This disclosure is directed to a cost effective method of synthesizing yttrium oxide, Y2O3, nano-powders and to composited made using such powders.
High performance, good erosion resistant multi-band transparent materials are in the strong demand for different application such as optical window coatings, medical instruments, lasers, lighting devices and other uses. Yttrium oxide, Y2O3, is one of the promising candidates with excellent optical performance through mid-range IR wavelengths at both ambient and elevated temperatures, and though it has low scattering and great machinability/shaping ability, it has limited commercial market due to its current high cost issue as well as thermo-mechanical properties that need improvement. Currently, the pure Y2O3 nano-sized powders are very expensive, and the breaking-down processing of the soft agglomeration of nano-powders for compacting is very time-consuming and costly. In addition, the inadequate mechanical properties of pure Y2O3 powders have limited its applications in coatings, illuminating devices and other areas. As a result, the production of lower-cost pure nano-sized Y2O3 powders is desired.
In one aspect the disclosure is directed to a method for inexpensively producing a Y2O3 nano-powder material, thereby facilitating the increased utilization of the material in different commercial application. In another aspect the disclosure is directed to Y2O3 nano-powder composite materials consisting of Y2O3 and at least one oxide selected from the group consisting of MgO, CaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and additional rare earth oxides.
In one aspect the disclosure is directed to a method of making yttrium oxide contain nano-particles, the method comprising preparing a solution Y(NO3)3.6H2O placing the solution in a vessel rotatable table; preparing a solution of ammonia carbonate solution containing ammonia sulfate and 0.2-1.0 wt. % of a water soluble polyethylene glycol as a dispersant; placing the vessel containing the Y(NO3)3 solution in a 60-80° C. water bath and titrating the Y(NO3)3 solution with the ammonium carbonate solution at the rate of 1-4 ml/min while the vessel containing the Y(NO3)3 solution was rotated at a speed in the range of 100-200 rpm to form a uniform precipitation of the yttrium nano-particles; spinning the precipitated yttrium nano-particles with sonication for a time in the range of 2-60 minutes after completion of the titration followed by decantation of the liquid and washing the nano-particles with an alcohol/water solution; collecting and drying the in vacuum at a temperature in the range of 15-30° C. to provide dried yttrium oxide nano-particles; and calcining dried yttrium oxide nano-particles at a temperature in the range of 1050° C. to 1150° C. for a time of at least 2 hours. During the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.7-9.0. In an embodiment at least one water soluble metal salt is added to the yttrium nitrate solution prior the beginning of the titration for forming a doped yttrium after calcination; the at least one water soluble metal salt being a chloride, nitrate or acetate selected from the group of metal consisting of MgO, CaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and the remaining rare earth metals.
In another aspect the disclosure is directed to a method for forming a yttrium oxide article, the method comprising preparing a solution Y(NO3)3.6H2O placing the solution in a vessel rotatable table; preparing a solution of ammonia carbonate solution containing ammonia sulfate and 0.2-1.0 wt. % of a water soluble polyethylene glycol as a dispersant; placing the vessel containing the Y(NO3)3 solution in a 60-80° C. water bath and titrating the Y(NO3)3 solution with the ammonium carbonate solution at the rate of 1-4 ml/min while the vessel containing the Y(NO3)3 solution was rotated at a speed in the range of 100-200 rpm to form a uniform precipitation of the yttrium nano-particles; spinning the precipitated yttrium nano-particles with sonication for a time in the range of 2-60 minutes after completion of the titration followed by decantation of the liquid and washing the nano-particles with an alcohol/water solution; collecting and drying the in vacuum at a temperature in the range of 15-30° C. to provide dried yttrium oxide nano-particles; calcining dried yttrium oxide nano-particles at a temperature in the range of 1050° C. to 1150° C. for a time of at least 2 hours; placing the calcined nano-particles in a hot isostatic pressing apparatus; sintering the calcined yttrium oxide nano-particle at a temperature in the range of 1200-1500° C. for a time in the range of 4-10 hours in a 15-20% V/V O2/Ar and a pressure of 1 atmosphere; and hot isostatic pressing by increasing the pressure to 200 MPa and holding the pressure for an additional time in the range 1 hour to 5 hours; and cooling to obtain yttrium oxide article. During the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.5-9.5 and the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.7-9.0. In an embodiment at least one water soluble metal salt is added to the yttrium nitrate solution prior the beginning of the titration for forming a doped yttrium after calcination; the at least one water soluble metal salt being a chloride, nitrate or acetate selected from the group of metal consisting of MgO, CaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and the remaining rare earth metals; and the yttrium oxide article that is obtained contains at least one selected metal as a metal oxide.
