The present disclosure relates to microchannel plates and, in particular, to a process of atomic layer deposition using functionalized substrates to provide improved secondary electron emission materials.
An electron amplifier structure or an electron multiplier may be used as a component in a detector system to detect low levels of electrons, ions, or photons, and provide an amplified response via a plurality of secondary electron emissions. Conventional electron amplifier structures, such as channeltrons (single channel tubes) and microchannel plates (“MCPs,” 2D arrays of micro channels), are generally fabricated using various types of glass such as lead glass. During fabrication, these electron amplifier structures are created via a hydrogen annealing treatment referred to as “hydrogen firing” that causes the formation of reduced lead oxide (PbOx) on the exposed surfaces of the channels and imparts electrical conductivity and secondary electron emissive properties.
Secondary electron emissive properties can also be imparted to MCPs using thin film coatings. Previously, thin film coatings of Al2O3 and MgO have been prepared on the exposed surfaces of MCP channels using a variety of thin film deposition techniques including atomic layer deposition.
It is desirable for a MCP being used as an electron multiplier to have a high, stable gain. MCPs with these properties are useful in a wide range of applications, including night vision, large area photodetectors, neutron sensing devices, and medical imaging. This gain is, at least in part, dictated by certain properties and features of the MCP. For example, secondary electron yield (“SEY”) of the surfaces inside the MCP channels have a significant impact in dictating the gain. MgO SEY layers prepared by atomic layer deposition have a large SEY value of ˜7.
The SEY itself is greatly impacted by factors such as the adsorption of molecules from the ambient environment, such as water or carbon dioxide. This is particularly impactful where the MCP may be exposed to extended processing, such as exposure outside of a high vacuum environment. MgO SEY coatings are particularly susceptible to ambient exposure. The MgO can form hydroxides and carbonates upon exposure to water and carbon dioxide. These hydroxides and carbonates have a lower SEY value compared to MgO and this reduces the MCP gain. Further, the SEY can be impacted by thermal annealing of the MCP. Such thermal annealing can result in solid state diffusion of elements. This results in a critical limitation on the processing options for a wide range of MCPs where thermal annealing is required to achieve stable operation. In addition, certain classes of MCPs may exhibit undesirable properties due to the presence of contaminants on or in the inner surface of the MCPs. Thus, there is a need for a process to produce MCPs with a stable structure to provide for a desired SEY without the deleterious impact of contaminants.
At least one embodiment relates to a method of forming a secondary electron emissive (“SEE”) coating. A substrate is provided within an atomic layer deposition (“ALD”) reactor. A coating of CaF2 is deposited by atomic layer deposition process including at least one cycle of: pulsing a first metal precursor comprising an alkaline metal amidinate into the reactor for a first metal precursor pulse time; purging the reactor of the first metal precursor; pulsing a second precursor comprising a fluorinated compound into the reactor for a second precursor pulse time; and purging the reactor of the co-reactant precursor. The depositing occurs at a reaction temperature greater than a highest sublimation temperature of the first metal precursor and the fluorinated compound and less than 50° C. below the smallest thermal decomposition temperature of the first metal precursor and the fluorinated compound.
Another embodiment relates to a method of forming an electron amplifier. An electron amplifier substrate having an emissive layer and a resistive layer is provided within an ALD reactor. A coating of CaF2 is deposited by atomic layer deposition process including at least one cycle of: pulsing a first metal precursor comprising [Ca(amd)2]2 into the reactor for a first metal precursor pulse time; purging the reactor of the first metal precursor; pulsing a second precursor selected from the group consisting of hydrogen fluoride (“HF”), HF-pyridine (“HF-Py”), WF6, TaF5, MoF6, and NbF5 into the reactor for a second precursor pulse time; and purging the reactor of the second precursor.
Another embodiment relates to an electron detector device comprising a microchannel plate having a plurality of channels extending there through. A resistive coating is deposited on the microchannel plate. The device further includes an emissive layer deposited on the resistive layer; the emissive layer comprising CaF2.
This summary is illustrative only and is not intended to be in any way limiting. Other aspects, inventive features, and advantages of the devices or processes described herein will become apparent in the detailed description set forth herein, taken in conjunction with the accompanying figures, wherein like reference numerals refer to like elements.
