Deposition Method, Continuous Deposition System, and Application Thereof

A deposition method, comprising the steps of exposing a carrier to moisture, so that a hydroxy group can be distributed on the surface of the carrier, and adding a liquid precursor to the hydroxy group to perform an alcohol condensation reaction to form a target atom layer or a target atom compound layer of the deposition carrier; the process provided by the present invention allows one or more liquid precursors to be freely selected for uniform deposition on the carrier. Compared to the current low-yield dry atomic deposition technology, it has no limitation on the volume of the reaction chamber, no complicated and diverse process, and can be designed as a continuous process to achieve wider industrial availability.

FIELD OF INVENTION

The present invention is related to a deposition method, in particular a method of depositing specific atoms or chemical functional groups on a carrier by a liquid precursor, continuous deposition system, and applications thereof. BACKGROUND OF THE INVENTION

Atomic Layer Deposition (ALD) is a method of depositing atoms layer by layer on the surface of a carrier (or substrate). Current ALD is a dry ALD process, as its steps and technologies are so complicated and diverse that it is still not applicable in the industry today.

The dry ALD process generally consists of two major steps of precursor adsorption on the powder and oxidant reaction, which also can be subdivided into four sub-steps for processing.

Step (1) the reaction of precursor gasification and adsorption on the powder, step (2) vacuuming or inert-gas purging to remove excess precursors and possible by-products of the process, step (3) the following adsorption reactions and steps for oxidant gasification, step (4) vacuuming or inert-gas purging to remove excess oxidant and possible by-products.

The above four steps are to complete one ALD cycle. By repeating the previous steps several times, the number of layers of target atoms deposited on or grown on the carrier can be controlled.

At present, the main reasons why this technology is still difficult to commercialize and cannot be produced on a large scale include:1. The powdered precursors and oxidants must be disturbed and flown to achieve adsorption on the carrier surface.2. The precursors and oxidants in the process need to maintain gasification and continue to fly, resulting in high energy consumption.3. To remove excess precursors or oxidants, vacuuming or inert-gas purging is required in the process because excess precursors or oxidants cannot be recycled, which creates waste, and vacuuming or inert-gas purging also increases the cost during the process.4. The powder tends to adhere to the wall of the reaction chamber, so the chamber must be cleaned between batches.

Hence, it is eager to have a new deposition method that will overcome or substantially ameliorate at least one or more of the deficiencies of a prior art, or to at least provide an alternative solution to the problems. It is to be understood that, if any prior art information is referred to herein, such reference does not constitute an admission that the information forms part of the common general knowledge in the art.

SUMMARY OF THE INVENTION

In order to overcome various shortcomings of the present atomic layer deposition process using powder-based reactants and a dry process, the present invention first provides a deposition method comprising the steps of:Step 1: providing a carrier;Step 2: exposing the carrier to moisture for a predetermined time such that a hydroxy group is distributed on the surface of the carrier;Step 3: adding a liquid precursor comprising a precursor and a corresponding solvent, the precursor comprising at least one target atom and a functional group capable of undergoing an alcohol condensation reaction with the hydroxy group;Step 4: bonding the functional group of the precursor to the hydroxy group on the surface of the carrier to perform an alcohol condensation reaction such that the target atom is bonded to the surface of the carrier through the functional group; andStep 5: calcining the resulting product which is dried so that the target atom forms a stable layer of a target atom or a layer of a target atom compound bonded to the surface of the carrier.

Furthermore, the present invention also provides a continuous deposition system according to the aforementioned deposition method, which includes a first mixing zone, a second mixing zone, and a product drying and calcining zone, and those three are interconnected by materials, wherein:the first mixing zone is connected to a moisture supply unit and a carrier supply unit respectively which are fed into the first mixing zone for a reaction respectively, so that the hydroxy group is distributed on the surface of the carrier;introducing the carrier in which the hydroxy group is distributed into the second mixing zone, the second mixing zone having a liquid precursor supply unit, a residual liquid precursor discharge outlet, and a product discharge outlet. After the carrier in which the hydroxy group is distributed has reacted with the liquid precursor in the second mixing zone, if there is any residual liquid precursor, it is discharged from the residual liquid precursor discharge outlet, and the product is discharged from the product discharge outlet.

Furthermore, the present invention also provides a electrochemical application having a electrode material comprising a layer of the target atom or a layer of the target atom compound obtained by the deposition method described above.

