Patent Application
20230150825
The present invention relates to a hybrid aerogel and a method for producing the same.
The present invention also relates to a thermal insulation material using a hybrid aerogel.
An aerogel is a material first published in 1931 (see NPL 1) and is generally defined as a porous material produced by replacing liquid content in a wet gel with gas by supercritical drying or atmospheric pressure drying while causing substantially no shrinkage (see NPL 2 and NPL 3). Methods for producing an aerogel are described in, for example, PTL 1 and PTL 2. Silicon dioxide is generally synthesized in a sol-gel process or a Stober process. As described in PTL 3 and PTL 4, for example, an aerogel is used as a thermal insulation material when placed between laminates.
Since an aerogel has the lowest thermal conductivity among other self-supporting solids, potential application thereof to thermal insulation materials has been studied (see PTL 3 and PTL 4, for example). To provide specific numerical values, while general thermal insulation materials have thermal conductivity of approximately 20 mW/(m·K) to 45 mW/(m·K), aerogels are often reported to have lower thermal conductivity, which means to have higher thermal insulation performance. Such extremely low thermal conductivity that is highly desirable for thermal insulation materials can be achieved as follows: in an aerogel structure, an aerogel skeleton partitions the space uniformly to form pores, so that neither gas convection nor thermal momentum exchange of molecules occurs inside the aerogel. The mean free path of nitrogen molecules, which is a main component of the atmosphere, at ambient temperature and pressure is approximately 70 nm (or 68 nm). This means that thermal insulation performance comparable to vacuum insulation can be achieved by partitioning the inside of an aerogel into spaces smaller than the mean free path of nitrogen molecules.
While aerogels are materials of extremely low density, putting them to practical use have involved difficulties due to their weakness, vulnerability and breakability. Therefore, mechanically strong novel aerogels are needed in engineering applications such as highly thermal insulation windows, novel filters, ultra-thin walls for refrigerators, and highly thermal insulation materials for buildings. To attain above goal, hybridized aerogels reinforced with fibers or other organic molecules have been studied, but one with sufficient properties has not yet to be achieved.
An objective of the present invention is to provide a mechanically strong, highly thermal insulation, and practically usable hybrid gel made from an extremely low density material.
An objective of the present invention is to provide a highly thermal insulation aerogel. More particularly, an objective of the invention is to provide a hybridized aerogel having a high porosity, and having a structure for further controlling gas flows through the pores.
As expected from the process of producing an aerogel, individual pores in an aerogel are connected with each other, causing slight gas flows within the aerogel. The present inventors have focused on heat transfer caused by the slight gas flows, and conceived an idea that it would be possible to further lower thermal conductivity of an aerogel by producing a hybridized aerogel in which other materials for blocking or reducing gas flows are mixed.
[1] The hybrid aerogel of the invention comprises, as illustrated in
[2] In the hybrid aerogel of the invention, preferably, the nano-size hollow particles may be 0.01% by weight or more and 30% by weight or less, and the balance may consist of the aerogel.
[3] In the hybrid aerogel of the invention, preferably, gas flow paths blocked by the shells of the nano-size hollow particles may be 10% or more and 90% or less with respect to the gas flow paths formed by the communication of the pores of the aerogel.
[4] The hybrid aerogel of the invention includes, as illustrated in
[5] In the hybrid aerogel of the invention, preferably, the micro-size hollow particles may be 0.01% by weight or more and 30% by weight or less, and the balance may consist of the aerogel.
[6] The hybrid aerogel of the invention includes: as illustrated in
[7] In the hybrid aerogel [6] of the invention, preferably, the hollow particles may include at least one of nano-size hollow particles of 30 nm or more and 360 nm or less in outer diameter and micro-size hollow particles of 1 μm or more and 23 μm or less in outer diameter.
[8] In the hybrid aerogel [7] of the invention, preferably, the nano-size hollow particles may be 0.01% by weight or more and 30% by weight or less, and the micro-size hollow particles may be 0.01% by weight or more and 30% by weight or less, and the balance may consist of the aerogel. More preferably, the nano-size hollow particles may be 0.1% by weight or more and 15% by weight or less, and the micro-size hollow particles may be 0.1% by weight or more and 15% by weight or less. More preferably, the nano-size hollow particles may be 1% by weight or more and 10% by weight or less, and the micro-size hollow particles may be 1% by weight or more and 10% by weight or less.