Before turning to the figures, which illustrate certain exemplary embodiments in detail, it should be understood that the present disclosure is not limited to the details or methodology set forth in the description or illustrated in the figures. It should also be understood that the terminology used herein is for the purpose of description only and should not be regarded as limiting.
Microchannel plates may be manufactured by a range of processes. In one approach, a conformal deposition technique is utilized to deposit a material on a substrate. Various deposition techniques have been used, including molecular-beam epitaxy (“MBE”), electron beam evaporation (“EBE”), physical vapor deposition (“PVD”), thermal evaporation, pulsed laser deposition (“PLD”), and chemical vapor deposition (“CVD”). Recently, ALD has been utilized for MCP materials. ALD typically utilizes temperatures above room temperature, often above 200° C., although recent research has shown sub−200° C. ALD deposition for MCPs.
MCPs may have a structure of a porous substrate coated with a secondary emission coating. As shown in
As previously noted, several commonly used structures for SEE materials exhibit undesirable characteristics, notably changes in the emissive layer through exposure to environmental materials such as reaction with water or carbon dioxide vapors or by migration of elements from the resistive layer, such as fluorine.
Mitigation of the issued noted with MgO as a SEE component can accomplished through several embodiments. In some embodiments a coating that is resistant to fluorine migration may be used as a barrier layer, for example the barrier layer may be an emissive layer and/or an interlayer. Further, the barrier layer may form an interlayer that is a part of an electron amplifier positioned between an emissive layer and a resistive layer. In one embodiment, an Al2O3 interlayer is formed between a fluorine containing resistive layer, such as W:AlOF, and MgO as the emissive layer. In another embodiment, a CaF2 interlayer is formed between a fluorine containing resistive layer, such as W:AlOF, and MgO as the emissive layer. In one embodiment, a SEE material includes a MgOxFy oxyfluoride SEE layer. In another embodiment, a SEE material includes a MgO/TiO2 mixed oxide SEE layer.
In some embodiments, ALD is utilized. In its simplest form, ALD is a sequence of two half-reactions or half-cycles, where, in a first half-cycle, a first precursor is pulsed or dosed such that it binds to the surface of the material to be coated (adsorption), the first precursor is purged, and then, in a second half-cycle, a second precursor (or co-reactant) is pulsed or dosed to react with the adsorbed/bound intermediate entity formed by the first precursor. The reaction of the second precursor with the first adsorbed entity forms a deposited material.
It should be appreciated that more complicated ALD schemes can be constructed as a super-cycle comprising various sub-cycles for depositing a material as described or for depositing multiple different materials for multiple dopants or formation of bi- (tri-, etc.) metallic materials, such as varying the parameters for any of the individual steps within a cycle. In one embodiment, the deposition may be a doped layer, a multi-layer, or a mixed metal composite. The respective pulse and purge times may be the same time or may be different for the different metal precursors and co-reactants.
In one embodiment, an Al2O3 barrier layer, such as an interlayer, is formed between W:AlOF and MgO layers. The Al2O3 layer may be deposited by ALD.
In one embodiment, the W:AlOF layer(s) is deposited by ALD using a ratio of 1 W ALD cycle to 8 Al2O3 ALD cycles and may comprising up to 500 total ALD cycles. The W:Al2O3 ratio may be from 1:1 to 1:50 and the total ALD cycles may be from 2 to 5000. MgO may be formed as a single layer or comprise 100 layers. The ratio of W:AlOF to MgO may be from 5:1 to 5000:1. The Al2O3 layer formed there between may be in a ratio of 1:2 to 1:5000 to W:AlOF and 1:1 to 500:1 to MgO. The Al2O3 may comprise a single layer or up to 500 layers. The W:AlOF ALD precursors may be tungsten hexafluoride (WF6) and disilane (Si2H6) for the conducting component and trimethyl aluminum (“TMA”) and H2O for the insulating component. In some embodiments the Si2H6 may be replaced with TMA. In other embodiments, the WF6 is replaced with molybdenum hexafluoride (MoF6) to create a Mo:AlOF resistive layer. The ALD temperature may be in the range of 20-350° C. and preferably 200° C. The pulse times may be in the range of 0.01-30 s and preferably is. The purge times may be in the range of 1-200 s and preferably 5 s. It should be appreciated that the precursor dose and purge time is based on the self-limiting behavior of the precursors. This can be varied in wide range from a few milliseconds to 100 s of seconds. Further if a longer dose time is utilized, the purge times may need to increase to avoid a CVD type reaction, which can result in non-uniformity and particle formation.
