KR20100073625A - Method for preparing hydrophobic aerogel granules - Google Patents

Abstract

PURPOSE: A manufacturing method of hydrophobic aerogel granules is provided to massively and inexpensively manufacture the hydrophobic aerogel granules within a short time with consecutive processes, and to effectively remove sodium ions among sodium silicate. CONSTITUTION: A manufacturing method of hydrophobic aerogel granules includes the following steps: diluting sodium silicate with a weight ratio of 1:1-1:10 in glass fiber and water, respectively; forming silica wet-gel of a monolith type by aging the diluted sodium silicate in 20 - 80 celsius degree after adjusting pH of the sodium silicate to pH 3 - 6; removing the sodium ion by dipping the silica wet-gel of the monolith type in water of 20 - 80 celsius degree; refluxing the silica wet-gel in n-butanol liquid including a silylating agent 1 - 10 weight% while agitating the wet gel with an agitating speed of 50 - 1000rpm; and drying the gained aerogel granules in 20-250°C.

Description

Method for preparing hydrogel granules having hydrophobicity {Method for Preparing Hydrophobic Aerogel Granules}

The present invention relates to a method for producing airgel granules having hydrophobicity. More specifically, the present invention relates to a method for producing aerogel granules having hydrophobicity by hydrophobization-granulation process under strong acidic conditions after removing sodium ions in the wet gel monolith prepared with water glass. In addition, the hydrophobic airgel granule manufacturing method according to the present invention does not require a separate additive and granules for airgel granulation and a separate material for removing sodium ions.

Airgel is a transparent ultra-low density material having a porosity of 90% or more and a specific surface area of several hundred to 1000 m ² / g. Therefore, porous airgel can be applied to the fields of ultra low dielectric, catalyst, catalyst carrier, heat insulating material, electrode material, and soundproof material.Since silica airgel has high light transmittance and low thermal conductivity, it has high potential as a transparent heat insulating material. In addition, it is a very efficient super insulation material that can be used in refrigerators, cars, aircraft, LNG carrier cargo insulation. In particular, the hydrophilic airgel absorbs moisture in the air to increase the thermal conductivity value, and therefore, the necessity of hydrophobicization of the airgel is essential to obtain a low thermal conductivity value.

Since the airgel powder, which is important as a heat insulating material, is scattered due to its low density and small particle size (several to several hundreds of mm) because of its low thermal conductivity, it is difficult to handle and also has a disadvantage in that filling is not easy. In addition, the airgel produced in the monolithic form is limited in the size that can be produced, there is a disadvantage that it is difficult to mold in various forms. Therefore, in order to solve the disadvantages of the airgel powder and the monolithic form, attempts have been made to increase the ease of handling and shape correspondence by manufacturing airgel granules having a size of 0.5 mm or more. The size of the airgel granules is 0.5mm-10mm, aerogel granules having a size of 0.5-5mm as a heat insulating filler is preferable considering the use.

Such airgel granules can be produced by several methods. For example, in US Pat. No. 6,620,355 (Korean Patent Publication No. 2001-12152), airgel particles are formed in order to form airgel particles of 2 mm or less into larger airgel particles. And compressed to form larger airgel particles. Additives, fillers and / or binders are imposed on the airgel particles to exhibit specific properties of the airgel particles. In addition, US Patent No. 6481649 (Korean Patent Publication No. 2001-12153) discloses a method for forming larger airgel particles by structurally agglomerating airgel particles by supplying and mixing airgel particles of 2 mm or less together with a binder and mixing with a binder. It is. The binder may be a non-aqueous solution, suspension, melt or solid material and the airgel is introduced using a spray. In the methods of US Pat. No. 6,620,355 and US Pat. No. 6,648,449, airgel particles are prepared, and then the prepared airgel particles are molded using a molding apparatus, and additives, fillers and / or binders are added to the airgel particles to obtain larger airgel particles. It is molded into an airgel of particles. However, the method requires two separate processes because (1) the aerogel manufacturing process and the granulation process for coagulating or compressing are separated, (2) additionally, a molding apparatus is required, and (3) additives such as binders. As a result, the technically complicated process and long process time are required, which is uneconomical.