Herein the terms “nano-powder,” “powder,” nano-particles,” and “particles” refer to the as-synthesized nano-material, The term “disc” means nano-powder that that been formed in to selected shaped, such as a disc as illustrated in
The present disclosure is directed to the synthesis of Y2O3 nano-powders, and composites of Y2O3/MOx (both after sintering), where MOx is at least one other metal oxide in which x is in the range of 1-3, using low-cost precursors in a time- and cost-saving way that is also ease to scale up to produce larger amounts of the material. Spinning and ultra-sonication are used to break down the Y2O3 soft agglomeration of the Nano powders in a fast and efficient way as compared to either traditional ball-milling, which is time-consuming, or freeze-drying which is expensive to use. The Y2O3 nano-powder or Y2O3/MOx composites, when consolidated as a composite/solid solution systems, including nanocomposites, are designed to and produced to get multiple functional ceramics or materials with improved thermal-mechanical properties compare to the pure Y2O3.
In general, the method involves dissolving yttrium nitrate in water in a vessel and titrating the resulting solution with an ammonium carbonate solution containing ammonium sulfate and a water soluble lubricant, for example, commercially available Lutrol E-400 which a polyethylene glycol (BASF) or similar material. The vessel is spun during the titration with control of the pH in the range of 8.3-9.5. In an embodiment the pH is controlled to be in the range of 8.7-9.0. After the titration is completed the precipitated and sonicated for an additional time to homogenize the precipitants. The precipitants are collected on a filter, an vacuum dried. Following the drying the precipitants are calcined.
(a) Synthesis of Pure Y2O3 Nano-Powders
A 0.5M solution Y(NO3)3.6H2O was prepared and place in a vessel. A solution of 2-2.5M ammonia carbonate solution containing 5 Mol % ammonia sulfate and 0.3-0.8 wt. % Lutrol E-400 [a polyethylene glycol, CAS 25322-68-3] as the dispersant. The vessel containing the Y(NO3)3 solution was placed in a 70° C. water bath and was titrated with the ammonium carbonate solution at the rate of 2-ml/min ammonia carbonate while the vessel containing the Y(NO3)3 solution was spun at a speed in the range of 120-150 rpm to five a uniform precipitation of the yttrium product. During the titration the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.7-9.0
(b) Synthesis of Y2O3-Based Composites/Compounds Y2O3/MOx (after Sintering)
The amount of the non-yttrium metal is determined beforehand and is added to the yttrium-containing solution. Depending on the amount of non-yttrium material that is used, the final functional material, after sintering and containing yttrium and at least one additional metal, can be a nano-composite or doped ceramic, a solid solution or a compound. The at least one additional metal M can be added to the yttrium containing solution as a nitrate, chloride or other water soluble salt in a selected percentage or Y:M ratio depending on the intended purpose of the final product. The Y/M containing solution is then titrated with an ammonium carbonate solution containing ammonium sulfate and a lubricant as described above and spun at a spinning in the range of 120-150 rpm while maintaining the pH in the range of 8.3-9.5, preferably in the range of 8.7-9.0. The material that can be added into the Y2O3 system include MgO, CaO, BaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and additional rare earth oxides. An exemplary Y2O3—ZrO2—MgO composite Y2O3 doped with 6-9 mol % ZrO2 and 0.5-2 mol % MgO. describes herein is a general COMPOSITE system
Once the titration has been completed, the precipitant in the vessel was further spun while sonicating the solution to homogenize the precipitant. This spinning/sonication treatment was done for a time in the range of 5-60 minutes.
The fluid in the vessel was decanted and the precipitate was water washed at least once to remove unreacted materials and the lubricant, alcohol washed using a C1-C3 alcohol, and was collected on a 0.2 μm-0.4 μm filter paper or equivalent filter, for example a frit filter.
4. The collected precipitate was then vacuum dried at room temperature, approximately 15-30° C., to fully dry and powderize the precipitant.
5. After the powder had been dried it was calcined in air at a selected temperature in the range of 1050° C. to 1150° C. for a time of at least 2 hours. In an embodiment the time is at least 4 hours. In a further embodiment the time is at least 6 hours. In an embodiment the calcination temperature 1100° C. and the time was 4 hours. Once the powder was fully dried and calcined it was used to form an article The dried, calcined nano-powder is illustrated in
(a) The calcined powder was suspended in an alcohol solution and ultrasonically treated for a time in the range of 5 minutes to 1 hour to breakdown the soft agglomeration of particles that is illustrated in
(b) The dried, ultra-sonicated nano-powder was then pressed into a die at a pressure 1500 psi, followed by cold isostatic pressing of 25-30 kpsi for the final compacting and to form an article that can be further processed.
(a) Two-Stage Sintering
Two-stage sintering includes:
(b) One-Stage Sintering
Some of the major differences between the method describes herein and the art include:
(1) The method disclosed herein does not use any binder or chelating agent s during the synthesis of the pellet.
(2) No sintering aid is added to the during the sintering stage.
(3) An ammonium carbonate solution was used as the precipitating agent instead of the ammonium bicarbonate used in the art. The use of ammonium carbonate results in a better product—fewer color centers, better nano-particle size distribution, fine particle size resulting in a clearer product.
(4) The inclusion of ammonium sulfate in the initial titrating solution and sulfate is included in the initial precipitation product. Sulfur is burned out as a gaseous oxide during the sintering process.