In one embodiment, a CaF2 barrier layer, such as an interlayer, is formed between resistive layers, such as W:AlOF, and emissive layers, such as MgO layers. The CaF2 layer may be deposited by ALD.
The CaF2 ALD process includes a first metal precursor. In one embodiment, the first metal precursor comprises an amidinate, such as calcium amidinate ([Ca(amd)2]2). The ALD process further includes a second precursor. The second precursor is reactive with the intermediate entity formed by the first metal precursor. The second precursor may be a fluorinated precursor. In some embodiments, the second precursor is selected from the group consisting of HF, HF-pyridine, WF6, TaF5, MoF6, and NbF5
In one embodiment, each ALD process consists of a cycle, which may be repeated to form a supercycle, with a first metal precursor vapor pulse, such as calcium amidinate ([Ca(amd)2]2) (e.g., for 3 seconds), for a first precursor exposure (e.g., for 3 seconds); followed by a first metal precursor purge (e.g., for 15 seconds), such as where the reactor is pumped to a vacuum; followed by a second precursor pulse, such as hydrogen fluoride (e.g., for 1 second), with a second precursor exposure (e.g., for 1 second); followed by a second precursor purge (e.g., for 10 seconds). It should be appreciated that the precursor dose and purge times are based on the self-limiting behavior of the precursors. This can be varied in wide range from a few milliseconds to tens of seconds. Further, if a longer dose time is utilized, the purge times may need to increase to avoid a CVD type reaction, which can result in non-uniformity and particle formation.
It should be appreciated that more complicated ALD schemes can be constructed as a super-cycle comprising various sub-cycles for depositing a material as described or for depositing multiple different materials for multiple dopants or formation of bi- (tri-, etc.) metallic materials, such as varying the parameters for any of the individual steps within a cycle. In one embodiment, the deposition may be a doped layer or a mixed metal composite.
The respective pulse and exposures may be the same time or pulse may be for a shorter time than the overall exposure.
In some embodiments, the first precursor is a vapor and the first precursor pulse comprises input to the reactor of a first precursor vapor for a first metal precursor pulse time of a few milliseconds to tens of seconds (e.g., 0.01, 0.05, 0.1, 0.5, 1, 5, 10, 20, or 30 seconds, inclusive of all ranges and values there between), such as 3 seconds. The first partial pressure of the first precursor pulse can be in the range of 0.01-1000 Torr (e.g., 10, 25, 50, 75, 100, 500, or 1000 Torr, inclusive of all ranges and values there between), such as, in one embodiment, at least 0.5-100 Ton, such as 0.88 Torr. One of skill in the art will appreciate that the time length, pressure, and amount of precursor for the pulse are all factors in determining the overall amount for each of those operation parameters. For example, the pressure and amount may follow from the duration of the pulse but depend on the size of the chamber and the type of valve as would be understood from general knowledge regarding ALD. The appropriate precursor pulse times will depend on the size, porosity, and number of substrates to be coated. Note, for ease of reference herein, the process is described with regard to the pulse duration, but it should be understood that the product of precursor partial pressure and time is what dictates the precursor exposures. A carrier gas, such as argon or other non-reactive (with the substrate, the resistive layer or the precursors) gas, may be used.
In some embodiments, the first precursor exposure comprises exposing the substrate to the first precursor for a first exposure time and a first partial pressure of the first metal precursor so that the first precursor binds with the substrate, a resistive layer deposited on the substrate previously, or coating from prior ALD cycle, including of CaF2. In some embodiments, given the short time for the pulse/exposure for this ALD process the pulse lasts the entire exposure until the purge starts with the pulse time and exposure time being the same. The first metal precursor pulse time may be less than the first exposure time, or they may be equal such that the exposure is the same as the pulse. The first exposure time can be in the range of 0.05-500 seconds (e.g., 0.05, 0.1, 0.5, 1, 5, 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 120, 140, 160, 180, 200, 220, 240, 260, 280, 300, 350, 400, 450 or 500 seconds, inclusive of all ranges and values there between). In some embodiments, the first predetermined time is in the range of 1-10 seconds (e.g., about 3 seconds). The first partial pressure of the first metal precursor can be in the range of 0.01-10 Torr (e.g., 0.01, 0.05, 0.1, 0.5, 1.0, 5.0, or 10 Ton, inclusive of all ranges and values there between). In some embodiments, the first partial pressure of the first metal precursor is in the range of 0.1-1 Torr (e.g., about 0.88 Torr). A longer dose is needed for coating high surface area substrates.