In accordance, the present invention has the following advantages and beneficial effects as following:1. The present invention provides a new type of wet atomic deposition technology in which one or more precursors can be freely selected for uniform deposition on the carrier powder. Compared to today's low-yield dry atomic deposition technology, there is no limitation on the volume of the reaction chamber and no complicated and diverse manufacturing process.2. The present invention provides a more economical and convenient process compared to existing deposition methods by using the wet atomic deposition technology in which the liquid precursors react with the carriers during the reaction process, eliminating the need to continuously maintain the precursor in a flying state as in the dry process, and eliminating the need to stop and sweep the powder during the process.

Many of the attendant features and advantages of the present invention will become better understood with reference to the following detailed description considered in connection with the accompanying figures and drawings.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

Reference will now be made in detail to the present preferred embodiments of the invention, examples of which are illustrated in the accompanying drawings. Wherever possible, the same reference numbers are used in the drawings and the description to refer to the same or like parts. It is not intended to limit the method by the exemplary embodiments described herein. In the following detailed description, for purposes of explanation, numerous specific details are set forth in order to attain a thorough understanding of the disclosed embodiments. It will be apparent, however, that one or more embodiments may be practiced without these specific details. As used in the description herein and throughout the claims that follow, the meaning of “a”, “an”, and “the” may include reference to the plural unless the context clearly dictates otherwise. Also, as used in the description herein and throughout the claims that follow, the terms “comprise or comprising”, “include or including”, “have or having”, “contain or containing” and the like are to be understood to be open-ended, i.e., to mean including but not limited to.

With reference toFIG.1, the present invention provides a deposition method comprising the steps of:Step S1) providing a carrier10, preferably in the form of powder or particles;Step S2) exposing the carrier10to moisture for a predetermined time so that the surface of the carrier10is distributed with a hydroxy group11(also known as —OH group); preferably, the carrier10can be stirred or turned in this step so that the carrier10can fully contact with the moisture as shown inFIG.1; The carrier10of the present invention comprises but not limited to all kinds of electrode material (both positive or negative material) which could be distributed with the hydroxyl group11for any electrochemical applications, such as lithium battery or sodium battery.Step S3) adding a liquid precursor20comprising a precursor21and a corresponding solvent22so that the precursor21is dissolved in the solvent22, preferably comprising anhydrous ethanol, anhydrous ether, anhydrous methanol, and/or anhydrous acetone; the precursor21containing at least one target atom211and a functional group212which can undergo alcohol condensation with the hydroxy group11, wherein, the precursor21being dissolved in the solvent22in an amount preferably >0.01 M, more preferably greater than 0.1 M or most preferably greater than 0.5 M, and essentially only a small amount of the precursor21is required to carry out the alcohol condensation reaction with at least part of the hydroxy group11, or even an excess of the precursor21, the alcohol condensation reaction can be carried out with most or all of the hydroxy group11;Step S4) bonding the functional group212of the precursor21to the —OH group on the surface of the carrier10to perform an alcohol condensation reaction so that the target atom211is bonded to the surface of the carrier10through the functional group212; preferably, the functional group212of the precursor21is ethoxy (O C2H5);Step S5) (optional) repeating the previous Steps 2 to 4 several times as required to achieve the desired number or stacking thickness of target atoms211bonded to the surface of the carrier10; andStep S6) calcining the resulting product obtained in the previous Step 4 or 5 that is dried so that the target atom211forms a stable layer of a target atom or a layer of a target atom compound30bonded to the surface of the carrier10. Wherein, the calcination step may result in a greater degree of complete sintering of the organic components of the previous step to form the target atom layer, or it may result in oxidation of the target atom211to form the target atom compound layer30. The temperature of calcination is preferably in the range of 500 to 1500° C.

First Preferred Embodiment

The first preferred embodiment of the deposition method of the present invention is to use a nickel-cobalt-manganese metal oxide (NMC/NMC811) as the carrier10, and finally deposit the aluminum target atom compound layer (aluminum trioxide, Al2O3) on its surface and stably bonded to the surface of the carrier10, comprising the following steps:Step S1-1) exposing the NMC10powder to moisture and controlling the distribution of the —OH group11on the surface of the NMC10;Step S1-2) adding the liquid precursor20, in which aluminum triethoxide (Al(OC2H5)2) is used as the precursor21and anhydrous ethanol (EtOH) is used as the solvent22; the aluminum triethoxide has an aluminum atom as the target atom211and triethanolic group as the functional group212;Step S1-3) the triethanolic group in the aluminum triethoxide21and the —OH group11on the surface of the NMC10undergo an alcohol condensation reaction to form —OAl(OC2H5)2which is bonded to the surface of the carrier10;Steps S1-4) (optional) repeating the above Steps 1-3 several times as required to achieve the desired number or stack thickness of aluminum atoms (target atoms)211and bond them to the surface of the NMC10; andSteps S1-5) drying and calcining the above product to obtain an Al2O3-NMC with aluminum trioxide (Al2O3) as the target atom compound layer30stably bonded and loaded on the surface of the carrier10.