Japanese Patent Application Laid-Open No. 1996-151210 discloses a reaction solution obtained by hydrolyzing an alkoxy silane as a filler using three methods, followed by polycondensation reaction with a catalyst, gelation, hydrophobization treatment with a hydrophobic agent, and then supercritical. A method of drying to obtain a hydrophobic airgel is disclosed. The three methods of preparing the filler are (1) a method in which a reaction solution is introduced into a vessel equipped with a partition and gelled, and then removed from the vessel. And (3) dropwise in a solvent such as normal hexane, followed by stirring and gelation.

However, the preparation of the aerogel fillers proposed in this patent requires (1) use of expensive alkoxy silanes and supercritical drying, (2) additional equipment such as containers or tubes, and (3) additional solvents. It is not suitable for mass production in that it has the technical problem of using a series of separate processes, and it is uneconomical.

In order to manufacture hydrophobic airgel granules with inexpensive raw materials and uniaxial and continuous process conditions, firstly, airgel granules having hydrophobicity should be manufactured by using inexpensive water glass and atmospheric pressure drying, and secondly, an additional apparatus is required to prepare granules. Third, no additional additives are required. Fourth, when water glass is used as a precursor, Na ions in the water glass must be effectively removed. In particular, since the additive or the like increases the thermal conductivity value of the airgel, the addition of the additive is not preferable for the preparation of the airgel granules as a heat insulating material.

Accordingly, one embodiment of the present invention to solve the problems of the prior art, to provide a hydrophobized airgel granules manufacturing method without using a separate molding apparatus, agglomeration, compression process or solvent or granulation additive in water glass and atmospheric pressure drying conditions will be.

Another embodiment of the present invention is to provide a method for preparing airgel granules having hydrophobicity in a single hydrophobization-granulation step.

Another embodiment of the present invention is to provide a method for mass production of airgel granules having low cost and hydrophobicity in a short time in a continuous process.

Furthermore, another embodiment of the present invention is to provide a method for producing airgel granules having hydrophobicity by effectively removing sodium ions in the wet gel monolith prepared by using water glass.

According to the present invention,

a) diluting the water glass (sodium silicate) such that the water glass: water ratio is 1: 1-1: 10 by weight;

b) adjusting the diluted water glass to pH 3-6, and then aging at 20-80 ° C. for 2-24 hours to form a monolithic silica wet gel;

c) immersing the monolithic silica wet gel in water at 20-80 ° C. to remove Na ions;

d) a hydrophobization-granulation step of putting the monolithic silica wet gel in an n-butanol solution containing 1-10 wt% of a silylating agent, refluxing at pH 1-5 and stirring at 50-1000 rpm at the same time; And

e) There is provided a method for producing airgel granules having a hydrophobic surface comprising the step of drying the obtained airgel granules at 20-250 ℃.

According to one embodiment of the present invention, sodium ions in the wet gel monolith prepared by using water glass are removed with water, and then the hydrogels are hydrophobized (silylated) and solvent-substituted by a single hydrophobization-granulation process under strong acidic conditions. Simultaneously pulverization yields porous airgel granules in which the airgel surface is hydrophobically modified. Hydrophobized airgel granules prepared by the method according to one embodiment of the present invention have low thermal conductivity, high porosity, high specific surface area, and are particularly easy to handle compared to powder. Furthermore, the method according to one embodiment of the present invention is economical because it does not require the following separate process, which is required when manufacturing airgel granules, is economical, and the process and time are shortened and mass production is possible. (1) after the preparation of the airgel powder, a separate compression or agglomeration process, (2) a granulation process using a granulation apparatus such as a separate nozzle, (3) a molding process using a separate molding apparatus, (4) granulation Addition of separate additives, dispersants, surfactants for. (5) Use of separate ion exchange resins to remove Na ions and, accordingly, add processes and facilities.

In addition, by using the airgel granules prepared by the method according to one embodiment of the present invention as a filler can be used as a heat insulating material of the heat insulating material. When the airgel granules prepared according to the airgel granule production method according to one embodiment of the present invention are used as a filler, the filling density may be efficiently controlled by separating (dividing) the airgel granules according to the size of the airgel granules. Filled airgel granules can be widely used as a heat insulating material with improved molding correspondence. Although not limited to this, for example, when the hydrophobic airgel granules obtained by the method according to the embodiment of the present invention are filled between the multilayer glass, it can be applied as a heat insulating multilayer glass having light transmitting properties and excellent heat insulating properties. As another example, it can be used as a heat insulator in a cold storage tank by filling a plywood case.