The first precursor purge evacuates unreacted precursor from the reactor. The first precursor purge may be for a first precursor purge time of 0.5-30 seconds (e.g., 0.5, 1, 5, 10, 20, or 30 seconds, inclusive of all ranges and values there between), such as 15 seconds. The first precursor purge reduces the pressure in the reactor to within the range of 0.01-10 Torr (e.g., 0.01, 0.05, 0.1, 0.5, 1.0, 5.0, or 10 Torr, inclusive of all ranges and values there between), such as substantially to vacuum. In some embodiments, the reactor pressure may remain essentially constant during the first precursor purge, but a constant flow of inert carrier gas such as Argon sweeps away residual unreacted precursor from the reactor.
In some embodiments, the base material can be heated to a predetermined temperature during the ALD process. For example, the first predetermined temperature can be in the range of 20-200° C. (e.g., 20, 30, 40, 50, 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170, 180, 190 or 200° C., inclusive of all ranges and values there between). In some embodiments, the first predetermined temperature is in the range of 100-400° C. (e.g., 225° C.). Temperature also impacts the overall energy in the system and the performance for diffusion and/or reaction. In an ALD process, the deposition temperature range where more or less the same growth occurs is referred to as the “ALD window.” The ALD reaction should occur at a temperature of the precursor sufficient to give constant precursors evaporation rate (i.e., vapor pressure). If vapor pressure is not enough, there may still be layer growth, but the surface coverage will be poor. If vapor pressure is too much, it will waste precursor, and there may be CVD growth if there is not sufficient purge time due to mixing of precursors. The temperature of the layer growth can be as low as the subliming temperature of the ALD precursors. For example, if the precursor sublimes at 150° C. films can also grow around that temperature. But generally, layer growth temperature is 25-50° C. higher than precursor sublimation temperature. The temperature must be lower than the thermal decomposition temperature of the precursor.
The substrate, after reaction with the first metal precursor, is then exposed to a second precursor by a second precursor pulse introducing the second precursor to the reactor and then exposing for the second precursor exposure such that the second precursor reacts with the first metal precursor or, more particularly, with intermediate entity formed by the first metal precursor and the substrate (or ALD coating on the substrate).
In some embodiments, the second precursor pulse comprises input to the reactor of the second precursor vapor for a second precursor pulse time of 0.01-30 seconds (e.g., 0.01, 0.05, 0.1, 0.5, 1, 5, 10, 20, or 30 seconds, inclusive of all ranges and values there between), such as 1 second. The first partial pressure of the second precursor pulse can be in the range of 0.01-10 Torr (e.g., 0.01, 0.05, 0.1, 0.5, 1.0, 5.0, or 10 Torr, inclusive of all ranges and values there between) such as 0.88 Torr.
In some embodiments, exposing the substrate to second precursor for a second precursor exposure time and a second partial pressure of the second precursor so that second precursor reacts with the entity formed by the first metal precursor reacting with the substrate (or previous ALD deposited coatings). The second precursor exposure time can be in the range of 0.05-500 seconds (e.g., 0.05, 0.1, 0.5 1, 5, 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 120, 140, 160, 180, 200, 220, 240, 260, 280, 300, 350, 400, 450 or 500 seconds, inclusive of all ranges and values there between), such as about 1 second. The second partial pressure of the second precursor can be in the range of 0.01-10 Torr (e.g., 0.01, 0.05, 0.1, 0.5, 1.0, 5.0, or 10 Torr, inclusive of all ranges and values there between). In some embodiments, the second partial pressure of the second precursor is in the range of 0.1-1 Torr (e.g., about 0.5 Torr) such as 0.88 Torr.
