CERAMIC COMPOSITE FOAMS WITH HIGH MECHANICAL STRENGTH

Abstract: The present invention relates to a ceramic foam structure characterized in that it is produced by using a reaction bonded power. The invention also relates to a method for producing a ceramic foam structure, characterized in that the method comprises the following steps: providing a reaction bonded power blend, producing a stable slurry of the powder blend in water or in a solvent, producing a foam, drying said foam, calcinating said foam, oxidizing said foam, and a final thermal treatment. Using this method, ceramic foams having better mechanical properties compared to classical foams can be prepared.

Description: Ceramic composite foams with high mechanical strength Field of the invention [0001] The present invention relates to ceramic composite foams with high mechanical strength, more particularly ceramic composite foams formed with reaction bonded (RB) materials (metals and metal oxides) and through a thermal treatment (slow oxidation) typical of this reaction bonded production way. State of the art [0002] Ceramic foam structures are porous materials with a very low density (from 10 to 20% theoretical density (TD) ) which are used m a wide range of applications such as filters for melt metals, furnace liners, soot filters, catalyst substrates, biomedical implants, electro-ceramics, etc. Ceramic foam structures are disclosed by L.M. Sheppard, "Porous Ceramics : Processing and Applications", pp. 3-23 m Ceramics Transactions, vol.31, Porous Materials, ed. by K. Ishizaki, L.M. Sheppard, S. Okada, T. Hamasaki, and B. Huybrechts, ACS, Westerville, OH, 1993 and by L. Montanaro, Y. Joyrand, G. Fantozzi and A. Negro "Ceramics Foams by Powder Processing" J. Eur . Ceram. Soc. 18 (1998), 1339-1350. [0003] Each new application requires specific properties such as a determined cell size, a satisfactory thermal shock strength, a mechanical strength and/or a determined resistance to crack propagation (toughness) . These two latter properties limit particularly a quick development, mainly m structural applications where an optimum strength/weight ratio is desired. [0004] Nowadays about 10 ceramic materials are commercially available as foams. The choice of the material type depends upon the specific properties. The most currently used production method for these foam structures is the PU-replica method wherein a soft PU- foam is dipped into a ceramic slurry. After elimination of the excess slurry and drying, the PU-foam is burnt off and, after sintering, a ceramic foam is obtained. [0005] This method has the advantage that the cell size of such structures can be easily adapted by starting from another PU-foam having the appropriate cell size. [0006] One inconvenience is the less satisfactory mechanical properties. Drying and burning off should be carefully carried out m order to prevent crack formation. Besides, "struts" (ribs) also occur naturally with typical prism-shaped cavities due to burning off of the PU-struts. This also is obviously an additional weakness for the foam structure. [0007] In another method, such as gel casting, somewhat better mechanical properties are observed with specific cell sizes. But, m this case, there are more problems to obtain a determined cell size. [0008] Nevertheless, whatever the production method is, the lifetime of foam structures m a number of applications is mainly limited due to their lack of mechanical strength. [0009] A reaction bonded composite material, manufactured and thermally treated m the right way has a strength which is normally twice to three times higher than a similar material produced with a traditional method [J. Luyten, J. Cooymans , C. Smolders, S. Vercauteren, E.F. Vansant, R. Leysen "Shaping of multilayer ceramic membranes by dip coating", J. Eur . Ceram. Soc.17, 273-279,1997] . Moreover, such production way is appropriate for incorporating all sorts of phases, providing new composite materials with optimalized properties [N. Claussen, Suxmg Wu and D. Holz, "Reaction Bonding of Aluminum Oxide (RBAO) Composites : Processing, Reaction Mechanisms and Properties, J. Eur. Ceram. Soc. 14 (1994) 97-109] . [0010] The production of dense RB materials is well known, specially disclosed by Prof. Claussen [N. Claussen, R. Janssen and D. Holz, J. Euram. Soc. Japan 103 [8] 749-758 (1995)]. Porous RBAO materials for membrane