Hereinafter, the present invention will be described in more detail.

According to an embodiment of the present invention, a wet gel monolith is prepared by using water glass, and sodium ions in the monolith are removed with water, and then hydrophobization and solvent replacement are performed at the same time to monolithic airgel pulverized into granules, thereby preparing hydrogel granules. It is characterized in that the manufacturing. In the present invention, the sodium component in the monolith is effectively removed by immersing the wet gel monolith in water without using a separate substance. In addition, the silylation step, the solvent replacement step, and the pulverization step do not need to be performed in separate steps, respectively, which shortens the manufacturing time and the process and is suitable for mass production. In addition, by the method according to an embodiment of the present invention it is possible to produce a permanently hydrophobized airgel granules without using a separate molding device, granulation additives or a separate solvent for granulation.

Furthermore, the hydrogel airgel granules prepared by the method according to one embodiment of the present invention can realize porosity, specific surface area, and thermal conductivity values equivalent to those of conventional airgel powders and monoliths. In addition, since Na ions are removed using water, the manufacturing cost is low.

The method for producing the hydrophobically surface-modified airgel granules of the present invention is shown in FIG. 1, and the method for producing the hydrophobically-modified airgel granules according to the present invention will be described in detail with reference to FIG. 1.

As shown in FIG. 1, the water glass solution is diluted so that the water glass and water have a weight ratio of 1: 1-1: 10. Thereafter, the diluted water glass is aged (gelled) to obtain a wet gel in the form of a monolith. If the water glass is not diluted, the specific gravity of the water glass is high, so it takes a long time to pass through the ion exchange resin, so it is preferable to dilute the water glass so that the water glass: water ratio is 1: 1-1: 10. If the dilution ratio of water glass is less than water glass: water = 1: 1 weight ratio, the water glass dilution effect is insufficient. If the water glass dilution ratio exceeds water glass: water = 1: 10, the strength of the produced monolithic wet gel is so weak that granules of desired particle size It is not desirable to get.

Since the water glass has a pH of about 12, HCl is added to the water glass until the pH of the water glass is about 3-6. If the pH of the gelling medium is lower than 3 or higher than 6, it is not preferable from the viewpoint of efficiency and economic efficiency of silica gel production because the reaction is too fast or the reaction is very slow to control the formation of the silica gel effectively. Dilute waterglass adjusted to pH 3 to 6 is aged at 20-80 ° C. for 2-24 hours to prepare a monolithic silica wet gel. When the reaction is less than 2 hours in the monolithic wet gel formation reaction conditions, the strength of the monolithic wet gel is low, so that it is difficult to obtain granules having a desired particle size, and when it exceeds 24 hours, the process time is long, which is not preferable. In addition, if the reaction temperature is less than 20 ℃ is not preferable because the silylation reaction is not made enough that the hydrophobicity is not sufficient, if it exceeds 80 ℃ it is not preferable because of the increase in the process cost due to high temperature.

Thereafter, the monolithic silica wet gel formed of the water glass is immersed in water to remove Na ions. At this time, it is preferable that the temperature of water is 20 degreeC-80 degreeC. In the process of immersing the monolithic silica wet gel in water to remove Na ions, aging is performed to increase the strength of the wet gel. Therefore, if the temperature of the water is less than 20 ° C, it is not preferable in that the wet gel of sufficient strength is not obtained, and if it exceeds 80 ° C, bubbles are generated in the water, which is not preferable in that the wet gel monolith is finely broken. The Na component in the wet gel monolith is more effectively removed by repeating the removal of Na ions by the above immersion. The number of repetitions is not limited, and may be performed so that Na ions can be sufficiently removed as necessary. Although not limited thereto, Na ions were sufficiently removed after about 3 to 5 repetitions. In the case of using the wet gel monolith without removing Na ions, it is pulverized into particles of 0.5 mm or less by agitation in the subsequent solvent substitution and silicification process, so that the granules do not become a desirable size.