[9] In the hybrid aerogel [7] of the invention, preferably, the nano-size hollow particle may be 0.00003% by volume or more and 17.6% by volume or less, and the micro-size hollow particle may be 0.00003% by volume or more and 22% by volume or less, and the balance may consist of the aerogel. More preferably, the nano-size hollow particles may be 0.0003% by volume or more and 8.1% by volume or less, and the micro-size hollow particles may be 0.0003% by volume or more and 10.6% by volume or less. More preferably, the nano-size hollow particles may be 0.0034% by volume or more and 5.2% by volume or less, and the micro-size hollow particles may be 0.0034% by volume or more and 7.0% by volume or less.
[10] In the hybrid aerogels [1] to[9] of the invention, preferably, the metal of the metal oxide may be a metal or a combination of metals-selected from the group consisting of silicon (Si), aluminum (Al), titanium (Ti), zirconium (Zr), hafnium (Hf), yttrium (Y), vanadium (V), cerium (Ce), lanthanum (La), neodymium (Nd), samarium (Sm), praseodymium (Pr), holmium (Ho) and molybdenum (Mo).
[11] The method for producing a hybrid aerogel of the invention comprises: preparing a metal alkoxide as a precursor; preparing hollow particles consisting of a metal oxide; preparing a colloidal solution by dissolving the precursor and the hollow particles in a solvent; preparing a gel by adding an acid catalyst to the colloidal solution to promote a hydrolysis reaction and a polycondensation reaction to the precursor in a sol-gel process; and drying the gel by supercritical drying with carbon dioxide or by atmospheric drying to produce a hybridized aerogel.
[12] In the method for producing a hybrid aerogel of the invention, preferably, the metal of the metal alkoxide may be a metal or a combination of metals selected from the group consisting of silicon (Si), aluminum (Al), titanium (Ti), zirconium (Zr), hafnium (Hf), yttrium (Y), vanadium (V), cerium (Ce), lanthanum (La), neodymium (Nd), samarium (Sm), praseodymium (Pr), holmium (Ho) and molybdenum (Mo).
[13] The method for producing a hybrid aerogel of the invention includes: as illustrated in
[14] In the method for producing a hybrid aerogel of the invention, preferably, at least one of tetraethoxysilane, trimethoxysilane, tetramethoxysilane, triethoxysilane, tripropoxysilane, tetrapropoxysilane and tributoxysilane may be used as the silicon alkoxide.
[15] In the method for producing a hybrid aerogel of the invention, it is desirable to further include replacing the gas inside the spherical cavities of the hollow particles with gas having thermal conductivity lower than that of the atmosphere.
[16] In the method for producing a hybrid aerogel of the invention, preferably, the hollow particles may be one of micro-size hollow particles, nano-size hollow particles, and a mixture of micro-size hollow particles and nano-size hollow particles.
[17] The thermal insulation material of the invention uses the hybrid aerogel according to any one of [1] to[10].
According to the hybrid aerogel of the invention, it is possible to provide a solid thermal insulation material with highly thermal insulation performance comparable to vacuum insulation and not collapsing even when atmospheric pressure acts thereon.
The invention will be described below with reference to the drawings.
An aerogel is a general term for a dry gel with low density and high porosity, and is a porous body obtained by drying a wet gel. Silica fine particles 10 are secondary particles (20 nm to 50 nm in diameter) formed by weakly bonded silica primary particles (approximately 1 nm to 2 nm in diameter). The silica fine particles 10 have a network structure created by the bonded silica secondary particles with the pores 20 formed among the secondary particles. The weak bonding strength is strong enough to keep the network structure as a gel skeleton.
The pores 20 of the network structure (porous structure) are typically 5 nm to 100 nm in diameter, and 20 nm to 40 nm in average pore diameter. This means that the network structure of a silica aerogel is very brittle.
The “average pore diameter” is obtained by, for example, acquiring an SEM image with a scanning electron microscope (SEM), obtaining a diameter of each pore through image analysis, and calculating an average radius for 100 or more pores as an arithmetic mean value (image analysis). A pore group forming one aggregated particle is counted as one pore.
The pore diameter of a general silica aerogel made from a silica compound is 67 nm or less, which is the mean free path of air at ambient temperature and pressure, and collision of gas molecules (i.e., heat transfer due to convection) rarely occurs within the pore of that size. Therefore, influences of thermal conductivity due to the gas component can be neglected, and thus the silica aerogel is low in thermal conductivity.