substrates were developed by the inventors [J. Luyten, J. Cooymans, C. Smolders, S. Vercauteren, E.F. Vansant, R. Leysen "Shaping of multilayer ceramic membranes by dip coating", J. Eur. Ceram. Soc. 17, 273- 279, 1997] . The pore size of such materials (1 μm) is indeed of another order than that of the foam structure (1 mm) . Reaction Bonding, Combustion Synthesis and Reaction Sintering are three different notions which should not be confused. [0011] In Reaction Bonding, the starting point is a blend of metal and/or metal oxide powders, which, after shaping, are allowed to react m a controlled way with a gas. For an Al/Al 2 0 3 powder blend for example, after shaping, air heating is very slowly performed while the Al-fraction is oxidized, forming a fine A1 2 0 3 granule network. This oxidation is completed at 900°C, but time and temperature obviously depend upon the thickness and density of the green starting core. In order to avoid cracking, such heating step should be performed slowly. Such oxidation is not accompanied with a densification of the piece, but with an expansion. Further heating provides for the necessary contraction and densification of the material . [0012] By Reaction Sintering it is meant a reaction of different materials m a solid state at a high temperature (> 1000°C), whereby beside the generation of new compounds, a densification of the material also occurs. An example thereof is the conversion of Al ^ C 3 and Sι0 2 into mullite (Al 6 Sι 2 0 ι3 ) . [0013] A filter and a method for obtaining such a filter through reaction sintering are disclosed m WO 98/25685. [0014] Combustion Synthesis is a production method wherein the starting point is ceramic precursors based on polymers. After shaping, a pyrolysis at high temperature (> 1000°C) is carried out m which a reaction occurs with the released carbon. An example is to heat silane compounds into ceramic material SiC through reaction of Si with C. [0015] Porous membranes and methods for obtaining such membranes are disclosed in WO 96/06814, WO 96/00125 and US 5 279 737. The disclosed method is each time a combustion synthesis. [0016] Other references include J. Saggio-Woyanski , C.E. Scott, WP Minnear, "Processing of Porous Ceramics" Amer. Ceram. Soc. Bull., vol. 71, n° 11, nov. 1992, pp. 1674-81 and P. Sepulveda, "Gelcasting foams for porous ceramics", Amer. Ceram. Soc. Bull., vol. 76, n° 10, oct. 1997,61-66. Aim of the invention [0017] In order to enhance application possibilities for ceramic foams, to extend their lifetime and to improve them qualitatively for the today application field, it is necessary to develop new strong ceramic foam structures starting from a modified production method and new material compositions. [0018] Accordingly, the invention aims to produce a ceramic foam having improved mechanical strength. Summary of the invention [0019] The present invention relates to a ceramic foam structure characterized in that it is produced from a reaction bonded powder. [0020] The foam structure can be open or closed. The reaction bonded powder comprises two or more elements selected from the group consisting of metal and metal oxide . [0021] Preferably, the average pore size is higher than 10 μm. [0022] Preferably, the 4p bending strength is higher than 2 MP . [0023] A second aspect of the present invention is a production method for producing a ceramic foam structure, characterized m that the method comprises the following steps: • providing a reaction bonded powder blend with metal and/or metal oxides, • producing a stable slurry of the powder blend m water or m a solvent, • producing a foam, • drying said foam, • calcinating said foam, • oxidizing said foam through slow air heating up to a final temperature between 900°C and 1100°C, and • a final thermal treatment . [0024] The foam production is preferably done through a technique selected from the group consisting of polyurethane replica technique and gel casting method. [0025] Providing the reaction bonded powder blend can be done by grinding the metal and/or the metal oxides m a solvent . The solvent for performing the method of the present invention is preferably selected from the group consisting of acetone, ethanol and methanol . [0026] In a preferred embodiment, the oxidation step comprises a step wherein the foam is maintained at the final temperature for one hour. The final thermal treatment