On the other hand, after removing the Na ions, in consideration of the subsequent stirring step may be further aged at 20-80 ℃ additionally for 1 hour or more at pH 3 ~ 6 to increase the strength of the monolithic silica wet gel. In an additional aging step, the pH is carried out at 3-6 in the same way as the wet gel formation step. In an additional aging step, the gelation rate is lower than 20 ° C., which is not preferable, and when it exceeds 80 ° C., monolith is pulverized in a state in which bubbles are generated in the water and do not have sufficient strength. The additional aging step is not preferable in that the strength of the wet gel is not strong enough if it is less than 1 hour, and the upper limit time for the additional aging treatment time is not limited, but if it is aged for 6 hours, the gel is sufficiently gelated to exceed 6 hours. Since the above increase in strength and gelation do not proceed, it can be further aged for about 1 hour to 6 hours.

The monolithic silica wet gel from which Na ions have been removed is placed in an n-butanol solution containing 1 to 10% by weight of a silylating agent (hereinafter referred to as 'n-butanol solution of silylating agent') to pH 1-5. After matching, the hydrophobization-granulation step is carried out by refluxing and stirring at a speed of 50-1000 rpm. If the silylating agent content is less than 1% by weight in the n-butanol solution of the silylating agent, the silica surface may not be sufficiently hydrophobized. If it exceeds 10% by weight, side reactions such as coupling between the siliciling agents may occur due to the high silicide concentration. have. The pH is not preferred because the silylation occurs slowly outside the range of 1-5. Although not limited to this, For example, it can adjust to pH 1-5 using hydrochloric acid.

Reflux time is the heating time until the vaporized n-butanol vapor is condensed by connecting a cooling tube until water no longer mixes with n-butanol, but is not limited thereto. It can be refluxed over time. If the reflux time is less than 2 hours, depending on the type of silylating agent, the silylation reaction time may not be sufficient, and if it exceeds 24 hours, an unwanted side reaction may occur. It is preferable to perform reflux at 100-150 degreeC. If the reaction temperature is less than 100 ℃ at reflux it is not preferable in that it is difficult to remove the water contained in the wet gel, if it exceeds 150 ℃ it is not preferable because it may be damaged by the thermal decomposition of the silylating agent.

The reaction in the hydrophobization-granulation step is also stirred at a stirring speed of 50-1000 rpm. When silylating monolithic wet gel without stirring, the inside of the wet gel having a size of 10 mm or more is not silylated within 2-24 hours. In the absence of stirring, it was not confirmed that the wet gel having a size of 10 mm or more was silylated even after reflux for 48 hours.

In addition, the monolithic airgel wet gel may be ground by stirring to obtain airgel granules having a desired particle size. By controlling the stirring speed, the granule size distribution of the airgel can be controlled. The stirring speed is 50-1000 rpm, preferably 200-500 rpm, and in this stirring speed range, airgel granules having a desired particle size, specifically 0.5 mm or more, preferably 0.5-10 mm, more preferably 1-5 mm, Mainly obtained. Specifically, when the stirring speed is less than 50rpm it is not preferable that the granules exceeding the size of 10mm is obtained, and when the excess of 1000rpm, most monolithic silica gels are less than 0.5mm, which is not preferable. However, the size of the granules may vary depending on the type and size of the stirrer. If the size of the airgel granules exceeds 10mm, there is a problem that the gap between the airgel granules during filling increases the poor thermal insulation effect, and if the size of the airgel granules is less than 0.5mm, it is difficult to handle because they scatter like conventional airgel powder.

As the silylating agent, a silane compound may be used, and more specifically, the chemical formula R _{1 4-n} -SiX _n where n is 1-3 and R ₁ is C ₁ -C ₁₀ Alkyl, C ₃ -C ₈ aromatic, C ₃ -C ₈ aromatic alkyl, C ₃ -C ₇ heteroaromatic alkyl (hetero element is at least one selected from the group consisting of O, N, S, P) and hydrogen Is selected from the group consisting of F, Cl, Br, I, C ₁ -C ₁₀ alkoxy group, C ₃ -C ₈ aromatic alkoxy group and C ₃ -C ₇ heteroaromatic alkoxy group ( Hetero-element is selected from the group consisting of at least one selected from the group consisting of O, N, S, P)) and R ₂ Si-O-SiR ₃ (where R ₂ , R ₃ groups are F, Cl , Br, halogen selected from the group consisting of I, C ₁ -C ₁₀ alkyl, C ₃ -C ₈ aromatic, C ₃ -C ₈ aromatic alkyl, C ₃ -C ₇ heteroaromatic alkyl (the hetero elements are O, N , At least one selected from the group consisting of S and P) and each independently selected from the group consisting of hydrogen). Since there can be selected. Alkyl, aromatic alkyl, heteroaromatic alkyl, alkoxy, heteroaromatic alkoxy, alkyl, and alkoxy in the substituted group in the formula of the silylating agent may have 1 to 10 carbon atoms. Specific examples of such silylating agents include, but are not limited to, hexamethyldisilane, ethyltriethoxysilane, trimethoxysilane, triethylethoxysilane, methyltrimethoxysilane, ethyltrimethoxysilane, At least one selected from the group consisting of methoxytrimethylsilane, trimethylchlorosilane and triethylchlorosilane can be used.