Each of the micro-size hollow particles 30 has a spherical hollow portion surrounded by a shell. As shown in Table 1, the range of the outer diameter D of the micro-size hollow particles 30 is preferably between the lower limit of 1 μm, which is approximately 15 times the mean free path λ of air at ambient temperature and pressure, and the upper limit of 23 μm. It is difficult to synthesize micro-size hollow particles with the outer diameter D of smaller than 1 μm. Besides, the wall thickness of those micro-size hollow particles is so thin that gas like carbon dioxide enclosed therein easily leaks out of the particles. Micro-size hollow particles with the outer diameter D exceeding 23 μm have a low thermal insulation effect, and due to its increased particle surface area, gas like carbon dioxide enclosed therein easily leaks out of the particles.
The range of the wall thickness t forming the shell of the micro-size hollow particles 30 is preferably 0.35 μm to 3 μm, and the range of outer diameter d of the pore (the hollow portion) is preferably 0.3 μm to approximately 22 μm.
The micro-size hollow particles 30 have a particle size larger than 15 times the mean free path of air at ambient temperature and normal pressure. Such particle dimension is effective in enhancing the structural strength of the brittle network structure (porous structure) in a hybridized aerogel.
In the hybrid aerogel of the invention, as shown in Table 1, the composition ratio of the micro-size hollow particles is preferably 0.01% by weight or more and 30% by weight or less, more preferably 0.10% by weight or more and 15% by weight or less, and most preferably 1.0% by weight or more and 10% by weight or less. When represented by % by volume, the composition ratio of the micro-size hollow particles is preferably 0.00003% by volume or more and 22.4% by volume or less, more preferably 0.0003% by volume or more and 10.6% by volume or less, and most preferably 0.0034% by volume or more and 7.0% by volume or less.
If the composition ratio of the micro-size hollow particles is less than 0.01% by weight, the micro-size hollow particles leak out of the solution at the production stage of the hybrid aerogel, resulting in a significantly poor yield. If the composition ratio of the micro-size hollow particles exceeds 30% by weight, it is difficult to disperse the micro-size hollow particles uniformly. This means that synthesis of the micro-size hollow particles is difficult.
Each of the nano-size hollow particles 40 has a spherical hollow portion surrounded by a shell. As shown in Table 2, the range of the outer diameter D of the nano-size hollow particles 40 is preferably between the lower limit of 30 nm, which is approximately half the mean free path λ of air at ambient temperature and pressure, and the upper limit of 360 nm, which is approximately five times the mean free path λ of air at ambient temperature and pressure. Nano-size hollow particles with the outer diameter D of smaller than 30 nm pass through a filter, are difficult to synthesize, and have so thin wall thickness that gas like carbon dioxide enclosed therein easily leaks out of the particles. Nano-size hollow particles with the outer diameter D exceeding 360 nm are difficult to synthesize because such large dimension exceeds the limit of core particle formation.
The wall thickness t of the shell of the nano-size hollow particle 40 is preferably in the range of 7.5 nm to 65 nm, and the outer diameter d of the pore (hollow portion) is preferably in the range of 15 nm to 345 nm.
Since the particle size of the nano-size hollow particle 40 includes the mean free path of air at ambient temperature and normal pressure, the nano-size hollow particles 40 greatly contribute to the thermal insulation effect of the hybridized aerogel.
In the hybrid aerogel of the invention, as shown in Table 2, the composition ratio of the nano-size hollow particles is preferably 0.01% by weight or more and 30% by weight or less, more preferably 0.10% by weight or more and 15% by weight or less, and most preferably 1.0% by weight or more and 10% by weight or less. When represented by % by volume, the composition ratio of the nano-size hollow particles is preferably 0.00003% by volume or more and 17.6% by volume or less, more preferably 0.0003% by volume or more and 8.1% by volume or less, and most preferably 0.0034% by volume or more and 5.2% by volume or less.
If the composition ratio of the nano-size hollow particles is less than 0.01% by weight, the nano-size hollow particles leak out of the solution at the production stage of the hybrid aerogel, resulting in a significantly poor yield. If the composition ratio of the nano-size hollow particles exceeds 30% by weight, it is difficult to disperse the nano-size hollow particles uniformly. This means that synthesis of the micro-size hollow particles is difficult.