Second Preferred Embodiment

The second preferred embodiment of the deposition method of the present invention, again, using nickel-cobalt-manganese metal oxide (NMC) as the carrier10, and finally deposit the aluminum target atom compound layer (lithium aluminate, LiAlO2) on its surface and stably bonded to the surface of the carrier10, comprising the following steps:Step S2-1) exposing the NMC10powder to moisture and controlling the distribution of the —OH group11on the surface of the NMC10;Step S2-2) adding the liquid precursor20, in which aluminum triethoxide and lithium hydroxide (LiOH) are used as the first and second precursors and the same anhydrous ethanol is used as the solvent22; the aluminum atom in the aluminum triethoxide and the lithium atom in the lithium hydroxide are two target atoms211, and the triethanolic group in the aluminum triethoxide and the hydroxide group in the lithium hydroxide are used as two functional groups212; the concentration of the aluminum triethoxide and the lithium hydroxide in the anhydrous ethanol is as described above, preferably >0.01M, more preferably greater than 0.1M, or most preferably greater than 0.5, and the equivalent of aluminum triethoxide to lithium hydroxide is preferably between 1:1˜1:10, more preferably 1:1˜1:5, or best 1:1˜1:3;Step S2-3) the triethanolic group in the aluminum triethoxide21and the hydroxide group in the lithium hydroxide react with the —OH group11on the surface of the NMC10to form —OLiAl(OC2H5)2which is bonded to the surface of the carrier10;Steps S2-4) (optional) repeating the above Steps 1-3 several times as required to achieve the desired number or stack thickness of lithium-aluminum (target atoms)211and bond them to the surface of the NMC10; andSteps S2-5) drying and calcining the above product to obtain a LiAlO2-NMC with lithium aluminate (LiAlO3) as the target atom compound layer30stably bonded and loaded on the surface of the carrier10.

Third Preferred Embodiment

The third preferred embodiment of the deposition method of the present invention, again, using nickel-cobalt-manganese metal oxide (NMC) as the carrier10, and finally deposit the lithium niobium (Nb) target atom compound layer (lithium niobate, LiNbO3) on its surface and stably bonded to the surface of the carrier10, comprising the following steps:Step S3-1) exposing the NMC10powder to moisture and controlling the distribution of the —OH group11on the surface of the NMC10;Step S3-2) adding the liquid precursor20, in which niobium pentaethoxide (Nb(OCH2CH3)5) and lithium hydroxide (LiOH) are used as the first and second precursors21and the same anhydrous ethanol is used as the solvent22; the niobium atom in the niobium pentaethoxide and the lithium atom in the lithium hydroxide are two target atoms211, and the alcohol group in the niobium pentaethoxide and the hydroxide group in the lithium hydroxide are used as two functional groups212; the concentration of the niobium pentaethoxide and the lithium hydroxide in the anhydrous ethanol is as described above, preferably >0.01M, more preferably greater than 0.1M, or most preferably greater than 0.5, and the equivalent of niobium pentaethoxide to lithium hydroxide is preferably between 1:1˜1:10, more preferably 1:1˜1:5, or best 1:1˜1:3;Step S3-3) the alcohol group in the niobium pentaethoxide and the hydroxide group in the lithium hydroxide react with the —OH group11on the surface of the NMC10to form —OLiAl(OC2H5)2which is bonded to the surface of the carrier10;Steps S3-4) (optional) repeating the above Steps 1-3 several times as required to achieve the desired number or stack thickness of lithium-niobium (target atoms)211and bond them to the surface of the NMC10; andSteps S3-5) drying and calcining the above product to obtain a LiNbO3-NMC with lithium niobate (LiNbO3) as the target atom compound layer30stably bonded and loaded on the surface of the carrier10.

<Table of Each Reaction Material Type>

Please refer to Tables 1˜3 below fora summary of the reactants, products and preferred embodiments in the previous reactions of the present invention.