By using a water glass to prepare a monolithic wet gel and immersing it in water to remove Na ions in the monolith, Na ions can be removed economically and effectively without using a separate material for removing Na ions. Further, in the hydrophobization-granulation step, the wet gel monolith is hydrophobized (silylated) and solvent-substituted in a single process step, as well as ground to granules of the desired size. The silica gel milled in this hydrophobization-granulation step, water removed by solvent substitution and hydrophobically surface modified is dried. Drying can be performed at normal pressure at 20-250 degreeC. Temperatures below 20 ° C. are undesirable because the drying rate is too slow, and temperatures above 250 ° C. are undesirable because hydrophobized silylated groups may be lost due to pyrolysis. The suitable time for drying is influenced by the structure of the resulting airgel, the particle size, the kind of solvent used and the residual content in the gel structure. Therefore, the optimum drying time can be determined by measuring the time that the dried particles are not detected by using a thermogravimetric analyzer (TGA). The n-butanol used for solvent replacement in the process step may be reused in the hydrophobization-granulation step.

Finally, the dried airgel granules are separated by size. At this time, the separation method of the airgel granule particles is not particularly limited, but the airgel granules may be separated using, for example, a vibration mill, a specific gravity separator, a rotary separator, a sieve, and the like. On the other hand, the airgel particles larger than the desired particle size may be regrind using a vibratory grinder, or a continuous process of recirculating and regrinding upon stirring may be possible. In the method according to one embodiment of the present invention, airgel granules having a hydrophobicity having a desired particle size, specifically, about 0.5 mm or more, preferably 0.5-10 mm, more preferably 1-5 mm, are obtained. . Such, the granule airgel prepared by the airgel granule manufacturing method according to one embodiment of the present invention is particularly suitable for use as a heat insulating filler.

According to the method according to one embodiment of the present invention, (1) Na ions in the monolithic wet gel are sufficiently removed using water, and the monolithic silica is further due to the effect of aging in the Na ions removal process using water. The strength of the wet gel is increased and the use of a separate ion exchange resin for removing Na ions and hence the need for additional processes and equipment, and (2) a single hydrophobicization of silylation, solvent replacement and grinding processes- It is carried out simultaneously by the granulation process step, (3) does not require granulation apparatus, such as a separate molding apparatus and nozzle for granulating the airgel, (4) separate additives, dispersants, The monolithic silica wet gel can be pulverized simultaneously with silylation and solvent replacement without using a surfactant or an organic solvent, and further, the prepared airgel granules can be continuously processed. By separating them can be separated (fractionated) and collecting the granules of various sizes into granules of a predetermined size can produce granules of various grades. In addition, the manufacturing process is simple compared to the conventional airgel granulation manufacturing process, there is an advantage suitable for mass production. The airgel granules thus prepared may be used as fillers for transparent insulation windows or insulation materials.

Hereinafter, the present invention will be described in more detail with reference to Examples. However, the following examples are intended to illustrate the present invention, which does not limit the present invention. Examples of airgel granules prepared by using an additive and dropping into an organic solvent containing additives were compared.