Each of the hollow particles has a spherical hollow portion surrounded by a shell. The hollow particles are desirably shaped as shown in Tables 1 and 2 according to the two particle types: the nano-size hollow particles 40 and the micro-size hollow particles 30. For example, the ranges of the outer diameter D of the hollow particles are 30 nm to 360 nm and 1 μm to 23 μm respectively, the ranges of the shell thickness t are 7.5 nm to 65 nm and 0.35 μm to 3 μm respectively, and the ranges of the diameter d of the core (hollow portion) are 15 nm to 345 nm and 0.3 μm to approximately 22 μm respectively. When a silica aerogel is used as silica fine particles and a silica aerogel is used as hollow particles, by finely adjusting the diameter of the hollow particles, the mixing rate of the hollow particles in the hybridized aerogel, etc., thermal conductivity of the hybridized aerogel can be made much lower than that (approximately 14 mW/m·K) of the silica aerogel, and even made quite close to those (8.0 mW/m·K) of vacuum insulated panels. That is, when air is enclosed in the hollow particles, thermal conductivity as low as 10.4 mW/m·K is achieved, and when carbon dioxide is enclosed in the hollow particles, thermal conductivity as low as 9.6 mW/m·K is achieved (see
In the invention, the hollow particles are classified into two types: the micro-size hollow particles 30 and the nano-size hollow particles 40.
As shown in Table 3, the density of the micro-size hollow particles is 0.23 g/cm3 to 2.65 g/cm3, the density of the nano-size hollow particles is 0.32 g/cm3 to 2.65 g/cm3, and the density of the entire aerogel is 0.009 g/cm3 to 0.220 g/cm3. The density of the hybrid aerogel of the invention is in the same range of to about half the density of the conventional aerogel (AZO Materials), which is 0.0011 g/cm3 to 0.5 g/cm3.
In a conventional aerogel base material, as illustrated in
In the invention, in contrast, as illustrated in
Further effects will be described in addition to those of the hollow particles noted above. The surface of the hollow particle is covered airtight with a shell so that the gas enclosed in the cavity inside the hollow particle can be retained. When an aerogel is used in usual atmosphere, the gas inside of the communicating pores is the atmosphere without exception. In contrast, when airtight hollow particles are used, gas prefilled in the hollow particles can be retained. In the new structure consisting of a solid skeleton and two types of pores (communicating pores and spherical cavities) formed by dispersing hollow particles in the aerogel, when the hollow particles are filled with gas (Xenon, CO2, ethylene, etc.) having thermal conductivity lower than that of air, thermal insulation performance of this hybrid aerogel can further be improved.
As a basic knowledge, a general process for producing a silica aerogel will be described.
A silica aerogel is produced by, for example, a sol-gel process or a Stober process.
In the sol-gel process, a solution of a metal alkoxide, as a starting material, is converted into a colloidal solution (sol) through hydrolysis and a polycondensation reaction. By further accelerating the reaction, glass and ceramic are produced via a gel. The sol-gel process, a production method from a liquid phase, has an advantage that raw materials can be mixed homogeneously at a molecular level, and thus it is advantageous of high degree of freedom in composition control.
The Stober process is a process to prepare small glass particles by rapidly reacting a small amount of silicon alkoxide in an ethanol-added alkaline aqueous solution. The particle size can be adjusted by changing the reaction time and the water/silicon ratio. In the conditions for the Stober process, the ethanol/water ratio and the water/silicon ratio are much higher than those in general sol-gel processes. Since the reaction proceeds uniformly in the Stober process, variation in particle size is small.
Next, a process for producing a hybridized aerogel will be described.
Silicon alkoxide or water glass (sodium silicate) as a precursor is first prepared (S100). An inorganic silica aerogel is traditionally produced through hydrolysis and condensation of a silica-based alkoxide (e.g., tetraethoxylsilane) or through gelation of silicic acid or water glass. Other relevant inorganic precursor materials for silica-based aerogel compositions may include, but not limited to, metal silicates such as sodium or potassium silicates, alkoxysilane, partially hydrolyzed alkoxysilane, tetraethoxylsilane (TEOS), partially hydrolyzed TEOS, condensation polymer of TEOS, tetramethoxylsilane (TMOS), partially hydrolyzed TMOS, condensation polymer of TMOS, tetra-n-propoxysilane, partially hydrolyzed tetra-n-propoxysilane and/or condensation polymer of tetra-n-propoxysilane, polyethyl silicate, partially hydrolyzed polyethyl silicate, monomeric alkylalkoxysilane, bis-trialkoxyalkyl or arylsilane, polyhedral silsesquioxane, or combinations thereof.