<Preferred Embodiment of Continuous Deposition System>

Referring toFIG.2, the present invention provides a continuous deposition system according to the above deposition method, comprising: a first mixing zone40, a second mixing zone50, and a product drying and calcining zone60, and those three interconnected by materials.

The first mixing zone40is connected to a moisture supply unit41and a carrier supply unit42which are fed into the first mixing zone40for reaction respectively, corresponding to the above method to react the moisture with the carrier10, so that the —OH group11is distributed on the surface of the carrier10;introducing the carrier10in which the —OH group11is distributed into the second mixing zone50, which is provided with a liquid precursor supply unit51, a residual liquid precursor discharge outlet52, and a product discharge outlet53. After the carrier10in which the —OH group11is distributed has reacted with the liquid precursor20in the second mixing zone50, if there is any residual liquid precursor20, it is discharged from the residual liquid precursor discharge outlet52, and the product is discharged from the product discharge outlet53, and depending on the process requirements, is redirected to the first mixing zone40or to the product drying and calcining zone60for drying and calcining.

Referring toFIGS.3A˜3D, which are Transmission Electron Microscope (TEM) images of the first preferred embodiment of the above-mentioned deposition method, inFIG.3Aclearly shows that aluminum atoms are distributed on the surface of the carrier10and that the carrier10is formed of NMC metal oxides of nickel, cobalt, and manganese.

Please referring toFIG.4, which are the preferred embodiments of embodiment 1-1: Al2O3-NMC, embodiment 2-1: LiAlO2-NMC_1Eq-LiOH (using 1Eq LiOH) and embodiment 2-1: LiAlO2-NMC_2Eq-LiOH (using 2Eq LiOH) produced by the first and second preferred embodiments of the aforementioned deposition method and the pristine NMC without a deposition coating as a comparative example that is respectively made as the cathodes (or positive electrodes) and assembled into an electrochemical battery (Li/NMC811) for a capacitance and coulombic efficiency comparison test. The electrochemical battery uses a liquid electrolyte of 1M LiPF6 in EC/DEC (1:1) solvent, the measured current is 0.1C, and the cut-off voltage is 3.0˜4.3V.

As can be seen inFIG.4, each embodiment of the present invention has shown a better capacitance and coulombic efficiency performance than the pristine group after at least 100 charge and discharge cycles.

Referring toFIG.5, which is embodiment 2-1: LiAlO2-NMC_1Eq-LiOH (using 1Eq LiOH) produced by the second series preferred embodiment of the aforementioned deposition method and the pristine NMC without deposition coating as the comparative example that is respectively made as the cathodes and assembled into an electrochemical battery (NMC811-1% VGCF∥P-LPSC∥In) for a capacitance comparison test. The electrochemical battery uses a solid electrolyte with 50˜55 mg of Li6PS5Cl (LPSC) particles, the charge/discharge current is 0.05C and the voltage is 2.0˜3.9V. Since this embodiment is a solid-state battery, the effect of the decomposition of Li6PS5Cl (LPSC) particles can be avoided by forming LiAlO2-NMC_1Eq-LiOH from embodiment 2-1 as the positive electrode material.

As can be seen inFIG.5, the embodiment 2-1 of the present invention has a better capacitance performance than the pristine group after 40 charge and discharge cycles.

Referring toFIGS.6,7and the following Table 4, which are the embodiment 3-1 and 3-2 produced by the third series of preferred embodiment of the aforementioned deposition method (LiNbO3-NMC calcined at 500° C. and 700° C., respectively) and the pristine NMC without deposition coating as the comparative example that is respectively made as the cathodes and assembled into an electrochemical battery (NMC811∥1M LiPF6 EC: EMC∥In) for a capacitance and coulombic efficiency comparison test. From the results, it can be seen that the present invention has a better residual capacitance and electrical performance than the pristine group after 100 charge and discharge cycles.

From the above test, it can be seen that the product made by the deposition method of the present invention can indeed increase the electrical performance of the battery when as a positive electrode material.

Besides the solid state battery, the present invention could also apply to any electrochemical applications such as enzyme, or all kinds of electrode material.

The above specification, examples, and data provide a complete description of the present disclosure and use of exemplary embodiments. Although various embodiments of the present disclosure have been described above with a certain degree of particularity, or with reference to one or more individual embodiments, those with ordinary skill in the art could make numerous alterations or modifications to the disclosed embodiments without departing from the spirit or scope of this disclosure.