The object of the current invention is a sol-gel method for preparation of metal oxide ceramic microtubes. Tubes are applicable for pumping liquids and gasses under 0-10000 atm difference of pressure applied inside the tubes compared to pressure applied outside the tubes in temperature range from 2 to 2000 K, as construction materials, as nozzles to generate liquid droplets or jets, as ion-conducting membranes to separate electronically conductive materials from each other, as light emitters, as carriers of catalyst particles and as optical or electrical gas sensors. The tubes are synthesised from precursor materials based on metal alkoxide, which contains 0-50% of solvent. The precursor is transformed to jets in a gas or liquid environment. The tubes form as a result of chemical processes caused by the humidity of the environment.
Several methods are proposed as prior art for preparation of 3-D ceramic micro-materials including microtubes. One of the methods, widely applied for preparation of micro tubular ceramic materials, is based on using organic or anorganic fibres, different membranes, ionic liquids [11] etc. as templates [1,2,3,4,5,6,7,8,9,10]. These templates are covered by a layer of ceramic materials by using sol-gel technology [5,12,13], coating of the surfaces by different mixtures of ceramic precursors [1,4], chemical vapour deposition (CVD) processes [15,16,17], laser deposition processes [1,8], thermal vapour deposition [1,9], layer by layer adsorption coating [20,21], electrophoretic deposition [22,23], hydrothermal deposition [24] or some other methods. The tubes are obtained when the template at the core of these structures is removed. This can be done by using burning, melting or dissolving of the template (
Another known method for preparation of ceramic tubes is extrusion, which enables to prepare hollow ceramic materials by pressing viscous-elastic precursor materials into a suitable shape mold. The tubes can also be prepared by pressing the precursor trough a suitable shape nozzle. Solidification of precursor is achieved as a response to cooling, chemical reaction or chemical reaction caused by UV radiation [25, 26, 27, 28, 29, 30, 31]. Minimal dimensions of materials obtained by extrusion remain in the 1 mm range defined by the dimensions of the mold or nozzle. The obtained fresh tubes are sintered at elevated temperatures to increase their density, to remove the additives and to increase the strength and hardness of the material. Extrusion is the most widely applied top-down approach for preparation of metal oxide ceramic materials. It's cheap to apply the technology in macro scale. However, the method cannot be applied for the preparation of microtubes, which have an inner diameter below 100 μm as in addition of miniature nozzles (diameter 100-1000 μm), advanced precursors are also desired. For that, the precursor should be homogenous in nano scale containing no particles bigger than 1-2 μm. Moreover, the precursors should have suitable viscous-elastic properties to avoid the collapse of freshly extruded structures under the high surface energy of the precursor. All those requirements make the method too expensive to apply to produce tubes in micro scale. Therefore the extrusion method is in use for preparing tubes with rather large diameters (5-200 mm). Disadvantage of the method is that freshly pressed tubes are soft and difficult to handle in further processing [32].
Metal oxide microtubes can be milled out from larger size monoliths. It can be done by cutting mechanically or by using an electron or ion-source. This method enables preparing the tubes made of almost all metal oxide materials including their very hard monocrystalline forms. The drawback of the method is its costly nature as exact mechanics and cutting tools and working in high vacuum are needed.
The method to build up the tubes atom by atom or molecule by molecule as a result of self-formation processes is known as bottom-up approach for materials preparation. The tubes form as energetically most favoured structures. Diameter of the tubes is defined by the size of catalysing particles. The method is suitable for preparation of very small nanotubes in diameter range from 1 to 100 nm. The formation of tubes with a bigger diameter is energetically unfavoured as growth remains too low and the number of defects in the tube structure increases.