The inorganic aerogel here is generally formed from a metal oxide or a metal alkoxide material. A metal oxide or a metal alkoxide material can be based on an oxide or an alkoxide of any metal capable of forming an oxide. Such metal may include, but not limited to, silicon, aluminum, titanium, zirconium, hafnium, yttrium, vanadium and cerium.
Next, micro-size hollow particles, nano-size hollow particles, or a mixture of micro-size hollow particles and nano-size hollow particles 40 are prepared as hollow particles (S110).
Then, the precursor and the hollow particles are dissolved in a solvent to prepare a colloidal solution (sol) (S120). The solvent may be, for example, methanol. Hydrolysis and polycondensation reactions proceed in the sol-gel process.
As the dehydration polycondensation reaction of the sol proceeds, the resulting siloxane polymers become linear chain-like structures. The siloxane polymers entangle together to form a three-dimensional network structure, hindering themselves from move around. Therefore, a gel with no fluidity is produced (S130). The sole use of the acid catalyst (excluding hydrofluoric acid) tends to form a gel with low reactivity and low density. Such a gel requires longer time before gelation and the resulting gel contains a large amount of H2O and alcohol as by-products.
Through a drying process of the gel, a hybridized aerogel is completed (S140). Supercritical drying using carbon dioxide, for example, is used for the drying process. Carbon dioxide is often used as a supercritical fluid. Carbon dioxide reaches a supercritical condition under the following conditions: at a critical temperature of 31.1° C. and a critical pressure of 7.38 MPa, which are less strict than those for water. In addition, since supercritical carbon dioxide has high solubility and evaporates and scatters when left at or below a critical point, it is possible to take only a dry sample out.
Ambient pressure drying (APD) may be used instead of supercritical drying. When an aerogel is produced by APD, it may be called a silica xerogel instead.
Double emulsion is defined simply as emulsion within emulsion. Emulsion is a dispersed multiphase system consisting of at least two immiscible liquids. The liquid that forms droplets is called a dispersed phase and most of the liquid surrounding the droplets is called a continuous phase. Double emulsion can be considered as a system in which two liquids are separated by a third liquid that is immiscible with the first two liquids. In the case of water and oil, there are two possible cases of double emulsion: water-in-oil-in-water (w/o/w) emulsion and oil-in-water-in-oil (o/w/o) emulsion. In the case of water-in-oil-in-water (w/o/w) emulsion, for example, each of the dispersed water droplets forms a vesicular structure, with separate single or multiple aqueous compartments forming a continuous aqueous phase layered by an oil phase.
Nano-size hollow particles (NHSPs) are prepared by a soft-template method.
The soft-template method is used to produce porous materials such as nanoporous materials, mesoporous materials and macroporous materials or nanomaterials such as nanospheres, nanorods and nanosheets by using a soft matter such as micelle, emulsion, liposome, polymer blend and liquid crystal as a template. In a hard-template method, in contrast, solid materials such as particles or zeolite are used as templates.
Examples of the hybridized aerogel according to the invention will be described.
Here, parameters of a sodium silicate solution (29.9 g silicon, 144 mmol) are fixed. The total volume of the solution was fixed at 36 mL as an aqueous phase 1 (W1). W1 was added to an oil phase (O1) consisting of a 72 mL of n-hexane solution containing 1.00 g of Tween™ 80 and 0.50 g of Span™ 80. The resulting two-phase solution (W1/O1) was homogenized using a homogenizer (max. 8000 rpm, 1 minute) to produce W1/O1 emulsion. The W1/O1 emulsion was immediately poured while stirring into an aqueous ammonium bicarbonate solution (2 mol·L−1; 250 mL) as a precipitant for the aqueous phase (W2).
Here, Tween™ 80 is also called “Polysorbate 80” or “Polyoxyethylene (20) sorbitan monooleate” whose chemical formula is C64H124O26. Tween™ 80 is a nonionic surfactant and emulsifier commonly used in food and cosmetics, and is a viscous, water-soluble, yellow liquid. Span™ 80 is also called Sorbitan monooleate, whose chemical formula is C24H44O6, and is a surfactant composed of a series of sorbitan esters. Span™ 80 is obtained by esterification of one or more sorbitan hydroxyl groups with fatty acids and is hydrophobic in nature.