Example

Inventive Example  One

Water glass solution (a solution of 35% sodium silicate solution diluted 3 times with water (water glass: water = 1: 3 weight ratio), Na content 2620ppm) was poured into a petri dish at pH 3.5 using HCl solution, and the mixture was kept at room temperature for about 2 hours. Aging was performed to prepare a monolithic wet gel. The monolithic wet gel thus prepared was placed in 50 ° C of separately prepared water corresponding to three times the volume of the wet gel and left for 2 hours while maintaining the temperature. Then, the monolithic wet gel was taken out and the water was discarded to monolithic wet. Na ions in the gel were removed. Separately, the prepared wet gel was added to n-butanol (5 wt% ETMS n-butanol solution) containing 5 wt% ethoxy trimethylsilane (ETMS), 1 M HCl was added thereto, and the pH was adjusted to 2, followed by 6 hours at 130 to 140 ° C. Reflux with stirring at 200 rpm. The wet gel treated with n-butanol was dried at 160 ° C. for 2 hours to remove n-butanol present on the gel surface, thereby obtaining airgel granules. The prepared granules are separated step by step using a sieve of 5mm, 1mm, 850mm, 500mm. The thermal conductivity of the granules (1-5mm) thus prepared was 11.1 mW / m · K as measured by the hot wire method. In addition, it was confirmed that both the airgel granules themselves and the finely divided powders were floating on the water surface without sinking even in the long term (more than 3 months), so that the airgel granules prepared from this were hydrophobized.

Inventive Example  2

Water glass solution (a solution of 35% sodium silicate solution diluted 3 times with water (water glass: water = 1: 3 weight ratio)) was poured into a petri dish at pH 3.5 using HCl solution and aged at room temperature for 2 hours. To produce a monolithic wet gel. The monolithic wet gel thus prepared was placed in 50 ° C of separately prepared water corresponding to three times the volume of the wet gel and left for 2 hours while maintaining the temperature. Then, the monolithic wet gel was taken out and the water was discarded to monolithic wet. Na ions in the gel were removed, and this Na ion removal step was repeated three times. Thereafter, it was further aged at 25 ° C. for 2 hours at pH 3.5. Meanwhile, the wet gel prepared above was added to n-butanol (5 wt% ETMS n-butanol solution) containing 5 wt% ethoxy trimethylsilane (ETMS) separately, 1 M HCl was added thereto, and the pH was adjusted to 2, at 130 to 140 ° C. It was refluxed with stirring at 200 rpm for 6 hours. The wet gel treated with n-butanol was dried at 160 ° C. for 2 hours to remove n-butanol present on the gel surface, thereby obtaining airgel granules. The prepared granules are separated step by step using a sieve of 5mm, 1mm, 850mm, 500mm. The thermal conductivity of the granules (1-5mm) thus prepared was 10.2 mW / m · K as measured by the hot wire method. In addition, it was confirmed that both the airgel granules themselves and the finely divided powders were floating on the water surface without sinking even during long-term standing (more than 3 months), and it was confirmed that the airgel granules prepared from this were hydrophobized.

Comparative example  One

A water glass solution (a solution of 35% sodium silicate solution diluted three times with water (water glass: water = 1: 3 weight ratio)) was passed through an ion exchange resin (DOWEX 50WX8-200) to remove Na ions. To the diluted waterglass solution from which Na ions have been removed, NH ₄ OH solution is added in small portions with stirring to adjust the pH of the solution to 3.5. This water glass solution was poured into a Petri dish and aged at room temperature for 2 hours to prepare a monolithic wet gel. Separately, the prepared wet gel was added to n-butanol (5 wt% ETMS n-butanol solution) containing 5 wt% ethoxy trimethylsilane (ETMS), 1 M HCl was added thereto, and the pH was adjusted to 2, followed by 6 hours at 130 to 140 ° C. Reflux with stirring at 200 rpm. The wet gel treated with n-butanol was dried at 160 ° C. for 2 hours to remove n-butanol present on the gel surface, thereby obtaining airgel granules. The prepared granules are separated step by step using a sieve of 5mm, 1mm, 850mm, 500mm. The thermal conductivity of the granules (1-5mm) thus prepared was 10 mW / m · K as measured by the hot wire method. In addition, it was confirmed that both the airgel granules themselves and the finely divided powders were floating on the water surface without sinking even in the long term (more than 3 months), so that the airgel granules prepared from this were hydrophobized.

Meanwhile, the Na ion amounts and thermal conductivity values of the airgel granules prepared in Inventive Examples 1 and 2 and Comparative Example 1 are summarized in Table 1. Na ion content of the airgel granules was measured by the ICP (Inductively Coupled Plasma) method.