The second precursor purge evacuates unreacted precursor from the reactor. The second precursor purge may be for a second precursor purge time of 0.5-500 seconds (0.5, 1, 5, 10, 20, 30, 40, 50, 60, 70, 80, 90, 100, 120, 140, 160, 180, 200, 220, 240, 260, 280, 300, 350, 400, 450 or 500 seconds, inclusive of all ranges and values there between), such as 10 seconds. The second precursor purge reduces the pressure in the reactor to within the range of 0.01-10 Torr (e.g., 0.01, 0.05, 0.1, 0.5, 1.0, 5.0, or 10 Ton, inclusive of all ranges and values there between), such as substantially to vacuum. In some embodiments, the reactor pressure may remain essentially constant during the second precursor purge, but a constant flow of inert carrier gas such as Argon sweeps away residual unreacted precursor from the reactor. In some embodiments, the second precursor may include one or more of HF, HF dissolved in pyridine, WF6, TaF5, MoF6, NbF5, and hexafluoroacetylacetone (“hfac”).
Any number of cycles of exposing the substrate or prior coatings to the first metal precursor and the second precursor can be performed to reach a thickness of coating or to provide a desired alteration of the substrate properties. In some embodiments, the number of cycles of the ALD process can be in the range of 1-50 (e.g., 1 cycle, 2, 3, 4, 5, 10, 15, 20, 25, 30, 35, 40, 45, or 50 cycles, inclusive of all ranges and values there between). CaF2 is an ionic crystal with the fluorite structure. The lattice is a face centered cubic (“FCC”) structure with three sub-lattices. The unit cell of the material is most easily described as a simple cubic lattice formed by the F− ions where a Ca2+ ion is contained in every second cube. The remaining empty cubes called as interstitial or hollow sites are important for defect formation and diffusion, but also for the accommodation of unwanted impurities like rare earth ions and dopants. The lattice constant is a=5.451 Å. The natural cleavage plane of the crystal is the (111) surface. It is built up from F−—Ca2+—F− triple layers of 3.14 Å distance and is terminated by fluorine ions. Consider the mass per steady state CaF2 ALD cycle is 12 ng/cm2 (F−—Ca2+—F−) or growth rate is 0.3 Å/cycle; therefore, in one embodiment, the process is depositing a partial layer in each cycle of CaF2. In one embodiment, the interlayer thickness is in the range of 0.3-30 nm. In some embodiments, the ALD deposition of the CaF2 interlayer proceeds for 10-1000 cycles.
In one embodiment, MgF2 may be used as an SEE layer as shown in
In one embodiment, an oxyfluoride barrier layer, such as an interlayer formed between the resistive layer, such as W:AlOF and MgO layers. The oxyfluoride layer may be MgOxFy, where x is (0<x<1) and y is (0<y<2), such as where x is greater than 0 and less than 1 and y is greater than 0 and less than 2(1−x). In one embodiment, the oxyfluoride is deposited by ALD. For example, ALD may be by a typical ALD process using 1×MgO and 2×MgF2 pulse exposures for 10 cycles total. The ratio of MgO:MgF2 pulses can range from about 10:1 to 1:10.
In one embodiment, the MgOxFy may be an SEE layer deposited directly on the resistive layer, such as W:AlOF. In one embodiment, the ALD process for deposition of MgOxFy uses bis(ethylcyclopentadienyl) magnesium (Mg(EtCp)2) and H2O for the MgO ALD and Mg(EtCp)2 and HF for the MgF2 ALD. The ALD temperature may be in the range of 20-350° C. and preferably 200° C. The pulse times may be in the range of 0.01-30 s and preferably 1 s. The purge times may be in the range of 1-200 s and preferably 5 s. It should be appreciated that the precursor dose and purge time is based on the self-limiting behavior of the precursors. This can be varied in wide range from a few milliseconds to 100 s of seconds. Further if a longer dose time is utilized, the purge times may need to increase to avoid a CVD type reaction, which can result in non-uniformity and particle formation. In one embodiment, a ratio of MgO deposition cycles to MgF2 deposition cycles is 20:1. In one embodiment, the ALD process utilizes 20 cycles of MgO ALD (such as Mg(EtCp)2 and H2O) to deposit a MgO layer followed by 1 cycle of MgF2 ALD (such as Mg(EtCp)2 and HF), such that the deposited MgO layer is converting to MgOxFy. The ratio of F:O can be adjusted by adjusting the relative number of MgO:MgF2 cycles and temperature.