After 2 hours of stirring, the W1/O1/W2 solution formed white colloidal suspension. Then the W1/O1/W2-colloidal solution was filtered, washed with deionized water/ethanol, vacuum dried at 120° C. for 24 hours, and calcined at 400° C. to remove excess surfactant. At the same time, micro-size hollow particles (MHSPs) polymerized in powder form were calcined (note: concentrations of sodium silicate, the precipitant and the surfactant in W1, W2 and O1 were unchanged.) The molar ratio of the precipitant to sodium silicate was fixed at 3.5 (precipitant/sodium silicate). W1 and W2 were unchanged (W1/W2=1/7).
Here, a water-based polyelectrolyte such as 40% by weight (wt %) of sodium polymethacrylate (NaPMA) was used as a template agent in an aqueous solution in combination with the catalyzed Stober process as the base. First, 0.40 g of NaPMA (MW˜4,000-6,000) is dissolved in 4.5 mL of ammonium hydroxide (NH4OH, MW˜35.05, 28%, reagent grade). Then 90 mL of ethanol (EtOH, MW˜46.07) is added to the mixture. As aliquots, five equal portions of tetraethylorthosilicate (TEOS, MW˜208.33, 98%, reagent grade) are prepared. 1.80 mL of TEOS was added in portions over 5 hours while vigorously magnetic stirring at ambient temperature.
After 10 hours of aging period, obtained was white colloidal suspension containing approximately 0.92% by weight of silicate particles in the solution. Removal of NH4OH and promotion of shell stability of defined silicate particles were performed by stirring the solution in an open beaker. The colloidal suspension was filtered, and washed three times with deionized water to remove aqueous polymers.
In the producing process of both the micro-size hollow particles (MHSPs) and the nano-size hollow particles (NHSPs), after filtering and washing, colloidal suspension was dried at 120° C. for 24 hours and then calcined at 400° C. to remove aqueous polymer and excess surfactant removal. In this manner, powdered MHSPs and NHSPs were completed by calcination. When drying and calcination were conducted under any required gas environment, any type of gas can be placed inside MHSPs and NHSPs.
Production of Aerogel with Micro-Size Hollow Particles and Nano-Size Hollow Particles Mixed
As illustrated in
A hybrid aerogel precursor was prepared from a mixture of hollow particles, methanol and TEOS. The hollow particles were mixed with methanol and then ultrasonic vibration was conducted for better dispersion of the hollow particles. TEOS was then added to the methanol/hollow particle solution. A total of 6.3 g of oxalic acid (0.01 M) was added to the solution. Finally, 1.5 g of NH4OH (0.5 M) was added to the mixed solution. This mixed solution, also called alcosol, was kept at ambient temperature to allow gelation to occur. After gelation was finished, alcogel was aged in methanol at 60° C. for 12 hours. An excess amount of methanol was added over the gel in consideration of evaporation during drying at elevated temperatures.
Methanol in the alcogel was replaced with a non-polar solvent (hexane). In this step, the alcogel was soaked in hexane at 60° C. for 10 hours. Hexane was replaced with hexane/TMCS for surface modification. TMCS is an abbreviation for trimethylchlorosilane, the chemical formula of which is (CH3)3SiCl, whose Japanese name is chlorotrimethylsilane.
The volume ratio of hexane/TMCS was kept constant at 4. In the surface modification step, the alcogel was soaked in the hexane/TMCS solution at 60° C. for 24 hours. Before drying the alcogel, the sample was soaked in pure hexane to remove the excess TMCS solvent at 60° C. for 6 hours. The final step of aerogel synthesis is drying, and the drying conditions are as shown in Table 4.
Next, the properties of the thus produced nano-size hollow particles will be described.