Widely-known method for the preparation of tubes is based on roll-up of thin layers of materials. The conditions have been suggested for self-formation of metal oxide ceramic tubes in micro-scale. For that, the selected substrate is coated with a metal oxide precursor. The tubes can roll up when the substrate is removed, which can be done by dissolution or mechanical cleaving. Roll-up process is supported by the tendency of materials to minimize their surface energy [33]. The parameters (length, wall thickness, and diameter) of the tubes are controlled by the length and thickness of the initial film piece and the selection of solvents. A drawback of the method is that the tubes which form have an open edge, wherefore they cannot be applied to pump liquids nor gasses under pressure.
Known method for preparation of different shape 3-D ceramic structures, including microtubes, is microstereolithography [34]. Process is controlled by using, e.g. a laser-beam. Structures are grown-up layer by layer. The method is rather expensive as it needs exact mechanics. As the final structures are achieved by growing them layer by layer, the process is also time consuming.
The use of sol-gel technology in preparation of metal oxide ceramic microtubes is known as a part of prior art. The function of sol-gel processing in those methods is to coat templates with thin metal oxide films [5, 6, 35].
The method to use sol-gel processes in preparation of metal oxide microtubes without using templates is known as a part of prior-art [36]. The process is carried out by using a precursor made from a mixture of Ti(i-OPr)4 and 2-propanol. Viscosity of the mixture is grown into 10-30000 P range that is required for drawing fibres. Increased viscosity of precursor material is achieved when it is left in the vessel, open to air humidity, for 1-2 days. The material in contact with air humidity undergoes chemical processes which lead to growth and agglomeration of particles of neat Ti(i-OPr)4, resulting in increased viscosity of the system. Fibres are pulled from the mixture 0.5-1.5 h prior to its final gelation. For pulling fibres, pulling speed 0.1-1 m/s is applied. More than 1.5 h prior to gelation, the viscosity is not suitable for pulling fibres due to too low viscosity (below 10 P). Pulling fibres from such a mixture is not possible as high surface tension of the matter leads to a collapse of the jets prior to their solidification when less time is left until final gelation of the mixture the viscosity grows too high (30000 P or more). This causes a break-up of the jets under cohesive forces as the material doesn't exhibit elongational behaviour when external forces are applied. Parameters of the method are defined by the concentration of solvents, acidity-alkalinity of mixture, air humidity, temperature and time.
For the preparation of microtubes (hollow fibres), it is needed to generate gas bubbles into the mixture prior to drawing the fibres. This could be done by mixing the solution intensively in the bulb with a rod for 5-10 minutes. The mixture is transformed into jets by using drawing or pressing through a nozzle or by using some combination thereof like extrusion or electrospinning. When electrospinning is applied, the material is pressed through the nozzle, whereafter it is additionally drawn by using electrostatic external forces. The tubes form when the bubbles which remain in the jet start to grow as a response to the decrease of the volume of the matter that is undergoing chemical processes. The bubbles grow and fuse together and finally form a hollow region in the centre of the structure.
The process for preparing tubes in this way is demonstrated on
The method enables to prepare TiO2 tubes which have outer diameters in the 50-200 μm and inner diameters in the 5-90 μm ranges.
Described process is technologically simple. Obtained tubes have optical quality and they are transparent, which proves nano scale structural homogeneity of the tube material. A drawback of the method is that it enables to prepare tubes with diameter in narrow region from 50 to 200 μm. Tubes with larger diameters crack during the thermal annealing process. Minimal diameter of the tubes is defined by the size of the bubbles. In addition, the solidification of jets less than 50 microns in diameter is too quick to fuse the bubbles together. It could be seen from illustrative images (
Current invention is an improved method for preparation of metal oxide microtubes. The formation of tubes in accordance with the current invention starts by formation of a solid shell on the surface of a viscous (10-30000 P) jet obtained by direct drawing or extrusion through a nozzle or by using any combination thereof. The solid content inside the precursor is in the form of metal alkoxide or metal oxo-alkoxide. The nature of chemical processes which lead to the formation of tubes is similar in both cases, being initiated by air humidity. The process differs from the prior art in the following:
Using the method disclosed in the current patent following materials can be obtained:
The present invention is illustrated with detailed Figures, where
A precursor which is a mixture comprising metal alkoxides (for example Hf, Zr, Ce, Al, V alkoxides), metal-organic compounds (metals from the lantanoid group in combination with etoxide, propoxide, iso-propoxide, butoxide, tert-butoxide, pentoxide) or metal salts and a high boiling-point solvent, should have a viscosity in the range from 10 to 30000 P. To achieve named viscosity is used in the mixture the high boiling-point (boiling point above 150° C.) organic solvent. For preparation of the tubes the precursor is drawn or pressed into jets through nozzles by applying a pulling speed of 0.1-1000 m/s. When the viscosity of precursor is below 10 P then it is not possible to convert the material to the form of stable jets. When viscosity is higher than 30000 P then the jets start to break off due to cohesive forces as the materials do not exhibit any more elongational behaviour.