may comprise a sintering step at a temperature comprised between 1600°C and 1700°C. [0027] The ceramic foam structure according to the present invention may be obtained with such method. [0028] Using this method, ceramic foams may be prepared which show better mechanical properties compared to traditional foams. Detailed description of the invention [0029] Bulk reaction bonded materials are a new kind of materials with a higher strength and which allow easily the incorporation into the structure of K 1C (crack propagation factor) enhancing phases. [0030] Consequently, the invention comprises on one hand producing new porous RB ceramic composites and on the other hand converting them, using one of the current methods, into a ceramic foam structure. [0031] The starting point here is a reaction bonded powder (i.e. a blend of metal and metal oxides), and the PU (polyurethane) replica method or the gel casting method is used. [0032] A possible flowsheet of a method according to the invention is shown m Fig. 1. [0033] Moreover, the production method offers the possibility to integrate m a simple way all kinds of phases into the matrix material. Thus, beside the mechanical strength, the requirements of a specific application may be satisfied. [0034] Combining different metals and metal oxides provides materials with a wide range of new properties and consequently of new possibilities. [0035] Producing powders, conditioning them and treating them thermally should be adjusted depending upon the composition of the composite. [0036] Preparation of the slurry should also be considered depending upon the composition, i.e. the additives are typical of the specific composition of the starting powder and of the applied producing way for producing a foam structure. If possible, an aqueous solution is preferred (environmental aspect) . [0037] The new proposed process comprises the following novelties compared to the traditional methods : a. the starting point is a blend of metals and metal oxides, b. they are conveniently conditioned, for example ground m acetone, c. preparing a stable suspension of a metal/metal oxide blend involves special requirements as to the producing method and the additives to be added, d. depending upon the selected production path for producing the green foam, new additives should be added, e.g., if the PU-replica method is used, a wetting agent should be added, while for the gel casting method a foam stabilizing agent should be used, etc . , e. the oxidation and final treatment should be performed with a sufficiently slow heating speed and with different temperature plateaus m order to allow for the conversion of metals into oxides to be completed and without crack formation. Such oxidation is mainly performed under 1000 °C. Example 1 Producing an appropriate powder blend [0038] An Al/Al 2 0 3 blend m a 40/60 ratio by weight is intensively ground m a solvent (acetone, ethanol, methanol , ...) . This may be done using an attritor and/or a planetary ball mill. Example 2 Producing a stable slurry [0039] The stable slurry may be prepared m a solvent such as acetone, ethanol or methanol, or m water. When using water, an Al/Al 2 0 3 powder blend should be first passivated so as to prevent hydrolysis and therefore H 2 generation. This can be done for example by adding an excess dispersing agent (e.g. Darvan C) . The dispersing agent is absorbed on the Al surface and protects it from water. [0040] Classical additives such as dispersing agents, an anti-foam agent, a wetting agent etc. are preferably added m order to optimize the properties. Example 3 Producing a new RB mullite structure Example of a porous reaction bonded composite structure [0041] Two compositions are used as starting points: AI/AI 2 O 3 /S1 and Al/Si/Al 2 0 3 /Zr0 2 [0042] Extra Zr0 2 is added m the second composition m order to increase strength and because it improves the wetting of Al with Al 2 0 3 [0043] Both compositions are ground m acetone m a planetary ball mill with Zr0 2 balls. [0044] The starting powders and the grinding time are selected m such a way that a porous structure is obtained after shaping (extrusion) and sintering (oxidation, mainly under 1000°C, and final thermal treatment) . XRD analysis shows formation of mullite with some Al 2 0 3 and Zr0 2 m the first composition, and mullite, Zr0 2 and some Al 2 0 3 m the second composition. Free