursor 106 may be repeated. In some embodiments, haloalkane precursor may be provided in the reaction chamber first 106. Thereafter, the reaction chamber may be purged 105 and transition metal precursor provided in the reaction chamber in one or more pulses 104.
For example, if a material comprising transition metal and halogen is deposited at a temperature of between 270 to 310° C., and the deposition cycle (providing transition metal precursor and haloalkane precursor, separated by purging) is repeated between 100 and 200 times, it may be possible to obtain a material with a thickness between approximately 10 nm and 40 nm, for example 20 nm or 30 nm.
The properties of a material may be modified by using a post-deposition anneal. For example, the material comprising transition metal and halogen can be converted into metallic transition metal by an annealing process. Annealing may be performed directly after depositing of a material, i.e. without additional layers being deposited. Alternatively, annealing may be performed after additional layers have been deposited. Material may be capped before annealing. A capping layer may comprise, consist essentially of, or consist of silicon nitride. An annealing temperature from about 320° C. to about 470° C. could be used. For example, an annealing temperature may be 330° C., 350° C., 380° C., 400° C., 430° C. or 450° C. Annealing may be performed in a gas atmosphere comprising, consist essentially of, or consist of argon, argon-hydrogen mixture, hydrogen, nitrogen or nitrogen-hydrogen mixture. Duration of annealing may be from about 1 minute to about 60 minutes, for example 5 minutes, 20 minutes, 30 minutes or 45 minutes. An annealing may be performed at a pressure of 0.05 to 760 Torr. For example, a pressure during annealing may be about 1 Torr, about 10 Torr, about 100 Torr or about 500 Torr.
Step 109 can be performed either simultaneously with steps 104 and/or 106 or before or after steps 104 and/or 106. In some embodiments, the three steps of the deposition, namely providing the transition metal precursor, the haloalkane precursor and the reactant into the reaction chamber (104, 106 and 109), may be repeated (loop 108). Such embodiments contain several deposition cycles. The thickness of the deposited material may be regulating by adjusting the number of deposition cycles. The deposition cycle (loop 108) may be repeated until a desired material thickness is achieved. For example about 50, 100, 150, 200, 250, 300, 400, 500, 600, 700, 800, 1,200 or 1,500 deposition cycles may be performed.
The amount of reactant deposited during one cycle (growth per cycle) varies depending on the process conditions, and may be, for example, from about 0.3 Å/cycle to about 4.5 Å/cycle, such as from about 0.5 Å/cycle to about 3.5 Å/cycle or from about 1.2 Å/cycle to about 3.0 Å/cycle. For example, the growth rate may be about 1.0 Å/cycle, 1.2 Å/cycle, 1.4. Å/cycle, 1.6 Å/cycle, 1.8 Å/cycle, 2 Å/cycle, 2.2 Å/cycle, 2.4 Å/cycle. Depending on the deposition conditions, deposition cycle numbers etc., material of variable thickness may be deposited.
Material layer comprising a transition metal and a haloalkane 204 can be formed according to a method described herein. In embodiments, in which an underlayer 206 is formed, the underlayer may be formed using a cyclical deposition process. In some embodiments, a material layer comprising a transition metal and a haloalkane may be deposited directly on the substrate. In such embodiments, there is no underlayer. As a further alternative, the structure or a device according to the current disclosure may comprise additional layers between substrate and material layer comprising a transition metal and a haloalkane.
In the illustrated example, deposition assembly 300 includes one or more reaction chambers 302, a precursor injector system 301, a transition metal precursor vessel 304, haloalkane precursor vessel 306, a purge gas source 308, an exhaust source 310, and a controller 312.
Reaction chamber 302 can include any suitable reaction chamber, such as an ALD or CVD reaction chamber.
The transition metal precursor vessel 304 can include a vessel and one or more transition metal precursors as described herein—alone or mixed with one or more carrier (e.g., inert) gases. Haloalkane precursor vessel 306 can include a vessel and one or more reactants as described herein—alone or mixed with one or more carrier gases. Purge gas source 308 can include one or more inert gases as described herein. Although illustrated with three source vessels 304-308, deposition assembly 300 can include any suitable number of source vessels. Source vessels 304-308 can be coupled to reaction chamber 302 via lines 314-318, which can each include flow controllers, valves, heaters, and the like. In some embodiments, the transition metal precursor in the transition metal precursor vessel may be heated. In some embodiments, the vessel is heated so that the transition metal precursor reaches a temperature between about 60° C. and about 160° C., such as between about 100° C. and about 145° C., for example 85° C., 100° C., 110° C., 120° C., 130° C. or 140° C.
Exhaust source 310 can include one or more vacuum pumps.
Controller 312 includes electronic circuitry and software to selectively operate valves, manifolds, heaters, pumps and other components included in the deposition assembly 300. Such circuitry and components operate to introduce precursors and purge gases from the respective sources 304-308. Controller 312 can control timing of gas pulse sequences, temperature of the substrate and/or reaction chamber 302, pressure within the reaction chamber 302, and various other operations to provide proper operation of the deposition assembly 300. Controller 312 can include control software to electrically or pneumatically control valves to control flow of precursors and purge gases into and out of the reaction chamber 302. Controller 312 can include modules such as a software or hardware component, which performs certain tasks. A module may be configured to reside on the addressable storage medium of the control system and be configured to execute one or more processes.
Other configurations of deposition assembly 300 are possible, including different numbers and kinds of precursor and reactant sources and purge gas sources. Further, it will be appreciated that there are many arrangements of valves, conduits, precursor sources, and purge gas sources that may be used to accomplish the goal of selectively and in coordinated manner feeding gases into reaction chamber 302. Further, as a schematic representation of a deposition assembly, many components have been omitted for simplicity of illustration, and such components may include, for example, various valves, manifolds, purifiers, heaters, containers, vents, and/or bypasses.
During operation of deposition assembly 300, substrates, such as semiconductor wafers (not illustrated), are transferred from, e.g., a substrate handling system to reaction chamber 302. Once substrate(s) are transferred to reaction chamber 302, one or more gases from gas sources 304-308, such as precursors, reactants, carrier gases, and/or purge gases, are introduced into reaction chamber 302.
This application claims priority to and the benefit of U.S. Provisional Application No. 63/407,193, filed Sep. 16, 2022, the entirety of which is incorporated by reference herein.
| Number | Date | Country | |
|---|---|---|---|
| 63407193 | Sep 2022 | US |