When directing the precursor material according to the present invention having viscosity from 10 to 30000 P into jets in a humid environment the surface of the jets starts to solidify by a polycondensation process, which leads to the formation of a three-dimensional network of precursor particles forming a rigid solid shell on the surface of the jet. The thickening of the rigid solid shell continues by consuming solid content of the precursor material to form a thicker shell wall until a microtube is formed, which is filled by a liquid phase of released organic substances contained in the precursor material. Thereafter the microtubes are aged in a gaseous environment for removal of the organic substances from the hollow core thereby densifying the wall material of the microtube. To obtain a stable tetragonal or cubic structure of microtube material the microtubes are heated after at 500-1000° C. for at least 2 hours. In alternative embodiment to stabilise the tetragonal or cubic phase of the material during forming of the microtubes the stabilizing compound is added to the precursor material before preparing the microtubes The stabilising compound is selected for example from compounds comprising metal from the third group of the periodic table, like Y or Sc. In addition the precursor material can be doped with a fluorescent compound before preparing the microtubes where the fluorescent compound is selected for example from the group comprising rare earth elements, quantum nano-dots or organic molecules, or a mixture thereof.
Only jets in the diameter range from 1-500 μm are used in preparation of the tubes. These jets can be prepared by using direct drawing, extrusion, electrospinning etc. Smaller diameter jets convert into fibres, not tubes, or collapse under the relatively high surface tension of the jets. Jets with larger diameters crack during the transition into tubes. Transformation of the jets into solid metal oxide microtubes is carried out in humid liquid or gas environment as a result of a reaction between precursor material and water vapour.
Mixture of 5 g Zr(OBu)4 and 5 g 1-butanol is made in a 100 ml reaction bulb. After 5 min of vigorous stirring, 5% Y(NO3)3 solution in 1-butanol is added dropwise into the solution. Addition of yttrium is carried out until the solution reaches atom ratio Y/Zr in range from 1/100 to 1/3. Subsequently, water, acidified by two drops (15-20 mg) of 35% HCl water solution is mixed into the solution as a solution in 10-15 ml 1-butanol. Water solution is added drop-by-drop during 10 minutes, stirring the solution vigorously at the same time, until water/butoxide molar ratio up to 0,9 is reached. After mixing all the components, the solvents are evaporated from the mixture and a precursor material ready for use in further experiments is obtained. Viscosity of obtained precursor remains in the range of 500 to 1000 P.
To prepare the tubes, the precursor is pulled into jets with length at least 0.5 cm by using a form of direct drawing. Surface of the jets solidifies in 0.001-1 second at 22° C. when relative air humidity is between 20-30%. Tube formation (formation of tube walls) continues for 5-10 minutes after fiber pulling. After that the tubes are left to age for two days in air as a first step of post-processing. Aging is needed to remove the organic substances from the core and to densify the solid material. For final densification of the material, the tubes are heated at 800-1000° C. Heating is important to obtain a stable tetragonal or cubic structure of material. Obtained microtubes are optically homogenous (applicable as waveguides), ion-conductive at temperatures above 300° C., mechanically and chemically stable. Tensile strength of the tubes ranges from 500 to 1000 MPa. Obtained tubes are stable in applications carried out in temperature range from 2-1500 K.