(5) The use of an alcohol washing agent which aids in dehydrating the product and reduces drying time.
(6) Using dispersion in an alcohol solution with sonication to de-agglomerate the soft agglomeration of particles, instead of the traditional ball milling, gives a more uniform nano-particle size distribution.
(7) The use of a 1-state HIP process which results in a time and cost savings over the traditional two-step process.
The collected nano-powder can then be used in forming the batched materials for conversion into the transparent Y2O3 based ceramics.
This disclosure is thus directed to a method of making yttrium oxide nano-particles, yttrium oxide nano-particles containing one or a plurality of selected dopants, and ceramic materials made the nano-particles or doped nano-particles. The method comprises preparing a solution Y(NO3)3.6H2O placing the solution in a vessel rotatable table; preparing a solution of ammonia carbonate solution containing ammonia sulfate and 0.2-1.0 wt. % of a water soluble polyethylene glycol as a dispersant; placing the vessel containing the Y(NO3)3 solution in a 60-80° C. water bath and titrating the Y(NO3)3 solution with the ammonium carbonate solution at the rate of 1-4 ml/min while the vessel containing the Y(NO3)3 solution was rotated at a speed in the range of 100-200 rpm to form a uniform precipitation of the yttrium nano-particles; spinning the precipitated yttrium nano-particles with sonication for a time in the range of 2-60 minutes after completion of the titration followed by decantation of the liquid and washing the nano-particles with an alcohol/water solution; collecting and drying the nano-particles in vacuum at a temperature in the range of 15-30° C. to provide dried yttrium oxide nano-particles; and calcining dried yttrium oxide nano-particles at a temperature in the range of 1050° C. to 1150° C. for a time of at least 2 hours. In one embodiment, during the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.5-9.5. in another embodiment, during the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.7-9.0. Making the doped yttrium oxide nanoparticles comprises adding least one water soluble metal salt to the yttrium nitrate solution prior the beginning of the titration for forming a doped yttrium after calcination. The at least one water soluble metal salt is a chloride, nitrate or acetate selected from the group of metal consisting of MgO, CaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and the remaining rare earth metals.
The disclosure is also directed to a method of making yttrium oxide articles, and articles made from a yttrium oxide doped with a selected dopant, the method comprising preparing a solution Y(NO3)3.6H2O placing the solution in a vessel rotatable table; preparing a solution of ammonia carbonate solution containing ammonia sulfate and 0.2-1.0 wt. % of a water soluble polyethylene glycol as a dispersant; placing the vessel containing the Y(NO3)3 solution in a 60-80° C. water bath and titrating the Y(NO3)3 solution with the ammonium carbonate solution at the rate of 1-4 ml/min while the vessel containing the Y(NO3)3 solution was rotated at a speed in the range of 100-200 rpm to form a uniform precipitation of the yttrium nano-particles; spinning the precipitated yttrium nano-particles with sonication for a time in the range of 2-60 minutes after completion of the titration followed by decantation of the liquid and washing the nano-particles with an alcohol/water solution; collecting and drying the in vacuum at a temperature in the range of 15-30° C. to provide dried yttrium oxide nano-particles; calcining dried yttrium oxide nano-particles at a temperature in the range of 1050° C. to 1150° C. for a time of at least 2 hours; placing the calcined nano-particles in a hot isostatic pressing apparatus;
sintering the calcined yttrium oxide nano-particle at a temperature in the range of 1200-1500° C. for a time in the range of 4-10 hours in a 15-20% V/V O2/Ar and a pressure of 1 atmosphere; and hot isostatic pressing by increasing the pressure to 200 MPa and holding the pressure for an additional time in the range 1 hour to 5 hours; and cooling to obtain yttrium oxide article. In one embodiment, during the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.5-9.5. In another embodiment, during the titration of the Y(NO3)3 solution the pH of the solution was controlled such that the pH of the precipitated material was in the range of 8.7-9.0. In addition, doped yttrium oxide articles can be made from a doped yttrium nano-particle by adding at least one water soluble metal salt to the yttrium nitrate solution prior the beginning of the titration for forming a doped yttrium after calcination. The at least one water soluble metal salt is a chloride, nitrate or acetate selected from the group of metal consisting of MgO, CaO, BeO2, Al2O3, TiO2, ZrO2, SiO2, HfO2, YbO2, GdO2, Lu2O3 and the remaining rare earth metals. The resulting yttrium oxide article thus contains the at least one selected metal as a metal oxide.
While the invention has been described with respect to a limited number of embodiments, those skilled in the art, having benefit of this disclosure, will appreciate that other embodiments can be devised which do not depart from the scope of the invention as disclosed herein. Accordingly, the scope of the invention should be limited only by the attached claims.
This application claims the benefit of priority under 35 U.S.C. §119 of U.S. Provisional Application Ser. No. 61/731,900 filed on Nov. 30, 2012 the content of which is relied upon and incorporated herein by reference in its entirety.
Number | Date | Country | |
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61731900 | Nov 2012 | US |