Porous ceramics can be used for many different applications. Particular applications include filtration of molten metals or particulates from exhaust gases, radiant burners, catalyst supports, biomedical devices, kiln furniture, reinforcement for metal and polymer matrix composites, bioreactors, solid oxide fuel cells, electrodes, heat exchangers, biological scaffolds and other filtration and insulation applications.
Porous ceramics are generally manufactured by replication of a sacrificial foam template. In this method, a flexible polymeric sponge is impregnated with a ceramic slurry. Excess slip is removed by physical pressure (squeezing) or centrifugation. The impregnated sponge is dried, a subsequent burn-out step eliminates the polymer template, and the remaining ceramic material is sintered at high temperature. The polymeric sponge is typically made of polyurethane, but polyvinyl chloride, polystyrene, cellulose and latex have also been used or tested.
Other porous ceramic manufacturing methods are currently in development. One of these methods involves direct foaming of a liquid slurry. Gas bubbles are generated within a liquid slurry containing ceramic powders or a ceramic precursor solution to create a foam. The foam is set so that it maintains its porosity and the foam is then heated to a high temperature for sintering/ceramization. Another method in development involves burn-out of fugitive pore formers. In this method, hollow cells are produced by the burn-out of solid material such as starch, wax, polymeric beads (e.g., polymethyl methacrylate, polystyrene, polyvinyl chloride), carbon black and sawdust.
Each of the aforementioned methods possesses disadvantages. For the sacrificial foam template and fugitive pore former processes, expansion and gas evolution from the polymer or pore former during heating can lead to the development of internal stresses. Liquid foam stability is an issue for the direct foaming process. Additionally, ceramic slurries are required for most of these methods. The drying of ceramic slurries is a time-consuming and cumbersome process and can lead to internal stresses due to differential shrinkage or gas pressure in the finished ceramic.
A method for forming a porous ceramic includes forming a mixture having at least one ceramic precursor and at least one pore-forming material and heating the mixture to oxidize the ceramic precursor and vaporize the pore-forming material.
According to the present invention, porous ceramics are formed without using ceramic starting materials, such as ceramic slurries. A porous ceramic is formed by heating a mixture of one or more ceramic precursors and one or more pore-forming materials. First, a mixture of the ceramic precursor and the pore-forming material is made. Then, the mixture is heated to oxidize the ceramic precursor and vaporize the pore-forming material, forming a porous ceramic in the process. The present invention enables the formation of porous ceramics at relatively low temperature and can create porous ceramics having a wide range of porosity and density, without the tedious and time-consuming additional steps needed for methods that use ceramic starting materials. Additionally, unlike other porous ceramic production methods, a highly controlled heating program is not needed to form porous ceramics according to the present invention.
Ceramic precursors suitable for forming porous ceramics according to the present invention include metals, alloys, binary carbides and nitrides, MAX phase compounds and combinations thereof. In some embodiments, ceramic precursors 12 are powders (e.g., metal powders). Suitable metals include, but are not limited to, titanium, vanadium, chromium, iron, cobalt, nickel, copper, zinc, zirconium, niobium, tantalum, hafnium, tungsten, aluminum and silicon. For the purposes of this patent application, silicon is considered a metal. Suitable alloys include, but are not limited to, alloys of titanium, vanadium, chromium, iron, cobalt, nickel, copper, zinc, zirconium, niobium, tantalum, hafnium, tungsten, aluminum, silicon and combinations thereof. Suitable binary carbides include, but are not limited to, TiC, SiC, TaC and ZrC. Suitable binary nitrides include, but are not limited to, TiN and Si3N4. MAX phase compounds are layered, hexagonal carbides and nitrides that have the general formula: Mn+1AXn, where n=1 to 3, M is an early transition metal, A is an A-group element (mostly IIIA and IVA, or groups 13 and 14) and X is either carbon and/or nitrogen. Suitable MAX phase compounds include, but are not limited to, Ti3SiC2, Ti2AlC, Cr2AlC, V2AlC, Ti2AlN, Nb2AlC and Ti4AlN3. In one particular embodiment, a combination of titanium powder and nickel powder are used together as the ceramic precursor.