Sι0 2 is no longer found, on the contrary, a full conversion into mullite occunng at temperatures not exceeding 1500°C is observed. The porosity is 35 to 40%, the maximum pore size is 2 μm and 4p bending strengths m the range from 50 to 100 MPa are obtained. Example 4 Producing a RBAO (Reaction Bonded Al 2 0 3 ) foam using the polyurethane replica technique [0045] A1/A1 2 0 3 50/50 vol% are intensively blended/ground under acetone. This powder is dispersed, after passivation, m water with Darvan C™ as a dispersing agent and gelatine as a wetting agent. The water/solids ratio is adjusted so that a little viscous and consequently castable slurry is obtained. [0046] A PU sponge (30 PPI) from Recticel company (Wetteren, Belgium) is dipped into this slurry. The excess slurry quantity is expressed from the sponge after which the assembly is dried. [0047] Slow air heating is subsequently carried out up to 1100°C, whereby the polyurethane is burnt off at a temperature lower than 500°C and the oxidation of the powder metal fraction starts simultaneously. Some oxidation is terminated at 900°C. Further heating up to 1100°C offers a limited presintering which allows handling the foams carefully. [0048] A final sintering operation for one hour at a temperature comprised between 1650 and 1700°C results in a 2.9 MPa three point bending strength for a foam having a cell size of approximatively 1.3 mm and a density in the range between 15 and 20% TD . [0049] An identical example may be presented, wherein the shaping operation, here the Pu-replica method, is replaced by gel casting. [0050] Generally speaking, the following can be stated regarding the temperatures and times that are used for the oxidation and sintering steps: • Oxidation: after the slow heating step, the material is heated for one hour at a temperature comprised between 900°C and 1100°C. The precise temperature depends upon the granularity (and therefore the reactivity) of the powder. • Sintering: sintering is completed by maintaining, in a final step, the material for one hour at a temperature comprised between 1600°C and 1700°C, depending upon the starting material and the desired final density.

Claims: CLAIMS 1. A method for producing a ceramic foam structure, characterized m that the method comprises the following steps: • providing a reaction bonded powder blend with metal and/or metal oxides, • producing a stable slurry of the powder blend m water or m a solvent, • producing a foam, • drying said foam, • calcinating said foam, • oxidizing said foam through slow air heating up to a final temperature comprised between 900 °C and 1100°C, and • a final thermal treatment. 2. The method according to claim 1, characterized m that the production of the foam is done through a technique selected from the group consisting of the polyurethane-replica technique and the gel casting method. 3. The method according to claim 1 or 2, characterized m that providing the reaction bonded powder blend is done by grinding the metal and/or the metal oxides m a solvent . 4. The method according to any one of claims 1 to 3 , characterized m that the solvent is selected from the group consisting of acetone, ethanol and methanol . 5. The method according to any one of claims 1 to 4, characterized m that the oxidation comprises a step wherein the foam is maintained for one hour at the final temperature. 6. The method according to any one of claims 1 to 5, characterized in that the final thermal treatment comprises a sintering step at a temperature comprised between 1600°C and 1700°C. 7. A ceramic foam structure characterized in that it can be obtained through the method according to any one of claims 1 to 6. 8. The ceramic foam structure according to claim 7, characterized in that the foam structure is open or closed. 9. The ceramic foam structure according to claim 7 or 8 , characterized in that the average pore size is higher than 10 μm. 10. The ceramic foam structure according to claim 7 or 9, characterized in that the 4p bending strength is higher than 2 MPa.

Inventors: COOYMANS JOZEF, LUYTEN JAN, SMOLDERS CARINA, COOYMANS, JOZEF, LUYTEN, JAN, SMOLDERS, CARINA
Applicants: COOYMANS JOZEF, LUYTEN JAN, SMOLDERS CARINA, VITO, COOYMANS, JOZEF, LUYTEN, JAN, SMOLDERS, CARINA, VLAAMSE INSTELLING VOOR TECHNOLOGISCH ONDERZOEK
Application year: 2001
Main classification: C04B38
IPC codes: B28B1, C04B38