In one embodiment, the W:AlOF layer(s) is deposited by ALD using a ratio of 1 W ALD cycle to 8 Al2O3 ALD cycles and may comprising 500 total ALD cycles. MgO may be formed as a single layer or comprise 100 layers. The ratio of W:AlOF to MgO may be from 5:1 to 5000:1. The MgOxFy, layer is deposited between the W:AlOF resistive layer and the MgO SEY layer and may be in a ratio of 1:2 to 1:5000 to W:AlOF and 1:1 to 500:1 to MgO. The MgOxFy, may comprise a single layer or up to 500 layers. Deliberately depositing controlled MgOxFy, as a SEE layer is believed to prevent the F-mitigation from the W:AlOF layer and can prevent uncontrolled F− mitigation from pure MgO/W:AlOF.
No claim element herein is to be construed under the provisions of 35 U.S.C. § 112(f), unless the element is expressly recited using the phrase “means for.”
As utilized herein, the terms “approximately,” “about,” “substantially,” and similar terms are intended to have a broad meaning in harmony with the common and accepted usage by those of ordinary skill in the art to which the subject matter of this disclosure pertains. It should be understood by those of skill in the art who review this disclosure that these terms are intended to allow a description of certain features described and claimed without restricting the scope of these features to the precise numerical ranges provided. Accordingly, these terms should be interpreted as indicating that insubstantial or inconsequential modifications or alterations of the subject matter described and claimed are considered to be within the scope of the disclosure as recited in the appended claims.
It should be noted that the term “exemplary” and variations thereof, as used herein to describe various embodiments, are intended to indicate that such embodiments are possible examples, representations, or illustrations of possible embodiments (and such terms are not intended to connote that such embodiments are necessarily extraordinary or superlative examples).
The term “coupled” and variations thereof, as used herein, means the joining of two members directly or indirectly to one another. Such joining may be stationary (e.g., permanent or fixed) or moveable (e.g., removable or releasable). Such joining may be achieved with the two members coupled directly to each other, with the two members coupled to each other using a separate intervening member and any additional intermediate members coupled with one another, or with the two members coupled to each other using an intervening member that is integrally formed as a single unitary body with one of the two members. If “coupled” or variations thereof are modified by an additional term (e.g., directly coupled), the generic definition of “coupled” provided above is modified by the plain language meaning of the additional term (e.g., “directly coupled” means the joining of two members without any separate intervening member), resulting in a narrower definition than the generic definition of “coupled” provided above. Such coupling may be mechanical, electrical, or fluidic. For example, circuit A communicably “coupled” to circuit B may signify that the circuit A communicates directly with circuit B (i.e., no intermediary) or communicates indirectly with circuit B (e.g., through one or more intermediaries).
The term layer or coating may refer to a complete layer, such as at least single atomic layer thick or may refer to an ad-island or other incomplete or non-uniform layer.
The term “or,” as used herein, is used in its inclusive sense (and not in its exclusive sense) so that when used to connect a list of elements, the term “or” means one, some, or all of the elements in the list. Conjunctive language such as the phrase “at least one of X, Y, and Z,” unless specifically stated otherwise, is understood to convey that an element may be either X, Y, Z; X and Y; X and Z; Y and Z; or X, Y, and Z (i.e., any combination of X, Y, and Z). Thus, such conjunctive language is not generally intended to imply that certain embodiments require at least one of X, at least one of Y, and at least one of Z to each be present, unless otherwise indicated.
References herein to the positions of elements (e.g., “top,” “bottom,” “above,” “below”) are merely used to describe the orientation of various elements in the figures. It should be noted that the orientation of various elements may differ according to other exemplary embodiments, and that such variations are intended to be encompassed by the present disclosure.
Although the figures and description may illustrate a specific order of method steps, the order of such steps may differ from what is depicted and described, unless specified differently above. Also, two or more steps may be performed concurrently or with partial concurrence, unless specified differently above.
This invention was made with government support under Contract No. DE-ACO2-06CH11357 awarded by the United States Department of Energy to UChicago Argonne, LLC, operator of Argonne National Laboratory. The government has certain rights in the invention.
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