Pore-forming materials suitable for forming porous ceramics according to the present invention include graphite, molybdenum oxides (for example, MoO3), polymers that decompose or oxidize to form one or more gases at temperatures above 200° C. and combinations thereof. Graphite oxidizes to form CO2 and vaporizes above about 800° C. Molybdenum oxides MoO2 and MoO3 sublime above about 1100° C. and about 1155° C., respectively. One example of a suitable polymer is polyethylene (PE). Depending on its density, PE generally melts at temperatures between about 105° C. and about 135° C. and has a flash point (i.e. vaporizes) between about 320° C. and about 350° C. In one particular embodiment, a combination of PE and graphite are used together as the pore-forming material.
As shown in
Once mixture 10 has been formed, and optionally compressed, mixture 10 is heated to oxidize ceramic precursor 12 and vaporize pore-forming material 14. Depending on the ceramic precursor and pore-forming material chosen, mixture 10 is generally heated to a final target temperature between about 900° C. and about 1500° C. Mixture 10 can be heated in a tube furnace or other appropriate heating device. In some embodiments, the temperature of the furnace or heating device is raised gradually (e.g., at a rate of about 4-5° C. per minute) until the final target temperature is reached. Once the final target temperature is reached, mixture 10 is heated until substantially all outer surfaces of the ceramic precursor 12 present in mixture 10 has been oxidized. For final target temperatures between about 900° C. and about 1500° C., oxidation is generally substantially complete after between about 3 hours and about 40 hours. In some embodiments, mixture 10 is heated to between about 1400° C. and about 1500° C. for between about 3 hours and about 6 hours. Unlike other porous ceramic production methods, complex controlled heating programs are not needed.
Pore-forming material 14 oxidizes and/or vaporizes during the heating step. Depending on the pore-forming material chosen, the temperature at which oxidation and/or vaporization occurs will differ. For example, PE will vaporize at a lower temperature than graphite and molybdenum oxide. As pore-forming material 14 oxidizes and/or vaporizes, pore-forming material 14 leaves mixture 10 as shown in
In some embodiments, mixture 10 includes two or more different pore-forming materials 14.
Mixture 10A is heated as described above. Because first pore-forming material 14A oxidizes and/or vaporizes at a lower temperature than second pore-forming material 14B, first pore-forming material 14A is removed from mixture 10A before second pore-forming material 14 as shown in
In some embodiments, mixture 10 includes two or more different ceramic precursors 12. Using different ceramic precursors 12 to form porous ceramic 18 enables the synthesis of new combinations of metals. For example, titanium and iron can be used as ceramic precursors 12 to form a FeTiO3 porous ceramic and titanium and nickel can be used as ceramic precursors 12 to form TiO2 and NiTiO3.
In some embodiments, additional materials can be premixed with ceramic precursors 12 so that porous mixed oxides are generated. Hydroxides, carbonates and oxides can be mixed with ceramic precursors 12 prior to or during the formation of mixture 10. Suitable hydroxides include, but are not limited to, NaOH, Ca(OH)2 and Mg(OH)2. Suitable carbonates include, but are not limited to, CaCO3, Na2CO3 and MgCO3. Suitable oxides include, but are not limited to, alkali metal oxides, alkaline earth metal oxides and oxides of titanium, vanadium, chromium, iron, cobalt, nickel, copper, zinc, zirconium, niobium, tantalum, hafnium, tungsten, aluminum and silicon. These additional materials provide porous ceramics 18 having combinations of different metal oxides. Some of these combinations are difficult to obtain by other means. For example, alkali metals and alkaline earth metals are unstable on their own, but combining oxides of alkali metals and alkaline earth metals with oxides of transitional metals yield porous ceramics 18 having interesting properties.