Next, effects of the size of the communicating pores of the base material and the size of the spherical cavities of the hollow particles will be described. In a free space, gas molecules are moving while colliding with one another. A distance in which a gas molecule can travel straight without colliding with other molecules is called its free path. Each gas molecule has a known average distance it can travel straight without colliding with other molecules at a certain temperature and pressure, which is called a mean free path. Although gas flows cause heat transfer, gas enclosed in a closed space smaller than the mean free path can transfers less heat caused by flowing. Therefore, it is known that the gas enclosed in a closed space smaller than the mean free path behaves as gas molecules having higher thermal insulation performance than those in a free space. Since gas molecules as the highly thermal insulation performance gas collide more frequently in spaces of the size of the mean free path of their own, a higher thermal insulation effect can be exhibited as the closed space becomes smaller. Therefore, hollow particles with small closed spaces may become excellent thermal insulation materials with little heat transfer caused by gas flows in the spherical cavities. In order to form hollow particles, however, shells are necessary as outer walls. If the shell thickness is great with respect to the spherical cavities, solid-state transfer will impair the thermal insulation performance. The optimum shape of the hollow particle will be determined in consideration of these both effects.
In the hybridized aerogel according to the embodiment, when solid transfer is to be reduced, the pore volume increases, and when the pores are communicating pores, heat transfer caused by gas flow increases heat transfer of the entire aerogel. This impairs thermal insulation performance of the aerogel. Further, a structure with all or a part of the communicating pores replaced with spherical cavities has further improved thermal insulation performance compared to a structure only with communicating pores. Here, the effect of improving thermal insulation performance by introducing the hollow particles differs depending on the size of the communicating pores of the original aerogel base material.
In
Further effects of hollow particles will be described. Since the hollow particles have an airtight structure through which gas cannot pass, the gas filled in the cavities of the hollow particles can be retained as it is. When an aerogel is used in usual atmosphere, the gas inside of the communicating pores is the atmosphere without exception. In contrast, when airtight hollow particles are used, gas prefilled in the hollow particles can be retained. When the hollow particles are filled with CO2 (carbon dioxide), a gas known to have low thermal conductivity, thermal insulation performance of the hybrid aerogel can further be improved.
According to the hybrid aerogel of the invention, sound waves entering the hollow parts of the particles reflect repeatedly on inner wall surfaces of the particle for quick dissipation of energy. Therefore, the hybridized aerogel of the invention can be used as a sound absorbing material.
The heat insulation technology using the hybrid aerogel of the invention is a technology that can realize, with a solid (hybrid aerogel) of a thermal insulation material, high thermal insulation performance that have only been achieved by vacuum insulation. Problems of vacuum insulation are as follows: severe limitation on production of its insulation structure; expensiveness; and short duration that thermal insulation performance deteriorates significantly as the vacuum is damaged. Particularly since a vacuum structure collapses at atmospheric pressure, vacuum insulation has been extremely difficult to use. The technology of the invention provides performance comparable to that of vacuum insulation while employing usual filling methods of thermal insulation materials. The economic effect is important in the following two respects. First is the effect of reducing the producing cost of the thermal insulation material and the producing equipment cost. Second is the effect of reducing maintenance and operation costs, such as the energy saving effect, by improving thermal insulation performance. This is because not only of energy reduction effects of heating and cooling will be reduced, but also of unnecessity of pumps that may be used in vacuum insulation.
As a result of thermal conductivity measurement, when hollow particles are added, the thermal conductivity of the hybrid aerogel decreases from 13.4 mW/m·K when the hollow particles are not included. In the case of micro-size hollow particles of 8 μm in an average outer diameter, the thermal conductivity was 11.8 mW/m·K when the content was 0.1% by weight. In the case of air-filled nano-size hollow particles of 120 nm in an average outer diameter, the thermal conductivity was 10.4 mW/m·K when the content was 0.1% by weight. In the case of CO2-filled nano-size hollow particles of 120 nm in an average outer diameter, the minimum value of the measured thermal conductivity of 9.6 mW/m·K was very close to the value 8.0 mW/m·K of the vacuum insulated panel.
According to the hybrid aerogel of the invention, it is possible to provide a long-life solid thermal insulation material with highly thermal insulation performance comparable to that of vacuum insulated panels, and with high stability not to collapse even when pressure nearly the size of atmospheric pressure acts thereon. Therefore, a practical effect thereof as thermal insulation material parts is significant. More particularly, when the hybrid aerogel of the invention is to be used as a thermal insulation material where a vacuum pump is used for vacuum insulation, necessary thermal insulation performance can be achieved without using a vacuum pump. Therefore, the invention has expanded industrial applicability.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2020-120921 | Jul 2020 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2021/021299 | 6/4/2021 | WO |