Mixture of 5 g Zr(OPr)4 and 5 g 1-propanol is made in a 100 ml reaction bulb. After 5 min of vigorous stirring, 5% Y(NO3)3 solution in 1-propanol is added dropwise into the solution. Addition of yttrium is carried out until reaching atom ratio Y/Zr in range from 1/100 to 1/3. Subsequently, water, acidified by two drops (15-20 mg) of 35% HCl water solution, is mixed into the solution as a solution in 10-15 ml 1-propanol. Water solution is added drop-by-drop during 10 minutes, stirring the solution vigorously at the same time, until a water/butoxide molar ratio up to 0,9 is reached. After mixing all the components, the solvents are evaporated from the mixture and a precursor material ready for use in further experiments is obtained. Viscosity of obtained precursor remains in the range of 500 to 1000 P.
The preparation of tubes from the precursor material and post-processing of tubes are carried out as described in Example 1. Properties of obtained tubes are similar to those described in Example 1.
Mixture of 5 g Hf(OBu)4 and 5 g 1-butanol is made in a 100 ml reaction bulb. Subsequently, water, acidified by two drops (15-20 mg) of 35% HCl water solution, is mixed into the solution as a solution in 10-15 ml 1-butanol. Water solution is added to the mixture drop-by-drop during 10 minutes, stirring the solution vigorously at the same time until a water/butoxide molar ratio up to 0.7 is reached. After mixing all the components, the solvents are evaporated from the mixture and a precursor material ready for use in further experiments is obtained. Viscosity of obtained precursor remains in the range of 500 to 1000 P.
The preparation of tubes from precursor material and post-processing of tubes are carried out as described in Example 1. Obtained microtubes are optically homogenous, mechanically and chemically stable. Tensile strength of tubes ranges from 50 to 1000 MPa.
In order to prepare CeO2 tubes, a material based on pure, untreated Ce(OBu)4 is used. The use of Ce(OBu)4 directly in experiments is possible as this alkoxide possesses suitable viscous-elastic properties for jet pulling, for which no additional polymerisation by adding water is necessary.
The preparation of tubes from the precursor material is carried out as described in example 1. For final densification of material, the tubes are heated at a temperature between 600-900° C. Heating is important to transform the material into stable nanocrystalline form.
Precursor material is prepared as described in Example 1. To prepare the tubes, precursor is pulled into jets in air by using a direct drawing method. The surface of the jets solidifies in 0.001-1 second at 22° C. when relative air humidity is between 20-30%. 10 seconds after jet pulling, the fibres are submerged into a dimethyl sulfoxide (DMSO) solution, containing 2-3% of water to induce hollowing of the fiber. Tubes form within 10 minutes after submerging as a result of reactions with the water in the solution. Reactions end within 1 h, after which the tubes are left to age for two days in air at temperature 22° C. as a first step of post-processing. Aging is needed to remove organic materials from the hollow core and to increase the density of the materials. For final densification of the material, the tubes are heated at 800-900° C. Heating is important to obtain a stable tetragonal or cubic structure of the material. Obtained microtubes are optically homogenous (applicable as waveguides), ion-conductive at temperatures above 300° C., mechanically and chemically stable. Tensile strength of tubes ranges from 50 to 1000 MPa.
Precursor material is prepared as described in examples 1-5. Jets are generated by pressing the precursor material through a nozzle with a 10-500 μm inner diameter. The resulting jet is spinned on the drum or stretched by gravity. After that the jets are exposed to a humid environment so that tubes' formation can proceed as described in examples 1-5. Post-processing of tubes (ageing and heating) is carried out as described in examples 1-5. The tubes can, for example, be applied in any of the following applications:
Number | Date | Country | Kind |
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P201000097 | Dec 2010 | EE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP11/74333 | 12/31/2011 | WO | 00 | 10/1/2013 |