A number of properties of porous ceramic 18, including porosity, average pore size, relative density, shrinkage and compressive strength can be tuned based on the types of ceramic precursor 12 and pore-forming material 14 selected, the final target temperature, the duration of treatment at elevated temperature, and the presence of any additional materials. The porosity of porous ceramic 18 formed according to the present invention can range from about 50% to about 85%. By varying the size of pore-forming material 14, one can vary the size of pores 20 within porous ceramic 18. According to International Union of Pure and Applied Chemistry (IUPAC) definitions, micropores have widths smaller than 2 nm, mesopores have widths between 2 nm and 50 nm, and macropores have widths larger than 50 nm. The average pore size of pores 20 within porous ceramics 18 can vary between about 2 nm and about 5000 μm. In some embodiments, the average pore size of pores 20 is between about 100 μm and about 1000 μm. The transverse compressive strength observed for porous ceramic 18 can range from about 0.5 MPa to about 14 MPa. The longitudinal compressive strength observed for porous ceramic 18 can range from about 0.3 MPa to about 6.5 MPa. The Examples that follow demonstrate the effect that the types of ceramic precursor 12 and pore-forming material 14 selected, the final target temperature, and the duration of treatment at elevated temperature have on the formed porous ceramics 18.
Table 1 illustrates the amounts of ceramic precursors and pore-forming materials used in the samples prepared and tested. Vfp refers to the volume fraction of the pore-forming material within a mixture.
3.5 grams of titanium (obtained from Alfa Aesar, Ward Hill, Mass.) was mixed with 0.5 grams of polyethylene (obtained from Sigma Aldrich, St. Louis, Mo.) in a ball mill (8000 M mixer mill, SPEX SamplePrep, Metuchen, N.J.) for 5 minutes. The mixtures were cold pressed using a laboratory press (Model 3853, Carver Inc., Wabash, Ind.) at a pressure of about 86 MPa. The pressed mixture was heated in a tube furnace (Model GSL-1100 X, MTI Co., Richmond, Calif.) at a rate of 5° C./min to 900° C. A control sample of pure Ti powder (no PE) was also prepared as described above.
Table 2 illustrates additional test parameters and some of the results obtained from the formed porous ceramics. In Table 2, the calculated porosity was corrected for those samples containing unreacted carbon.
The amount of ceramic precursor (Ti and Ni, obtained from Alfa Aesar, Ward Hill, Mass.) indicated in Table 1 was mixed with the amount of pore-forming material (PE and graphite, obtained from Sigma Aldrich, St. Louis, Mo.) indicated in Table 1 in a ball mill for 5 minutes. The mixtures were cold pressed using a laboratory press at a pressure of about 86 MPa. The pressed mixture was heated in a tube furnace at a rate of 4° C./min to the temperature listed in Table 2. The sample was kept at the listed temperature for the amount of time indicated in Table 2.
The porous ceramics obtained were evaluated. Weight and dimensions were measured before and after heat treatment. The dimensions of the samples were measured using a Vernier caliper. Positive shrinkage values in Table 2 reflect expansion while negative values indicate shrinkage. X-ray diffraction (XRD) patterns were collected from 10-90° (2) with a 0.02° step size and 1 second count time using a Rigaku Ultima IV X-ray Diffractometer (obtained from Rigaku Americas, The Woodlands, Tex.) with Cu—Ka radiation operated at 40 kV and 44 mA. Compressive strengths were measured using an AG-50 Universal Testing Machine (obtained from Shimadzu) at a deflection rate of 1 mm/min. Reported compressive strengths are the average of at least 3 samples. The transverse direction is perpendicular to the direction mixture 10 was compressed, and the longitudinal direction is parallel to the direction mixture 10 was compressed. The microstructure of the samples was studied using a Hitachi S-3400 N scanning electron microscope (SEM, obtained from Hitachi, Schaumburg, Ill.).
While the invention has been described with reference to exemplary embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiments disclosed, but that the invention will include all embodiments falling within the scope of the appended claims.