TABLE 1

Na ion amount (ppm) Thermal Conductivity (mW / mK) Inventive Example 1 54.2 11.1 Inventory 2 16.4 10.2 Comparative Example 1 9.94 10.0

As can be seen in Table 1, Inventive Examples 1 and 2 were prepared by preparing a monolithic wet gel using water glass and removing Na ions using water to prepare Na-gel using an ion exchange resin to remove Na. In addition to showing almost the same thermal conductivity as one of the airgel granules, it was confirmed that most of 2620 ppm of Na ions contained in the water glass used as the reactant were removed, thereby reducing the Na ion content in the final granular airgel.

Furthermore, Inventive Example 2 subjected to three times of Na ion removal treatment showed more excellent thermal conductivity and reduced Na ions content in the final airgel granules compared to that of Invention subjected to Na ion removal treatment once. From this, the airgel granules prepared by preparing monolithic wet gel using water glass and removing Na ions using water not only exhibit excellent physical properties as aerogels, but also sufficiently absorb Na ions from the monolithic silica wet gel using water. It was confirmed that it could be removed.

1 is a view showing a method for producing airgel granules having hydrophobicity according to the present invention.

Claims (10)

a) water glass: diluting the water glass (sodium silicate) so that the water is 1: 1-1: 10 weight ratio; b) adjusting the diluted water glass to pH 3-6, and then aging at 20-80 ° C. for 2-24 hours to form a monolithic silica wet gel; c) immersing the monolithic silica wet gel in water at 20-80 ° C. to remove Na ions; d) hydrophobization to remove the Na-ion monolithic silica wet gel in n-butanol solution containing 1-10% by weight of silylating agent at reflux at pH 1-5 and stirring at 50-1000 rpm stirring speed Granulation step; And e) drying the obtained airgel granules at 20-250 ° C .; Airgel granules manufacturing method having a hydrophobic comprising a. The method of claim 1, further comprising the step of aging the monolithic silica wet gel from which Na is removed at pH 3-6 and at 20-80 ° C. for at least 1 hour between steps c) and d). Airgel granules manufacturing method having a hydrophobicity to. The method of claim 1, wherein the hydrophobization-granulation step is performed at 100 to 150 ° C. The compound of claim 1, wherein the silylating agent is of formula R _{1 4-n} -SiX _n where n is 1-3 and R ₁ is C ₁ -C ₁₀ Alkyl, C ₃ -C ₈ aromatic, C ₃ -C ₈ aromatic alkyl, C ₃ -C ₇ heteroaromatic alkyl (hetero element is at least one selected from the group consisting of O, N, S, P) and hydrogen Is selected from the group consisting of F, Cl, Br, I, C ₁ -C ₁₀ alkoxy group, C ₃ -C ₈ aromatic alkoxy group and C ₃ -C ₇ heteroaromatic alkoxy group ( Hetero-element is selected from the group consisting of at least one selected from the group consisting of O, N, S, P)) and R ₂ Si-O-SiR ₃ (where R ₂ , R ₃ groups are F, Cl , Br, halogen selected from the group consisting of I, C ₁ -C ₁₀ alkyl, C ₃ -C ₈ aromatic, C ₃ -C ₈ aromatic alkyl, C ₃ -C ₇ heteroaromatic alkyl (the hetero elements are O, N , At least one selected from the group consisting of S and P) and each independently selected from the group consisting of hydrogen). Since airgel granules having a hydrophobic method to select that feature. The method of claim 4, wherein the silylating agent is hexamethyldisilane, ethyltriethoxysilane, trimethoxysilane, triethylethoxysilane, methyltrimethoxysilane, ethyltrimethoxysilane, methoxytrimethylsilane, trimethyl A method for producing hydrogel granules having hydrophobicity, characterized in that at least one selected from the group consisting of chlorosilane and triethylchlorosilane. According to claim 1, Airgel granules manufacturing method characterized in that the size of the granules is adjusted according to the stirring speed. The method of claim 1, further comprising separating the dried airgel granules by particle size after the drying step. 8. The method of claim 7, wherein the separating step is performed using a vibration mill, a rotary separator, a specific gravity separator and / or a sieve. The method of claim 8, further comprising the step of recirculating the airgel granules of the large particles separated after the separation step to re-pulverize into small particles. The method of claim 1, wherein the n-butanol used for solvent replacement is sent to a distillation process for reuse.

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